268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 1 of 357
Minutes of the 268thmeeting of the State Level Expert Appraisal Committee held on 1st Sep 2021 through
Video Conference (VC) on National Informatics Centre (NIC).
In the wake of recent crisis of COVID-19, lockdown situation, the agenda of the present meeting was mailed to
expert Committee in advance and a Video conference meeting on NIC was organized in this regard on 01-09-
2021 at 13:30 hrs.
The 268thmeeting of the State Level Expert Appraisal Committee (SEAC) was held online by Video conferencing
on 01st September 2021 at 13:30 hrs. Following members joined the meeting:
1. Shri Akshay Kumar Saxena, Chairman, SEAC
2. Dr. S. C. Pant, Vice Chairman, SEAC
3. Dr. M. N. Patel, Member, SEAC
4. Shri D. C. Chaudhari, Member, SEAC
5. Shri J. K. Vyas, Member, SEAC
6. Shri Anand Zinzala, Member, SEAC
7. Shri B. M. Tailor, Member, SEAC
8. Shri A.V.Shah, Secretary, SEAC
The Committee considered the applications made by project proponents, additional details submitted as required
by the SEAC/SEIAA and details furnished in the Form-1, PFR, EMP reports etc.
The agenda of total twelve cases of Category 8 (a) were taken up during the meeting. The applicants made
presentation on the activities to be carried out along with other details furnished in the Form-1, Form-1A &
Conceptual Plan.
Sr No Proposal No Name and Address Remarks
1 SIA/GJ/IND2/152395/2020
PI Industries Limited
Plot No. 237, GIDC Industrial Estate, Panoli, Ankleshwar, Bharuch
EC reconsideration
Category of the unit: 5(f)
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Project status: Expansion
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/152395/2020 on
dated 27.11.2020 for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is an existing unit of technical pesticide manufacturing unit and now proposes new
project for manufacturing of synthetic organic chemicals [API and API Intermediates] as
tabulated below,
Brief Note of Product Profile
1. No of Manufacturing Plants -1
2. Brief Note Regarding number of Products to be manufactured considering plant
capacity- 1
ENDUSE OF PROPOSED PRODUCTS
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category of Product (API/ Intermediate)
In case of intermediate stage of API
Said API is used for/End Use of said API
Stage ie, n-1, n-2 etc
Name of API in which Intermediate Used/ End use of said Intermediate
CAS No. (API)
DEAM/ DEAM. HCl/ Bromo Compound
6829-40-9/ 13433-00-6
Intermediate n-1 Favipiravir 259793-96-9
Favipiravir which is a medicine being used for COVID-19 treatment
Brief Summary regarding End -Uses of Product Profile DEAM/ DEAM. HCl/ Bromo Compound product is a N-1 stage Intermdiate pharma product. It will be used in manufacturing of Favipiravir, which is a final API and a medicine being used for COVID -19 treatment.
• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA
Notification 2006 and amendment dated 27th March, 2020.
• The proposal was considered in the SEAC video conference meeting dated 12.03.2021.
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• During the meeting dated 12.03.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and Technical expert of PP, M/s. Shree Green Consultants remains
present during video conference meeting.
• This is an existing unit of technical pesticide manufacturing unit and now proposed new
project of API and Its Intermediates plant in same premises at GIDC Panoli. Source of water
supply is bore well. Committee noted that PP submitted undertaking regarding there is no
legal court case, public complaint and no legal action taken against unit by GPCB in last
three years. PP submitted EC order for pesticide manufacturing unit and valid CCA for
existing project. PP submitted self certified compliance report (CCR) for existing plant EC
and CCA compliance report. Product profile along with End Use discussed in depth.
• Looking to proposed API production in existing technical pesticide manufacturing plant
which is exclusively for technical pesticide and pesticide formulation plant, Committee asked
for feasibility of API plant in existing technical pesticide manufacturing plant. PP said that
they have proposed API intermediate products which are n-1 stage products for Favipiravir,
which is a medicine being used for COVID -19 treatments. Also PP informed that they will
provide separate infrastructure for API plant in existing production plant premises.
Committee insisted for technical feasibility for proposed API plant in existing technical
pesticide manufacturing and pesticide formulation plant with technical control measures to
avoid contamination of dusting of pesticide and volatile material from pesticide
manufacturing plant towards proposed API intermediate manufacturing plant. As Phorate
pesticide products banned by Honorable Supreme court and looking to proposed product,
namely HCl, distilled solvent, NaBr, sulphuric acid which are Hazardous waste and power
plant which are not in line with MoEF&CC’s Notification vide S.O. 1223 (E) dated
27/03/2020 in respect of Active Pharmaceutical Ingredients (API) as category B2 projects,
Committee insisted for revised product profile with discontinue of existing banned technical
pesticide products as per Honorable supreme court order, HCl, distilled solvent, NaBr,
sulphuric acid and power plant and subsequent change in form-1, PFR and EMP. Also
Committee insisted for chemical name of proposed product namely bromo compound,
DEAM, DEAM. HCl and authenticated document for n-1 stages for manufacturing of
Favipiravir with chemical reaction.
• Committee noted that PP has addressed area adequacy for proposed project with layout
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plan. Looking to layout plan, Committee insisted for revised layout plan with mentioning
feasibility of proposed API plant in existing pesticide plant, adequate size peripheral road for
easy movement of fire tender and emergency vehicle, separate entry and exit and fire
hydrant network with water sprinkler in solvent storage area and ETP area, separate and
isolated raw material and finished good storage for existing pesticide and proposed API
plant etc and revised area adequacy with land break up. Also Committee insisted for
separate manpower for proposed API plant and existing pesticide manufacturing plant.
• Looking to water balance diagram, Committee insisted for revised waste water treatment
proposal and water balance diagram considering compliance of Direction under section
18(1) (B) for additional waste water discharge at FETP of M/s NCTL for further treatment
considering quality and quantity of effluent. Looking to air matrix, Committee insisted for
revised air emission matrix with mentioning approved fuel other than furnace oil and
adequate stack height for thermic fluid heater , two stage scrubber for each process stack
instead of single stage scrubber and adequate APCM for incinerator as per CPCB guideline.
• Committee noted that PP has addressed Hazardous waste matrix, EMP, CER, greenbelt
area, LDAR and solvent recovery, Fire load calculation, safety measures for storage and
handling of Hazardous chemicals, adoption of auto control system for critical process, fire
evacuation plan etc. Looking to proposed quantity mentioned for distilled solvent, HCl,
sulphuric acid and NaBr in product profile which seems Hazardous waste, Committee
insisted for revised Hazardous waste matrix with mentioning distilled solvent, HCl, sulphuric
acid and NaBr as Hazardous waste with its proper disposal. Also Committee insisted for
technical justification regarding generation quantity of distilled solvent, HCl, sulphuric acid
and NaBr along with mass balance and stages from where it can be generated from
proposed products with chemical reaction of proposed products. Looking to storage and
safety details of hydrogen , bromine and Ammonia for proposed product, Committee insisted
for submission of risk assessment for storage and handling of Hydrogen, bromine and
Ammonia with super imposition of dispersion model on proposed plant area and its effect in
surrounding habitat area with it safety control measures. Also Committee insisted for revised
EMP with mentioning cost of auto control system like DCS for critical process, cost of
adequate APCM and stack height, adequate fire hydrant network, adequate size fire water
tank, adequate capacity fire extinguishers etc in it and also status of fire NOC from
respective competent authority for existing plant .
• After detailed deliberation, Committee unanimously decided to consider the project in
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one of upcoming meeting after submission of following documents,
1. Technical feasibility for proposed API plant in existing technical pesticide
manufacturing and pesticide formulation plant with technical control measures to
avoid contamination of dusting of pesticide and volatile material from pesticide
manufacturing plant towards proposed API intermediate manufacturing plant.
2. Revised product profile with discontinue of existing banned technical pesticide
products as per Honorable supreme court order, HCl, distilled solvent, NaBr,
sulphuric acid and power plant and subsequent change in form-1, PFR and EMP.
Also submit authenticated document regarding stoppage of Banned product like
Phorate, as per Honorable Supreme Court order.
3. Submit details regarding chemical name of proposed product namely bromo
compound, DEAM, DEAM. HCl and authenticated document for n-1 stages for
manufacturing of Favipiravir with chemical reaction.
4. Revised layout plan with mentioning feasibility of proposed API plant in existing
pesticide plant, adequate size peripheral road for easy movement of fire tender and
emergency vehicle, separate entry and exit and fire hydrant network with water
sprinkler in solvent storage area and ETP area, separate and isolated raw material
and finished good storage for existing pesticide and proposed API plant etc and
revised area adequacy with land break up. Also notarized undertaking regarding
separate manpower for proposed API plant and existing pesticide manufacturing
plant.
5. Revised waste water treatment proposal and water balance diagram considering
compliance of Direction under section 18(1) (B) for additional waste water discharge
at FETP of M/s NCTL for further treatment considering quality and quantity of
effluent.
6. Revised air emission matrix with mentioning approved fuel other than furnace oil and
adequate stack height for thermic fluid heater , two stage scrubber for each process
stack instead of single stage scrubber and adequate APCM as per CPCB guideline
with incinerator.
7. Revised Hazardous waste matrix with mentioning distilled solvent, HCl, sulphuric
acid and NaBr as Hazardous waste with its proper disposal. Also technical
justification regarding generation quantity of distilled solvent, HCl, sulphuric acid and
NaBr along with mass balance and stages from where it can be generated from
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proposed products with chemical reaction of proposed products.
8. Submission of risk assessment for storage and handling of Hydrogen, bromine and
Ammonia with super imposition of dispersion model on proposed plant area and its
effect in surrounding habitat area with it safety control measures.
9. Revised EMP with mentioning cost of auto control system like DCS for critical
process, cost of adequate APCM and stack height, adequate fire hydrant network,
adequate size fire water tank, adequate capacity fire extinguishers etc in it.
10. Status of fire NOC from respective competent authority for existing plant.
• PP submitted their reply for the query raised by SEAC during SEAC meeting dated
20.05.2021 through email.
• The proposal was reconsidered in the SEAC video conference meeting dated 07.06.2021.
• Revised Salient features of the project including Water, Air and Hazardous waste
management are as under:
Sr. no.
Particulars Details
A-1
Total cost of Proposed Project (Rs. in Crores):
Proposed
12 Cr
Break Up of Proposed Project Cost Rs. In crores)
Details Existing Proposed Total
Land - - -
Plant & Machinery
- 12 12
Miscellaneous - - -
A-2 Details of EMP As below
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Sr. No.
Unit Details
Capital Cost
(Rs. In Lakhs)
Operating Maintenance Total
Recurring
Cost in Lacs/Months
1 Air Pollution
Control
2 stage Scrubbing
system and increase in the stack
height
39.00 4.00 2.50 6.50
2 Water
Pollution Control
ETP upgradation
30.00 4.00 1.00 5.00
3
Environment Monitoring and solid
waste Management
Hazardous waste facility upgradation
5.00 0.50 0.50 1.00
4 Occupational
Health - 5.00 1.05 0.45 1.50
5 Green Belt - 2.00 0.42 0.18 0.60
6 Fire Safety & Equipment
Camera at prominent
plant location
6.00 0.87 0.38 1.25
7
DCS or PLC system (Part
of Project cost)
Installation of DCS or
PLC system for
Automation
100.00 7.00 3.00 10.00
8
Fire hydrant network, fire water tank (470 KLD),
fire extinguisher *
Fire extinguisher
type ABC type:11 Nos (5 Kg), CO2 Type: 120 Nos,
Sand bucket type : 229
Nos, Foam Type:
40 Nos, DCP Type:
239 Nos
15.00 0.15 0.10 0.25
Total 202.00 17.99 8.11 26.10
A- Details of CER as per OM dated . As below
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3 01/05/2018
The unit has planned to spend 2-time slabs given in the OM dated 0.1.05.2018 for CER. As per that and OM dated 31st oct 2019 for CPA unit will spend 1% of the total cost of the proposed project i.e 12 lacks, for CER activity. As per project cost the CER amount comes as Rs.12 Lacs. But as corporate unit, we will be budgeting Rs. 80 Lacs as CER fund for carrying out below mentioned activities. Brief note on Proposed activities
Sr. No.
Description
Year Total 1 2 3 4 5
1 Provision of RO for Drinking Water Facility by Infrastructure development in Alonj village
2.5 2.5 5.0 5.0 5.0 20.0
2 Organize Health checkup Camps and Distribution of nutrition food for Children in Panoil & Bhadi village
2.5 2.5 5.0 5.0 5.0 20.0
3 Provisional of Internet medium for digital education in school of karmali Village.
2.5 2.5 5.0 5.0 5.0 20.0
4 Provide Infrastructural facilities solid waste management by providing dustbins & distribution
2.5 2.5 5.0 5.0 5.0 20.0
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of paver blocks in Umarwada village.
Total (Rs. in Lakhs)
10.0
10.0
20.0
20.0
20.0
80.00
B Land/Plot ownership details
B1 Total Plot area (sq. meter) Total plot area is 56868.00 Sq. m
Existing Proposed Total
56868.00 sq. m - 56868.00 sq. m
B2 Brief note on Area adequacy in line to proposed project activities: Project is proposed to expand production capacity in existing unit. Since it is planned to produce API pharma product of n-1 stage, which can be produce in existing facility with minor modification; There is no need additional land for new plant.
B3 Green belt area ( sq. meter) Total: 22748 Sq. m.
existing Proposed Total
Area in Sq. meter 22748.00sq. m 0.00 22748.00sq. m
% of Total Area 33% Total Area
C Employment generation Proposed:50
Existing Proposed Total
- 50 50
D Water
D1
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Water Supply
Status of permission from the concern authority.
Obtained
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D2 Water consumption (KLD)
Sr. No.
Particulars Fresh Water Consumption (KLD)
Existing Additional Total after expansion
1 Domestic 55 5 60
2 Gardening 53 50 103.00 (50 recycled)
3
Industrial
a) Process 128 312 440
b) Cooling (Make-up)
136 304 440 (184 recycled)
c) Boiler 121 4 125
d) other 35 0 35
Sub-Total: Industrial
420 620 1040
Grand Total 528 675 1203
Brief Note on worst case scenario for water consumption: Since we are proposing only one product so water consumption will
remain same in worst case scenario.
Summary of water
requirement
Existing KLD
Proposed (Additional) KLD
Total after
Expansion KLD
Remarks
Total water requirement for the project (A)
528 675 1203 -
Quantity to be recycled (B)
-- 234 234 --
Total fresh water requirement (C)
528 441 969 -
Ensure Total water requirement = Fresh water + Recycled water i.e. A = B + C
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. NA
Total recycle water 234 KLD (recycle water)
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Source of waste water for recycle with quantity in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse i.e.
Treated Domestic effluent 50 KLD and process effluent 184 KLD
Used in Garden 50 KLD and Cooling Tower 184 KLD
PH: 6.5-7.5 COD: <100 BOD: <30
1) Total water requirement for the project:1203 KLD 2) Quantity to be recycled: 234 3) Total fresh water requirement: 969 KLD Total water requirement = Fresh water
D3
Waste water generation (KLD)
Sr. No.
Particulars Waste Water Generation (KLD)
Existing
Additional
Total after expansion
Recycle
Net Effluent to be discharge
1. Domestic 33.675 16.325 50 50 Nil
2.
Industrial
a) Process 276.699
156.301 433 184 168
b) Washing - - - 0 -
c) Cooling (Make-up)
22.029 38.971 61 0 61
d) Boiler 7.536 14.464 22 0 22
e) Other - - - - -
Sub-Total: Industrial
306.264
209.736 516 184 251
Grand Total 339.939*
226.061 566** 234 251
*In present scenario, total w/w generation is around 339.939 KLD; out of which 19.36 KLD goes to incinerator, 177 KLD high TDS effluent treating in MEE and its condensate is recycled into cooling tower. Remaining 143.575 KLD waste water generation goes for treatment to ETP for ultimate disposal after treatment. ** In proposed scenario, total w/w generation will be 566 KLD after expansion. Out of which 48 KLD will go to incinerator, 50 KLD domestic effluent will be treated in STP for recycling into gardening/ CT. High TDS effluent 217 KLD will be treated in MEE and condensate will be recycled into cooling tower. Remaining 251 KLD, low TDS waste water will go to ETP for treatment and final disposal.
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Brief Note on worst case scenario for waste water generation (Qualitative and Quantitative): *In present scenario, total w/w generation is around 339.939 KLD; out of which 19.36 KLD goes to incinerator, 177 KLD high TDS effluent treating in MEE and its condensate is recycled into cooling tower. Remaining 143.575 KLD waste water generation goes for treatment to ETP for ultimate disposal after treatment. ** In proposed scenario, total w/w generation will be 566 KLD after expansion. Out of which 48 KLD will go to incinerator, 50 KLD domestic effluent will be treated in STP for recycling into gardening/ CT. High TDS effluent 239 KLD will be treated in MEE and condensate will be recycled into cooling tower. Remaining 251 KLD, low TDS waste water will go to ETP for treatment and final disposal.
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project
(Whichever is applicable).
D4 Mode of Disposal and Final meeting point (Existing and Proposed)
Domestic:
Sewage / domestic effluent will be treating in a new sewage treatment plant and treated effluent will be recycled into cooling tower / in house gardening. Sewage treatment plant under flow/ bio mass will be treated in our existing effluent treatment plant
Industrial:
*In present scenario, total w/w generation is around 339.939 KLD; out of which 19.36 KLD goes to incinerator, 217 KLD high TDS effluent treating in MEE and its condensate is recycled into cooling tower. Remaining 143.575 KLD waste water generation goes for treatment to ETP for ultimate disposal after treatment. ** In proposed scenario, total w/w generation will be 566 KLD after expansion. Out of which 48 KLD will go to incinerator, 50 KLD domestic effluent will be treated in STP for recycling into gardening/ CT. High TDS effluent 239 KLD will be treated in MEE and condensate will be recycled into cooling tower. Remaining 251 KLD, low TDS waste water will go to ETP for treatment and final disposal.
D5 Treatment Facilities: For Domestic waste water Capacity of STP: 50 KLD
Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary),
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➢ 350 m3/Day
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) Characteristics of Final treated effluent as below.
Parameter Untreated Primary Treated
After ETP
Temperature Ambient Ambient Ambient
COD 4000 - 10000 mg/L
4000 - 8000 mg/L
< 900 mg/L
BOD 3000 - 8000 mg/L
4000 - 6000 mg/L
< 190 mg/L
Suspended Solids
200-400 mg/L 100-200 mg/L <100 mg/L
PH 3.0-10.5 6.0-8.5 6.5-8.1
Total Dissolved Solids
6500 – 7500 mg/L
6500 – 7500 mg/L
<7500 mg/L
Ammonical Nitrogen
245 – 445 mg / L
230 – 430 mg / L
<40 mg / L
Oil & Grease 8 – 10 mg/L 8 – 10 mg/L < 10 mg/L
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP. ➢ The non-toxic effluent conforming to the GPCB standards is discharged into final
pumping station at Panoli and conveyed to FETP of NCTL and Panoli Industrial association for ultimate disposal in deep sea.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): -
D-6
In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
➢ NA
(For waste water treatment) M/s Bharuch Enviro Infrastructure Ankleshwar / Dahej
M/s Saurastra Enviro Projects Pvt. Ltd., Kutch/Dahej/Ankleshwar
M/s Detox India Ptv. Ltd. Kutch/Dahej/Ankleshwar
D-7
Simplified water balance diagram with reuse / recycle of waste water
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E Air
E1 E2
Brief Note on fuel-based heat energy requirement and worst case scenario thereof: The proponent uses furnace oil and natural gas for heat energy requirement. Two boiler of 10 MT and 17 MT are being used for generation of steam. Beside two thermic fluid heaters of 6 Kcal are also used for generation of hot oil, however it is not used in the proposed product. The company also produces power of 4290 KWH capacity through in-house natural gas-based power plant, For heat recovery, company uses waste heat recovery boiler of 2 MT/ hr capacity to recover waste heat of power plant. The company also proposes to put up a waste heat economizer to recover waste heat of boiler.
To conserve energy, company recycles steam condensate up to 65%. Various efforts are being made to increase steam condensate recovery further. Company carries out energy audit from external agency, once in a three-year period to identify opportunities for energy savings. The recommendations are compiled and tracked for implementation.
Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Existing & Proposed
Sr. No.
Source of emission With Capacit
y
Stack Height (mete
r)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions i.e. Air Polluta
nts
Permissible limit
APCM
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Existing (Flue Gas Emission)
1
Boiler 1 (17 MT) Boiler 2 (10 MT) Common Stack
54
NG /FO
NG – 40000
SM3/Day
And/or
FO – 17544 Lit/Day
PM 150 mg/Nm3 Stack with
adequate
height
SO2 100 ppm
NOx 50 ppm
2
Thermic Flued Heater (6Lac Kcal)
20
NG /FO
PM 150 mg/Nm3 Stack with
adequate
height
SO2 100 ppm
NOx 50 ppm
3 Power Plant 1
30
NG
PM 150 mg/Nm3 Stack with
adequate
height
SO2 100 ppm
NOx 50 ppm
4 Power Plant 2
30
NG
PM 150 mg/Nm3 Stack with
adequate
height
SO2 100 ppm
NOx 50 ppm
Proposed
1
GG Power Plant
30 Natural
Gas
12000 Sm3/Da
y
PM 120 mg/Nm3 Stack with
adequate
height
SO2 80 ppm
NOx 40 ppm
2
Steam Economizer
12 -
- PM 120 mg/Nm3 Stack with
adequate
height
SO2 80 ppm
NOx 40 ppm
3
D.G. Set (2000 KVA), 3no.
11(03 nos.
stack) HSD
6000 Lit/Day
PM 120 mg/Nm3 Stack with
adequate
height
SO2 80 ppm
NOx 40 ppm
E3 Process gas Existing & Proposed
Sr. No.
Specific Source of emission (Name of the Product & Process)
Type of emission
Stack/Vent Height (meter)
APCM
Scrubbing Media
Existing
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1 Process Stack
MPP-1
HBr 30 mg/Nm3
40
Packed Bed Scrubber
Alkali
Bromine 2 mg/Nm3
NOx 25 mg/Nm3
SO2 40 mg/Nm3
H2S 45 mg/Nm3
PM with pesticide compound 20
mg/Nm3
2 Process Stack MPP 2 Plant
HCl 20 mg/Nm3
26.5
Packed Bed
Scrubber
Alkali
CL2 09 mg/Nm3
HC 15 mg/Nm3
3 Process Stack MPP 3 Plant
HCl 20 mg/Nm3
26.5
Packed Bed Scrubber
Alkali
CL2 05 mg/Nm3
Mercaptan 0.5 ppm
NOx 25 mg/Nm3
NH3 30 mg/Nm3
4 Process Stack MPP 4 Plant
HCl 20 mg/Nm3
26.5
Packed Bed Scrubber
Alkali
Mercaptan 0.5 ppm
5 Process vent
MEE 1
HC 20 mg/Nm3
26.5
Packed Bed Scrubber
Alkali
PM 150 mg/Nm3
6 Process vent
MEE 2
HC 20 mg/Nm3
26.5
Packed Bed Scrubber
Alkali
PM 150 mg/Nm3
7 Dust Collector Vent MEE 2
PM 150 mg/Nm3 26.5 Dust
Collector
-
8 Fume Incinerator PM 50 mg/Nm3
40
Quencher,
multi- cyclone
& Packed
Bed Scrubb
er
Alkali
SO2 200 mg/Nm3
9 Rotary Kiln Incinerator
PM 50 mg/Nm3 Alkali
HCl 50 mg/Nm3
SO2 200 mg/Nm3
CO 300 mg/Nm3
(30 min)
CO 50 mg/Nm3 (24 hr)
TOC 20 mg/Nm3
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Total Dioxine and Furan 0.1 ng
TEQ/Nm3
Sb+ As + Pb + Cr + CO + Cu + Mn + Ni + V + their compound 0.05 mg/Nm3
PROPOSED PROCESS STACK
1 Process Stack MPP 4A Plant
HCl 20 mg/Nm3
26.5
Alkaline
Scrubber
Alkali
CL2 09 mg/Nm3
NH3 30 mg/Nm3
2 Charcoal Bed
absorber
formulation HC 20 mg/Nm
3 26 CHARCO
AL BED 1
PROPOSED PROCESS VENTS
1
Hydrogenation vents -2 nos.
HC 20 mg/Nm3 11
-
Note:
1. Two gasses raw material namely hydrogen gas and Dry HCl gas area used as raw material in the proposed product. Adequate scrubbing arrangements by way of connectivity the vents to alkali scrubber have been proposed.
2. Yearly approximately 3100 kl of bleed liquor generated from scrubbing process, which is treated in MEE.
E4 Fugitive emission details with its mitigation measures.
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For control of fugitive emission following practices are implemented in unit.
• The raw materials are stored in closed containers and will be handled through closed system to avoid the handling losses.
• Reflux condenser are provided over reactor.
• System of leak detection and repair of pump/pipeline based on preventive maintenance.
• The reactors are connected to an efficient condenser system with cooling/chilling water/brine circulation.
• Reactor and solvent handling pumps are having mechanical seals to prevent leakages. Also provide with breather valve to prevent losses.
• Solvent are taken from storage tank to reactors through closed pipe line.
• Storage tanks are vented through trap receiver & condenser operated on cooling water.
• The condensers are provided with sufficient HTA and residence time so as to prevent any loss of solvent.
• Proper earthing is provided were ever solvent handling is done.
• Entire plant is flameproof.
• Solvents are stored as per statutory requirement. Solvent are kept at a separate specified area with all the safety measures.
• The sprinkling of water is done along the internal roads in the plant in order to control the dust arising due to the movement of vehicular traffic.
• Thick greenbelt is developed around the plant to arrest the fugitive emissions.
F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.) ➢ Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle
within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and
calculations shall be incorporated in EMP details separately. Existing & Proposed
F1
Sr. No.
Type of Waste
Specific Source of generation
Category No.
Quantity MT/Year Mode of Disposal Existin
g Proposed
Total
1 Sludge (ETP) From ETP 34.3 900 0 900 Collection, storage, transportation and disposal in
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approved common TSDF
Sludge (MEE) From MEE 34.3 4113 1550 5663 Collection, storage, transportation and disposal in approved common TSDF
2 Incinerator Ash
From Incinerator
37.2 1646 0 1646 Collection, storage, transportation and disposal in approved common TSDF
3 Process solid wastes /residues
From Manufacturing Process
29.1 504 1000 1504 Collection, storage, & Incineration in house or in approved common incineration facility or co-incineration
4 Spent oil/other spent lube oil/ system
From Manufacturing Process
5.1 252.12 0 252.12
Collection, storage, & Incineration in house or in approved common incineration facility or
5 Packing waste
From Packing Unit
33.1 318 0 318 Recycled or sold to authorized end users or disposal in approved common TSDF
6 Discarded bag, containers/barrels
- 33.1 0.0 50000 Nos
50000 Nos
Contaminated drums to send to common decontamination facility or after decontamination recycled back or sold to authorized end users.
7 Date –Expired and off specification pesticides
- 29.3 2.4 0 2.4 Collection, storage, & Incineration in house or in approved common incineration facility
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8 Spent Solvent From Manufacturing Process
29.4 3000 5000 8000 Collection, storage, & Incineration in house or at authorized CHWI facility or Co-processing or reuse by in-house solvent distillation. In Some of the product where purity requirements are very high, recycling is not possible due to build-up of moisture or some specific impurity, such solvents are required to be sent to authorized as well as CPCB registered solvent distillation unit. Sold to GPCB Authorized rule 9 approved recyclers/ distillators/re-processor.
9 Solvent Distillation Residue
From Manufacturing Process
20.3 688 120 808 Collection, storage, & Incineration in house or in approved common incineration facility or co-Processing / incineration
10 Spent catalyst From Manufacturing Process
29.5 60 0 60 Collection, storage, & Incineration in house or in approved common incineration facility or sold to Authorized rule 9 approved recyclers/ re-processors for recovery & recycling
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11 Spent Carbon From Manufacturing Process
36.2 120 0 120 Collection, storage, & Incineration in house or in approved common incineration facility or sold to Authorized rule 9 approved recyclers/ re-processors for recovery
12 Spent Resin From Manufacturing Process
35.2 2 0 2 Collection, storage, transportation and disposal in approved common TSDF
13 Filter & Filter cake
From Manufacturing Process
35.1 4.32 0 4.32 Collection, storage, & Incineration in house or in approved common incineration facility
For API product
Input kg Output kg
Diethylmalonate 413 Liquid Waste 3372
Sodium nitrite 256 Water Wash 10321
Acetic acid (Net ) 295 Aqueous layer 4710
Sodium chloride 331 By-Product (H2SO4) 323
Water 36735 Solvent Recycle 7245
H2So4 1115 Distilled Solvent 6452
Ammona solution 1947 Spent Solvent 1613
Magnesium sulphate anhydrous 41
Solvent Distillation Residue 39
Ethyl acetate 9925 Residue 323
H2 9 By-Product (HCl) 6775
HCl 566 Solvent Rcovery
14434
Sodium Sulfite 8442 By-Product (NaBr/HBr) 19355
NaOH Lye 1027 Product 1000
40% Gyloxal 1675
Acetonitrile 6872
Methanol 4738
Bromine 1575
Total 75962 75962
F2 Membership details of TSDF, CHWIF etc. Unit has membership of TSDF site of
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(For HW management) M/s Bharuch Enviro Infrastructure Ankleshwar / Dahej M/s Saurastra Enviro Projects Pvt. Ltd., Kutch/Dahej M/s Detox India Pvt. Ltd. Kutch/Dahej/Ankleshwar
F3 Details of Non-Hazardous waste & its disposal (MSW and others)
NA
G Solvent management, VOC emissions etc.
G1 Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)
Solvent management, VOC emissions etc. Solvent Management Plan
Atmospheric distillation of Solvents like, MDC etc.: Primary Condenser HE-01: Cooling Tower water will be used to condense the solvents and the non-condensed vapors will be condensed in a Secondary Condenser Secondary Condenser HE-02: Chilled water at 6 0C will be used to condense the non-condensed vapors in the Secondary Condenser VOC Trap Condenser HE-03: Chilled Brine at -35 0C will be used to trap any traces of Solvent which is slipped from Secondary condenser.
In API manufacturing solvents are used for
• Work up for chemical reaction
• Removal of impurities
• Purification of crude API
• Cleaning of equipment’s
• Removal of moisture Therefore, quality of solvent should be like to like with fresh solvent. It is
observed that contamination in solvent make the drug also contaminated.
• Washing of ml for removal of impurities
• Solvent containing dissolved solids are flash distilled
• Solvent containing miscible impurity or other solvent are fractional distilled
• Solvent are distilled in useful fraction & non-useful fractions (containing low boilers & high boilers) low boilers are mixed solvent & high boilers are along with residues
Note –some of the solvents are recovered in-situ & directly used in next batch. (part of process)
G2 Brief Note on LDAR proposed: Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB guidelines. LDAR Logbooks shall be maintained.
G3 VOC emission sources and its mitigation measures
➢ Provision of mechanical seal in pump.
➢ Regular inspection of tank roof seals.
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➢ Adequate measures for the minimization/prevention of the fugitive emission.
➢ Regular maintenance of valves, pumps and other equipment to prevent leakage.
➢ Entire process to be carried out in the closed reactors with proper maintenance of
temperature.
➢ Regular periodic monitoring of work area to check the fugitive emission.
➢ Adequate stack heights as per the CPCB estimation will be provides at all locations
to reduce GLCs of pollutants.
➢ Air Pollution Control System is installed in the plant.
H SAFETY details
H1 • Details regarding storage of Hazardous chemicals
Sr. No.
Name of Materials Stored
Quantity (Maximum)
Location of Storage
Operating Pr./Temp
Type of Hazard
Control provided
BROMINE (IN TANKS)
40 MT MPP-1 Atmospheric
Bromine Leakage Toxic gas./Toxic liquid
Neutralizing media provided. Arrangement made for respiratory protection. Dyke provided. Detection & Alarm system provided. Kept under vacuum. Scrubber Provided Foam generator provided Buffer tank Provided with discharge facility
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METHANOL
15 Kl Tank Farm Atmospheric
Fire Stored in explosive yard Area is restricted entry area. Proper earthing and Bonding provided. Smoking prohibited in area Skirting provided. Hydrant point provided near by. Medium Velocity sprinkler provided
HYDROGEN NEST
414 kg 810 cylinders each)
Hydrogenation
150 kg/cm2
Fire leakage-detection and alarm system provided Proper earthing provided hydrant system provided area restricted from unauthorized person operation from remote by PLC Hydrogen leakage detector provided. Water sprinkler provided Area is restricted entry area Provided proper Earthing to the nest. Only FLP tools and equipments are used in the area.
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CAT-55 200 kg Hydrogenation
Atmospheric
fire due to pyropheric nature
Store in wet / aqueous media SOP made for safe handling Training given to personnel handling it
SODIUM NITRITE
5 MT MPP3/ 4 Atmospheric
Detonating properties
Keep in restricted area. Kept at isolated area SOP made for safe handling
HCL 30 KL MPP2 Atmospheric
Health hazards
Keep in restricted area. Kept at isolated area SOP made for safe handling PVC Air Pressure suit to be used while loose handling. Dyke walls provided
SULFURIC ACID
15 KL Tank Farm Atmospheric
Health hazards
Keep in restricted area. Kept at isolated area SOP made for safe handling PVC Air Pressure suit to be used while loose handling. Dyke walls provided
SODIUM SULFITE
10 MT RM Storage/ MPP-4A
Atmospheric
Health Hazard
Keep in restricted area. Kept at isolated area SOP made for safe handling
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ACETONITRIL
20 MT RM Storage/ MPP-4A
Atmospheric
Fire and Health Hazard
Keep in restricted area. Kept at isolated area SOP made for safe handling
ETHYL ACETATE
20.0 T Ware House
Atmospheric
Health Hazard
Keep in restricted area. Kept at isolated area Proper earthing and Bonding provided. Smoking prohibited in area SOP made for safe handling PVC suit and air bubbler to be used while loose handling
N-METHYL-2-PYRROLIDONE
15.0 Warehouse
Atmospheric
Health Hazard Fire Hazard
SOP made for safe handling Area is restricted entry area. Proper earthing and Bonding provided. Smoking prohibited in area Skirting provided. Hydrant point provided nearby
Safety details of Hazardous chemicals (To be stored in storage tanks)
Given in above table Applicability of PESO:
1. PESO license for Hydrogen is required but existing facility already have PESO license for storage of hydrogen cylinder so no need to take approval for additional hydrogen quantity.
2. For Dry HCl, number of cylinder used at a time are less than 10, therefore no license is required.
H2 Types of hazardous Processes involved and its safety measures
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Name of hazardous process & operation
Material in the process/
operation with their
Qty.
Name of the equipment &
and its location
Operating parameters Temp/Pr.
Type of hazard
possible Toxic gas release /
Fire / explosion / run away reaction /
rupture etc
Control measures provided
Hydrogenation for
DEAM.HCL
Di-methyl melonate– 413
Kg Sodium Nitrate – 256 Kg Acetic Acid -
295 kg
OR-1502, SS-316 6 Kl
1st Floor (Hydrogenatio
n)
Hydrogen Feed= 55-60°C &
Pressure 4.5 to 5.0Kg/Cm2
*Pressurization
Hydrogen Feeding actuated valves inter locked with reactor temp >65°C & Pressure >5.0 kg/Cm2 If temperature > 70°C and Pressure >5.5 Kg/Cm2 Agitator stopped SRV,RD, Emergency vent, Separate Blower
Bromination for
DEAM.HCL/ Bromo
Compound
Bromine=1575 kg DM water=19538kg
Intermediate mass = 1154kg
OR05701 (1ST Floor –
MPP-1A)
Temp=5-10°C Pressure=Negati
ve
Run away reaction
/ Rupture
Rupture disc vent outlet connected to Knock out pot Interlocks: If temperature is <2°C or>10°C, pressure :0.25Kg/cm2, Agitation stopped, feeding stopped. Temperature Indicator
H3 Details of fire load calculation
Total Plot area 56868
Area utilized for plant activity 34120.8 m2
Area utilized for hazardous chemical storage
3412 m2
Number of floors 4
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Water requirement for firefighting in KLD
273 KL/Hr
Water storage tank provided for firefighting in KL
450
Details of Hydrant pumps Main Pump 1 nos Jockey Pump 2 nos Diesel Pump 1 nos ( stand by)
Nearest fire station Panoli
Applicability of off site emergency plan
Existing facility have Onsite / offsite emergency plan and submitted to authority, will be update after obtaining EC considering process hazard before start-up production activity.
H4 Details of Fire NOC/Certificate: DPMC certificate no. 028 and membership no.LM/LE/030
H5 Details of Occupational Health Centre (OHC)
Number of permanent Employee 714
Number of contractual person/Labour 1000
Area provided for OHC 300 sq. feet
Number of First Aid boxes 5 nos.
Nearest General hospital Jayaben hospital
Name of Antidotes to be stored in plant 1. Inj.Atropin 2. Inj.PAM
• During the meeting dated 07.06.2021, PP presented and submitted as below:
➢ Following control measures will be taken to avoid contamination of dusting of
pesticide and volatile material from pesticide manufacturing plant towards proposed
API intermediate manufacturing plant.
✓ The utility will be separate for pharma plant & API intermediate manufacturing
plant.
✓ Separate and isolated raw material and finished good storage for existing
pesticide and proposed API plant.
✓ Fencing will provide between pharma plant and pesticide unit.
✓ Manpower will be separate & different for the pharma plant & API Plant
✓ API product will be 24 hrs vigilance, that there will be no contamination.
✓ Entry and exit of the both plant will be separated & different.
➢ Application as new API intermediate product excluding existing Pesticide products.
➢ Undertaking for discontinuation of banned technical pesticide products.
➢ Manufacturing process with chemical reaction & material balance for DEAM/DEAM,
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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HCl/ Bromo Compound.
➢ Revised plan layout.
➢ Separate manpower for proposed API plant and existing pesticide manufacturing
plant will be provided. Undertaking is submitted.
➢ Revised waste water treatment proposal and water balance diagram considering
compliance of Direction under section 18(1) (B) for additional waste water discharge
at FETP of M/s NCTL for further treatment considering quality and quantity of
effluent.
➢ For proposed project they will use only natural gas as fuel.
➢ They have submitted the undertaking for discontinue the use of Furnace Oil.
➢ Revised Hazardous waste matrix with sound management mentioning distilled
solvent, HCl, sulphuric acid and NaBr as Hazardous waste with technical justification
for quantity along with mass balance.
➢ Risk assessment for storage and handling of hazardous waste and its effect in
surrounding habitat area with safety control measures.
➢ Revised EMP.
➢ Copy of fire NOC of existing plant.
• Committee deliberated on the above mentioned reply and found that there is descripancy in
compliance of Direction under section 18(1) (B) for additional waste water discharge at
FETP of M/s NCTL for further treatment considering quality and quantity of effluent.
• After detailed deliberation, Committee unanimously decided to consider the project in
one of upcoming meeting after submission of following documents,
1. Revised waste water treatment proposal and water balance diagram considering compliance of Direction under section 18(1) (B) for additional waste water discharge at FETP of M/s NCTL for further treatment considering quality and quantity of effluent.
• Later on PP replied to the ADS through Parivesh Portal.
• The proposal was considered in the SEAC video conference meeting dated 01-09-2021.
• Project proponent (PP) and Technical expert of PP, M/s. Shree Green Consultants remains
present during video conference meeting.
• Committee discussed on revised water balance diagram submitted by the PP. PP will
discharge 218 KLD will be sent to NCT.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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condition:
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon’ble Supreme
Court of India in Civil Appeal no. 8478/2020 regarding operation of the Hon’ble NGT orders
dated 10/07/2019 & 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change in
product mix, after the 30th September 2020, considered as per the provisions in force at that
time as mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients
(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any
subsequent amendments.
4. PP shall submit six monthly compliance report of Environmental Clearance without fail and
the same shall be critically assessed by the regulatory authority.
5. Total number of products manufacturing shall not exceeding one (1) at a given point of time
as per the plant capacity shown in plant layout.
6. Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB
directions to all SPCB vide letter no. B-29016/04/06PCI-1/5401 dated 05/02/2014 for
effluent discharge and air emission as per pollutants discharge/emission from respective
project and an arrangement shall also be done for reflecting the online monitoring results on
the company's server, which can be assessable by the GPCB/CPCB on real time basis.
[For Small/Large/Medium (Red Category) & Whichever (Air emission & Effluent
discharge) is applicable].
7. Close loop solvent recovery system with adequate condenser system shall be provided to
recover solvent vapours in such a manner that recovery shall be maximum and recovered
solvent shall be reused in the process within premises.
8. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the
CPCB guidelines. LDAR Logbooks shall be maintained
WATER
9. Total water requirement for the project shall not exceed 1203 KLD. Unit shall reuse 234 KLD
of treated industrial effluent within premises. Hence, fresh water requirement shall not
exceed 969 KLD and it shall be met through GIDC only.
10. The industrial effluent generation from the project shall not exceed 566 KLD.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 31 of 357
11. Industrial effluent shall be segregated into two streams (1) High COD and TDS effluent (2)
Low COD and TDS effluent and it shall be managed as below.
• High COD and TDS effluent (227 KLD)
➢ 227 KLD will be treated in MEE and condensate will be recycled into cooling
tower.
• Low COD and TDS effluent (251 KLD):
➢ 251 KLD effluent will be treated into ETP and out of this 33 KLD treated
effluent will be recycled into incinerator/ quenching.
➢ Remaining 218 KLD will be discharged into NCT for further treatment and
disposal into deep sea.
12. Unit shall feed wastewater to in-house MEE only after ensuring content of effluent for
COD/VOC so as not to get air borne during evaporation in order to achieve no adverse
impacts on Environment and Human Health.
13. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during any shut down of in-house MEE.
14. Treated waste water shall be sent to common facilities (CETP, Common MEE, Spray dryer
etc.) only after complying with the inlet norms of common facilities prescribed by GPCB to
ensure no adverse impact on Human Health and Environment
15. Domestic wastewater generation shall not exceed 50 KL/day for proposed project and it
shall be treated in STP. It shall not be disposed off through soak pit/ septic tank.
16. Domestic wastewater generation shall not exceed 50 KL/day for proposed project and it
shall be treated in STP. Treated sewage shall be recycled after achieving on-land discharge
norms prescribed by the GPCB.
17. During monsoon season when treated sewage may not be required for the plantation /
Gardening / Green belt purpose, it shall be stored within premises. There shall be no
discharge of waste water outside the premises in any case.
18. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
19. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
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AIR
20. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned in
flue gas matrix.
21. Unit shall provide APCM and stack height as mentioned in process gas matrix.
22. PP shall use approved fuels only as fuel in boilers.
23. Alkali scrubbing medium shall be installed for control of Process Gas emission.
HAZARDOUS & SOLID WASTE
24. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
25. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
26. The PP shall develop green belt within premises (22748.00 Sq. m i.e. 33 % of the total plot
area) as per the undertaking submitted before SEAC. Green belt shall be developed
with native plant species that are significant and used for the pollution abatement as per the
CPCB guidelines. It shall be implemented within 3 years of operation phase in consultation
with GPCB.
27. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 33 of 357
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
m) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.
n) Unit shall Store Bromine Bottle in cool dry separate area, out of direct sunlight.
2 SIA/GJ/IND2/152953/2020 Zaffre Synthesis LLP
Block No: 344/P/1, Lunej, Khambhat, Anand
EC reconsideration
Category of the unit: 5(f)
Project status: New
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/152953/2020 for
obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is a new unit proposes for expansion in manufacturing of synthetic organic chemicals
[API and API Intermediates] as tabulated below,
Sr. No
Name of the Products API OR
IntermediaCAS no. /
Quantity
End-use of the products*
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 34 of 357
. te CI no. MT/month
1 Para Toluic Acid Intermediat
e 99-94-
5 20
Chiral resolving agent
2 6-Chloro-2-Hexanone Intermediat
e 10226-30-9
6 to treat blood flow problem
3 2 Acetyl Thiophene Intermediat
e 88-15-
3 20 to treat depression and
anxiety
4 Dibutyl Oxalate Intermediat
e 2050-60-4
7.5 anticonvulsants/ hypnotics
5 Methyl Thioglycolate Intermediat
e 2365-48-2
25 nonsteroidal anti-inflammatory drugs(NSAID)
6 Celecoxib API 169590-
42-5 3 nonsteroidal anti-
inflammatory drug(NSAID)
7 2 Thiophene Ethanol Intermediat
e 5402-55-1
15 antiplatelet medications
8
Heptylamine 99% Intermediate
111-68-2
15 Intermediate for BulkDrug Ramelteon(melatonin
receptor antagonist)Insomnia Drug.
9 Domperidone API 57808-
66-9 5
dopamine antagonists
10 Glycine Methyl Ester Hydrochloride
Intermediate
5680-79-5
50 nonsteroidal anti-inflammatory drugs(NSAID)
11 Abacavir sulphate API 136470
-78-5 1.5 Antiviral,
nucleosidereversetranscriptase inhibitors-NRTI
12 Glycine Intermediat
e 56-40-
6 20 anti-ulcer and anti-
inflammatory drug
13 3,4-Methylenthedioxyl Phenol (Sesamol)
Intermediate
533-31-3
50 Antidepressant selective serotonin reuptake inhibitors
(SSRIs)
14 1 Benzyl piperazine 99% API 2759-
28-6 10 xenobiotic, recreational drug,
psychotropic drug and a serotonergic agonist
15 1-(3-chlorophenyl) piperazine99%
Intermediate
65369-76-8
10 SR-2B and SR-2C receptor agonist
16 1-(4-Flurophenyl)piperazine 98%
recreational drugs(API)
64090-19-3
5 recreational drugs
17 1-[2-(2-hydroxyethyl)ethoxy] piperazine 99%
Intermediate
13349-82-1
5 antipsychotics
18 1-(2-Methoxyphenyl) piperazine hydrochloride 98%
Intermediate
5464-78-8
5 reference material
for forensic laboratories
19 1-(3-chloropropyl)-4-(3chlorophenyl)piperazin
Intermediate
52605-52-4
15 antidepressant
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Page 35 of 357
e hydrochloride 98%
20 4 Benzyloxy aniline hydrochloride 98%
Intermediate
51388-20-6
10 building block for biochemical synthesis
21 Isovaleryl chloride 98% Intermediat
e 108-12-3
5 Intermediate of Aliskiren
22 1-Indanone 98% Intermediat
e 83-33-
0 5
acetylcholinesterase inhibitor
23 Vetraldehyde 98% Flavorant
and odorant
120-14-9
5 flavorant and odorant
24 2 -Methoxybenzyl amine 98%
Intermediate
6850-57-3
10 Intermediate in the biosynthesis ofCapsaicin
25 Cyclopropylthio acetic acid
Intermediate
162515-68-
6
5 leukotriene receptor
antagonists
26 2- Chlorobenzimidazole98%
Intermediate
4857-06-1
5 Intermediate of
Mizolastine.Anti-Histamine
27 4,7 Dichloroquionoline Intermediat
e 86-98-
6 15.0
Antimalarial
28 Hydroxy Chloroquine Sulphate
API 747-36-4
25.0 Antimalarial
29 R & D products 0.1
Total 373.1
ENDUSE OF PRODUCTS
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category of
Product (API/ Intermediate)
In case of Intermediate stage of API Said API is used for End Use of said API
Name of API in which
Stage i.e. n-1, n-2
CAS No. (API)
1 Para Toluic acid 99-94-5 Intermediate Di-p-Toluoyl D Tartaric acid and Dip-Toluoyl L Tartaric acid
n-1 3263468-7 and 32634-66-5
Chiral resolving agent
2 6-Chloro-2-Hexanone
10226-30-9
Intermediate Pentoxifylline n-2 649305-6 to treat blood flow problem
3 2 Acetyl Thiophene
88-15-3 Intermediate Duloxetine hydrochloride
n-1 13643434-9
to treat depression and anxiety
4 Dibutyl oxalate 2050-60-4 Intermediate Phenobarbital n-1 50-06-6 anticonvulsants/ hypnotics
5 Methyl thioglycolate
2365-48-2 Intermediate Tenoxicam n-2 5980437-4 nonsteroidal anti-inflammatory
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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drugs (NSAID)
6 Celecoxib 169590-42-5
API Celecoxib - 16959042-5
nonsteroidal antidrug inflammatory (NSAID)
7 2 Thiophene Ethanol
5402-55-1 Intermediate Clopidogrel n-2 11366584-2
antiplatelet medications
8 Heptylamine 99% 111-68-2 Intermediate Drug Intermediate
n-1 [19659726-9]
Intermediate for Bulk Drug Ramelteon (melatonin receptor antagonist) Insomnia Drug.
9 Domperidone 57808-66-9
API Domperidone - 5780866-9 dopamine antagonists
10 Glycine Methyl Ester Hydrochloride
5680-79-5 Intermediate Tenoxicam n-2 5980437-4 Nonsteroidal anti- inflammatory drugs (NSAID)
11 Abacavir sulfate 136470-78-5
API Abacavir sulfate
- 13647078-5
Antiviral, nucleoside reverse transcriptase inhibitors-NRTI
12 Glycine 56-40-6 Intermediate Rebamipide n-1 9009804-7 anti-ulcer and anti-inflammatory drug
13 3,4-Methylenthedioxyl Phenol (Sesamol)
533-31-3 Intermediate paroxetine n-2 6186908-7 Antidepressant selective serotonin reuptake inhibitors (SSRIs)
14 1-Benzyl
piperazine 99%
2759-28-6 API 1 Benzyl
piperazine
- 275928-6 xenobiotic,
recreational
drug,
psychotropic
drug and a
serotonergic
agonist
15 1- (3-chlorophenyl)
piperazine 99%
65369-76-
8
Intermediate SR-2B and
SR-2C
receptor
n-2 6536976-8 SR-2B and SR-
2C
receptor agonist
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 37 of 357
agonist
16 1-(4-Flurophenyl)
piperazine 98%
6409019-3
Recreational
drugs (API)
recreational
drugs
- 6409019-3 recreational
drugs
17 1-[2-(2-
hydroxyethyl)
ethoxy] piperazine
99%
13349-82-
1
Intermediate quetiapine
fumarate
n-2 11197469-
7
antipsychotics
18 1-(2-
Methoxyphenyl)
piperazine
hydrochloride 98%
5464-78-8 Intermediate reference
material for
forensic
laboratories
n-2 546478-8 reference material for forensic laboratories
19 1-(3-chloropropyl)-
4-(3chlorophenyl)
piperazine
hydrochloride 98%
52605-52-
4
Intermediate Trazodone n-2 1979493-5 antidepressant
20 4-Benzyloxy
aniline
hydrochloride 98%
51388-20-
6
Intermediate Biochemical
Synthesis
n-1 - building block
for biochemical
synthesis
21 Isovaleryl chloride
98%
108-12-3 Intermediate Bulk Drug
Intermediate
n-1 17333457-
1
Intermediate of
Aliskiren
22 1-Indanone 98% 83-33-0 Intermediate 11H-Indeno-
[1,2-
b]quinolin-10-
ylamine
n-1 - acetylcholineste
rase inhibitor
23 Vetraldehyde 98% 120-14-9 Flavorant and
odorant (API)
flavorant and
odoran
- 120-149 flavorant and
odoran
24 2 -Methoxybenzyl
amine 98%
6850-57-3 Intermediate Biosynthesis
Intermdiate
n-1 Intermediate in the biosynthesis of Capsiacin
25 Cyclopropylthio
acetic acid
162515-
68-6
Intermediate Montelukast
sodium
n-2 15176702-
1
leukotriene
receptor
antagonists
26 2-
Chlorobenzimidaz
ole
98%
4857-06-1 Intermediate Raw material of 1methyl-2-
chlorobenzimi
dazole
n-1 184902-1 Intermediate of Mizolastine. Anti Histamine
27 4,7
Dichloroquionoline
86-98-6 Intermediate Hydroxy
Chloroquine
Sulphate
n-1 747-364 Antimalaria
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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28 Hydroxy
Chloroquin
e Sulphate
747-36-4 API Hydroxy
Chloroquine
Sulphate
- 747-364 Antimalaria
29 R &D product
• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA
Notification 2006 and amendment dated 27th March, 2020.
• The proposal was considered in the SEAC video conference meeting dated 12.03.2021
• During the meeting dated 12.03.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and Technical expert of PP, M/s. Shree Green Consultants remains
present during video conference meeting.
• This is a Greenfield project for API and Its Intermediates plant located at Village - Lunej, Tal
- Khambhat, Dist - Anand, outside Notified area. Source of water supply is bore well.
Committee insisted for ground water source will not be provided without CGWA permission.
• PP submitted Google map showing that there is no any water bodies, villages, School,
monuments etc. within 500 m radius of the project site. There are no Eco sensitive zones,
wild life sanctuaries within the 10 km area from the boundary of the project site. Looking to
Google map showing coastal area in nearby of proposed project, Committee insisted for
mentioning CRZ applicability to proposed project with CRZ map super imposition on
proposed project area and High tide line distance from proposed project. Product profile
along with End Use discussed in depth. Committee noted that PP submitted area adequacy
and layout plan with mentioning adequate size peripheral road, green belt, storage area as
per type of hazard etc. PP said that they will not manufacture more than five products at a
time from proposed product list. Committee insisted for revised layout plan with mentioning
separate entry and exit, storage of Hazardous chemicals considering its type of hazard and
as per compatibility chart, fire hydrant network with water sprinkler system and revised area
adequacy with land break up. Committee insisted for technical justification regarding R & d
products capacity proposed 2.5 MT/Month in place of Kg/Month with details regarding
proposed R & D laboratory infrastructure and also mentioning water, air and Hazardous
waste details, specifically for R & D section.
• Committee noted that total industrial effluent stream will be segregated and high COD
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 39 of 357
stream will be treated in in-house MEE. Low COD stream will be treated in ETP and RO
plant. Committee insisted for revised water balance diagram and treatment proposal of
primary ETP and solvent stripper for high COD stream before evaporating, in place of
directly evaporation in in-house MEE.
• Committee noted that bio fuel and white coal will be used as fuel for boiler, HAG and thermo
pack. Looking to APCM and stack height and biofuel, Committee insisted for revised air
matrix with mentioning approved fuel other than biofuel, adequate APCM like bag filter
instead of dust collector and stack height of 30 meter in place of 15 meter with HAG. Two
stage scrubbers will be provided as APCM with each process stacks. Technical expert
addressed hazardous waste management including scrubber bleed liquor and spent solvent
disposal.
• Committee noted that PP has addressed LDAR and solvent recovery, green belt
development, auto control system for critical process, EMP and CER for proposed project.
Committee insisted for revised EMP with mentioning cost of DCS control system for critical
process, cost of oxygen detector, fire hydrant network cost, adequate APCM and ETP cost,
adequate size fire water tank cost and adequate fire extinguisher like trailer pump and fire
proximity suit provision. PP explained regarding safety control measures for Hazardous
chemical storage and its management. Committee discussed in length regarding fire hydrant
system, evacuation plan. Committee insisted for submission of risk assessment for
hydrogen storage and its safety measures with superimposition of dispersion model for it on
proposed project area and its impact on surrounding habitat and its mitigation measures.
• Since, the unit falls in B2 category as per the MoEF&CC’s amended EIA Notification vide
S.O. 1223(E) dated 27.03.2020, the public consultation is not applicable as per paragraph
7(i) III (i) (e) of the Environment Impact Assessment Notification-2006.
• After detailed discussion, Committee unanimously decided to consider the project
only after submission of following documents,.
1. CRZ applicability to proposed project with CRZ map super imposition on proposed
project area and High tide line distance from proposed project.
2. Technical justification regarding R & D products capacity proposed 2.5 MT/Month in
place of Kg/Month with details regarding proposed R & D laboratory infrastructure
and also mentioning water, air and Hazardous waste details, specifically for R & D
section.
3. Revised layout plan with mentioning separate entry and exit, storage of Hazardous
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 40 of 357
chemicals considering its type of hazard and as per compatibility chart, fire hydrant
network with water sprinkler system and revised area adequacy with land break up.
4. Revised water balance diagram and treatment proposal of primary ETP and solvent
stripper for high COD stream before evaporating, in place of directly evaporation in
in-house MEE.
5. Revised air matrix with mentioning approved fuel other than biofuel, adequate APCM
like bag filter instead of dust collector and stack height of 30 meter in place of 15
meter with HAG.
6. Revised EMP with mentioning cost of DCS control system for critical process, cost of
oxygen detector, fire hydrant network cost, adequate APCM and ETP cost, adequate
size fire water tank cost and adequate fire extinguisher like trailer pump and fire
proximity suit provision.
7. Submission of risk assessment for hydrogen storage and its safety measures with
superimposition of dispersion model for it on proposed project area and its impact on
surrounding habitat and its mitigation measures.
• PP submitted their reply for the query raised by SEAC during SEAC meeting dated
16.02.2021 through email.
• The proposal was reconsidered in the SEAC video conference meeting dated 07.06.2021.
• Revised Salient features of the project including Water, Air and Hazardous waste
management are as under:
Sr. no. Particulars Details
A-1 Total cost of Proposed Project
(Rs. in Crores):
Total Project
25 Crores
Break-up of proposed project Cost:
Details Project Cost
(Rs. In Crores)
Land 4.0
Building 9.21
Machinery 7.4
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 41 of 357
EPCM cost 4.39
Total 25
A-2 Details of Environmental Management Plan
(EMP)
As below:
Sr.
No. Unit Detail
Capital
Cost
(Rs. In
Lacs)
Cost (Rs. In Lacs/Month)
Operating Maintenance Recurring
1 Water ETP 153.00 5.25 2.25 7.50
2 Air APCM 45.00 5.60 2.40 8.00
3
Hazardous
Management
and AWH
Monitoring
- 40.00 2.80 1.20 4.00
4
Fire & Safety
(Part of Project
cost) *
Provision of Safety
Measures including fire
alarm systems, fire
hydrant network, Fire
Water Tank, Fire
Extinguisher and Trailer
Pump system, Earthing
relays and fire sprinklers
65.00 3.00 2.00 5.00
5 Green Belt
Development - 17.00 1.36 0.24 1.60
6 Noise Pollution
Control 15.00 0.56 0.24 0.80
7 Occupational
Health - 24.00 2.80 0.00 2.80
8
DCS & PLC
system (Part of
Project cost),
oxygen detector
- 135.00 5.75 3.00 8.75
Total - 494.00 27.12 11.33 38.45
Summary
Cost of Project in Crores per Annum: 25
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 42 of 357
EMP Capital Cost in Crores per Annum and
Percentage:
4.94 (19.76%)
EMP Recurring Cost in Crores per Annum
and Percentage:
4.6 (18.4 %)
A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA,
CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2
times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC’s OM
vide 31.10.2019.)
% as per the OM Rs. in Crores
2 0.5
Brief note on proposed activities:
➢
B Land / Plot ownership details:
(Total: 4450.00 Sq. m)
B-1 Plot area
Total Plot area
4450.00 Sq. m
B-2 Brief note on Area adequacy in line to proposed project activities:
B-3 Green belt area
Total
(Sq. meter)
Area in
Sq. meter
1470.00
% of total
area
33.00
C Employment generation
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 43 of 357
Total
100 Nos
D WATER
D-1
Source of Water Supply
(GIDC, Bore well, Surface water, Tanker supply etc...)
Status of permission from the concern authority.
➢ Outside farming well
D-2
Water consumption (KLD)
Category Quantity KLD Remarks
(A) Domestic 5.00 -
(B) Gardening 3.00 -
(C) Industrial
Process 57.00 -
Washing& Cooling 15.00 -
Boiler 15.00 -
Scrubber 5.00 -
Industrial Total 92.00
Grand Total
(A+B+C)
100.00 -
Brief Note on worst case scenario for water
consumption:
-
Summary of water
requirement
Quantity
KLD
Remarks
Total water
requirement
100.00 --
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 44 of 357
for the project
(A)
Quantity to be
recycled (B)
74.00 --
Total fresh water
requirement
(C)
26.00 --
Ensure Total water requirement = Fresh
water + Recycled water
i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility.
[Source of reuse & application area]
Source of
waste
water for
reuse in
KLD (From
where it is
coming)
Application
area with
quantity in
KLD (Where it
is used)
Characteristics
of waste water
to be reused
(COD, BOD, TDS etc.)
Remarks
regarding
feasibility
to reuse
74 KLD
from ETP &
MEE with
Tertiary
treatment
74 KLD to be reused
in all processes
of industrial process.
COD < 30 mg/L BOD < 10 mg/L TDS < 100 mg/L
In case of no reuse/recycle of waste water, Give brief
note on justification as why no reuse/recycle.
➢
D-3
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 45 of 357
Waste water generation (KLD)
Category Waste water
KLD
Remarks
(A) Domestic 4.50 --
(B) Industrial
Process 65.00 (40.5 LTDS +
24.5 HTDS)
--
Washing Cooling 7.00
Boiler 2.00
Others 5.00*
Total Industrial
waste water
79.00
Total [A + B] 83.50
Brief Note on worst case scenario for waste water generation(Qualitative and
Quantitative):
Brief justification in case of no process effluent generation or no industrial effluent
generation or no high concentration effluent generation from proposed project
(Whichever is applicable).
➢
D-4 Mode of Disposal & Final meeting point
-
Domestic: ➢ The Total Waste Water generation will be 83.50 KLD [Domestic Waste water 4.5 KLD + Industrial Waste Water 74.0 KLD + Scrubbing water 5.0 KLD].
➢ ➢ Waste water will be segregated into two stream, High Concentrate Stream
and Low Concentrate Stream. ➢ ➢ Low Concentrate effluent 54.0 KLD (Domestic waste water 4.5 KLD +
Industrial Waste water 49.5 KLD) will be treated in Proposed ETP followed by RO. RO permeate 44.00 KLD will be reused in plant activities and RO reject 10.0 KLD will be sent to MEE for further treatment.
➢ ➢ High Concentrate effluent 24.5 KLD (Industrial) along with RO Reject will be
treated in multi effect evaporator. MEE condensate (30 KLD) will be reused
Industrial:
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 46 of 357
in plant activities and MEE salt will be disposed of at TSDF site. ➢ Scrubbing waste salt will be sent to TSDF site.
Clearly mention about final disposal
D-5 Treatment facilities
For Domestic waste water:
Capacity of STP: NA
Domestic effluent will be treated in proposed ETP along with industrial effluent
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case
of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
Parameter Value
COD < 100 mg/l
BOD < 30 mg/l
Suspended Solids < 100 mg/l
PH 6.5 to 8.5
Total Dissolved Solids < 2100 mg/I
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention
and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ Not applicable
There is no any CETP discharge, thus it is not applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
➢ The Total Waste Water generation will be 83.50 KLD [Domestic Waste water 4.5 KLD + Industrial Waste Water 74.0 KLD + Scrubbing water 5.0 KLD].
➢ Waste water will be segregated into two stream, High Concentrate Stream and Low Concentrate Stream.
➢ Low Concentrate effluent 54.0 KLD (Domestic waste water 4.5 KLD + Industrial Waste water 49.5 KLD) will be treated in Proposed ETP followed by RO. RO permeate 44.00 KLD will be reused in plant activities and RO reject 10.0 KLD will be sent to MEE for further treatment.
➢ High Concentrate effluent 24.5 KLD (Industrial) along with RO Reject will be treated in multi effect evaporator. MEE condensate (30 KLD) will be reused in plant activities and MEE salt will be disposed off at TSDF site.
➢ Scrubbing waste salt will be sent to TSDF site.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF
etc.
Name of Common facility (CF) (For waste water treatment)
➢ NA
Membership of Common facility (CF) mentioning total capacity, consented
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 47 of 357
quantity, occupied capacity and spare capacity and norms of acceptance
of effluent from member units in-line with the direction given by GPCB
vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
➢ NA
D-7 Simplified water balance diagram with reuse / recycle of waste water
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case
scenario thereof: NA
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the
MOEFCC’s OM vide dated 31.10.2019)
Sr.
no.
Source
of
emission
With
Capacity
Stack
Height
(meter)
Type of
Fuel
Quantity of
Fuel
MT/Day
Type of
emissions i.e.
Air Pollutants
Air Pollution
Control
Measures
(APCM)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 48 of 357
1
Steam
Boiler -1
(3000
Kg/hr)
30
Briquettes
of bio coal
0.2 T/hr
4.8MT/day PM 150 mg/Nm³
SO2 100 ppm
NOx 50 ppm
Bag filter
&water
scrubber
2
Steam
Boiler -2
(3000
Kg/hr)
30
Briquettes
of bio coal
0.2 T/hr
4.8MT/day PM 150 mg/Nm³
SO2 100 ppm
NOx 50 ppm
Bag filter
&water
scrubber
3 Hot Air
Generator 30
Briquettes
of bio coal
0.2 T/hr
4.8MT/day PM 150 mg/Nm³
SO2 100 ppm
NOx 50 ppm
Bag filter
4.
TFH
(600000
L
Kcal)
30
Briquettes
of bio
coal
2.4MT/day
PM 150 mg/Nm³ SO2 100 ppm
NOx 50 ppm
Cyclone
separator
followed by
water
scrubber
5 D.G. Set
(1000
KVA)
15 HSD .
180 Ltr/Hr PM 150 mg/Nm³ SO2 100 ppm NOx 50 ppm
Adequate
Stack Height
E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr. no.
Specific Source of emission (Name of the
Product & Process)
Type of emission
Stack/Vent
Height (meter)
Air Pollution Control
Measures (APCM)
1 Reaction vessel – 1 to 5
HCl 20 mg/Nm3
11
Two stage Water scrubbers followed by Alkali scrubber
2 Reaction vessel – 6 to 10
HCl 20 mg/Nm3
SO2 40 mg/Nm3
11
Two stage Water scrubbers followed by Alkali scrubber
3 Reaction vessel – 11 to 14
NH3 30 mg/Nm3
11
Two stage Water scrubber followed
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 49 of 357
water packed column by acidic media column scrubber.
Note:
➢ Details of gaseous raw materials used in proposed project
Sr. No. Product Name Gaseous Raw Material
1 Heptylamine 99 % Hydrogen gas
2 Heptylamine 99 % Ammonia gas
3 Celecoxib HCL
4 Celecoxib Ammonia
5 4 -Benzyloxy aniline hydrochloride 98 %
Hydrogen
6 2 -Methoxybenzyl amine 98 % Ammonia
7 2 -Methoxybenzyl amine 98 % Hydrogen
➢ Estimation of process gas emission (Product wise and Total)
Sr. No. Product Name Process gas emission
Quantity (kg/kg of product)
1 Para Toluic acid Ammonia 14
2 6-Chloro-2-Hexanone CO2 33.24
3 2-Acetyl Thiophene HCL 173
4 Celecoxib HCL 24.38
5 Celecoxib Ammonia 10.6
6 Domperidone HCL 4.2
7 Glycine Methyl Ester Hydrochloride
SO2 171
8 Glycine Methyl Ester Hydrochloride
HCL 97
9 Isovaleryl chloride 98% SO2 164
10 Isovaleryl chloride 98% HCL 94
11 1-Indanone 98% HCL 74
12 2 -Methoxybenzyl amine 98%
Ammonia 127
13 Cyclopropylthio acetic acid
HCL 31
14 Cyclopropylthio acetic acid
SO2 52
15 2- Chlorobenzimidazole 98%
Ammonia 80
➢ Requirement of the scrubbing media (KL per Day) considering solubility
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 50 of 357
(Product wise and Total)
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above
and its sound management in HW matrix.
E-4 Fugitive emission details with its mitigation measures.
• The raw materials will be stored in closed containers and will be handled through closed
system to avoid the handling losses.
• System of leak detection and repair of pump/pipeline based on preventive maintenance. • The reactors are connected to an efficient condenser system with cooling/chilling
water/brine circulation.
• Reactor and solvent handling pumps are having mechanical seals to prevent leakages. Also, provide with breather valve to prevent losses. • Solvent are taken from storage tank to reactors through closed pipe line. • Storage tanks are vented through trap receiver & condenser operated on cooling water. • The condensers are provided with sufficient HTA and residence time so as to prevent
any loss of solvent.
• Proper earthing is provided were ever solvent handling is done. • Entire plant is flameproof. • Solvents are stored as per statutory requirement. Solvent are kept at a separate
specified area with all the safety measures.
• The sprinkling of water is done along the internal roads in the plant in order to control the
dust arising due to the movement of vehicular traffic.
Thick greenbelt is developed around the plant to arrest the fugitive emissions.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9
permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass
balance and calculations shall be incorporated in EMP details
separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
-
Sr. No.
Waste Source
Category as
HWM Rules 2016
Quantity MT/Year
Disposal method
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 51 of 357
1. Filter & filter material which have organic liquids in them FM mineral
Raw Materials/ Products
35.1 Sch -1
1.6 MT/Year
Collection, Storage, Transportation, disposal at TSDF site
2. ETP/MEE Sludge ETP/MEE 34.3 Sch -1
170 MT/year
Collection, Storage, Transportation, disposal at TSDF site
3. Used Oil/Spent Oil/Gear Oil
Machineries/ Utility
5.1 Sch -1 15 Lit/year
Collection, Storage, Transportation, disposal by selling to registered recyclers
4. Discard Containers & bags Empty Barrels /containers/ liners contaminated with hazardous Chemicals /waste
Raw Materials/ Products
33.1 Sch -1
20 MT/Year
Collection, Storage, decontamination sold to GPCB authorized & registered scrap vendors or send back to suppliers for reuse.
5. Spent Carbon Manufacturing process
28.3 Sch –I
25 MT/Year
Collection, Storage, Transportation and final disposal at common TSDF or Disposal to Co – Processing.
6. Distillation residue Manufacturing process
20.3 Sch. - I
150 MT/Year
Collection, Storage, Transportation, disposal at TSDF site
7. Off Specification Products
Manufacturing process
28.4 Sch. - I
0.5 MT/Year
Disposal at authorized Common Hazardous Waste Incinerator Facility(CHWIF)
8. Process residue and wastes
Manufacturing process
28.1 Sch –I
320 MT/Year
Disposal at authorized Common Hazardous Waste Incinerator Facility(CHWIF)
9. Inorganic salt Manufacturing process
B15 Sch- II
60 MT/Year
Collection, storage, transportation & Disposal, Reuse, by reused within plant
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility.
➢ Will be obtained
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
NA
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 52 of 357
G Solvent management, VOC emissions etc.
Solvent Management Plan In API manufacturing solvents are used for
• Work up for chemical reaction
• Removal of impurities
• Purification of crude API
• Cleaning of equipment’s
• Removal of moisture •
Therefore, quality of solvent should be like to like with fresh solvent. It is observed that contamination in solvent make the drug also contaminated.
• Washing of ml for removal of impurities
• Solvent containing dissolved solids are flash distilled
• Solvent containing miscible impurity or other solvent are fractional distilled
• Solvent are distilled in useful fraction & non-useful fractions (containing low boilers & high boilers) low boilers are mixed solvent & high boilers are along with residues Note –some of the solvents are recovered in-situ & directly used in next batch. (part of process)
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery,
reuse of recovered Solvents etc.
Solvent Input (MT)
Recover (MT)
Losses (MT)
% Recover
% Losses
Methanol 37.86 35.31 2.56 93.25 6.75
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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MDC 23.38 22.09 1.29 94.48 5.52
THF 4.28 3.98 0.30 92.99 7.01
Toluene 55.88 52.98 2.90 94.81 5.19
Triethyl ortho formate 2.70 2.57 0.13 95.19 4.81
IPA 21.03 20.26 0.77 96.34 3.66
ethyl acetate 3.88 3.68 0.20 94.85 5.15
Petroleum ether 13.20 11.89 1.31 92.08 7.92
chloroform 3.10 2.93 0.17 94.52 5.48
xylene 4.40 4.24 0.16 96.36 3.64
dichloro ethane 8.35 7.99 0.36 95.69 4.31
DMF 4.00 3.32 0.68 90.00 10.00
n Hexane 8.00 7.60 0.40 95.00 5.00
G-2 Brief Note on LDAR proposed:
Leak Detection and Repair (LDAR) program shall be prepared and implemented as per
the CPCB guidelines. LDAR Logbooks shall be maintained
G-3 VOC emission sources and its mitigation measures
Provision of mechanical seal in pump.
➢ Regular inspection of tank roof seals. ➢ Adequate measures for the minimization/prevention of the fugitive emission. ➢ Entire process to be carried out in the closed reactors with proper maintenance of
temperature. ➢ Regular periodic monitoring of work area to check the fugitive emission.
Adequate stack heights as per the CPCB estimation will be provides at all locations to
reduce GLCs of pollutants.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
Sr.no Name of Chemicals
Capacity of tank (KL)
Number of
tanks
Tank Type
diameter in m
Height
in m
Hazardous characteristics of chemicals
1 Toluene
20 2 Horizontal Cylinder
2.60 4.00 Highly flammable liquid and vapour
2 Aniline 20 2 Horizontal Cylinder
2.60 4.00 Extremely flammable
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3 Methanol
20 2 Horizontal Cylinder
2.60 4.00 highly flammable and toxic
4 Isopropyl Alcohol
20 2 Horizontal Cylinder
2.60 4.00 Highly flammable liquid and vapour
-Brief note on storage of Hazardous chemicals in Tanks
• As above
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels,
Carboys, Bags etc.
Safety details of Hazardous Chemicals:
Type of
Hazardous
Chemicals
Safety measures
Toluene Rinse mouth with water. Immediately after ingestion: give lots of water to drink. Do not give milk/oil to drink. Do not induce vomiting.
Give activated charcoal
Aniline Wear chemical safety goggles and face shield when contact is
possible. Skin Protection: Avoid repeated or prolonged skin contact.
Wear chemical protective clothing e.g. gloves, aprons, boots.
Methanol
Wash hands before breaks and immediately after handling the product.
Avoid contact with skin, eyes, and clothing.
Isopropyl
Alcohol
Use chemical safety goggles and/or a full-face shield where splashing
is possible. Maintain eye wash fountain and quick-drench facilities in
work area.
• Applicability of PESO : NA
H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of process Safety measures including Automation
Hydrogenation process
SPECIAL PRECAUTIONS FOR HANDLING HYDROGEN: ❖ CCE approved premises with door having locking
arrangement provided. Protect cylinders against physical damage.
❖ Store in cool, dry, well-ventilated area, away from sources of heat, ignition and direct sunlight.
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❖ Do not allow area where cylinders are stored to exceed 52°C (125°F).
❖ Isolate from oxidizers such as oxygen, chlorine, or fluorine.
❖ Use a check valve or trap in the discharge line to prevent hazardous backflow.
❖ Cylinders should be stored upright and be firmly secured to prevent falling or being knocked over.
❖ Cylinders can be stored in the open, but in such cases, should be protected against extremes of weather and from the dampness of the ground to prevent rusting.
❖ Never tamper with pressure relief devices in valves and cylinders. Electrical equipment should be non-sparking or explosion proof.
❖ Flammable high-pressure gas. ❖ Use only in a closed system. ❖ Use piping and equipment adequately designed to
withstand pressures and temperatures to be encountered.
❖ Gas can cause rapid suffocation due to oxygen deficiency.
❖ Never work on a pressurized system. ❖ If there is a leak, close the cylinder valve. Blow the
system down in a safe and environmentally sound manner in compliance with all federal, state, and local laws; then repair the leak.
❖ Never place a compressed gas cylinder where it may become part of an electrical circuit.
❖ Apron, Hand gloves, gumboot, goggles & helmet provided.
❖ ISI Portable fire extinguisher & Hydrant line is provided as per TAC norms.
❖ Flame proof fitting provided & Sufficient Nos. of SBA sets & 2 No. of Airline mask.
Following safety Measures will be taken while storage & handling of Hydrogen gas:
❖ Measures to be taken to prevent such accident: for H2 Rack Handling
❖ Hydrogen Cylinder rack will be parked in barricaded Separate area
❖ FLP Electrical Installation provide near storage area ❖ Vehicle allowed with Spark Arrestor ❖ No Smoking / Hot work allowed ❖ Trained staff ❖ Special Vehicle with Trained Operating staff for H2 Rack ❖ PPE Warned ❖ Spark proof tools used
Safety shower, eye wash with quenching unit will be provided in handling / storage area
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SOP for Handling Hydrogen Gas 1. Design Requirements 2. Location & Buildings 3. Reactor Arrangement
- Hydrogen Manifold - Pressure Relief - Heating - Pipelines and Discharge Devices - Truck Mounted Cylinders
Identification of and Access to Hazard Zones
H-3 Details of Fire Load Calculation
-
Total Plot Area: 4450.00 sq. m
Area utilized for plant activity: 1520 sq. m
Area utilized for Hazardous Chemicals Storage: 500 sq. m.
Number of Floors: Ground+First
Water requirement for firefighting in KLD : 67.2 KL
Water storage tank provided for firefighting in
KLD:
100 KL
Details of Hydrant Pumps: Main Pump: 1 Nos.Jockey pump: 1 Nos.
Diesel pump: 1 Nos.(SB)
Nearest Fire Station : Simruba fire station
Applicability of Off Site Emergency Plan: After obtaining EC, we will develop off-site emergency plan for the same.
-
H-4 Details of Fire NOC/Certificate:
➢ After obtaining EC, we will apply for the fire NOC/certificate for the same.
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 70
Number of Contractual person/Labour : 30
Area provided for OHC: 60 sq. m
Number of First Aid Boxes : 2
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Nearest General Hospital : The Cambay General Hospital
Name of Antidotes to be store in plant : 5
• During the meeting dated 07.06.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and their Technical Expert from M/s. Shree green Consultants
remain present during video conference meeting.
• Since, the unit falls in B2 category as per the MoEF&CC’s amended EIA Notification vide
S.O. 1223(E) dated 27.03.2020, the public consultation is not applicable as per paragraph
7(i) III (i) (e) of the Environment Impact Assessment Notification-2006.
• Committee noted the following:
✓ Distance of proposed project is 250-300 meter from CRZ boundary.
✓ Site Plan/ layout with fire plan & floor plans with provision of separate entry & exit. Also
presented area adequacy for storage of finished goods, raw material, drums, tank farm
and hazardous waste, etc.
✓ Revised product profile with mentioning R & D product 0.1 MT/Month in place of 2.5
MT/Month.
✓ Revised water balance diagram with mentioning ETP and solvent stripper followed by
MEE in place of only MEE.
✓ Bio coal is proposed as fuel in place of bio fuel.
✓ Revised EMP and risk assessment for hydrogen gas handling.
• Looking to reply submitted by technical expert of which is found inadequate, Committee
asked to submit (1) Revised layout plan with mentioning adequate size peripheral road and
internal road , revised green belt area, secure distance of storage and boiler area from
proposed process area and revised area adequacy considering it (2) Revised Hazardous
waste matrix with mentioning mixed solvent from solvent stripper details and spent solvent
from process details separately (3) Revised EMP with mentioning adequate auto control
cost for critical process and CER cost mentioned in EMP(4) revised air matrix with adequate
fuel consumption details considering capacity of boiler, TFH , HAG etc and (4) adequate
details of risk assessment for hydrogen storage and its safety measures with
superimposition of dispersion model for it on proposed project area and its impact on
surrounding habitat and its mitigation measures for proposed project in place of general data
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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for hydrogen gas risk assessment.
• After detailed discussion, Committee unanimously decided to consider the project in
one of upcoming meeting after submission of following documents:
1. Revised layout plan with mentioning adequate size peripheral road and internal road
, revised green belt area, secure distance of storage of various hazardous chemicals
considering its compatibility chart and boiler area from proposed process area and
revised area adequacy considering it.
2. Revised Hazardous waste matrix with mentioning mixed solvent from solvent stripper
details and spent solvent from process details separately.
3. Revised air matrix with adequate fuel consumption details considering capacity of
boiler, TFH , HAG etc.
4. Revised EMP with mentioning adequate auto control cost for critical process and
CER cost mentioned in EMP.
5. Adequate details of risk assessment for hydrogen storage and its safety measures
with superimposition of dispersion model for it on proposed project area and its
impact on surrounding habitat and its mitigation measures for proposed project in
place of general data for hydrogen gas risk assessment
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Shree green Consultants
remain present during video conference meeting.
• Committee discussed regarding :
✓ Revised layout. Land breakup submitted. Location of OHC was asked. PP submitted that
it is provided inside admin office block. Upon asking PP submitted that it is G+ 2. Area
table and floor plan was asked from the PP. PP was thus asked to submit revised
area/land breakup table after including floor plan and nos. of floors. Area adequacy was
asked from the PP.
✓ Revised Hazardous waste generation details were submitted. It was found distillation
residue generated is 150 MT/Yr against solvent generation of 95 MT /Year is not
justifiable. PP was asked to submit revised hazardous waste table.
✓ EMP budget was discussed. PP was asked to revise EMP wrt the Fire and Safety, OHS
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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cost, DCS system cost and information of where DCS system is to be provided for which
processes etc.
✓ PP was asked to include Capacity of firefighting systems in the presentation.
✓ Dispersion of hazardous hydrogen chemical was discussed. Again PP was asked to
submit details of the same.
• After detailed discussion, Committee unanimously decided to consider the proposal
in one of the upcoming SEAC meeting only after satisfactory submission of following
details:
1. Revised area/land breakup table after including floor plan and nos. of floors.
2. Revised hazardous waste table.
3. PP was asked to include Capacity of firefighting systems in the presentation.
4. Details of Dispersion of hazardous hydrogen chemical.
3 SIA/GJ/IND2/173246/2020 Asceneo Labs Pvt Ltd.
Plot No. 55/3, Phase I, GIDC Estate, Vatva , Ahmedabad
EC reconsideration
Category of the unit: 5(f)
Project status: New
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173246/2020 on
dated 18.09.2020 for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is a new project proposed for manufacturing of synthetic organic chemicals [API and
Its Intermediates] as tabulated below:
Sr.
No.
Name of the
Products
API
OR
INTERMEDIATE
CAS no. Quantity
MT/Month
*End-use of
products
1 Dobutamine
HCl
API 49745-95-1 4.0 Cardiogenic
shock
2 Dopamine HCl API 51-61-6 low blood
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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pressure
3 Papaverine
HCl
API 61-25-6 Vasospasm
4 Tetra hydro
papaverine
hydrochloride
API 6429-04-5 4.0 Neuromuscular
blocking
5 Des
Venlafaxine
API 93413-62-8 Antidipressant
6 levetiracetam
API
122767-28-
2
Anticonvulsants
7 Benzethonium
chloride
API 121-54-0 6.0 Surfactant, antis
eptic
8 Diclofenac
sodium API 15307-79-6
nonsteroidal
anti-
inflammatory
9 3,3-Bis
(Methoxymeth
yl)-2,6-
Dimethylhepta
ne
API 129228-11-
1
Neuromuscular
blocking agents
10 Mebeverine
HCl
API 2753-45-9 6.0 Antispasmodic
11 Telmisartan
API 144701-48-
4
Angiotensin II
receptor
12 Metyrosine API 672-87-7 Antihypertensive
13 Citalopram
hydrobromide
API 59729-32-7 Antidipressant
14 Cyanodiol
hydrobromide
API 103146-25-
4
0.75 Anti-
inflammatory
15 Eltrombopag
olamine
API 496775-61-
2
Thrombocytopen
ia
16 Escitalopram
oxalate
API 219861-08-
2
treat depression
and anxiety
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17 Verdenafil
hydrochloride
trihydrate
API 224785-90-
4
Erectile
dysfunction
18 2-(3,4-
dimethoxyphen
yl)-5-methyl-
1H-pyrazol-
3(2H)-one
Intermediate
(n-1)
277299-70-
4
Thrombocytopen
ia
19 Furalic acid
API 1135-24-6 10 Anti-
inflammatory
20 Paliperidone
API 144598-75-
4
Antipsychotic
21 AmbroxolHydr
ochloride API 23828-92-4
Respiratory
diseases
22 Ciprofloxacen
hydrochloride API 86393-32-0
Antibiotic
23 Nateglinide
API 105816-04-
4
10 type 2 diabetes
24 Bezafibrtae API 41859-67-0 Hyperlipidemia
25 Development
Product
API -- 0.1
TOTAL 40.85
# Brief Note of Product Profile:
1. No of Manufacturing Plants: 2 nos
2. Brief Note regarding number of Products to be manufactured considering plant capacity:
• At a time, maximum 2 product will be manufactured.
Specific End-use of each product:
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category of Product (API/ Intermediate)
In case of Intermediate stage of API
Said API is used for/End Use of said API
Stage i.e. n-1, n-2, etc.
Name of API in which Intermediate Used/ End use of said
CAS no. (API)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 62 of 357
Intermediate
1 Dobutamine HCl
49745-95-1
API -- -- -- Cardiogenic shock
2 DOPAMINE HCl
51-61-6 API -- -- -- low blood pressure
3 Papaverine HCl
61-25-6 API -- -- -- Vasospasm
4 Tetra hydro papaverine hydrochloride
6429-04-5
API -- -- -- Neuromuscular blocking
5 Des Venlafaxine
93413-62-8
API -- -- -- Antidipressant
6 levetiracetam
122767-28-2
API -- -- -- Anticonvulsants
7 Benzethoniumchloride
121-54-0 API -- -- -- Surfactant, antiseptic
8 Diclofenac sodium
15307-79-6
API -- -- -- nonsteroidal anti-inflammatory
9 3,3-Bis (Methoxymethyl)-2,6-Dimethylheptane
129228-11-1
API -- -- -- Neuromuscular blocking agents
10 Mebeverine HCl
2753-45-9
API -- -- -- Antispasmodic
11 Telmisartan
144701-48-4
API -- -- -- Angiotensin II receptor
12 Metyrosine 672-87-7
API -- -- -- Antihypertensive
13 Citalopram hydrobromide
59729-32-7
API -- -- -- Antidipressant
14 Cyanodiol hydrobromide
103146-25-4
API -- -- -- Anti-inflammatory
15 Eltrombopag
496775-61-2
API -- -- -- Thrombocytopenia
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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olamine
16 Escitalopram oxalate
219861-08-2
API -- -- -- treat depression and anxiety
17 Verdenafil hydrochloride trihydrate
224785-90-4
API -- -- -- Erectile dysfunction
18 2-(3,4-dimethoxyphenyl)-5-methyl-1H-pyrazol-3(2H)-one
277299-70-4
Intermediate n-1 Eltrombopag olamine
277299-70-4
Thrombocytopenia
19 Furalic acid
1135-24-6
API -- -- -- Anti-inflammatory
20 Paliperidone
144598-75-4
API -- -- -- Antipsychotic
21 Ambroxol Hydrochloride
23828-92-4
API -- -- -- Respiratory diseases
22 Ciprofloxacen hydrochloride
86393-32-0
API -- -- -- Antibiotic
23 Nateglinide
105816-04-4
API -- -- -- type 2 diabetes
24 Bezafibrtae
41859-67-0
API -- -- -- Hyperlipidemia
• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA
Notification 2006 and amendment dated 27th March, 2020.
• The proposal was considered in the SEAC video conference meeting dated 15.12.2020.
• Salient features of the project including Water, Air and Hazardous waste management are
submitted.
• During the meeting dated 15.12.2020, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and their Technical Expert from M/s Bhagwati Enviro Care Pvt. Ltd
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 64 of 357
remain present during video conference meeting.
• PP informed that the unit is having lease agreement for a period of 50 years from date
01.08.2020 and unit have applied for GIDC plot transfer letter but till date they have not
received.
• After deliberation, SEAC unanimously decided to defer the proposal and consider the
same in one of the upcoming meeting of SEAC after submission of GIDC plot transfer
letter.
• PP submitted the reply of the said points along with other supporting documents.
• This proposal is reconsidered in SEAC meeting dated 01.04.2021. PP along with their
technical expert/consultant from M/s Bhagwati Enviro Care Pvt. Ltd remains present in the
meeting and made presentation before committee.
• PP presented revised salient features of the project including Water, Air and Hazardous
waste management are as under:
Sr.
no.
Particulars Details
A-1 Total cost of Proposed Project
(Rs. in Crores):
Total Project
19 Crores
Break-up of proposed project Cost:
Details Project Cost
(Rs. In Crores)
Land
developing
& Building
8.0
Machinery 10
Other 1.0
A-2 Details of Environmental Management Plan (EMP) As below:
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Sr. No
Unit Detail
Capital Cost (Rs. In Lac)
Operating Cost (Rs. In Lac)
Maintenance Cost (Rs. In Lac)
Total Recurring Cost (Rs. In Lac)
1 Waste Water
ETP & STP 30 1.5 0.5 2.0
Spray Drying at common spray dryer
0 348 0.5 348.5
2 Air Steam Boiler, TFH 5.0 2.5 1.0 3.5
3 Hazardous Management
Membership fees of TSDF & disposal
3.5 5.0 1.0 6.0
Prepare Storage area
1.0 0.0 0.1 0.1
4 Fire & Safety
Fire Hydrant System & Fire Extinguishers
42 0.0 0.5 0.5
Provision of safety equipment
3.0 0.1 0.2 0.3
5 AWH Monitoring
Monitoring by authorized agency
2.4 0.5 0.5 1.0
6. Green Belt Development
For develop gardening area & trees planted
3.2 1.0 1.0 2.0
7. Occupational Health
OHC & health checkup of workers
10.0 2.0 1.0 3.0
8. Process & Hazard Control
DCS System provided
20 1.0 1.0 2.0
9. CER Activity
CER fund allocation for social activity at nearest villages.
38 0 0 0
TOTAL 158.1 361.6 7.3 368.9
Summary
Cost of Project in Crores: 19
EMP Capital Cost in Crores per Annum and
Percentage:
1.581 Crore &8.32%
EMP Recurring Cost in Crores per Annum
and Percentage:
3.689 Crore/Annum
&19.41%
A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA, CER
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 66 of 357
fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in
case of Environmental Clearance as per the mechanism published vide MoEF&CC’s OM vide 31.10.2019.)
% as per the OM
Rs. in Crores
2% 0.38
Brief note on proposed activities:
M/s. Asceneo Labs Pvt. Ltd. CER Budget: 38 Lacs (For Five Year) Propose Planning for CER Activity (2021-2025)
Cost in Lacs/Yr
2021 2022 2023
− Rs 3.0 Lacs for construction work in Hospital at Vinzol village.
− Rs 7.6 Lac for Rain Water Harvesting in Vinzol & Vatva village with the help of village people & Sarpanch of Vinzol & Vatva village.
− Rs 3.6 Lacs for Education at Primary School of Vatva & Ramol Village
We will provide necessary things as per his requirement.
− Rs 3.0 Lacs for drinking water facility at Vinzol village.
We will provide drinking water stand with RO system in Vinzol village.
− Rs 4.0 Lacs for Dinking Water Facility at Vatva Village.
We will provide drinking water stand with RO system in Vatva village.
− Rs 1.6 Lacs for Infrastcture development activity in Vinzol Village.
We will develop Community hall of Vinzol Village.
Total: Rs 7.6 Lacs Total: Rs 7.6 Lacs Total: Rs 7.6 Lacs
M/s. Asceneo Labs Pvt. Ltd. CER Budget: 38 Lacs (For Five Year) Propose Planning for CER Activity (2021-2025)
Cost in Lacs/Yr
2024
− Rs 3.0 Lacs for Education at Primary School of Narol village.
We will provide necessary things as per his requirement.
− Rs 1.6 Lacs for Education at Primary School of Gamdi & Vanch village.
We will provide necessary things as per his requirement.
− Rs 1.6 Lacs for drinking water facility at Ramol village.
− Rs 3.0 Lacs for drinking water facility at Narol village.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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We will provide drinking water stand with RO system in Ramol village.
We will provide drinking water stand in Narol village.
− Rs 3.0 Lacs for Infrastcture development activity in Vatva Village.
As per requirement we will provide CER fund to develop Infrastcture facility.
− Rs 3.0 Lacs for Infrastcture development activity in Ramol Village.
As per requirement we will provide CER fund to develop Infrastcture facility.
Total: Rs 7.6 Lacs Total: Rs 7.6 Lacs
B Land / Plot ownership details:
Lease Agreement between M/s. Metrochem Capital Trust Limited & Ms. Asceneo
Labs Pvt. Ltd.
B-1 Plot area
Total Plot area
1843 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Sr. No.
Particulars Ground
Floor Area (Sq. m.)
First Floor
Area (Sq. m.)
Second Floor Area (Sq. m.)
Terrace Floor Area
(Sq. m.) TOTAL
1 BOILER HOUSE 54 - - - 54
2 ENGG. OFFICE 30 - - - 30
3 PRIMARY TREATMENT TANK
42 - - - 42
4 HAZARD WASTE 18 - - - 18
5 TANK-FARM 70 - - - 70
6 PRODUCTION
UNIT 322 322 322 - 966
7 FG WARE-HOUSE 224 - - - 224
8 ADMIN. OFFICE 126 - - - 126
9 FIRE HYDRANT PUMP HOUSE
44 - - - 44
10 SECURITY CABIN 7.5 - - - 7.5
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12 RM STORE - 224 - - 224
13 QA&QC LAB - 126 - - 126
15 UTILITY AREA - - 224 322 546
16 R&D BUILDING - - 126 - 126
17 AHU'S AREA - - - 224 224
18 GREEN BELT: 377 - - - 140
19 ROAD & OPEN
SPACE 528.5 - - - 765.5
TOTAL 1843 672 672 546 3733
B-3 Green belt area
Total
(Sq. meter)
Area in
Sq. meter
377 Sq. m. (In Plant
Premises)
% of total
area
(20.5% In Plant Premises)
Additional Greenbelt area develop & Trees Plantation in Vinzol Parabadi Trust (Vinzol
Village) – 365 Sq. m. (19.8% of total plot Area)
C Employment generation
Total
70 Nos.
D WATER
D-1
Source of Water Supply
(GIDC, Bore well, Surface water, Tanker supply etc...)
GIDC Vatva Water Supply
Status of permission from the concern authority.
➢ Yes We obtained Permission.
D-2
Water consumption (KLD)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Category
Quantity
KLD
Remarks
(D) Domestic 1.5
(E) Gardening
1.0
(F) Industrial
Process 14
Washing 1.0
Boiler 4.0
Cooling 12
Scrubber 1.0
Industrial Total
32
Grand Total
(A+B+C)
34.5
Brief Note on worst case scenario for water
consumption:
Sr. No.
Product Qty. Water Consumption
KL/B KL/M KL/D
1 Dobutamine HCl 4.000 2.352941 9.411765 0.313725
2 DOPAMINE HCl 4.000 2 8 0.266667
3 Papaverine HCl 4.000 3.214286 12.85714 0.428571
4 Tetra hydro papaverine 4.000 2.06 8.24 0.274667
5 Des Venlafaxine 4.000 0 0 0
6 levetiracetam 4.000 14.7619 59.04762 1.968254
7 Mebeverine HCl 6.000 6.444444 38.66667 1.288889
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8 Benzethoniumchloride 6.000 2.644737 15.86842 0.528947
9 Diclofenac sodium 6.000 4.833333 29 0.966667
10 3,3-Bis (Methoxymethyl)-2,6-Dimethylheptane
6.000 5.517241 33.10345 1.103448
11 Telmisartan 6.000 17.12 102.72 3.424
12 Metyrosine 6.000 10.3 61.8 2.06
13 Citalopram hydrobromide 6.000 7.66 45.96 1.532
14 Cyanodiol hydrobromide 0.750 8.31 6.2325 0.20775
15 Eltrombopag olamine 0.750 30.76 23.07 0.769
16 Escitalopram oxalate 0.750 66.36 49.77 1.659
17 Verdenafil hydrochloride trihydrate 0.750
62.28 46.71 1.557
18
2-(3,4-dimethoxyphenyl)-5-methyl-1H-pyrazol-3(2H)-one 0.750
69.315 51.98625 1.732875
19 Furalic acid 10.000 5.833333 58.33333 1.944444
20 Paliperidone 10.000 6.166154 61.66154 2.055385
21 Nateglinide 10.000 2.769231 27.69231 0.923077
22 Ambroxol Hydrochloride 10.000 6.25 62.5 2.083333
23 Bezafibrtae 10.000 3 30 1
24 ciprofloxacen hydrochloride 10.000 8 80 2.666667
-
Summary of water
requirement
Quantity
KLD
Remarks
Total water
requirement for
the project (A)
34.5
Quantity to be
recycled (B)
1.3
Total fresh water
requirement (C)
33.2
Ensure Total water requirement = Fresh water
+ Recycled water
i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility.
[Source of reuse & application area]
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Source of waste
water for reuse
in KLD (From where
it is coming)
Application
area with
quantity in
KLD (Where it is
used)
Characteristics of
waste water to be
reused (COD, BOD, TDS
etc.)
mg/l
Remarks
regarding
feasibility
to reuse
Domestic
Wastewater
generation 1.3
KLD treat in STP
1.0 KLD In
Gardening
purpose within
premises.
0.3 KLD reuse
in cooling
within
premises.
pH: 7.3-7.6
COD<100
TDS<50
In case of no reuse/recycle of waste water, Give brief
note on justification as why no reuse/recycle.
➢ Not Applicable
D-3
Waste water generation (KLD)
Category Waste water
KLD
Remarks
(C) Domestic 1.3
(D) Industrial
Process 20
Washing 1.0
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Boiler 0.2
Cooling 0.2
Scrubber 0.5
Total Industrial
waste water
21.9
Total [A + B]
Brief Note on worst case scenario for waste water generation(Qualitative and
Quantitative):
Sr. No.
Product Qty. Wastewater Generation
KL/B KL/M KL/D
1 Dobutamine HCl 4.000 6.917647 27.67059 0.922353
2 DOPAMINE HCl 4.000 7.6 30.4 1.013333
3 Papaverine HCl 4.000 4.614286 18.45714 0.615238
4 Tetra hydro papaverine 4.000 1.94 7.76 0.258667
5 Des Venlafaxine 4.000 3.722222 14.88889 0.496296
6 levetiracetam 4.000 16.6381 66.55238 2.218413
7 Mebeverine HCl 6.000 10.44444 62.66667 2.088889
8 Benzethoniumchloride 6.000 5.641228 33.84737 1.128246
9 Diclofenac sodium 6.000 5.791111 34.74667 1.158222
10 3,3-Bis (Methoxymethyl)-2,6-Dimethylheptane
6.000 10.22069 61.32414 2.044138
11 Telmisartan 6.000 21.08 126.48 4.216
12 Metyrosine 6.000 25.8 154.8 5.16
13 Citalopram hydrobromide 6.000 11.92 71.52 2.384
14 Cyanodiol hydrobromide 0.750 14.51 10.8825 0.36275
15 Eltrombopag olamine 0.750 34.89 26.1675 0.87225
16 Escitalopram oxalate 0.750 71.7 53.775 1.7925
17 Verdenafil hydrochloride trihydrate 0.750
67.69 50.7675 1.69225
18
2-(3,4-dimethoxyphenyl)-5-methyl-1H-pyrazol-3(2H)-one 0.750
112.84 84.63 2.821
19 Furalic acid 10.000 8.435 84.35 2.811667
20 Paliperidone 10.000 7.676923 76.76923 2.558974
21 Nateglinide 10.000 4.912308 49.12308 1.637436
22 Ambroxol Hydrochloride 10.000 9.765 97.65 3.255
23 Bezafibrtae 10.000 3.380952 33.80952 1.126984
24 ciprofloxacen hydrochloride 10.000 8.976 89.76 2.992
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Brief justification in case of no process effluent generation or no industrial effluent
generation or no high concentration effluent generation from proposed project
(Whichever is applicable).
➢ Not Applicable
D-4 Mode of Disposal & Final meeting point
-
Domestic: 1.3 KLD Treat in STP then reuse in Gardening & Cooling within premises.
Industrial: 21.9 KLD Generated Industrial Effluent will be treated in ETP (Having
Primary Treatment Unit) then send to Common Spray Dryer facility at
Chhatral Environment Management System Pvt. Ltd. Dhanot for Spray
Drying.
-
Clearly mention about final disposal
Common Spray Drying Facility at CEMSPL Dhanot for Spray Drying.
D-5 Treatment facilities
For Domestic waste water:
Capacity of STP: 1.5 KLPD Modular STP
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case
of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
➢ ETP (25 KL – Having Primary Treatment Unit)
21.9 KLD Industrial Effluent will be treated in ETP (Having Primary Treatment Unit) then send to Common Spray Drying facility at CEMSPL Dhanot for Spray Drying.
Sr. No. Parameter Before Treatment After Treatment
1 pH 4.0 – 4.5 7.0 - 7.5
2 Total Suspended Solid 300 – 320 50 – 70
3 Total Dissolved Solid 11300 – 11600 12000 – 12200
4 Oil & Grease 2.5 – 3.5 2.0 – 2.5
5 COD 9000 – 9800 7300 – 7600
6 BOD 3000 - 3400 2400 – 2700
Note: (In case of CETP discharge) :
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention
and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ No CETP Discharge
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
➢ 21.9 KLD Generated Industrial Effluent will be treated in ETP (Having Primary
Treatment Unit) then send to Common Spray Dryer facility at Chhatral Environment
Management System Pvt. Ltd. Dhanot for Spray Drying.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE,
CHWIF etc.
Name of Common facility (CF) (For waste water treatment)
➢ Common Spray Drying Facility of Chhatral Environment
Management System Pvt. Ltd. Dhanot
Membership of Common facility (CF) mentioning total capacity, consented
quantity, occupied capacity and spare capacity and norms of
acceptance of effluent from member units in-line with the direction given
by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated
08/01/2020.
➢ As per attached in Presentation PPT
D-7 Simplified water balance diagram with reuse / recycle of waste water
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All Figure in KL/Day
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario
thereof:
Fuel: Natural Gas
Steam Boiler (1.0 KLD): 520000 k cal/hr required
TFH (2 Lac k cal/hr): 200000 k cal/hr required
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC’s
OM vide dated 31.10.2019)
Sr.
no.
Source
of
emission
With
Capacity
Stack
Height
(meter)
Type
of
Fuel
Quantity
of Fuel
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air
Pollution
Control
Measures
(APCM)
1 Steam Boiler (1.0 TPH)
20 PNG 1365
SCM/D
SPM SOx NOx
Adequate Stack Height
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2
Thermic Fluid Heater (2 Lac k cal/hr)
20 PNG 510
SCM/D
SPM SOx NOx
Adequate Stack Height
E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr. no.
Specific Source of emission (Name of the
Product & Process)
Type of emission
Stack/Vent Height (meter)
Air Pollution Control
Measures (APCM)
1 Reaction Vessel
HCl
SO2 15
Two Stage Water Scrubber
2 Reaction Vessel
NH3
HBr 15
Two Stage Water Scrubber
Note:
➢ Details of gaseous raw materials used in proposed project
No Gaseous Raw Material
➢ Estimation of process gas emission (Product wise and Total)
Show in Hazardous Waste Table
➢ Requirement of the scrubbing media (KL per Day) considering solubility
(Product wise and Total)
Show in Hazardous Waste Table
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above
and its sound management in HW matrix.
Yes
E-4 Fugitive emission details with its mitigation measures.
Sources of fugitive emissions include storage of chemicals, loading and unloading section,
raw material handling and hazardous waste storage area.
Mitigation Measures - Water shall be sprinkled during the construction - Mechanical seals for
pumps etc. should be used and maintained. - Closed unloading, conveying and packing
system - All the reactors shall be closed. - Safety devices shall be provided to workers - Raw
material storage in closed storage area
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9
permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and
calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
-
Sr.
no.
Type/Name of
Hazardous
waste
Specific
Source of
generation
(Name of the
Activity,
Product etc.)
Category and
Schedule as
per HW Rules.
Quantity
(MT/Annum)
Management
of HW
1 ETP Sludge From
Effluent
Treatment
Plant
35.3 15 Collection,
Storage,
Transportation
and send to
TSDF site for
disposal.
2
Used Oil
From plant
machinery
5.1 0.24 kl Collection,
Storage,
Transportation
& Disposed by
selling to
Registered
refiners or
reuse as
lubricant.
3 Discarded
Containers
(Bag, Barrel,
Drum)
From raw
material/
production
section
33.1 70 Collection,
Storage,
Transportation
& Disposed by
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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selling to
authorized
recycler.
4
Spent Catalyst
Generated
from
manufactur
ing process
ofPapaveri
ne HCl,
3,3-Bis
(Methoxym
ethyl)-2,6-
Dimethylhe
ptane,
28.2 1.2 Collection,
Storage,
Transportation
and send
back to
supplier for
recharging.
5
Spent Carbon
Generated
from
manufactur
ing process
ofBenzetho
niumchlorid
e,
Diclofenac
sodium,
Telmisarta
n,
Metyrosine
,
ciprofloxaci
n
hydrochlori
de.
28.3 50.6 Collection,
Storage,
Transportation
and send to
Co processing
unit.
6 Distillation
Residue
From
Distillation
36.1 58.5 Collection,
Storage,
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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process of
solvent.
Transportation
and send to
CHWIF for
incineration.
7
Spent Solvent
From
Distillation
process of
solvent.
28.6 1513.25 Collection,
Storage,
Recover &
Reuse in mfg.
process within
our premises.
8
Dil. HCl (25-
30% Solution)
HCl gas
generated
from mfg.
process
ofDiclofena
c sodium,
Nateglinide
,
Bezafibrtae
,
ciprofloxac
en
hydrochlori
de
35.1 180
Collection,
Storage,
Transportation
and sell to
Rule 9
authorized
industries.
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility.
➢ We are applied for TSDF & CHWIF membership certificate
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
No
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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1 STP Sludge
STP 0.2 Used as manure within premises.
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of
recovered Solvents etc.
Type of solvents % recovery % Losses
Air Water Haz
IPA 96 1.0 -- 3.0
Di Chloro Methane
96.7 1.2 -- 2.1
Methyl Ethyl Ketone
96.5 1.2 -- 2.3
Toluene 97.12 1.11 -- 1.77
Hexane 96.8 1.0 -- 2.2
Methanol 98 0.8 -- 1.2
Acetonitrile 98.3 0.7 -- 1.0
Ethyl Acetate 97 1.0 -- 2.0
Acetone 98.4 0.5 -- 1.1
Name of Solvent Total requirement Total quantity of solvent recovered
IPA 29.75 28.56
Di Chloro Methane 20.37 19.7
Methyl Ethyl Ketone 54.18 52.28
Toluene 19.41 18.85
Hexane 10.3 9.97
Methanol 29.21 28.63
Acetonitrile 32 31.46
Ethyl Acetate 20.18 19.57
Acetone 41.59 40.92
G-2 Brief Note on LDAR proposed:
➢ Attached as Annexure - I
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G-3 VOC emission sources and its mitigation measures
➢ Leak Free Pumps for transfer ofsolvents. ➢ MSW Gaskets in solvent pipelines to prevent leakage fromflanges. ➢ Minimum number of flanges, joints and valves inpipelines. ➢ To eliminate chances of leakages from glands of pumps, mechanical seal will be
provided at all solventpumps. ➢ All the rotating equipment like pumps will be installed with Mechanical Seals to arrest
any sort ofemissions. ➢ Condenser and scrubber post Reactor with coolingarrangement. ➢ Enclosures to chemical storage area, collection of emission from loading of raw
materials in particular solvents through hoods and ducts by induced draft, and control by condenser to beensured.
➢ In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send toETP.
➢ If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent ElectricSpark.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
-
Sr. no Name of Chemical Capacity of
Tank
Number of
Tanks
Hazardous
Characteristics
of Chemical
1 Con. Hydrochloric
Acid
10 KL 1 Flammable
2 Caustic Lye (48%) 5 KL 1 Corrosive
Brief note on storage of Hazardous chemicals in Tanks
• Dyke will be provided to storage tank to collect leakage/spillage
• Provision of Static Earthing
• Fire Extinguisher/Fire Hydrant System
• Lighting /Proper Illumination
• Lightening arrestor
• Trained and experience operators
• NFPA label capacity and content should display on storage tank
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels,
Carboys, Bags etc.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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• Drums will be stored at designated location or secured in a safety storage cabinet.
• Proper ventilation will be provided in Godown.
• Proper label and identification board /stickers will be provided in the storage area.
• Drum handling trolley / stackers/fork lift will be used for drum handling.
• Separate dispensing room with local exhaust and static earthing provision will be
made.
• Materials will be transferred by pumping through pipeline or by vacuum, from drums.
• Drums for flammable liquids will have proper closures that can withstand the
expected handling conditions without leaking.
• FLP type light fittings will be provided.
Safety details of Hazardous Chemicals:
Type of
Hazardous
Chemicals
Safety measures
Flammable − Materials will be stored as per its compatibility study and separate
area will be available for flammable, corrosive and toxic chemical
drums storage.
− Smoking and other spark, flame generating item will be banned
from this area.
− NFPA labels will be provided on drums for hazard identification of
the chemicals
− Safety shower and eyewash shower will be provided near storage
area and plant area.
− Flame proof electrical equipment’s provided in process and storage
area.
Onsite emergency will be prepared as per GJR 68 J (9) and train all
team members for emergency situation as per risk assessment
scenarios outcome.
• Applicability of PESO: Due to the less storage quantity PESO will not applicable.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of
Process
Safety measures including Automation
-- --
H-3 Details of Fire Load Calculation
-
Total Plot Area: 2880
Area utilized for plant activity:
Area utilized for Hazardous Chemicals
Storage:
70
Number of Floors: 3
Water requirement for firefighting in KLD :
260 KLD
Water storage tank provided for firefighting in
KLD:
200 KL
Details of Hydrant Pumps: 1 ) Main Pump : Flow : 137m3/Hr , Head : 75Meter 2 ) Diesel Pump :Flow : 137m3/Hr , Head :75 Meter 3) Jockey Pump : Flow : 10.8 m3/Hr , Head : 75 Meter
Nearest Fire Station : 1.76 km, Jashoda Nagar Fire Station
Applicability of Off Site Emergency Plan: No
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-
H-4 Details of Fire NOC/Certificate:
Due to the proposed project Fire NOC will not applicable.
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 60
Number of Contractual person/Labour : 10
Area provided for OHC: 15
Number of First Aid Boxes : 40
Nearest General Hospital : 2.18 km, Kashiba
General Hospital
Name of Antidotes to be store in plant : --
• During meeting dated: 01.04.2021, PP presented that the land was acquired by Nakoda
Enterprise (now known as Metrochem Capital Trust Ltd. or MCTL) in an auction of GSFC
from Gujarat Surgical mfg. through proper registered Deed of Assignment (Dastavej) in year
1986 and the said land has been taken on lease for 50 Years by M/s. Asceneo Labs Pvt.
Ltd. Also, unit has applied for transfer of name to GIDC. Earlier provisional NOC of GIDC in
transferring the land was subjected to the payment of transfer fees. PP also presented
Payment receipt of all the dues of electricity, GIDC charges, water bills. Now, GIDC is
asking for 50% transfer fees for the transfer of said plots. Therefore, Committee noted that
the plot transfer procedure by GIDC is their administrative issue. Further, unit has carried
out Lease deed for a period of fifty years which serves the purpose of land ownership.
• PP informed that OM dated 07.10.2014 issued by MOEF with regards to the provision of
granting EC even if the land acquisition is not fully completed, as the EC clearance is site
specific and EC may be granted if a credible document showing the status, or even intent, of
land acquisition is provided.
• In view of the facts stated above, Committee felt that the subject land is in no dispute of
possession as it is only a formality of the transfer of name by GIDC. Hence, Committee was
of the view that such cases shall be considered based on the Lease deed and merits of the
case.
• Committee noted the following:
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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✓ Product profile with specific end-use of each product and mentioning manufacturing of R
& D product as 0.5 MT/M which is quite higher quantity.
✓ Site Plan/ layout with fire plan & floor plans and with provision of separate entry & exit, 4
m& 6 m wide roads for emergency exit, OHC (15 Sq. m.), assembly point, raw material&
finished goods storage areas, production plant, utility, ETP, hazardous waste storage
area, 7.50 % greenbelt within premises, etc. Also, presented land area break-up for each
components.
✓ Generated industrial effluent will be treated in primary ETP and sent to Common spray
dryer M/s Chhatral Environment Management system Pvt Ltd.
✓ Domestic will be treated in STP and reused for gardening & cooling.
✓ PP submitted hazardous waste matrix mentioning source of generation, quantity and
Mode of disposal and committed to comply the Hazardous and Other Wastes
(Management and Transboundary Movement) Rules 2016.
✓ PNG is proposed as fuel in boiler and TFH.
✓ Two stage scrubbing system is proposed for control of process gas emission.
✓ Scrubbing liquor will be sold to authorized actual users.
✓ Greenbelt development plan mentioning 140 Sq m (7.50%) within premises and 470 Sq
m (25.50%) outside premises in GIDC Vatva.
✓ Fire load calculation mentioning Fire water reservoir (Cap: 200 KL) and 10Nos of foam
type extinguishers.
• Committee deliberated on Product profile, Layout plan, Storage details, Process safety, Fire
safety, water balance & waste water management, Flue gas and process gas emission & Air
Pollution Control System, Hazardous waste matrix, EMP, CER, Green belt, etc.
• Committee asked the following details upon which PP could not reply satisfactorily:
✓ Decrease the quantity of manufacturing of R & D product looking to production capacity.
✓ Revised Site Plan/ layout by increasing greenbelt within premises at least 20-25% of plot
area.
✓ Concern authority permission letter for development of greenbelt outside the premises.
✓ Membership of common spray dryer mentioning capacities i.e consented, booked,
occupied and spare capacities.
• After deliberation, Committee decided to consider the proposal in one of the
upcoming SEAC meeting after submission of following details:
1. Revised product profile mentioning revised quantity of manufacturing of R & D
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 86 of 357
product looking to production capacity.
2. Revised Site Plan/ layout by increasing greenbelt within premises at least 20-25% of
plot area.
3. Concern authority permission letter for development of greenbelt outside the
premises.
4. Membership of common spray dryer mentioning consented, booked, occupied and
spare capacities.
• Later on PP has replied wrt ADS through Parivesh Portal. Their project was scheduled for
the presentation in the SEAC VC Meeting dated 01-09-2021.
• Project proponent (PP) and their Technical Expert from M/s. Bhagwati Enviro Care Pvt. Ltd
remain present during video conference meeting.
• Committee discussed on the following:
✓ Revised product profile was discussed. R&D product is reduced to 0.1 MT/M. Thus
total product will reduce.
✓ Green belt is increased to 20.5% and its location in layout was discussed.
✓ Land breakup was submitted. Green belt will be developed at land of Vinzol Parabdi
trust , letter from them accepting the same was submitted. PP was asked to submit
MOU with the trust for development of green belt.
✓ Membership certificate of Common spray dryer was submitted.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon’ble Supreme
Court of India in Civil Appeal no. 8478/2020 regarding operation of the Hon’ble NGT orders
dated 10/07/2019 & 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change in
product mix, after the 30th September 2020, considered as per the provisions in force at that
time as mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients
(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any
subsequent amendments.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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4. PP shall submit six monthly compliance report of Environmental Clearance without fail and
the same shall be critically assessed by the regulatory authority.
5. Total number of products manufacturing shall not exceeding two (2) at a given point of time
as per the plant capacity shown in plant layout.
6. (a) R & D products shall be of similar chemistry in line with the EIA Notification vide S.O.
1223 (E) dated 27/03/2020 and the pollution load shall remain the same as committed. (b)
Project proponent shall not take continuous/commercial production of the R & D materials.
Necessary approvals shall be obtained from the concern authorities prior to commercial
production of R & D materials. (c) Unit shall submit relevant details of R & D products like
raw materials, its safety measures to the regulatory authority well before R & D activity. (d)
Unit shall submit relevant details of R & D products like different wastes generated (Quantity
& Quality) and its management to the regulatory authority within a month of R & D activity.
7. Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB
directions to all SPCB vide letter no. B-29016/04/06PCI-1/5401 dated 05/02/2014 for
effluent discharge and air emission as per pollutants discharge/emission from respective
project and an arrangement shall also be done for reflecting the online monitoring results on
the company's server, which can be assessable by the GPCB/CPCB on real time basis.
[For Small/Large/Medium (Red Category) & Whichever (Air emission & Effluent
discharge) is applicable].
8. Close loop solvent recovery system with adequate condenser system shall be provided to
recover solvent vapours in such a manner that recovery shall be maximum and recovered
solvent shall be reused in the process within premises.
9. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the
CPCB guidelines. LDAR Logbooks shall be maintained
WATER
10. Total water requirement for the project shall not exceed 34.5 KLD. Unit shall reuse 1.3 KLD
of treated industrial effluent within premises. Hence, fresh water requirement shall not
exceed 33.2 KLD and it shall be met through GIDC only.
11. The industrial effluent generation from the project shall not exceed 21.9 KLD.
12. Generated Industrial Effluent shall be treated in ETP (Having Primary Treatment Unit) then
sent to Common Spray Dryer facility at Chhatral Environment Management System Pvt. Ltd.
Dhanot for Spray Drying
13. Treated waste water shall be sent to common facilities (CETP, Common MEE, Spray dryer
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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etc.) only after complying with the inlet norms of common facilities prescribed by GPCB to
ensure no adverse impact on Human Health and Environment
14. Domestic wastewater generation shall not exceed 1.3 KL/day for proposed project and it
shall be treated in STP. It shall not be disposed off through soak pit/ septic tank. Treated
sewage shall be utilized for gardening and cooling purpose within premises after achieving
on-land discharge norms prescribed by the GPCB.
15. During monsoon season when treated sewage may not be required for the plantation /
Gardening / Green belt purpose, it shall be stored within premises. There shall be no
discharge of waste water outside the premises in any case.
16. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
17. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
18. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned in
flue gas matrix.
19. Unit shall provide APCM and stack height as mentioned in process gas matrix.
20. PP shall use approved fuels only as fuel in boilers.
21. Two Stage Water Scrubber system shall be provided for control of process gas emission.
HAZARDOUS & SOLID WASTE
22. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
23. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
24. The PP shall develop green belt [377 Sq. m. (20.50%) inside plant premises + 365 Sq. m
m2 (19.8% ) at Vinzol Parabadi Trust (Vinzol Village) = Total: 742 Sq. m.) i.e. 40.3 % of
total plot area ] as per the undertaking submitted before SEAC. Green belt shall be
developed with native plant species that are significant and used for the pollution abatement
as per the CPCB guidelines. It shall be implemented within 3 years of operation phase in
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consultation with GPCB.
25. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
4 SIA/GJ/IND2/144902/2020
M/S. MORTAR & PESTLE
New Survey No. 542 (Old Survey No. 175),
EC reconsideration
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Khed, Himatnagar, Sabarkanthat.
Category of the unit: 5(f)
Project status: New
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/174902/2020on
dated 05.02.2021for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is a new project proposed for manufacturing of synthetic organic chemicals [API] as
tabulated below.
Sr.
No. Name of Products
API
OR
INTERMEDIA
TE
CAS No. Quantity
(Kg/M) *End-use of products
Group 1
1. Hydroxy progesterone
caproate API 630-56-8
500
To prevent preterm birth in
pregnant woman
2. Nandrolone
Decanoate API 360-70-3
Anemias, wasting syndrome
and osteoporosis in
menopausal women
Group 2
3. Norethistrone API 68-22-4
500
Birth control pill, menopausal
hormone therapy and
gynaecological disorders
4. Norethistrone Acetate API 51-98-9
Birth control pill, menopausal
hormone therapy and
gynaecological disorders
5. Progesterone API 57-83-0 To support pregnancy and
fertility in women
Group 3
6. Levonorestrel API 17489-40-6
200
As an emergency birth
control
7. Mifepristone API 84371-65-3 For medical abortion,
cushing’s syndrome
8. Nandrolone
Phenylpropanoate API 62-90-8 Breast cancer
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9. Norethisterone
Enanthate API 3836-23-5
Long-acting injectable female
contraceptive
Total
(Kg/MONTH) 1200
# Brief Note of Product Profile:
1. No of Manufacturing Plants: 1 no.
2. Brief Note regarding number of Products to be manufactured considering plant capacity:
• Total 9 nos. of products will be manufactured in the said plant.
Specific End-use of each proposed products:
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category of
Product (API/
Intermediate)
In case of Intermediate stage of API
Said API is used for/End Use of said
API
Stage i.e.
n-1, n-2, etc.
Name of API in which
Intermediate Used/ End use
of said Intermediate
CAS no.
(API)
1. Hydroxy
progesterone caproate
630-56-8 API -- -- -- To prevent preterm birth in pregnant woman
2. Nandrolone Decanoate
360-70-3 API -- -- --
Anemias, wasting syndrome and osteoporosis in menopausal women
3. Norethistrone 68-22-4 API -- -- --
Birth control pill, menopausal hormone therapy and gynaecological disorders
4. Norethistrone
Acetate 51-98-9 API -- -- --
Birth control pill, menopausal hormone therapy and gynaecological disorders
5. Progesterone 57-83-0 API -- -- -- To support pregnancy and fertility in women
6. Levonorestrel 17489-40-6 API -- -- -- As an emergency birth control
7. Mifepristone 84371-65-3 API -- -- -- For medical abortion, cushing’s syndrome
8. Nandrolone
Phenylpropanoate
62-90-8 API -- -- -- Breast cancer
9. Norethisterone
Enanthate 3836-23-5 API -- -- --
Long-acting injectable female contraceptive
• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA
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Notification 2006 and amendment dated 27th March, 2020.
• PP submitted an undertaking ensuring proposed product profile is in line with MoEF&CC’s
Notification vide S.O. 1223 (E) dated 27/03/2020 in respect of Active Pharmaceutical
Ingredients (API) as category B2 projects. Undertaking as proposal of said product are
eligible to consider under B2 category as per the notification of MoEF&CC dated 27.03.2020
• The proposal was considered in the SEAC video conference meeting dated 13.05.2021.
• Salient features of the project including Water, Air and Hazardous waste management are
as under:
Sr. no. Particulars Details
A-1 Total cost of Proposed Project (Rs. in Crores):
Total Project
1 Crore
Break-up of proposed project Cost:
Sr. No. Description Cost
(Rs. in Crores)
1. Land & land development 0.0*
2. Civil Work & Office Infrastructure 0.120
3. Plant & Machineries 0.445
4. EMP including (ETP, APCM, HWM & Greenbelt, DCS system, CER, etc.)
0.435
Total 1.0
* The proposed would be set-up on lease / rented shed /land.
A-2 Details of Environmental Management Plan (EMP) As below:
Sr. No.
Environmental Management
Aspect
Capital Cost [Rs. In Lakh]
Recurring Cost/Annum [Rs. In Lakh]
Remarks
1. Water Pollution 15,00,000 3,15,000 Capital cost would include cost of septic tank/soak pit system, ETP & evaporator etc. and recurring cost would include maintenance charges, manpower salary, sample analysis charges & cost for operating ETP etc.
2. Air Pollution 6,00,000 1,00,000 Capital cost would include air pollution control devices and the recurring cost would include operation and maintenance of pollution control devices and stack emission monitoring & sample analysis charges.
3. Hazardous / Solid Waste
Management
1,00,000 5,70,000 Capital cost would include expense for providing storage area for hazardous waste and recurring cost would be for solid/ hazardous waste packing & its
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disposal and for the membership of TSDF site.
4. Noise Pollution 10,000 10,000 Capital cost would include providing adequate sound enclosures and recurring cost would include monitoring of noise level.
5. Fire & Safety 11,00,000 2,00,000 Capital cost would include cost of Fire extinguishers, Fire hydrant system, Foam trolley, Fire proximity suit, Fire water tank, Flam proof fixtures, First aid kit, Automatic Control System and recurring cost would include maintenance charges.
6. AWH Monitoring 0 2,50,000 Regular monitoring of various environment parameters
7. Green Belt 20,000 2,00,000 Capital cost would include development of green belt within and outside the project premises and recurring cost would include maintenance charges, manpower salary etc.
8. Occupational Health & Safety
1,00,000 1,00,000 Capital cost would include cost of OHS centre, PPEs, First Aid, Fire Extinguisher, Fire Hydrant system, Medical facility, Mock drill / training awareness and recurring cost would include maintenance charges
9. Miscellaneous including DCS /
Automation system
7,20,000 1,70,000 Miscellaneous activity such as DCS / Automation system development of rain water harvesting system, and recurring cost would include maintenance charges and monitoring cost
10. CER Activity 2,00,000 0 CER activities will be implanted within nearby village of the project site as per their necessity in consultation with local sarpanch/needy fellow, during the above stated period of years after obtaining EC / starting the project activities as per implementation schedule.
Total 43,50,000 19,15,000
Summary
Cost of Project in Crores per Annum: 1 Crore
EMP Capital Cost in Crores per Annum and Percentage: 0.435 Crore & 43.5 %
EMP Recurring Cost in Crores per Annum and Percentage: 0.1915 Crore & 19.15 %
A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA, CER
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fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC’s OM vide 31.10.2019.)
% as per the OM Rs. in Crores
2 % 0.02
Brief note on proposed activities:
Proposed CER Activities* Budgetary Cost (Rs.) * Implementation
• Solar street light in primary school for electrification in khed village.
1,00,000 2021-22
• Provision of medical facilities like medical check-up camps in Raisingpura, Khed village.
1,00,000 2022-23
Total 2,00,000
B Land / Plot ownership details: ➢ Land / Plot ownership details are given in Annexure – 10 of Form-1
B-1 Plot area
Total Plot area
552.04 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities: ➢ Available land area is adequate for this project.
B-3 Green belt area
Total
(Sq. meter)
Area in Sq. meter 170
% of total area 30.8 %
C Employment generation
Total
9
D WATER
D-1
Source of Water Supply (GIDC, Bore well, Surface water, Tanker supply etc...) ➢ Local Water Tanker Supply
Status of permission from the concern authority. ➢ Unit will take necessary permission from the concern authority.
D-2 Water consumption (KLD)
Sr. No.
Purpose Water Consumption Quantity
(KL/Day)
A. Domestic 0.9
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B. Industrial
• Process 0.3
• Washing 0.04
Sub-total; (B) 0.34
C. Gardening NIL
TOTAL (A+B+C) 1.24
Brief Note on worst case scenario for water consumption: ➢ In the worst-case scenario, the max. process water requirement is 0.3 KLD and ➢ the total industrial water requirement will be 0.34 KLD Overall water consumption i.e. 0.9 KLD (domestic water) + 0.34 KLD (Industrial water) + NIL (Gardening) = 1.24 KLD
-
Summary of water requirement Quantity
KLD Remarks
Total water requirement for the project (A) 1.24
Quantity to be recycled (B) 0
Total fresh water requirement (C) 1.24
Ensure Total water requirement = Recycled water + Fresh water
i.e., A = B + C
1.24 = 0 + 1.24
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]
Source of waste water for reuse in KLD (From
where it is coming)
Application area with
quantity in KLD (Where it
is used)
Characteristics of waste water to be
reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
-- -- -- --
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. ➢ Total 0.35 KLD Industrial Effluent (Consisting 0.04 KLD from Washing & 0.31 KLD
from Process) will be generated, which will be will be treated ETP and treated effluent will be Evaporated through an electric evaporation system. Thus, unit will maintain Zero Liquid Discharge (ZLD).
D-3 Waste water generation (KLD)
Sr. No.
Purpose Wastewater Generation
Quantity (KL/Day) Remarks
A. Domestic 0.7 • Septic Tank/ Soak pit
B. Industrial
• Process 0.31 • Process effluent (0.35 KLD)
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• Washing 0.04 will be treated and then evaporated in evaporator
Sub-total; (B) * 0.35
C. Gardening Nil
TOTAL (A+B+C) 1.05
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative): ➢ In the worst-case scenario, the max. process wastewater generation is 0.31 KLD and ➢ The total industrial wastewater generation will be 0.35 KLD, which will be treated and then evaporated
in evaporator ➢ Overall wastewater generation i.e. 0.7 KLD (domestic wastewater) + 0.35 KLD (Industrial wastewater)
= 1.05 KLD
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (Whichever is applicable). ➢ Not Applicable
D-4 Mode of Disposal & Final meeting point
-
Domestic: Domestic Effluent (0.7 KLD) will be disposed to septic tank / soak pit system.
Industrial: Total 0.35 KLD Industrial Effluent (Consisting 0.04 KLD from Washing & 0.31 KLD from Process) will be generated, which will be will be treated ETP and treated effluent will be Evaporated through an electric evaporation system. Thus, unit will maintain Zero Liquid Discharge (ZLD).
- Clearly mention about final disposal ➢ Unit will adopt the ZLD system.
D-5 Treatment facilities
For Domestic waste water: ➢ Capacity of STP: Unit will provide septic tank / soak pit system.
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed. ➢ Total 0.35 KLD Industrial Effluent (Consisting 0.04 KLD from Washing & 0.31 KLD from Process) will
be generated, which will be will be treated ETP and treated effluent will be Evaporated through an electric evaporation system. Thus, unit will maintain Zero Liquid Discharge (ZLD). o Waste water generated from industrial activity (process, washing) will be collected into collection
cum neutralization tank. o Then wastewater will be given Chemical Oxidation treatment. o After completion of Chemical Oxidation Treatment, wastewater will be taken to Nutch Filter/Settling
Tank for chemical sludge separation. o After that it will be sent to Evaporator system. o ETP sludgealong with evaporation residue from Evaporator will be disposed off at TSDF site. Thus,
unit will maintain ZERO LIQUID DISCHARGE.
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP. ➢ Not Applicable
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Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ➢ The wastewater generated from the proposed manufacturing industry will be treated in a proposed
effluent treatment plant and the treated water will be evaporated in evaporator. Thus, unit will maintain the Zero Liquid Discharge (ZLD).
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
➢ Not Applicable
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
➢ Not Applicable
D-7 Simplified water balance diagram with reuse / recycle of waste water
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario thereof:
E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC’s OM vide dated 31.10.2019)
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of Fuel Quantity of Fuel MT/Day
Type of emissions i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
1 D. G. Set (65 KVA)
6 Diesel 11 Liter/Hr Particulate Matter
SO2 NOX
Adequate Stack Height
E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
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-
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emission Stack/Vent
Height (meter)
Air Pollution Control Measures (APCM)
1 Solvent Recovery Facility VOC 11 VOC Scrubber
Note: ➢ Details of gaseous raw materials used in proposed project: Acetylene Gas will be used as raw
material. ➢ Estimation of process gas emission (Product wise and Total): -- ➢ Requirement of the scrubbing media (KL per Day) considering solubility (Product wise and
Total): -- ➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its sound
management in HW matrix: --
E-4 Fugitive emission details with its mitigation measures.
F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
-
Sr. no.
Type/Name of Hazardous waste
Specific Source of generation (Name of
the Activity, Product
etc.)
Category and
Schedule as per HW Rules.
Quantity (MT/Annum
) Management of HW
1. ETP Sludge (Evaporation
Residue) ETP 35.3 2.4
Collection, storage and disposal at TSDF site.
2. Process Residue Mfg.
Process 28.1 33.6
Collection, storage and disposal at CHWIF site
3. Process Waste (Inorganic Salt)
Mfg. Process
28.1 0.6 Collection, storage and disposal at TSDF site.
4. Spent Carbon Mfg.
Process 28.3 1.2
Collection, storage and disposal at CHWIF site
5. Used / Spent Oil Mfg.
Process 5.1 1.2
Collection, storage and use within premises as a low-grade lubricants and /excess quantity (if any) sell to registered
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recycler
6. Discarded Bags/
Drums/ Containers
Raw Material Storage
Area
33.1 12.0 Collection, storage and sell to authorized vendor
7. Off Specification
Product Mfg.
Process 28.4 0.6
Collection, storage and disposal at CHWIF site
8. Spent Solvent Solvent
Recovery System
28.6 12.0 Collection, storage and disposal at CHWIF site
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility. ➢ We will become member of authorized TSDF site after getting EC.
F-3 Details of Non-Hazardous waste & its disposal (MSW and others)
--
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
1 -- -- -- --
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.
It may be noted that various solvents will be used to manufacture our proposed products; these solvents will be recovered/reused to the extent of minimum 95 % recovery. Details are given below;
Sr. No.
Name of Solvent Quantity (MT/Month) Recovery
(%) Requirement Recovery Loss
1 1.4-Doxane 3.80 3.648 0.152 96%
2 Acetone 1.00 0.950 0.050 95%
3 Di-Iso Propyl Ether 1.50 1.455 0.045 97%
4 Dichloromethane 3.46 3.391 0.069 98%
5 Dimethyl Sulfoxide 0.75 0.720 0.030 96%
6 Isopropyl Alcohol 0.10 0.099 0.001 99%
7 Methanol 3.65 3.577 0.073 98%
8 Tetra hydrofuran 1.89 1.814 0.076 96%
9 Toluene 4.00 3.920 0.080 98%
Solvent recovery/distillation system to be adopted during processing consisting:
• Reactor attached to primary condenser having chilled water circulation of 5°C followed by secondary condenser having chilled brine circulation of -15°C followed by scrubber.
• This will ensure that they get max. >95% recovery of solvent and if at all any vapors escapes it will be scrubbed in scrubber.
• The company do not have separate solvent recovery unit within premises, all solvent distillation is done during processing as a part of process.
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Recovered (distilled) solvents generated from the processing will be reused back in manufacturing process
G-2 Brief Note on LDAR proposed:
➢ LDAR system will be adopted; which mainly includes preventive / maintenance / monitoring schedule of all potential source of leakages / emissions viz, pumps, valves, flanges, etc. More details are presented in EMP.
➢ Close handling system and material transfer pumps with mechanical seals will be adopted. ➢ Solvent recovery will be done through series of condensers having cooling water & chilled water along
with scrubber to control VOC emission, (if any)
G-3 VOC emission sources and its mitigation measures
➢ Close handling system and material transfer pumps with mechanical seals will be adopted. ➢ Solvent recovery will be done through series of condensers having cooling water & chilled water along
with scrubber to control VOC emission, (if any)
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
-
Sr.no Name of Chemical Capacity of
Tank Number of
Tanks
Hazardous Characteristics
of Chemical
1 -- -- -- --
➢ It may be noted that no chemical will be stored in tank Brief note on storage of Hazardous chemicals in Tanks ➢ It may be noted that no chemical will be stored in tank Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc. ➢ All chemical/ materials will be stored in drum/barrels/carboys/bags. and all the chemicals / hazardous
chemicals will be stored as per PESO / Safety guidelines. Safety details of Hazardous Chemicals:
Type of Hazardous Chemicals
Safety measures
Detailed list of hazardous chemicals as per MSIHC rules are given in Annexure – 5 of Form-1
• All the chemicals / hazardous chemicals will be stored as per PESO / Safety guidelines. All the required safety measures will be undertaken as per safety guidelines.
• Applicability of PESO: Applicable permission will be obtained from the concern department prior to getting Consent from the GPCB.
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of Process
Safety measures including Automation
Exothermic Reaction:
➢ Exothermic reaction will be controlled by adequate dosing of reaction chemicals in a fixed time (not short duration) having adequate cooling water circulation in jacket of reaction vessels. Thus, any energy generated due to exothermic reaction will be controlled by external cooling circulation and therefore vessels will not be
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pressurized ➢ Reactant mass in reactor should be added such that surface-to-volume ratio is
maintained and runaway reaction is prevented. ➢ Cooling – jacketed system for the reactor should be in place to maintain the
reaction temperature.
➢ All the chemicals / hazardous chemicals will be stored as per PESO / Safety guidelines.
➢ Auto control system like DCS system will be provided.
H-3 Details of Fire Load Calculation
-
Total Plot Area: 552.04 m2
Area utilized for plant activity: 823 m2
Area utilized for Hazardous Chemicals Storage: 147.18 m2
Number of Floors: G+2
Water requirement for firefighting in KLD : 3.30
Water storage tank provided for firefighting in KLD: 100
Details of Hydrant Pumps: Yes, Two electrical (180 liter/min) and one diesel pump (2280 liter/min) at 7.5 kg/cm2 pressure.
Nearest Fire Station : Approx. 1.5 km away from the project site
Applicability of Off Site Emergency Plan: --
-
H-4 Details of Fire NOC/Certificate:
Unit will take Fire NOC certificate from concern authority.
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 9
Number of Contractual person/Labour : 0
Area provided for OHC: 117.58 m2
Number of First Aid Boxes : 5
Nearest General Hospital : Approx. 1.5 km away from the project site
Name of Antidotes to be store in plant : Required antidotes will be available at site.
• During the meeting dated 13.05.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and their Technical Expert from M/s Paramarsh (Servicing
Environment & Development) remain present during video conference meeting.
• This is Greenfield project proposed for manufacturing of synthetic organic chemicals [API&
its Intermediates] at Survey No. 542 (Old Survey No. 175), AT & PO: Khed, TA:
Himatnagar, District: Sabarkantha. Total plot area is 552.04Sq. m.
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• PP submitted that nearest residential area of Raisingpura Village is @ 0.50 Km and Khed
village @ 1.00 Km. There is no water bodies, natural drain within 500 m radius from the
project boundary. There is Roda Temple @ 0.67 KM. There are no Eco sensitive zones,
wild life sanctuaries within the 10 km area from the boundary of the project site.
• Committee asked project proponent to submit the Satellite image mentioning distance of
nearest villages i.e Raisingpura & Khed and Roda Temple from project site.
• Since, the unit falls in B2 category as per the MoEF&CC’s amended EIA Notification vide
S.O. 1223(E) dated 27.03.2020, the public consultation is not applicable as per paragraph
7(i) III (i) (e) of the Environment Impact Assessment Notification-2006.
• Committee noted the following:
✓ NA in the name of land owner and mentioning purpose of NA as industrial purpose.
✓ Rent agreement between land owner and the unit for a period of ten years.
✓ Product profile with specific End-use of each product.
✓ Site Plan/ layout with fire plan & floor plans and provision of separate entry & exits,
peripheral road, OHC, production area, raw material & finished goods storage area, ETP
area, hazardous waste storage area, utility area, 30.80% greenbelt within premises, etc.
✓ Source of water is tanker water supply. PP submitted undertaking regarding no borewell
digging within premises.
✓ Generated industrial effluent will be treated in primary ETP followed by electric
evaporator.
✓ Domestic effluent will be disposed through septic tank or soak pit. Committee insisted to
treat the domestic effluent.
✓ PP submitted hazardous waste matrix mentioning source of generation, quantity and
Mode of disposal and committed to comply the Hazardous and Other Wastes
(Management and Transboundary Movement) Rules 2016.
✓ Diesel is proposed as fuel in D G Set.
✓ VOC scrubbing system is proposed for control of process gas emission.
✓ Fire load calculation mentioning fire water storage (Cap: 100 KL), 3 Nos of foam type
extinguishers (Cap: 6 Kgs) and 3 Nos of foam trolley (Cap: 50 Kgs).
• Committee deliberated on Product profile, Layout plan, Storage details, Process safety, Fire
safety, water balance & waste water management, Flue gas and process gas emission & Air
Pollution Control System, Hazardous waste matrix, EMP, CER, Green belt, etc.
• After detailed discussion, Committee unanimously decided to consider the proposal
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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in the upcoming SEAC meeting only after satisfactory submission of the following:
1. Satellite Image mentioning distance of nearest villages i.e Raisingpura & Khed and Roda
Temple from project site.
2. Revised water balance mentioning treatment of domestic effluent.
• Later on PP has replied wrt ADS through Parivesh Portal. Their project was scheduled for
the presentation in the SEAC VC Meeting dated 01-09-2021.
• Project proponent (PP) and their Technical Expert from M/s. Bhagwati Enviro Care Pvt. Ltd
remain present during video conference meeting.
• Committee discussed on the following:
✓ Satellitte image of the project site was observed for revieweing of siting criteria.
✓ Water balance diagram was submitted where domestic water generated will be treated alomg with industrial effluent in ETP.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. PP shall comply conditions of any subsequent amendment or expansion or change in
product mix, after the 30th September 2020, considered as per the provisions in force at that
time as mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020.
2. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients
(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any
subsequent amendments.
3. PP shall submit six monthly compliance report of Environmental Clearance without fail and
the same shall be critically assessed by the regulatory authority.
4. Total number of products manufacturing shall not exceeding nine (9) at a given point of time
as per the plant capacity shown in plant layout.
5. Close loop solvent recovery system with adequate condenser system shall be provided to
recover solvent vapours in such a manner that recovery shall be maximum and recovered
solvent shall be reused in the process within premises.
6. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the
CPCB guidelines. LDAR Logbooks shall be maintained
WATER
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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7. Total water requirement for the project shall not exceed 1.24 KLD. fresh water requirement
shall not exceed 1.24 KLD and it shall be met through GIDC only.
8. The industrial effluent generation from the project shall not exceed 0.35 KLD.
9. Total 0.35 KLD Industrial Effluent (Consisting 0.04 KLD from Washing & 0.31 KLD from
Process) will be generated, which shall be treated in ETP and treated effluent will be
Evaporated through an electric evaporation system. Thus, unit will maintain Zero Liquid
Discharge (ZLD).
28. PP shall maintain Complete Zero Liquid Discharge [ZLD] status all the time and there shall
be no drainage connection from the premises and no wastewater discharge outside
premises by any means.
29. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days
10. Domestic wastewater generation shall not exceed 0.7 KL/day for proposed project and 0.7
KLD) shall be evaporated in evaporator. It shall not be disposed off through soak pit/ septic
tank.
11. During monsoon season when treated sewage may not be required for the plantation /
Gardening / Green belt purpose, it shall be stored within premises. There shall be no
discharge of waste water outside the premises in any case.
12. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
13. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
14. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned in
flue gas matrix.
15. Unit shall provide APCM and stack height as mentioned in process gas matrix.
16. PP shall use approved fuels only as fuel in boilers.
17. VOC Scrubber system shall be provided for control of process gas emission.
HAZARDOUS & SOLID WASTE
26. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
27. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
28. The PP shall develop green belt within premises (170 Sq. m i.e. 30.8 % of the total plot
area) as per the undertaking submitted before SEAC. Green belt shall be developed
with native plant species that are significant and used for the pollution abatement as per the
CPCB guidelines. It shall be implemented within 3 years of operation phase in consultation
with GPCB.
29. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
m) Unit shall provide safety valve and rapture disc, as well as auto dump or auto
quench/, suppress system for exothermic reaction vessel safety.
5 SIA/GJ/IND2/175373/2020
Novazeal Lifesciences
Plot No. 806, GIDC, Kerala, Bavla, Ahmedabad
EC reconsideration
Category of the unit: 5(f)
Project status: Expansion
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/175373/2020 for
obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is an existing unit and now proposed for expansion in manufacturing of synthetic
organic chemicals [API and Its Intermediates] as tabulated below: (Revised)
Sr. no.
Name of the Products
API OR
INTERMEDIATE
CAS. No.
Quantity MT/Month
End-use of the
products* Existin
g Propose
d Total
1 Sodium Bromide solution
--- 7647-15-6
5 0 5 Hypnotic,
Anticonvulsant
2 Chlomiphene
Citrate --- 50-41-9 1 0 1 Treating Infertility.
3 Oxyclozanide --- 2277-92-1
15 0 15
Used In The Treatment And
Control Of Fascioliasis In
Ruminants.
4 Bupropione hydrochlorid
e ---
31677-93-7
5 0 5
To Treat Major Depressive
Disorder & Seasonal
Affective Disorder.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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5 Benfotiamine --- 22457-89-2
1 0 1
Diabetic Neuropathy, Alcoholism, Alzheimer
disease, arthritis
6 n-butyl
bromide And/Or
--- 109-65-
9
30 -20 10
Used As A Source Of
The Butyl Group In Organic Synthesis
7 Iso propyl bromide And/Or
--- 75-26-3
8 n-propyl bromide
--- 106-94-
5
9 Chlorzoxazon
e --- 95-25-0 10 0 10 Muscle Relaxer.
10
Piroxicam --- 36322-90-4
5 0 5
Used To Reduce Pain, Swelling,
And Joint Stiffness From
Arthritis.
11
Nitrazepam And/Or
--- 146-22-
5
10 0 10
Used For Short-Term Treatment
Of Sleeping Problems
12
Diazepam --- 439-14-
5
To Treat Anxiety, Alcohol
Withdrawal, And Seizures
13
Buclazine dihydrochlori
de And/Or
--- 129-74-
8 10 0 10
Used As An Antivertigo
/Antiemetic Agent.
14
Meclazine dihydrochlori
de ---
1104-22-9
Used To Prevent And Treat
Nausea, Vomiting,
15
Tramadol hydrochlorid
e ---
36282-47-0
5 0 5
To Help Relieve Moderate To
Moderately Severe Pain Bulk Drugs
16
Duloxetine hydrochlorid
e ---
136434-34-9
5 0 5 Used To
Treat Depression And Anxiety
17
Dapoxetine hydrochlorid
e ---
129938-20-1
5 0 5 Bulk Drugs
18
Lidocaine hydrochlorid
e --- 73-78-9 5 0 5
Used To Decrease Discomfort
Or Pain.
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19
Lurasidone And/Or
API 367514-88-3
0
20 20
Treatment of schizophrenia and
bipolar depression.
20
Brexpiprazole
And/Or API
913611-97-9
Treatment of major depressive disorder (MDD)
and for treatment of schizophrenia.
21
Vilazodone Hydrochlorid
e And/Or
API 163521-08-2
Treatment of depression
22
Vortioxetine Hydrobromid
e And/Or
API 960203-27-4
Treatment of major depressive
disorder.
23
Quetiapine Fumarate
And/Or API
111974-69-7
Treatment of Schizophrenia
24
Clozapine And/Or
API 5786-21-0
Treatment of Schizophrenia
25
Olmesartan Medoxomil
And/Or API
144689-63-4
Treatment of high blood pressure.
26
Tenaligliptin hydrobromid
e And/Or
API 906093-29-6
Treatment of type 2 diabetes mellitus.
27
Losarton Potassium
API 124750-99-8
Treatment of high blood pressure.
Total 112 00 112
# Brief Note of Product Profile:
1. No of Manufacturing Plants: 1 no.
2. Brief Note regarding No of Products to be manufactured considering plant capacity:
• The proposed project is addition of new API products without increase in existing
consented product, i.e. 112 MT/month. The existing products namely n-butyl
bromide And / OR Iso Propyl bromide And / OR n-Propyl bromide, will be
manufactured @ 10 MT/month in place of consented capacity – 30 MT/month and
the proposed products mentioned above will be manufactured @ 20 MT/month.
End-use of Product:
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category
of Product (API/
In case of Intermediate stage of API
Said API is used for/End Use of said
API Stage of Intermedi
Name of APin which
CAS No.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 109 of 357
Intermediate)
ate n-1, n-2,
etc
Intermediate Used/ End use of said
Intermediate
(API)
1 Lurasidone 367514-
88-3 API --- --- --- Treatment of
schizophrenia and bipolar depression.
2 Brexpipraz
ole 913611-
97-9 API --- --- ---
Treatment of major depressive diso
rder (MDD) and for treatment of
schizophrenia
3 Vilazodone Hydrochlori
de
163521-08-2 API --- --- ---
Treatment of depression
4
Vortioxetine Hydrobromi
de
960203-27-4 API --- --- ---
Treatment of major depressive disorder.
5 Quetiapine Fumarate
111974-69-7 API --- --- ---
Treatment of Schizophrenia
6 Clozapine 5786-21-
0 API --- --- --- Treatment of
Schizophrenia
7 Olmesartan Medoxomil
144689-63-4 API --- --- ---
Treatment of high blood pressure.
8
Tenaligliptin
hydrobromide
906093-29-6 API --- --- ---
Treatment of type 2 diabetes mellitus.
9 Losarton
Potassium 124750-
99-8 API --- --- --- Treatment of high blood pressure.
• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA
Notification 2006 and amendment dated 27th March, 2020.
• PP submitted an undertaking ensuring proposed product profile is in line with MoEF&CC’s
Notification vide S.O. 1223 (E) dated 27/03/2020 in respect of Active Pharmaceutical
Ingredients (API) as category B2 projects. Undertaking as proposal of said product are
eligible to consider under B2 category as per the notification of MoEF&CC dated 27.03.2020
• The proposal was considered in the SEAC video conference meeting dated 25.02.2021.
• During the meeting dated 25.02.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and their Technical Expert from M/s. Excel Envirotech remain
present during video conference meeting.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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• Committee noted that this is expansion proposal for manufacturing of Synthetic organic
chemicals [API and Its Intermediates] plant at GIDC Kerala.Source of Water supply is GIDC.
Unit is having valid EC and CCA for existing plant and self certified compliance report of EC
and CCA submitted by PP. PP submitted undertaking stating that there is no legal court
case, legal notices and public complaint against unit.
• Looking to product profile presented by technical expert of PP during meeting, The
Committee members noticed that details regarding proposed production capacity and total
production capacity of each group mentioned are not matching with total proposed
production capacity and total capacity after expansion. On querying, the consultant
accepted that, they have made typographic error in product profile presented by him in
prsentation. Also Product profile submitted as per prescribed format showing proposed
production capacity and total production capacity of each group mentioned with total
proposed production capacity and total capacity after expansion is quite differ, specifically
for Lidocaine Hydrochloride,Tenaligliptin Hydrobromide and Loasarto Potassium proposed
products in presentation.
• Committee noted that this is serious process lapse wherein the submission of misleading
information regarding production capacity in presentation made before committee. Since
SEAC takes its decision on basis of details provided/ committed officially, such lapse needs
to be plugged.
• In view of above committee decided to suspend the presentation with decision that,
same will be re-scheduled after the official receipt or advance communication of
clarification regarding misleading information regarding products profile presented
by technical expert during meeting. The Committee conveyed this decision to the
presenter with instruction to follow this scrupulously.
• PP submitted reply of above query through e-mail along with supporting documents in
SEAC.
• This proposal is reconsidered in SEAC meeting dated 28.04.2021. PP along with their
technical expert/consultant from Excel Envirotech remains present in the meeting and made
presentation before committee.
• PP presented revised salient features of the project including Water, Air and Hazardous
waste management are as under:
Sr. Particulars Details
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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no.
A-1 Total cost of Proposed Project
(Rs. in Crores):
Existing
Proposed Total
1.75 Crores 0.50 Crores 2.25 Crores
Break-up of proposed project Cost:
Details Existing
(Rs. In Crores)
Proposed
(Rs. In Crores)
Total
(Rs. In Crores)
Land 0.42 0.00 0.42
Building 0.55 0.00 0.55
Machinery 0.78 0.50 1.25
A-2 Details of Environmental Management Plan (EMP) As below:
Sr
No. Unit Detail
Capital
Cost
(Rs. In
Lakh)
Operating
Cost
(Rs. In Lakh)
Maintenance
Cost
(Rs. In Lakh)
Total
Recurrin
g Cost
(Rs. In Lakh)
1 Waste Water ETP +
Evaporator 15 20 3.5 23,5
2 Air
Cyclone
Separator+Bag
Filter
2 2.8 1.2 4.0
3 Hazardous
Management
Storage and
membership 1 0.70 0.4 1.10
4 Fire & Safety
Fire fighting
equipment and
safety
measures
4.0 0 0.6 0.6
5 AWH
Monitoring Outsourced 0 0.3 0.25 0.55
6 Green Belt
Development -- 1 -- 0.35 0.35
7 Occupational
Health
First aid kits
and tie up with
doctor, PPE
2.5 -- 0.5 0.5
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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8 CER 1 % of new
investment 0.5 0 0 0
9 Process
automation
Cut off switches
and level
sensors
5.0 1.2 1.2 2.4
Total 31 25 8 33
Summary
Cost of Project in Crores Existing project cost: 1.75 crore.
Proposed project cost: 0.50 crore.
Total project cost: 2.25 crore.
EMP Capital Cost in Crores per
Annum and Percentage:
Capital cost: 0.25 crore.
Percentage: 11%
EMP Recurring Cost in Crores per
Annum and Percentage:
Recurring cost: 0.33 Percentage:
15 %
A-3 Details of CER as per OM dated 01/05/2018 (In case of project falls under
CPA/SPA, CER fund allocation to be atleast 1.5 times the slabs given in the OM
dated 01.05.2018 for SPA and 2 times for CPA in case of Environment Clearance as
per the mechanism published vide MoEF&CC’s OM vide 31.10.2019)
% as per the OM
Rs. In Crores
1 % 0.005
Brief note on proposed activities:
➢ The unit has planned to spend 1 % of the total cost of the proposed project.
Sr. No.
Area CER – Proposed planned Activities
Yearly Budgetary Provision (Rs)
Time Frame
1 Solar Panel
Provision of Solar Panel 1 (kW) AT Amipura Village
50,000/- 2022
Total 50,000/-
B Land / Plot ownership details:
B-1 Plot area
Existing
Proposed Total
1036 Sq. m. 00 Sq. m. 1036 Sq. m.
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B-2 Brief note on Area adequacy in line to proposed project activities:
➢ The proposed project has been done within the plant premises, so there
no any additional land will be acquired. The area of existing plot is 1036
sq m. However there will be no changes in existing layout plan.
B-3 Green belt area
Existing
Proposed
Total
Area in Sq. m
180 125 305
% of total area 17.37 0.12 30.00
C Employment generation
Existing
Proposed Total
15 5 20
D Water
D-1
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
GIDC water supply.
Status of permission from the concern authority.
➢ The water supply is from GIDC water supply.
D-2
Water consumption (KLD)
Category Existing
KLD
Proposed (Additional)
KLD
Total after Expansion
KLD Remarks
(G) Domestic 3.0 0.0 3.0
(H) Gardening
0.5 0.0 0.5
(I) Industrial
Process 1.7 13.2 14.9 The water requirement will be after proposed project.
Washing 0.5 0.0 0.5
Boiler 12.0 0.0 12.0
Cooling 3.0 0.0 3.0
Others 0.2 0.0 0.2
Industrial Total
17.4 13.2 30.6 --
Grand Total (A+B+C)
20.9 13.2 34.1 --
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Brief Note on worst case scenario for water consumption: ➢ The total water consumption is calculated based on the
worst case scenario of the products.
-
Summary of water requirement
Existing KLD
Proposed (Additional)
KLD
Total after Expansion
KLD Remarks
Total water requirement for the project (A)
20.9
13.2 34.1 --
Quantity to be recycled (B)
4.0 - 4.0 0.0 --
Total fresh water requirement I
16.9 17.2 34.1 --
Ensure Total water requirement = Fresh water + Recycled water
i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility. Not applicable for proposed project. [Source of reuse & application area]
Source of waste water for
reuse in KLD (From where it
is coming)
Application area with
quantity in KLD (where it is
used)
Characteristics of the waste water to be
reused (COD, BOD, TDS etc.)
Remarks regarding
feasibility to reuse
-- -- -- --
-- -- -- --
-- -- -- --
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle.
➢ For the proposed project, the generated waste water from the plant premises will be sent to Common Spray Dryer System.
D-3 Waste water generation (KLD)
Category Existing
KLD
Proposed (Additional)
KLD
Total after Expansion
KLD Remarks
(E) Domestic 2.2 0.0 2.2 Used for
Gardening
(F) Industrial
Process 3.4 15.8 19.20 After
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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proposed project, the
total generated
waste water from the
plant premises [for existing and proposed] will be sent to Common Evaporation
System.
Washing 0.5
0.0 0.5
Boiler 0.5
0.0 0.5
Cooling 0.02
0.0 0.02
Others 0.2
0.0 0.2
Total Industrial waste water
4.62 15.8 20.42 --
Total [A+B] 6.87 -- 22.62 --
Brief Note on worst case scenario for waste water generation(Qualitative and
Quantitative):
➢ The generated waste water from the plant premises @ 20.42 KL/day will be
subjected to solvent stripper and then primary treatment in ETP. The primary treated
waste water will be sent to Common Spray Dryer System.
Brief justification in case of no process effluent generation or no industrial effluent
generation or no high concentration effluent generation from proposed project
(Whichever is applicable).
➢ Not applicable.
D-4 Mode of Disposal & Final meeting point(Existing and Proposed)
Existing and Proposed
Domestic: For Existing: Domestic waste water will be disposed off through soak-pit
system.
For Proposed: Domestic waste water will be treated in STP and used for
gardening.
Industrial: For Existing: The generated waste water is subjected to primary treatment
and then sent to evaporator within the plant premises to maintain Zero
Liquid Discharge.
For Proposed: The generated industrial waste water will be sent to
Common Spray Dryer System after having primary treatment.
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-
Clearly mention about final disposal
D-5 Treatment facilities:
For Domestic waste water:
Capacity of STP: 3 KLD
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each stream
i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-
2….) for each stream shall be proposed
Sr. No. Name of Unit Capacity in m3 Remarks
1 Collection Cum Equalization Tank 5.00 Existing
2 Neutralizer Tank 5.00 Existing
3 Filter Press 24 X 24 X 24 nos. Existing
4 Final Holding Tank 2 nos., 10.00 KL
each. Additional.
5 Stripper unit 250 kg/hr Existing.
6 Evaporator --
At present evaporator is installed. After
proposed project, the generated waste
water will be discharged to
Common MEE.
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the
Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding
compliance of CETP.
➢ Not applicable.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
➢ Not applicable for proposed project.
D-6 In case of Common facility (CF) i.e CETP, Common Spray dryer, Common MEE,
CHWIF etc.
Name of Common facility (CF)(For waste water treatment)
➢ Common Spray Dryer
Membership of Common facility (CF) mentioning total capacity, consented
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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quantity, occupied capacity and spare capacity and norms of acceptance of
effluent from member units in-line with the direction given by GPCB vide Letter No.
GPCB/P-1/8-G (5)/550706 dated 08/01/2020
D-7 Simplified water balance diagram with reuse / recycle of waste water(Existing
and Proposed
Existing :
Raw Water [Fresh + Reuse]
20.9 [16.9 + 4.0] KL/day
Domestic
water
3.0 KL/day
Cooling Tower
(Make up)
3 KL/day
Effluent 0.02
KL/day
Sewage 2.2 KL/day
To Soak-Pit
ETP
4.62 KL/Day
Effluent 3.4
KL/day
Process
water
1.7 KL/day
Boiler [make up]
12 KL/day
Blow down 0.5
KL/day
Washing
0.5 KL/day
Effluent 0.5
KL/day
Scrubbing
0.2 KL/day
Evaporated within the
plant premises
4.62 KL/Day
Effluent 0.2 KL/day
Condensate Recovery
4.00 KL/Day
Proposed:
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E Air
E-1 Brief Note on fuel based heat energy requirement and worst case scenario
thereof:
➢ Coal / Agro waste - @ 0.8 T/hr
➢ Diesel for DG set - @ 7.5 L/hr [ for emergency]
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr,
KVA etc.
(in case of project located within CPA/SPA, APCM shall be in line to the mechanism
published in the MoEFCC’s OM vide dated 31.10.2019
Existing & Proposed
Sr.
Source of emission With Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions i.e. Air Pollutants
Air Pollution Control Measures (APCM)
1 Steam boiler
[2 nos. 1 TPH each]
30 m
Coal / Agro
Briquettes
@ 0.8 T/hr PM < 150 mg/Nm3
SO2 < 100 ppm NOx< 50
ppm
Multi cyclone, bag filter
followed by water scrubber
2 D. G. set
(100 KVA) 11 m Diesel @ 7.5 L/hr ---
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-
E-3 Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
Existing & Proposed
Sr. no.
Specific Source of emission (Name of the Product & Process)
Type of emission
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
1
Reaction [product - Source –
Oxyclozanide, Nitrazepam,
Lidocaine Hydrochloride]
HCl 11
HCl<20 mg/Nm3
Cl2< 09 mg/Nm3
SO2< 40 mg/Nm3
NOx< 25 mg/Nm3
Note:
➢ Details of gaseous raw materials used in proposed project
➢ Estimation of process gas emission (Product wise and Total)
➢ Requirement of the scrubbing media (KL per Day) considering solubility
(Product wise and Total)
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above
and its sound management in HW matrix.
E-4 Fugitive emission details with its mitigation measures.
➢ Measures like pumps with mechanical seals, proper ventilation, not any
leakages, use of adequate PPEs.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary
Movement) Rules 2016.
Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9
permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and
calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
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F-1 Hazardous waste management matrix
Existing & Proposed
Sr.
no.
Type/Name
of
Hazardous
waste
Specific
Source of
generation
(Name of the
Activity,
Product etc.)
Category
and
Schedule
as per HW
Rules.
Quantity
(MT/Annum)
Manageme
nt of HW Existing Proposed Total
1
Discarded
containers/
barrels /
liners
Packing of
Raw materials 33.1 5 0 5
Collection,
Storage,
transportati
on and sold
out to
Registered
Recyclers
2 Used oil From
machineries 5.1 0.305 0.0 0.305
Collection,
Storage,
transportati
on and sold
out to
Registered
Recyclers
3 Spent Solvent From process 20.2 300 125 425
Recycled
and
Reused
back in next
batch
4 Distillation
Residue
From solvent
recovery
system
20.3 8 0 8
Collection,
Storage,
transportati
on and sent
to CHWIF.
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5
Inorganic
Acid
HCl
From
manufacturing
of
Oxyclozanide,
Nitrazepam,
Lidocaine
Hydrochloride
B-15 15 0 15
Collection,
storage,
transportati
on and sold
out to the
authorized
person.
6 ETP sludge From ETP 35.3 14 0 14
Collection,
Storage,
transportati
on and sent
to secured
land fill site.
7. Process
Residue
From
manufacturing
process
28.1 0 82 82
Collection,
Storage,
transportati
on and sent
to secured
land fill site
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
Details of Membership Letter no. Date with spare capacity of the common Facility.
➢ TSDF: DIPL/1300000457/2020-21/245
➢ CHWIF: SEPPL/1300000457/2020-21/163
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Not Applicable
G Solvent management, VOC emissions etc.
G-1 Brief note on Types of solvents, Details of Solvent recovery, % recovery, reuse of
recovered Solvents etc
Sr.No.
Name of Product Solvent Input Input Qty. (MT/batch)
Qty. (MT/Month)
Solvent Recovered
Solvent Recovered
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(MT/Batch) (MT/Month)
1 Clomiphene Citrate
MDC 0.07 1.85 0.0676 1.79
2-Me THF 0.16 4.23 0.155 4.10
IPA 0.1 2.65 0.095 2.51
Chloroform 0.15 3.97 0.145 3.84
MEK 0.11 2.91 0.106 2.80
2 Oxyclozanide MCB 0.92 55.20 0.875 52.50
Acetone/ Methanol 0.766 45.96 0.73 43.80
3 Bupropione
Hydrochloride
MDC 0.27 9 0.26 8.67
IPA+ HCL 0.41 13.67 0.39 13
4 Benfotiamine Chloroform 0.28 1.67 0.27 1.61
Mysol 0.14 0.83 0.137 0.82
5 Chloroxazone Methanol 0.5 12.50 0.48 12.00
6 Piroxicam o-xylene 2.1 31.82 1.998 30.27
IPA 1.5 22.73 1.43 21.67
7 Nitrazepam AND /
OR
Toluene 1 41.67 0.955 39.79
Methanol 1.25 52.08 1.19 49.58
8 Diazepam Toluene 1 41.15 0.96 39.51
Methanol 1.25 51.44 1.1195 46.07
9 Buclazine
dihydrochloride AND / OR
Toluene 1 22.22 0.95 21.11
Acetone 0.8 17.78 0.765 17.00
10 Meclazine
dihydrochloride
Toluene 1 24.39 0.95 23.17
Acetone 0.8 19.51 0.77 18.78
11 Tramadol HCl Toluene/THF 1.13 20.93 1.075 19.91
Acetone 1 18.52 0.955 17.69
12 Duloxetine HCl
Toluene 1.5 25 1.41 23.50
Methanol 0.8 13.33 0.765 12.75
DMSO 0.6 10 0.575 9.58
Acetone 1 16.67 0.955 15.92
13 Dapoxetine
Hydrochloride
Methanol 0.8 11.94 0.76 11.34
Toluene 0.8 11.94 0.765 11.42
Acetone 1.2 17.91 1.15 17.16
14 Lidocaine
Hydrochloride
Toluene 1.1 20.75 1.05 19.81
Acetone 0.8 15.09 0.76 14.34
15 Losartan Potassium MDC 0.0065 130 0.00598 119.6
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AND / OR Toulene 0.0086 172 0.0078 156
Methanol 0.0047 94 0.00414 82.8
Acetone 0.0055 110 0.00443 88.6
16 Lurasidone AND /
OR
Tetrahydrofuran 0.3 35.29 0.291 34.24
Cyclohexane 0.38 44.71 0.36 42.35
Dichloro methane 0.18 21.18 0.17 20.00
17 Brexpiprazole AND
/ OR
Methanol 0.2 5.33 0.19 5.07
Dichloromethane 0.2 5.33 0.19 5.07
18 Vortioxetine
Hydrobromide AND / OR
n-Butanol 0.2 33.33 0.19 31.67
Ethyl acetate 0.3 50.00 0.29 48.33
19 Quetiapine
Fumarate AND / OR
Toluene 0.4 50 0.39 48.75
Methanol 0.2 25 0.18 22.5
20 Clozapine AND / OR Toluene 0.3 50 0.29 48.33
Isopropyl alcohol 0.2 33.33 0.18 30.00
21 Olmesartan
Medoxomil AND / OR
Methanol 0.2 36.36 0.19 34.55
Ethanol 0.3 54.55 0.29 52.73
Toluene 0.3 54.55 0.29 52.73
Diisopropylether 0.15 27.27 0.145 26.36
22 Teneligliptin
Hydrobromide Toluene 0.3 46.15 0.29 44.62
G-2 Brief Note on LDAR proposed:
• Methodology of Leak Detection And Repair: 1. Identification of component 2. Leak definition 3. Monitoring components 4. Repairing components 5. Recording
➢ Solvent Recovery Before LDAR
Sr. No
Name of Product Solvent Input Qty.
(MT/Month)
Solvent Recovered (MT/Month)
Solvent Recovered
%
1 Clomiphene
Citrate
MDC 1.85 1.79 97
2-Me THF 4.23 4.10 97
IPA 2.65 2.51 95
Chloroform 3.97 3.84 97
MEK 2.91 2.80 96
2 Oxyclozanide MCB 55.20 52.50 95
Acetone/ Methanol 45.96 43.80 95
3 Bupropione
Hydrochloride MDC 9.00 8.67 96
IPA+ HCL 13.67 13.00 95
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4 Benfotiamine Chloroform 1.67 1.61 96
Mysol 0.83 0.82 98
5 Chloroxazone Methanol 12.50 12.00 96
6 Piroxicam o-xylene 31.82 30.27 95
IPA 22.73 21.67 95
7 Nitrazepam AND
/ OR
Toluene 41.67 39.79 96
Methanol 52.08 49.58 95
8 Diazepam Toluene 41.15 39.51 96
Methanol 51.44 46.07 90
9 Buclazine
dihydrochloride AND / OR
Toluene 22.22 21.11 95
Acetone 17.78 17.00 96
10 Meclazine
dihydrochloride Toluene 24.39 23.17 95
Acetone 19.51 18.78 96
11 Tramadol HCl Toluene/THF 20.93 19.91 95
Acetone 18.52 17.69 96
12 Duloxetine HCl
Toluene 25.00 23.50 94
Methanol 13.33 12.75 96
DMSO 10.00 9.58 96
Acetone 16.67 15.92 96
13 Dapoxetine
Hydrochloride
Methanol 11.94 11.34 95
Toluene 11.94 11.42 96
Acetone 17.91 17.16 96
14 Lidocaine
Hydrochloride
Toluene 20.75 19.81 95
Acetone 15.09 14.34 95
15 Losartan
Potassium AND / OR
MDC 130.00 119.60 92
Toluene 172.00 156.00 91
Methanol 94.00 82.80 88
Acetone 110.00 88.60 81
16 Lurasidone AND / OR
Tetrahydrofuran 35.29 34.24 97
Cyclohexane 44.71 42.35 95
Dichloro methane 21.18 20.00 94
17 Brexpiprazole
AND / OR
Methanol 5.33 5.07 95
Dichloromethane 5.33 5.07 95
18 Vortioxetine
Hydrobromide AND / OR
n-Butanol 33.33 31.67 95
Ethyl acetate 50.00 48.33 97
19 Quetiapine Fumarate AND / OR
Toluene 50.00 48.75 98
Methanol 25.00 22.50 90
20 Clozapine AND /
OR
Toluene 50.00 48.33 97
Isopropyl alcohol 33.33 30.00 90
21 Olmesartan Medoxomil AND / OR
Methanol 36.36 34.55 95
Ethanol 54.55 52.73 97
Toluene 54.55 52.73 97
Diisopropylether 27.27 26.36 97
22 Teneligliptin
Hydrobromide Toluene 46.15 44.62 97
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➢ Solvent Recovery After LDAR
Sr. No
Name of Product
Solvent Input
B.P. °C
V.P.mm Hg
Qty. (MT/Month)
Solvent
Recovered
(MT/Month)
Solvent
Recovered
%
Percentage
of Losse
s in Air
Percentage
of Losse
s in Efflue
nt
Distillation Resid
ue Percentage
1 Clomiph
ene Citrate
MDC 39 350
mbar 1.85 1.79 97 0.2 0.3 2.93
2-Me THF
66 145 mm
Hg 4.23 4.10 97 0.2 0.4 2.53
IPA 82.5 760 2.65 2.51 95 0.5 0.3 4.20
Chloroform
61 160 mm
Hg 3.97 3.84 97 0.6 0.8 1.93
MEK 79.6 95 hPa 2.91 2.80 96 0.2 0.9 2.54
2 Oxycloza
nide
MCB 131 12 mbar 55.20 52.50 95 0.6 0.9 3.39
Acetone/ Methanol
56.1/64.7
30.93 kPa/128 mm Hg
45.96 43.80 95 0.5 0.3 3.90
3
Bupropione
Hydrochloride
MDC 39 350
mbar 9 8.67 96 0.2 0.3 3.20
IPA+ HCL
82.5 760 13.67 13 95 0.5 0.3 4.08
4 Benfotia
mine
Chloroform
61 160 mm
Hg 1.67 1.61 96 0 0.8 2.77
Mysol 64.7 128 mm
Hg 0.83 0.82 98 0.4 0.6 1.14
5 Chloroxa
zone Methanol 64.7
128 mm Hg
12.50 12.00 96 0.5 0.8 2.70
6 Piroxica
m
o-xylene 144 882 hPa
31.82 30.27 95 0.4 0.5 3.96
IPA 82.5 760 22.73 21.67 95 0.5 0.3 3.87
7 Nitrazepam AND
/ OR
Toluene 111 29 mbar 41.67 39.79 96 0.5 0.9 3.10
Methanol 64.7 128 mm
Hg 52.08 49.58 95 0.5 0.8 3.50
8 Diazepa
m
Toluene 111 29 mbar 41.15 39.51 96 0.5 0.6 2.90
Methanol 64.7 128 mm
Hg 51.44 46.07 90 0.8 1.9 7.74
9
Buclazine
dihydrochloride AND /
OR
Toluene 111 29 mbar 22.22 21.11 95 0.5 0.6 3.90
Acetone 56.1 30.93 kPa
17.78 17.00 96 0.3 0.6 3.48
10
Meclazine
dihydrochloride
Toluene 111 29 mbar 24.39 23.17 95 0.4 0.8 3.80
Acetone 56.1 30.93 kPa
19.51 18.78 96 0.3 0.6 2.85
1 Tramado Toluene/ 111/ 29 20.93 19.91 95 0.6 0.6 3.67
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1 l HCl THF 66 mbar/145 mm
Hg
Acetone 56.1 30.93 kPa
18.52 17.69 96 0.3 0.8 3.40
12
Duloxetine HCl
Toluene 111 29 mbar 25 23.50 94 0.5 0.6 4.90
Methanol 64.7 128 mm
Hg 13.33 12.75 96 0.5 0.8 3.07
DMSO 189 0.600
mm Hg 10 9.58 96 0.3 0.8 3.07
Acetone 56.1 30.93 kPa
16.67 15.92 96 0.3 0.6 3.60
13
Dapoxetine
Hydrochloride
Methanol 64.7 128 mm
Hg 11.94 11.34 95 0.5 0.8 3.70
Toluene 111 29 mbar 11.94 11.42 96 0.5 0.9 2.97
Acetone 56.1 30.93 kPa
17.91 17.16 96 0.3 0.7 3.17
14
Lidocaine
Hydrochloride
Toluene 111 29 mbar 20.75 19.81 95 0.5 0.8 3.25
Acetone 56.1 30.93 kPa
15.09 14.34 95 0.3 0.6 4.10
15
Losartan Potassiu
m AND /
OR
MDC 39 350
mbar 130 119.6 92 0.2 0.3 7.50
Toulene 111 29 mbar 172 156 91 0.3 0.6 8.40
Methanol 64.7 128 mm
Hg 94 82.8 88 0.9 2.5 8.51
Acetone 56.1 30.93 kPa
110 88.6 81 0.3 0.6 18.55
16
Lurasidone AND
/ OR
Tetrahydrofuran
66 145 mm
Hg 35.29 34.24 97 0.3 0.6 2.10
Cyclohexane
80.75
21.1 mm Hg
44.71 42.35 95 0.2 0.9 4.16
Dichloro methane
39 350
mbar 21.18 20.00 94 0.5 0.3 4.76
17
Brexpiprazole AND /
OR
Methanol 64.7 128 mm
Hg 5.33 5.07 95 0.5 0.8 3.70
Dichloromethane
39 350
mbar 5.33 5.07 95 0.5 0.3 4.20
18
Vortioxetine
Hydrobromide AND /
OR
n-Butanol 117.
7 6 mm
Hg 33.33 31.67 95 0.4 0.8 3.80
Ethyl acetate
77 73 mm
Hg 50.00 48.33 97 0.4 0.8 2.13
19
Quetiapine
Fumarate
AND / OR
Toluene 111 29 mbar 50 48.75 98 0.5 0.6 1.40
Methanol 64.7 128 mm
Hg 25 22.5 90 0.6 1.9 7.50
20
Clozapine AND /
OR
Toluene 111 29 mbar 50 48.33 97 0.5 0.6 2.23
Isopropyl alcohol
82.5 760 33.33 30.00 90 0.4 0.3 9.30
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21
Olmesartan
Medoxomil
AND / OR
Methanol 64.7 128 mm
Hg 36.36 34.55 95 0.5 0.8 3.70
Ethanol 78.3
7 5.950 kPa
54.55 52.73 97 0.4 0.6 2.33
Toluene 111 29 mbar 54.55 52.73 97 0.5 0.6 2.23
Diisopropylether
68.5 277 hPa
27.27 26.36 97 0.3 0.7 2.33
22
Teneligliptin
Hydrobromide
Toluene 111 29 mbar 46.15 44.62 97 0.5 0.8 2.03
Worst Case for Spent Solvent Generation (MT/Month)
951.62 -- 13.3 22.6 138.25
2
Worst Case for Spent Solvent Generation (MT/Annum)
11419 -- 159.6 271.2 1659.0
24
Percentage % 97 13.3 22.6 138.25
2
G-3 VOC emission sources and its mitigation measures
VOC will be generated from the manufacturing activities due to use of solvent and raw
materials.
Mitigation Measures :
➢ Provide the close handling system.
➢ Do the regular maintenance of valves, pipes, etc.
➢ Pneumatically transfer of liquid raw material in reactor.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages including spent acid and spent solvent tanks)
Name of chemical Capacity of
Tank Number of
Tanks
Hazardous Characteristics
of Chemical
1 -- -- -- --
2 -- -- -- --
3 -- -- -- --
Brief note on Storage of Hazardous chemicals in tanks
➢ Not applicable as the hazardous chemicals are not stored in tanks.
Brief note on Storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels,
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Carboys, Bags etc.
➢ Hazardous chemicals will be stored at designated storage area.
Safety details of Hazardous Chemicals:
Sr. No Type of hazardous chemical Type of Hazardous Safety measures
1 Acetone Extremely
Flammable
❑ Barrel Must Be Labeled ❑ Heat/Spark, Flame, Wear PPE And
Self Contain Breathing Apparatus ❑ Containers and equipment used for
storage and processing of corrosive material will be corrosion resistant
❑ Avoid Leakages ,Barrel Tightly Closed, Ground/Bond Barrel And Receiving Equipment
❑ Use Non Sparking Tools And Equipment,
❑ Precaution Measure Against Static Discharge
❑ Explosion Proof Electrical Lighting ❑ Eye Washer And Safety Shower
Should Be Provided. ❑ Use Water Spray, Dry Chemical
,Foam, Co2 Based Fire Extinguisher, Sand Bucket Must Be Provided
❑ Do Not Flush To Sewer.
2 Chloroform Toxic, Corrosive
3 Cyclohexane Extremely
Flammable
4 Dichloromethane or Methylene
chloride or Methylene dichloride
Extremely Hazardous
5 Ethanol Flammable
6 Ethyl acetate Flammable
7 Iso propanol/ IPA Highly Flammable
8 Methanol Toxicity, Highly
Flammable
9 n-Butanol Flammable
10 Tetra hydro furan Flammable
11 Toluene Highly Flammable
12 Methyl Ethyl Ketone Flammable
13 Mono Chloro Benzene Flammable
14 O-Xylene Highly Flammable
15 Dimethyl Sulfoxide Combustible
16 Diisopropylether Flammable
➢ Applicability of PESO:
Permission from PESO is not applicable.
H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic
Reaction etc.)
Types of Safety Measures including Automation
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Process
Manufacturing process
For Chlorination, proper scrubbing system should be required. SOP will be prepared for handling of chlorine gas. Chlorine emergency kit will be provided.
H-3 Details of Fire Load Calculation
Total Plot Area: 1036 sq. m.
Area utilized for plant activity: 375 sq. m.
Area utilized for Hazardous Chemicals Storage: 10 sq. m.
Number of Floors: Ground + 2 floor
Water requirement for firefighting in KLD: 0.937 KLD
Water storage tank provided for firefighting in KLD: 20 KL
Details of Hydrant Pumps: 50 mm pipe
Nearest Fire Station: Sanand Fire Station @ 25 km
Applicability of Off Site Emergency Plan: Yes
H-4 Details of Fire NOC/Certificate:
Will be obtained.
H-5 Details of Occupational Health Centre:
Number of permanent employee: 20
Number of Contractual person/Labour: --
Area provided for OHC: 15 sq. m.
Number of First Aid Boxes: 2
Nearest General Hospital: Parekh Hospital @6.7 km
Name of Antidotes to be store in plant: As per requirement.
• During the meeting dated 28.04.2021, PP presented revised product profile mentioning
existing and proposed products production capacities.
• Committee noted that this is an existing unit involved in manufacturing of synthetic organic
chemicals [API & its intermediates] for which obtained EC on dated: 31.08.2018 Self-
certified compliance report of existing EC & CCA is submitted.
• Committee noted that there are no court cases pending, litigation and no public complaints
against the project. There is no action taken by GPCB in last three years.
• Now, unit has proposed for manufacturing of synthetic organic chemicals [API & its
intermediates] at GIDC Kerala.Total plot area is 1036 Sq. m.
• Committee noted the following:
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✓ Site Plan/ layout with fire plan & floor plans with provision of separate entry & exit, 6 m
peripheral road for emergency exit, OHC, production plant, raw material & finished
goods storage, 30 % greenbelt within premises, etc.
✓ Generated industrial effluent will be treated in primary ETP and sent to Common spray
dryer.
✓ Domestic effluent will be treated in STP and reused for gardening/ plantation.
✓ Coal or briquette is proposed as fuel in boiler.
✓ Two stage scrubbing system is proposed for control of process gas emission.
✓ Scrubbing liquor will be treated in ETP.
✓ PP submitted hazardous waste matrix mentioning source of generation, quantity and
Mode of disposal and committed to comply the Hazardous and Other Wastes
(Management and Transboundary Movement) Rules 2016.
✓ Fire load calculation mentioning fire water storage (Cap: 20 KLand 20 Nos of foam
trolley (Cap: 50 Kgs).
• Committee deliberated on Product profile, Layout plan, Storage details, Process safety, Fire
safety, water balance & waste water management, Flue gas and process gas emission & Air
Pollution Control System, Hazardous waste matrix, EMP, CER, Green belt, etc.
• Committee insisted to submit the following details:
✓ Revised water balance mentioning recycle/ reuse of water.
✓ Flue gas matrix mentioning adequate stack height with boiler as coal / briquette is
proposed as fuel.
✓ Adequate fire water storage looking to plot size and storage of hazardous chemicals.
• After detailed discussion, Committee decided to consider the proposal in one of the
upcoming meeting of SEAC after submission of following details,
1. Revised water balance mentioning recycle/ reuse of water.
2. Revised Flue gas matrix mentioning adequate stack height with boiler as coal/ briquette
is proposed as fuel. Revised fire load calculation mentioning adequate fire water storage
looking to the plot size and storage of hazardous chemicals.
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Excel Envirotech remained
present during video conference meeting.
• Committee discussed regarding :
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Page 131 of 357
✓ Water balance diagram was discussed.
✓ Fire load calculation.
✓ Revise fire water storage tank capacity.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. PP shall comply conditions of any subsequent amendment or expansion or change in
product mix, after the 30th September 2020, considered as per the provisions in force at
that time as mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020.
2. PP shall carry out proposed project/activities in respect of Active Pharmaceutical
Ingredients (API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020
and any subsequent amendments.
3. PP shall submit six monthly compliance report of Environmental Clearance without fail and
the same shall be critically assessed by the regulatory authority.
4. Close loop solvent recovery system with adequate condenser system shall be provided to
recover solvent vapours in such a manner that recovery shall be maximum and recovered
solvent shall be reused in the process within premises.
5. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the
CPCB guidelines. LDAR Logbooks shall be maintained
WATER
6. Total water requirement for the project shall not exceed 34.1KLD. fresh water requirement
shall not exceed 34.1KLD and it shall be met through GIDC only.
7. The industrial effluent generation from the project shall not exceed 20.42KLD.
8. The generated industrial waste water shall be sent to Common Spray Dryer System after
having primary treatment.
9. Treated waste water shall be sent to common facilities (CETP, Common MEE, Spray dryer
etc.) only after complying with the inlet norms of common facilities prescribed by GPCB to
ensure no adverse impact on Human Health and Environment
10. Domestic wastewater generation shall not exceed 2.2KL/day for proposed project and it
shall be treated in STP. It shall not be disposed off through soak pit/ septic tank.Treated
sewage shall be utilized for gardening and plantation purpose within premises after
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Page 132 of 357
achieving on-land discharge norms prescribed by the GPCB.
11. During monsoon season when treated sewage may not be required for the plantation /
Gardening / Green belt purpose, it shall be stored within premises. There shall be no
discharge of waste water outside the premises in any case.
12. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
13. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
14. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned
in flue gas matrix.
15. Unit shall provide APCM and stack height as mentioned in process gas matrix.
16. PP shall use approved fuels only as fuel in boilers.
17. Alkali scrubbing system shall be provided for control of Process gas emission.
HAZARDOUS & SOLID WASTE
18. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
19. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
20. The PP shall develop green belt within premises (305 Sq. m i.e. 30 % of the total plot area)
as per the undertaking submitted before SEAC. Green belt shall be developed with native
plant species that are significant and used for the pollution abatement as per the CPCB
guidelines. It shall be implemented within 3 years of operation phase in consultation with
GPCB.
21. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 133 of 357
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
6 SIA/GJ/IND2/175379/2020
MAHADEV CHEMICALS
Plot no. C-1/264, Phase –II, GIDC Vatva, Ahmedabad-382445
EC Reconsideration
Category of the unit: 5(f)
Project status: Expansion
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/175379/2020 on
dated 04.11.2020 for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is an existing unit and now proposes for expansion in manufacturing of synthetic
organic chemicals [API and API Intermediates] as tabulated below
Sr. No.
Name of Products
API Or
Intermediate
CAS Numb
er
Quantity MT/Month
End users Existing
Proposed
Total
1
Para Chloro Benzene Sulphonyl Chlorides
Intermediate
98-60-2
5.00 -3.00 2.00
Intermediate used to manufacture of glimepiride
2 Para Chloro Benzene Sulphonamide
Intermediate
98-64-6
8.00 -6.00 2.00
Intermediate used to manufacture of Chlorzoxazone
3 Acetyl Sulphanilamide
Intermediate
121-61-9
2.00 0.0 2.00
Intermediate used to manufacture of Sulfamethoxazole
4 Sulphanilamide Intermedia
te 63-74-
1 0.00 4.00 4.00
Intermediate used to manufacture of Sulfamethoxazole
5 Beta Phenyl Acetamide Sulfonamide
Intermediate
41472-49-5
0.00 8.00 8.00
Intermediate used to manufacture of Glibenclamide
6 4-Amino pyridine-3-sulphonic Acid
Intermediate
29452-57-1
0.00 2.00 2.00
Intermediate used to manufacture of Torsemide
Total 15.00 5.00 20.00
# Brief Note of Product Profile:
1. No of Manufacturing Plants: 1 Nos.
• Brief Note regarding number of Products to be manufactured considering plant
capacity: Unit is already having existing infrastructure in the form of equipment /
machinery with sufficient capacity to cater to the requirement of proposed
expansion / inclusion of new products.Considering manufacturing Plant capacity:
Existing: 0.5 Ton/Day & Proposed: 0.2 Ton/Day
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ENDUSE OF PRODUCTS
Sr. No.
Name of the Product
CAS No.
(Product)
In case of Intermediate stage of API
CAS No.
(API)
Said API is used for/End Use of
said API
Stage i.e. n-1, n-2, etc.
Type/ Category of
Product (API/
Intermediate)
Name of API in which
Intermediate Used/ End use
of said Intermediate
1.
Para ChloroBenzene sulphonyl Chlorides
98-60-2
n-1 Intermediat
e Glimepiride
93479-97-1
Intermediate used to manufacture of glimepiride
2. Para Chloro Benzene Sulphonamide
98-64-6 n-1
Intermediate
Chlorzoxazone 95-25-
0
Intermediate used to manufacture of Chlorzoxazone
3. Acetyl Sulphanilamide
127-56-0
n-1 Intermediat
e
Sulfamethoxazole
723-46-6
Intermediate used to manufacture of Sulfamethoxazole
4. Sulphanilamide 63-74-1 n-2
Intermediate
Sulfamethoxazole
723-46-6
Intermediate used to manufacture of Sulfamethoxazole
5. Beta Phenyl Acetamide Sulfonamide
41472-49-5
n-1 Intermediat
e Glibenclamide
10238-21-8
Intermediate used to manufacture of Glibenclamide
6. 4-Amino Pyridine-3-sulphonic Acid
29452-57-1
n-1 Intermediat
e Torsemide
56211-40-6
Intermediate used to manufacture of Torsemide
• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA
Notification 2006 and amendment dated 27th March, 2020.
• PP submitted an undertaking ensuring proposed product profile is in line with MoEF&CC’s
Notification vide S.O. 1223 (E) dated 27/03/2020 in respect of Active Pharmaceutical
Ingredients (API) as category B2 projects. Undertaking as proposal of said product are
eligible to consider under B2 category as per the notification of MoEF&CC dated 27.03.2020
• The proposal was considered in the SEAC video conference meeting dated 07.01.2021.
• During the meeting dated 07.01.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and Technical expert from Ramans Enviro Services Pvt.Ltd,
Ahmedabad remains present during video conference meeting.
• Committee noted that Green belt, Roads etc not properly shown in the Lay Out plan
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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presented before the Committee. Committee felt that Lay out Plan is very sketchy and
important aspects are not covered by PP, which was agreed upon by the PP.
• In view of the above, Committee decided to defer the project and consider the
proposal in one of the upcoming meeting of SEAC after submission of adequate reply
of following details:
1) Revised layout plan with mentioning adequate size peripheral road for easy movement
of fire tender and emergency vehicle, separate entry and exit and fire hydrant network
with water sprinkler in solvent storage area and ETP area, adequate size OHC etc and
revised area adequacy with land break up.
• PP submitted the reply of the said above points along with other supporting documents,
through e-mail.
• This proposal is reconsidered in SEAC meeting dated 27.07.2021. PP along with their
technical expert/consultant from M/s Envycraft Environmental Services remains present in
the meeting and made presentation before committee.
• PP presented revised salient features of the project including Water, Air and Hazardous
waste management are submitted as follows
Sr. no. Particulars Details
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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A-1 Total cost of Proposed Project
(Rs. in Crores):
Existing Proposed Total
0.6684crores 0.1611 Crores 0.829crores
Break-up of proposed project Cost:
Sr. No.
Description Existing
cost (Rs. In Lacks.)
Proposed Cost (Rs. In Lacks)
Total Cost
(Rs. In Lacks)
1 Land 9.500 0.000 9.500
2 Building Maintanace/Upgradation 43.500 2.000 45.500
3 Plant and Machinery 13.500 1.500 15.000
4 Electricity 0.220 0.100 0.320
5 Env. Protection & Safety -- 12.350 12.350
6 Q.A. Lab Equipment 0.120 -- 0.120
7 Preoperative + Contingency -- -- --
8 Initial budget for activities related to CER -- 0.162 0.162
Total 66.840 16.11 82.90
A-2 Details of Environmental Management Plan (EMP) As below:
Sr. No
Unit Detail Capital
Cost (Rs. In Lakhs
Operating Cost
(Rs. In Lakhs)
Maintenance Cost
(Rs. In Lakhs)
Total Recurring
Cost (Rs. In Lakhs)
1 Wastewater ETP Up-gradation of
existing 1.00 7.80 0.55 8.35
2 Air Up-gradation of Scrubber
System 2.00 0.08 0.05 0.13
3 Fire & Safety Fire Protective System & Safety equipments/PPEs
1.75 0.8 0.06 0.86
3 Hazardous Management
Membership and Storage Area
2 0.15 0.08 0.23
4 Environment Monitoring
Water & Wastewater, AAQI, Flue Gas
emission, Process gas emission, Work zone
monitoring
1.5 0.07 0.04 0.11
5 Green Belt Development
Development of Greenbelt area
0.85 0.03 0.03 0.06
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6. Occupational Health
OHC Facilities, doctor visit to plant, Periodical medical Check-up, Etc
3.25 0.66 0.05 0.71
7. CER Activity Nearby Village 0.162 0.005 0.005 0.01
Total 12.5 10.46
Summary
Cost of Proposed Project in Crores: Rs.0.82 Cr.
EMP Capital Cost in Crores per Annum and Percentage: Rs. 0.125 Cr.
EMP Recurring Cost in Crores per Annum and Percentage: Rs. 1.25Cr.
A-
3
Details of CER as per OM dated 01/05/2018 (In case of project falls under CPA/SPA, CER fund
allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for
CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC’s OM vide
31.10.2019.)
% As per the OM Rs. in Crores
1% Rs. 0.162 lacks
Brief note on proposed activities:
Sr. No.
Type of activities Name of
Surrounding Village/Area
Budget Amount (In
Lakhs)
1st Year
1 Sanitation Facility (Toilet & bathroom ) at Ropada village
Ropada Village
0.162
Total 0.162
B Land / Plot ownership details:
GIDC/RM/ABD/TFR/VTW/SHD/2715 Dated: 19/06/2007 B-1 Plot area
Existing Proposed Total
760Sq. m. 00 Sq. m. 760Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
➢ Production capacity: 20 MT/Month ➢ Company will store its major consumable raw material in Drums &Tanks (We procure
Raw Materials from the local market. 90% of these raw materials are easily available from this market. Hence, no excess quantity of raw materials will be stored).
➢ List of Hazardous chemicals stored in tanks shown below.
Sr.
no Name of Chemical
Capacity of Tank
Number of Tanks
Total Qty. to be store (KL)
Non-PESO Tank- 6 No.
1 Chloro Sulphonic Acid 12 KL 1 12 KL
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2 Liq. Ammonia 5 KL 1 5 KL
3 Caustic Lye 5 KL 1 5 KL
4 Spent Sulphuric Acid 10 KL 1 10 KL
5 Spend HCL 10 KL 1 10 KL
6 High COD effluent 10 KL 1 10 KL
➢ Area required for ETP 32.0 m2. ➢ 28.0 m² area provided for the Boiler & Utility. ➢ Company has provided 12 m2 for storage fly ash storage area (fly ash will be collect,
stored in hazardous area). ➢ 247 m² (G+2) area will be provided for the manufacturing of the proposed products.
S. N.
Particulars Criteria
for Storage
Inventory Required (MT)(KL)
Area Required
m2
Area Proposed
m2
1. Finished product storage area (2-week inventory)
0.5 MT/ 1m2 10 20 24
2. Other Tanks 10 KL X 3 5 KL X 2
40 50 59
3. Raw Material Storage Area (2-week inventory)
0.7 MT/ 1m2
20 30 40
4. Tank farm Area (Non-
PESO) Tanks
12 KL x1 12 6 16
5. Hazardous Waste Storage Area (90 Days inventory)
- 35 & 10 (Fly Ash) 25 48
127 MT
131 m2
187 m2
Hence, adequate area will be available for the manufacturing of proposed products.
B-3 Green belt area
Details Existing (Sq. meter)
Proposed (Sq. meter)
Total (Sq. meter)
Area in Sq. meter
0.00
650 Sq. m. [400 Sq. m Outside Plant
Premises (Approx. 52.6 % of total plot area) + 250 Sq. m.
in GIDC (Approx. 33 % of total plot area)]
650 Sq. m. [400 Sq. m Outside Plant
Premises (Approx. 52.6 % of total plot area) + 250 Sq. m. in GIDC (Approx. 33 %
of total plot area)]
% Of total area
0.00 85.6 % 85.6 %
C Employment generation
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Existing Proposed Total
9 4 & 5 (Contract base) 14
D WATER
D-1
Source of Water Supply
(GIDC, Bore well, Surface water, Tanker supply etc...)
GIDC water supply
Status of permission from the concern authority.
➢ GIDC supply is available to the unit.
D-2 Water consumption (KLD)
Sr. No.
Details Water Consumption in KLD
Remark Existing Proposed Ultimate
1 Domestic 1.50 0.5 2.0
Fresh Water from GIDC
supply
2 Gardening Outside the premises
3 Industrial
a. Process 10.00 -3.5 6.5
b. Cooling make up 1.20 Nil 1.20
c. Boiler 0.40 0.6 1.0
d. Washing/Scrubbing system 1.00 3.5 4.5
e. Scrubbing System - 0.5 0.5
Total of Industrial 12.60 1.1 13.7
Total (1+2+3) 14.10 1.6 15.7
Brief Note on worst case scenario for water consumption:
➢ Total Water Requirement of the proposed project will be 15.2 KLD, out of which Water Consumption for Process will be 6.5 KLD.
Sn
Product Water Req. (In Kl)
For 1 Ton Production
Total Production (Mt/Month)
Total Water Req. (KLD)
Existing
1 Para chloro benzene
sulphonyl chloride 6.61 2 0.44
2 Para Chloro Benzene
Sulphonamide 11.54 2 0.77
3 Acetyl sulphanamide 19.8 2 1.32
Proposed
4 Sulphanillamide 0 4 0
5 Beta Phenyl Acetamide
Sulphonamide 12.78 8 3.40
6 4-amino pyridine-3-
Sulphonic acid 5.73 2 0.38
Hence Worst Case Considered is 6.31~6.5 KLD
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Reuse/Recycle details (KLD) with feasibility.
[Source of reuse & application area]
Source of waste water for reuse in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, and TDS etc.)
Remarks regarding feasibility to reuse
- - - -
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle.
➢ Nil
Summary of water requirement
Existing KLD
Proposed (Additional) KLD
Total after Expansion KLD
Remarks
Total water requirement for the project (A)
14.10 1.6 15.7
GIDC Water Supply
Quantity to be recycled (B)
NIL NIL Nil
Total fresh water requirement (C)
14.10 1.6 15.7
Ensure Total water requirement = Fresh water + Recycled water
i.e. A = B + C
D-3 Waste water generation (KLD)
Sr. No
Details Wastewater Generation in KLD
Disposal System Existing Proposed Ultimate
1 Domestic 1.50 0.00 1.50 Treated in Primary ETP
2 Gardening 0.00 0.00 0.00
3 Industrial
-
a. Process 8.60 0.7 9.3
b. Cooling 0.30 0.00 0.30
c. Boiler blow down 0.10 0.10 0.20
d. Washing 1.00 3.50 4.5
e. Scrubbing 0.0 0.5 0.5
Total of Industrial(3) 10.00 4.8 14.8
Total(1+2+3) 11.50 4.8 16.3
Brief Note on worst case scenario for wastewater generation(Qualitative and Quantitative):
➢ Total Waste Water Generation of the proposed project will be 16.3 KLD (Industrial + Domestic), out of which Waste Water Generation for Process will be 9.3 KLD.
➢ Worst Case Scenario for waste water generation;
Sn Product Waste water total Total waste Characteristics
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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gen. (in KL) for 1 ton
production
production
(MT/month)
water (KLD)
Existing
1. Para chloro benzene sulphonyl chloride Effluent: 0.0 +
Spent Acid: 8.08 2
Effluent: 0.0 + Spent Acid: 0.53
pH – 6.5 to 7.5 (Neutralization at source) TSS – 220 mg/l TDS – 19460 mg/l BOD – 9099 mg/l COD– 23370 mg/l
2. Para Chloro Benzene Sulphonamide
11.2 2 0.75
3. Acetyl sulphanamide Effluent: 7.5 + Spent Acid: 17.68
2 Effluent: 0.5 + Spent Acid: 1.18
Proposed
4. Sulphanillamide 9 4 1.20
5. Beta Phenyl Acetamide Sulphonamide
Effluent: 5.8 + Spent Acid: 11.57
8 Effluent: 1.55 + Spent Acid: 3.08
6. 4-amino pyridine-3-Sulphonic acid
Effluent: 0.0 + Spent Acid: 7.6
2 Effluent: 0.0 + Spent Acid: 0.5
Hence Worst Case Considered is 9.3 KLD
➢ High COD Stream: 4 KLD (Sent to Common Spray Dryer Facility of Green Environment Services Co-
op. Society Ltd., Vatva&2 KLD to Common Evaporation facility of Society for Clean Earth) &5.3 KLD
Spent Acid to NOVEL.
➢ Low COD Stream: 6.8 KLD (wastewater generated from Boiler, Cooling. Washing, Scrubbing will
combine with Domestic wastewater and treated in ETP) sent to CETP of Green Environment Services
Co-op. Society Ltd., Vatva
Brief justification in case of no process effluent generation or no industrial effluent generation or
no high concentration effluent generation from proposed project (Whichever is applicable).
➢ Not applicable
D-4 Mode of Disposal & Final meeting point (Existing and Proposed)
Existing and Proposed
Domestic: Existing: domestic wastewater will be disposed of to soak pit through septic tank. Proposed: Domestic wastewater will be treated into ETP.
Industrial: Existing:The industrial wastewater generation will remain10.0 KLDwill be treated in primary ETP and it will be disposed to CETP of Green Environment Services Co-op. Society Ltd., Vatva. Proposed: High COD Stream: 4 KLD (Sent to Common Spray Dryer Facility of Green Environment Services Co-op. Society Ltd., Vatva & 2 KLD to Common Evaporation
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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facility of Society for Clean Earth) & 5.3 KLD Spent Acid to NOVEL. Low COD Stream: 6.8 KLD (wastewater generated from Boiler, Cooling. Washing, Scrubbing will combine with Domestic wastewater and treated in ETP) sent to CETP of Green Environment Services Co-op. Society Ltd., Vatva
-
Clearly mention about final disposal
D-5 Treatment facilities
For Domestic waste water:
Capacity of STP: -- NA
For Industrial waste water: Treatment facility within premises with capacity
Low COD Stream Stream 1 –
✓ Wastewater 5.5 KLD (0.2 KLD from Boiler & 0.3 KLD from cooling, 4.5 Washing, 0.5 KLD Scrubbing) will be collected and treated in Primary ETP.
Sr. No.
Parameter Unit Stream from other utilities Characteristics
Combine Effluent Boiler Cooling Washing
Scrubbing
Quantity (KLD) 0.2 0.3 4.5 0.5 5.5
1 pH pH Unit
7.5-8.0 7.5-8.0 7.5-8.0 7.5-8.0 7.5-8.0
2 TSS mg/L 52 60 139 120 139
3 TDS mg/L 1100 1200 2196 500 2196
4 BOD mg/L 10 16 446 210 446
5 COD mg/L 30 50 1311 625 1311
6 Ammo.
Nitrogen mg/L Nil Nil Nil Nil Nil
➢ Combine effluent 5.5 KLD will combine with domestic wastewater 1.5 KLD and treated in ETPand
sent to CETP of Green Environment Services Co-op. Society Ltd., Vatva
Sr. No.
Parameter Unit Combine Effluent
Domestic Primary
ETP Primary ETP
Outlet
Quantity (KLD) 5.5 1.5 7 6.8
1 pH pH Unit 6.5-7.5 6.5-7.5 6.5-7.5 6.0-7.0
2 TSS mg/L 139 300 173.5 52
3 TDS mg/L 2196 750 1886 1980
4 BOD mg/L 446 250 404 323
5 COD mg/L 1311 10 1032 825
6 Ammo. Nitrogen mg/L Nil Nil Nil Nil
High COD Stream Stream 2 –
Wastewater generated from process @ 9.3 KLD, out of which 5.3 KLD spent acid will be sent to NOVEL and 2 KLD will be sent to Common Spray Dryer Facility of Green Environment Services Co-op.
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Society Ltd., Vatva and 2 KLD to Common Evaporation facility of Society for Clean Earth.
Sr. No. Parameter Unit Process
Quantity (KLD) 4
1 pH pH Unit 6.0-8.0
2 TSS mg/L 220
3 TDS mg/L 19460
4 BOD mg/L 9099
5 COD mg/L 23370
6 Ammo. Nitrogen mg/L Nil
Stream 3 –
➢ 5.3 KLD (25-30% Spent Sulphuric acid) will be sent to Spent Acid Management Facilityfrom NOVEL.
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of
Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ NA
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
➢ Not Applicable
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility (CF) (For waste water treatment)
➢ CETP of M/s. Green Environment Co-op Society Ltd.,Vatva
➢ Spray Dryer of M/s. Green Environment Co-op Society Ltd., Vatva
➢ Common Evaporation facility ofSociety for Clean Earth, Vatva
D-7 Simplified water balance diagram with reuse / recycle of waste water (Existing and
Proposed)
Water Balance Diagram Existing + Proposed
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E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario thereof:
➢ Total 1.0 MT/Day will be used as fuel in boiler. E-2 Flue gas emission details
Existing
Sr. No.
Stack attached to
Stack Height in (Meter)
Type of Fuel Quantity of Fuel MT/Day
Type of emissions i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
1 Boiler
0.3 TPH 12
Agro waste/Briquettes
instead of fire wood
1.0 MT/Day
SPM < 150 mg/Nm3
SO2 < 100 ppm NOX < 50 ppm
Multi cyclone
After Proposed Expansion
Sr. No.
Stack attached to
Stack Height in (Meter)
Type of Fuel Quantity of Fuel MT/Day
Type of emissions i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
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1 Boiler
0.3 TPH 30/0.5
Agro waste/Briquettes
instead of fire wood
1.0 MT/Day
SPM < 150 mg/Nm3
SO2 < 100 ppm NOX < 50 ppm
Multi cyclone
E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing
Sr. No.
Specific Source of emission(Name of the Product &
Process)
Type of Emission
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
1 Amination Vessel NH3 < 175 mg/Nm3
11 Condenser followed by
receiver followed by dipping tank
2 Sulphonation Vessel
HCl < 20 mg/Nm3 SO2< 40 mg/Nm3
11 Two Stage Alkali Scrubber
After Proposed Expansion
Sr. No.
Specific Source of emission (Name of the Product & Process)
Type of Emission
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
1 Amination Vessel (product no. 2,3,4,5)
NH3 < 175 mg/Nm3
18/0.2 Condenser followed by
receiver followed by dipping tank
2 Sulphonation Vessel (product no. 1,3,5)
HCl < 20 mg/Nm3 SO2< 40 mg/Nm3
18/0.2 Two Stage Alkali Scrubber
3 Reaction Vessel for (Product no.6) HCl < 20 mg/Nm3
18/0.2 Two Stage Alkali Scrubber
Note:
➢ Details of gaseous raw materials used in proposed project
No gaseous raw material will be used.
➢ Estimation of process gas emission (Product wise and Total)
Worst case for chlorination & Sulphonation of PCBSC, PCBS,AC, BPAS and 4-Amino pyridine-3-sulphonic acid and is given below table.
➢ Requirement of the scrubbing media (KL per Day) considering solubility (Product wise and
Total)
Sr no.
Source of emission (Name of
the Product)
Emission Assumed
Quantity of Gaseous
Emissions (KG/Day)
Water required to
scrub pollutants (KL/Day)
NaCl Sol. KL (25-30 %) (KL/Day) HCl
1 Para Chloro Benzene Sulphonyl HCl 0.02 0.05 0.07
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Chlorides
2 Acetyl Sulphanilamide
HCl 0.03 0.06 0.08
3 Beta Phenyl Acetamide Sulfonamide
HCl 0.07 0.016 0.23
4 4-Amino pyridine-3-sulphonic Acid
HCl 0.02 0.04 0.06
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its
sound management in HW matrix.
Sr. No.
Type of Waste
Source of Generation
Category Quantity,
MT/Annum Disposal/Management
1 NaCl Sol. From
scrubbing system
28.1 140 Collection, Storage and treat in ETP
for further treatment.
E-4 Fugitive emission details with its mitigation measures.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
Note:
➢ Priorities for HW Management: Reuse/Recycle within premises, Sell out to actual users
having Rule-9 permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and
calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Existing & Proposed
Sr. No.
Type of Waste
Source of Generation
Category Quantity, MT/Annum
Disposal/Management Existing Proposed Ultimate
1 Used Oil Plant Machineries
5.1 0.01 0.0 0.01
Collection, storage, transportation and sold out to the registered Recyclers.
2 Discarded Container/ Liners
Storage of Raw material and
33.1 22.50 0.0 22.50 Collection, Storage, Transportation & Disposal by sold out to
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 148 of 357
Products authorized recyclers
3 ETP Sludge
From ETP plant
35.3 97.2 0.0 97.2
Collection, storage, transportation and disposal to authorized TSDF.
4 Spent Sulphuric Acid
From Process (product no. 1,3,5& 6)
28.1 1200 700 1900
Collection, Storage, transportation and Disposal to actual users and/or NOVEL-spent acid management facility.
5 Scrubbing Sol. NaCl
From Scrubbing system
28.1 60 80 140 Collection, Storage and treat in ETP for further treatment.
6 Ammonia Solution
From Process (Product no. 2,3,4&5)
28.1 -- 54 54
Collection, Storage and reused in mfg process of PCBS, Acetyl sulphanilamide, Sulphanilamide & BPASwithin premises.
F-2 Membership details of TSDF, CHWIF etc.
Membership of Ecocare Infrastructure Pvt Ltd.
Details of Membership letter no. & Date with spare capacity of the Common Facility.
➢ M/s. Novel Spent Acid Management Dated: 23th Feb, 2019
➢ Ecocare Infrastructure Pvt Ltd. vide letter No.: ECIPL-296
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Fly Ash
Sr. no.
Type/Name of Other
wastes
Specific Source of generation
(Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
Existing Proposed Total
1 Fly Ash Agro waste/Briquettes 35 -- 35
Collection, storage, transportation & send to Brick manufacturer OR farmer for
agricultural purposes.
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered
Solvents etc.
There is no solvent use in manufacturing process.
G-2 Brief Note on LDAR proposed:
The Following methodology to be adopted during LDAR study:
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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➢ Identify the Chemical streams that must be monitored. ➢ Types of components (pumps, valves, connectors, etc.) to be monitored ➢ Frequency of monitoring. ➢ Actions to be taken if a leak is detected. ➢ Length of time in which an attempt to repair the leak must be performed. ➢ Actions that must be taken if a leak cannot be repaired within guidelines. ➢ Record-keeping and reporting requirements.
G-3 VOC emission sources and its mitigation measures
➢ Not required.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
-
Sr.
no Name of Chemical
Capacity of Tank
Number of Tanks
Total Qty. to be store (KL)
Non-PESO Tank- 6 No.
1 Chloro Sulphonic Acid 12 KL 1 12 KL
2 Liq. Ammonia 5 KL 1 5 KL
3 Caustic Lye 5 KL 1 5 KL
4 Spent Sulphuric Acid 10 KL 1 10 KL
5 Spend HCL 10 KL 1 10 KL
6 High COD effluent 10 KL 1 10 KL
Brief note on storage of Hazardous chemicals in Tanks
• Non-PESO-6 No.
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags
etc.
Safety Measures for Drum Storage area: ✓ Some chemicals will be received at plant in drums by road truck and stored in a separate drum
storage area. ✓ FLP type light fittings will be provided. ✓ Proper ventilation will be provided in go down. ✓ Proper label and identification board /stickers will be provided in the storage area. ✓ Conductive drum pallets will be provided. ✓ Drum handling trolley / stackers/fork lift will be used for drum handling. Separate dispensing room
with local exhaust and static earthing provision will be made. ✓ Materials will be stored as per its compatibility study and separate area will be made for
flammable, corrosive and toxic chemical drums storage. ✓ Smoking and other spark, flame generating item will be banned from the Gate.
Safety details of Hazardous Chemicals:
Type of Safety measures
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 150 of 357
Hazardous Chemicals
Non PESO tank
Safety measures for Acid storage Tank: ✓ Storage tank will be stored away from the process plant. ✓ Tanker unloading procedure will be prepared and implemented. ✓ Caution note and emergency handling procedure will be displayed at unloading
area and trained all operators. ✓ NFPA label will be provided. ✓ Required PPEs like full body protection PVC apron, Hand gloves, gumboot,
Respiratory mask etc. will be provided to operator. ✓ Neutralizing agent will be kept ready for tackle any emergency spillage. ✓ Safety shower, eye wash with quenching unit will be provided in acid storage area. ✓ Material will be handled in close condition in pipe line. ✓ Dyke wall will be provided to all storage tanks, collection pit with valve provision. ✓ Double drain valve will provided. ✓ Level gauge will be provided on all storage tanks. ✓ Safety permit for loading unloading of hazardous material will be prepared and
implemented. TREM CARD will be provided to all transporters and will be trained for transportation Emergency of Hazardous chemicals.
✓ Fire hydrant system with jockey pump as per TAC norms will be installed.
Safety Measures of Non PESO Tank ✓ Leakage / spillage mitigation plan ✓ Tank shall be rubber lined to prevent the corrosion ✓ Dyke wall shall be provided for containment ✓ Rubber type hand gloves and chemical splash goggles and full-face cartridge
type mask and PVC apron shall be used while manual handling ✓ Lime shall be readily available during leak to neutralize the spill material ✓ Safety shower, eye wash with quenching unit will be provided in acid storage
area. ✓ Material will be handled in close condition in pipe line. ✓ Double drain valve will provided. ✓ Level gauge will be provided on all storage tanks. ✓ Fire hydrant system with jockey pump as per TAC norms will be installed
• Applicability of PESO:NA
H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
SulphonationReaction
Type of Process Safety measures including Automation
Sulphonation /
Chlorination
➢ Provisions of safety rupture disk on reactor. ➢ Provisions of auto dumping Vessel. ➢ Required PPEs like full body protection PVC apron, Hand gloves, gumboot,
Respiratory mask etc. will be provided to operator. ➢ Charging will be done only through closed line and system. Scrubber
attached with closed system. ➢ Make sure the absorber unit (two stage Alkali scrubber) is working and
capable of handling vented HCl fumes.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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➢ Neutralizing agent will be kept ready for tackle any emergency spillage. ➢ Safety Shower and eye wash will be provided near process area. ➢ Emergency siren and wind sock will be provided. ➢ Tele Communication system and mobile phone will be used in case of emergency
situations for communication. ➢ Caution note and emergency first aid will be displayed and train for the same to
all employees. ➢ First Aid Boxes will be available in process area. ➢ Emergency organization and team will be prepared as per On site-Off site
emergency planning. ➢ Emergency team will be prepared and trained for scenario base emergency. Like
Toxic control team, Fire control team, First aid team, communication and general administration team, Medical team etc.
➢ Do not touch damaged containers or spilled material unless wearing appropriate protective clothing.
➢ Use water spray to reduce vapors; do not put water directly on leak, spill area or inside container. Keep combustibles (wood, paper, oil, etc.) away from spilled material.
➢ Cover with DRY earth, DRY sand or other non-combustible material followed with plastic sheet to minimize spreading or contact with rain.
H-3 Details of Fire Load Calculation
-
Total Plot Area: 760 Sq. M
Area utilized for plant activity: 247 Sq. M (G+2)
Area utilized for Hazardous Chemicals Storage: 48 Sq. M
Number of Floors: G+2
Water requirement for firefighting in KLD: 11205 Liter
Water storage tank provided for firefighting in KLD: 100000Liter
Details of Hydrant Pumps: Fire water Pump will be available. We will have 01 No’s of electrical fire water Pump located at pump house having capacity 4550.0 litres/min and 01 No’s of Diesel pump having capacity 4550.0 litres/min. Apart from this we have 01 Nos Jockey Pumps of capacity 1080.0 litres/min which maintains the Fire water Header Pressure at 8.0 kg/cm²
Nearest Fire Station: Jashodanagar Fire Station@ 4.31 Km
Applicability of Off-Site Emergency Plan: --
-
H-4 Details of Fire NOC/Certificate:obtained
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H-5 Details of Occupational Health Centre (OHC):
Number of permanent Employee : 9
Number of Contractual person/Labour : @ 4
Area provided for OHC: @16
Number of First Aid Boxes : 2
Nearest General Hospital Vatva @ 1.5 KM
Name of Antidotes to be store in plant : Milk of Magnesia, 4% Sodium Hydro Carbonate Solution. Wash affected skin with plenty of water. Administer Oxygen or shift to Fresh air.
• Committee noted that PP submitted revised rent deed for proposed project of 12 years in
between land owner and the unit.
• Committee noted the following:
➢ Product profile with specific End-use of each product. At a time, 12 products can be
manufactured.
➢ Source of water is Surface Water (Gujarat Water Infrastructure Limited-GWIL).
➢ Unit had proposed total industrial effluent will be segregated and high COD stream
will be evaporated in in-house MEE after treatment and low COD stream will be
treated in ETP and RO plant. RO permeate will be reused will be reused within
premises and RO reject will be evaporated in in-house MEE. Hence maintain ZLD.
➢ Agro waste/coal is proposed as fuel in boiler and APCM like MCS, Bag filter and
water scrubber proposed for boiler.
➢ Two stage scrubbers proposed for process stack.
➢ PP submitted hazardous waste matrix mentioning source of generation, quantity and
Mode of disposal and committed to comply the Hazardous and Other Wastes
(Management and Transboundary Movement) Rules 2016.
➢ Greenbelt development plan with 728.90 Sq m (30 %) of plot area.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 153 of 357
• Committee deliberated on Product profile, Layout plan, Storage details, Process safety, Fire
safety, water balance & waste water management, Flue gas and process gas emission & Air
Pollution Control System, Hazardous waste matrix, EMP, CER, Green belt, etc.
• Since, the unit falls in B2 category as per the MoEF&CC’s amended EIA Notification vide
S.O. 1223(E) dated 27.03.2020, the public consultation is not applicable as per paragraph
7(i) III (i) (e) of the Environment Impact Assessment Notification-2006.
• Committee asked for following details during meeting,
✓ Revised CER activity for concrete environment related proposal in place of activity
like tricycle to handicaps and assistance for medical instrument in PHC.
✓ Revised area break up and layout plan with mentioning separate solvent storage
area at ground floor in place of first floor.
✓ Revised greenbelt area proposal asper CPCB guideline instead of 30% of plot area.
✓ Risk assessment for chlorine gas considering its storage and its handling and super
imposition of dispersion model of chlorine gas on proposed project area considering
any leakage or blast of chlorine gas tonner or its handling and its impact on
surrounding residential area with its remediation control measures, looking to project
located outside notified area.
• After detailed discussion, Committee unanimously decided to consider the project in
one of upcoming meeting after submission of following documents:
1. Revised CER activity for concrete environment related proposal in place of activity
like tricycle to handicaps and assistance for medical instrument in PHC.
2. Revised area break up and layout plan with mentioning separate solvent storage
area at ground floor in place of first floor.
3. Revised greenbelt area proposal as per CPCB guideline instead of 30% of plot area.
4. Risk assessment for chlorine gas considering its storage and its handling and super
imposition of dispersion model of chlorine gas on proposed project area considering
any leakage or blast of chlorine gas tonner or its handling and its impact on
surrounding residential area with its remediation control measures, looking to project
located outside notified area
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Envycraft Environmental
Services remained present during video conference meeting.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 154 of 357
• Committee discussed regarding :
✓ Layout plan with mention of green belt, entry and exit was discussed.
✓ Greenbelt development was discussed. Pp has proposed to develop the green belt at Ropada village. PP had submitted the letter from Village gram panchayat.
✓ Membership certificate was submitted.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. PP shall comply conditions of any subsequent amendment or expansion or change in
product mix, after the 30th September 2020, considered as per the provisions in force at that
time as mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020.
2. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients
(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any
subsequent amendments.
3. PP shall submit six monthly compliance report of Environmental Clearance without fail and
the same shall be critically assessed by the regulatory authority.
4. Close loop solvent recovery system with adequate condenser system shall be provided to
recover solvent vapours in such a manner that recovery shall be maximum and recovered
solvent shall be reused in the process within premises.
5. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the
CPCB guidelines. LDAR Logbooks shall be maintained
WATER
6. Total water requirement for the project shall not exceed 15.7KLD. fresh water requirement
shall not exceed 15.7KLD and it shall be met through GIDC only.
7. The industrial effluent generation from the project shall not exceed 16.3 KLD.
8. Industrial effluent shall be segregated into two streams (1) High COD and TDS effluent (2)
Low COD and TDS effluent and it shall be managed as below.
• High COD and TDS effluent (4 KLD)
➢ High COD Stream: 4 KLD (Sent to Common Spray Dryer Facility of Green
Environment Services Co-op. Society Ltd., Vatva & 2 KLD to Common
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 155 of 357
Evaporation facility of Society for Clean Earth) & 5.3 KLD Spent Acid to
NOVEL..
• Low COD and TDS effluent (6.8 KLD):
➢ 6.8 KLD (wastewater generated from Boiler, Cooling. Washing, Scrubbing will
combine with Domestic wastewater and treated in ETP) sent to CETP of Green
Environment Services Co-op. Society Ltd., Vatva.
9. Treated waste water shall be sent to common facilities (CETP, Common MEE, Spray dryer
etc.) only after complying with the inlet norms of common facilities prescribed by GPCB to
ensure no adverse impact on Human Health and Environment
10. Domestic wastewater generation shall not exceed 1.5 KL/day for proposed project and it
shall be treated in ETP. It shall not be disposed off through soak pit/ septic tank.
11. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
12. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned in
flue gas matrix.
13. Unit shall provide APCM and stack height as mentioned in process gas matrix.
14. PP shall use approved fuels only as fuel in boilers.
15. Two Stage Alkali Scrubber, Condenser followed by receiver followed by dipping tank shall
be provided for control of Process gas emission.
HAZARDOUS & SOLID WASTE
16. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
17. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
18. The PP shall develop green belt [250 m2 (33%) inside plant premises + 400 m2 (52.6
%) Outside Plant Premises = Total: 650 Sq. m.) i.e. 85.5 % of total plot area ] as per the
undertaking submitted before SEAC. Green belt shall be developed with native plant
species that are significant and used for the pollution abatement as per the CPCB
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 156 of 357
guidelines. It shall be implemented within 3 years of operation phase in consultation with
GPCB.
19. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
m) Unit shall provide chlorine leakage control emergency kit and FRP hood with
scrubber system for chlorine safety.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 157 of 357
7 SIA/GJ/IND2/175649/2020
Aariva Pharma Pvt. Ltd
Survey No. 809 Samlaya, Savali, Vadodara
EC Reconsideration
Category of the unit: 5(f)
Project status: Expansion
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/175469/2020on
dated 05.11.2020 for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is an existing unit and now proposes expansion in manufacturing of synthetic organic
chemicals [API and API Intermediates] as tabulated below,
S
r.
N
o
Compan
y
Product
s
CAs
No
Type/
Categor
y of
Product
Quantity
(MT/Month) End Use
Existi
ng
Propos
ed
Tot
al
1. Silver
Fluoride -
Pharma
Ingredien
ts Salt
0.1 - 0.1
It is a topical medication used
to treat and prevent dental
caries (tooth decay) and
relieve dentinal hypersensitivity
2. Sodium
Iodide -
Pharma
Ingredien
ts Salt
2.1 - 2.1
The use of
sodium iodide is
contraindicated in pregnancy
and hyperthyroidism. , in the
treatment of thyroid, cancer
and hyperthyroidism or as
radiolabeling tracers in imaging
3. Potassiu
m Iodide -
Pharma
Ingredien
ts Salt
10.5 - 10.5
It may be used both to In a
radiation
emergency, potassium
iodide blocks only the thyroid
from absorbing
radioactive iodine, protecting it
from damage and reducing the
risk of thyroid cancer
4. Potassiu
m Iodate -
Pharma
Ingredien
ts Salt
3.0 - 3.0
As a medication it is used to
treat hyperthyroidism, in
radiation emergencies, and to
protect the thyroid gland
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 158 of 357
5.
Sodium
Citrate
Dihydrat
e/
Anhydro
us
-
Pharma
Ingredien
ts Salt
20.0 - 20.0
It is used as alkalizing agent, in
medicine. It is used in food and
beverages industry.
6.
Sodium
Phospha
te Di
basic/An
hydrous
-
Pharma
Ingredien
ts Salt
7.0 - 7.0
Sodium phosphate is used
in adults 18 years of age or
older to empty the colon (large
intestine, bowel) before
a colonoscopy (examination of
the inside of the colon to check
for colon cancer and other
abnormalities) so that the
doctor will have a clear view of
the walls of the colon.
7.
Sodium
Phospha
te Mono
Basic
-
Pharma
Ingredien
ts Salt
5.0 - 5.0
Sodium phosphate is used
in adults 18 years of age or
older to empty the colon (large
intestine, bowel) before
a colonoscopy (examination of
the inside of the colon to check
for colon cancer and other
abnormalities) so that the
doctor will have a clear view of
the walls of the colon.
8.
Potassiu
m
Phospha
te Mono
basic
-
Pharma
Ingredien
ts Salt
5.0 - 5.0
Potassium
phosphate is used to treat or
prevent hypophosphatemia
(low blood levels
of phosphorus). Potassium
phosphate is sometimes
added to intravenous (IV)
fluids given to people who
cannot eat or drink anything.
9.
Potassiu
m
Citrate
Dihydrat
e/
Anhydro
us
-
Pharma
Ingredien
ts Salt
5.0 - 5.0
Potassium citrate is used to
treat a kidney stone condition
called renal tubular acidosis. It
is also used to prevent kidney
stones that may occur
with gout. Potassium citrate is
a urinary alkalinizer. It works
by making the urine more
alkaline (less acid)
1
0.
PREGA
BLINE
1485
53-API - 10 10
Pregabline API is a class of
pharmaceutical drug called
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 159 of 357
50-8 anticonvulsants. Pregabalin is
used to relieve peripheral
neuropathic pain (pain from
damaged nerves) that can
occur in arms, fingers, hands,
legs, feet, or toes. It is also
used to treat fibromyalgia (a
long-lasting condition that may
cause pain in muscle stiffness
and, tiredness, tenderness,
and difficulty falling asleep or
staying asleep).
1
1.
PIPRAZI
NE
CITRAT
E
110-
85-0 API - 15 15
Piperazine belongs to the
family of medicines called
anthelmintics. Anthelmintics
are used in the treatment of
worm infections.
Piperazine is used to treat:
• common roundworms
(ascariasis) and
• pinworms
(enterobiasis;
oxyuriasis).
1
2.
PIPRAZI
NE
HEXAH
YDRAT
E
143-
63-2 API - 10 10
common roundworms
(ascariasis)
1
3.
PIPRAZI
NE
ADIPAT
E
142-
88-1 API - 15 15
alternative treatment for
ascariasis
1
4.
PIPRAZI
NE
DIHYDR
OCHLO
RIDE
142-
64-3 API - 15 15
Used as a one day wormer,
either in water or feed, for the
control of Round worms in
poultry, swine, and horses. It
will also control nodular worms
in swine, and small strongyles
in horses.
1
5.
PIPRAZI
NE
PHOSP
ATE
1453
8-56-
8
API - 15 15
An anti-nematodal agent
effective against the intestinal
nematodes ASCARIS
LUMBRICOIDES (roundworm)
and ENTEROBIUS
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Page 160 of 357
VERMICULARIS (pinworm,
threadworm)
1
6.
POVIDO
NE
IODINE
2565
5-41-
8
API - 15 15
Spectrum antiseptic for topical
application in the treatment
and prevention of wound
infection. It may be used in first
aid for minor cuts, grazes,
burns, abrasions and blisters.
Total 57.7 95 152.
70
ENDUSE OF PRODUCTS
Sr. No.
Name of the Product
CAS No.
(Product)
Type/ Catego
ry of Produc
t (API/
Intermediate)
In case of Intermediate stage of
API
Said API is used for/End Use of said API
Stage of
Intermediate n-1, n-2, etc
Name of API in which
Intermediate
Used/ End use of said
Intermediate
CAS No.
(API)
Existing
7. Silver
Fluoride -
Pharm
a
Ingredi
ents
Salt
- - -
It is a topical medication used to
treat and prevent dental
caries (tooth decay) and relieve
dentinal hypersensitivity
8. Sodium
Iodide -
Pharm
a
Ingredi
ents
Salt
- - -
The use of
sodium iodide is contraindicated in
pregnancy
and hyperthyroidism. , in the
treatment
of thyroid,cancer and hyperthyroidi
sm or as radiolabeling tracers in
imaging
9. Potassium
Iodide -
Pharm
a
Ingredi
ents
Salt
- - -
It may be used both to In a
radiation emergency, potassium
iodide blocks only the thyroid
from absorbing radioactive iodine,
protecting it from damage and
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 161 of 357
reducing the risk of thyroid cancer
10. Potassium
Iodate -
Pharm
a
Ingredi
ents
Salt
- - -
As a medication it is used to treat
hyperthyroidism, in radiation
emergencies, and to protect the
thyroid gland
11.
Sodium
Citrate
Dihydrate/
Anhydrous
-
Pharm
a
Ingredi
ents
Salt
- - -
It is used as alkalizing agent, in
medicine. It is used in food and
beverages industry.
12.
Sodium
Phosphate Di
basic/Anhydr
ous
-
Pharm
a
Ingredi
ents
Salt
- - -
Sodium phosphate is used
in adults 18 years of age or older
to empty the colon (large intestine,
bowel) before
a colonoscopy (examination of
the inside of the colon to check
for colon cancer and other
abnormalities) so that the doctor
will have a clear view of the walls
of the colon.
13.
Sodium
Phosphate
Mono Basic
- Pharm
a
Ingredi
ents
Salt
- - - Sodium phosphate is used
in adults 18 years of age or older
to empty the colon (large intestine,
bowel) before
a colonoscopy (examination of the
inside of the colon to check
for colon cancer and other
abnormalities) so that the doctor
will have a clear view of the walls
of the colon.
14.
Potassium
Phosphate
Mono basic
- Pharm
a
Ingredi
ents
Salt
- - - Potassium phosphate is used to
treat or prevent
hypophosphatemia (low blood
levels of phosphorus). Potassium
phosphate is sometimes added to
intravenous (IV) fluids given to
people who cannot eat or drink
anything.
15.
Potassium
Citrate
Dihydrate/
Anhydrous
- Pharm
a
Ingredi
ents
Salt
- - - Potassium citrate is used to treat
a kidney stone condition called
renal tubular acidosis. It is also
used to prevent kidney stones that
may occur with gout. Potassium
citrate is a urinary alkalinizer. It
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 162 of 357
works by making the urine more
alkaline (less acid)
Proposed
16.
PREGABLIN
E
1485
53-
50-8
API - - - PREGABLINE API is a class of
pharmaceutical drug called
anticonvulsants. Pregabalin is
used to relieve peripheral
neuropathic pain (pain from
damaged nerves) that can occur
in arms, fingers, hands, legs, feet,
or toes. It is also used to treat
fibromyalgia (a long-lasting
condition that may cause pain in
muscle stiffness and, tiredness,
tenderness, and difficulty falling
asleep or staying asleep).
17.
PIPRAZINE
CITRATE
110-
85-0
API - - - Piperazine belongs to the family of
medicines called anthelmintics.
Anthelmintics are used in the
treatment of worm infections.
Piperazine is used to treat:
• common roundworms
(ascariasis) and
• pinworms (enterobiasis;
oxyuriasis).
18.
PIPRAZINE
HEXAHYDR
ATE
143-
63-2
API - - - Benzyl benzoate is used to treat
lice and scabies infestations. It is
an effective and an inexpensive
treatment available over the
counter. It is used externally as a
cream or emulsion.
19.
PIPRAZINE
ADIPATE
142-
88-1
API - - - Permethrin is used for the
treatment of head lice and
scabies.
Permethrin is sprayed to control
mosquitoes during spring and
summer. It is used as a wood
preservative. It is used on many
food/feed crops, on farm animals
and in barns.
20.
PIPRAZINE
DIHYDROCH
LORIDE
142-
64-3
API - - - Used as a one day wormer, either
in water or feed, for the control of
Round worms in poultry, swine,
and horses. It will also control
nodular worms in swine, and small
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 163 of 357
strongyles in horses.
21.
PIPRAZINE
PHOSPATE
1453
8-56-
8
API - - - An anti-nematodal agent effective
against the intestinal nematodes
ASCARIS LUMBRICOIDES
(roundworm) and ENTEROBIUS
VERMICULARIS (pinworm,
threadworm)
22.
POVIDONE
IODINE
2565
5-41-
8
API - - - Spectrum antiseptic for topical
application in the treatment and
prevention of Wound Infection. It
may be used in first aid for minor
cuts, grazes, burns, abrasions and
blisters.
• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA
Notification 2006 and amendment dated 27th March, 2020.
• The proposal was considered in the SEAC video conference meeting dated 05.01.2021
• During the meeting dated 05.01.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and Technical expert from Satva Environ Consultancy remains
present during video conference meeting.
• Committee noted that this is an existing unit and now proposed for manufacturing of API
plant at Survey No. 809, Village: Samlaya, Ta: Savali, Dist. Vadodara. Committee noted that
unit is having valid CCA of the Board for existing project and presented self-compliance
report for existing CCA. PP submitted undertaking that there is no public complaint, legal
notices/closure from GPCB and legal court case against unit. Product profile along with End
Use discussed in depth. Looking to the some of the proposed API products like Benzyl
alcohol, Benzyl Benzoate etc. seems basic chemicals instead of API, Committee insisted for
submit technical justification regarding Benzyl alcohol, Benzyl Benzoate etc products falls in
API and in line with MoEF&CC’s Notification vide S.O. 1223 (E) dated 27/03/2020 in respect
of Active Pharmaceutical Ingredients (API) as category B2 projects.
• In view of the above, Committee decided to defer the project and consider the
proposal in one of the upcoming meeting of SEAC after submission of adequate reply
of following details:
1. Submit technical justification regarding Benzyl alcohol, Benzyl Benzoate etc. products
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 164 of 357
falls in API and in line with MoEF&CC’s Notification vide S.O. 1223 (E) dated 27/03/2020
in respect of Active Pharmaceutical Ingredients (API) as category B2 projects with
technical and authenticated supporting documents.
• PP submitted the reply of the said points along with other supporting documents.
• This proposal is reconsidered in SEAC meeting dated 31.05.2021. PP along with their
technical expert/consultant from M/s Satva Environ Consultancy remains present in the
meeting and made presentation before committee.
• PP presented revised salient features of the project including Water, Air and Hazardous
waste management are submitted.
• During meeting dated: 31.05.2021, PP presented Product profile along with End Use
discussed in depth. PP also presented form of API, brand name/ generic name along with
photographs. Looking to the some of the proposed API products like Benzyl alcohol, Benzyl
Benzoate etc. seems basic chemicals instead of API, Committee insisted for submit
technical justification regarding Benzyl alcohol, Benzyl Benzoate etc products falls in API
and in line with MoEF&CC’s Notification vide S.O. 1223 (E) dated 27/03/2020 in respect of
Active Pharmaceutical Ingredients (API) as category B2 projects.
• In view of the above, Committee decided to again defer the project and consider the
proposal in one of the upcoming meeting of SEAC after submission of adequate reply
of following details:
1. Submit technical justification regarding Benzyl alcohol, Benzyl Benzoate etc. products falls in API and in line with MoEF&CC’s Notification vide S.O. 1223 (E) dated 27/03/2020 in respect of Active Pharmaceutical Ingredients (API) as category B2 projects with technical and authenticated supporting documents.
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Satva Environ Consultancy
remained present during video conference meeting.
• Revised Salient features of the project is as undr:
Sr. no. Particulars Details
A-1 Total cost of Proposed Project
(Rs. in Crores):
Existing Proposed Total
1.5Crores 0.50Crores 2.0Crores
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Break-up of proposed project Cost:
Details Existing
(Rs. In Crores)
Proposed
(Rs. In Crores)
Total
(Rs. In Crores)
Land 0.50 - 0.50
Building 1.00 1.0 2.0
Machinery
A-2 Details of Environmental Management Plan (EMP) As below:
Sr.
No Unit Details
Capital
Cost
(Rs.in
Lacs )
Operati
ng
Cost
(Lacs
/Month)
Maintena
nce Cost
(Lacs/
Month)
Total
Recurring
Cost
(Lacs/
Month)
1
Effluent
Treatment
Plant
Installation of ETP and evaporator 5.0 0.50 0.10 0.80
2 Air
Installation of stack/vent & its
monitoring facilities including
provision of air pollution control
System
3.0 0.30 0.10 0.40
3 AWH
Monitoring
To conduct EMS efficacy &
environment monitoring - 0.50 - 0.50
4 Hazardous
Management Getting membership of TSDF site 0.50 0.1 - 0.1
5 Green belt
development Development of Greenbelt Area 3.0 - 0.20 0.20
6 Health &
Safety
Provision of Occupational Health
Centre with Antidotes 7.0 0.5 0.2 0.7
7
Fire
Prevention
Provision of Safety Measures
including Fire Detectors, Ammonia
Sensors, Siren/Alarm, Fire Hydrant,
Fire Extinguishers, Proxymate
Suits, SCBA, Foam Trolley,
25.0 1.0 0.5 1.5
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Lightening arrestors etc.
8 Other
CER Cost 1.0 - - -
Provision of PLC based SCADA
system 10.0 2.6 1.0 3.6
Total 54.5 5.5 2.0 7.5
Summary
Cost of Project in Crores per Annum: 1.0
EMP Capital Cost in Lakh per Annum and Percentage: 54.5
EMP Recurring Cost in Lakh per Annum and Percentage: 90.0
A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA, CER
fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in
case of Environmental Clearance as per the mechanism published vide MoEF&CC’s OM vide 31.10.2019.)
% as per the OM Rs. in Lakh
1 % 1.0
Brief note on proposed activities:
No. CER-Proposed Planned Activities Identified Villages
Year wise Budget (Lakhs)
1st Year
Capital
1 Providing RO System with 100 LPH capacity at primary School and Primary Health Center
Samlaya 1.0
Total (Year Wise) 1.0
Grand Total 1.0 lac
B Land / Plot ownership details:
B-1 Plot area
Existing Proposed Total
6300 Sq. m. NIL 6300 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Sr No.
Description of Area Existing After Expansion
Sq. m Sq. m For API Plant
1 Manufacturing Area - 650
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2 Raw material Storage - 379
3 Finish Good Storage - 474
4 Solvent Storage Tank Area - 99
5 Haz. Waste storage - 60 Existing Product
7 Production Area 500 500
8 Raw material Storage 50 50
9 Product Storage Area 50 50
10 Office and Lab area 25 36
11 OHC + Room area - 88
12 Utility area 211 211
13 ETP Area - 76.0
14 Green belt area 150 2079
15 Open 5313.75 1658
TOTAL 6300 6300
S
r
N
o
.
Description of Area
Criteria
for
Storage
Inventory
Required
(MT) (KL)
Area
Requir
ed
(m2)
Area
Propos
ed (m2)
1 Finished Product Storage Area
API (2 Week inventory) 95 MT 47.5 54.62 474
2 Raw Material Store area
(2 Week inventory)
600 Nos.
Bag 23.0 37.0
379 105 Nos.
Drum 36.0 80.0
3 Solvent Storage Area 3 KL X 1 3 20 99
4 Hazardous Waste Storage area
(ETP) (90 Day Inventory)
1.8
MT/Year 0.45 MT 5
76
5 Effluent Treatment Plant With
In house Evaporation 4.20 KLD 4.20 KLD 40
6
Utility Area - TFH 60
211 Fly ash - 45 MT 50
Fuel Storage Area (5 Day 1.5 7.5 20
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 168 of 357
inventory) MT/Day MT/Day
7 Process Waste Storage (2
Week inventory)
68.16
MT/Year
2.84
MT/Month 50 60
8 Manufacturing Area for API 95
MT/Month - - 650.0
9 Manufacturing Area for Existing
Product
57.7
MT/Month - - 400
1
0
Raw material storage for
Existing Product - 30 MT 40 50
1
1
Finish Good Storage for
Existing Product - 28.85 MT 40 50
1
2 Admin Office - - - 36
1
3 Occupation Health center - - - 36
B-3 Green belt area
Existing Proposed
(Sq. meter)
Total
(Sq. meter)
Area in Sq.
meter 150 1929 2079
% of total
area 2.38 30.62 33.00
C Employment generation
Existing Proposed Total
5 10 15
D WATER
D-1
Source of Water Supply
(GIDC, Bore well, Surface water, Tanker supply etc...)
Own Bore well
Status of permission from the concern authority.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 169 of 357
D-2 Water consumption (KLD)
Sr No
Category Water Consumption KLD Remark
Existing Additional Total
1. Domestic Purpose 0.5 2.5 3.0
2. Gardening - 2.5 2.5 Reuse
From STP
3.
INDUSTRIAL
Process 1.28 2.5 3.78
Boiler NIL NIL NIL
Cooling 0.1 - 0.1
Washing NIL 0.5 0.5
Total water Consumption (Domestic)
0.5 2.5 3.0
Total water Consumption (Industrial )
1.38 3.0 4.38
Brief Note on worst case scenario for water consumption:
Sr. No
Name of Product KL Per MT of Product KL Per Day
Water Consumption Water
Consumption
1. Pregabline 4.66 1.864
2. Piprazine citrate 0.2 0.12
3. Piprazinehexahydrate 0.55 0.22
4. Piprazineadipate 0.2 0.12
5. Piprazinedihydrochloride 0 0
6. Piprazinephospate 0.3 0.18
7. Povidone iodine 0 0
Total 2.504
-
Summary of water
requirement
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
Total water requirement
for the project (A) 1.88 8.0 9.88
Quantity to be recycled
(B) - 2.5 2.5
Total fresh water
requirement I 1.88 5.5 7.38
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Ensure Total water requirement = Fresh water + Recycled water
i.e. A = B + C
Reuse/Recycle details (2.5 KLD) with feasibility.
[Source of reuse & application area]
Source of
waste water for
reuse in KLD
(From where it is
coming)
Application
area with
quantity in
KLD (Where it is
used)
Characteristics of
waste water to be
reused (COD, BOD, TDS
etc.)
Remarks
regarding
feasibility
to reuse
Domestic 2.5
KLD
Gardening 2.5
KLD
pH 7-8
TDS < 200
COD < 10
In case of no reuse/recycle of waste water, Give brief note on justification as
why no reuse/recycle.
Total industrial 4.20 KLD Waste water generation from manufacturing Process
and other ancillary Operation, which is treated in Effluent Treatment plant and
then after Discharge though In house Evaporation.
D-3 Waste water generation (KLD)
Sr No
Category
Waste Water Generation KLD
Remark Existing
Proposed
Total
1. Domestic Purpose 0.4 2.1 2.5 Send to
STP
2.
INDUSTRIAL
Process NIL 3.65 3.65
Boiler NIL NIL NIL
Cooling NIL 0.05 0.05
Washing NIL 0.5 0.50
Total wastewater Generation (Domestic)
0.4 2.1 2.5 Send to
STP
Total wastewater generation (Industrial )
- 4.20 4.20
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative):
Sr. No
Name of Product
KL Per MT of Product KL Per Day
Waste Water Generation Waste Water Generation
1. Pregabline 4.63 1.852
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2. Piprazine citrate 0.62 0.372
3. Piprazinehexahydrate 0.3 0.12
4. Piprazineadipate 0.66 0.396
5. Piprazinedihydrochloride 0.9 0.54
6. Piprazinephospate 0.6 0.36
7. Povidone iodine 0 0
Total 3.64
Brief justification in case of no process effluent generation or no industrial effluent
generation or no high concentration effluent generation from proposed project (Whichever is
applicable).
➢ Not applicable
D-4 Mode of Disposal & Final meeting point (Existing and Proposed)
Existing and Proposed
Domestic: Domestic sewage 2.5 KLD generated will be Reuse in Gardening and
Plantation After treatment in STP Plant.
Industrial: Total industrial 4.20 KLD Waste water generation from manufacturing
Process and other ancillary Operation, which is treated in Effluent Treatment
plant and then after Discharge though In house Evaporation
-
Clearly mention about final disposal
In house evaporator
D-5 Treatment facilities
For Domestic waste water:
Capacity of STP: 2.5
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream
segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
Sr. No. Name of Unit Capacity
1. Effluent collection tank 5.0
2. Neutralization Tank 3.0
3. Primary Settling tank 2.0
4. Treated Effluent Collection tank 5.0
5. Solvent stripper -
6. Evaporate -
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Sr No Parameter Unit Process Washing Cooling bleed off
Combine
1. pH pH Scale 4-5 7-8 7-8 4-5
2. T.D.S. mg/l 4000-5000 1500-2000 1500-2000 4000-5000
3. C.O.D mg/l 2000-4500 1200-1500 400-500 2000-4500
Sr No Parameter Unit ETP inlet After primary treatment
Evaporate
1. pH pH Scale 4-5 7-8 7-8
2. T.D.S. mg/l 4000-5000 5000-6000 5000-6000
3. C.O.D mg/l 2000-4500 1800-2000 1800-2000
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and
Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ Total industrial 4.20 KLD Waste water generation from manufacturing Process and other
ancillary Operation, which is treated in Effluent Treatment plant and then after Discharge
though In house Evaporation.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
➢ Total industrial 4.20 KLD Waste water generation from manufacturing Process and other
ancillary Operation, which is treated in Effluent Treatment plant and then after Discharge
though In house Evaporation
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility (CF) (For waste water treatment)
➢ Not Applicable
Membership of Common facility (CF) mentioning total capacity, consented quantity,
occupied capacity and spare capacity and norms of acceptance of effluent from
member unitsin-line with the direction given by GPCB vide Letter No. GPCB/P-
1/8-G (5)/550706 dated 08/01/2020.
➢ Not Applicable
D-7 Simplified water balance diagram with reuse / recycle of waste water (Existing
and Proposed)
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Page 173 of 357
Existing Water Balance
After Expansion Water Balance
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario
thereof:
Total Water Consumption
1.88 KLD
Domestic
0.5 KLD
Sewage
0.4 KLD
Soak Pit
Industrial
1.38 KLD
Process
1.28 KLD
NIL
Cooling
0.1 KLD
NIL
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 174 of 357
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC’s
OM vide dated 31.10.2019)
Existing & Proposed
Sr.
no
Stack
attached to
Stack
height
and dia
Fuel Consumpt
ion
APCM Types of
Emission
Remark
1 Steam boiler
(500
kg/hr)(will be
dismantle
after getting
EC NOC
from GPCB)
15.0 m Fire
wood
(remove)
0.7
MT/day
(remove)
Multi
Cyclone
separator
PM
SOx
NOX
Existing
(will be
dismantle
after getting
EC NOC
from
GPCB)
2 Thermic fluid
heater (2 lac
kcal/hr)
15.0 m Agro
waste
(Propose
d)
1.5
MT/day
(Proposed)
Multi
Cyclone
separator
PM
SOx
NOX
Proposed
E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
Existing & Proposed
There is no process gas emission
Note:
➢ Details of gaseous raw materials used in proposed project
➢ Estimation of process gas emission (Product wise and Total)
➢ Requirement of the scrubbing media (KL per Day) considering solubility (Product wise
and Total)
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its
sound management in HW matrix.
E-4 Fugitive emission details with its mitigation measures.
➢ The entire manufacturing activities will be carried out in the closed reactors and regular checking and maintenance of reactors will be carried out to avoid any leakages.
➢ The tank vents will be equipped with either a carbon filter or an oil trap to prevent water vapour from entering the tank as it breathes.
➢ All the motors of pumps for the handling of hazardous chemicals will be flame
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 175 of 357
proof and provided with suitable mechanical seal with stand-by arrangement ➢ Control of all parameters on a continuous basis will be done by adequate
control valves, pressure release valves and safety valves etc. ➢ All the flange joints of the pipe lines will be covered with flange guards. ➢ All the raw materials will be stored in isolated storage area and containers
tightly closed. ➢ There will also be provision of adequate ventilation system in process plant and
hazardous chemical storage area.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9
permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance
and calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Existing & Proposed
Sr. No
Types of Hazardous
Waste Sources
Category
Propose MT/Year
Disposal Existing Proposed Total
1. ETP
Sludge ETP area 35.3 NIL 1.8 1.8
Collection, Storage,
transportation and disposal at any registered
TSDF site
2. Used Oil Plant
Machinery 5.1 NIL 0.02 0.02
Collection, Storage,
Transportation, sell to MoEFCC
approved recyclers OR Reused as
Lubricant within premises
3. Discarded Container/
Liner
Material Storage and
Handling 33.3 2.4 2.6 5.0
Collection, storage,
Transportation and Dispose to
Registered
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 176 of 357
Recycler
4. Solvent residue
Distillation Unit
26.3 NIL 0.8 0.8
Collection, Storage,
Transportation and disposal by co processing or
by disposal to CHWIF
5. Spent solvent
Permrthrine, pregabline
26.4 NIL 40 40
Recovered, storage and reused in the next batch of same product
after Distillation
6. Sodium Chloride
Benzyl acetate, Benzyl
benzoate, Permithrine, Pregabline
28.4 NIL 45.6 45.6
Collection, Storage,
Transportation, sell to Authorized
Party having permission of
Rule -9
7. Sodium Sulfate
Pregabline 28.4 NIL 22.56 22.56
Collection, Storage,
Transportation, sell to Authorized
Party having permission of
Rule -9
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
We have membership of TSDF
Details of Membership letter no. & Date with spare capacity of the Common Facility.
➢ Not Applicable
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
Existing Proposed Total
1 NA NA NA NA NA NA
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 177 of 357
recovered Solvents etc.
Sr. No
Name of Product
Solvent
Total Solvent Quantity
Recover of Solvent
Loss of Solvent
% of recovery
% of Losses
1.0 PREGABLINE N- Butanol 2.66 2.60 0.06 97.75 2.25
G-2 Brief Note on LDAR proposed:
➢ The entire manufacturing activities & distillation process will be carried out in totally closed system.
➢ Regular maintenance of the pipeline and valves & fittings will be carried out regularly to avoid any leakages.
➢ Distillation column will be connected with condenser where cooling water will be used as media and also equipped with vacuum system.
➢ The condenser will be provided with the sufficient HTA and residence time to achieve more than 98% recovery.
➢ During the manufacturing activity as well as during distillation process 2% of the total solvent
will be lost; approx. 98 % of solvent will be recovered during the process. The fresh solvent
requirement will depend on solvent loss during distillation as well as manufacturing activity.
G-3 VOC emission sources and its mitigation measures
• Sources of fugitive emissions include storage of chemicals, solvents storage, loading and unloading section, raw material handling and, hazardous waste storage area
Measures :
• The fugitive emissions in terms of handling losses will get reduced by proper storage and handling.
• Hazardous chemicals will be stored as per standard criteria.
• Periodically monitoring will be carried out as per the post project monitoring plan.
• Proper ventilation in storage & production area shall be ensured
• All materials must be stored in suitable packing to prevent contamination of air.
• Enclosed system & efficient procedures for materials charging shall be ensured.
• Procedures for start-up shut down, operation & maintenance procedures shall be established & maintained.
The coverage of greenbelt around the plant also acts as natural barrier to stop carrying of dust along with the wind current.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
-
There is no storage Tank
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 178 of 357
Sr
N
o
Name
of
Raw
Materi
al
Stat
e
Storag
e
Capaci
ty
Numb
er of
drum/
Cylind
er
Stora
ge at
time
(KL)
ID
L
H
p
p
m
Boil
ing
Poi
nt
°C
Fl
as
h
Po
int
°C
Hazard
characteris
tic
Fire
extinguis
her Type
2
N-
Butan
ol
Liqui
d 3 KL 1 3
N
A
117.
6 35 Flammable
CO2, Dry
Chemical
or Foam
Brief note on storage of Hazardous chemicals in Tanks
➢ The Entire plant will be operated by PLC based SCADA System and semi automization
➢ The 200 KL water will be spare for firefighting system equipped with Jockey Pump and
Diesel Pump
➢ Appropriate and adequate size of dyke wall will be provided for each tank separately
➢ The entire plant will having flame proof feeting with earthing arrangement
➢ Receiver tank is provided for each chemicals to minimize the risk
➢ Fire Hydrant and Sprinkler System will be provided in tank farm and at dedicated area to
scrub the material in case of leakage
➢ Solvent Storage Area will be on Ground Floor only
➢ Tanks Equipped with Pressure Release Valve and NRV
➢ Loading and Unloading in supervision of trained Staff as per SOP
➢ Solvent Storage area will be equipped with B Type and DCP Type and CO2 Type Fire
Extinguishers
➢ No Manual Handling and handling only with Fixed Pipe line
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys,
Bags etc.
➢ Sodium Carbonate ➢ Sodium Acetate ➢ H2SO4
Safety details of Hazardous Chemicals:
Type of Safety measures
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 179 of 357
Hazardous
Chemicals
N-Butanol • The charging of material will be carried out by PLC based SCADA System semi automization
• Tank, valve, pipeline are checked and maintain, in good condition through preventive maintenance
• Joints are checked regularly to detect any Leakage. • ISI Portable fire extinguisher & Fire Hydrant line is provided as
per TAC norms. • Flame proof electrical fittings / installation provided. • Proper Earthing, Bonding & flange-to-flange jump ring is
provided. • Flame arrester provided on vent line. • CCE approved Separate Storage area with door having locking
arrangement. • Auto & manual sprinkler provided. • Spark arrester are installed on all vehicles inside the premises. • Apron, Hand gloves, gumboot, goggles and helmet provided. • Train operator employed. • Eye washer & shower provided. • Good ventilation in the area. • Flame arrester with breather valve. • Perforated dip pipe in dyke wall will be provided to monitor &
detect any leakage from tank. • Sump will be made under dyke to recover leakage material from
dyke. • Drum storage will be kept under RCC dyke.
• Applicability of PESO : Not Applicable
H-2 Types of hazardous Processes involved and its safety
measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic
Reaction etc.)
-
Type of
Process
Safety measures including Automation
NO NO
H-3 Details of Fire Load Calculation
-
Total Plot Area: 6300
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Area utilized for plant activity: 2438
Area utilized for Hazardous Chemicals Storage: 149
Number of Floors: GF
Water requirement for firefighting in KL : 162.66 KL
Water storage tank provided for firefighting in KL: 200 KL
Details of Hydrant Pumps: 6.0 Inch Diameter fire hydrant line will be provided connected to Jockey Pump Followed by Diesel Pump having 07 bar pressure with sprinkler system. The jockey pump is placed with the fire water tank having capacity of 200 KL.
Nearest Fire Station : Halol GIDC fire station With 13.20 KM distance
Applicability of Off Site Emergency Plan: NA
-
H-4 Details of Fire NOC/Certificate:
We will obtained after getting NOC from GPCB
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 15
Number of Contractual person/Labour : 20
Area provided for OHC: 36.0 Sq. m
Number of First Aid Boxes : At least one box containing such items and placed
and maintained in accordance with the requirements
of Sec. 45 is separately provided.
Nearest General Hospital : General Hospital Halol @ 17.83 Km
Name of Antidotes to be store in plant : Injection -morphia, pethidins, atropins, adrenaline,
coramine, novocanAntidotes: Fomepizole, formic
acid
• Committee discussed regarding :
✓ Revised product list submitted was discussed. PP has removed 4 nos of product
from their product list.
✓ Plot area is 6300 sq mts.
✓ PP will dismantle boiler and has proposed to install Thermic fluid heater .Stack
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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height mentioned is 15 mts. As fuel used is Agro waste so PP was asked to increase
the height of stack to 30 mts.
✓ EMP was discussed and PP was asked to revise the EMP budget considering fire
and safety budget allocation.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. PP shall comply conditions of any subsequent amendment or expansion or change in
product mix, after the 30th September 2020, considered as per the provisions in force at that
time as mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020.
2. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients
(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any
subsequent amendments.
3. PP shall submit six monthly compliance report of Environmental Clearance without fail and
the same shall be critically assessed by the regulatory authority.
4. Close loop solvent recovery system with adequate condenser system shall be provided to
recover solvent vapours in such a manner that recovery shall be maximum and recovered
solvent shall be reused in the process within premises.
5. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the
CPCB guidelines. LDAR Logbooks shall be maintained
WATER
6. Total water requirement for the project shall not exceed 9.88 KLD. Unit shall reuse 2.5KLD
of treated industrial effluent within premises. Hence, fresh water requirement shall not
exceed 7.38 KLD and it shall be met through borewell only.
7. PP shall obtain CGWA permission for ground water source i.e. bore well within premises
before start production activity.
8. The industrial effluent generation from the project shall not exceed 2.5 KLD.
9. Waste water generation from manufacturing Process and other ancillary Operation, which is
treated in Effluent Treatment plant and then after Discharge though In house Evaporation.
10. PP shall maintain Complete Zero Liquid Discharge [ZLD] status all the time and there shall
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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be no drainage connection from the premises and no wastewater discharge outside
premises by any means.
11. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
12. Unit shall feed wastewater to in-house MEE only after ensuring content of effluent for
COD/VOC so as not to get air borne during evaporation in order to achieve no adverse
impacts on Environment and Human Health.
13. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during any shut down of in-house MEE.
14. Domestic wastewater generation shall not exceed 2.5 KL/day for proposed project and it
shall be treated in STP. Treated sewage shall be utilized for gardening and plantation
purpose within premises after achieving on-land discharge norms prescribed by the GPCB.
15. During monsoon season when treated sewage may not be required for the plantation /
Gardening / Green belt purpose, it shall be stored within premises. There shall be no
discharge of waste water outside the premises in any case.
16. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
17. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
18. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned in
flue gas matrix.
19. Unit shall provide APCM and stack height as mentioned in process gas matrix.
20. PP shall use approved fuels only as fuel in boilers.
HAZARDOUS & SOLID WASTE
21. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
22. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
23. The PP shall develop green belt within premises (2079 Sq. m i.e. 33 % of the total plot area)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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as per the undertaking submitted before SEAC. Green belt shall be developed with native
plant species that are significant and used for the pollution abatement as per the CPCB
guidelines. It shall be implemented within 3 years of operation phase in consultation with
GPCB.
24. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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8 SIA/GJ/IND2/190249/2
020
VRS LAB
PLOT NO - 621-P/39, GIDC INDUSTRIAL
ESTATE, PANOLI Anklesvar, Bharuch
EC
Reconsi
deration
Category of the unit: 5(f)
Project status: New
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/190249/2020 on
dated 24.09.2020 for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is a new project proposed for manufacturing of synthetic organic chemicals [API and
API Intermediates] as tabulated below.
Sr. No.
Name of Product CAS NO. Quantity (MT/Month
)
End Use
1 Benzhydryl Piperazine 841-77-0
50.0
Intermediate of Cinnarizine
2 Para Chloro Benzophenone 134-85-0 Intermediate of Levocetirizine
3 Para Chloro Benzhydryl Piperazine
303-26-4 Intermediate of Cetirizine
4 10-Methoxy Iminostibene 4698-11-7 Intermediate of Oxcarbazepine
5 4-Amino-1,2,4 –Triazole 584-13-4 Intermediate of Fluconazole
6 2,4-Difluoro-Alpha-(1H-1,2,4-Triazole) Acetophenone
86404-63-9 Intermediate of Fluconazole
7 Chlorohexidine Base 55-56-1 disinfectant and topical anti-infective agent
8 Favipiravir 259793-96-9
antiviral drugs
9 Umifenovir 131707-23-8
Used in the finished formulation to treat mild to moderate COVID-19 cases
10 Amoxicillin Trihydrate 61336-70-7 Anti Biotic
11 Doxycyline 564-25-0 Anti Biotic
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7 -(2,2-Dimethoxyethyl) T heophylline
52943-53-0 Intermediate of Doxycyline
12 Levofloxacin 100986-85-4
Antibiotic
Ethyl 3-[[(1S)-2-hydroxy-1-methylethyl]amino]-2-(2,3,4,5-tetrafluorobenzoyl) prop-2-enoate
N/A
Intermediate of Levofloxacin (3S)-9,10-difluoro-3-methyl-7-oxo-
2,3-dihydro-7H-[1,4] oxazino [2,3,4-ij]quinoline-6-carboxylic acid
82419-35-0
13 Gabapentin 60142-96-3 Anticonvulsant
2-Azaspiro[4.5]decan-3-one 64744-50-9 Intermediate of Gabapentin
1,1-Cyclohexanediacetic acid monoamide
99189-60-3
14 Azithromycin 83905-01-5 Anti Biotic
15 Ciprofloxacin 85721-33-1 Anti Biotic
16 Ofloxacin 82419-36-1 Anti Biotic
17 Diclofenac Sodium 15307-79-6 Anti Flammatory
(2,6-Dichloro Phenylamine) 15307-93-4
Intermediate of Diclofenac Sodium
(N-Chloroacetyl, 2,6-Dichloro Phenylamine)
15308-01-7
(1-(2,6 -Dichlorophenyl) 2-Indolinone)
15362-40-0
18 Clarithromycin 81103-11-9 Anti Biotic
Erythromycin oxime 13127-18-9 Intermediate of Clarithromycin
19 Paracetamol 103-90-2 painkiller
20 Oxcarbazepine 28721-07-5 Anticonvulsants
10-Methoxy Carbezapine 28721-09-7 Intermediate of Oxcarbazepine
21 Metformin 657-24-9 Used to control high blood sugar
22 Losratan 114798-26-4
Antihypertensive
4’-Bromomethyl-biphenyl-2-carbonitrile
114772-54-2
Intermediate of Losratan
2-butyl-4-chloro-5-formylimidazole 83857-96-9
4’-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile
11477-55-3
2-Butyl-5-chloro-3-[2’(2H-tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde
114798-36-6
23 Olemesartan 144689-63-4
Used to treat high blood pressure
[Ethyl-4-(1-Hydroxy-1-methylethyl)-2-propyl-1-{4-[2-trityltetrazole-5-yl)phenyl} methylimidazole-5-carboxylate]
144690-92-6
Intermediate of Olemesartan
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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24 Ornidazole 16773-42-5 Antibiotic
25 Lopinavir 192725-17-0
Used to control HIV infection
26 Levocetirizine
130018-77-8
Antihistamine
(4-chlorphenyl)phenyl methyl amine hydrochloride
410077-96-2
Intermediate of Levocetirizine
(4-chlorphenyl)phenyl methyl amine
28022-43-7
1-Methanesulphonyl-4methyleneznene (2-chloroehtyl)-chloromethyl amine
N/A
1-[((4-chlorphenyl)phenyl- methyl]-4-(toluene-4-sulfonyl)-piperazine
163837-56-7
1-(4-[((4-chloorphenyl)phenyl- methyl]- piperazine-1-yl)-ethanol
164726-80-1
27 Montelukast Sodium 151767-02-1
Used to control and prevent symptoms caused by asthma
28 R&D -- 0.1
TOTAL 50.1
Specific End-use of each proposed products:
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category
of Product (API/
Intermediate)
Stage of
Intermediate
n-1, n-2, etc
Name of API in which
Intermediate Used/
End use of said
Intermediate
CAS No. (API)
Said API is used
for/End Use of said
API
1 Benzhydryl Piperazine
841-77-0 Intermediate
(n-2) Intermediate of Cinnarizine
298-57-7 Antihistamine
2 Para Chloro Benzophenone
134-85-0 Intermediate
(n-2) Intermediate of Levocetirizine
130018-77-8
Antihistamine
3 Para Chloro Benzhydryl Piperazine
303-26-4 Intermediate
(n-2) Intermediate of Cetirizine
83881-51-0
Antihistamine
4 10-Methoxy Iminostibene
4698-11-7 Intermediate
(n-1) Intermediate of Oxcarbazep
28721-07-5
Anticonvulsants
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 187 of 357
ine
5 4-Amino-1,2,4 –Triazole
584-13-4 Intermediate
(n-3) Intermediate of Fluconazole
86386-73-4
Anti fungal
6 2,4-Difluoro-Alpha-(1H-1,2,4-Triazole) Acetophenone
86404-63-9 Intermediate
(n-1) Intermediate of Fluconazole
86386-73-4
Anti fungal
7 Chlorohexidine Base
55-56-1 API -- -- -- disinfectant and topical anti-infective agent
8 Favipiravir 259793-96-9
API -- -- -- antiviral drugs
9 Umifenovir 131707-23-8
API -- -- -- Used in the finished formulation to treat mild to moderate COVID-19 cases
10
Amoxicillin Trihydrate
61336-70-7 API -- -- -- Anti Biotic
11
Doxycyline 564-25-0 API -- -- -- Anti Biotic
7 -(2,2-Dimethoxyethyl) T heophylline
52943-53-0 Intermediate
(1-n ) Intermediate of Doxycyline
564-25-0 Anti Biotic
12
Levofloxacin 100986-85-4
API -- -- -- Anti Biotic
Ethyl 3-[[(1S)-2-hydroxy-1-methylethyl]amino]-2-(2,3,4,5-tetrafluorobenzoyl) prop-2-enoate
N/A Intermediate (2-n )
Intermediate of Levofloxacin
100986-85-4
Anti Biotic
(3S)-9,10-difluoro-3-methyl-7-oxo-2,3-dihydro-7H-[1,4] oxazino [2,3,4-ij]quinoline-6-carboxylic acid
82419-35-0 Intermediate (1-n )
Intermediate of Levofloxacin
100986-85-4
Anti Biotic
1 Gabapentin 60142-96-3 API -- -- -- Anticonvul
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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3 sant
2-Azaspiro [4.5]decan-3-one
64744-50-9 Intermediate (n-3)
Intermediate of Gabapentin
60142-96-3
Anticonvulsant
1,1-Cyclohexanediacetic acid monoamide
99189-60-3 Intermediate (n-2)
Intermediate of Gabapentin
60142-96-3
Anticonvulsant
14
Azithromycin 83905-01-5 API -- -- -- Anti Biotic
15
Ciprofloxacin 85721-33-1 API -- -- -- Anti Biotic
16
Ofloxacin 82419-36-1 API -- -- -- Anti Biotic
17
Diclofenac Sodium
15307-79-6 API -- -- -- Anti Flammatory
(2,6-DICHLORO PHENYLAMINE)
15307-93-4 Intermediate
(n-4) Intermediate of Diclofenac Sodium
15307-79-6
Anti Flammatory
(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)
15308-01-7 Intermediate
(n-3) Intermediate of Diclofenac Sodium
15307-79-6
Anti Flammatory
(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)
15362-40-0 Intermediate
(n-2) Intermediate of Diclofenac Sodium
15307-79-6
Anti Flammatory
18
Clarithromycin 81103-11-9 API -- -- -- Anti Biotic
Erythromycin oxime
13127-18-9 Intermediate
Intermediate of Clarithromycin
81103-11-9
Anti Biotic
19
Paracetamol 103-90-2 API -- -- -- painkiller
20
Oxcarbazepine 28721-07-5 API -- -- -- Anticonvulsants
10-Methoxy Carbezapine
28721-09-7 Intermediate
(n-2) Intermediate of Oxcarbazepine
28721-07-5
Anticonvulsants
21
Metformin 657-24-9 API -- -- -- Used to control
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high blood sugar
22
Losratan 114798-26-4
API -- -- -- Antihypertensive
4’-Bromomethyl-biphenyl-2-carbonitrile
114772-54-2
Intermediate
(n-4) Intermediate of Losratan
114798-26-4
Antihypertensive
2-butyl-4-chloro-5-formylimidazole
83857-96-9 Intermediate
(n-3) Intermediate of Losratan
114798-26-4
Antihypertensive
4’-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile
11477-55-3 Intermediate
(n-3) Intermediate of Losratan
114798-26-4
Antihypertensive
2-Butyl-5-chloro-3-[2’(2H-tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde
114798-36-6
Intermediate
(n-2) Intermediate of Losratan
114798-26-4
Antihypertensive
23
Olemesartan 144689-63-4
API -- -- -- Used to treat high blood pressure
[Ethyl-4-(1-Hydroxy-1-methylethyl)-2-propyl-1-{4-[2-trityltetrazole-5-yl)phenyl} methylimidazole-5-carboxylate]
144690-92-6
Intermediate
(n-2) Intermediate of Olemesartan
144689-63-4
Used to treat high blood pressure
24
Ornidazole 16773-42-5 API -- -- -- Antibiotic
25
Lopinavir 192725-17-0
API -- -- -- Used to control HIV infection
26
Levocetirizine 130018-77-8
API -- -- -- Antihistamine
1-Methanesulphonyl-4methylenezne
N/A Intermediate
(n-4) Intermediate of Levocetirizine
130018-77-8
Antihistamine
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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ne (2-chloroehtyl)-chloromethyl amine
1-[((4-chlorphenyl)phenyl- methyl]-4-(toluene-4-sulfonyl)-piperazine
163837-56-7
Intermediate
(n-3) Intermediate of Levocetirizine
130018-77-8
Antihistamine
1-(4-[((4-chloorphenyl)phenyl- methyl]- piperazine-1-yl)-ethanol
164726-80-1
Intermediate
(n-2) Intermediate of Levocetirizine
130018-77-8
Antihistamine
27
Montelukast Sodium
151767-02-1
API -- -- -- Used to control and prevent symptoms caused by asthma
• During the meeting dated 15.04.2021, Project proponent (PP) and their Technical Expert
from M/s. Ozone Enviro Tech remained present during video conference meeting.
• The technical expert informed the Committee that their application for sub-plotting is yet to
be approved by GIDC.
• After deliberation, SEAC unanimously decided to defer the proposal and consider the same in one of the upcoming meeting of SEAC upon submission of approval of GIDC in the matter of sub-plotting.
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Ozone Enviro Tech remained
present during video conference meeting.
• Revised Salient features of the project submitted as under:
Sr. no. Particulars Details
A-1 Total cost of Proposed Project (Rs. in Crores):
3.5 Crores
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 191 of 357
Break-up of proposed project Cost:
Sr. No.
Particulars Estimated Cost
(INR In Lakhs)
1 Land and Site Development 80
2 Building 70
3 Plant and Machineries 125
4 Environment protection measures (includes cost of ETP, Tree Plantation, etc.)
75
Total 350
A-2 Details of Environmental Management Plan (EMP) As below:
Details of EMP
Sr. No
Unit Installed Capacity
(KLD)
Capital Cost (Rs. In Lakhs )
Operating Cost
(Lacs/Year)
Maintenance Cost
(Lacs/Year)
Total Recurring
Cost (Lacs/Year)
1 Waste Water ETP (Primary) 20.0 KLD
11.0 212.97 -- 212.97
2 Air 25.5 -- 3.40 3.40
3 Hazardous Management
6.0 86.73 -- 86.73
4 Fire & Safety 15.0 -- 3.20 3.20
5 AWH Monitoring
1.0 -- 1.00 1.00
6. Green Belt Development
2.10 -- 1.80 1.80
7. Occupational Health
1.00 -- 1.85 1.85
8. CER Year 2021-
2023 14.00
Total 75.60 299.70 11.25 310.75
Summary
Cost of Project in Crores per Annum: 3.5 Cr.
EMP Capital Cost in Crores per Annum and Percentage: 0.75 Cr. (21.42 %)
EMP Recurring Cost in Crores per Annum and Percentage: 3.10 Cr
--
A-3 Details of CER as per OM dated 01/05/2018 As below:
As per OM no. 22-65/2017 on dated 01/05/2018 regarding “Corporate Environment Responsibility”
(CER), Greenfield projects have to contribute 2% (Rs. 7.0 Lack) of the Capital Investment (3.5 Cr).
But as per New Mechanism of CPCB vide letter no CPCB/IPC-VII/CEPI/NGT/2019 on dated
25/10/2019, we shall commit to do 4% (Rs. 14 Lack) of Project Cost as a CER. Our CER activity are
as below table…
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Component As per Norms Allocation
CER Rs. 7.0 Lakhs (2 %) Rs. 14 Lakhs (4 %)
Activities to be carried out under CER:
CER Activities Fund (Rs.)
2021-2022
Provided Solar street light set with battery backup (18W -14 Nos.) in Kharod Village
4,00,000/-
2022-2023
Company will construct 1,00,000/- Liter RCC collection tank with filtration facility for rain water harvesting in Kharod village
10,00,000/-
TOTAL 14,00,000 /-
-
B Land / Plot ownership details:
B-1 Total Plot area ( sq. meter) 1787.50 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Sr. No.
Description Sq. Meter
1 Production Area 80
2 Raw Material Storage Area 200
3 Finish Product Storage Area 30
4 Haz. Waste Storage Area 100
5 Boiler Area 100
6 ETP 50
7 Admin Building & OHC Room 40
8 Green Belt Area (40%) 715
9 Gas Storage Area 20
10 Road & Open Area 442.5
11 Security Cabin 10
TOTAL 1787.50
--
B-3 Green belt area ( sq. meter)
715 Sq. m. (40% of total area)
C Employment generation 25
D Water
D-1
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Water Supply
Status of permission from the concern authority.
D-2 Water consumption (KLD)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 193 of 357
Category Quantity
KLD Remarks
(J) Domestic 2.0
(K) Gardening 2.0
(L) Industrial
Process 15.0
Washing 2.0
Boiler 8.0
Cooling 5.0
Others (Scrubber) 2.7
R&D 0.3
Industrial Total 33.0
Total (A + B + C)
37.0
--
Brief Note on worst case scenario for water consumption: Worst case scenario for water consumption are Product No. 20 (15.0 KLD)
Summary of water requirement Quantity
KLD Remarks
Total water requirement for the project (A) 37
Quantity to be recycled (B) 11.9
Total fresh water requirement (C) 25.1
Ensure Total water requirement = Fresh water + Recycled water
(37.0 = 25.1 + 11.9)
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]
Source of waste water for reuse in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
1.5 KLD Domestic effluent
Gardening Purposed
BOD-30 --
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. --
D-3 Waste water generation (KLD)
Category Waste water
KLD Remarks
(G) Domestic 1.5
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(H) Industrial
Process 16.2
Washing 2.0
Boiler 0.8
Cooling 0.5
Others (Scrubber) 3.06
R&D 0.3
Total Industrial waste water
22.78
Total [A + B] 24.28
-
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative): Worst case scenario for water consumption are Product No. 20 (16.12 KLD)
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (If any applicable to proposal).
➢ Not Applicable
D-4 Mode of Disposal & Final meeting point
Domestic: 1.5 KL/Day Domestic waste water will be sent to Septic Tank & Soak Pit.
Industrial: 19.72 KLD Effluent from process and utility will be treated into primary ETP and primary treated effluent send to common MEE for the final treatment and disposal. 3.06 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9 Permission.
-
D-5 Treatment facility within premises with capacity
For Domestic waste water: Capacity of STP: STP is not provided because domestic effluents send to low COD steam ETP.
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ➢ ETP (Primary ) : 20 KLD
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.)
Sr. No.
Parameter
Characteristics(mg/L)
Primary treated Process
Boiler blow down
Cooling Tower blow down
Washing Compo
site
1 pH 3-9 8 - 8.5 8 - 8.5 5.5 - 8.5 3-9 6.5-7.5
2 TDS 28000 350 250 1000 28000 28700
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3 TSS 500 250 350 200 500 75
4 COD 20000 70 100 600 20000 13000
5 BOD3 700 20 30 200 700 490
--
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ Not Applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Industrial:- 19.72 KLD Effluent from process and utility will be treated into primary ETP and primary
treated effluent send to common MEE for the final treatment and disposal. 3.06 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9 Permission.
Domestic:- 1.5 KLD domestic effluent will be sent to STP and reused for gardening purposed.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.Name of Common facility (CF) (For waste water treatment)
➢ Common MEE of M/s BEIL, Ankleshwer
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
➢ Common MEE of M/s BEIL, Ankleshwer
D-7 Simplified water balance diagram with reuse / recycle of waste water
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E Air
E-1 Brief Note on fuel based heat energy requirement and worst case scenario thereof:
SR. NO. NAME OF FUEL QUANTITY
1. Briquette of Bio Coal 8 MT/Day
2. HSD 30 Lit/hr
Power Requirements: Proposed: Power required from DGVCL is 250 KVA. Standby power supply from D.G. set (125 KVA) in emergency case. --
E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC’s OM vide dated 31.10.2019)
-
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions i.e.
Air Pollutant
s
Air Pollution Control
Measures (APCM)
1 Boiler
(Capacity: 1.5 TPH)
30
9.1 Bri
que
tte
of
Bio
Co
al
9.2 5
M
T/
D
ay
PM SO2 NOx
9.3 Multicycl
one
Separato
r With
Bag
Filter
2
Thermic fluid heater
(Capacity: 2 Lakh Kcal/ Hr)
9.4 Bri
que
tte
of
Bio
Co
al
3 MT/Day
9.5 Multicycl
one
Separato
r With
Bag
Filter
3 D. G. Set (125
KVA) 11
9.6 HS
D
9.7 30
9.8 Lit
er
/h
r
9.9 Adequat
e Stack
Height
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-
E-3 Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx
etc.)
-
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emission
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
1 Process Vent -1 Product No. 2&4
HCl Cl2
11 Two Stage Scrubber
(Water + Alkali)
2 Process Vent -1 Product No. 4
Br2 11 Two Stage Alkali
Scrubber
3 Process Vent -2 (Ammonification) Product No. 24
NH3 11 Two Stage Water
Scrubber
Note: ➢ Details of gaseous raw materials used in proposed project - Ammonia & Bromine are
used ➢ Estimation of process gas emission (Product wise and Total) - Worst case for
chlorination is product no- 2&4, for Bromination is product no-4, for Ammonification is product no-24
➢ Requirement of the scrubbing media (KL per Day) considering solubility (Product wise and Total)
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its sound management in HW matrix.
E-4 Fugitive emission details with its mitigation measures:
Following measures will be adopted to prevent and control fugitive emissions…
➢ Solid raw material charging will be done through closed system to avoid fugitive emissions. ➢ Airborne dust at all transfers operations/ points will be controlled either by spraying water or
providing enclosures. ➢ Adequate ventilation will be provided. ➢ Periodic monitoring of work area will be carried out to check the fugitive emission. ➢ Minimum number of flanges, joints and valves in pipelines. ➢ Regular inspection of floating roof seals and proper preventive maintenance of roofs and
seals for tanks. ➢ Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer
area will be collected through hoods and ducts by induced draft and controlled by scrubber/ dust collector / bad filter.
➢ Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
F Hazardous waste management matrix (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
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Note: ➢ Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Sr. no.
Type/Name of Hazardous waste
Specific Source of generation
(Name of the Activity,
Product etc.)
Category & Schedule as
per HW Rules.
Quantity (MT/
Annum)
Management of HW
1 ETP Sludge ETP SCH-I/35.3 50 Collection, Storage, Transportation and Disposal at common TSDF site.
2 Discarded Drums/Bags/ Liners
Raw Materials/ Products
SCH-I/33.1 30 Collection, Storage, Transportation, Decontamination & Sale to GPCB approved vendors/ reuse /send back to supplier.
3 Used/ Spent Oil
Machineries/Utility
SCH-I/5.1 1.0 Collection, Storage, Disposal by reuse in plant machinery as lubricant or transportation & Sale to GPCB registered re-processor.
4 Distillation Residue
Distillation SCH-I/20.3 184 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
5 Spent Solvent
Process SCH-I/28.6 7194 Collections, Storage, distillation and reuse in plant premises. Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
6 Spent Carbon Process (Product No
– 12)
SCH-I/28.3 40
7 Organic Residue
Process (Product No
– 18)
SCH-I/28.1 335 Collection, Storage, Transportation and sent for co-processing in cement
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industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
8 Inorganic Residue
Process (Product No
– 11)
SCH-I/28.1 61 Collection, Storage, Transportation and Disposal at common TSDF site.
9 Aluminium Chloride
Process (Product No.
6)
SCH-I/28.1 1800 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
10 Spent Sulphuric Acid
Process (Product No.
26)
SCH-I/28.1 399 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
11 Dilute HCl (30%)
Scrubber SCH- II / B 15
450 Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 1 – 1788 MT/Year)
12 Sodium Hypo Chloride (20-22%)
Scrubber SCH-I/28.1 50 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission
13 Sodium Bromide Solution (30%)
Scrubber SCH-I/28.1 573 Collection, Storage, & Sell to end user who is having Rule-9 Permission.
14 Liq. Ammonia (25%)
Scrubber SCH-II/B15 30 Collection, Storage and reuse in plant premises. (Requirement of Liq. Ammonia in Product No 10 - 156.24MT/Year)
15 Off Specification Products
From mfg. Process (Batch failure)
SCH-I/28.4 5 Collection, Storage, Transportation and sent for co-processing in cement industries (in case of non-operation of co-processing site) Disposal at common incineration site.
R&D
16 ETP Sludge ETP SCH-I/35.3 1.0 Collection, Storage, Transportation & disposal in TSDF.
17 Residue from Distillation/ Organic Process Waste
R&D SCH-I/28.1 2.0 Collection, Storage, Transportation & send to cement industries for co-processing or incineration in CHWIF.
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18 Discarded Drum
Raw Materials/Pro
ducts
SCH-I/33.1 10 Nos./Year
Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
19 Discarded Bags / Liner
Raw Materials/Pro
ducts
SCH-I/33.1 0.1 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
20 Off Specification Products
R&D SCH-I/28.4 0.5 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.
-
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Ankleshwar for Common TSDF & CHWIF
F-3 Details of Non-Hazardous waste & its disposal (MSW and others)
Not Applicable
G Solvent management, VOC emissions etc.
G-1 Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)
SOLVENT RECOVERY AFTER LDAR
Sr. No.
Type of Solvent
% Recovery
% Losses
Air Water Haz
1 Mehtylene Dichloride 96.2 0.96 1.89 0.95
2 Dimethyl formamide 96.3 0.97 1.81 0.92
3 Methanol 96.2 0.98 1.87 0.95
4 Toluene 96.6 0.77 1.78 0.85
5 N-Butanol 96.4 0.89 1.81 0.90
6 Ethyl acetate 96.2 0.97 1.88 0.95
7 IPA 96.3 0.93 1.85 0.92
Justification of Reuse of solvent
Name of Solvent Total
requirement MT/Month
Total quantity of solvent recovered MT/Month
Mehtylene Dichloride 321.75 309.56
Dimethyl formamide 126.58 121.95
Methanol 237.25 228.16
Toluene 316.00 305.33
N-Butanol 390.50 376.29
Ethyl acetate 912.50 877.89
IPA 250.00 240.73
--
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G-2 Brief Note on LDAR proposed:
➢ Company will be installed double mechanical seal and MSW Gaskets in solvent pipelines to prevent leakage from flanges
➢ Company will be reduced the joints and valves in pipelines. ➢ All the rotating equipment like pumps will be installed with double Mechanical Seals to arrest
any sort of emissions. ➢ Flanges will be sealed so less losses will be there. ➢ Down the Temperature of Cooling tower to 5 0C ➢ Chilled Brine at -10 0C will be used to trap any traces of Solvent which is slipped from
Secondary condenser. ➢ Closed loop system. ➢ For continue vapor travelling 100mm of Hg (slight vacuum) will be applied on secondary
condenser. --
G-3 VOC emission sources and its mitigation measures (Brief note on LDAR)
➢ Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.
➢ Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.
➢ To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps.
➢ Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with on-line pH meter with hooter system for better operational control.
➢ Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers.
➢ All the raw materials will be pneumatically transfer to the reactor. ➢ Emphasis will be given to solvent management/solvent loss prevention. ➢ Control by having proper scrubbing system. ➢ Condenser to trap VOC. ➢ Proper gland packing will be maintained for pumps and valves and to the extent possible
pumps with mechanical seal.
H Safety Detail
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
Storage details Name of major Hazardous chemicals
Remarks
Storage tanks (If any) --
Drums/Bags Acetone/ Liquid Ammonia/ MDC/ Hexane/ Acetonitrile/ THF/ Ethyl Acetate
Cylinder Ammonia
Bottle Bromine
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
➢ FLP type light fittings will be provided. ➢ Proper ventilation will be provided in Godown.
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➢ Proper label and identification board /stickers will be provided in the storage area. ➢ Conductive drum pallets will be provided. ➢ Drum handling trolley / stackers/fork lift will be used for drum handling. ➢ Separate dispensing room with local exhaust and static earthing provision will be made. ➢ Materials will be stored as per its compatibility study and separate area will be made for
flammable, corrosive and toxic chemical drums storage. ➢ Smoking and other spark, flame generating item will be banned from the Gate.
Applicability of PESO : Company will apply for PESO after getting EC if applicable
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of Process
Safety measures including Automation
Bromination ➢ Bromine handling areas will be clearly marked and restricted to qualified, trained personnel only.
➢ Bromine process area will be done with good ventilation ➢ We will maintain bromine vapor concentration in the work area to
less than 0.1 ppm with adequate exhaust hoods, ventilation systems and scrubbers. Analyze air for proper control.
➢ Transfer or repackage bromine only in a controlled, closed environment.
➢ Exhaust ventilating systems will be used in enclosed areas where bromine is handled.
➢ Personal Protective Equipments are to be made compulsory when handling Bromine
Ammonia ➢ Valve, pipeline will be checked and maintain, in good condition. ➢ All Gaskets will be checked periodically & if new one replaces
found defective. ➢ Joints will be checked regularly to found any Leakage. ➢ ADEQUATE PPE will be kept to handle the Hazard. ➢ ISI Portable fire extinguisher & Hydrant line will be provided as
per TAC norms. ➢ Sufficient amount of sand/soil are kept to control any spillage. ➢ Flame proof fitting provided. ➢ Eye washer cum shower will be provided near tank-farm area. ➢ Spark arrester will be installed on all vehicles inside the premises. ➢ SBA set, Canister mask and airline mask will be provided. ➢ Earthing& bonding on tanks will be provided. ➢ Vent line dipped in water will be provided.
--
H-3 Details of Fire Load Calculation
-
Total Plot Area: 1787.50
Area utilized for plant activity: 240
Area utilized for Hazardous Chemicals Storage: 450
Number of Floors: G+2
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Water requirement for firefighting in KL/hr: 2.5
Water storage tank provided for firefighting in KL 100
Details of Hydrant Pumps: One Fire pump, One diesel driven pump and one Jockey pump are being implemented.
Nearest Fire Station : Panoli GIDC - 0.91 Km
Applicability of Off Site Emergency Plan: N.A
-
H-4 Details of Fire NOC/Certificate: Company will apply for Fire NOC/Certificate after getting EC if applicable
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 14
Number of Contractual person/Labour : 11
Area provided for OHC: 15 Sq. Meter provided in Ground Floor at Admin Building
Number of First Aid Boxes : 2
Nearest General Hospital : Welcare Hospital – 3.00 KM
Name of Antidotes to be store in plant :
--
• Committee discussed regarding :
✓ Plot allotment letter was submitted in name of Mercury Tera Pharma and a rent agreement for 7 years.
✓ Layout of the project was discussed.
✓ CER fund allocation was discussed and PP was asked to revise the CER activities. PP was asked to submit revised CER.
✓ EMP budget was discussed and PP was asked to rework on EMP Budget and submit revised Emp.
• Later on PP vide their e-mail dated 01-09-2021 has submitted revised CER and EMP details.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon’ble Supreme
Court of India in Civil Appeal no. 8478/2020 regarding operation of the Hon’ble NGT orders
dated 10/07/2019 & 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change in
product mix, after the 30th September 2020, considered as per the provisions in force at that
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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time as mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients
(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any
subsequent amendments.
4. PP shall submit six monthly compliance report of Environmental Clearance without fail and
the same shall be critically assessed by the regulatory authority.
5. Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB
directions to all SPCB vide letter no. B-29016/04/06PCI-1/5401 dated 05/02/2014 for
effluent discharge and air emission as per pollutants discharge/emission from respective
project and an arrangement shall also be done for reflecting the online monitoring results on
the company's server, which can be assessable by the GPCB/CPCB on real time basis.
[For Small/Large/Medium (Red Category) & Whichever (Air emission & Effluent
discharge) is applicable].
6. Close loop solvent recovery system with adequate condenser system shall be provided to
recover solvent vapours in such a manner that recovery shall be maximum and recovered
solvent shall be reused in the process within premises.
7. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the
CPCB guidelines. LDAR Logbooks shall be maintained
WATER
8. Total water requirement for the project shall not exceed 37.0KLD. Unit shall reuse 11.9 KLD
of treated industrial effluent within premises. Hence, fresh water requirement shall not
exceed 25.1KLD and it shall be met through GIDC only.
9. The industrial effluent generation from the project shall not exceed 22.78KLD.
10. 19.72 KLD Effluent from process and utility will be treated into primary ETP and primary
treated effluent send to common MEE for the final treatment and disposal.
11. 3.06 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9
Permission..
12. Treated waste water shall be sent to common facilities (CETP, Common MEE, Spray dryer
etc.) only after complying with the inlet norms of common facilities prescribed by GPCB to
ensure no adverse impact on Human Health and Environment
13. Domestic wastewater generation shall not exceed 1.5 KL/day for proposed project and it
shall be treated in STP. Treated sewage shall be utilized for gardening and plantation
purpose within premises after achieving on-land discharge norms prescribed by the GPCB.
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14. During monsoon season when treated sewage may not be required for the plantation /
Gardening / Green belt purpose, it shall be stored within premises. There shall be no
discharge of waste water outside the premises in any case.
15. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
16. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
17. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned in
flue gas matrix.
18. Unit shall provide APCM and stack height as mentioned in process gas matrix.
19. PP shall use approved fuels only as fuel in boilers.
20. Two Stage water and alkali Scrubber shall be provided to control process gas emission.
HAZARDOUS & SOLID WASTE
21. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
22. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
23. The PP shall develop green belt within premises (715 Sq. m. i.e. 40 % of the total plot area) as per the undertaking submitted before SEAC. Green belt shall be developed with native plant species that are significant and used for the pollution abatement as per the CPCB guidelines. It shall be implemented within 3 years of operation phase in consultation with GPCB.
24. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 206 of 357
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
m) Unit shall Store Bromine Bottle in cool dry separate area, out of direct sunlight.
n) Unit shall provide water sprinkler to the ammonia storage cylinder.
9 SIA/GJ/IND2/190264/2020
WILL CARE PHARMA
PLOT NO - 621-P/03, PANOLI GIDC, Anklesvar, Bharuch
EC Reconsideration
Category of the unit: 5(f)
Project status: New
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/190264/2020 on
dated 15.09.2020 for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
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• This is an existing unit proposed for manufacturing of synthetic organic chemicals [API and
API Intermediates] as tabulated below.
Sr. No.
Name of Product CAS NO. Quantity (MT/Mont
h) End Use Remarks
GROUP-A
1 Oxcarbazepine & it’s intermediate
28721-07-5
60.0
Anticonvulsants
Unit is proposed to mfg either individual or total production of (Product No.- 1 to 23) shall not exceed 60 MT/Month.
10-Methoxy Carbezapine 28721-09-7
Intermediate of Oxcarbazepine
2 Fluconazole & it’s intermediate 86386-73-4
Anti allergies
DFTA(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl)Acetophenone)
86404-63-9
Intermediates of Fluconazole
(1-[2-(2,4- difluorophenyl)-2,3-epoxypropyl]-1H-1,2,4-Trizole)
86386-76-7
3 Gapapentin & it’s intermediate Anticonvulsant
2-Azaspiro[4.5]decan-3-one 64744-50-9 Intermediate of
Gabapentin 1,1-Cyclohexanediacetic acid monoamide
99189-60-3
4 Quetiapine Fumarate 111974-69-7
anti-psychotic
5 Fenofibrate 49562-28-9
Antihyperlipidemic
6 Telmisartan & it’s intermediate 144701-48-4
Antihypertensive
4-Methyl -6-(1-methyl-1H-benzoimidozol-2-yl)-2-propyl-1H-benzo imidazole
152628-02-9
4-Bromomethyl)biphenyl-2-carboxylic acid methyl ester
114772-38-2
Mehtyl -4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]methyl]biphenyl carboxylate
528560-93-2
7 Losartan Potassium & it’s intermediate
114798-26-4
Antihypertensive
4’-Bromomethyl-biphenyl-2-carbonitrile
114772-54-2
Intermediate of Losratan
2-butyl-4-chloro-5-formylimidazole
83857-96-9
4’-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile
11477-55-3
2-Butyl-5-chloro-3-[2’(2H- 114798-
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tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde
36-6
8 Teneligliptin & it’s intermediate 760937-92-6
Anti Diabetic
tert-butyl 4-oxo-2-(1,3-thiazolidin-3-ylcarbonyl)pyrrolidine-1-carboxylate OR (2S)-4-Oxo-2-(3-thiazolidinylcarbonyl)-1-pyrrolidinecarboxylic acid tert-butyl ester
401564-36-1
Intermediates of Teneligliptin
9 Aceclofenac Sodium & it’s intermediate
89796-99-6
Anti Flammatory
Tert Buyl Chloroacetate 107-59-5 Intermediate of Aceclofenac
10 Hyscin Butylbromide & it’s intermediate
149-64-4 Antimuscarinic
11 Rabeprazole Sodium & it’s intermediate
117976-89-3
Antiulcer
2-[[[4-(3-methoxypropoxy)-3-methyl-2-pyridinyl] methyl] thio]-1H-benzimidazole
117977-21-6
Intermediates of Rabeprazole Sodium
2-[[4-(3-methoxypropoxy)-3-methyl-pyridin-2-yl]methylsulfinyl]-1H-benzoimidazole
N/A
12 Etoricoxib & it’s intermediate 202409-33-4
anti-inflammatory
2-Chloro -3-(dimethylamino)propene-1-iminium
N/A Intermediate of Etoricoxib
13 Tranexamic Acid & it’s intermediate
1197-18-8 Used to treat heavy bleeding during your menstrual period
4(Aminomethyl)benzoic acid 56-91-7 Intermediate of Tranexamic Acid
4(Aminomethyl)cyclohexanecar boxilic acid
1197-18-8
14 Pantoprazole & it’s intermediate 102625-70-7
Used for heartburn, acid reflux and gastro-oesophageal reflux disease
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2-Chloromethyl-3,4-dimethoxypyridini hydrochloride
72830-09-2 Intermediates
of Pantoprazole
5-Difluoromethoxy-2-{[(3,4-dimethoxy-2-pyridinyl)methyl]thio}-1H-benzimidazole
102625-64-9
15 Clopidogrel Bisulphate 120202-66-6
Antiplatelet
Methyl (+)-alpha-(2-thienylethylamino)(2-chlorophenyl)acetate
141109-
19-5
Intermediate of Clopidogrel Bisulphate
16 2-n-Butyl-3(4-Hydroxy Benzoyl) Benzofuran (n-3)
52490-15-0
Intermediate of Amiodarone HCL
17 4-(2-Methoxy ethyl) Phenol 56718-71-9
Intermediate of Metoprolol succinate
18 P-chloro benzophenone 134-85-0 Intermediate of Cetirizine Dihydrochloride
19 P- chloro Benzhydryl chloride 134-83-8 Intermediate of Cetirizine Dihydrochloride
20 P-chloro benzhydryl piperazine 303-26-4 Intermediate of Cetirizine Dihydrochloride
21 Ketosulfone 221615-75-4
Intermediate of Etoricoxib
22 Thiophene-2-ethanol 5402-55-1 Intermediate of Nebivolol HCI
23 Bis-(2-chloroethyl amine)hydrochloride
821-48-7 Intermediate of Apiprazole
GROUP-B
24 Pregabalin & it’s intermediate
148553-50-8
20.0
Anti -nervousness
Unit is proposed to mfg either individual or total production of (Product No.- 24 to 32)
R-(-)-3-(Carbomethyl)-5-mehtyl hexonic acid R(+)-Alpha Phenylamine salt
3886-69-9 Intermediate of Pregabalin
25 Rosuvastatin Calcium 147098-20-2
Cardiovascular Disease
N-[4-4-Fluoro-phenyl)5-formyl-6-isopropyl-pyrimidine -2-yl]-N-methyl-methanesulfonamide
147118-37-4
3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-
147118-35-2
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isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid ethyl ester
shall not exceed 20 MT/Month.
7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy-5-oxo-hept-6-enoic acid ethyl ester
851443-04-4
26 Atorvastatin Calcium & it’s intermediate
134523-00-5
Antihypertensive
[6-(2-Aminol-ethyal)-2,2 dimethyl-[1,3]dioxin-4-y]-acetic acid tert-buytl ester
125995-13-3
Intermediate of Atorvastatin
6-[2[,2-(4-phenyl-fluoro)-5-4-phenyl-3-isopropyl
-yl[-1-pyrrol-phenylcarbomoyldimethyl-2,2-ethyl}- [1,3]dioxin-4-
yl)- butyl ester-aceticacid tert
125971-95-1
7-[2-(4-flouro-phenyl)-5-isopropyl-3-phenyl-4-phentlcarbomyl-pyrrol-1-yl]-3,5 hydroxy-heptanoic acid-tert butyl(
134395-00-9
27 Carvedilol
72956-09-3
Antihypertansive
3-(Phenylhydrazino)cyclohexanone
27385-45-1
Intermediate of Carvedilol
4-Oxo-1,2,3,4-tetrahydrocarbezole
15128-52-6
4-(2,3-Epoxypropoxy)carbazole 51997-51-4
28 Glimipride & it’s intermediate 93479-97-1
To treat type 2 diabetes
(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1(N—2-phenyl ethyl)-carboxamido]
N/A
Intermediate of Glimipride 4-[2-[(3-Ethyl-4-methyl-2-oxo-3-
pyrrolin-1-yl) carboxamido] ethyl]benzene sulfonamide
119018-29-0
29 Thiocolchicoside 602-41-5 used as a muscle relaxan
30 Nimesulide & it’s intermediate 51803-78-2
anti-inflammatory drug
O- Phenoxy Nitrobenzene 2216-12-8 Intermediate of Nimesulide
O- Phenoxy Aniline 2688-84-8
O- Phenoxy Methane N/A
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31 Diclofenac Sodium & it’s intermediate
15307-79-6
Anti Flammatory
(2,6-DICHLORO PHENYLAMINE)
15307-93-4
Intermediate of Diclofenac Sodium
(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)
15308-01-7
(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)
15362-40-0
32 Albendazole 54965-21-8
Anthelmintic
4-Thiocyno-2-Nitro- anilnemol 54029-45-7
Intermediate of Albendazole
2-Nitro-4-propyl thio aniline 54393-89-4
1,2,diamine-5-propyl thio benznene
66608-52-4
33 R&D -- 0.1
Total 80.1
# Brief Note of Product Profile: 1. No of Manufacturing Plants: 1 Nos 2. Brief Note regarding number of Products to be manufactured considering plant capacity:
We have applied for (32 + R&D) nos. of product in either & or condition, we will not manufacturing above 80.1 MT/Month. And as per the list of machinery, we will be manufacturing 2 to 3 products at a time as orders received from market.
Specific End-use of each proposed products:
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category
of Product
(API/ Intermedi
ate)
Stage of Intermedi
ate n-1, n-2,
etc
Name of API in which
Intermediate Used/ End use of said Intermediat
e
CAS No.
(API)
Said API is used
for/End Use of said API
GROUP-A (Unit is proposed to mfg either individual or total production of Group - A (Product No.- 1 to 23) shall not exceed 60 MT/Month.)
1 Oxcarbazepine & it’s intermediate
28721-07-5
API -- -- -- Anticonvulsants
10-Methoxy Carbezapine
28721-09-7
Intermediate
(n-2) Intermediate of Oxcarbazepine
28721
-07-5
Anticonvulsants
2 Fluconazole & it’s intermediate
86386-73-4
API -- -- -- Anti allergies
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DFTA(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl)Acetophenone)
86404-63-9
Intermediate
(n-2) Intermediates of Fluconazole
86386
-73-4
Anti allergies
(1-[2-(2,4- difluorophenyl)-2,3-epoxypropyl]-1H-1,2,4-Trizole)
86386-76-7
Intermediate
(n-3) Intermediates of Fluconazole
86386
-73-4
Anti allergies
3 Gapapentin & it’s intermediate
60142-96-3
API -- -- -- Anticonvuls
ant
2-Azaspiro[4.5]decan-3-one
64744-50-9
Intermediate
(n-3) Intermediate
of
Gabapentin
60142
-96-3
Anticonvuls
ant
1,1-Cyclohexanediacetic acid monoamide
99189-60-3
Intermediate
(n-2) Intermediate of Gabapentin
60142
-96-3
Anticonvuls
ant
4 Quetiapine Fumarate
111974-69-7
API -- -- -- anti-psychotic
5 Fenofibrate 49562-28-9
API -- -- -- Antihyperlipidemic
6 Telmisartan & it’s intermediate
144701-48-4
API -- -- -- Antihypertensive
4-Methyl -6-(1-methyl-1H-benzoimidozol-2-yl)-2-propyl-1H-benzo imidazole
152628-02-9
Intermediate
(n-4) Intermediate of Telmisartan
144701-48-4
Antihypertensive
4-Bromomethyl) biphenyl-2-carboxylic acid methyl ester
114772-38-2
Intermediate
(n-3) Intermediate of Telmisartan
144701-48-4
Antihypertensive
Mehtyl -4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]methyl]biphenyl carboxylate
528560-93-2
Intermediate
(n-2) Intermediate of Telmisartan
144701-48-4
Antihypertensive
7 Losartan Potassium & it’s intermediate
114798-26-4
API -- -- -- Antihypertensive
4’-Bromomethyl-biphenyl-2-carbonitrile
114772-54-2
Intermediate
(n-4) Intermediate
of Losratan
11479
8-26-4
Antihyperte
nsive
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2-butyl-4-chloro-5-formylimidazole
83857-96-9
Intermediate
(n-3) Intermediate
of Losratan
11479
8-26-4
Antihyperte
nsive
4’-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile
11477-55-3
Intermediate
(n-3) Intermediate of Losratan
11479
8-26-4
Antihypertensive
2-Butyl-5-chloro-3-[2’(2H-tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde
114798-36-6
Intermediate
(n-2) Intermediate of Losratan
11479
8-26-4
Antihypertensive
8 Teneligliptin & it’s intermediate
760937-92-6
API -- -- -- Anti Diabetic
tert-butyl 4-oxo-2-(1,3-thiazolidin-3-ylcarbonyl)pyrrolidine-1-carboxylate OR (2S)-4-Oxo-2-(3-thiazolidinylcarbonyl)-1-pyrrolidinecarboxylic acid tert-butyl ester
401564-36-1
Intermediate
(n-1) Intermediate
s of
Teneligliptin
76093
7-92-6
Anti
Diabetic
9 Aceclofenac Sodium & it’s intermediate
89796-99-6
API -- -- -- Anti Flammatory
Tert Buyl Chloroacetate
107-59-5 Intermediate
(n-1) Intermediate of Aceclofenac
89796-99-6
Anti Flammatory
10 Hyscin Butylbromide & it’s intermediate
149-64-4 API -- -- -- Antimuscarinic
11 Rabeprazole Sodium & it’s intermediate
117976-89-3
API -- -- -- Antiulcer
2-[[[4-(3-methoxypropoxy)-3-methyl-2-pyridinyl] methyl] thio]-1H-benzimidazole
117977-21-6
Intermediate
(n-2) Intermediates of Rabeprazole Sodium
11797
6-89-3
Antiulcer
2-[[4-(3- N/A Intermedi (n-1) Intermediate 11797 Antiulcer
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methoxypropoxy)-3-methyl-pyridin-2-yl]methylsulfinyl]-1H-benzoimidazole
ate s of
Rabeprazole
Sodium
6-89-3
12 Etoricoxib & it’s intermediate
202409-33-4
API -- -- -- anti-inflammatory
2-Chloro -3-(dimethylamino) propene-1-iminium
N/A Intermediate
(n-1) Intermediate of Etoricoxib
202409-33-4
anti-inflammatory
13 Tranexamic Acid & it’s intermediate
1197-18-8 API -- -- -- Used to treat heavy bleeding during your menstrual period
4(Aminomethyl)benzoic acid
56-91-7 Intermediate
(n-2) Intermediate
of
Tranexamic
Acid
1197-
18-8
Used to
treat heavy
bleeding
during your
menstrual
period
4(Aminomethyl)cyclohexanecar boxilic acid
1197-18-8 Intermediate
(n-1) Intermediate of Tranexamic Acid
1197-
18-8
Used to treat heavy bleeding during your menstrual period
14 Pantoprazole & it’s intermediate
102625-70-7
API -- -- -- Used for heartburn, acid reflux and gastro-oesophageal reflux disease
2-Chloromethyl-3,4-dimethoxypyridini hydrochloride
72830-09-2
Intermediate
(n-3) Intermediates of Pantoprazole
10262
5-70-7
Used for heartburn, acid reflux and gastro-oesophageal reflux disease
5- 102625- Intermedi (n-1) Intermediate 10262 Used
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Difluoromethoxy-2-{[(3,4-dimethoxy-2-pyridinyl)methyl]thio}-1H-benzimidazole
64-9 ate s of Pantoprazole
5-70-7 for heartbur
n, acid
reflux and
gastro-
oesophage
al reflux
disease
15 Clopidogrel Bisulphate
120202-66-6
API -- -- -- Antiplatelet
Methyl (+)-alpha-(2-thienylethylamino)(2-chlorophenyl)acetate
141109-19-5
Intermediate
(n-1) Intermediate of Clopidogrel Bisulphate
12020
2-66-6
Antiplatelet
16 2-n-Butyl-3(4-Hydroxy Benzoyl) Benzofuran
52490-15-0
Intermediate
(n-3) Intermediate of Amiodarone HCL
19774
-82-4
Anti-
arrhythmic
17 4-(2-Methoxy ethyl) Phenol
56718-71-9
Intermediate
(n-3) Intermediate of Metoprolol succinate
98418
-47-4
Antihyperta
nsive
18 P-chloro benzophenone
134-85-0 Intermediate
(n-4) Intermediate of Cetirizine Dihydrochloride
83881
-52-1
Antihistamin
e
19 P- chloro Benzhydryl chloride
134-83-8 Intermediate
(n-3) Intermediate of Cetirizine Dihydrochloride
83881
-52-1
Antihistamin
e
20 P-chloro benzhydryl piperazine
303-26-4 Intermediate
(n-2) Intermediate
of Cetirizine
Dihydrochlor
ide
83881
-52-1
Antihistamin
e
21 Ketosulfone 221615-75-4
Intermediate
(n-3) Intermediate of Etoricoxib
20240
9-33-4
NSAID
22 Thiophene-2-ethanol
5402-55-1 Intermediate
(n-3) Intermediate of Nebivolol HCI
12020
2-66-6
Antiplatelet
23 Bis-(2-chloroethyl amine)hydrochloride
821-48-7 Intermediate
(n-3) Intermediate of Aripiprazole
12972
2-12-9
Antidepressant
GROUP-B(Unit is proposed to mfg either individual or total production of Group - B (Product No.- 24 to 32) shall not exceed 20 MT/Month.)
24 Pregabalin & it’s intermediate
148553-50-8
API -- -- -- Anti -
nervousnes
s
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R-(-)-3-(Carbomethyl)-5-mehtyl hexonic acid R(+)-Alpha Phenylamine salt
3886-69-9 Intermediate
(n-2) Intermediate
of
Pregabalin
14855
3-50-8
Anti -
nervousnes
s
25 Rosuvastatin Calcium
147098-20-2
API -- -- -- Cardiovasc
ular
Disease
N-[4-4-Fluoro-phenyl)5-formyl-6-isopropyl-pyrimidine -2-yl]-N-methyl-methanesulfonamide
147118-37-4
Intermediate
(n-4) Intermediate of Rosuvastatin Calcium
14709
8-20-2
Cardiovascular Disease
3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid ethyl ester
147118-35-2
Intermediate
(n-3) Intermediate of Rosuvastatin Calcium
14709
8-20-2
Cardiovascular Disease
7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy-5-oxo-hept-6-enoic acid ethyl ester
851443-04-4
Intermediate
(n-2) Intermediate of Rosuvastatin Calcium
14709
8-20-2
Cardiovascular Disease
26 Atorvastatin Calcium & it’s intermediate
134523-00-5
API -- -- -- Antihypertensive
[6-(2-Aminol-ethyal)-2,2 dimethyl-[1,3]dioxin-4-y]-acetic acid tert-buytl ester
125995-13-3
Intermediate
(n-3) Intermediate of Atorvastatin
13452
3-00-5
Antihypertensive
6-[2[,2-(4--fluoro-phenyl(5
-3-isopropyl-4-phenyl
-phenylcarbomoyl
125971-95-1
Intermediate
(n-2) Intermediate of Atorvastatin
13452
3-00-5
Antihypertensive
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-ethyl}-yl[-1-pyrrol2,2-dimethyl-
[1,3]dioxin-4-yl)- -aceticacid tert
butyl ester
7-[2-(4-flouro-phenyl)-5-isopropyl-3-phenyl-4-phentlcarbomyl-pyrrol-1-yl]-3,5 hydroxy-heptanoic acid-tert butyl
134395-00-9
Intermediate
(n-1) Intermediate of Atorvastatin
13452
3-00-5
Antihypertensive
27 Carvedilol 72956-09-3
API -- -- -- Antihypertansive
3-(Phenylhydrazino) cyclohexanone
27385-45-1
Intermediate
(n-3) Intermediate of Carvedilol
72956
-09-3
Antihypertansive
4-Oxo-1,2,3,4-tetrahydrocarbezole
15128-52-6
Intermediate
(n-2) Intermediate of Carvedilol
72956
-09-3
Antihypertansive
4-(2,3-Epoxypropoxy) carbazole
51997-51-4
Intermediate
(n-1) Intermediate of Carvedilol
72956
-09-3
Antihypertansive
28 Glimipride & it’s intermediate
93479-97-1
API -- -- -- To treat type 2 diabetes
(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1(N—2-phenyl ethyl)-carboxamido]
N/A Intermediate
(n-2) Intermediate of Glimipride
93479
-97-1
To treat type 2 diabetes
4-[2-[(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1-yl) carboxamido] ethyl]benzene sulfonamide
119018-29-0
Intermediate
(n-1) Intermediate of Glimipride
93479
-97-1
To treat type 2 diabetes
29 Thiocolchicoside 602-41-5 API -- -- -- used as a muscle relaxan
30 Nimesulide & it’s intermediate
51803-78-2
API -- -- -- anti-inflammatory drug
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O- Phenoxy Nitrobenzene
2216-12-8 Intermediate
(n-3) Intermediate of Nimesulide
51803-78-2
anti-inflammatory drug
O- Phenoxy Aniline
2688-84-8 Intermediate
(n-2) Intermediate of Nimesulide
51803-78-2
anti-inflammatory drug
O- Phenoxy Methane
N/A Intermediate
(n-1) Intermediate of Nimesulide
51803-78-2
anti-inflammatory drug
31 Diclofenac Sodium & it’s intermediate
15307-79-6
API -- -- -- Anti Flammatory
(2,6-DICHLORO PHENYLAMINE)
15307-93-4
Intermediate
(n-4) Intermediate of Diclofenac Sodium
15307
-79-6
Anti Flammatory
(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)
15308-01-7
Intermediate
(n-3) Intermediate of Diclofenac Sodium
15307
-79-6
Anti Flammatory
(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)
15362-40-0
Intermediate
(n-2) Intermediate of Diclofenac Sodium
15307
-79-6
Anti Flammatory
32 Albendazole 54965-21-8
API -- -- -- Anthelmintic
4-Thiocyno-2-Nitro- anilnemol
54029-45-7
Intermediate
(n-3) Intermediate of Albendazole
54965
-21-8
Anthelmintic
2-Nitro-4-propyl thio aniline
54393-89-4
Intermediate
(n-2) Intermediate of Albendazole
54965
-21-8
Anthelmintic
1,2,diamine-5-propyl thio benznene
66608-52-4
Intermediate
(n-1) Intermediate of Albendazole
54965
-21-8
Anthelmintic
Brief Note regarding End-Use of Product Profile:
1. Total No of API: 24 Nos
2. Total No of Intermediates (n-1): 12 Nos
3. Total No of Intermediates (n-2) & Other: 39 Nos
• During the meeting dated 15.04.2021, Project proponent (PP) and their Technical Expert
from M/s. Ozone Enviro Tech remained present during video conference meeting.
• The technical expert informed the Committee that their application for sub-plotting is yet to
be approved by GIDC.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 219 of 357
• After deliberation, SEAC unanimously decided to defer the proposal and consider the same in one of the upcoming meeting of SEAC upon submission of approval of GIDC in the matter of sub-plotting.
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Ozone Enviro Tech remained
present during video conference meeting.
• Revised Salient features of the project submitted as under:
Sr. no.
Particulars Details
A
A-1 Total cost of Proposed Project (Rs. in Crores):
3.90 crores
Break-Up of Project Cost
Particulars Proposed Amount
(Rs. in Crore)
Land Cost & It’s Development 1.00
Civil Structure & Building 0.90
Plant & Machinery Cost 1.05
Environment protection measures (includes cost of ETP, Tree Plantation, etc.)
0.95
Total Project Cost 3.90
-
A-2 Details of Environmental Management Plan (EMP) As Below
Bifurcation of EMP Cost
Sr. No
Unit Installed Capacity
(KLD)
Capital Cost (Rs. In Lakhs )
Operating Cost
(Lacs/Year)
Maintenance Cost
(Lacs/Year)
Total Recurring
Cost (Lacs/Year)
1 Waste Water 30 KLD 17.0 291.60 -- 291.60
2 Air -- 27.50 -- 3.40 3.40
3 Hazardous Management
-- 6.0 108.91 -- 108.91
4 Fire & Safety -- 25.0 -- 3.00 3.00
5 AWH Monitoring
-- 1.0 -- 1.00 1.00
6 Green Belt Development
-- 2.76 -- 1.80 1.80
7 Occupational Health
-- 1.0 -- 1.85 1.85
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8 Corporate Environment Responsibility
For Year 2021-2024 15.6 -- -- --
Total 96.56 400.51 11.05 411.56
Summary
Cost of Project in Crores per Annum: 3.90 Cr.
EMP Capital Cost in Crores per Annum and Percentage: 0.95 Cr. (24.35%)
EMP Recurring Cost in Crores per Annum and Percentage: 4.11 Cr
--
A-3 Details of CER (As per MoEF&CC OM dated 01/05/2018) As Below
As per OM no. 22-65/2017 on dated 01/05/2018 regarding “Corporate Environment Responsibility” (CER), Greenfield projects have to contribute 2% (Rs. 7.80 Lack) of the Capital Investment (3.90 Cr). But as per New Mechanism of CPCB vide letter no CPCB/IPC-VII/CEPI/NGT/2019 on dated 25/10/2019, we shall commit to do 4% (Rs. 15.60 Lack) of Project Cost as a CER. Our CER activity are as below table…
Component As per Norms Allocation
CER Rs. 7.80 Lakhs (2 %) Rs. 15.6 Lakhs (4 %)
Activities to be carried out under CER:
-
CER Activities Fund (Rs.)
2021-2022
Provided Solar street light set with battery backup (18W -15 Nos.) in Kharod Village
4,50,000/-
2022-2023
Company provide R.O. Plant (2000 Liter/hr) and drinking water storage tank in Bakrol village
4,00,000/-
2023-2024
Company will construct 75,000/- Liter RCC collection tank with filtration facility for rain water harvesting in Bhadkodra Village
7,10,000/-
TOTAL 15,60,000 /-
B Land / Plot ownership details:
B-1 Total Plot area ( sq. meter) 2268.75 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Sr. No.
Description Gr. Floor
Area Sq. Meter
First Floor B/U Area Sq. Meter
Second Floor B/U Area Sq. Meter
1 Production Building 100 100 100
2 Raw Material Storage Area 200 -- --
3 Finish Product Storage Area 50 -- --
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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4 Haz. Waste Storage Area 150 -- --
5 Boiler Area 120 -- --
6 ETP 50 -- --
7 Hydrogen Storage Area 20 -- --
8 Gas storage Area 20 -- --
9 Admin & OHC Room 50 50 50
10 Green Belt Area (40%) 908 -- --
11 Road & Open Area 590.75 -- --
12 Security Cabin 10 -- --
TOTAL 2268.75
Company have store 1056 MT material as per calculations, we require 405 MT storage of material. Hence company has adequate area for storage of the Raw Material / Haz. Chemicals, Hazardous waste and Product. --
B-3 Green belt area ( sq. meter)
908 Sq. m. (40%)
C Employment generation Direct - 15 Employees Indirect - 10 Employees Total - 25 Employees
D Water
D-1 Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Water Supply
Status of permission from the concern authority.
D-2 Water consumption (KLD)
Category
Quantity KLD
Remarks
(M) Domestic 3.0
(N) Gardening 6.0
(O) Industrial
Process 12.4
Washing 5.0
Boiler 45.0
Cooling 30.0
Scrubber 2.4
Other (R&D) 0.2
Industrial Total 95.0
Total (A + B + C) 104.0
--
As per our proposed product profile manufacturing process and mass balance, worst case scenario for water consumption is (Product no- 20) (P-chloro benzhydryl piperazine ) (4.80) and (Product no- 27) (Carvedilol) (7.57).
Summary of water requirement Quantity
KLD Remarks
Total water requirement for the project (A) 104.0
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Quantity to be recycled (B) 62.5
Total fresh water requirement (C) 41.5
Ensure Total water requirement = Fresh water + Recycled water
(104.0 = 41.5 + 62.5)
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]
Source of waste water for reuse in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
2.5 KLD Domestic effluent
Gardening Purposed
BOD-30 --
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. --
D-3 Waste water generation (KLD)
Category
Waste water KLD
Remarks
(A) Domestic 2.5
(B) Industrial
Process 14.3
Washing 5.0
Boiler 4.5
Cooling 3.0
Scrubber 3.2
Other (R&D) 0.2
Industrial Total 30.2
Total (A + B) 32.7
-
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative): As per our proposed product profile manufacturing process and mass balance, worst case scenario for waste water generation is (Product no- 22) (Thiophene-2-ethanol) (5.4) and(Product no- 27) (Carvedilol) (8.99)
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (If any applicable to proposal).
➢ Not Applicable
D-4 Mode of Disposal & Final meeting point
Domestic: 2.5 KLD domestic effluent will be treated into STP and reused for gardening purposed
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Industrial: 27.0 KLD Effluent from process and utility will be treated into primary ETP and primary treated effluent send to common MEE for the final treatment and disposal. 3.2 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9 Permission.
-
D-5 Treatment facility within premises with capacity
For Domestic waste water: Capacity of STP – 3.0 KLD.
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ➢ In-house ETP @ 30 KLD
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.)
CHARACTERISTICS BEFORE & AFTER TREATEMENT OF EFFLUENT
Sr. No.
Parameter
Characteristics(mg/L)
Primary treated Process
Boiler blow down
Cooling Tower blow down
Washing Composite
1 pH 3-9 8 - 8.5 8 - 8.5 5.5 - 8.5 3-9 6.5-7.5
2 TDS 28000 350 250 1000 28000 28700
3 TSS 500 250 350 200 500 75
4 COD 20000 30 100 600 20000 13000
5 BOD3 700 10 30 200 700 490
--
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ Not Applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Total proposed waste water generation from the industry will be 32.7 KLD (Ind. – 30.2 KLD + Dom. –2.5) Industrial:- 27.0 KLD Effluent from process and utility will be treated into primary ETP and primary
treated effluent send to common MEE for the final treatment and disposal. 3.2 KLD Scrubbing media reuse in plant premises & Sell to end user who is having
Rule-9 Permission. Domestic:- 2.5 KLD domestic effluent will be treated into STP and reused for gardening purposed.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
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➢ Common MEE Ms/ BEIL, Ankleshwer
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
➢ M/s. BEIL, Ankleshwar for Common MEE vide letter no BEIL/ANK/2021 dated 21/07/2021
D-7 Simplified water balance diagram with reuse / recycle of waste water
E Air
E-1 Brief Note on fuel based heat energy requirement and worst case scenario thereof:
SR. NO.
NAME OF FUEL QUANTITY
1. Briquette of Bio Coal 13 MT/Day
2. HSD 50 Lit/hr
Power Requirements: Proposed: Power required from DGVCL is 1000 KVA. Standby power supply from D.G. set (500 KVA) in emergency case. --
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E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC’s OM vide dated 31.10.2019)
-
SR. NO.
SOURCE OF EMISSION
WITH CAPACITY
STACK HEIGHT (METER)
TYPE OF FUEL
QUANTITY OF FUEL
TYPE OF EMISSIONS
I.E. AIR POLLUTANTS
AIR POLLUTION CONTROL
MEASURES (APCM)
1
Boiler
(Cap. - 1.5
MT/hr & 4.0
MT/hr) 9.10 3
0
M
9.11 B
riqu
ette
of
Bio
Coa
l
9.12 1
0
MT
/D
ay 9.13 PM
SO2 NOx
9.14 M
ulticy
clone
Separ
ator
With
Bag
Filter
2
Thermic Fluid Heater (Cap. - 1 Lakh Kcal/ Hr)
Briquette of Bio Coal
3 MT/Day
Multicyclone
Separator
With Bag
Filter
3
D.G. Sets
(Stand by)
(Cap. – 500 KVA)
18 M HSD
9.15 5
0
Liter/hr
Adequate
Stack Height
-
E-3 Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr. No.
Stack Attached To Stack Height
Air Pollution Control System
Parameter
1 Process Vent -1 (Chlorination/Sulphonation) Product No. 23
11 M
Two stage Scrubber (Water +
Alkali)
HCl SO2
2 Process Vent -2 (Nitrification) Product No. 30
11 M Two stage Alkali
Scrubber NOx
3 Process Vent -3 Product No. 5,32
11 M Two stage Alkali
Scrubber HBr
4 Process Vent -4 (Ammonification) Product No. 27
11 M Two stage
water Scrubber
NH3
5 Process Vent -5 (Chlorination) Product No. 32
11 M Two stage
water Scrubber
Cl2
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Note: ➢ Details of gaseous raw materials used in proposed project – Hydrogen gas,
Ammonia gas and Chlorine gas are used
➢ Estimation of process gas emission (Product wise and Total) – process gas
emission for chlorination & Sulphonation – Product No.- 23, process gas
emission for Nitrification – Product No.- 30, process gas emission for
Bromination– Product No.- 5,32 process gas emission for Ammonification –
Product No.- 27, process gas emission for Chlorination– Product No.- 32.
➢ Requirement of the scrubbing media (KL per Day) considering solubility
(Product wise and Total).
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above
and its sound management in HW matrix. Complied
E-4 Fugitive emission details with its mitigation measures: Following measures will be adopted to prevent and control fugitive emissions…
➢ Solid raw material charging will be done through closed system to avoid fugitive emissions. ➢ Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing
enclosures. ➢ Adequate ventilation will be provided. ➢ Periodic monitoring of work area will be carried out to check the fugitive emission.
➢ Minimum number of flanges, joints and valves in pipelines. ➢ Regular inspection of floating roof seals and proper preventive maintenance of roofs and
seals for tanks. ➢ Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer
area will be collected through hoods and ducts by induced draft and controlled by scrubber/ dust collector / bad filter.
➢ Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
F Hazardous waste management matrix (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Sr. no.
Type/Name of Hazardous
waste
Source of generation
Category and
Schedule as per HW
Rules.
Quantity (MT/Annum)
Disposal Method
1 ETP Sludge ETP SCH-I/35.3 90 Collection, Storage, Transportation and
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Disposal at common TSDF site.
2 Discarded Drums/Bags/ Liners
Raw Materials/ Products
SCH-I/33.1 35 Collection, Storage, Transportation, Decontamination & Sale to GPCB approved vendors/ reuse /send back to supplier.
3 Used/ Spent Oil Machineries/Utility
SCH-I/5.1 1.4 Collection, Storage, Disposal by reuse in plant machinery as lubricant or transportation & Sale to GPCB registered re-processor.
4 Distillation Residue
Distillation SCH-I/20.3 184 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
5 Spent Solvent Process SCH-I/28.6 7311 Collections, Storage, distillation and reuse in plant premises.
6 Spent Carbon Process SCH-I/28.3 76 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
7 Organic Residue Process SCH-I/28.1 159 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
8 Inorganic residue Process SCH-I/28.1 58 Collection, Storage, Transportation and sent for co-processing in cement industries or Disposal at common TSDF Site .
9 Spent Catalyst Process SCH-I/28.1 25 Collection, Storage, reuse in the plant premises or Transportation and send to regenerator under Rule-9.
10 Iron Sludge Process (Product
SCH-I/28.1 277 Collection, Storage, Transportation and sent for
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No. 30) co-processing in cement industries (in case of non-operation of co-processing site) Disposal at common incineration site.
11 Aluminum chloride
Process (Product
No. 18,31)
SCH-I/28.1 1193 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
14 Dilute HCl (28%) Process (Product No.- 25)
+ Scrubber (Product
No.- 23, 32)
SCH- II / B 15
10.70 +
468.3 = 479
Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 19 – 849 MT/Year)
15 Sodium bi sulphite (30%)
Scrubber SCH- II / B 15
82 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
16 Sodium Nitrate Scrubber SCH-I/28.1 22 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission
17 Sodium Bromide (25%)
Process (Product No.- 22)
+ Scrubber (Product
No.- 5,32)
SCH- II / B 15
492.12 +
516= 1009
Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
18 Liq. Ammonia (25%)
Scrubber SCH- II / B 15
159 Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 13 – 593.16 MT/Year)
19 Off Specification Products
From mfg. Process (Batch failure)
SCH-I/28.4 10 Collection, Storage, Transportation and sent for co-processing in cement industries (in case of non-operation of co-processing site) Disposal at common incineration site.
R&D
20 ETP Sludge ETP 35.3 3.0 Collection, Storage, Transportation & disposal in TSDF.
21 Residue from Distillation/
R&D 28.1 4.0 Collection, Storage, Transportation & send to
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-
Organic Process Waste
cement industries for co-processing or incineration in CHWIF.
22 Discarded Drum Raw Materials/Pr
oducts
33.1 20 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
23 Discarded Bags / Liner
Raw Materials/Pr
oducts
33.1 0.2 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
24 Off Specification Products
R&D 28.4 1.0 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Company is obtain the provisional membership of TSDF & CHWIF
Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Ankleshwar for Common MEE vide letter no BEIL/ANK/2021 dated 21/07/2021
F-3 Details of Non-Hazardous waste & its disposal (MSW and others)
Not Applicable
G Solvent management, VOC emissions etc.
G-1 Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)
SOLVENT RECOVERY AFTER LDAR
Sr. No.
Type of Solvent
% Recovery
% Losses
Air Water Haz
1 Methanol 96.4 0.86 1.84 0.90
2 Cyclohexane 96.0 0.93 2.07 1.00
3 Methylne Dichloride 96.3 0.89 1.96 0.95
4 Ethyl Acetate 96.4 0.91 1.79 0.90
5 Dimethyl Formamide 96.5 0.76 1.87 0.87
6 Ethylene Dichloride 96.3 0.97 1.81 0.92
7 Acetone 96.4 0.88 1.82 0.90
8 Toluene 96.3 0.94 1.84 0.92
Justification of Reuse of solvent
Name of Solvent Total
requirement MT/Month
Total quantity of solvent recovered MT/Month
Methanol 95.06 91.63
Cyclohexane 37.40 35.89
Methylne Dichloride 64.00 61.6
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Ethyl Acetate 44.00 42.41
Dimethyl Formamide 24.00 23.15
Ethylene Dichloride 210.00 202.26
Acetone 30.00 28.92
Toluene 260.00 250.32
--
G-2 Brief Note on LDAR proposed:
➢ Company will be installed double mechanical seal and MSW Gaskets in solvent pipelines to prevent leakage from flanges
➢ Company will be reduced the joints and valves in pipelines. ➢ All the rotating equipment like pumps will be installed with double Mechanical Seals to arrest
any sort of emissions. ➢ Flanges will be sealed so less losses will be there. ➢ Down the Temperature of Cooling tower to 5 0C ➢ Chilled Brine at -10 0C will be used to trap any traces of Solvent which is slipped from
Secondary condenser. ➢ Closed loop system. ➢ For continue vapor travelling 100mm of Hg (slight vacuum) will be applied on secondary
condenser. --
G-3 VOC emission sources and its mitigation measures (Brief note on LDAR) ➢ Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent
leakages and thus minimizing the fugitive emissions of VOCs. ➢ Entire process will be carried out in the closed reactors with proper maintenance of pressure and
temperature. ➢ To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent
pumps. ➢ Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with on-line pH
meter with hotter system for better operational control. ➢ Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be
connected to vent chillers. ➢ All the raw materials will be pneumatically transfer to the reactor. ➢ Emphasis will be given to solvent management/solvent loss prevention. ➢ Control by having proper scrubbing system. ➢ Condenser to trap VOC. ➢ Proper gland packing will be maintained for pumps and valves and to the extent possible pumps with
mechanical seal.
H Safety Detail
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
Details regarding storage of Hazardous chemicals
Storage details Name of major Hazardous chemicals Remarks
Storage tanks -- --
Drum/Barrel storage
All Other Raw material storage into Drum & Bags only like Methylene Dichloride, Acetic acid, Hydrochloric acid, Sulphuric acid.
Bottles --
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Cylinder Ammonia gas, Hydrogen gas & Chlorine gas
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
➢ FLP type light fittings will be provided. ➢ Proper ventilation will be provided in Godown. ➢ Proper label and identification board /stickers will be provided in the storage area. ➢ Conductive drum pallets will be provided. ➢ Drum handling trolley / stackers/fork lift will be used for drum handling. ➢ Separate dispensing room with local exhaust and static earthing provision will be made. ➢ Materials will be stored as per its compatibility study and separate area will be made for
flammable, corrosive and toxic chemical drums storage. ➢ Smoking and other spark, flame generating item will be banned from the Gate.
Safety details of Hazardous Chemicals:
Type of Hazardous Chemicals
Safety measures
Sulfuric Acid Milk of magnesia
Hydrochloric Acid Milk of Magnesia, Drink Large Quantity of Water
Acetic Acid Milk of magnesia
Methanol In case of acidosis give Sodium Bicarbonate. In case of delirium give Diazepam 10 mg. by intravenous injection.
Acetonitrile Hydroxocobalamin or the cynide antidote kit
Applicability of PESO : Company will apply for PESO after getting EC if applicable
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
Type of Process
Safety measures including Automation
Hydrogenation ➢ Installed DCS System ➢ FLP type area will be provided. ➢ Total enclosed process system. ➢ Instrument & Plant Air System. ➢ Nitrogen blanketing in Hydrogenation reactor. ➢ Safety valve and Rupture disc provided on reactor. ➢ Cooling Chilling and power alternative arrangement have been
made on reactor. ➢ Hydrogen and Nitrogen Cylinder bank away from the auto clave
reactor. ➢ PRV station with shut off valve, safety valve provision will be
made for hydrogenation reaction safety. ➢ Before Hydrogen Gas charging in to reactor and after completion
of reaction Nitrogen flushing will be done. ➢ Flame arrestor will be provided on vent line of reactor and it will
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be extended up to roof level. ➢ Open well ventilated and fragile roofs will be provided to on
reactor. ➢ Safe Catalyst charging method will be adopted. ➢ SOP will be prepared and operators will be trained for the same. ➢ Static earthing and electric earthing (Double) provided. ➢ Reactor vent extended outside the process area and flame
arrestor provided on vent line. ➢ Dumping vessel arrangement will be made. ➢ Dumpers for static earthing on pipeline flanges of flammable
chemical will be provided.
Ammonia ➢ Valve, pipeline will be checked and maintain, in good condition. ➢ All Gaskets will be checked periodically & if new one replaces
found defective. ➢ Joints will be checked regularly to found any Leakage. ➢ ADEQUATE PPE will be kept to handle the Hazard. ➢ ISI Portable fire extinguisher & Hydrant line will be provided as
per TAC norms. ➢ Sufficient amount of sand/soil are kept to control any spillage. ➢ Flame proof fitting provided. ➢ Eye washer cum shower will be provided near tank-farm area. ➢ Spark arrester will be installed on all vehicles inside the premises. ➢ SBA set, Canister mask and airline mask will be provided. ➢ Earthing& bonding on tanks will be provided. ➢ Vent line dipped in water will be provided.
Chlorination ➢ Chlorine Hood with blower will be provided with scrubbing arrangement.
➢ Chlorine absorption system will be provided. In case of chlorine leakage in chlorine shed it will be suck through blower and it will be scrubbed in Caustic scrubber.
➢ Safety Shower and eye wash will be provided in Chlorine shed area.
➢ Emergency siren will be provided. ➢ First Aid Boxes and Occupational health centre will be made at
site. ➢ Chlorine cylinders will be stored in cylinder storage area. ➢ Safety Valve and pressure gauge will be provided on reactor. ➢ All emergency valves and switches and emergency handling
facilities will be easily assessable. ➢ All the vessels and equipments will be earthed appropriately and
protected against Static Electricity. ➢ Materials will be transferred by pumping through pipeline or by
vacuum ➢ Flame proof light fittings will be installed in the plant. ➢ All the Plant Personnel will be provided with PPE ➢ All employees will be given and updated in Safety aspects
through periodic training in safety
Nitration ➢ The Reactor will have Temperature control system cascaded with cooling water system consisting of Cooling tower, pumps and
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circulating system. In case of high temperature the steam will get cut off and cooling water will start circulating through the reactor coils. Alternately Chilled water system is also provided for extreme emergencies.
➢ The Reactor will have rupture disc and safety valves which will take care of excess pressure and the outlet of which is connected to the scrubbers.
➢ The Reactor will also have a separate high local vent with pressure relief valve which is connected to a catch pot with water. The catch pot contents will be separated for recycle purpose. This will be additional safety, if 1 & 2 fail at the same time, which is unlikely.
➢ In case of contact with eyes, immediately flush eyes with plenty of water for at least 15 minutes. Cold water may be used. Get medical attention immediately.
➢ In case of contact with skin, immediately flush skin with plenty of water for at least 15 minutes while removing contaminated clothing and shoes. Cover the irritated skin with an emollient. Cold water may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention immediately.
➢ Wash with a disinfectant soap and cover the contaminated skin with an anti-bacterial cream. Get medical attention.
➢ If inhaled, remove to fresh air. If not breathing, give artificial respiration. If breathing is difficult, give oxygen. Get medical attention immediately.
➢ Evacuate the victim to a safe area as soon as possible.
--
H-3 Details of Fire Load Calculation
Total Plot Area: 2268.75
Area utilized for plant activity: 300
Area utilized for Hazardous Chemicals Storage: 710
Number of Floors: G+2
Water requirement for firefighting in KL/hr: 3.63
Water storage tank provided for firefighting in KL 100
Details of Hydrant Pumps: One Fire pump, One diesel driven pump and one Jockey pump are being implemented.
Nearest Fire Station : Panoli GIDC – 0.91 Km
Applicability of Off Site Emergency Plan: N.A
-
H-4 Details of Fire NOC/Certificate: Company will apply for Fire NOC/Certificate after getting EC if applicable
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 15
Number of Contractual person/Labour : 10
Area provided for OHC: 15 Sq. Meter provided in Ground
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Floor at Admin Building
Number of First Aid Boxes : 2
Nearest General Hospital : Welcare hospital – 3.0 KM
Name of Antidotes to be store in plant :
--
• Committee discussed on the following:
✓ Plot allotment letter was submitted.
✓ Layout of the project was discussed.
✓ CER fund allocation was discussed and PP was asked to revise the CER activities. PP was asked to submit revised CER.
• Later on PP vide their e-mail dated 01-09-2021 has submitted revised CER details.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon’ble
Supreme Court of India in Civil Appeal no. 8478/2020 regarding operation of the
Hon’ble NGT orders dated 10/07/2019 & 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change
in product mix, after the 30th September 2020, considered as per the provisions in
force at that time as mentioned in the Notification vide S.O. 1223 (E) dated
27/03/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical
Ingredients (API) as per the amended EIA Notification vide S.O. 1223 (E) dated
27/03/2020 and any subsequent amendments.
4. PP shall submit six monthly compliance report of Environmental Clearance without
fail and the same shall be critically assessed by the regulatory authority.
5. Total number of products manufacturing shall not exceeding two-three (2-3) at a
given point of time as per the plant capacity shown in plant layout.
6. (a) R & D products shall be of similar chemistry in line with the EIA Notification vide
S.O. 1223 (E) dated 27/03/2020 and the pollution load shall remain the same as
committed. (b) Project proponent shall not take continuous/commercial production of
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the R & D materials. Necessary approvals shall be obtained from the concern
authorities prior to commercial production of R & D materials. (c) Unit shall submit
relevant details of R & D products like raw materials, its safety measures to the
regulatory authority well before R & D activity. (d) Unit shall submit relevant details of
R & D products like different wastes generated (Quantity & Quality) and its
management to the regulatory authority within a month of R & D activity.
7. Unit shall install CEMS [Continuous Emission Monitoring System] in line to
CPCB directions to all SPCB vide letter no. B-29016/04/06PCI-1/5401 dated
05/02/2014 for effluent discharge and air emission as per pollutants
discharge/emission from respective project and an arrangement shall also be done
for reflecting the online monitoring results on the company's server, which can be
assessable by the GPCB/CPCB on real time basis. [For Small/Large/Medium (Red
Category) & Whichever (Air emission & Effluent discharge) is applicable].
8. Close loop solvent recovery system with adequate condenser system shall be
provided to recover solvent vapours in such a manner that recovery shall be
maximum and recovered solvent shall be reused in the process within premises.
9. Leak Detection and Repair (LDAR) program shall be prepared and implemented as
per the CPCB guidelines. LDAR Logbooks shall be maintained
WATER
10. Total water requirement for the project shall not exceed 104.0KLD. Unit shall reuse
62.5KLD of treated industrial effluent within premises. Hence, fresh water
requirement shall not exceed 41.5 KLD and it shall be met through GIDC only.
11. The industrial effluent generation from the project shall not exceed 30.2KLD.
12. 27.0 KLD Effluent from process and utility will be treated into primary ETP and
primary treated effluent send to common MEE for the final treatment and disposal.
3.2 KLD Scrubbing media reuse in plant premises & Sell to end user who is having
Rule-9 Permission.
13. Treated waste water shall be sent to common facilities (CETP, Common MEE, Spray
dryer etc.) only after complying with the inlet norms of common facilities prescribed
by GPCB to ensure no adverse impact on Human Health and Environment
14. Domestic wastewater generation shall not exceed 2.5 KL/day for proposed project
and it shall be treated in STP. Treated sewage shall be utilized for gardening and
plantation purpose within premises after achieving on-land discharge norms
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 236 of 357
prescribed by the GPCB.
15. During monsoon season when treated sewage may not be required for the plantation
/ Gardening / Green belt purpose, it shall be stored within premises. There shall be
no discharge of waste water outside the premises in any case.
16. Unit shall provide buffer water storage tank of adequate capacity for storage of
treated waste water during rainy days.
17. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
18. Unit shall not exceed fuel consumption and provide APCM and Stack height as
mentioned in flue gas matrix.
19. Unit shall provide APCM and stack height as mentioned in process gas matrix.
20. PP shall use approved fuels only as fuel in boilers.
21. Two stage Alkali Scrubber shall be provided for control of Process gas emission.
HAZARDOUS & SOLID WASTE
25. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
26. The unit shall submit the list of authorized end users of hazardous wastes along with MoU
signed with them at least two months in advance prior to the commencement of production.
In the absence of potential buyers of these items, the unit shall restrict the production of the
respective items.
GREENBELT AREA
27. The PP shall develop green belt within premises (908 Sq. m. i.e. 40 % of the total plot area)
as per the undertaking submitted before SEAC. Green belt shall be developed with native
plant species that are significant and used for the pollution abatement as per the CPCB
guidelines. It shall be implemented within 3 years of operation phase in consultation with
GPCB.
28. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 237 of 357
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
m) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.
n) Unit shall provide water sprinkler to the ammonia storage cylinder.
o) Unit shall provide chlorine leakage control emergency kit and FRP hood with
scrubber system for chlorine safety.
p) Unit shall provide safety valve and rapture disc, as well as auto dump or auto
quench/, suppress system for nitration vessel safety.
10 SIA/GJ/IND2/190442/2020
SOHANG PHARMA
Plot No - 621-P/21, Near Petl, GIDC Industrial Estate, Panoli, Bharuch
EC Reconsideration
Category of the unit: 5(f)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 238 of 357
Project status: New
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/190442/2020 on
dated 30.12.2020 for obtaining Environmental Clearance.
• Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment
Management Plan as per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th
March, 2020 regarding consideration of proposals or activities in respect of Active
Pharmaceuticals Ingredients (API) as B2 category.
• This is a new project proposed for manufacturing of synthetic organic chemicals [API and
API Intermediates] as tabulated below:
Sr. No.
Name of Product CAS NO. Quantity (MT/Mont
h) End Use Remarks
GROUP-A
1 2-(2-HYDROXY ETHOXY ETHYL PIPERAZINE) [HEEP]
13349-82-1
45.0
Intermediate of Quitiapine
Unit is proposed to mfg either individual or total production of (Product No.- 1 to 21) shall not exceed 45 MT/Month.
2 MANNICH HYDROCHLORIDE
42036-65-7
Intermediate of Tramadol
3 1-(3-DIMETHYLAMINOPROPYL)-3-ETHYLCARBODIIMIDE HYDROCHLORIDE [EDC HCL]
25952-53-8
Intermediate of gliptine
series
4 3-DI-METHYL AMINO 1-PROPYL CHLORIDE HYDROCHLORIDE OR 3-DI-METHYL AMINO 1-PROPYL CHLORIDE HYDROCHLORIDE SOLUTION
5407-04-5
Intermediate of Imipramine
5 1-(2,3-DICHLOROPHENYL)PIPERAZINE HCL
119532-26-2
Intermediate of Aripiprazole
6 1-(3-CHLOROPHENYL)-4-(3-CHLOROPROPYL) PIPERAZINE HCL
52605-52-4
Intermediate of Trazodone
7 DI-METHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE OR DI-METHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE
4584-46-7
Intermediate of
Chlorpheniramine
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 239 of 357
SOLUTION
8 DI-ETHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE
869-24-9 Intermediate
of Amiodarone
9 4- HYDROXY BENZYL ALCOHOL
623-05-2 Intermediate of Bisoprolol
Fumarat
10 THEOBROMINE
83-67-0 Intermediate of
Pentoxifylline
11 4-CHLORO 4–HYDROXY BENZOPHENONE
42019-78-3
Intermediate of Fenofibrate
12 2,4-DIFLUORO-ALPHA-(1H-1,2,4-TRIAZOLE) ACETOPHENONE
86404-63-9
Intermediate of Fluconazole
13 [ETHYL‐4‐(1‐HYDROXY‐1‐ METHYLETHYL)‐2‐PROPYL‐1‐{4‐[2‐ TRITYLTETRAZOLE‐5‐YL)PHENYL} METHYLIMIDAZOLE‐5‐CARBOXYLATE]
144690-33-5
Intermediate of Olmesartan
14 METHYL-6-CHLORO-4-HYDROXY-2-METHYL-2H-THIENO[2,3 E][1,2] THIAZINE-3- CARBOXYLATE-1,1-DIOXIDE
70374-51-5
Intermediate of Lornoxicam
15 2-CHLORO TRITYL CHLORIDE
42074-68-0
Intermediate of
Clotrimazole
16 METHYL-2-METHOXY-5-SULFAMOYL BENZOATE
33045-52-2
Intermediate of
Levosulpride
17 METHYL-3-AMINO CROTONATE
14205-39-1
Intermediate of Amlodipine
Besylate
18 (±)-3-(CARBAMOY METHYL)-5-METHYL HEXANOIC ACID
181289-33-8
Intermediate of Prgabalin
19 1,2,4-TRIAZOLO(4,3-A) PYRIDINE-3-(2H)-ONE
6969-71-7
Intermediate of Trazodone
20 1-(3-CHLOROPHENYL) PIPERAZINE
65369-76-8
Intermediate of Trazodone
21 OTBN(2-CYANO-4-METHYL BI PHENYL)
114772-53-1
Intermediate of Valsartan
GROUP-B
22 2-[4-[[4-METHYL-6-(1-METHYLBENZIMIDAZOL-
144701-48-4
15.0 Anti Hypertensive
Unit is proposed to
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 240 of 357
2-YL)-2-PROPYLBENZIMIDAZOL-1-YL]METHYL]PHENYL]BENZOIC ACID OR TELMISARTAN
mfg either individual or total production of (Product No.- 22 to 51) shall not exceed 15 MT/Month. 23 (5-METHYL-2-OXO-1,3-
DIOXOL-4-YL)METHYL 4-(2-HYDROXY-2-PROPANYL)-2-PROPYL-1-{[2'-(1H-TETRAZOL-5-YL)-4-BIPHENYLYL]METHYL}-1H-IMIDAZOLE-5-CARBOXYLATE OR OLMESARTAN
144689-63-4
Anti Hypertensive
24 6-HEPTENOIC ACID, 7-[4-(4-FLUOROPHENYL)-6-(1-METHYLETHYL)-2-[METHYL(METHYLSULFONYL)AMINO]-5-PYRIMIDINYL]-3,5-DIHYDROXY OR ROSUVASTATIN
287714-41-4
Used to to prevent heart and blood vessel disease
25 (2S)-1-[2-[(3-HYDROXY-1-ADAMANTYL)AMINO]ACETYL]PYRROLIDINE-2-CARBONITRILE OR VILDAGLIPTIN
274901-16-5
Anti Diabetic
26 2-(4-PROPAN-2-YLOXYPHENYL)-1-[3-PROPAN-2-YL-5-[(2S,3R,4S,5S,6R)-3,4,5-TRIHYDROXY-6-(HYDROXYMETHYL)OXAN-2-YL]OXY-1H-PYRAZOL-4-YL]ETHANONE OR REMOGLIFLOZIN
329045-45-6
Anti Diabetic
27 6-CHLORO-4-HYDROXY-2-METHYL-N-(2-PYRIDINYL)-2H-THIENO[2,3-E][1,2]THIAZINE-3-CARBOXAMIDE 1,1-DIOXIDE OR LORNOXICAM
70374-39-9
Anti Inflammatory
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 241 of 357
28 4-HYDROXY-2-METHYL-N-(5-METHYL-1,3-THIAZOL-2-YL)-2H-1,2-BENZOTHIAZINE-3-CARBOXAMIDE 1,1-DIOXIDE OR MELOXICAM
71125-38-7
Anti Inflammatory
29 10-OXO-10,11-DIHYDRO-5H-DIBENZO[B,F]AZEPINE-5-CARBOXAMIDE OR OXCARBAZEPINE
28721-07-5
Anticonvulsants
30 (2E)-[(4R)-4-(2,4-DICHLOROPHENYL)-1,3-DITHIOLAN-2-YLIDENE](1H-IMIDAZOL-1-YL)ACETONITRILE OR LULICONAZOLE
187164-19-8
Antifungal
31 (2R,3S)-2-(2,4-DIFLUOROPHENYL)-3-(5-FLUORO-4-PYRIMIDINYL)-1-(1H-1,2,4-TRIAZOL-1-YL)-2-BUTANOL OR VORICONAZOLE
137234-62-9
Antifungal
32 1-[2-[(7-CHLORO-1-BENZOTHIOPHEN-3-YL)METHOXY]-2-(2,4-DICHLOROPHENYL)ETHYL]IMIDAZOLE OR SERTACONAZOLE
99592-32-2
Antifungal
33 (2-BUTYL-1-BENZOFURAN-3-YL){4-[2-(DIETHYLAMINO)ETHOXY]-3,5-DIIODOPHENYL}METHANONE HYDROCHLORIDE (1:1) OR AMIODARONE HCL
19774-82-4
Anti-arrhythmic
34 1-(3-CHLOROPHENYL)-2-[(2-METHYL-2-PROPANYL)AMINO]-1-PROPANONE HYDROCHLORIDE (1:1)
31677-93-7
antidepressant
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 242 of 357
OR BUPROPION HCL
35 6-[3-(ADAMANTAN-1-YL)-4-METHOXYPHENYL]-2-NAPHTHOIC ACID OR ADAPALENE
106685-40-9
Anti Acne
36 8-CHLORO-11-(4-PIPERIDINYLIDENE)-6,11-DIHYDRO-5H-BENZO[5,6]CYCLOHEPTA[1,2-B]PYRIDINE OR DESLORATADINE
100643-71-8
Anti Histamine
37 2-[(2,3-DIMETHYLPHENYL)AMINO]BENZOIC ACID OR MAFENAMIC ACID
61-68-7 anti-inflammatory
38 1H-1,2,4-TRIAZOLE-1-ETHANOL, Α-(2,4-DIFLUOROPHENYL)-Α-(1H-1,2,4-TRIAZOL-1-YLMETHYL)- OR FLUCONAZOLE
86386-73-4
Antifungal
39 BENZENECARBOTHIOIC ACID, S-[(1Z)-2-[[(4-AMINO-2-METHYL-5-PYRIMIDINYL)METHYL]FORMYLAMINO]-1-[2-(PHOSPHONOOXY)ETHYL]-1-PROPEN-1-YL] ESTER OR BENFOTIAMINE
22457-89-2
used for Alzheimer disease, arthritis
40 1-[(2-CHLOROPHENYL)(DIPHENYL)METHYL]-1H-IMIDAZOLE OR CLOTRIMAZOLE
23593-75-1
Antifungal
41 (8S,9S,10R,13S,14S,17S)-17-ACETYL-10,13-DIMETHYL-1,2,6,7,8,9,10,11,12,13,14,15,16,17-TETRADECAHYDRO-3H-CYCLOPENTA[A]PHENANTHREN-3-ONE
57-83-0 Hormon
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 243 of 357
OR PROGESTERONE
42 DEXTROMETHORPHANHBR
125-68-8 cough suppressant
43 1-{4-[(2-ISOPROPOXYETHOXY)METHYL]PHENOXY}-3-(ISOPROPYLAMINO)-2-PROPANOL (2E)-2-BUTENEDIOATE (1:1) OR BISOPROLOL FUMERATE
104344-23-2
Anti hypertension
44 (S)-5-AMINOSULFONYL-N-[(1-ETHYL-2-PYRROLIDINYL)METHYL]-2-METHOXYBENZAMIDE OR LEVOSULPIRIDE
23672-07-3
Antipsychotic
45 4-AMINO-N-[(1-ETHYL-2-PYRROLIDINYL)METHYL]-5-(ETHYLSULFONYL)-2-METHOXYBENZAMIDE OR AMISULPRIDE
53583-79-2
Antiemitic
46 [3-(4-CHLOROPHENYL)-3-(2-PYRIDYL)PROPYL]DIMETHYLAMINE OR CHLORPHENERAMINE MALEATE
113-92-8 Antihistamine
47 2-[(2-AMINOETHOXY)-METHYL]-4-(2-CHLOROPHENYL)-1,4-DIHYDRO-6-METHYL-3,5- PYRIDINEDICARBOXYLIC ACID 3-ETHYL 5-METHYL ESTER BENZENE SULFONATE OR AMLODIPINE BESELATE
111470-99-6
Antihypertansive
48 5-CHLORO-N-(2-{4-[(CYCLOHEXYLCARBAMOYL)SULFAMOYL]PHENYL}ETHYL)-2-METHOXYBENZAMIDE OR GLIBENCLAMIDE
10238-21-8
Anti-diabetic
49 1H-PURINE-2,6-DIONE, 7- 69975- Used for
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 244 of 357
(1,3-DIOXOLAN-2-YLMETHYL)-3,7-DIHYDRO-1,3-DIMETHYL- OR DOXOPHYLLINE
86-6 prevention and treatment of asthma and COPD
50 3-[(1R)-1-HYDROXY-2-(METHYLAMINO)ETHYL]PHENOL;HYDROCHLORIDE OR PHENYLEPHRINE HCL
61-76-7 Used for the temporary relief of stuffy nose, sinus, and ear symptoms
51 S-(+)-3- AMINO METHYL)-
5-METHYL HEXANOIC
ACID
OR
PREGABALIN
148553-50-8
Fibromyalgia
52 R&D -- 0.1
Total 60.1
Specific End-use of each proposed products:
Sr. No.
Name of the Product CAS No. (Product)
Type/ Category of
Product (API/
Intermediate)
Name of API in which
Intermediate Used/
End use of said
Intermediate
CAS No. (API)
Said API is used
for/End Use of said
API
GROUP-A (Unit is proposed to mfg either individual or total production of Group - A (Product No.- 1 to 21) shall not exceed 45 MT/Month.)
1 2-(2-HYDROXY ETHOXY ETHYL PIPERAZINE) [HEEP]
13349-82-1
Intermediate (n-1)
Intermediate of Quitiapine
111974-69-7
Antidepressant
2 MANNICH HYDROCHLORIDE
42036-65-7
Intermediate (n-1)
Intermediate of Tramadol
27203-92-5
Opiate analgesic
3 1-(3-DIMETHYLAMINO-PROPYL)-3-ETHYL-CARBODIIMIDE HYDROCHLORIDE [EDC HCL]
25952-53-8
Intermediate (n-3)
Intermediate of gliptine series
25952-53-8
Antidiabatic
4 3-DI-METHYL AMINO 1-PROPYL CHLORIDE HYDROCHLORIDE
5407-04-5 Intermediate (n-1)
Intermediate of Imipramine
50-49-7 Antidepressants
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 245 of 357
OR 3-DI-METHYL AMINO 1-PROPYL CHLORIDE HYDROCHLORIDE SOLUTION
5 1-(2,3-DICHLOROPHENYL)PIPERAZINE HCL
119532-26-2
Intermediate (n-2)
Intermediate of Aripiprazole
129722-12-9
Antidepressant
6 1-(3-CHLOROPHENYL)-4-(3-CHLOROPROPYL) PIPERAZINE HCL
52605-52-4
Intermediate (n-1)
Intermediate of Trazodone
19794-93-5
Antidepressant
7 DI-METHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE OR DI-METHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE SOLUTION
4584-46-7 Intermediate (n-1)
Intermediate of Chlorpheniramine
132-22-9 Antihistamine
8 DI-ETHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE
869-24-9 Intermediate (n-1)
Intermediate of Amiodarone
1951-25-3
Anti-arrhythmic
9 4- HYDROXY BENZYL ALCOHOL
623-05-2 Intermediate (n-2)
Intermediate of Bisoprolol Fumarat
104344-23-2
Used to treat high blood pressure
10 THEOBROMINE 83-67-0 Intermediate (n-1)
Intermediate of Pentoxifylline
6493-05-6
Peripheral artery disease
11 4-CHLORO 4–HYDROXY BENZOPHENONE
42019-78-3
Intermediate (n-2)
Intermediate of Fenofibrate
49562-28-9
Antihyperlipidemic
12 2,4-DIFLUORO-ALPHA-(1H-1,2,4-TRIAZOLE) ACETOPHENONE
86404-63-9
Intermediate (n-1)
Intermediate of Fluconazole
86386-73-4
Anti allergies
13 [ETHYL‐4‐(1‐HYDROX
Y‐1‐ METHYLETHYL)‐2‐PR
OPYL‐1‐{4‐[2‐ TRITYLTETRAZOLE‐5‐YL)PHENYL} METHYLIMIDAZOLE‐5‐CARBOXYLATE]
144690-33-5
Intermediate (n-1)
Intermediate of Olmesartan
144689-63-4
Antihypertensive
14 METHYL-6-CHLORO-4-HYDROXY-2-
70374-51-5
Intermediate (n-3)
Intermediate of
70374-39-9
Anti-Inflammato
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 246 of 357
METHYL-2H-THIENO[2,3 E][1,2] THIAZINE-3- CARBOXYLATE-1,1-DIOXIDE
Lornoxicam ry
15 2-CHLORO TRITYL CHLORIDE
42074-68-0
Intermediate (n-2)
Intermediate of Clotrimazole
23593-75-1
Antifungal
16 METHYL-2-METHOXY-5-SULFAMOYL BENZOATE
33045-52-2
Intermediate (n-2)
Intermediate of Levosulpride
23672-07-3
Antipsychotic
17 METHYL-3-AMINO CROTONATE
14205-39-1
Intermediate (n-1)
Intermediate of Amlodipine Besylate
111470-99-6
Lowering blood pressure
18 (±)-3-(CARBAMOY METHYL)-5-METHYL HEXANOIC ACID
181289-33-8
Intermediate (n-2)
Intermediate of Prgabalin
148553-50-8
Fibromyalgia
19 1,2,4-TRIAZOLO(4,3-A) PYRIDINE-3-(2H)-ONE
6969-71-7 Intermediate (n-1)
Intermediate of Trazodone
19794-93-5
Antidepressant
20 1-(3-CHLOROPHENYL) PIPERAZINE
65369-76-8
Intermediate (n-2)
Intermediate of Trazodone
19794-93-5
Antidepressant
21 OTBN(2-CYANO-4-METHYL BI PHENYL)
114772-53-1
Intermediate (n-2)
Intermediate of Valsartan
137862-53-4
To treat a variety of cardiac conditions including hypertension, diabetic nephropathy and heart failure.
GROUP-B (Unit is proposed to mfg either individual or total production of Group - B (Product No.- 22 to 51) shall not exceed 15 MT/Month.)
22 2-[4-[[4-METHYL-6-(1-METHYLBENZIMIDAZOL-2-YL)-2-PROPYLBENZIMIDAZOL-1-YL]METHYL]PHENYL]BENZOIC ACID OR TELMISARTAN
144701-48-4
API -- -- Anti Hypertensive
23 (5-METHYL-2-OXO-1,3-DIOXOL-4-
144689-63-4
API -- -- Anti Hypertensi
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Page 247 of 357
YL)METHYL 4-(2-HYDROXY-2-PROPANYL)-2-PROPYL-1-{[2'-(1H-TETRAZOL-5-YL)-4-BIPHENYLYL]METHYL}-1H-IMIDAZOLE-5-CARBOXYLATE OR OLMESARTAN
ve
24 6-HEPTENOIC ACID, 7-[4-(4-FLUOROPHENYL)-6-(1-METHYLETHYL)-2-[METHYL(METHYLSULFONYL)AMINO]-5-PYRIMIDINYL]-3,5-DIHYDROXY OR ROSUVASTATIN
287714-41-4
API -- -- Used to to prevent heart and blood vessel disease
25 (2S)-1-[2-[(3-HYDROXY-1-ADAMANTYL)AMINO]ACETYL]PYRROLIDINE-2-CARBONITRILE OR VILDAGLIPTIN
274901-16-5
API -- -- Anti Diabetic
26 2-(4-PROPAN-2-YLOXYPHENYL)-1-[3-PROPAN-2-YL-5-[(2S,3R,4S,5S,6R)-3,4,5-TRIHYDROXY-6-(HYDROXYMETHYL)OXAN-2-YL]OXY-1H-PYRAZOL-4-YL]ETHANONE OR REMOGLIFLOZIN
329045-45-6
API -- -- Anti Diabetic
27 6-CHLORO-4-HYDROXY-2-METHYL-N-(2-PYRIDINYL)-2H-THIENO[2,3-E][1,2]THIAZINE-3-CARBOXAMIDE 1,1-DIOXIDE OR LORNOXICAM
70374-39-9
API -- -- Anti Inflammatory
28 4-HYDROXY-2-METHYL-N-(5-METHYL-1,3-THIAZOL-
71125-38-7
API -- -- Anti Inflammatory
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 248 of 357
2-YL)-2H-1,2-BENZOTHIAZINE-3-CARBOXAMIDE 1,1-DIOXIDE OR MELOXICAM
29 10-OXO-10,11-DIHYDRO-5H-DIBENZO[B,F]AZEPINE-5-CARBOXAMIDE OR OXCARBAZEPINE
28721-07-5
API -- -- Anticonvulsants
30 (2E)-[(4R)-4-(2,4-DICHLOROPHENYL)-1,3-DITHIOLAN-2-YLIDENE](1H-IMIDAZOL-1-YL)ACETONITRILE OR LULICONAZOLE
187164-19-8
API -- -- Antifungal
31 (2R,3S)-2-(2,4-DIFLUOROPHENYL)-3-(5-FLUORO-4-PYRIMIDINYL)-1-(1H-1,2,4-TRIAZOL-1-YL)-2-BUTANOL OR VORICONAZOLE
137234-62-9
API -- -- Antifungal
32 1-[2-[(7-CHLORO-1-BENZOTHIOPHEN-3-YL)METHOXY]-2-(2,4-DICHLOROPHENYL)ETHYL]IMIDAZOLE OR SERTACONAZOLE
99592-32-2
API -- -- Antifungal
33 (2-BUTYL-1-BENZOFURAN-3-YL){4-[2-(DIETHYLAMINO)ETHOXY]-3,5-DIIODOPHENYL}METHANONE HYDROCHLORIDE (1:1) OR AMIODARONE HCL
19774-82-4
API -- -- Anti-arrhythmic
34 1-(3-CHLOROPHENYL)-2-[(2-METHYL-2-
31677-93-7
API -- -- antidepressant
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 249 of 357
PROPANYL)AMINO]-1-PROPANONE HYDROCHLORIDE (1:1) OR BUPROPION HCL
35 6-[3-(ADAMANTAN-1-YL)-4-METHOXYPHENYL]-2-NAPHTHOIC ACID OR ADAPALENE
106685-40-9
API -- -- Anti Acne
36 8-CHLORO-11-(4-PIPERIDINYLIDENE)-6,11-DIHYDRO-5H-BENZO[5,6]CYCLOHEPTA[1,2-B]PYRIDINE OR DESLORATADINE
100643-71-8
API -- -- Anti Histamine
37 2-[(2,3-DIMETHYLPHENYL)AMINO]BENZOIC ACID OR MAFENAMIC ACID
61-68-7 API -- -- Anti-inflammatory
38 1H-1,2,4-TRIAZOLE-1-ETHANOL, Α-(2,4-DIFLUOROPHENYL)-Α-(1H-1,2,4-TRIAZOL-1-YLMETHYL)- OR FLUCONAZOLE
86386-73-4
API -- -- Antifungal
39 BENZENECARBOTHIOIC ACID, S-[(1Z)-2-[[(4-AMINO-2-METHYL-5-PYRIMIDINYL)METHYL]FORMYLAMINO]-1-[2-(PHOSPHONOOXY)ETHYL]-1-PROPEN-1-YL] ESTER OR BENFOTIAMINE
22457-89-2
API -- -- Used for Alzheimer disease, arthritis
40 1-[(2-CHLOROPHENYL)(DIPHENYL)METHYL]-1H-IMIDAZOLE OR CLOTRIMAZOLE
23593-75-1
API -- -- Antifungal
41 (8S,9S,10R,13S,14S,17 57-83-0 API -- -- Hormon
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S)-17-ACETYL-10,13-DIMETHYL-1,2,6,7,8,9,10,11,12,13,14,15,16,17-TETRADECAHYDRO-3H-CYCLOPENTA[A]PHENANTHREN-3-ONE OR PROGESTERONE
42 DEXTROMETHORPHAN HBR
125-68-8 API -- -- cough suppressant
43 1-{4-[(2-ISOPROPOXYETHOXY)METHYL]PHENOXY}-3-(ISOPROPYLAMINO)-2-PROPANOL (2E)-2-BUTENEDIOATE (1:1) OR BISOPROLOL FUMERATE
104344-23-2
API -- -- Anti hypertension
44 (S)-5-AMINOSULFONYL-N-[(1-ETHYL-2-PYRROLIDINYL)METHYL]-2-METHOXYBENZAMIDE OR LEVOSULPIRIDE
23672-07-3
API -- -- Antipsychotic
45 4-AMINO-N-[(1-ETHYL-2-PYRROLIDINYL)METHYL]-5-(ETHYLSULFONYL)-2-METHOXYBENZAMIDE OR AMISULPRIDE
53583-79-2
API -- -- Antiemitic
46 [3-(4-CHLOROPHENYL)-3-(2-PYRIDYL)PROPYL]DIMETHYLAMINE OR CHLORPHENERAMINE MALEATE
113-92-8 API -- -- Antihistamine
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47 2-[(2-AMINOETHOXY)-METHYL]-4-(2-CHLOROPHENYL)-1,4-DIHYDRO-6-METHYL-3,5- PYRIDINEDICARBOXYLIC ACID 3-ETHYL 5-METHYL ESTER BENZENE SULFONATE OR AMLODIPINE BESELATE
111470-99-6
API -- -- Antihypertansive
48 5-CHLORO-N-(2-{4-[(CYCLOHEXYLCARBAMOYL)SULFAMOYL]PHENYL}ETHYL)-2-METHOXYBENZAMIDE OR GLIBENCLAMIDE
10238-21-8
API -- -- Anti-diabetic
49 1H-PURINE-2,6-DIONE, 7-(1,3-DIOXOLAN-2-YLMETHYL)-3,7-DIHYDRO-1,3-DIMETHYL- OR DOXOPHYLLINE
69975-86-6
API -- -- Used for prevention and treatment of asthma and COPD
50 3-[(1R)-1-HYDROXY-2-(METHYLAMINO)ETHYL]PHENOL;HYDROCHLORIDE OR PHENYLEPHRINE HCL
61-76-7 API -- -- Used for the temporary relief of stuffy nose, sinus, and ear symptoms
51 S-(+)-3- AMINO METHYL)-5-METHYL HEXANOIC ACID OR PREGABALIN
148553-50-8
API -- -- Fibromyalgia
• During the meeting dated 15.04.2021, Project proponent (PP) and their Technical Expert
from M/s. Ozone Enviro Tech remained present during video conference meeting.
• The technical expert informed the Committee that their application for sub-plotting is yet to
be approved by GIDC.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 252 of 357
• After deliberation, SEAC unanimously decided to defer the proposal and consider the
same in one of the upcoming meeting of SEAC upon submission of approval of GIDC
in the matter of sub-plotting.
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Ozone Enviro Tech remained
present during video conference meeting.
• Revised Salient features of the project submitted as under:
Sr. no. Particulars Details
A-1 Total cost of Proposed Project (Rs. in Crores):
3.5 Crores
Break-up of proposed project Cost:
Sr. No.
Particulars Estimated Cost
(INR In Lakhs)
1 Land and Site Development 60
2 Building 70
3 Plant and Machineries 130
4 Environment protection measures (includes cost of ETP, Tree Plantation, etc.)
90
Total 350
A-2 Details of Environmental Management Plan (EMP) As below:
Details of EMP
Sr. No
Unit Installed Capacity
(KLD)
Capital Cost (Rs. In Lakhs )
Operating Cost
(Lacs/Year)
Maintenance Cost
(Lacs/Year)
Total Recurring
Cost (Lacs/Year)
1 Waste Water ETP (Primary) 20.0 KLD
16.0 183.60 -- 183.60
2 Air 26.5 -- 3.40 3.40
3 Hazardous Management
6.0 46.47 -- 46.47
4 Fire & Safety 15.0 -- 3.20 3.20
5 AWH Monitoring
1.0 -- 1.00 1.00
6. Green Belt Development
1.41 -- 1.20 1.20
7. Occupational Health
1.00 -- 1.85 1.85
8. CER Year 2021- 14.00 -- -- --
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2023
Total 90.91 230.07 10.65 240.72
Summary
Cost of Project in Crores per Annum: 3.5 Cr.
EMP Capital Cost in Crores per Annum and Percentage: 0.90 Cr. (25.71%)
EMP Recurring Cost in Crores per Annum and Percentage: 2.40Cr
--
A-3 Details of CER as per OM dated 01/05/2018 As below:
As per OM no. 22-65/2017 on dated 01/05/2018 regarding “Corporate Environment Responsibility”
(CER), Greenfield projects have to contribute 2% (Rs. 7.0 Lack) of the Capital Investment (3.5 Cr).
But as per New Mechanism of CPCB vide letter no CPCB/IPC-VII/CEPI/NGT/2019 on dated
25/10/2019, we shall commit to do 4% (Rs. 14 Lack) of Project Cost as a CER. Our CER activity are
as below table…
Component As per Norms Allocation
CER Rs. 7.0 Lakhs (2 %) Rs. 14 Lakhs (4 %)
Activities to be carried out under CER:
CER Activities Fund (Rs.)
2021-2022
Provided Solar street light set with battery backup (18W -14 Nos.) in Alonj Village
4,00,000/-
2022-2023
Company will provide R.O. Plant (Cap. 2000 Liter/hr) with drinking water storage tank in Alonj Village.
4,00,000/-
2023-2024
Supply & Installation of Organic Waste Converter (OWC) having capacity of 500 Kg with four side closed shed room in Alonj Village.
6,00,000/-
TOTAL 14,00,000 /-
-
B Land / Plot ownership details:
B-1 Total Plot area ( sq. meter) 1174.10 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Sr. No.
Description Gr. Floor
Area Sq. Meter
First Floor B/U Area Sq. Meter
Second Floor B/U
Area Sq. Meter
1 Production Area 80 80 80
2 Raw Material Storage Area 100 -- --
3 Finish Product Storage Area 30 -- --
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4 Haz. Waste Storage Area 120 -- --
5 Boiler Area 80 -- --
6 ETP 50 -- --
7 Admin Building & OHC Room 30 30 30
8 Green Belt Area (40%) (Inside – 256 + Outside - 214) 256
-- --
9 Hydrogen Storage Area 10
10 Gas Storage Area 20 -- --
11 Road & Open Area 388.1 -- --
12 Security Cabin 10 -- --
TOTAL 1174.10
--
B-3 Green belt area ( sq. meter)
470 Sq. m.(40% of total area) Inside - 256 Se. Meter Outside - 214 Sq. meter
C Employment generation 25 Nos
D Water
D-1
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Water Supply
Status of permission from the concern authority.
D-2 Water consumption (KLD)
Category Quantity
KLD Remarks
(P) Domestic 3.0
(Q) Gardening 3.0
(R) Industrial
Process 16.4
Washing 1.0
Boiler 10.0
Cooling 6.0
Others (Scrubber) 2.0
Scrubber 2.8
R&D 0.2
Industrial Total 38.4
Total (A + B + C) 44.4
--
Brief Note on worst case scenario for water consumption: Worst case scenario for water consumption are in Group A (Product No. 6 - 11.25 KLD) & Group B (Product No. 23 - 5.15 KLD)
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Summary of water requirement Quantity
KLD Remarks
Total water requirement for the project (A) 44.4
Quantity to be recycled (B) 15.3
Total fresh water requirement (C) 29.1
Ensure Total water requirement = Fresh water + Recycled water
(44.4 = 29.1 + 15.3)
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]
Source of waste water for reuse in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
1.5 KLD Domestic effluent
Gardening Purposed
BOD-30 --
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle.
D-3 Waste water generation (KLD)
Category Waste water
KLD Remarks
(I) Domestic 2.5
(J) Industrial
Process 12.2
Washing 1.0
Boiler 1.0
Cooling 0.6
Others (Scrubber) 2.0
Scrubber 4.4
R&D 0.2
Total Industrial waste water
21.4
Total [A + B] 23.9
-
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative): Worst case scenario for water consumption are in Group A (Product No. 13 - 7.80 KLD) & Group B (Product No. 47 - 4.42 KLD)
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (If any applicable to proposal).
➢ Not Applicable
D-4 Mode of Disposal & Final meeting point
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Domestic: 2.5 KL/Day Domestic effluent will be sent to STP and reused for gardening purposed.
Industrial: 17 KLD Effluent from process and utility will be treated into primary ETP and primary treated effluent send to common MEE for the final treatment and disposal. 4.4 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9 Permission.
-
D-5 Treatment facility within premises with capacity
For Domestic waste water: Capacity of STP: STP is not provided because domestic effluents send to low COD steam ETP.
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ➢ ETP (Primary ) : 20 KLD
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.)
Sr. No.
Parameter
Characteristics(mg/L)
Primary treated Process
Boiler blow down
Cooling Tower blow down
Washing Compo
site
1 pH 3-9 8 - 8.5 8 - 8.5 5.5 - 8.5 3-9 6.5-7.5
2 TDS 28000 350 250 1000 28000 28700
3 TSS 500 250 350 200 500 75
4 COD 20000 70 100 600 20000 13000
5 BOD3 700 20 30 200 700 490
--
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ Not Applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Industrial:- 17 KLD Effluent from process and utility will be treated into primary ETP and primary
treated effluent send to common MEE for the final treatment and disposal. 4.4 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9 Permission.
Domestic:- 2.5 KLD domestic effluent will be sent to STP and reused for gardening purposed.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.Name of Common facility (CF) (For waste water treatment)
➢ Common MEE of M/s BEIL, Ankleshwer
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Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
➢ M/s. BEIL, Ankleshwar for Common MEE
D-7 Simplified water balance diagram with reuse / recycle of waste water
E Air
E-1 Brief Note on fuel based heat energy requirement and worst case scenario thereof:
SR. NO. NAME OF FUEL QUANTITY
1. Briquette of Bio Coal 8 MT/Day
2. HSD 25 Lit/hr
Power Requirements: Proposed: Power required from DGVCL is 500 KW. Standby power supply from D.G. set (250 KVA) in emergency case. --
E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC’s OM vide dated 31.10.2019)
-
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Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions i.e.
Air Pollutant
s
Air Pollution Control
Measures (APCM)
1 Boiler (Cap. - 1.5 MT/hr)
30
9.16 B
riqu
ette
of
Bio
Co
al
9.17 5
M
T/
D
ay
PM SO2 NOx
Multicyclone Separator
9.18 Wi
th Water
Scrubber
2
Thermic Fluid Heater (Cap. - 2 Lakh Kcal/ Hr)
9.19 B
riqu
ette
of
Bio
Co
al
3 MT/Day
Multicyclone Separator
9.20 Wi
th Water
Scrubber
3
D.G. Sets (Stand by) (Cap. – 250 KVA)
18 9.21 H
SD
9.22 2
5
Lit
er
/h
r
9.23 A
dequate
Stack
Height
-
E-3 Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx
etc.)
-
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emission
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
1 Process Vent -1 (Chlorination/Sulphonation) Product No. 7
HCl SO2
11 Two stage Scrubber
(Water + Alkali)
2 Process Vent -2 Product No.18
NH3 11 Two stage water
Scrubber
3 Process Vent -3 Product No.21
Cl2 11 Two stage Alkali
Scrubber
4 Process Vent -4 Product No. 34
HBr 11 Two stage Alkali
Scrubber
Note:
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➢ Details of gaseous raw materials used in proposed project – Hydrogen, Ammonia & Bromine are used
➢ Estimation of process gas emission (Product wise and Total) - Worst case for chlorination is product no- 2&4, for Bromination is product no-4, for Ammonification is product no-24
➢ Requirement of the scrubbing media (KL per Day) considering solubility (Product wise and Total)
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its sound management in HW matrix.
E-4 Fugitive emission details with its mitigation measures:
Following measures will be adopted to prevent and control fugitive emissions…
➢ Solid raw material charging will be done through closed system to avoid fugitive emissions. ➢ Airborne dust at all transfers operations/ points will be controlled either by spraying water or
providing enclosures. ➢ Adequate ventilation will be provided. ➢ Periodic monitoring of work area will be carried out to check the fugitive emission. ➢ Minimum number of flanges, joints and valves in pipelines. ➢ Regular inspection of floating roof seals and proper preventive maintenance of roofs and
seals for tanks. ➢ Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer
area will be collected through hoods and ducts by induced draft and controlled by scrubber/ dust collector / bad filter.
➢ Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
F Hazardous waste management matrix (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Sr. no.
Type/Name of Hazardous waste
Specific Source of generation
(Name of the Activity,
Product etc.)
Category & Schedule as
per HW Rules.
Quantity (MT/
Annum)
Management of HW
1 ETP Sludge ETP SCH-I/35.3 90 Collection, Storage, Transportation and Disposal at common TSDF site.
2 Discarded Drums/Bags/
Raw Materials/
SCH-I/33.1 70 Collection, Storage, Transportation,
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Liners Products Decontamination & Sale to GPCB approved vendors/ reuse /send back to supplier.
3 Used/ Spent Oil
Machineries/Utility
SCH-I/5.1 3.6 Collection, Storage, Disposal by reuse in plant machinery as lubricant or transportation & Sale to GPCB registered re-processor.
4 Distillation Residue
Distillation SCH-I/20.3 55 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
5 Spent Solvent
Process SCH-I/28.6 2100 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
6 Spent Carbon + Hyflo
Process SCH-I/28.3 39 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
7 Organic Residue
Process SCH-I/28.1 185 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
8 Inorganic salt Process SCH-I/28.1 65 Collection, Storage, Transportation and sent for co-processing in cement industries or Disposal at common TSDF Site .
9 Spent Catalyst
Process SCH-I/28.1 19 Collection, Storage, reuse in the plant premises or Transportation and send to regenerator under Rule-9.
10 Potassium Bromide solution
Process (Product No.
22)
SCH-I/28.1 73 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
11 Hydrogen Process SCH-I/28.1 288 Collection, Storage,
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Bromide solution
(Product No. 49)
Transportation and Sell to end user who is having Rule-9 Permission.
12 Sodium sulphate solution
Process (Product No.
31)
SCH-I/28.1 90 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
13 Aluminum chloride
Process (Product No.
11)
SCH-I/28.1 851 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
14 Phosphoric acid
Process (Product No.
42)
SCH-I/28.1 1332 Collection, Storage and reuse in plant premises. (Requirement of Phosphoric acid in Product No. 42 – 1332 MT/Year).
15 Dilute HCl (28%)
Process (Product No.-
5,47) +
Scrubber (Product No.-
7)
SCH- II / B 15
572 +
675 = 1247
Collection, Storage and reuse in plant premises. (HCl reused in Product No. 5 - 540 MT/Year) and remaining sell to end user who is having Rule-9 Permission.
16 Sodium bi sulphite (30%)
Scrubber (Product No.-
7)
SCH- II / B 15
411 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
17 Sodium Bromide (25%)
Process (Product No.-
6) +
Scrubber (Product No.-
34)
SCH- II / B 15
630 +
4 = 634
Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
18 Liq. Ammonia (25%)
Process (Product No.-
48) + Scrubber
(Product No.- 18)
SCH- II / B 15
56 +
151= 207
Collection, Storage and reuse in plant premises. (Requirement of Liq. Ammonia in Product No. 12 – 270 MT/Year).
19 Sodium hypo chloride (20%)
Scrubber (Product No.-
21)
SCH- II / B 15
332 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
20 Off Specification Products
From mfg. Process (Batch failure)
SCH-I/28.4 10 Collection, Storage, Transportation and sent for co-processing in cement industries (in case of non-operation of co-processing
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site) Disposal at common incineration site.
R&D
21 ETP Sludge ETP 35.3 3.0 Collection, Storage, Transportation & disposal in TSDF.
22 Residue from Distillation/ Organic Process Waste
R&D 28.1 4.0 Collection, Storage, Transportation & send to cement industries for co-processing or incineration in CHWIF.
23 Discarded Drum
Raw Materials/Pro
ducts
33.1 20 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
24 Discarded Bags / Liner
Raw Materials/Pro
ducts
33.1 0.2 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
25 Off Specification Products
R&D 28.4 1.0 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.
-
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Ankleshwar for Common TSDF & CHWIF
F-3 Details of Non-Hazardous waste & its disposal (MSW and others)
Not Applicable
G Solvent management, VOC emissions etc.
G-1 Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)
SOLVENT RECOVERY AFTER LDAR
Sr. No.
Type of Solvent
% Recovery
% Losses
Air Water Haz
1 Acetic Acid 96.13 0.95 1.22 0.92
2 Benezene 96.20 0.93 1.55 0.89
3 Hexan 96.42 0.97 1.42 0.94
4 DMF 96.27 0.98 1.34 0.90
5 MDC 96.05 0.96 1.49 0.95
6 EDC 96.69 0.93 1.24 0.96
7 IPA 96.53 0.97 1.48 0.93
Justification of Reuse of solvent
Name of Solvent Total
requirement Total quantity of solvent
recovered
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MT/Month MT/Month
Acetic Acid 49.05 47.15
Benezene 82.80 79.65
Hexan 41.38 39.90
DMF 37.50 36.10
Methanol 88.88 85.50
EDC 40.80 39.45
IPA 70.65 68.20
--
G-2 Brief Note on LDAR proposed:
➢ Company will be installed double mechanical seal and MSW Gaskets in solvent pipelines to prevent leakage from flanges
➢ Company will be reduced the joints and valves in pipelines. ➢ All the rotating equipment like pumps will be installed with double Mechanical Seals to arrest
any sort of emissions. ➢ Flanges will be sealed so less losses will be there. ➢ Down the Temperature of Cooling tower to 5 0C ➢ Chilled Brine at -10 0C will be used to trap any traces of Solvent which is slipped from
Secondary condenser. ➢ Closed loop system. ➢ For continue vapor travelling 100mm of Hg (slight vacuum) will be applied on secondary
condenser. --
G-3 VOC emission sources and its mitigation measures (Brief note on LDAR)
➢ Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.
➢ Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.
➢ To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps.
➢ Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with on-line pH meter with hooter system for better operational control.
➢ Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers.
➢ All the raw materials will be pneumatically transfer to the reactor. ➢ Emphasis will be given to solvent management/solvent loss prevention. ➢ Control by having proper scrubbing system. ➢ Condenser to trap VOC. ➢ Proper gland packing will be maintained for pumps and valves and to the extent possible
pumps with mechanical seal.
H Safety Detail
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
Storage details Name of major Hazardous chemicals
Remarks
Storage tanks (If any) --
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Drums/Bags Acetone/ Liquid Ammonia/ MDC/ Hexane/ Acetonitrile/ THF/ Ethyl Acetate
Cylinder Ammonia, Hydrogen,
Bottle Bromine
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
➢ FLP type light fittings will be provided. ➢ Proper ventilation will be provided in Godown. ➢ Proper label and identification board /stickers will be provided in the storage area. ➢ Conductive drum pallets will be provided. ➢ Drum handling trolley / stackers/fork lift will be used for drum handling. ➢ Separate dispensing room with local exhaust and static earthing provision will be made. ➢ Materials will be stored as per its compatibility study and separate area will be made for
flammable, corrosive and toxic chemical drums storage. ➢ Smoking and other spark, flame generating item will be banned from the Gate.
Applicability of PESO : Company will apply for PESO after getting EC if applicable
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of Process
Safety measures including Automation
Hydrogenation ➢ Installed DCS System ➢ FLP type area will be provided. ➢ Total enclosed process system. ➢ Instrument & Plant Air System. ➢ Nitrogen blanketing in Hydrogenation reactor. ➢ Safety valve and Rupture disc provided on reactor. ➢ Cooling Chilling and power alternative arrangement have been
made on reactor. ➢ Hydrogen and Nitrogen Cylinder bank away from the auto clave
reactor. ➢ PRV station with shut off valve, safety valve provision will be
made for hydrogenation reaction safety. ➢ Before Hydrogen Gas charging in to reactor and after completion
of reaction Nitrogen flushing will be done. ➢ Flame arrestor will be provided on vent line of reactor and it will
be extended up to roof level. ➢ Open well ventilated and fragile roofs will be provided to on
reactor. ➢ Safe Catalyst charging method will be adopted. ➢ SOP will be prepared and operators will be trained for the same. ➢ Static earthing and electric earthing (Double) provided. ➢ Reactor vent extended outside the process area and flame
arrestor provided on vent line.
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➢ Dumping vessel arrangement will be made. ➢ Dumpers for static earthing on pipeline flanges of flammable
chemical will be provided.
Bromination ➢ Bromine handling areas will be clearly marked and restricted to qualified, trained personnel only.
➢ Bromine process area will be done with good ventilation ➢ We will maintain bromine vapor concentration in the work area to
less than 0.1 ppm with adequate exhaust hoods, ventilation systems and scrubbers. Analyze air for proper control.
➢ Transfer or repackage bromine only in a controlled, closed environment.
➢ Exhaust ventilating systems will be used in enclosed areas where bromine is handled.
➢ Personal Protective Equipments are to be made compulsory when handling Bromine
Ammonia ➢ Valve, pipeline will be checked and maintain, in good condition. ➢ All Gaskets will be checked periodically & if new one replaces
found defective. ➢ Joints will be checked regularly to found any Leakage. ➢ ADEQUATE PPE will be kept to handle the Hazard. ➢ ISI Portable fire extinguisher & Hydrant line will be provided as
per TAC norms. ➢ Sufficient amount of sand/soil are kept to control any spillage. ➢ Flame proof fitting provided. ➢ Eye washer cum shower will be provided near tank-farm area. ➢ Spark arrester will be installed on all vehicles inside the premises. ➢ SBA set, Canister mask and airline mask will be provided. ➢ Earthing& bonding on tanks will be provided. ➢ Vent line dipped in water will be provided.
--
H-3 Details of Fire Load Calculation
-
Total Plot Area: 1174.10
Area utilized for plant activity: 240
Area utilized for Hazardous Chemicals Storage: 360
Number of Floors: G+2
Water requirement for firefighting in KL/hr: 2.2
Water storage tank provided for firefighting in KL 100
Details of Hydrant Pumps: One Fire pump, One diesel driven pump and one Jockey pump are being implemented.
Nearest Fire Station : Panoli GIDC - 0.91 Km
Applicability of Off Site Emergency Plan: N.A
-
H-4 Details of Fire NOC/Certificate: Company will apply for Fire NOC/Certificate after getting EC if applicable
H-5 Details of Occupational Health Centre (OHC):
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-
Number of permanent Employee : 14
Number of Contractual person/Labour : 11
Area provided for OHC: 15 Sq. Meter provided in Ground Floor at Admin Building
Number of First Aid Boxes : 2
Nearest General Hospital : Welcare Hospital – 3.00 KM
Name of Antidotes to be store in plant :
--
• Committee discussed on the following:
✓ Land breakup area was discussed. Risk and hazardous waste management was discussed. EMP and Green belt development was discussed.
• Later on PP vide their e-mail dated 01-09-2021 has submitted revised CER details, Green belt development, Inclusion of Water Sprinkler in Fire and safety provisions .
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon’ble
Supreme Court of India in Civil Appeal no. 8478/2020 regarding operation of the
Hon’ble NGT orders dated 10/07/2019 & 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change
in product mix, after the 30th September 2020, considered as per the provisions in
force at that time as mentioned in the Notification vide S.O. 1223 (E) dated
27/03/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical
Ingredients (API) as per the amended EIA Notification vide S.O. 1223 (E) dated
27/03/2020 and any subsequent amendments.
4. PP shall submit six monthly compliance report of Environmental Clearance without
fail and the same shall be critically assessed by the regulatory authority.
5. Total number of products manufacturing shall not exceeding two-three (2-3) at a
given point of time as per the plant capacity shown in plant layout.
6. (a) R & D products shall be of similar chemistry in line with the EIA Notification vide
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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S.O. 1223 (E) dated 27/03/2020 and the pollution load shall remain the same as
committed. (b) Project proponent shall not take continuous/commercial production of
the R & D materials. Necessary approvals shall be obtained from the concern
authorities prior to commercial production of R & D materials. (c) Unit shall submit
relevant details of R & D products like raw materials, its safety measures to the
regulatory authority well before R & D activity. (d) Unit shall submit relevant details of
R & D products like different wastes generated (Quantity & Quality) and its
management to the regulatory authority within a month of R & D activity.
7. Unit shall install CEMS [Continuous Emission Monitoring System] in line to
CPCB directions to all SPCB vide letter no. B-29016/04/06PCI-1/5401 dated
05/02/2014 for effluent discharge and air emission as per pollutants
discharge/emission from respective project and an arrangement shall also be done
for reflecting the online monitoring results on the company's server, which can be
assessable by the GPCB/CPCB on real time basis. [For Small/Large/Medium (Red
Category) & Whichever (Air emission & Effluent discharge) is applicable].
8. Close loop solvent recovery system with adequate condenser system shall be
provided to recover solvent vapours in such a manner that recovery shall be
maximum and recovered solvent shall be reused in the process within premises.
9. Leak Detection and Repair (LDAR) program shall be prepared and implemented as
per the CPCB guidelines. LDAR Logbooks shall be maintained
WATER
10. Total water requirement for the project shall not exceed 44.4 KLD. Unit shall reuse
15.3 KLD of treated industrial effluent within premises. Hence, fresh water
requirement shall not exceed 29.1 KLD and it shall be met through GIDC only.
11. The industrial effluent generation from the project shall not exceed 21.4 KLD.
12. 17 KLD Effluent from process and utility will be treated into primary ETP and primary
treated effluent send to common MEE for the final treatment and disposal. 4.4 KLD
Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9
Permission.
13. Treated waste water shall be sent to common facilities (CETP, Common MEE, Spray
dryer etc.) only after complying with the inlet norms of common facilities prescribed
by GPCB to ensure no adverse impact on Human Health and Environment.
14. Domestic wastewater generation shall not exceed 2.5 KL/day for proposed project
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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and it shall be treated in STP. Treated sewage shall be utilized for gardening and
plantation purpose within premises after achieving on-land discharge norms
prescribed by the GPCB.
15. During monsoon season when treated sewage may not be required for the plantation
/ Gardening / Green belt purpose, it shall be stored within premises. There shall be
no discharge of waste water outside the premises in any case.
16. Unit shall provide buffer water storage tank of adequate capacity for storage of
treated waste water during rainy days.
17. During monsoon season, PP shall use treated effluent in fermentation process after
advanced treatment.
AIR
18. Unit shall not exceed fuel consumption and provide APCM and Stack height as
mentioned in flue gas matrix.
19. Unit shall provide APCM and stack height as mentioned in process gas matrix.
20. PP shall use approved fuels only as fuel in boilers.
21. Two stage Scrubber (Water + Alkali) shall be provided for control of Process gas
emission.
HAZARDOUS & SOLID WASTE
22. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
23. The unit shall submit the list of authorized end users of hazardous wastes along with
MoU signed with them at least two months in advance prior to the commencement of
production. In the absence of potential buyers of these items, the unit shall restrict the
production of the respective items.
GREENBELT AREA
24. The PP shall develop green belt [256 m2 (21.80%) inside plant premises + 214 m2
(22.59%) at Block No. 82, 83 & 106, Village Gabheni, Surat = Total: 470 Sq. m.) i.e.
40.03 % of total plot area ] as per the undertaking submitted before SEAC. Green
belt shall be developed with native plant species that are significant and used for the
pollution abatement as per the CPCB guidelines. It shall be implemented within 3
years of operation phase in consultation with GPCB.
25. Safety & Health:
a) Unit shall obtain all required permissions from the Narcotics Control Bureau for
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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manufacturing, storage and handling of Acetic Anhydride & any such chemicals
b) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
c) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
d) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
e) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
f) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
g) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labour within premises.
j) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
k) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
l) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
m) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.
n) Unit shall Store Bromine Bottle in cool dry separate area, out of direct sunlight
o) Unit shall provide water sprinkler to the ammonia storage cylinder.
11 SIA/GJ/IND2/57830/2018
YES CHEM
Survey No. 830, indrad, Kadi, Mehsana
EC Reconsideration
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Category of the unit: 5(f)
Project status: New
• Project proponent (PP) has submitted online application vide no.
SIA/GJ/IND2/57830/2018dated 17.11.2020 for obtaining Environmental Clearance.
• SEIAA issued TOR to PP vide their letter dated 01/11/2018.
• Project proponent has submitted EIA Report prepared by Green Circle Inc based on the
TOR issued by SEIAA.
• Public Hearing of the Project was carried out by Gujarat Pollution Control Board on
06/10/2020 at Survey No. 830, Village: indrad, Taluka: Kadi, Dist. Mehsana.
• This is a new project proposes for manufacturing of synthetic organic chemicals (dyes and
dyes intermediates) as below:
• The project falls under B1 category of project activity 5(f) as per the schedule of EIA
Notification 2006.
• PP was called for presentation on SEAC video conference meeting dated 02.02.2021.
• During the SEAC Video conference meeting dated 02.02.2021, Project Proponent (PP) and
their technical expert and EIA consultant from Green Circle Inc.remain present and made
technical presentation before the Committee.
• During the meeting, the project was appraised based on the information furnished in the EIA
Report, issues raised during public hearing and details presented during the meeting.
• Committee also deliberated on area expert members and EIA co-coordinators engaged in
preparation of EIA/EMP report and Details/information provided in the EIA report.
• The baseline environmental quality has been assessed for various components of the
environment viz. air, noise, water, biological and socioeconomic aspect. The baseline
SR.
NO PRODUCT NAME CAS No.
Total proposed
Product
MT/Month
END Use
1 Resist Salt 127-68-4 160
Dyes and
Dyes
Intermediates
2 Metanilic Acid 121-47-1 100
3 Aniline 2-4 Disulphonic Acid 137-51-9 50
4 Aniline 2-5 Disulphonic Acid 98-44-2 50
5 Sulfalinic Acid 121-57-3 100
Total 460
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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environmental study has been conducted for the study area of 10 km radial distance from
project site for the period March 2018 to May 2018. Ambient Air Quality monitoring was
carried out for PM10, PM2.5, SO2, NOX, and VOC at Nine locations, including the project site.
Values conform to the prescribed standards for Ambient Air Quality. The incremental
Ground Level Concentration (GLC) has been computed using AERMOD. All the results of
measure parameters were found to be below the NAAQS limits at all the locations. The
modeling study proved that the air emissions from the proposed plant would not affect the
ambient air quality of the region in any significant manner. The ambient air quality around
the proposed project site will remain within the National Ambient Air Quality Standards
(NAAQS).
• Risk assessment including prediction of the worst-case scenario and maximum credible
accident scenarios has been carried out. The detailed proposed safeguard measures
including On-Site / Off-Site Emergency Plan has been covered in the RA report.
• This is Greenfield project located outside notified area. Source of water supply is Borewell.
Committee insisted for submission of status of application for ground water source
permission from CGWA by PP.Committee noted that PP has addressed reply of written and
oral questions raised during public hearing. Looking to reply submitted by PP regarding
written and oral questions raised during public hearing for proposed project, Committee
insisted for time bound action plan with concrete mitigation measures for proposed project in
tabular form for questions raised during public hearing and written questions submitted by
complainants regarding project. During SEAC meeting, Committee noted that PP has
addressed there is no residential habitat and water bodies etc within 500 km radius of
proposed project area and there is no Eco sensitive zone within 10 Km radious of proposed
project.
• Committee deliberated on Product profile, Layout plan, area adequacy submitted by
unit.Looking to storage capacity presented by PP for oleum (65%) and oleum (23%),
Committee insisted for justification regarding proposed project not coved under the category
of MAH units as per the Management, Storage, Import of Hazardous Chemical Rules
(MSIHC Rules)’ 1989 with authenticated supporting documents for threshold limit for storage
of oleum applicability to proposed project.
• PP presented that total effluent will be treated in primary ETP and then will be evaporated
in in-house evaporator.Looking to details submitted for evaporator, Committee inssited for
adequacy of evaporator proposed for industrial effluent evaporation along with technical
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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details regarding capacity of evaporator, steam requirement for evaporation and inlet quality
of effluent to be feed in evaporator. Also Committee insisted for technical justification
regarding reuse of process effluent after primary treatment for manufacturing of resist salt
and total evaporation of effluent in evaporator.
• Committee deliberated on Air Matrix, Hazardous waste matrix, baseline data, ToR
compliances, storage of hazardous chemicals & its safety measures and greenbelt
development plan. Committee asked for readdress specific ToR no- 5 with mentioning
adequate details of adoption of renewable energy for proposed project.
• PP presented risk assessment considering the worst case scenario of chemicals evolved
and process hazard for critical process.Committee insisted for risk assessment of oleum
storage& its handling considering worst case scenario of any blast, leakage or fire and super
impose of satellite image for dispersion model with mentioning its impact on surrounding
village’s resiedential habitat areaand its mitigation measures. Also Committee insisted for
standard operating procedure (SOP) for handling and storage of oleum and emergency
spare storage tank for oleum storage.
• PP has addressed fire load calculation for proposed project, fire evacuation plan, fire
hydrant network system, CER and EMP. Committee insisted for submission of revised CER
activity to fulfill need of surrounding villages which is raised during public hearing.
• After deliberation, SEAC unanimously decided to consider the proposal in one of the
upcoming meeting of SEAC after satisfactory submission of following details:
1. Submit time bound action plan with concrete mitigation measures for questions raised
during public hearing in tabular form.
2. Submit at present current status of CGWA permission for ground water source for
proposed project.
3. Justification regarding proposed project not coved under the category of MAH units as
per the Management, Storage, Import of Hazardous Chemical Rules (MSIHC Rules)’
1989 with authenticated supporting documents for threshold limit for storage of oleum
applicability to proposed project.
4. Adequacy of evaporator proposed for industrial effluent evaporation along with technical
details regarding capacity of evaporator, steam requirement for evaporation and inlet
quality of effluent to be feed in evaporator.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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5. Technical justification regarding reuse of process effluent after primary treatment for
manufacturing of resist salt and total evaporation of effluent in evaporator.
6. Readdress specific ToR no- 5 with mentioning adequate details of adoption of renewable
energy for proposed project.
7. Risk assessment of oleum storage& its handling considering worst case scenario of any
blast, leakage or fire and super impose of satellite image for dispersion model with
mentioning its impact on surrounding village’s resiedential habitat area and its mitigation
measures. Also standard operating procedure (SOP) for handling and storage of oleum
and emergency spare storage tank for oleum storage.
8. Revised CER activity to fulfill need of surrounding villages which is raised during public
hearing.
• PP submitted their reply for the query raised by SEAC during SEAC meeting dated
02.02.2021 through email.
• The proposal was reconsidered in the SEAC video conference meeting dated 07.06.2021.
• Revised Salient features of the project including Water, Air and Hazardous waste
management are as under:
Sr. no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores):
Proposed: 2.0 Cr.
ii EMP details (Capital cost & Recurring cost)
Sr.
No Unit Details
Capital
Cost
(Rs.in
Lacs )
Operating
Cost
(Lacs
/Month)
Maintenance
Cost (Lacs/
Month)
Total
Recurring
Cost
(Lacs/
Month)
1
Effluent
Treatment
Plant
Installation of ETP and Evaporator 10 0.70 0.10 0.80
2 Air
Installation of stack/vent & its
monitoring facilities including
provision of air pollution control
system
7.0 0.30 0.10 0.40
3 AWH
Monitoring
To conduct EMS efficacy &
environment monitoring - 0.50 - 0.50
4 Hazardous
Management Getting membership of TSDF site 1.0 1 .0
5 Green belt Development of Greenbelt Area 3.0 - 0.20 0.20
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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development
6 Health &
Safety
Provision of Occupational Health
Centre with Antidotes 7.0 0.5 0.2 0.7
7
Fire
Prevention
Provision of Safety Measures
including Fire Detectors, Sensors,
Alarm, Fire Hydrant, Fire
Extinguishers, Proxymate Suits,
Foam Trolley, Lightening arrestors
etc.
30.0 1.0 0.5 1.5
8 Other
CER Cost 4.0 - - -
Provision of PLC based SCADA
system 25.0 2.6 1.0 3.6
Total 87 5.6 2.1 8.7
iii CER details (As per MoEF&CC OM dated 01/05/2018)
Sr. No.
CER-Proposed Planned Activities Identified Villages
Year wise Budget (Lakhs)
1st Year
1
Skill Development – (On basis of Needs Assessment)
• Supporting technical and vocational training for
women like Training in Hnadicraft& Tailoring will be
provided ranging from 1 month to 7 months
depending upon the nature of the course to women in
poverty, people with disabilities, and unemployed
rural youth after consultation wih Village Panchayat.
Indrad 4.0
Total (Year Wise) 4.0
Grand Total 4.0
B Total Plot area ( sq. meter)
Proposed: 6120 Sq. m.
Green belt area ( sq. meter)
Proposed: 2019 Sq. m
C Employment generation 10
D Water
i
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
Bore well Water Supply
Status of permission from the concern authority. Application no for NOC from CGWA:
21-4/6802/GJ/IND/2020 dated 31/12/2021
ii Water consumption (KLD)
Sr No Category Water Consumption KLD
Remark
1. Domestic 1.5
2. Gardening 1.0 Treated waste
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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water will be utilized
3.
Industrial
Processes 20.7 5.5 KLD Water reuse in process and 20.2 KLD Water received through Borewell
Washing 0.500
Boiler 3.00
Industrial Total 24.2
Total Industrial + Domestic 25.7
Total reuse 5.5
Fresh water requirement 20.2
4) Total water requirement for the project: 26.7 KLD 5) Quantity to be recycle: 6.5 KLD 6) Total fresh water requirement: 20.2 KLD
iii Waste water generation (KLD)
Sr No Category Waste Water Generation KLD
Remark
1. Domestic 1.0 Send to STP
2.
(B) Industrial
Process 5.5 5.5 KLD waste water reuse and remaining 0.7 KLD waste water evaporate
Washing 0.5
Boiler 0.2
Total Industrial waste water 6.2
Total Domestic Sewage 1.0 Send to STP
iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Sr No.
Description Unit
Capacity Dimension
1 Collection cum
Neutralization Tank 2 18 KL
3.0mX 2.0m X
2.0m
2 Holding Tank 1
5 KL 3.0mX 2.0m X
2.0m
3 Collection tank 1
450 X 450 X 12 Plate
2.0mX 2.0m X
2.0m
4 Filter press 1 20 KL 460x460x20 plates
5 Final treated tank 1 - 2.0 m X
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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3.04mX2.13m
Treatment scheme including segregation at source.
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ Total industrial 6.2 KLD Waste Water Generated from ancillary operation, in which 5.5 KLD Effluent will be reuse in Resist salt manufacturing process and Remaining 0.7 KLD Waste Water generated from washing and boiler blow down which is discharge though in house Evaporation system, hence ultimately zero discharge unit.
v
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ➢ Total industrial 6.2 KLD Waste Water Generated from ancillary operation, in which 5.5 KLD
Effluent will be reuse in Resist salt manufacturing process and Remaining 0.7 KLD Waste Water generated from washing and boiler blow down which is discharge though in house Evaporation system, hence ultimately zero discharge unit.
Domestic: The generated sewage @1.0 KLD will be Utilized in Gardening after treated in STP
Industrial: Total industrial 6.2 KLD Waste Water Generated from ancillary operation, in which 5.5 KLD Effluent will be reuse in Resist salt manufacturing process and Remaining 0.7 KLD
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Waste Water generated from washing and boiler blow down which is discharge though in house Evaporation system, hence ultimately zero discharge unit.
vi
In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
• Not Applicable
Membership of Common facility (CF)
(For waste water treatment) ➢ Not Applicable.
vii Simplified water balance diagram with reuse / recycle of waste water
viii Reuse/Recycle details (6.5 KLD)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Total reuse
Source of waste water for reuse with quantity
in KLD (From where it is coming)
Application area with quantity in KLD
(Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS
etc.)
Remarks regarding
feasibility to reuse i.e.
Process 5.5 Resist salt Process
5.5 KLD PH 7-8
COD <200 TDS <1000
Domestic 1.0 Gardening 1.0
E Air
i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of Fuel Quantity of
Fuel MT/Day
Type of emissions i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
1 Boiler (1 TPH)
30
Briquettes or Bio Fuel
5 MT/Day PM SO2
NOx
Multi Cyclone Separator + Water scrubber
2. TFH For Evaporator – 1 Lac Kcal/hr
30 5 MT/Day Multi Cyclone Separator + Water scrubber
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
Sr. no. Source of emission Type of
emission Stack/Vent
Height (meter)
Air Pollution Control Measures (APCM)
1 Attached to Reaction vessel in sulfanilic product
SO2 30 Two stage Alkali scrubber
iii Fugitive emission details with its mitigation measures.
• The entire manufacturing activities will be carried out in the closed reactors and regular checking and maintenance of reactors will be carried out to avoid any leakages.
• The tank vents will be equipped with either a carbon filter or an oil trap to prevent water vapour from entering the tank as it breathes.
• Control of all parameters on a continuous basis will be done by adequate control valves, pressure release valves and safety valves etc.
• All the flange joints of the pipe lines will be covered with flange guards.
• All the raw materials will be stored in isolated storage area and containers tightly closed.
• There will also be provision of adequate ventilation system in process plant and hazardous chemical storage area
• A regular preventive maintenance will be planned to replace or rectify all gaskets, joints etc.
• The unit will also develop green belt within the factory premises to control the fugitive emission from spreading into surrounding environment.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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F
Hazardous wastes (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
i
Sr.
No
Types of
Hazardous
Waste
Sources Categ
ory
Proposed
MT/Year Disposal
1
ETP Sludge
&
Evaporation
salt
ETP Area 35.3
23.0 &
1.00
Collection, storage,
Transportation and
Dispose to Active TSDF
Site
2 Used Oil Plant
Machinery 5.1 0.05
Collection, storage, Reuse
within premises.
3
Discarded
Container/
Bags
Material
Storage
and
Handling
33.1 36.0
Collection, storage,
Transportation and
Dispose to Registered
Recycler
4 Iron sludge
Mfg.
Process
(metanilic
Acid)
26.1 165.0
Collection, storage,
Transportation and Send
for co-processing or TSDF
5 Gypsum
sludge
Mfg.
Process
(Resist
Salt)
26.1 657
Collection, storage,
Transportation and Send
for co-processing or Active
TSDF Site
6
Spent
(H2SO4)
Acid – 22 %
to 27 %
(Aniline 2
4 DSA,
Aniline 2
5 DSA)
26.3 3779
Collection storage and
reuse in Aniline 2-4
DSA(900 MT/year , Aniline
2-5 DSA(982 MT/year,
Sulfanilic acid(1920
MT/year and or Metalinic
acid(1800 MT/year), the
total requirement of spent
acid will be 5603 MT/year
7 Sodium
Bisulphite
Scrubbing
media 37 30 KL
Collection, Storage,
transportation and send to
actual users having
permission under Rule 9
ii Membership details of TSDF, CHWIF etc. (For HW management)
We will obtained after getting NOC from GPCB.
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iii Details of Non-Hazardous waste & its disposal(MSW and others) Not Applicable.
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format).
Not Applicable
ii VOC emission sources and its mitigation measures
• Sources of fugitive emissions include storage of chemicals, solvents storage, loading and unloading section, raw material handling and, hazardous waste storage area Measures:
• The fugitive emissions in terms of handling losses will get reduced by proper storage and handling.
• Hazardous chemicals will be stored as per standard criteria.
• Periodically monitoring will be carried out as per the post project monitoring plan.
• Proper ventilation in storage & production area shall be ensured
• All materials must be stored in suitable packing to prevent contamination of air
• Enclosed system & efficient procedures for materials charging shall be ensured.
• Procedures for start-up shut down, operation & maintenance procedures shall be established & maintained.
• The coverage of greenbelt around the plant also acts as natural barrier to stop carrying of dust along with the wind current.
H
• Details regarding storage of Hazardous chemicals
Storage details Name of major Hazardous chemicals Remarks
Storage tanks
Sr. No.
Name of Equipment
Maximum storage Capacity
KL
No. Tank
Spare tank Storage
Details
1 Oleum 65% 8.00
1 1 10 KL Tank
2 Oleum 23% 8.00
1 10 KL Tank
3 Spare tank for Oleum
10.00 1 - 10 KL
Tank
4 Nitrobenzene 5.00
1 - 8.0 KL Tank
• Applicability of PESO : Not Applicable
• During the meeting dated 07.06.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and their Technical Expert from M/s. Green Circle remain present
during video conference meeting.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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• Committee noted the following:
➢ Time bound action plan with concrete mitigation measures for questions raised
during public hearing in tabular form.
➢ Apply for CGWA permission for ground water source for proposed project.
➢ Justification regarding proposed project not coved under the category of MAH units
as per the Management, Storage, Import of Hazardous Chemical Rules (MSIHC
Rules)’ 1989 with authenticated supporting documents for threshold limit for storage
of oleum applicability to proposed project.
➢ Adequacy of evaporator proposed for industrial effluent evaporation along with
technical details regarding capacity of evaporator, steam requirement for evaporation
and inlet quality of effluent to be feed in evaporator.
➢ Technical justification regarding reuse of process effluent after primary treatment for
manufacturing of resist salt and total evaporation of effluent in evaporator.
➢ Readdress specific ToR no- 5 with mentioning adequate details of adoption of
renewable energy for proposed project.
➢ Risk assessment of oleum storage& its handling considering worst case scenario of
any blast, leakage or fire and super impose of satellite image for dispersion model
with mentioning its impact on surrounding village’s resiedential habitat area and its
mitigation measures. Also standard operating procedure (SOP) for handling and
storage of oleum and emergency spare storage tank for oleum storage.
➢ Revised CER activity to fulfill need of surrounding villages which is raised during
public hearing.
• Looking to reply submitted by technical expert of which is found inadequate, Committee
asked to submit (1) Readdress specific ToR no- 5 with mentioning adequate details of
adoption of renewable energy for proposed project (2) Adequacy of evaporator proposed for
industrial effluent evaporation along with technical details regarding capacity of evaporator,
steam requirement for evaporation and inlet quality of effluent to be feed in evaporator along
with quality of effluent from each proposed product and total effluent evaporation in
proposed evaporator (3) revised adequate details of each point for Risk assessment of
oleum storage& its handling considering worst case scenario of any blast, leakage or fire
and super impose of satellite image for dispersion model with mentioning its impact on
surrounding village’s residential habitat area and its mitigation measures. Also standard
operating procedure (SOP) for handling and storage of oleum and emergency spare storage
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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tank for oleum storage and details of offsite emergency plan details considering population
affected due to proposed Hazardous chemicals storage along with its remedial measures .
• After detailed discussion, Committee unanimously decided to consider the project in
one of upcoming meeting after submission of following documents:
1. Readdress specific ToR no- 5 with mentioning adequate details of adoption of
renewable energy for proposed project.
2. Adequacy of evaporator proposed for industrial effluent evaporation along with
technical details regarding capacity of evaporator, steam requirement for evaporation
and inlet quality of effluent to be feed in evaporator along with quality of effluent from
each proposed product and total effluent evaporation in proposed evaporator.
3. Revised adequate details of Risk assessment of oleum storage & its handling
considering worst case scenario of any blast, leakage or fire and super impose of
satellite image for dispersion model with mentioning its impact on surrounding
village’s residential habitat area and its mitigation measures. Also standard operating
procedure (SOP) for handling and storage of oleum and emergency spare storage
tank for oleum storage and details of offsite emergency plan details considering
population affected due to proposed Hazardous chemicals storage along with its
remedial measures .
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Green Circle, INC remained
present during video conference meeting.
• Committee discussed on the following:
✓ Oleum storage spare tank is not provided. Capacity of storage of oloeum, MAH rules applicability, neutralizing details.
• Later on vide e-mail dated 01-09-2021 PP has submitted the SOP for oleum storage and revised presentation.
• After detailed discussion, Committee unanimously decided to recommend the project
to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
26. All measures shall be taken to prevent soil and ground water contamination.
27. The National Ambient Air Quality Emission Standards issued by the Ministry vide G. S.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 283 of 357
R. No. 826 (E) dated 16th November, 2009 shall be complied with.
28. National Emission Standards for Organic Chemicals Manufacturing Industry issued by
the Ministry vide G. S. R. 608 (E) dated 21/07/2010 and amended from time to time
shall be followed.
29. Unit shall have to adhere to the prevailing area specific policies of GPCB with respect
to the discharge of pollutants, and shall carry out the project development in
accordance & consistence with the same.
30. The project proponent must strictly adhere to the stipulations made by the Gujarat
Pollution Control Board, State Government and/or any other statutory authority.
WATER
31. Total water requirement for the project shall not exceed 25.7 KLD. Unit shall reuse 5.5
KLD of treated industrial effluent within premises. Hence, fresh water requirement shall
not exceed 20.2 KLD and it shall be met through GIDC only.
32. The industrial effluent generation from the project shall not exceed 6.2 KLD.
33. 5.5 KLD Effluent shall be reuse in Resist salt manufacturing process and Remaining
0.7 KLD Waste Water generated from washing and boiler blow down which is
discharge though in house Evaporation system, hence ultimately zero discharge unit.
34. PP shall maintain Complete Zero Liquid Discharge [ZLD] status all the time and there
shall be no drainage connection from the premises and no wastewater discharge
outside premises by any means.
35. Unit shall feed wastewater to in-house Evaporator only after ensuring content of
effluent for COD/VOC so as not to get air borne during evaporation in order to achieve
no adverse impacts on Environment and Human Health.
36. Domestic wastewater generation shall not exceed 1 KL/day for proposed project and it
shall be treated in STP. It shall not be disposed off through soak pit/ septic tank.
Treated sewage shall be utilized for gardening and plantation purpose within premises
after achieving on-land discharge norms prescribed by the GPCB.
37. During monsoon season when treated sewage may not be required for the plantation /
Gardening / Green belt purpose, it shall be stored within premises. There shall be no
discharge of waste water outside the premises in any case.
38. Unit shall provide buffer water storage tank of adequate capacity for storage of treated
waste water during rainy days.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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AIR
39. Unit shall not exceed fuel consumption and provide APCM and Stack height as
mentioned in flue gas matrix.
40. Unit shall provide APCM and stack height as mentioned in process gas matrix.
HAZARDOUS & SOLID WASTE
41. All hazardous solid waste shall be managed as mentioned in hazardous waste matrix.
42. The unit shall submit the list of authorized end users of hazardous wastes along with
MoU signed with them at least two months in advance prior to the commencement of
production. In the absence of potential buyers of these items, the unit shall restrict the
production of the respective items.
GREENBELT AREA
43. The PP shall develop green belt within premises (2019 Sq. m i.e. 33 % of the total plot
area) as per the undertaking submitted before SEAC. Green belt shall be developed
with native plant species that are significant and used for the pollution abatement as
per the CPCB guidelines. It shall be implemented within 3 years of operation phase in
consultation with GPCB.
44. Safety & Health:
a) PP shall obtain PESO permission for the storage and handling of hazardous
chemicals.
b) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life
Safety Measures Act, 2016.
d) Unit shall adopt functional operations/process automation system including
emergency response to eliminate risk associated with the hazardous processes.
e) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
f) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
g) PP shall take all the necessary steps for control of storage hazards within premises
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
h) PP shall take all the necessary steps for human safety within premises to ensure that
no any harm is caused to any worker/employee or labor within premises.
i) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
j) Unit shall never store drum/barrels/carboys of incompatible material/chemical
together.
k) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
12 SIA/GJ/IND2/59728/2020
M/s. Biosynth Industries
Plot No 1713 1715 1716 GIDC Sarigam, Taluka Umbergam, District Valsad
EC Reconsideration
Category of the unit: 5(f)
Project status: Expansion
• Project proponent (PP) submitted online application vide No- SIA/GJ/IND2/59728/2020 on
dated 25.01.2020 for obtaining Environmental Clearance (EC).
• The SEIAA issued TOR to PP vide their letter dated 09.10.2020.
• Project proponent has submitted EIA Report prepared by M/s Green Circle Inc based on the
TOR issued by SEIAA.
• This is an existing unit proposed for manufacturing of synthetic organic chemical
(pharmaceuticals products & resins) as tabulated below:
Grou
p
No.
Sr.
No.
Name of the
Products
API Or
Intermed
iate*
CAS
No. /
CI No.
Quantity MT/Month End-use of
the products Existin
g
Propose
d Total
A
Inorganic Products (Existing Product)
1 Copper Sulphate
AND/OR NA
7782-63-
0 25.00
0
400
AND/
OR
InorganicProd
ucts
-Used as raw
materials in
chemical
industries
2 Ferrous Sulphate
AND/OR NA
10034-
96-5 250.00
3 Manganese
Sulphate NA
7786-81-
4 50.00
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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AND/OR
4 Nickel Sulphate
AND/OR NA
7733-02-
0 25.00
5 Zinc Sulphate NA 7758-99-
8 50.00
B
Pharma Intermediate (Proposed Product)
0.00 25.00 25.00
Used as
Pharma
Intermediate
in
Pharmaceutic
al industries
6 Phenyl Hydrazine
AND/OR NA 100-63-0
7 Ferrous Ascorbate
AND/OR NA
14356-
17-5
8 Ferrous Fumarate
AND/OR NA 141-01-5
9
Chlorotrityl
Chloride(2-
CTC) AND/OR
NA 42074-
68-0
10
Ethyl Ethoxy
Methylene
Malonate
NA 87-13-8
C
Resin (Proposed Product)
11 Alkyd Resin
AND/OR NA
9003-35-
4 0.00
200.00 200.0
0
Used to Ink
Manufacturin
g units
12 Polyamide Resin
AND/OR NA
63428-
84-2 0.00
13 Polyester Resin
AND/OR NA
113669-
95-7 0.00
14 Acrylic Resin
AND/OR NA
25034-
86-0 0.00
15 Rosin Ester
AND/OR NA
68475-
37-6 0.00
16 Epoxy Resin NA 24969-
06-0 0.00
17 Alkyl Resin NA 9003-35-
4 0.00
TOTAL PRODUCTION 400.0 225.0 625.
0
# Brief Note of Product Profile:
1. No of Manufacturing Plants: 1 no.
2. Brief Note regarding number of Products to be manufactured considering plant capacity:
4 number of products will be manufactured at a time.
• The project falls under Category B of project activity 5(f) as per the schedule of EIA
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 287 of 357
Notification 2006.
• The presentation was considered in the video conference meeting dated 07.04.2021.
• Salient features for project details and water, Air and Hazardous Waste Management are
submitted.
• During the meeting dated 07.04.2021, the project was appraised based on the information
furnished in Form – 1, Pre-Feasibility Report, Environment Management Plan and details
submitted by e-mail.
• Project proponent (PP) and their Technical Expert from M/s Green Circle Inc remain present
during video conference meeting.
• Committee noted that this is an existing unit involved in manufacturing of inorganic products
for which CCA was obtained valid upto dated: 30.06.2022. Upon asking regarding
discontinuation of existing products, PP informed that they will continue with existing
products.
• Now, unit has proposed for manufacturing of synthetic organic chemicals [pharmaceuticals
products and Resins] at GIDC Sarigam. Total plot area is 2829.07 Sq. m. Product profile
discussed in depth.
• PP presented Site Plan/ layout with provision of separate entry & exit, 5 m wide peripheral
road, separate plant area for existing and proposed products with raw material and finished
goods storage area, utility area, OHC (15 Sq m), etc.
• Upon asking regarding (1) Compliance of existing CCA and (2) Isolation of Pharma & resins
plants and separate raw material & finished goods storage area for Pharma & resins, PP
could not reply satisfactorily.
• Further, PP has submitted the project details as new project though it is an existing unit.
Committee noted that PP/ technical expert has submitted wrong information and mislead the
Committee.
• After detailed discussion, it was decided to defer the proposal and consider the
project for appraisal only after re-submission of revised project details along with
revised Site Plan/ layout with isolation of Pharma and resins products with separated
storage area of raw material and finished goods for both plants.
• PP submitted the reply of the said points along with other supporting documents.
• This proposal is reconsidered in SEAC meeting dated 05.07.2021. PP along with their
technical expert/consultant from M/s Green Circle Incremains present in the meeting and
made presentation before committee.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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• PP presented revised salient features of the project including Water, Air and Hazardous
waste management are as under:
Sr. no. Particulars Details
A-1 Total cost of Proposed Project (Rs. in Crores):
Existing
Proposed
Total
0.7226 Crores 1.5413 Crores 2.2639 Crores
Break-up of proposed project Cost:
Details Existing (Rs. In Crores)
Proposed (Rs. In Crores)
Total (Rs. In Crores)
Land 0.3958 - 0.3958
Building 0.2218 0.1525 0.3743
Machinery 0.105 0.49 0.595
Others - 0.8988 0.8988
A-2 Details of Environmental Management Plan (EMP) As below:
Sr. No
Unit Detail
Capital Cost (Rs. In Crores)
Operating Cost/ Annum (Rs. In Crores)
Maintenance Cost / Annum (Rs. In Crores)
Total Recurring Cost / Annum (Rs. In Crores)
1 Waste Water Effluent
Treatment Plant
0.17 0.07 0.005 0.075
2 Air APCM 0.14 0.03 0.01 0.04
3 Hazardous Management
- 0.025 0.01 - 0.01
AWH Monitoring Cost
- 0.015 0.015 - 0.015
4 Fire & Safety Includes
PLC system
0.40 0.05 0.03 0.08
5. Green Belt Development
- 0.01 - 0.002 0.002
6. CER - 0.0148 - - -
Total 0.78 0.222
A total of greenbelt will be developed in 1000 m2 area outside the plant. Summary
Cost of Project in Crores 1.48
EMP Capital Cost in Crores per Annum and Percentage:
0.78 ~52.0 %
EMP Recurring Cost in Crores per Annum and Percentage:
0.22 ~14.8 %
A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA, CER
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 289 of 357
fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC’s OM vide 31.10.2019.)
% as per the OM Rs. in Crores
1.0 0.0154
Brief note on proposed activities: ➢ Skill training and awareness programs for women like stitching and beauty parlor courses in village
Daheli. ➢ Distribution of medical equipment like Stretcher, wheel chair & Blood testing kits in Primary health
centers in village Bhilad..
B Land / Plot ownership details: Unit has obtained plot allotment letter from GIDC Sarigam vide letter no GIDC/RM/VPI/SRG/PLT/AMAL/FTO/3887, dated 23/03/2018.
B-1 Plot area
Total Plot area
2829.07 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities: Proposed manufacturing plant is having total land of 2829.07 Sq.m, out of which sufficient area for ETP (55 Sq.m), solid raw material and product storage (120 Sq.m) & Tank farm area with 4 tanks (120.0 Sq.m), Hazardous waste storage (40 Sq.m) has been demarcated.
B-3 Green belt area
Existing
Proposed (Sq. meter)
Total (Sq. meter)
Area in Sq. meter
- 466.08 m2 (Inside plant)
466.08 m2 (Inside plant)
% of total area
- 16.47 % (To compensate the 33 % area of green belt, Plantation will be done in 1000 Sq. m. area by M/s. Biosynth Industries at Kalgam site in association with “Sarigam Industries Association”)
C Employment generation
Existing Proposed Total
10 30 40
D WATER
D-1
Source of Water Supply (GIDC, Bore well, Surface water, Tanker supply etc...) GIDC Sarigam Water Supply
Status of permission from the concern authority. ➢ Permission obtained for 12 KLD vide letter no NAO/SRG/586 Dtd.17/19/2019.
D-2 Water consumption (KLD)
Category
Existing KLD
Proposed (Additional) KLD
Total after Expansion KLD
Remarks
Domestic 1.5 0.3 1.8
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Gardening 0 0.2 0.2
Industrial
Process 2 0 2
Floor and Vessel Washing
0
2 2 2 KLD Reused water will be used
Boiler 0 5 5 2 KLD condensate recovered will be reused in boiler
Cooling 0 2 2
Scrubber 0 3 3
Industrial Total 2 12 14
Grand Total (A+B+C) 3.5 12.5 16
Brief Note on worst case scenario for water consumption:
Sr. no
Product Water req. (in kl) for 1 ton
production
Total production (MT/month)
Total water req. KLD
1 None (Expansion products do not require water)
- - -
Summary of water requirement Quantity KLD
Remarks
Total water requirement for the project (A) 16.0
Quantity to be recycled (B) 4.0
Total fresh water requirement (C) 12.0
Ensure Total water requirement = Fresh water + Recycled water
i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]- Not applicable In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle.
➢ 2 KLD of waste water from Boiler and cooling blow - down will be used for washing. Boiler condensate will be reused for boiler makeup.
D-3 Waste water generation (KLD)
Category Existing KLD
Proposed (Additional) KLD
Total after Expansion KLD
Remarks
Domestic 1 0.5 1.5
Industrial
(C ) Process 2 13 15
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Boiler 0 1 1 Reuse in Washing
Cooling 0 1 1 Reusing in Washing
Scrubber 0
3 3 1.5 KLD will use in recovery of NaSH and 1.5 KLD will sent to CETP Sarigam
Washing 0 2 2 No fresh water used for washing
Total Industrial waste water
0 20 22
Total 3 20.5 23.5
Brief Note on worst case scenario for waste water generation (Qualitative and Quantitative):
Sr no Product name Waste Water Gen. (in KL) for
1MT production
Total Production (MT/Month)
Total Waste water Gen.
(KLD)
Characteristics
1 Phenyl Hydrazine
8.6 625 20 pH : 6-8 COD: 9000 - 11000 BOD: < 1500 TDS: < 14500
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (Whichever is applicable).
➢ During the manufacturing of the process of proposed products organic load (COD) would be maximum at 11000 mg/L, hence it will treated with low concentration stream in ETP having primary, secondary and tertiary unit and then disposed through CETP Sarigam.
D-4 Mode of Disposal & Final meeting point
-
Domestic: Will be treated in in-house ETP and ultimately disposed to CETP Sarigam.
Industrial: Will be given primary, secondary& tertiary treatment and disposed to CETP Sarigam for further treatment.
D-5 Treatment facilities
For Domestic waste water: Capacity of STP: Not applicable as domestic water will be treated in in house ETP.
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
➢ ETP having primary, secondary & tertiary units with capacity to treat 25 KLD waste water.
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP. First of all, non-toxic and biodegradable stream of wastewater will be collected in Equalization cum Neutralization Tanks (ENTs). Here, caustic is added from Caustic Dosing Tank (CDT) by gravity to maintain
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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neutral pH of wastewater. Mixer is provided in ENT to keep all suspended solids in suspension and to provide proper mixing. After that, neutralized wastewater will go to Flash Mixer (FM). Alum and Polyelectrolyte will be dosed from Alum Dosing Tank (ADT) and Polyelectrolyte Dosing Tank (PEDT) respectively by gravity into FM to carry out coagulation by using a Flash Mixer. Then after, coagulated wastewater will be settled in Flocculator (FL). Clears supernatant from FL will be passed in Aeration Tank (AT). In AT, biodegradation of organic matter of the wastewater will be carried out by bacteria (suspended growth) and for that oxygen will be supplied by 2 nos. of air blowers (B-01) through diffusers. Due to Aeration, MLSS will remain in suspension. Nutrients will be added from Nutrient Dosing Tank (NDT) to Aeration Tank for growth of Bacteria. After that, waste water will go to Secondary Settling Tank (SST) from AT. Here, the suspended solids will be settled. Sludge will be removed from bottom of SST and pumped to AT to maintain MLSS and excess activated sludge will be sent to Sludge Drying Beds (SDBs). Clear supernatant from SST will be collected in Intermediate Sump (IS). Then after treated effluent will pump to dual Media filter (DMF) to remove left out SS and for polishing treatment. Then clear effluent will be collected in Treated Effluent Sump (TES) before sending to GIDC CETP. Back wash from DMF will be sent to ENT for further treatment. Sludge settled in FL and excess sludge from SST will be sent to Sludge Drying Beds (SDBs) where, dewatering shall be carried out before storage in HWSA and ultimate disposal to TSDF.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ➢ Not Applicable
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
➢ Sarigam clean Initiative CETP
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
➢ M/s. SARIGAM CLEAN INITIATIVE – CETP Sarigam for effluent, Membership Letter no SCI/CETP/2019-20/051 dated 12/10/2019
D-7 Simplified water balance diagram with reuse / recycle of waste water
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E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario thereof:
Unit has proposed to use LPG, Coal/Bio Coal as fuel and will provide Multi cyclone Dust collector/ Bag filter + water scrubber and adequate stack height as APCM for control of flue gas emissions.
E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC’s OM vide dated 31.10.2019)
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel
MT/Day
Type of emissions i.e. Air
Pollutants
Air Pollution Control
Measures (APCM)
1
Thermic fluid heater 1
(Existing) (600 kg/hr
11 LPG 0.03 MT/day
PM<150 ppm SO2<100 ppm NOx<50 ppm
Stack height of 11 m
2 Steam boiler (850 Kg/Hr) 30
Coal / BioCoal
0.6 MT/Day /0.8 MT/day
Multi cyclone Dust collector/ Bag filter + water scrubber
3
Thermic fluid heater 2 (Proposed) (4 Lakh Kcal/hr)
30 Coal /
BioCoal 1.2 MT/day 1.5 MT/day
PM<150 ppm SO2<100 ppm NOx<50 ppm
Multi cyclone Dust collector/ Bag filter + water scrubber
DG Set (100 kVA)
11 Diesel 18 Lit/Hr Stack height of 11m
E-3 Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
-
Sr. No.
Specific Source of emission (Name of the Product &
Process) Type of emission
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
1 Process Vent-I (attached to Drier & Cooler)
PM< 150 mg/Nm3 18
Multi cyclone Separator/Bag Filter
2 Process Vent-II (attached to Reaction Vessel)
SOx< 40 ppm H2S < 30 ppm NH3< 175 ppm
18 Two Stage Alkali Scrubber
3 FBD (Fluidise Bed Reactor) PM < 150 mg/Nm3
18 Bag Filter
Note: ➢ Details of gaseous raw materials used in proposed project : None ➢ Estimation of process gas emission (Product wise and Total)
Sr NO
Name of Product Type of Emission Max Emission
(MT/Day) Max Emission (MT/Annum)
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1 Chlorotrityl Chloride (2-CTC) SO2 0.075 27
2 Ferrous Fumarate NH3 0.030 10
3 Phenyl Hydrazine H2S 0.036 13.14
➢ Requirement of the scrubbing media (KL per Day) considering solubility (Product wise and
Total)
Sr No Types of Emission Name of Scrubbing Media Requirement of
Scrubbing Media (kL/Day)
1 SO2 Two stage water + Alkali Scrubber 1.0
2 NH3 Two stage water + Alkali Scrubber 1.0
3 H2S Two stage water + Alkali Scrubber 1.0
➢ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its sound
management in HW matrix.- Complied
Sr No Type/Name of
Hazarodus Waste Specific Source of
Generation
Total Quantity (MT/Year)
Management of HW
1 Sodium Sulfite
Na2SO3(15-18%)
Scrubber 322
Collection, Storage, Transportation & Disposal by selling to authorized end user whom have valid permission from GPCB as per Haz. Waste Rule-9
2 Nash 25-30%
Scrubbing Solution ~ 360
Collection, Storage & reuse with in the premises.
E-4 Fugitive emission details with its mitigation measures. All the raw materials will be stored in isolated storage area and containers tightly closed.
The unit will also develop green belt within the factory premises to control the fugitive emission from spreading into surrounding environment. A regular preventive maintenance will be planned to replace or rectify all gaskets, joints etc
F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
➢ Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
➢ Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
➢ Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
-
Sr. no.
Type/Name of Hazardous waste
Specific Source of generation (Name of the Activity, Product etc.)
Category and Schedule as per HW Rules.
Quantity (MT/Annum)
Management of HW
Existing
Proposed Total
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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1 Used Oil Plant Machinery
Sch-I/ 5.1 - 0.192
MT/Annum
0.192 MT/Annu
m
Collection, Storage, Reuse or sell to GPCB Registered Refiners.
2 ETP sludge ETP plant Sch-I/ 35.3
-
200 MT/Annu
m
200 MT/Annu
m
Collection, Storage & send to common TSDF site BEIL Dahej.
3 Discarded/Containe
rs/ Barrels/ liners
From Raw material Storage Section
Sch-I/ 33.1
-
19.92
MT/Annum
19.92
MT/Annum
Collection, Storage, Reuse or sell to GPCB authorized recycler /vendor.
4 Zinc Chloride Wet
From product of Ethylethoxy methylene Malonate
Sch-I/ 6.1
-
855
MT/Annum
855
MT/Annum
Collection, Storage & sell to end user/s having rule 9 permission
5 Sodium Sulphite
From product of Ferrous Ascorbate
Sch-I/ 26.1
-
180
MT/Annum
180
MT/Annum
Collection, Storage & sell to end user/s having rule 9 permission
6 Ammonium Sulphate
From Ferrous Fumarate
Sch-I/ 26.1
-
822 MT/Annu
m
822 MT/Annu
m
Collection, Storage & sell to end user/s having rule 9 permission.
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7 Inorganic Process
Waste
Process of product 4 CAP, 4 NAP
Sch-I 37.3
-
15 MT/Annu
m
15 MT/Annu
m
Collection, Storage & send to common TSDF site BEIL Dahej.
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL Infrastructure Limited (Bharuch Enviro Infrastructure Limited) vide Letter no. BEIL/ANK/2019, Dated 18/11/2019
F-3 Details of Non-Hazardous waste & its disposal(MSW and others)
Not applicable
Sr No
Type/Name of Waste
Specific Source Of Generation
(Name of the Activity Product etc.)
Quantity (MT/Annum) Category
of Waste Management of
Wastes
1
Concerete and Brick Material
Proposed Construction
activity
0.2 C & D Waste
Temporary store, reuse to increase plinth level and in road area
Steel, glass, wood
0.025
2
Domestic Waste (Food Waste, Paper Waste
etc.)
Employee working in the
premises 0.25 MSW
Collected in separate bin and dispose to bin of GIDC
3 Industrial Waste
(Wooden Pellets)
From Raw Material &
Product Storage Area
0.05 ISW Sell to local scrap vendor
4 E-Waste Entire Plant 0.20 E-waste
Collection, Storage and disposal to GPCB Authorized E-Waste Management Facility
5 Fly Ash
Boiler
Briquettes/Agro Waste
55 MT/Annum Fly Ash
Notification
Collection, storage, Transportation (thorough GPS Mounted Vehicles) & disposal by selling to cement/brick manufacturing unit / local road contractor
Thermic Fluid Heater
Briquettes/Agro Waste 70.04
MT/Annum
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.
SR PRODUCT SOLVENT Qty Recovery Loss %
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NO (Mt/MT) Recovery
1 Ferrous Ascorbat Isopropanol 400 380 20 95
2 Chlorotrityl Chloride (2-CTC) Methanol 2000 1980 20 99
Details of Solvent Losses (%)
Sr. no.
Name of the Products
Type of Solvent
Recovery% Loss
%
% Losses
Air Water Haz
1 Ferrous Ascorbat Chlorotrityl Chloride (2-CTC):
Isopropanol Methanol 95 5 1 2.7 1.3
2 Ferrous Ascorbat Isopropanol 99 1 0.01 0.89 0.1
SOLVENT MANAGEMENT PLAN
➢ All the solvents shall be directly distilled from product mixes and; if required shall be purified in packed column with the help of reflux.
➢ The solvent distillation system shall be designed so as to achieve minimum 95.0 % recovery of solvent.
➢ All the pumps shall be mechanical seal type to avoid any leakage of solvent. ➢ All necessary firefighting systems shall be provided with alarm system. Flame proof wiring and flame
proof electrical accessories shall be provided to avoid any mishap.
G-2 Brief Note on LDAR proposed:
➢ Minimum number of flanges, joints and valves in pipelines. ➢ All the rotating equipments like pumps will be installed with double Mechanical Seals to arrest any
sort of emissions. ➢ Flanges will be sealed so less losses will be there ➢ Closed loop system. ➢ Proper Ventilation ➢ Adequate PPEs
G-3 VOC emission sources and its mitigation measures
➢ Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.
➢ Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.
➢ Controlled by having proper scrubbing system. ➢ VOCs detectors will be installed.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
-
Sr. no Name of Chemical Capacity of Tank (KL)
Number of Tanks
Hazardous Characteristics of Chemical
1 Conc. HCL 5 1 Toxic & Corrosive
2 Sodium Hydrogen Sulfide
5 1 Toxic
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3 Vegetable Fatty Acids 5 1 Toxic & Corrosive
4 Sodium Hydroxide 5 1 Toxic
Brief note on storage of Hazardous chemicals in Tanks
• Storage tank will be stored away from the process plant.
• Tanker unloading procedure will be prepared and implemented.
• Caution note and emergency handling procedure will be displayed at unloading area and trained all operators.
• NFPA label will be provided.
• Required PPEs like full body protection PVC apron, Hand gloves, gumboot, Respiratory mask etc. will be provided to operator.
• Neutralizing agent will be kept ready to tackle any emergency spillage.
• Safety shower, eye wash with quenching unit will be provided in acid storage area.
• Material will be handled in close condition in pipe line.
• Dyke wall will be provided to all storage tanks, collection pit with valve provision.
• Double drain valve will provided.
• Level gauge will be provided on all storage tanks.
• Safety permit for loading unloading of hazardous material will be prepared and implemented.
• Proper earthing will be provided.
Sr. No.
Name of the Hazardous material
Maximum Storage (MT)
Actual Storage (MT)
Mode of Storage
Possible type of Hazards
Pharmaceutical Raw Material
1 Aniline 3 3 Drum storage Irritant
2 Sodium Nitrite 3 3 Drum storage Irritant
3 Conc. HCL 5 5 Tank Storage Corrosive and Hazardous
4 Sodium Hydrogen Sulfide
5 5 Tank Storage Irritant
5 Zn Dust 2 2 Woven bag storage
Irritant
6 Acetic Acid 2 2 Drum storage Corrosive
7 Ferrous Sulphate 3 3 Drum storage Irritant
8 Ascorbate Acid 2 2 Drum storage Non toxic, irritant
9 Isopropanol 2 2 Drum storage Flammable
10 Sodium Hydroxide 5 5 Tank Storage Corrosive, Irritant
11 Ferrous Sulphate Heptahydrate
2 2 Drum storage Irritant,Toxic
12 Liq. Ammonia 2 2 Drum storage Corrosive, Irritant
13 Fumaric Acid 2 2 Drum storage Toxic
14 Triphenyl Methane 2 2 Drum storage Nontoxic/harmful
15 Sulfuryl Chloride 2 2 Drum storage Corrosive,irritant
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16 Methanol 3 3 Drum storage Flammable
17 Ethyl Malonate 3 3 Drum storage Irritant
18 Ethyl Orthoformate 2 2 Drum storage Flammable
19 Acetic Anhydride 2 2 Drum storage Harmful Flammable
20 Anhydrous Zinc Chloride 2 2 Woven bag storage
Irritant, Harmful
Resin Raw Material
21 Vegetable Fatty Acids/Oil 5 5 Tank Storage Non toxic
22 Phthalic Anhydride 2 2 Woven bag storage
Corrosive. Irritant
23 Glycerin 3 3 Drum storage Irritant
24 Xylene 2 2 Drum storage Flammable
25 Toluene 2 2 Drum storage Irritant, permeator
26 Di Acid 2 2 Drum storage Irritant
27 Ethylene diamine 2 2 Drum storage Flammable, toxic
28 Mono Acid 2 2 Drum storage Corrosive, Irritant
29 Propyl Glycol 1 1 Drum storage Irritant
30 Styrene 2 2 Drum storage Toxic, Irritant
31 Methyl Methacrylate 1 1 Drum storage Toxic
32 Ethyl Acrylates 2 2 Drum storage Toxic, Flammable
33 Styrene 2 2 Drum storage Irritant
34 Rosin 2 2 Drum storage Irritant
35 Epichlorohydrin 2 2 Drum storage Irritant
36 Bis Phenol A 1 1 Drum storage Hazardous
37 Alkyle Phenol 1 1 Drum storage Irritant, harmful
38 Formaldehyde 1 1 Drum storage Toxic
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
• FLP type light fittings will be provided.
• Proper ventilation will be available in Drum storage area.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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• Proper label and identification board /stickers will be provided in the storage area.
• Conductive drum pallets are provided.
• Drum handling trolley / stackers/fork lift are used for drum handling.
• Separate dispensing room with local exhaust and static earthing provision will be available.
• Materials are stored as per its compatibility study and separate area will be available for flammable, corrosive and toxic chemical drums storage.
• Smoking and other spark, flame generating item are banned from the Gate.
• NFPA labels are provided on drums for hazard identification of the chemicals.
• Exhaust will be provided at ground level in drum storage area.
• Drum loading unloading procedures are prepared and implemented. Safety details of Hazardous Chemicals:
Type of Hazardous Chemicals
Safety measures
Flammable
Wear personal protective equipment. Do not get in eyes, on skin, or on clothing. Avoid ingestion and inhalation. Ensure adequate ventilation. Keep away from open flames, hot surfaces and sources of ignition. Use only non-sparking tools. To avoid ignition of vapors by static electricity discharge, all metal parts of the equipment must be grounded. Take precautionary measures against static discharges. Containers will be kept in tightly closed in a dry, cool and well-ventilated place and kept away from heat and sources of ignition.
Toxic & Corrosive
Wear personal protective equipment/face protection. Do not get in eyes, on skin, or on clothing. Use only under a chemical fume hood. Do not breathe dust. Do not ingest. If swallowed then seek immediate medical assistance. Do not allow contact with water. Handle under an inert atmosphere. Containers will be kept tightly closed in a dry, cool and well-ventilated place. They will not be stored in metal containers.
• Applicability of PESO : NA
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
Manufacturing of proposed products involve various unit operations like distillation, condensation, purification, filtration, drying, reduction, coupling and esterification.
H-3 Details of Fire Load Calculation
Total Plot Area: 2829.07 m2
Area utilized for plant activity: 1475
Area utilized for Hazardous Chemicals Storage: 315
Number of Floors: G+2
Water storage tank provided for firefighting in KLD: 300
Details of Hydrant Pumps: Electricity operated jockey pump of capacity 150 LPM Diesel operated Jockey pump of capacity 150 LPM (Stand by)
Nearest Fire Station : Sarigam GIDC fire station @ 1.25 Km
Applicability of Off Site Emergency Plan: Yes
-
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H-4 Details of Fire NOC/Certificate:
Unit will get Fire NOC after obtaining Environment Clearance.
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 30
Number of Contractual person/Labour : 10
Area provided for OHC: 15 sq.m
Number of First Aid Boxes : 10
Nearest General Hospital : Rotary hospital 0.8 km
Name of Antidotes to be store in plant : Folic Acid, Ethanol, Sodium Thiosulfate, Deferoxamine, Pyridoxine etc will be provided.
• During meeting dated: 05.07.2021, PP presented revised Site Plan/ layout mentioning
separate production area, raw material and finished goods for pharma products and resin
products by separating it with 3-3.50 m wide road. Also, PP has provide separate inorganic
production plants and other related facility. Also presented Area adequacy for storage of raw
material of Pharma and resins products.
• Committee insisted to isolate the production plants & other related facilities of
pharmaceuticals products from resin and inorganic products only separation by 3-3.50 m
wide road is not sufficient to avoid contamination.
• The baseline environmental quality has been assessed for various components of the
environment viz. air, noise, water, biological and socioeconomic aspect. The baseline
environmental study has been conducted for the study area of 10 km radial distance from
project site for the period Oct -2019 to Dec- 2019. Ambient Air Quality monitoring was
carried out PM10, PM2.5, SOx, NOx, CO, NH3, Pb, O3, C6H6, As, Ni, benzo (a) pyrene and
TVOC at Eight locations, including the project site. Values conform to the prescribed
standards for Ambient Air Quality. The incremental Ground Level Concentration (GLC) has
been computed using “AERMOD”.Incremental GLC’s for all parameters remain within 500 m
from the project site. The resultant concentrations are within the NAAQS. The modelling
study proved that the air emissions from the proposed plant would not affect the ambient air
quality of the region in any significant manner. The ambient air quality around the proposed
project site will remain within the National Ambient Air Quality Standards (NAAQS).
• Risk assessment including prediction of the worst-case scenario and maximum credible
accident scenarios has been carried out. The detailed proposed safeguard measures
including On-Site / Off-Site Emergency Plan has been covered in the RA report.
• Committee noted the following:
✓ Fire load calculation mentioning fire water storage (Cap: 500 KL) and 4 Nos of foam
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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trolley (Cap: 50 Litres).
✓ Source of water is GIDC water supply.
✓ Industrial and domestic effluent will be treated in primary & secondary ETP and sent to
CETP-Sarigam.
✓ Scrubbing liquor will reused within premises.
✓ Obtained NOC for accepting treated effluent in CETP-Sarigam dated: 12.10.2019 which
was valid for a period of four months.
✓ Sarigam Industries Association letter for development of greenbelt in year: 2019-2020.
✓ LPG or coal or biocoalis proposed as fuel in boiler and TFHs.
✓ Two stage scrubbing system is proposed for control of process gas emission.
✓ Scrubbing liquor will be reused within premises or sold as per Hazardous waste Rules.
✓ PP submitted hazardous waste matrix mentioning source of generation, quantity and
Mode of disposal and committed to comply the Hazardous and Other Wastes
(Management and Transboundary Movement) Rules 2016. Also submitted area
adequacy for storage of raw material, products and machineries.
• Committee deliberated on Product profile, Layout plan, Storage details, Process safety, Fire
safety, water balance & waste water management, Flue gas and process gas emission & Air
Pollution Control System, Hazardous waste matrix, EMP, CER, Green belt, TOR
compliances, etc.
• Committee insisted to provide the following details:
✓ SOP for handling and storage of styrene monomer & its safety measures.
✓ Details of storage and handling of LPG which is used as fuel in existing TFH along with
its safety measures.
✓ Risk assessment of LPG and styrene monomer along with details of population affected
considering the worst case scenario.
✓ Water balance mentioning quantity of total water requirement, fresh water requirement
and recycle/ reuse of water.
✓ Validated membership of CETP-Sarigam for sending treated effluent.
✓ Concern authority permission letter for development of greenbelt for this proposed
project.
✓ Copy of PESO license for storage of LPG as fuel in existing project.
• After detailed discussion, Committee unanimously decided to consider the proposal
in the upcoming SEAC meeting only after satisfactory submission of the following:
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 303 of 357
1. Revised Site Plan/ layout mentioning separate Pharma products manufacturing
plants & other facilities and separate Resin products & inorganic products
manufacturing plants & other facilities. Also earmarked storage of LPG which is used
as fuel in existing project.
2. SOP for handling and storage of styrene monomer & its safety measures.
3. Details of storage and handling of LPG which is used as fuel in existing TFH along
with its safety measures.
4. Risk assessment of LPG and styrene monomer along with details of population
affected considering the worst case scenario.
5. Revised water balance mentioning quantity of total water requirement, fresh water
requirement and recycle/ reuse of water.
6. Validated membership of CETP-Sarigam for sending treated effluent and mentioning
capacities as per GPCB circular dated: 08.01.2020.
7. Concern authority permission letter for development of greenbelt for this proposed
project.
8. Copy of PESO license for storage of LPG as fuel in existing project.
• Later on PP has replied through Parivesh Portal and their project was scheduled on 01-09-
2021.
• Project proponent (PP) and their Technical Expert from M/s. Green Circle, INC remained
present during video conference meeting.
• Committee discussed on the following:
✓ Layout, styrene monomer details were observed and pp was asked to provide spare tank for styrene monomer.
✓ Members insisted that DCS system should be provided for styrene storage tan.PPsubmitted that they will submit undertaking for the same.
✓ Water balance diagram was discussed it was fund that PP has mentioned the reuse of chemicals as a part of water balance. So PP was asked to rework the same and submit revised water balance diagram.
✓ Membership certificsate was submitted.
✓ PP submitted that PESO liscence is not applicable to their unit.
✓ PP was also asked to submit SOP for LPG and styrene.
• Later on vide e-mail dated 01-09-2021 PP has submitted the Revised SOP of Storage & Transferring of Styrene Monomer , Revised Balance Diagram , undertaking of Fresh Greenbelt Development
• After detailed discussion, Committee unanimously decided to recommend the project
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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to SEIAA, Gujarat for grant of Environment Clearance with the following specific
condition:
SPECIFIC CONDITIONS:
1. All measures shall be taken to prevent soil and ground water contamination.
2. The National Ambient Air Quality Emission Standards issued by the Ministry vide G.
S. R. No. 826 (E) dated 16th November, 2009 shall be complied with.
3. National Emission Standards for Organic Chemicals Manufacturing Industry issued
by the Ministry vide G. S. R. 608 (E) dated 21/07/2010 and amended from time to
time shall be followed.
4. Unit shall have to adhere to the prevailing area specific policies of GPCB with
respect to the discharge of pollutants, and shall carry out the project development in
accordance & consistence with the same.
5. The project proponent must strictly adhere to the stipulations made by the Gujarat
Pollution Control Board, State Government and/or any other statutory authority.
WATER
6. Total water requirement for the project shall not exceed 24.71 KLD. Unit shall reuse
12.71 KLD of treated industrial effluent within premises. Hence, fresh water
requirement shall not exceed 12.0 KLD and it shall be met through GIDC only.
7. The industrial effluent generation from the project shall not exceed 22 KLD.
8. 22 KLD industrial effluent shall be treated in primary, secondary& tertiary treatment
and disposed to CETP Sarigam for further treatment
9. Domestic wastewater generation shall not exceed 1.5 KL/day for proposed project
and it shall be treated in ETP and ultimately disposed to CETP Sarigam. It shall not
be disposed off through soak pit/ septic tank.
10. During monsoon season when treated sewage may not be required for the plantation
/ Gardening / Green belt purpose, it shall be stored within premises. There shall be
no discharge of waste water outside the premises in any case.
11. Unit shall provide buffer water storage tank of adequate capacity for storage of
treated waste water during rainy days.
AIR
12. Unit shall not exceed fuel consumption and provide APCM and Stack height as
mentioned in flue gas matrix.
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Page 305 of 357
13. Unit shall provide APCM and stack height as mentioned in process gas matrix.
HAZARDOUS & SOLID WASTE
14. All hazardous solid waste shall be managed as mentioned in hazardous waste
matrix.
15. The unit shall submit the list of authorized end users of hazardous wastes along with
MoU signed with them at least two months in advance prior to the commencement of
production. In the absence of potential buyers of these items, the unit shall restrict
the production of the respective items.
GREENBELT AREA
16. The PP shall develop green belt within premises (339 Sq. m i.e. 33 % of the total plot
area) as per the undertaking submitted before SEAC. Green belt shall be developed
with native plant species that are significant and used for the pollution abatement as
per the CPCB guidelines. It shall be implemented within 3 years of operation phase
in consultation with GPCB.
17. Safety & Health:
a) PP shall obtain PESO permission for the storage and handling of hazardous chemicals.
b) PP shall provide Occupational Health Centre (OHC) as per the provisions under the
Gujarat Factories Rule 68-U.
c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the
concern authority as per the prevailing Rules / Gujarat Fire Prevention and Life Safety
Measures Act, 2016.
d) Unit shall adopt functional operations/process automation system including emergency
response to eliminate risk associated with the hazardous processes.
e) PP shall carry out mock drill within the premises as per the prevailing guidelines of
safety and display proper evacuation plan in the manufacturing area in case of any
emergency or accident.
f) PP shall install adequate fire hydrant system with foam trolley attachment within
premises and separate storage of water for the same shall be ensured by PP.
g) PP shall take all the necessary steps for control of storage hazards within premises
ensuring incompatibility of storage raw material and ensure the storage keeping safe
distance as per the prevailing guidelines of the concerned authority.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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h) PP shall take all the necessary steps for human safety within premises to ensure that no
any harm is caused to any worker/employee or labor within premises.
i) Flame proof electrical fittings shall be provided in the plant premises, wherever
applicable.
j) Unit shall never store drum/barrels/carboys of incompatible material/chemical together.
k) Unit shall provide effective Isolation for Process area and storage of hazardous
chemicals.
13 SIA/GJ/MIS/59238/2019 M/s.Nirma Limited
Bhavnagar creek , Khar 1 and Khar 2, Kalatalav Village, Bhavnagar
EC Reconsideration
Category of the unit: 7(e)
Project status: New
• Project proponent (PP) submitted online application vide No.SIA/GJ/MIS/59238/2019 for
obtaining Environmental Clearance (EC).
• The SEIAA issued TOR to PP vide their letter dated 04.11.2019 and 21.01.2020.
• Project proponent has submitted EIA Report prepared by M/s. Indomer Coastal Hydraulics
(P) Ltd., 63, Gandhi Road, Alwarthirunagar, Chennai based on the TOR issued by SEIAA.
• Public Hearing was conducted by Gujarat Pollution Control Board on 12.10.2020 at project
site of M/s. Nirma Limited, R. S. no. 478/p, 447-453, 455-457 of Village Kalatalav, Ta.:
Bhavnagar, Dist.: Bhavnagar.
• This is anew project, i.e. 4.5 Million TPA cargo handling facility and auxiliary unit through
captive jetty at PLOT Plot No. Khar 1 and Khar 2, Kalatalav Village, Bhavnagar District,
Gujarat. Product profile is as below:
Sr. no.
Type of activity Capacity (MMTPA) Remarks
Phase - I Phase - II
Projected cargo handling
1 Limestone 1.7 2.5 -
2 Coal/pet coke 1.0 1.7 -
3 Gypsum Nil 0.05 -
4 Rock Phosphate Nil 0.25
Total 2.7 4.5 Proposed captive jetty and auxiliary
facilities will be designed according
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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to the round off projected cargo
handling capacity of 4.5 Million
TPA.
• The project falls under Category B of project activity 7(e) as per the schedule of EIA
Notification 2006.
• The presentation was considered in the video conference meeting dated 23.04.2021.
• Project proponent and technical expert of PP remained present during video conference
meeting dated 23.04.2021.
• During the meeting, the project was appraised based on the information furnished in the EIA
Report, Public hearing proceedings and details presented during the meeting by technical
expert M/s. Indomer Coastal Hydraulics (P) Ltd.
• PP presented that
✓ No protected areas as per Wildlife (Protection) Act, 1972 exist within 15 Km radius of
the proposed project site.
✓ Velavadar National Park is located about 20.3 km from the proposed project site.
✓ No any CEPI area within 10 Km radius of the Project site.
✓ Ecologically sensitive areas such as sand dunes, salt marshes, turtle nesting ground,
sea grass beds, bird nesting ground, national parks, sanctuaries, reserve forests,
wildlife habitats and other protected areas under the provisions of Wild Life Act,
Forest (Conservation) Act, including Biosphere Reserves were absent in the 5 km
project radius.
✓ Yes, as per the CRZ map, a portion of approach channel of area wherein 100 m x 15
m (1500 m2) i.e. 0.15 ha. Creek bank falls with sparse mangroves. The buffer zone
of 50 m of this sparse mangrove fall inside the approach channel is about 0.09 ha.
Whereas dense mangroves are present at 1.16 km SE.
• Upon asking regarding justification of the proposed project, PP informed that Nirma Limited
(NL) located near Kalatalav village is presently utilizing the port facilities available at New
Bhavnagar Port (GMB) for importing the raw materials. The materials are then transported
by dumpers to the plant by road to 24 km from the New Bhavnagar Port. The system
involves double handling of the material coupled with many environmental issues, higher
cost of handling etc. In order to solve the existing issues, they have explored viable options
where the materials can be moved to an exclusive marine facility close to the plant site by
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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barges through Bhavnagar creek and unload the Cargo through suitable material handling
equipment installed on the jetty. Accordingly, Nirma Ltd. has proposed to develop 4.5 Million
TPA cargo handling facility and auxiliary unit through development of captive jetty at
Bhavnagar Creek, close to existing Nirma plant.
• The baseline environmental quality has been assessed for various components of the
environment viz. air, noise, water, biological and socioeconomic aspect. The baseline
environmental study has been conducted for the study area of 10 km radial distance from
project site for post-monsoon (October-2017 to Novemner-2017) as well as pre-monsoon
(April-2018 to May-2018). Ambient Air Quality monitoring was carried out PM10, PM2.5, SO2,
NO2, CO, NH3, Ozone, heavy metals and hydrocarbons at four locations, including the
project site. Values conform to the prescribed standards for Ambient Air Quality. The
incremental Ground Level Concentration (GLC) has been computed using “AERMOD”.
Incremental GLC’s for all parameters remain within 500 m from the project site. The
resultant concentrations are within the NAAQS. The modelling study proved that the air
emissions from the proposed plant would not affect the ambient air quality of the region in
any significant manner. The ambient air quality around the proposed project site will remain
within the National Ambient Air Quality Standards (NAAQS).
• Permission from GMB and Land Possession:
✓ GMB NOC for EIA study was granted on 24/08/2017.
✓ GMB NOC for development of Jetty Project is applied on 15/07/2019 which is under
process.
✓ Major part of jetty land is falling under the salt works lease area and other in
Government Waste Land. Application submitted to obtain permission from the
Revenue Department on 27.06.2019, which is under final consideration.
• Presence of endangered species and Mangroves:
✓ Mangroves: As per the CRZ map, a portion of approach channel of area wherein 100
m x 15 m (1500 m2) i.e. 0.15 ha. Creek bank falls with sparse mangroves. The buffer
zone of 50 m of this sparse mangrove fall inside the approach channel is about 0.09
ha. Whereas dense mangroves are present at 1.16 km SE. However, banks of
Bhavnagar creek immediate to the south of project site are occupied with
mangroves. Totally 6 mangrove species belonging to 3 families were observed in the
study area. They are Avicennia alba Blume, Avicennia marina (Forssk.) Vierh.,
Avicennia officinalis L., Suaeda fruticosa (L.) Forsk. Fl., Suaeda maritima (L.)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Dumort., Salvadora persica L. Dominant mangrove species observed is Avicennia
marina (Forssk.).
✓ Endangered Species: Not present
• Project activities:
✓ In brief proposed project includes the following:
✓ Captive jetty of handling capacity 4.5 Million TPA
✓ 18 m wide tidal lock gate system to maintain seawater inside the jetty basin
✓ Capital and maintenance dredging in Jetty basin and Navigational channel
✓ Slope protection and reclamation works
✓ Installation of material handling system
✓ Construction of coal stack yard and limestone stack yard
✓ Construction approach road connecting captive jetty and Nirma plant
✓ Other on shore supporting infrastructures
✓ Committee noted that this is a 4.5 Million TPA cargo handling facility and auxiliary
unit through captive jetty at Bhavnagar. Total plot area is 3,09,600 Sq m.
• Committee deliberated on project location, proposed marine & terrestrial facilities and
activities, Project outlook, Layout plan, Storage details, dredge material management, CRZ
status, Fire safety, water balance & waste water management, Flue gas emission & Air
Pollution Control System, Hazardous waste matrix, EMP, CER, Green belt, TOR
compliances, etc.
• Committee noted the following:
✓ Product activities with different phases.
✓ Distance of CRZ area and Non-CRZ area and inter-tidal zone
✓ Affected mangrove area
✓ Impact on fisheries and fishing and noted that the fishing area is 18 km away from
the site
✓ Adverse impact on protected areas like Velavadar National Park and sea weeds and
sea grass
✓ Erosion & accretion study, marine parameters etc.
✓ 153 Ha mangrove plantation area
✓ CER and CSR activities
✓ Points raised in public hearing
✓ Permission from Gujarat Maritime Board is yet to be received
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✓ Recommendation from GCZMA is awaited
✓ Land possession document to be received by Collector upon submission of
recommendation by GCZMA
✓ Mangroves and mudflats are the sensitive environmental factors present close to
dredge location.
✓ Biologically active mudflat and mangroves are sensitive factors of project site.
✓ During construction phase, clear marking of construction corridor. Buffer zone of 50
m shall be marked in the mangrove and mudflat area with warn sign board.
✓ In order to predict the sediment transport pattern, shoreline behavior, areas of
erosion & accretion and to predict the amount of maintenance dredging required,
sediment transport study using MIKE 21 ST is conducted.
✓ Mathematical modeling study predicted no excessive accretion/erosion along
Bhavnagar Creek. Hence, no impact envisaged.
✓ Baseline study The EIA study covers only two seasons though it was mentioned
Comprehensive EIA report.
✓ Field studies were undertaken during Post monsoon (October – November 2017)
and Pre monsoon (April – May 2018).
✓ Compliance of Written representation received during the public hearing was not
covered in the presentation.
• After detailed discussion, Committee unanimously decided to consider the proposal
in upcoming SEAC meeting upon submission of below mentioned details:
1. Status of CRZ clearance Recommendation letter issued by GCZMA.
2. Revised CER activities with monitorable targets.
3. Requisite permissions/Approvals from the Gujarat Maritime Board (GMB).
4. Land Possession Documents issued by the concern Authorities.
5. Justification regarding validity of the Baseline data in line to the MoEF&CC’s OM
dated 29.08.2017.
6. Clarification on the EIA report i.e. whether the report is Comprehensive or Rapid?
7. Time bound action plan with concrete mitigation measures for issues raised during
public hearing including written representation received during public hearing.
8. Addendum to the EIA report incorporating above mentioned points and complete
compliance of the Terms of Reference issued by SEIAA.
9. Approved conservation plan for near Threated species/Schedules species through
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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the competent authority.
10. Valid Certificate of accreditation issued by the NABET, QCI.
• PP submitted their reply for the query raised by SEAC during SEAC meeting dated
23.04.2021 through email.
• The proposal was reconsidered in the SEAC video conference meeting dated 20.07.2021.
• Project proponent (PP) and their Technical Expert from M/s. Indomer Coastal Hydraulics
(P) Ltd. remain present during video conference meeting.
• Revised project details, water, air and Hazardous waste management are as under,
Sr.
no. Particulars Details
A-1 Total cost of Proposed Project
(Rs. in Crores): Six Hundred
Total Project Cost
Phase I -180 Crores
Phase II -420 Crores
Total -600 Crores
Break-up of proposed project Cost:
Details Project Cost
(Rs. In Crores)
Land -
Building 86.58
Machinery 94.02
A-2 Details of Environmental Management Plan (EMP) As below:
Sr. No
Unit Detail
Capital Cost (Rs. In Crores)
Operating Cost (Rs. In Crores)
Maintenance Cost (Rs. In Crores)
Total Recurring Cost (Rs. In Crores)
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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1 Waste Water
No industrial effluent
generation
- - - -
2 Air - 0.02 - - 0.01
3 Hazardous Management
- 0.005 0.002
4 Fire & Safety - 0.15 - - 0.015
5 AWH Monitoring
- 0.5 - - 0.3
6. Green Belt Development
- 0.515 - - 0.025
7. Occupational Health
Covered under sr.
no. 4 - - - -
Total 1.19 - - 0.352
Summary
Phase - I Phase - II
Cost of Project in Crores per Annum: 180 420
EMP Capital Cost in Crores per Annum and
Percentage:
1.19
(0.4 %)
EMP Recurring Cost in Crores per Annum
and Percentage:
0.352
(0.11%)
A-3 Details of CER:
Fund allocation for Corporate Environment Responsibility (CER) for various activities
therein. The details of fund allocation and activities for CER shall be incorporated in
EIA/EMP report. The entire activities proposed under CER shall be part of
Environment Management Plan (EMP) as per the MoEF&CC’s OM no. F. No. 22-
65/2017-IA.III dated 30.09.2020.
Brief note on proposed activities for CER:
• As an approach of sustainable development, The Company will also contribute a stock of
their capital investment for the development of the neighboring environment. In view of
this aspect, the project proponent should allot 1 % of the capital cost (>from 500 Crores
to 1000 Crores) to monitor the surrounding environment periodically through corporate
environment responsibility.
• The CER fund allocation will be utilized to develop infrastructure facilities like drinking
water supply, sanitation and health, access roads, cross drainage, electrification through
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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solar panel installation.
• The Company also confirm that the aspects followed in the corporate environment
responsibility will be implemented and periodically monitored. The same will be compiled
and a compliance report will be forwarded to the concerned pollution control board/
MoEF&CC regional office and to the district magistrate for review.
• A total of 600 lakhs will be separated as CER accounting 180 lakhs and 420 lakhs in
Phase I and II respectively. CER activities for the proposed project site for a period of ten
years (2021 - 2031) is given in Table below.
Proposed CER activities and allocated budget (2021 - 2031)
CER Activities *Phase I (Lakhs) *Phase II (Lakhs)
FY 2021-2026 FY 2026-2031
Human Development
and Capacity Building
50 120
Infrastructure 70 100
Health & Hygiene 30 90
Socio-economic Development 15 80
Sports & Recreation 15 30
Total 180 420
*Phase I and Phase II periods are subject to alteration.
B Land / Plot ownership details:
Major part of jetty land is falling under the salt works lease area and other in
Government Waste Land. Application submitted to obtain permission from the
Revenue Department on 27.06.2019, which is under final consideration.
B-1 Plot area
Total Plot area
3,09,600 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
The land use plan has been prepared after identifying the requirement of land for
various jetty related activities of the proposed terminal. While preparing the land use
plan the extent and limits of surrounding development, limitation/ development needs
of infrastructural facilities, ease of access, cargo handling requirements,
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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environmental and safety requirements have been given due consideration. Following
table shows the summery of land use plan.
The first phase of the development is conceptualized and planned considering
expansion potential in phase‐II based on cargo ramp‐up and enhancement of
mechanized handling system. Second phase can easily be accommodated without
changing the existing facility and without tempering the current operation of phase‐l
while providing additional facilities for phase‐ll.
Area breakup is as under:
Sl. No. Details Area (ha)
1 Jetty 0.64
2 Basin & Dredge Slope 4.79
3 Entrance channel & Dredge Slope 2.34
4 Storage Area 9.80
5 Immediate Backup Area 0.21
6 Road Network 2.17
7 Building & Infrastructure 0.22
8 Green Space 10.22
9 Open Area 0.31
10 Parking Area 0.26
Total Area 30.96
Area is adequate as per Pre-Feasibility Report.
B-3 Green belt area
Total
(Sq. meter)
Area in Sq. meter 1,02,200
% of total area 33.01
C Employment generation
Total
Construction Phase: 250 Indirect
Operation Phase:600 (100 Direct + 500 Indirect)
D WATER
D-1 Source of Water Supply From existing Nirma
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(GIDC, bore well, Surface water, Tanker supply etc...)
Plant, located at Village
Kalatalav, Bhavnagar.
Status of permission from the concern authority. -
D-2 Water consumption (KLD)
Category
Quantity
(KLD) Remarks
(S) Domestic 5 -
(T) Gardening (including Green belt)
35 -
(U) Industrial
(ii) Process -
(iii)Washing -
(iv)Boiler -
(v)Cooling -
(vi)Others (Dust suppression)
15 To supress dust generated during material handling and storage
Industrial Total 15 -
Total (A + B + C) 55 KLD Total consumption will be met from
the existing Nirma Plant
7) Total water requirement for the project: 55 KLD
8) Quantity to be recycled: 0 KLD
9) Total freshwater requirement: 55 KLD
(Total water requirement = Fresh water + Recycled water)
D-3 Waste water generation (KLD)
Category
Wastewa
ter (KLD) Remarks
(K) Domestic 4 Wastewater generated will be 80% of raw water.
(L) Gardening
(including Greenbelt) 0 Complete utilization. No wastewater
generation
(M) Industrial
Process -
Washing -
Boiler -
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Cooling -
Others (Dust suppression)
0 Complete utilization. No wastewater generation
Total Industrial wastewater
0 -
Total [A + B+C] 4 Wastewater generated (Domestic) will be disposed into septic tank
Brief Note on worst case scenario for waste water generation (Qualitative and
Quantitative):Not Applicable
Brief justification in case of no process effluent generation or no industrial effluent
generation or no high concentration effluent generation from proposed project
(Whichever is applicable): Not Applicable
Proposed project is for development of jetty and auxiliary facilities. Hence, no industrial
wastewater generation.
D-4 Mode of Disposal & Final meeting point
Domestic: Septic tank/soak pit
Industrial: Proposed project is for development of jetty and auxiliary facilities.
Hence, no industrial wastewater generation.
-
Clearly mention about final disposal - no industrial effluent generation.
D-5 Treatment facilities
For Domestic waste water:
Capacity of STP: Septic tank/soak pit.
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each stream
i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-
2….) for each stream shall be proposed.
• No industrial effluent generation.
Note: (In case of CETP discharge) :
Management of wastewater keeping in view direction under section 18 (1) (b) of the
Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding
compliance of CETP.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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• Not Applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
• Not Applicable
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE,
CHWIF etc.
Name of Common facility (CF) (For wastewater treatment)
• Not Applicable
Membership of Common facility (CF) mentioning total capacity, consented quantity,
occupied capacity and spare capacity and norms of acceptance of effluent from
member units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G
(5)/550706 dated 08/01/2020.
• Not Applicable
D-7 Simplified water balance diagram with reuse / recycle of waste water
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario
thereof:Not Applicable
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr,
KVA etc.
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(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism
published in the MOEFCC’s OM vide dated 31.10.2019)
Sr.
no.
Source of
emission
With Capacity
Stack
Height
(meter)
Type
of
Fuel
Quantity
of Fuel
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air Pollution
Control Measures
(APCM)
1 DG Set (500
KVA) - 2 Nos. 30 m HSD 5 KL/day
SPM, Nox
and SO2
Guidelines provided by CPCB will be followed to control emission from DG sets. Hence, anticipated emission from DG sets are expected to be well with stipulated limits.
E-3 Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
• Not Applicable
E-4 Fugitive emission details with its mitigation measures.
Construction Phase: Temporary increase in pollutants due to operation of
construction equipment, transport of construction materials, handling of construction
materials etc., would be present for short period. Emission of pollutants like CO, SO2,
NOX from the vehicles moving with construction materials, running machineries and
other machineries like dredger, concrete mixer etc. are associated with construction
phase.
Operational Phase: Fugitive emission from material transportation.
Mitigation: i) Water sprinkling will be done to suppress fugitive dust during
earthworks, stack yard and along unpaved sections of access roads. ii) The vehicles
conforming to emission noise of CPCB and having valid Pollution Under Control
(PUC) certificates will be used iii) Development of green belt in 102200 Sq.m around
captive jetty area. iv) Provision for Personnel Protective Equipment as per the
industry norms will be addressed for labours working in construction areas.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary
Movement) Rules 2016.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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F-1 Hazardous waste management matrix
Sr.
no.
Type/Name of
Hazardous
waste
Specific
Source of
generation
(Name of
the
Activity,
Product
etc.)
Category and
Schedule as
per HW Rules.
Quantity
(MT/Annum)
Management of
HW
1 Used oil Machinery
5.1 15 Collection,
Storage,
Transportation,
disposal by
selling to
Registered
recycler.
2 Discarded
containers/
barrels
Empty
Carbos
33.1 24 nos./Annum Through authorized vendors
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
• Not Applicable
Details of Membership letter no. & Date with spare capacity of the Common Facility.
• Not Applicable
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Municipal solid waste generated
during
construction and operational waste
will be
disposed off with proper
treatment/nearest
MSW treatment site. No
commercial waste
will be generated.
Sr.
no.
Type/Name of
MSW
Specific Source of
generation
Quantity
(MT/Annum)
Management of
MSW
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 320 of 357
(Name of the Activity,
Product etc.)
1 Domestic and
operational
waste
Canteen
40 kg/day Through Municipality/ authorized
vendors
G Solvent management, VOC emissions etc.
G-1
• Not Applicable
G-2 Brief Note on LDAR proposed:
• Not Applicable
G-3 VOC emission sources and its mitigation measures
• Not Applicable
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
• There is no hazardous chemicals storage on site, however fire hydrant system as a part
of safety requirement will be provided.
H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic
Reaction etc.)
• Not Applicable
H-3 Details of Fire Load Calculation - engineering consultant will help
Total Plot Area: 30.96 Hector
Area utilized for plant activity: 23.83 Hector
Area utilized for Hazardous Chemicals
Storage:
Not Applicable. No Hazardous Chemical Storage provision in the proposed development
Number of Floors: Open Area + various single story buildings
Water requirement for firefighting in KLD:
8,20,000 liter
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Water storage tank provided for firefighting in
KLD:
Water storage tank with two compartment of 4,10,000 liter capacity each
Details of Hydrant Pumps: • 1 no. of Electric Driven Pump (Main) - Capacity 273 m3 (4550 lpm) @ 70 M head
• 1 no. of Diesel Engine Driven Pump (Main) - Capacity 273 m3 (4550 lpm) @ 70 M head
• 1 no. of Jockey Pump - Capacity 10.8 m3 (180 lpm) @ 88 M Head (approx. 10 Kw)
• 31 fire Hydrants points
Nearest Fire Station : Nirma Limited, Kalatalav, Tal &Dist.: Bhavnagar
Applicability of Off Site Emergency Plan: Not Applicable
H-4 Details of Fire NOC/Certificate: will be obtained prior commencement of the project.
H-5 Details of Occupational Health Centre (OHC):
A dedicated OHC of adjoining Nirma Plant is already there.
Number of permanent Employee : 100 nos.
Number of Contractual person/Labour : 500 nos.
Area provided for OHC: Existing: 360 m2 (12 Mtr. x 30 Mtr.)
Proposed Expansion: 270 m2 (9 Mtr. x 30 Mtr.)
Number of First Aid Boxes : 25 nos.
Nearest General Hospital : Sir Takhtasinhji Hospital, Bhavnagar
14 Km from Site
Name of Antidotes to be store in plant : -------
• During the meeting, Committee deliberated on CRZ status, CER, Permissions from the
GMB, Land Possession documents etc.
• PP presented that they have already applied for CRZ Clearance and presently their
proposal is at final stage of approval. They ensured that they will submit the
recommendation letter to SEIAA once they received from GCZMA.
• Further, PP presented that GMB NOC for development of Jetty Project is applied on
15/07/2019 which is under process.
• While discussion regarding Land possession documents, Committee observed that Part of
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 322 of 357
jetty land (28.9 ha) is falling under the salt works lease area and other in Government Waste
Land (2 ha). Application submitted to obtain permission from the Revenue Department on
27.06.2019, which is under final consideration.
• Committee felt that though only 2.0 Ha land out of total project area 30.9 ha is to be
purchased, PP shall furnish primary documents from revenue department.
After detailed discussion, Committee unanimously decided to reconsider the proposal in
upcoming SEAC meeting upon satisfactory submission of the required documents regarding
Land possession and GMB permission to discuss the issues raised during the earlier SEAC VC
dated 23.04.2021.
• PP submitted reply for the above mentioned points on 03.08.2021.
• Proposal was considered in the SEAC VC meeting dated 01.09.2021.
=Salient features of the project submitted by PP are as mentioned below.
✓ This is the proposed project for development of 4.5 million TPA cargo handling
facility and auxiliary units through captive jetty at bhavnagar in bhavnagar creek,
kalatalav village, bhavnagar district
✓ The jetty will be located along the Bhavnagar Creek of Gulf of Khambhat near
existing Bhavnagar New Port.
✓ Proposed project is a pilled Jetty for barges operation for various cargos. The
Berthing area is required to service mostly barges up to 2500 DWT. The Deck Top
level shall be kept + 12.96 Meters with respect to Chart Datum. There will be four
berths within jetty basin area. Berth shall be on piled structures in basin, out of four,
three berths having length 298 meter and one berth having length of 122 meter.
Basin lock gate width in approach channel shall be 20 Meters. Berths shall be
designed for handling 4 nos. of different capacity barges up to 2500 DWT at a time.
✓ The land on which backup area is planned; @ 2,31,900 Sq. m, fall under Khar No. 2
belongs to village Kalatalav.
✓ Total water consumption will be 55 KLD. Total Industrial wastewater generation will
be NIL.
✓ Diesel will be used as fuel for D.G. Set. There will be no process gas emission.
✓ The baseline environmental quality has been assessed for various components of
the environment viz. air, noise, water, biological and socioeconomic aspect. The
baseline environmental study has been conducted for the study area of 10 km radial
distance from project site for the period for post monsoon September,2017 to
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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November,2017 and pre monsoon April, 2018 to May,2018.
✓ Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, at four
locations. Values conform to the prescribed standards for Ambient Air Quality. The
incremental Ground Level Concentration (GLC) has been computed using ISC-ST3.
The resultant concentrations are within the NAAQS. The modelling study proved that
the air emissions from the proposed project would not affect the ambient air quality of
the region in any significant manner. The ambient air quality around the proposed
project site will remain within the National Ambient Air Quality Standards (NAAQS).
All parameters of ground water and surface water samples found within the norms.
✓ As per the marine ecological survey, project area has moderate productivity. No
major impacts are anticipated on marine ecology due to construction and operation
of the proposed project.
✓ MIKE 21 HD sediment transport model was utilized to predict the process of erosion,
transport and deposition of sediment for various tidal conditions i.e. spring and neap
tides. The sediment transport model was run for 29 days continuously covering
spring and neap tide conditions to understand the basic sediment transport behavior
in the study domain without any development.
✓ It was observed that there will be no significant change in the sedimentation
processes due to the development of jetty facilities.
✓ Potential impacts pertaining to the air environment, water environment, land / soil
environment, noise environment, socio-economic environment etc. have been
identified and appropriate mitigation measures including comprehensive monitoring
program has been prescribed for the same.
✓ Risk assessment including prediction of the worst-case scenario and maximum
credible accident scenarios has been carried out. The detail proposed safeguard
measures including On-Site / Off-Site Emergency Plan has been covered in the EIA
report.
✓ Public Hearing was conducted on 12/10/2020 at 11:00 Hrs. at project site of Nirma
Limited; R S no.478/P,447-453,455-457 of Kalatalav Village, Bhavnagar Taluka,
Bhavnagar District. Major issues were discussed during public hearing was
discussed in meeting in detail and its reply was found satisfactory.
✓ PP has applied for CRZ clearance to GCZMA, Gujarat.
✓ The main features of the proposed project are listed below;
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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✓ Proposed project is a pilled Jetty for barges operation for various cargos.
✓ The Berthing area is required to service mostly barges up to 2500 DWT
✓ The Deck Top level shall be kept + 12.96 Meters with respect to Chart Datum.
✓ There will be four berths within jetty basin area.
✓ Berth shall be on piled structures in basin, out of four, three berths having length 298
meter and one berth having length of 122 meter. Basin lock gate width in approach
channel shall be 18 Meters.
✓ The jetty will be constructed as a RCC deck platform, which will be supported on
cast-in-situ RCC piles. The RCC deck will be part precast and part cast-in-situ. The
installation of piles will be done first over which superstructure will be installed. The
proposed jetty will have 222 piles with 1.2 meter diameter each.
✓ Berths shall be designed for handling 4 nos. of different capacity barges up to 2500
DWT at a time.
✓ Heavy duty Bollards designed for BP about 10 T shall be provided. Suitable rubber
fenders shall provide to withstand the berthing forces of the vessel as per the
engineering design.
✓ It is proposed to use self-propelled barges for this project.
✓ The turning circle will have a diameter of 125 m with a depth of 6.70 m inside the
basin area. The approach channel and turning circle is designed to cater barges up
to 2500 DWT size.
✓ The land on which backup area is planned; @ 2,31,900 Sq. m, fall under, Khar No. 2
belongs to village Kalatalav.
✓ The water front area immediately after high tide line is subjected to tidal influence
mostly during the spring tides. A portion of approach channel of area wherein 100 m
x 15 m (1500 m2) i.e. 0.15 ha. creek bank falls with sparse mangroves. The buffer
zone of 50 m of this sparse mangrove fall inside the approach channel is about 0.09
ha. Whereas dense mangroves are present at 1.16 km SE.
✓ Along the proposed channel of the terminal a rock slope protection will be developed.
The shore protection work will be having various layers of rock armour layer and core
material. The toe will be provided at the bottom of the shore protection work. The
average bottom level of the slope protection work will be @ + 4.0 m CD. The top of
the shore protection work will be @ + 12.96 m w.r.t. CD.
✓ Moorings shall be provided to prevent vessels from drifting away from a berth or from
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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colliding with adjacent moored vessels or adjacent structures. Movement of the
barges shall be restrained by means of an adequate number of mooring lines, which
can be readily handled by the operating personnel, compatible with the conditions of
winds, tides, waves and other effects likely to be experienced during the period a
barge is berthed.
✓ Water supply required in various locations at jetty and premises will be source from
adjacent Nirma Plant.
✓ Anticipated Quantity of raw water requirement is 55 KL / day.
✓ No water is required for industrial applications. The major use of water will be mainly
for canteen, drinking, cleaning, toilets, dust suppression, gardening and as a storage
in fire main tanks.
✓ No industrial liquid and solid waste generation expected from the jetty operation. The
only waste generation expected is from domestic usage, the sewage generated from
canteen, washing area and toilet blocks shall be only 4 KLD which will be treated
through septic tank/soak pit.
✓ Power requirement during construction period will be approx. 100 KVA and during
the operation of jetty the anticipated requirement is 500 KVA. The required Electric
Power will be fetched from existing co-generation power plant of Nirma Ltd.
✓ As standby arrangement of power two diesel driven DG Sets of 500 KVA is
envisaged. This D.G set will be operational only during the power failure conditions
or on emergency. Fuel consumption will be HSD 5 KL/day.
✓ High tide and low tide demarcation as per CRZ notification 2011 was conducted
through Institute of Remote Sensing (IRS), Anna University, Chennai had carried out
the required surveys and field measurements for the demarcation of CRZ
boundaries. Proposed location of Jetty along the Bhavnagar Creek falls in CRZ-I A,
CRZ-IB and CRZ-III, which is permissible activity as per CRZ Notification 2011.
✓ The REIA report prepared by M/s Indomer Coastal Hydraulics P. Ltd. and submitted by
the project proponent covers the baseline data, prediction and evaluation of impacts,
environmental management plan etc.
• Committee deliberated on CRZ status, CER, Permissions from the GMB, Land Possession
documents etc.
• During the presentation, PP presented as below:
✓ Application for CRZ Clearance recommendation has been already made dated
15.02.2020 to get the permission on time & expedite EC process. Subsequent
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 326 of 357
presentation before GCZMA Committee (i.e. 10th TCM dated 18.09.2020 & 56th meeting
of GCZMA dated 10.03.2021) & Site visits by GCZMA Officials (i.e. 11.01.2021 &
01.04.2021) have been carried out and presently proposal is at final stage of approval.
✓ PP ensured that they will submit the CRZ clearance Recommendation letter once
received from the authority.
✓ As an approach of sustainable development, The Company will contribute a stock of its
capital investment for the development of the neighboring environment. In view of this
aspect, the Company will allot 6 crores to monitor the surrounding environment
periodically through corporate environment responsibility. Detailed CER activities with
monitorable targets is submitted.
✓ Further, PP presented that GMB NOC for development of Jetty Project is applied on
15/07/2019 which is under process.
✓ GMB NOC for EIA study was granted on 24/08/2017. GMB NOC for development of
Jetty Project is applied on 15/07/2019 which is under process. They have also
approached GMB to consider our proposal as per the port policy at the time of
application
✓ PP request your kind authority to issue Environment Clearance with condition for
obtaining GMB permissions prior commencement of any project activities.
✓ While discussion regarding Land possession documents, Committee observed that Part
of jetty land (28.9 ha) is under possession of Nirma Ltd. and other in Government Waste
Land (2 ha). Application submitted to obtain permission from the Revenue Department
on 27.06.2019, which is under final consideration.
✓ After last SEAC Meeting dated 20.07.2021, as discussed during the meeting, they
approached to the Collector Office for issuance of Land. In response to their request
Collector & District Magistrate Office is seeking Environment Clearance for issuance of
Land vide their letter no. jamin/3/industry/8124/2021 dated 22.07.2021.
✓ PP requested for issuance of the Environment Clearance with condition for obtaining
Land Possession prior commencement of any project activities.
✓ The baseline study which was carried out between September to November, 2017 (Post
Monsson) & April 2018 to May 2018 (Pre Monsoon). With reference to ToR granted by
SEAC, public hearing was originally scheduled on 15th April 2020 and was finally held
on 12th October 2020 which is being delayed due to nationwide covid pandemic. Then
after, proposal for grant of EC has been uploaded on site dated 21.12.2020, which was
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 327 of 357
accepted by SEIAA.
✓ It is rapid EIA report. As per the OM vide no. 15-3/2009-IA-III dated 03rd November,
2009, Bhavnagar Coastal stretches are not falling under list of coastal stretches where
shoreline changes has been observed.
✓ Action Plan along with budgetary provision for issues raised during public hearing
including written representation received during public hearing has been included in final
EIA report under Section 7. However, revised action plan with concrete mitigation
measures for issues raised during public hearing including written representation
received during public hearing is submitted.
✓ Compliance of Terms of Reference (ToR) is included in the EIA report. However, the
comments raised by SEAC has been addressed and an addendum has been added to
the EIA report.
✓ They have prepared detailed conservation plan for the study area & got it approved from
competent authority. Same is submitted.
✓ Valid Certificate of accreditation issued by the NABET, QCI. Valid NABET, QCI
certificate is submitted.
• Committee was of the view that the Environmental and CRZ Clearance to the project is
primarily under provisions of EIA Notification, 2006 and CRZ Notification, 2011. It does not
tantamount to approvals/consent/permissions etc required to be obtained under any other
Act/Rule/regulation. Hence, the Project Proponent is under obligation to obtain approvals
/clearances under any other Acts/ Regulations or Statutes as applicable to the project.
• Committee found compliance of the ToR satisfactory.
• Considering the facts above and merit of the case, the SEAC, hereby recommend to
grant the Environmental Clearance to the proposed project subject to the strict
compliance of the following conditions:
Conditions with which Environment Clearance is recommended:
SPECIFIC CONDITIONS:
1. The provisions of the CRZ Notification of 2018 shall be strictly adhered to by M/s Nirma
Ltd. No activity in contradiction to the provisions of the CRZ Notification shall be carried
out by Nirma Ltd.
2. The Environmental and CRZ Clearance to the project is primarily under provisions of EIA
Notification, 2006 and CRZ Notification, 2011. It does not tantamount to
approvals/consent/permissions etc required to be obtained under any other
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 328 of 357
Act/Rule/regulation. The Project Proponent is under obligation to obtain approvals
/clearances under any other Acts/ Regulations or Statutes as applicable to the project.
3. Nirma Ltd. shall obtain prior permission from GMB.
4. All the recommendations, EMP, mitigation measures, environmental protection
measures and safeguards proposed in the EIA report of the project prepared by M/s:
Indomer Coastal Hydraulics P. Ltd. and commitments made during presentation before
SEAC and proposed in the EIA report shall be strictly adhered to in letter and spirit by
Nirma Ltd.
5. Nirma Ltd. shall obtain all necessary permissions from different Government
Departments / Agencies before commissioning their activities.
6. Nirma Ltd. shall obtain necessary permission from the Gujarat Maritime Board for marine
structure, if required, before commencing their activities.
7. Nirma Ltd. shall ensure that there shall be no discharge of any effluent/sewage in to
marine environment.
8. Dredging shall be carried out as and when require as mention in EIA report. All
conditions of the CRZ clearance to be followed in letter and spirit.
9. Disposal of dredged to be generated during maintenance dredging shall be done as per
the recommendations of scientific study carried out by Indomer, which is part of EIA
report.
10. No groundwater shall be tapped to meet with the water requirements during the
construction and/or operation phases.
11. Nirma Ltd. shall ensure that there shall be no damage to the existing mangrove patches
near the site and also ensure the free flow of water to avoid damage to the mangrove (If
any).
12. Nirma Ltd. shall ensure that there shall not be any discharge of pollutants in to Sea,
Creek etc., which affects the marine water and marine ecology like discharge from
barges, accidental spillage of oils from barges etc.
13. Nirma Ltd. shall take up green belt development activities in propose project premises.
Nirma Ltd. shall take up mangroves plantation to be suggested in CRZ Clearance in
consultation with the Forests Department / GEER Foundation / Gujarat Ecology
Commission. A comprehensive plan for this purpose has to be submitted to the Forests
& Environment Department SEIAA and MoEF&CC.
14. Detailed traffic control management plan shall be prepared and its recommendations
shall be strictly followed / adhered to in order to reduce adverse impacts and to avoid
problems to fishermen.
14 SIA/GJ/NCP/63481/2019 M/s. Quantum Environment Engineers
Survey No. 467/1, Near Vadodara Municipal
EC Reconsi
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 329 of 357
Corporation Sewage Treatment Plant, opp. Cargo Motors, Munjmahuda, Tal & Dist: Vadodara
deration
Category of the unit: 7 (da)
Project status: Expansion
• Project proponent (PP) has submitted online application vide no. SIA/GJ/NCP/63481/2019
on dated 31/05/2021 for obtaining Environmental Clearance.
• SEIAA issued TOR to PP vide letter dated 15/07/2020.
• Project proponent has submitted EIA Report prepared by M/s. En-vision Enviro
Technologies Pvt. Ltd based on the TOR issued by SEIAA.
• Public hearing was carried out on dated 04/05/2021 at Akota Atithigruh, Opp. Alka Society,
Near Akota Water Tank ,BPC road, Vadodara, Gujarat for proposed expansion project.
• This is an existing CBWTF facility and proposed for expansion of CBWTF as mentioned
below:
Sr.
no.
Name of the
Activity at
CBWTF
Quantity
MT/Day
Remarks
Existing Proposed Total
1 Incineration 1.175 3.825 5.0 Working hour 20
2 Autoclave 3.0 0.0 3.0 Working hour 20
3 Shredder 4.0 0.0 4.0 Working hour 13
Types of units to be set at CBWTF:
Sr. No.
Facility
Capacity Working hours per day and no. of
days per year
Waste to be
Handled
(MT/Day)
E P T
1. Incinerator
50 kg/hr x 1 No.
-50 kg/hr x 1 No. 250 kg/hr x 1
No 20 hr and 365 days
5.0
- 250 kg/hr x 1
No.
2. Autoclave
125 kg/Hr x 1 No.
25 kg/hr x 1 No.
-
125 kg/Hr x 1 No.
25 kg/hr x 1 No.
20 hr and 365 days
3.0
3. Shredder
150 kg/Hr x 2 Nos.
- 150 kg/Hr x 2
Nos. - -
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Details of project activity to be carried out for proposed CBWTF site:
• Details of transportation system for collection of BMW.
➢ The bio-medical waste collected will be transported to the CBWTF in a fully covered
vehicle designed as per the CPCB guideline for CBMWTF. Such vehicle shall be
dedicated for transportation of bio-medical waste only. Depending upon the volume
of the wastes to be transported, the vehicle may be a three-wheeler, light motor
vehicle or heavy duty vehicle. The vehicle shall be labeled with the bio-medical
waste symbol (as per the schedule IV of the BMWM rule) and shall display the
name, address and telephone number of the CBWTF
• Brief about Segregation, Storage &Type of treatment:
➢ Only segregated waste will be collected from the source point. Storage of the
untreated and treated Bio Medical waste in a proper way as clearly labelled &
in designated storage areas only as per the guideline. Waste shall be store in
leak proof bags and properly sealed containers.
➢ Cleanliness of roads and storage area is done regularly to prevent
accumulation of dust and waste material. Treated waste will be stored at
separate storage area.
➢ Adequate storage will be provided for Treated, Untreated BMW and other Hazardous wastes
• Reuse/ Recycle of BMW:
➢ Disinfected materials (Shredded plastic, glass etc.) will be sent to authorized recyclers
• Proposal of online monitoring system for parameters to be monitored in line with
Central Pollution Control Board (CPCB) guidelines:
➢ PM, CO and CO2 will be monitored through online monitoring system
• The project falls under B1 category of project activity 7(da) as per the schedule of EIA
Notification 2006.
• PP was called for Video conference meeting for presentation on dated 15.07.2021.
• Salient features of the project including Water, Air and Hazardous waste management as
below,
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Sr.
no
.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing:0.80
Proposed:1.75
Total: 2.55
Details of EMP
Sr. No
Unit
Capital Cost
(INR in Lacs)
Recurring cost (INR in Lacs per Annum)
Remarks Operating Cost
Maintenance Cost
Total Recurring
Cost
1 Air Pollution
Control 37 14.6 7 21.6
Collection unit/Cyclone Separator Air Cooler Gas neurilazation unit
Filter unit
2 Water
Pollution Control
3 2 0.4 2.4 ETP, STP
3
Solid and Hazardous
Waste Management
1 4.8 0 4.8 Membership & disposal cost of common facility
4 Occupational
Health 1.75 1.3 0.6 1.9
PPE, Medical checkup, OHC
5 Fire and Safety
8 0 2.5 2.5
Fire fighting equipments, Fire hydrant
system
6 AWH
Monitoring 2 3.9 0.1 4 -
7 Green belt
development 1.5 0 0.5 0.5
Additional green belt
development.
8 CER 1.75 - - - -
Total 56 26.6 11.1 37.7 -
Rs. 56 lakh
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Details of CER
Sr. No.
Area CER –Proposed Planned
Activities Village
Year wise budget (INR in Lakhs) for
CER Activities
1st
Years
2nd
Years
3rd
Years
Grand Total
1 Educati
on
Providing scholarship to 2
bright students of 10th /
12th class who goes for
further education
Akota,
Kalali,
0.15
0.15
0.15
0.45
School kit (Bag, Notebooks, Stationary
accessories distribution in schools
0.05
0.05
0.05
0.15
2 Health
Contribution in organization of medical
health camp, Payment of medical bills of need people from the
area
Talsat,
Samiyala
0.33
0.33
0 0.66
3 Environ
ment
Contribution in providing dust bins for Solid Waste
Management system Bill,
Bhaili
0.07
0.07
0.05
0.19
Tree plantation in villages with tree guard
0.1 0.1 0.1 0.3
Year wise Total (INR in Lakhs) 0.7 0.7 0.3
5 1.75
Rs. 1.75 Lakh
B Total Plot area
( sq. meter)
Existing: 1,000
Sq. m.
Proposed:
1,245 Sq. m.
Total: 2,245 Sq.
m.
Green belt area,/Tree Plantation area
( sq. meter)
Existing: 160
Sq. m.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 333 of 357
Proposed: 581
Sq. m.
Total: 741 Sq.
m.
C Employment generation Existing: 22
Proposed: 15
Total: 37
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
Ground water
Status of permission from the concern authority.
Facility falls in SMALL
category as per MSME
certificate and freshwater
requirement is less than
10KLD. Hence, facility is
exempted from obtaining
the CGWA permission.
ii
Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(V) Domestic 0.28 1.1 1.38 -
(W) Gardening 0.8 1.6 2.4 -
(X) Industrial
Process 1.5 0 1.5
Washing 0.09 1.91 2.00
Boiler 0 0 0
Cooling 0 0 0
Others 0 0 0
Industrial Total 1.59 1.91 3.5
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Grand Total
(A+B+C) 2.67 4.61 7.28
(4.08 KLD
fresh + 3.2
KLD
recycled)
10) Total water requirement for the project: 7.28 KLD
11) Quantity to be recycled:3.2 KLD
12) Total fresh water requirement: 4.08 KLD
iii
Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(N) Domestic 0.25 1.00 1.25
(O) Industrial
Process 0 0 0
Washing 0.07 1.88 1.95
Boiler 0 0 0
Cooling 0 0 0
Others 0 0 0
Total Industrial
waste water 0.07 1.88 1.95
Total (A + B + C) 0.32 2.88 3.2
iv Treatment facility within premises with capacity [For existing and Proposed]
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
➢ 2 KLD ETP having primary and tertiary treatment
v Mode of Disposal & Final meeting point
Domestic:
STP (2KLD Capacity) & treated water will be used for green belt
Industrial:
ETP and treated water will be reused Industrial purpose
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE,
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 335 of 357
CHWIF etc.
Name of Common facility
➢ Not any
Membership of Common facility (CF)
➢ Not any
Simplified water balance diagram with reuse/recycle of waste water
vii Reuse/Recycle details (KLD)
[Source of reuse & application area]
Total reuse 3.2 KLD
Source of waste water for reuse with quantity
Application area with quantity
Characteristics of waste water to be
reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
Treated water from ETP – 1.95 KLD
Industrial (Washing)1.95 KLD
pH: 7-8 COD: 70-90 mg/l BOD: 10-20 mg/l TDS: 1,220-1,280 mg/l TSS:50-60 mg/l
As per the Characteristics of ETP treated water, it is completely feasible to reuse in the said application area.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 336 of 357
Treated water from STP – 1.25 KLD
Greenbelt -1.25 KLD pH: 6.5-8.5 COD: 40-50 mg/l BOD: 10-20 mg/l TDS: 80-100 mg/l TSS:10-20 mg/l
Feasible to reuse
E Air
i Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA
etc.
Existing & Proposed
-
Sr.
no.
Source of
emission
With
Capacity
Stack
Height
(meter)
Type
of
Fuel
Quantity
of Fuel
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air
Pollution
Control
Measures
(APCM)
Existing
- - - - - - -
Proposed
1 D.G. set
(30 kVA) 11
Diese
l 0.264
SPM
SO2
NOX
Adequate
Stack
height
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing & Proposed
-
Sr.
no.
Source of
emission
Type of
emission
Stack/Vent
Height (meter)
Air Pollution
Control Measures
(APCM)
Existing
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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1 Incinerator*
(50 kg/hr)
PM
NOX
HCl
Total Dioxins and Furans
Hg
30 Cyclone Separator
Ventury Scrubber
Proposed (after expansion)
2 1 Incinerator
(250 kg/hr)
PM
NOX
HCl
Total Dioxins and Furans
Hg
30
(Dry Technology) Collection unit/Cyclone Separator Air Cooler Gas neutralization unit Filter unit
*Existing Incinerator will be removed
-
iii Fugitive emission details with its mitigation measures.
• Incineration ash is stored in a designated closed area
• All internal roads will be RCC or paved
• Airborne dust will be controlled by sprinkling of water
• Maintenance of air pollution control equipment is being carried out regularly
• Provision of PPE (dust mask) to workers involved in waste handling
• The coverage of greenbelt around the plant consisting acts a barrier so that noise does not propagate outside.
• Good housekeeping is maintained in the plant.
• The open area will be covered with either greenbelt or paved surface to avoid dust during transportation within plant.
F Hazardous waste
(as per the Hazardous and Other Wastes (Management and Transboundary Movement)
Rules 2016.
Existing & Proposed
i
Sr. no.
Type/Name of Hazardous
waste
Specific Source of generation
Category and
Schedule
Quantity (MT/Annum)
Disposal Method
Existing
Proposed
Total
1 Incineration Ash
Existing Incinerator (50 kg/hr)#
Schedule-I &
Category 20 -20 0
Collection, Storage, Transportation
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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Proposed Incinerator (250 kg/hr)
37.2 0 150 150
and sent to nearest TSDF for landfill
2 ETP Sludge ETP
Schedule-I &
Category 35.3
0 2 2
Collection, Storage, Transportation and sent to nearest TSDF for landfill
3
Disinfected materials
(Shredded plastic, glass
etc.)
Autoclave - 900 0 900 Send to authorized recycler.
4
Encapsulated Waste
(sharps, containers of
mercury waste)
Process -
2.5 2.5 5.0* Collection, Storage, Transportation and sent to nearest TSDF for landfill or disposed to In-house sharp pit.
*As sharps, containers of mercury waste
5 Used or
Spent Oil DG set
Cat.: 5.1
Sch-I 0 0.03 0.03
Collection, storage, transportation and sell to authorized recyclers
#Existing 50 kg/hr incinerator will be removed
ii Membership details of TSDF, CHWIF etc.
TSDF membership is obtained from
M/s. Eco care Infrastructures Pvt.
Ltd. On 28/10/2020 with membership
no. ECIPL-1832
CHWIF membership is obtained from
Nandesari Environment Control Ltd.
On dated 7/1/2014
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
• Not any
ii VOC emission sources and its mitigation measures
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 339 of 357
• Not any
• During the SEAC Video conference meeting dated 15.07.2021, Project Proponent (PP) and
their technical expert and EIA consultant from M/s. En-vision Enviro Technologies Pvt. Ltd
remain present and made technical presentation before the Committee.
• During the meeting, the project was appraised based on the information furnished in the EIA
Report, issues raised during public hearing and details presented during the meeting.
• The baseline environmental quality has been assessed for various components of the
environment viz. air, noise, water, biological and socioeconomic aspect. The baseline
environmental study has been conducted for the study area of 10 km radial distance from
project site for the period December 2019 to February 2020. Ambient Air Quality monitoring
was carried out for PM10, PM2.5, SO2, NOx, CO, VOC, HCl, Cl2 and Hg at Eight locations,
including the project site. Values conform to the prescribed standards for Ambient Air
Quality. The incremental Ground Level Concentration (GLC) has been computed using
“AERMOD”.The resultant concentrations are within the NAAQS. The modeling study proved
that the air emissions from the proposed plant would not affect the ambient air quality of the
region in any significant manner. The ambient air quality around the proposed project site
will remain within the National Ambient Air Quality Standards (NAAQS). High level of
pollutants are observed at project site as it is located within waste management zone of
Vadodara Municipal Corporation and Kaccha road is passing adjacent to the project site in E
direction. It is estimated that after establishment of proposed expansion project, these
concentrations are found to be well below the permissible NAAQS norms for rural/residential
zone and Industrial zone. Therefore, the proposed activity will not have any significant
adverse impact on the air environment.
• Following measures will be adopted by PP for mitigation measures of high level of pollutants
are observed at project site :
➢ Barrier sheet will be provided to avoid dispersion of dust in surrounding area.
➢ Dismantling work will be carried out in day time only.
➢ Trucks carrying waste will be covered with tarpaulin.
➢ Vehicles with PUC will be allowed.
➢ Water sprinkling will be carried out so that fugitive emission does not go outside the
premises.
➢ Waste will be covered to avoid fugitive emission
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 340 of 357
➢ Incineration ash is stored in designated closed area
• Risk assessment including prediction of the worst-case scenario and maximum credible
accident scenarios has been carried out. The detail proposed safeguard measures including
On-Site / Off-Site Emergency Plan has been covered in the RA report.
• Upon asking regarding QCI/NABET accreditation for preparation of EIA preparation for
proposed project, technical expert of PP informed that they have obtained QCI/NABET
accreditation for preparation of EIA/EMP report as per the amended EIA Notification vide
S.O. 648 (E) Dated 03.03.2016.
• This is an expansion project proposed for CBWTF site at Survey No. 467/1, Near Vadodara
Municipal Corporation Sewage Treatment Plant, opp. Cargo Motors, Munjmahuda, Ta. &
Dist: Vadodara, outside notified area. This CBWTF site is established before year 2006. Unit
is having Valid CCA of the Board for existing plant. PP submitted CC&A compliance report
for existing plant. Source of water supply is bore well. Committee noted that PP has
addressed there is no legal court case and public complaint against unit. PP presented one
show cause notice issued by GPCB and its compliance reply submitted at GPCB was
presented by PP during meeting. Total Plot area is 2245 Sq m. CGWA permission is
exempted as raw water requirement for proposed expansion project is below 10 KLD.
Committee noted that PP has addressed action plan for issues raised during public hearing
for proposed project.
• Looking to siting criteria showing Vishwamitri River at 470 meter distance and residential
habitat at 300 meter distance from proposed CBWTF site, Committee insisted for
clarification regarding compliance of siting criteria. Technical expert of PP informed that this
proposed facility is situated at solid waste management cell running by Vadodara Municipal
Corporation and proposed CBWTF facility, is at higher level than nearby Vishwamitri River
and existing facility of CBWTF established in year of 2003 and residential habitat is not
major issue at that time. After detailed deliberation at length regarding siting criteria
compliance, Committee insisted for submission of justification regarding increase in
residential habitat area in year of 2003 to year of 2021 with Google map and other
authenticated proof for residential habitat at 300 meter from proposed CBWTF site, looking
to foul odor pollution potential and air pollution potential load of proposed CBWTF site. Also
Committee insisted for justification regarding why PP have not submitted proposal of
CBWTF site in area where compliance of siting criteria other than this proposed project site,
looking to proposed site in flood prone zone area of Vishwamitri River and residential habitat
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 341 of 357
at nearby proposed site. Also Committee insisted for submission of clarification regarding
this CBWTF facility is at higher level than nearby Vishwamitri River with authenticated proof
like super imposition of site on flood prone zone map of Vadodara Municipal Corporation.
Also Committee insisted for submission of request letter regarding proposal of CBWTF site
other than existing site at Vadodara Municipal corporation in past by PP, looking to not
fulfilling siting criteria for proposed project.
• Looking to layout plan, Committee insisted for revised layout plan with mentioning color
coding for existing and proposed project infrastructure, adequate green belt area as per
CPCB guideline, adequate size peripheral road with separate entry and exit, vehicle
washing area as per CBWTF guideline protocol, fire hydrant network in existing facility and
proposed area, assembly point, OHC area, fuel storage area etc.
• Committee deliberated on the synopsis of the proposed project, Capacity, technology,
Weightage Criteria (As per GPCB Guidelines), Ownership of the plot, Baseline study, BAT,
Comparison of Dry and Wet Technology, prevailing Guidelines/Rules published by
MoEF&CC and CPCB, mercury waste (MW) management, design of Incinerator, Autoclave,
Shredder and storage facilities, Layout plan, water balance, management of waste water,
Air emission and Hazardous wastes, Anticipated environmental impacts due to the proposed
project, Construction as well as Operation Phase impacts and Mitigation Measures,
Occupational Health Impacts and its mitigation measures, safety and health protection
measures, Risk assessment, DMP, Existing CBWTF and its compliance, measures to
control emission of Dioxin and Furan, Odour & Its Control Measures, EMP, CER, Certificate
of accreditation issued by the NABET, QCI to the environmental consultant, Fire NOC,
Green Belt etc.
• Committee noted the following:
✓ Project proponent assured that they will dismantle existing facility after obtaining valid
CTO from GPCB for new facility at proposed project.
✓ Proposal of CBWTF site and design of Incinerator.
✓ Types of waste to be stored, maximum time of storage, material of waste storage
containers.
✓ Waste collecting vehicles and its navigation through GPS.
✓ Design and operation of existing and proposed incinerator.
✓ They will provide training to all the members on all aspects of bio-medical waste
Management time to time and as required by members to create awareness among all
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the stakeholders involved in the subject.
✓ Handling and encapsulation of mercury waste
✓ The total industrial waste water & Domestic waste water generated from the proposed
project will be 12.70 KL/day. The same will be treated in proposed in –house ETP. The
treated water will be used for washing and scrubber along with fresh water to make the
whole system Zero Liquid discharge.
✓ PP submitted hazardous waste matrix mentioning source of generation, quantity and
Mode of disposal and committed to comply the Hazardous and Other Wastes
(Management and Transboundary Movement) Rules 2016.
• Looking to residential habitat and Vishwamitri River at nearby project site, Committee
insisted for proposal of dry static incineration process due to the reasons like (1) This
technology is a static incinerator with dry scrubbing system which does not generate any
industrial effluent, (2) This technology controls all the parameters w.r.t air prescribed under
BMW rule 2016, (3) Ensuring zero liquid discharge, (4) The corrosion rate is comparatively
less then Wet technology in place of proposal of conventional Incinerator for proposed
project and readdress ToR no- 9. Also Committee insisted for addendum to EIA report
considering changes due to adoption of dry static incineration process with showing
changes made in EIA report in tabular form.
• Looking to dioxin and furan parameters generation from proposed project and ToR no- 7 for
installation of dioxin and furan with stack attached to incinerator, Committee insisted for
readdress ToR no-7 with notarized undertaking regarding justification for not installation of
online monitoring system for dioxin and furan parameters for stack attached to incinerator
along with proposal of mechanism adopted by PP for control of Dioxin and Furan
parameters like there is no any type of chlorinated waste procure at proposed site for
incineration.
• Also technical expert of PP mentioned that they have not facility for dioxin and furan
parameters monitoring for stack attached to incinerator and presented CPCB analysis report
of Dioxin and Furan parameter of before two years and hence Committee insisted for
submission of Notarized undertaking for regular monitoring and submission of analysis
report for Dioxin and Furan parameter from stack attached to incinerator, from third party
recognized NABL and MoEF&CC accredited laboratory as per CPCB guidelines for CBWTF
site.
• Committee noted that source of water is GIDC. Effluent generated from floor washing,
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vehicle washing will be treated in proposed in-house ETP and treated effluent will be
reused/recycled back in plant. Hence, Unit will maintain Zero Liquid Discharge (ZLD). PP
has proposed Incinerator for treating of Bio-Medical Wastes. Committee insisted for submit
revised air matrix with mentioning fuel consumption details for existing and proposed
incinerator. Also Committee insisted for status of fire NOC for existing CBWTF facility from
competent authority and revised EMP with mentioning fire hydrant network, OHC, revised
dry static basis incinerator etc. cost in it.
• After detailed discussion, Committee unanimously decided to consider the project in
one of upcoming meeting after submission of following documents and submission
of addendum EIA report considering adoption of dry static incineration process in
place of wet technology for Incinerator:
1. Submission of justification regarding increase in residential habitat area in year of
2003 to year of 2021 with Google map and other authenticated proof for
residential habitat at 300 meter from proposed CBWTF site, looking to foul odor
pollution potential and air pollution potential load of proposed CBWTF site.
2. Justification regarding why PP have not submitted proposal of CBWTF site in
area where compliance of siting criteria other than this proposed project site,
looking to proposed site in flood prone zone area of Vishwamitri River and
residential habitat at nearby proposed site.
3. Submission of clarification regarding this CBWTF facility is at higher level than
nearby Vishwamitri River with authenticated proof like super imposition of site on
flood prone zone map of Vadodara Municipal Corporation.
4. Submission of request letter regarding proposal of CBWTF site other than
existing site at Vadodara Municipal corporation in past by PP, looking to not
fulfilling siting criteria for proposed project.
5. Revised layout plan with mentioning color coding for existing and proposed
project infrastructure, adequate green belt area as per CPCB guideline, adequate
size peripheral road with separate entry and exit, vehicle washing area as per
CBWTF guideline protocol, fire hydrant network in existing facility and proposed
area, assembly point, OHC area, fuel storage area etc.
6. Revised proposal of dry static incineration process due to the reasons like (1)
This technology is a static incinerator with dry scrubbing system which does not
generate any industrial effluent, (2) This technology controls all the parameters
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w.r.t air prescribed under BMW rule 2016, (3) Ensuring zero liquid discharge, (4)
The corrosion rate is comparatively less then Wet technology in place of proposal
of conventional Incinerator for proposed project and readdress ToR no- 9.
7. Readdress ToR no-7 with notarized undertaking regarding justification for not
installation of online monitoring system for dioxin and furan parameters for stack
attached to incinerator along with proposal of mechanism adopted by PP for
control of Dioxin and Furan parameters like there is no any type of chlorinated
waste procures at proposed site for incineration.
8. Notarized undertaking for regular monitoring and submission of analysis report
for Dioxin and Furan parameter from stack attached to incinerator, from third
party recognized NABL and MoEF&CC accredited laboratory as per CPCB
guidelines for CBWTF site.
9. Submit revised air matrix with mentioning fuel and its consumption details for
existing and proposed incinerator.
10. Status of fire NOC for existing CBWTF facility from competent authority and
revised EMP with mentioning fire hydrant network, OHC, revised dry static basis
incinerator etc. cost in it.
• PP submitted reply for the above mentioned points on 03.08.2021.
• Proposal was considered in the SEAC VC meeting dated 01.09.2021.
• During the presentation, PP presented as below:
✓ Facility is in operation since year 2003 within waste management zone of V.M.C. when
no major residential areas were located within 500 m. Google maps submitted and PP
stated that there was marginal increase in the residential habitat area within 500 m
radius from the project site from year 2003-2021.
✓ Till date no public compliant has been filed by the nearby residents regarding foul odour
or air pollution from their facility. No other suitable site was available with VMC and as it
is already located with waste management zone of VMC, they have allotted additional
adjoining land for the said expansion project of CBWTF. Project area is not listed in the
low lying area of the Vadodara City as per the Flood Response Plan-2021 of V.M.C. and
existing facility is not hampered by flood in past. They are going to dismantle the existing
facility and new facility will be constructed after considering plinth height of 1 m.
✓ Further, as per the siting criteria mentioned in clause No. 5 (b) of the Revised Guidelines
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for Common Bio-medical Waste Treatment and Disposal Facilities by CPCB dated
21/12/16, we have obtained Consent to Establish from GPCB vide outward No. 18531
dated 03/11/2020 and adopted the following practices: Best available technologies for
CBWTF i.e. Incineration and Dry Air Pollution Control Devices, Stringent standards for
operation of the CBWTF, Zero liquid discharge scheme for effluent discharge
✓ Area does not fall under list of low lying area affected due to floods in Vishwamitri River.
The elevation profile of Vishwamitri varies around 21 m to 23 m near the project site
while the elevation of Project Site is around 32 m. Hence, project site is at higher level
than nearby Vishwamitri River.
✓ They are going to dismantle existing facility and establish the new facility as per the
above layout plan, it is not possible to demarcate existing structures of the same layout.
However, Boundary of the existing plot is demarcated on proposed layout. Separate
existing layout is also provided
✓ They will adopt the Dry Air Pollution Control System instead of wet system. Accordingly,
following figures/particulars will be revised: Water Consumption: From 17.28 KLD to 7.28
KLD, Industrial Waste Water generation: From 11.45 KLD to 1.95 KLD, Total waste
water: From 12.7 KLD to 3.2 KLD, ETP Sludge: From 8 TPA to 2 TPA.
✓ Considering the nearby residential area, facility has adopted following additional control
measures: Adoption of best available technologies (BAT) by the proponent of CBWTF.
From the different technologies, Incineration is most feasible technology after
considering Environmental, Technical & Economical aspects. Further, incinerator is
designed as per the CPCB guideline. Adoption of stringent standards for operation of the
CBWTF. Adoption of zero liquid discharge by the CBWTF
✓ As per the CPCB guideline for CBWTF published on 21st December, 2016 and letter
issued by CPCB to the SPCB, vide letter No. B-31011/BMW(61.1)/2019/WMD-
I/9996.10030 dated 17/12/2019; it is not mandatory to install online monitoring system
for Total dioxin and furans. We ensure you that we will install the same once it becomes
mandatory. The notarized undertaking for the same is submitted
✓ Mechanism adopted for control of Dioxin and Furan parameters is submitted. :
✓ Dioxin and furan are formed from the thermal breakdown of organic materials combined
with transitional metals and chlorinated compounds. Dioxin are chemically formed at
temperature above 200°C & completely destroyed at 800°C. Reformation of dioxin
occurs, when the temperature lies between 200°C to 400°C. Chlorine availability and
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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process temperature are the two important factors responsible for dioxin formation.
Chlorine input has a definite role in formation of dioxin and furan. As per the Office
Memorandum of MoEF&CC vide File No. 18-15/2016-HSMD dated 30/05/2016, it is
mandatory to phase out use of chlorinated plastic bags, gloves and blood bags. Hence,
no chlorinated materials are utilized at present. To reduce the precursors essential for
formation of Dioxins & Furans, proper combustion in secondary chamber by maintaining
minimum temperature of about 1050 +/- 50 oC and a residence time of at-least 2
seconds will be ensured. Flue gas temperatures will be dropped from 500°C to less than
220°C by adopting heat exchanger system.
✓ Notarized undertaking for regular monitoring and submission of analysis report for Dioxin
and Furan parameter from stack attached to incinerator, from third party recognized
NABL and MoEF accredited laboratory as per CPCB guidelines for CBWTF site is
submitted.
✓ Revised Air matrix with detailing of fuel and its consumption for existing and proposed
incinerator is submitted.
✓ They ensured that they will initiate the process to obtain fire NOC as per the Factory Act
etc. from the competent authority of Gujarat State after construction of proposed facility.
Copy of fire NOC will be submitted to SEAC once they received the same. Accordingly,
they will submit the application to the concerned authority within three weeks’ time &
undertaking for the same is also submitted. EMP has been revised by considering cost
of fire hydrant network, OHC, revised dry static basis incinerator etc.
• Committee noted that PP has proposed to adopt Dry technology for proposed total capacity
of CBWTF and they have proposed all the mitigation measures for the probable pollutants.
PP also ensured to comply all the prevailing guidelines of CPCB/MoEF&CC for CBWTF.
• Effluent generated from floor washing, vehicle washing will be treated in proposed in-house
primary, secondary and tertiary ETP and treated effluent will be reused/recycled back for
lime slurry preparation purpose. Hence, Unit will maintain Zero Liquid Discharge (ZLD). PP
has proposed Incinerator for treating of Bio-Medical Wastes. Fuel used will be HSD.
• Compliance of ToR was found satisfactory.
• Considering the above mentioned facts and merit of the case, Committee
unanimously decided to recommend the project to SEIAA, Gujarat for grant of
Environment Clearance with the following specific conditions.
Conditions with which Environment Clearance is recommended:
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CONSTRUCTION PHASE: a. Water demand during construction phase shall be reduced by use of curing agents,
super plasticizers and other best construction practices. b. Project proponent shall ensure that surrounding environment shall not be affected due to
construction activity. Construction materials shall be covered during transportation and regular water sprinkling shall be done in vulnerable areas for controlling fugitive emission.
c. All required sanitary and hygienic measures shall be provided before starting the construction activities and to be maintained throughout the construction phase.
d. First Aid Box shall be made readily available in adequate quantity at all the times. e. The project proponent shall strictly comply with the Building and other Construction
Workers’ (Regulation of Employment & Conditions of Service) Act 1996 and Gujarat rules made there under and their subsequent amendments. Local bye-laws of concern authority shall be complied in letter and spirit.
f. Ambient noise levels shall conform to residential standards both during day and night. Incremental pollution load on the ambient air and noise quality shall be closely monitored during construction phase.
g. Use of Diesel Generator (DG) sets during construction phase shall be strictly equipped with acoustic enclosure and shall conform to the EPA Rules for air and noise emission standards.
h. Safe disposal of waste water and municipal solid wastes generated during the construction phase shall be ensured.
i. All topsoil excavated during construction activity shall be used in horticultural / landscape development within the project site.
j. Excavated earth to be generated during the construction phase shall be utilized within the premises to the maximum extent possible and balance quantity of excavated earth shall be disposed off with the approval of the competent authority after taking the necessary precautions for general safety and health aspects. Disposal of the excavated earth during construction phase shall not create adverse effect on neighboring communities.
k. Project proponent shall ensure use of eco-friendly building materials including fly ash bricks, fly ash paver blocks, Ready Mix Concrete [RMC] and lead free paints in the project.
l. Fly ash shall be used in construction wherever applicable as per provisions of Fly Ash Notification under the E.P. Act, 1986 and its subsequent amendments from time to time.
m. “Wind – breaker of appropriate height i.e. 1/3rd of the building height and maximum up to 10 meters shall be provided. Individual building within the project site shall also be provided with barricades.
n. “No uncovered vehicles carrying construction material and waste shall be permitted.” o. “No loose soil or sand or construction & demolition waste or any other construction
material that cause dust shall be left uncovered. Uniform piling and proper storage of sand to avoid fugitive emissions shall be ensured.”
p. Roads leading to or at construction site must be paved and blacktopped (i.e. – metallic roads).
q. No excavation of soil shall be carried out without adequate dust mitigation measures in place.
r. Dust mitigation measure shall be displayed prominently at the construction site for easy public viewing.
s. Grinding and cutting of building materials in open area shall be prohibited. t. Construction material and waste should be stored only within earmarked area and road
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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side storage of construction material and waste shall be prohibited. u. Construction and demolition waste processing and disposal site shall be identified and
required dust mitigation measures be notified at the site. (If applicable). SPECIFIC CONDITIONS
1. Project proponent (PP) - M/s. Quantum Environment Engineers-CBWTF shall remove
their existing Incinerator ( 50 Kg/hr) and the proposed CBWTF facility shall be based on
the Dry Technology in which consume less water for lime slurry making and Operated by
PLC with SCADA control auto system.
2. CBWTF shall comply conditions of revised Guidelines (Rev.2) for Handling, Treatment
and Disposal of Waste Generated during Treatment/Diagnosis/Quarantine of COVID-19
Patients published by CPCB vide no. B-31011/BMW (94)/2020/WM-I dated 19/04/2020.
3. CBWTF shall comply all the conditions/ Amendments of BMW Rules and Guidelines
issued by the CPCB from time to time.
4. CBWTF shall setup technology system as per CPCB guideline strictly comply the design
criteria for incinerator, autoclave and shredder as per the CPCB guidelines.
5. CBWTF shall allocate the separate fund of Rs. 1.75 Lakhs as committed before
SEAC. The entire activities [Distribution of school kit, Organizing medical health camp,
solid waste management and tree plantation] proposed under CER shall be part of the
Environment Management Plan (EMP) as per the MoEF&CC’s OM no. F. No. 22-
65/2017-IA.III dated 30.09.2020. This shall be monitored and the monitoring report shall
be submitted to the regional office of MoEF&CC as a part of half-yearly compliance
report and to the District Collector. The monitoring report shall be posted on the website
of the project proponent.
6. In case of any regulatory action including closure of any existing CBWTF is inevitable,
the respective SPCB/PCC may take action under the BMWM Rules including for making
alternate arrangement to ensure safe disposal of the bio-medical waste generated from
the member health care facilities of such default CBWTF through CBWTF located
nearby.
7. All the recommendations, mitigation measures, environmental protection measures and
safeguards proposed in the EIA report of the project prepared by M/s. En-Vision Enviro
Technologies Pvt. Ltd, Surat was submitted by project proponent vide letter no. NIL
dated 23.02.2021 and commitments made during presentation before SEAC and
proposed in the EIA report shall be strictly adhered to in letter and spirit.
8. CBWTF shall strictly ensure mercury waste management at health care facility as per
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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the Bio-Medical Waste Management Rules 2016.
9. CBWTF shall establish Standard Operating Procedure [SOP] for waste collection,
handling, transportation, treatment and disposal as per Biomedical Waste Management
Rules 2016 and amended time to time.
10. Consent to Operate [CTO] shall be obtained from GPCB under Air (Prevention & Control
of Pollution) Act, 1981 and Water (Prevention & Control of Pollution) Act, 1974 before
operation, failing which the Environmental Clearance herein shall be deemed to be
withdrawn.
11. CBWTF shall provide Continuous Emission Monitoring System [CEMS] and an
arrangement shall also be done for reflecting the online monitoring results on the
company's server, which can be assessable by the GPCB on real time basis.
12. Authorization from Gujarat Pollution Control Board shall be obtained as applicable under
Bio-Medical Waste Management Rules 2016.
13. CBWTF shall comply with the Environmental standards notified by Ministry of
Environment, Forest & Climate Change for incinerators along with the
technology/guidelines.
14. There shall not be any spillage from the transportation Vehicles.
15. CBWTF shall set up separate Environmental Management Cell for effective
implementation of stipulated environmental safeguards under the supervision of Senior
Executive.
16. All measures shall be taken to prevent soil and ground water contamination.
17. Complete Zero Liquid Discharge [ZLD] status shall be maintained all the time and there
shall be no drainage connection to discharge waste water from the premises.
WATER:
18. Total water requirement for the project shall not exceed 7.28 KL/day. The CBWTF shall
reuse/recycle 3.2 KL/day of treated waste water to use for Lime Slurry preparation along
with fresh water to make whole system zero discharge. Hence, fresh water requirement
shall not exceed 4.08 KLD and it shall be met through Bore well.
19. Prior permission from concerned authority shall be obtained for withdrawal of water, if
applicable.
20. The industrial effluent generation from the project (Washing) shall not exceed 1.95
KL/day.
21. Water meter shall be installed and its record of daily water consumptions shall be
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maintained.
22. Entire quantity of Waste water shall be treated in proposed ETP. (Cap 2 KL/Day)
23. The CBWTF shall provide adequate effluent treatment plant (ETP) comprises of Primary
and Tertiary treatment plants and it shall be operated regularly and efficiently so as to
ensure reuse for Lime slurry preparation within premises.
24. Separate energy meter shall be provided at ETP. A proper operation logbook of the ETP
containing records of quantities and qualities of treated effluent.
25. The domestic wastewater generation shall not exceed 1.25 KL/day for proposed
expansion project and it shall be treated in In-House STP.
26. Zero Liquid Discharge (ZLD) condition shall be maintained all the time with utilizing
treated effluent for Lime slurry preparation within premises.
27. All the pipelines carrying water/ waste water should be distinguished using colour coding
on raw water pipes and reuse lines of treated water.
28. CBWTF shall provide electromagnetic flow meter at the inlet & outlet of the water supply,
Inlet & outlet of the ETP and shall maintain a record of readings of each such meter on
daily basis.
29. The quantity of fresh water usage and water recycling shall be measured and recorded
to monitor the water balance as projected by the project proponent. The record shall be
submitted to the GPCB, State Level Environment Impact Assessment Authority &
Regional Office, MoEF&CC along with six monthly Monitoring reports.
AIR:
30. The CBWTF shall not exceed fuel consumption for Incinerator and stand-by DG set as
mentioned below:
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of
Fuel
Quantity of
Fuel
Type of emissions i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
HSD 2,500 lit/day
PM
NOX
HCl
Hg
Total Dioxins and Furans
(Dry Technology) Collection unit/cyclone Separator Air Cooler Gas Neutralization Unit Filter Unit
1
Incinerator – 2 250 kg/hr. (Proposed)
30 .0 Meters
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2.
D.G. set. (30 kVA) (Proposed)
11.0 Meter
Diesel
0.264 MT/d
ay
SPM SO2 NOx
Adequate Stack height and Acoustic
enclosures
31. CBWTF shall provide adequate stack height with flue gas generation sources as
mentioned above.
32. Treated flue gas emissions discharged through stack to atmosphere shall always be less
than specific emission standards.
33. Utilization of Diesel power generating sets is subject to power failure condition only. The
DG sets proposed as a source of power back up during operation phase should be of
enclosed type, low Sulphur diesel run and conform to rules made under the Environment
(Protection) Act, 1986. The DG sets should be subjected to periodic noise and stack
monitoring.
34. CBWTF shall provide adequate APCM comprises of Collection unit/ Cyclone Separator,
Air Cooler, Gas neutralization unit & filter unit.
35. Regular monitoring of ground level concentration of PM10, PM2.5, NOx, HCl,, Hg and
VOC shall be carried out at the site and downwind direction and its records shall be
maintained. Ambient air quality levels shall not exceed the standards stipulated by the
CPCB. If at any stage these levels are found to exceed the prescribed limits, necessary
additional control measures shall be taken immediately.
36. CBWTF shall strictly follow the odor control measures as suggested in environmental
management plan.
37. Proponent shall strictly follow the Environmental Monitoring program for ambient air
quality monitoring.
38. Treated flue gas emissions discharged through stack to atmosphere shall always be less
than CPCB stipulated emission standards.
SOLID/ HAZARDOUS WASTE:
39. CBWTF shall strictly comply with the rules and regulations with regards to handling and
disposal of Hazardous waste in accordance with the Hazardous and Other Wastes
(Management and Transboundary Movement) Rules 2016, as may be amended from
time to time. Authorization of the GPCB shall be obtained for collection / treatment /
storage / disposal of hazardous wastes.
40. Hazardous wastes shall be dried, packed and stored in separate designated hazardous
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waste storage facility with pucca bottom and leachate collection facility, before its
disposal.
41. CBWTF shall obtain necessary permission from the nearby TSDF site and CHWIF.
(Whichever is applicable)
42. Trucks/Tankers used for transportation of hazardous waste shall be in accordance with
the provisions under the Motor Vehicle Act, 1988, and rules made there under.
43. The design of the Trucks/tankers shall be such that there is no spillage during
transportation
44. All possible efforts shall be made for Co-Processing of the Hazardous waste prior to
disposal into TSDF/CHWIF.
45. Hazardous / Solid waste management shall be as below:
Sr. no.
Type/Name of Hazardous
waste
Specific Source of generation
Category and
Schedule
Quantity (MT/Annum)
Disposal Method
Existing
Proposed
Total
1 Incineration Ash
Existing Incinerator (50 kg/hr)#
Schedule-I &
Category 37.2
20 -20 0 Collection, Storage, Transportation and sent to nearest TSDF for landfill
Proposed Incinerator (250 kg/hr)
0 150 150
2 ETP Sludge ETP
Schedule-I &
Category 35.3
0 2 2
Collection, Storage, Transportation and sent to nearest TSDF for landfill
3
Disinfected materials
(Shredded plastic, glass
etc.)
Autoclave - 900 0 900 Send to authorized recycler.
4
Encapsulated Waste
(sharps, containers of
mercury waste)
Process -
2.5 2.5 5.0* Collection, Storage, Transportation and sent to nearest TSDF for landfill or disposed to In-house sharp pit.
*As sharps, containers of mercury waste
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5. Used or Spent
Oil DG set
Cat.: 5.1
Sch-I 0 0.03
0.0
3
Collection, storage, transportation and sell to authorized recyclers
#Existing 50 kg/hr incinerator will be removed
46. Authorized end-users shall have permissions from the concerned authorities under the
Rule 9 of the Hazardous and Other Wastes (Management and Transboundary
Movement) Rules 2016
47. Management of fly ash (If any) shall be as per the Fly ash Notification 2009 & its
amendment time to time and it shall be ensured that there is 100% utilization of fly ash to
be generated from The CBWTF.
48. Treated biomedical waste shall be sold out to GPCB authorized recyclers only. Used oil
shall be use within the premises or burnt into in-house incinerator. Treated glass waste
shall be sold out to GPCB authorized recycler only. Sharp waste shall be disposed
through TSDF after encapsulation and possible try for metal recovery.
SAFETY
49. The occupier/manager shall strictly comply the provisions under the Factories Act 1948
and the Gujarat Factories Rules 1963.
50. CBWTF shall strictly comply with the provisions made in Manufacture, Storage and
Import of Hazardous Chemicals Rules (MSIHC) 1989, as amended time to time and the
Public Liability Insurance Act for handling of hazardous chemicals etc. Necessary
approvals from the Chief Controller of Explosives and concerned Govt. Authorities shall
be obtained before commissioning of the project. Requisite On-site and Off-site Disaster
Management Plans have to be prepared and implemented.
51. Main entry and exit shall be separate and clearly marked in the facility.
52. Sufficient peripheral open passage shall be kept in the margin area for free movement of
fire tender/ emergency vehicle around the premises.
53. Sufficient number of fire extinguishers shall be provided near the plant and storage area.
54. All necessary precautionary measures shall be taken to avoid any kind of accident
during loading, unloading and transportation of biomedical waste.
55. The project management shall ensure to comply with all the environment protection
measures, risk mitigation measures and safeguards mentioned in the Risk Assessment
report.
56. Only flame proof electrical fittings shall be provided in the plant premises.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
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57. All the waste storage room shall be marked with color coding as per the CPCB
guidelines time to time.
58. CBWTF shall tie up with nearby health care facility for any emergency cases.
59. Personal Protective Equipment (PPEs) shall be provided to workers and its usage shall
be ensured and supervised.
60. First Aid Box in The CBWTF shall be made readily available in adequate quantity.
61. Training shall be imparted to all the workers on safety and health aspects of biomedical
waste handling.
62. Occupational health surveillance of the workers shall be done and its records shall be
maintained. Pre-employment and periodical medical examination for all the workers shall
be undertaken as per the Factories Act & Rules.
63. Transportation of biomedical waste shall be done as per the provisions of the Motor
Vehicle Act & Rules.
64. The company shall implement all preventive and mitigation measures suggested in the
Risk Assessment Report.
65. Necessary provision shall be made for firefighting facilities within the complex.
NOISE: 66. The overall noise level in and around the plant area shall be kept well within the
standards by providing noise control measures including engineering controls like
acoustic insulation hoods, silencers, enclosures etc. on all sources of noise generation.
The ambient noise level shall confirm to the standards prescribed under The
Environment (Protection) Act, 1986 & Rules.
67. Noise should be controlled to ensure that it does not exceed the prescribed standards.
During night time the noise levels measured at the boundary of the building shall be
restricted to the permissible levels to comply with the prevalent regulations.
GREEN BELT AND OTHER PLANTATION: 68. CBWTF shall develop green belt of 741 Sq. m i.e. 33 % of the total plot area) within
premises as committed before the SEAC. Green belt shall be developed with native
plant species that are significant and used for the pollution abatement as per the CPCB
guidelines. It shall be implemented within 3 years of operation phase in consultation with
GPCB.
69. Drip irrigation / low-volume, low-angle sprinkler system shall be used for the green belt
development within the premises.
OTHER CONDITIONS
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70. Rain water recharging of surface as well as rooftop runoff shall be undertaken and the
same water shall be used for the various activities of the project to conserve fresh water
as well as to recharge ground water. Before recharging the surface run off, pre-treatment
must be done to remove suspended matter.
71. CBWTF shall join and participate financially and technically for any common
environmental facility infrastructure as and when the same is taken up either by the
Industrial Association or GIDC or GPCB or any such authority created for this purpose
by the Govt. GIDC.
72. The area earmarked as green area shall be used only for plantation and shall not be
altered for any other purpose.
73. Energy Conservation measures such as LEDs light for common lighting of areas,
signage etc should be adopted.
74. All the commitments undertakings given to the SEAC during the appraisal process for
the purpose of environmental protection and management shall be strictly adhered to.
75. CBWTF shall also comply with any additional condition that may be imposed by the
SEAC or the SEIAA or any other competent authority for the purpose for the
environmental protection and management.
76. In the event of failure of any pollution control system adopted by The CBWTF. The
CBWTF shall be safely closed down and shall not be restarted until the desired
efficiency of the control equipment has been achieved.
77. CBWTF must strictly adhere to the stipulations made by the Gujarat Pollution Control
Board (GPCB), State Government and any statutory authority.
78. During biomedical waste unloading there shall be no spillages and garland drain shall be
constructed to avoid mixing of accidental spillages with domestic wastewater or storm
water.
79. Pucca flooring impervious layer shall be provided in the work areas, biomedical waste
storage areas and chemical handling areas to minimize soil contamination.
80. No further expansion or modifications in the plant likely to cause environmental impacts
shall be carried out without obtaining prior Environment Clearance from the concerned
authority.
81. The above conditions will be enforced, inter-alia under the provisions of the Water
(Prevention & Control of Pollution) Act,1974, Air (Prevention & Control of Pollution) Act,
1981, the Environment (Protection) Act, 1986, Hazardous & other Wastes (Management
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 356 of 357
and Transboundary Movement) Rules, 2016 and the Public Liability Insurance Act, 1991
along with their amendments and rules.
82. CBWTF shall comply all the conditions mentioned in "The Companies (Corporate Social
Responsibility Policy) Rules, 2014" and its amendments from time to time in a letter and
spirit.
83. CBWTF shall ensure that the CBWTF complies with all the environment protection
measures, risk mitigation measures and safeguards recommended in the EMP report
and Risk Assessment study report as well as proposed by project proponent.
84. CBWTF shall earmark adequate funds to implement the conditions stipulated by SEIAA
as well as GPCB along with the implementation schedule for all the conditions stipulated
herein. The funds so provided shall not be diverted for any other purpose.
85. CBWTF shall inform the public that the project has been accorded environmental
clearance by the SEIAA and that the copies of the clearance letter are available with the
GPCB and may also be seen at the Website of SEIAA/SEAC/GPCB. This shall be
advertised within seven days from the date of the clearance letter, in at least two local
newspapers that are widely circulated in the region, one of which shall be in the Gujarati
language and the other in English. A copy each of the same shall be forwarded to the
concerned Regional Office of the Ministry.
86. It shall be mandatory for the project management to submit half-yearly compliance report
in respect of the stipulated environmental clearance terms and conditions in hard and
soft copies to the regulatory authority concerned, on 1st June and 1st December of each
calendar year. The project authorities shall earmark adequate funds to implement the
conditions stipulated by SEIAA as well as GPCB
87. Concealing factual data or submission of false/fabricated data and failure to comply with
any of the conditions mentioned above may result in withdrawal of this clearance and
attract action under the provisions of Environment (Protection) Act, 1986.
88. The SEIAA may revoke or suspend the clearance, if implementation of any of the above
conditions is not found satisfactory.
89. CBWTF in a time bound manner shall implement these conditions. The SEIAA reserves
the right to stipulate additional conditions, if the same is found necessary.
90. CBWTF shall inform the GPCB, Regional Office of MoEF&CC and SEIAA about the date
of financial closure and final approval of the project by the concerned authorities and the
date of start of the project.
268thmeeting of SEAC-Gujarat, Dated 01.09.2021
Page 357 of 357
91. This environmental clearance is valid for seven years from the date of issue.
92. Any appeal against this environmental clearance shall lie with the National Green
Tribunal, if preferred, within a period of 30 days as prescribed under Section 16 of the
National Green Tribunal Act, 2010.
The meeting ended with a vote of thanks to the chair. ***
Minutes approved by:
1. Shri Akshay Kumar Saxena, Chairman, SEAC
2. Dr. S. C. Pant, Vice Chairman, SEAC
3. Dr. M. N. Patel, Member, SEAC
4. Shri D. C. Chaudhari, Member, SEAC
5. Shri J. K. Vyas, Member, SEAC
6. Shri Anand Zinzala, Member, SEAC
7. Shri B. M. Tailor, Member, SEAC
8. Shri A. V. Shah, Secretary, SEAC
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