SIA/GJ/IND2/152395/2 020 PI Industries Limited Plot No. 237 ...

268thmeeting of SEAC-Gujarat, Dated 01.09.2021

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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


- 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


adequate

height

SO2 100 ppm

NOx 50 ppm

3 Power Plant 1

30

NG


adequate

height

SO2 100 ppm

NOx 50 ppm

4 Power Plant 2

30

NG


adequate

height

SO2 100 ppm

NOx 50 ppm

Proposed

1

GG Power Plant

30 Natural

Gas

12000 Sm3/Da

y


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


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


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


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,

multicyclone

& 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


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


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


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



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ACETONITRIL

20 MT RM Storage/ MPP-4A

Atmospheric

Fire and Health Hazard


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,


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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.



• 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


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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.


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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.


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.


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


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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


Project status: New

• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/152953/2020 for

obtaining Environmental Clearance.





• 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*


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. 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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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


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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


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


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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


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28 Hydroxy

Chloroquin

e Sulphate

747-36-4 API Hydroxy

Chloroquine

Sulphate

- 747-364 Antimalaria

29 R &D product



• The proposal was considered in the SEAC video conference meeting dated 12.03.2021






• 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


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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


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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.






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


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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


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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


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Total

100 Nos

D WATER

D-1

Source of Water Supply

(GIDC, Bore well, Surface water, Tanker supply etc...)


➢ 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 --


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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


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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


➢

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:


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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


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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.

➢ 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)


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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


SO2 100 ppm

NOx 50 ppm

Bag filter

&water

scrubber

3 Hot Air

Generator 30

Briquettes

of bio coal

0.2 T/hr


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


HCl 20 mg/Nm3

SO2 40 mg/Nm3

11

Two stage Water scrubbers followed by Alkali scrubber


NH3 30 mg/Nm3

11

Two stage Water scrubber followed


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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


SO2 171


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


HCL 31


SO2 52

15 2- Chlorobenzimidazole 98%

Ammonia 80

➢ Requirement of the scrubbing media (KL per Day) considering solubility


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(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


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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


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


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


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


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


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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


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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


2.60 4.00 highly flammable and toxic

4 Isopropyl Alcohol


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


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Nearest General Hospital : The Cambay General Hospital

Name of Antidotes to be store in plant : 5




• Project proponent (PP) and their Technical Expert from M/s. Shree green Consultants

remain present during video conference meeting.




• 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


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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


• 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


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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


Project status: New







• 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

https://en.wikipedia.org/wiki/Cardiogenic_shock



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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

https://en.wikipedia.org/wiki/Vasospasm


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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


Stage i.e. n-1, n-2, etc.

Name of API in which Intermediate Used/ End use of said

CAS no. (API)


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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



https://en.wikipedia.org/wiki/Vasospasm


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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




• Salient features of the project including Water, Air and Hazardous waste management are

submitted.




• Project proponent (PP) and their Technical Expert from M/s Bhagwati Enviro Care Pvt. Ltd


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• 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


(Rs. in Crores):

Total Project

19 Crores



(Rs. In Crores)

Land

developing

& Building

8.0

Machinery 10

Other 1.0

A-2 Details of Environmental Management Plan (EMP) As below:


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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


Percentage:

1.581 Crore &8.32%


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


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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% 0.38


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.


− Rs 1.6 Lacs for Education at Primary School of Gamdi & Vanch village.


− Rs 1.6 Lacs for drinking water facility at Ramol village.

− Rs 3.0 Lacs for drinking water facility at Narol village.


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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


Lease Agreement between M/s. Metrochem Capital Trust Limited & Ms. Asceneo

Labs Pvt. Ltd.

B-1 Plot area

Total Plot area

1843 Sq. m.


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)


Total

70 Nos.

D WATER

D-1



GIDC Vatva Water Supply


➢ Yes We obtained Permission.

D-2



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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


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




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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



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]


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


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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➢ Not Applicable


-

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.

-


Common Spray Drying Facility at CEMSPL Dhanot for Spray Drying.



Capacity of STP: 1.5 KLPD Modular STP



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



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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


➢ 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.


➢ Common Spray Drying Facility of Chhatral Environment

Management System Pvt. Ltd. Dhanot


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



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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



(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



-

Sr. no.

Specific Source of emission (Name of the

Product & Process)

Type of emission



Measures (APCM)

1 Reaction Vessel

HCl

SO2 15

Two Stage Water Scrubber

2 Reaction Vessel

NH3

HBr 15

Two Stage Water Scrubber

Note:


No Gaseous Raw Material


Show in Hazardous Waste Table



Show in Hazardous Waste Table



Yes


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



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Note:





calculations shall be incorporated in EMP details separately.



-

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


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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.


Storage,

Transportation

and send to

Co processing

unit.

6 Distillation

Residue

From

Distillation


Storage,


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process of

solvent.

Transportation

and send to

CHWIF for

incineration.

7

Spent Solvent

From

Distillation

process of

solvent.


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.


(For HW management)


➢ We are applied for TSDF & CHWIF membership certificate


(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


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1 STP Sludge

STP 0.2 Used as manure within premises.


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


➢ Attached as Annexure - I


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➢ 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



-

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.


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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.


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.


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-

Type of

Process

Safety measures including Automation

-- --


-

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


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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-


Due to the proposed project Fire NOC will not applicable.


-



Area provided for OHC: 15


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.



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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


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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


• 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.



condition:




dated 10/07/2019 & 14/11/2019.








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5. Total number of products manufacturing shall not exceeding two (2) at a given point of time


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.













WATER

10. Total water requirement for the project shall not exceed 34.5 KLD. Unit shall reuse 1.3 KLD


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



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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.







advanced treatment.

AIR


flue gas matrix.



21. Two Stage Water Scrubber system shall be provided for control of process gas emission.






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.





chemicals.



















applicable.


together.


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.


Project status: New

• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/174902/2020on

dated 05.02.2021for obtaining Environmental Clearance.





• 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


1. No of Manufacturing Plants: 1 no.


• 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)


Said API is used for/End Use of said

API

Stage i.e.

n-1, n-2, etc.


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



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• 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


• Salient features of the project including Water, Air and Hazardous waste management are

as under:


A-1 Total cost of Proposed Project (Rs. in Crores):

Total Project

1 Crore


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.


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 %



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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.)


2 % 0.02


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 %


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


-

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.


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


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


Measures (APCM)

1 D. G. Set (65 KVA)

6 Diesel 11 Liter/Hr Particulate Matter

SO2 NOX




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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: --


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.



-

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


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


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.



Quantity (MT/Annum)


1 -- -- -- --


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


➢ 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)


➢ 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


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.


-

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: --

-


Unit will take Fire NOC certificate from concern authority.


-



Area provided for OHC: 117.58 m2


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.




• 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.





✓ 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.




✓ 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).






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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



✓ 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.



condition:










4. Total number of products manufacturing shall not exceeding nine (9) at a given point of time







WATER


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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.


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.


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.







advanced treatment.

AIR


flue gas matrix.



17. VOC Scrubber system shall be provided for control of process gas emission.






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respective items.

GREENBELT AREA

28. The PP shall develop green belt within premises (170 Sq. m i.e. 30.8 % of the total plot


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.





chemicals.



















applicable.



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together.


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



• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/175373/2020 for

obtaining Environmental Clearance.





• 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.


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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


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


Total 112 00 112



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/


Said API is used for/End Use of said

API Stage of Intermedi

Name of APin which

CAS No.


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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 --- --- ---


6 Clozapine 5786-21-

0 API --- --- --- Treatment of

Schizophrenia

7 Olmesartan Medoxomil

144689-63-4 API --- --- ---


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.











• Project proponent (PP) and their Technical Expert from M/s. Excel Envirotech remain



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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.


technical expert/consultant from Excel Envirotech remains present in the meeting and made

presentation before committee.



Sr. Particulars Details


of 357

no.


(Rs. in Crores):

Existing

Proposed Total

1.75 Crores 0.50 Crores 2.25 Crores


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


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


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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


➢ 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-1 Plot area

Existing

Proposed Total

1036 Sq. m. 00 Sq. m. 1036 Sq. m.


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➢ 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


Existing

Proposed Total

15 5 20

D Water

D-1


(GIDC Bore well, Surface water, Tanker supply etc...)

GIDC water supply.


➢ The water supply is from GIDC water supply.

D-2


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


KLD


KLD Remarks


20.9

13.2 34.1 --


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


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.


Category Existing

KLD


KLD


KLD Remarks

(E) Domestic 2.2 0.0 2.2 Used for

Gardening

(F) Industrial

Process 3.4 15.8 19.20 After


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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 --


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.




➢ 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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-


D-5 Treatment facilities:


Capacity of STP: 3 KLD



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.


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.


➢ 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



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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]


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


Type of Fuel




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.


Type of emission



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:








➢ 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:








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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


(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


(MSW and others)

Not Applicable


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


• 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


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


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


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


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


16.67 15.92 96 0.3 0.6 3.60

13

Dapoxetine

Hydrochloride


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


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


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


Hg 94 82.8 88 0.9 2.5 8.51


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


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


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


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


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


(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.


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.


(Hydrogenation process, Nitration process, Chlorination process, Exothermic

Reaction etc.)

Types of Safety Measures including Automation


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Process


For Chlorination, proper scrubbing system should be required. SOP will be prepared for handling of chlorine gas. Chlorine emergency kit will be provided.


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


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.



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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.


✓ Scrubbing liquor will be treated in ETP.




✓ Fire load calculation mentioning fire water storage (Cap: 20 KLand 20 Nos of foam

trolley (Cap: 50 Kgs).




• 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.


2021.

• Project proponent (PP) and their Technical Expert from M/s. Excel Envirotech remained




of 357

✓ Water balance diagram was discussed.

✓ Fire load calculation.

✓ Revise fire water storage tank capacity.



condition:



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.








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.




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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achieving on-land discharge norms prescribed by the GPCB.







advanced treatment.

AIR

14. Unit shall not exceed fuel consumption and provide APCM and Stack height as mentioned

in flue gas matrix.



17. Alkali scrubbing system shall be provided for control of Process gas emission.






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.





chemicals.



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applicable.


together.


chemicals.

6 SIA/GJ/IND2/175379/2020

MAHADEV CHEMICALS

Plot no. C-1/264, Phase –II, GIDC Vatva, Ahmedabad-382445

EC Reconsideration








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• 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


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


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)


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)


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


4. Sulphanilamide 63-74-1 n-2

Intermediate

Sulfamethoxazole

723-46-6


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











• 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


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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.


technical expert/consultant from M/s Envycraft Environmental Services remains present in

the meeting and made presentation before committee.


waste management are submitted as follows



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(Rs. in Crores):


0.6684crores 0.1611 Crores 0.829crores


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


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


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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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


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


GIDC/RM/ABD/TFR/VTW/SHD/2715 Dated: 19/06/2007 B-1 Plot area


760Sq. m. 00 Sq. m. 760Sq. m.


➢ 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 %



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9 4 & 5 (Contract base) 14

D WATER

D-1



GIDC water supply


➢ GIDC supply is available to the unit.


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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Source of waste water for reuse in KLD (From where it is coming)


Characteristics of waste water to be reused (COD, BOD, and TDS etc.)


- - - -


➢ Nil

Summary of water requirement

Existing KLD


Total after Expansion KLD

Remarks


14.10 1.6 15.7

GIDC Water Supply


NIL NIL Nil

Total fresh water requirement (C)

14.10 1.6 15.7


i.e. A = B + C


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


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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



6. 4-amino pyridine-3-Sulphonic acid



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)


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


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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

-




Capacity of STP: -- NA


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.


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


➢ Not Applicable

D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.


➢ 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


➢ 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)




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)




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


Existing

Sr. No.

Specific Source of emission(Name of the Product &

Process)

Type of Emission



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.


Type of Emission



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:


No gaseous raw material will be used.


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.


F Hazardous waste


Note:

➢ Priorities for HW Management: Reuse/Recycle within premises, Sell out to actual users

having Rule-9 permission, TSDF/CHWIH.





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


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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.


Membership of Ecocare Infrastructure Pvt Ltd.


➢ M/s. Novel Spent Acid Management Dated: 23th Feb, 2019

➢ Ecocare Infrastructure Pvt Ltd. vide letter No.: ECIPL-296


(MSW and others)

Fly Ash

Sr. no.

Type/Name of Other

wastes


(Name of the Activity, Product etc.)

Quantity (MT/Annum)



1 Fly Ash Agro waste/Briquettes 35 -- 35

Collection, storage, transportation & send to Brick manufacturer OR farmer for

agricultural purposes.


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.


The Following methodology to be adopted during LDAR study:


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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.


➢ Not required.

H SAFETY details



-

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


• 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.


Type of Safety measures


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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



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.


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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.


-

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


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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Number of Contractual person/Labour : @ 4

Area provided for OHC: @16


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.


➢ 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



➢ Greenbelt development plan with 728.90 Sq m (30 %) of plot area.


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• 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.



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


2021.

• Project proponent (PP) and their Technical Expert from M/s. Envycraft Environmental

Services remained present during video conference meeting.


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✓ 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.



condition:















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.


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


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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.





shall be treated in ETP. It shall not be disposed off through soak pit/ septic tank.


advanced treatment.

AIR


flue gas matrix.



15. Two Stage Alkali Scrubber, Condenser followed by receiver followed by dipping tank shall

be provided for control of Process gas emission.






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


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GPCB.





chemicals.



















applicable.


together.


chemicals.

m) Unit shall provide chlorine leakage control emergency kit and FRP hood with

scrubber system for chlorine safety.


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7 SIA/GJ/IND2/175649/2020

Aariva Pharma Pvt. Ltd

Survey No. 809 Samlaya, Savali, Vadodara

EC Reconsideration



• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/175469/2020on






• 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


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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


in adults 18 years of age or

older to empty the colon (large

intestine, bowel) before




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


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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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


Stage of

Intermediate n-1, n-2, etc


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

https://en.wikipedia.org/wiki/Topical_medication

https://en.wikipedia.org/wiki/Dental_caries

https://en.wikipedia.org/wiki/Dental_caries

https://en.wikipedia.org/wiki/Thyroid_cancer

https://en.wikipedia.org/wiki/Hyperthyroidism

https://en.wikipedia.org/wiki/Hyperthyroidism

https://en.wikipedia.org/wiki/Isotopic_labeling


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

- - -


in adults 18 years of age or older

to empty the colon (large intestine,

bowel) before




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


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


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


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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 proposal was considered in the SEAC video conference meeting dated 05.01.2021




• Project proponent (PP) and Technical expert from Satva Environ Consultancy remains


• 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



1. Submit technical justification regarding Benzyl alcohol, Benzyl Benzoate etc. products


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.



technical expert/consultant from M/s Satva Environ Consultancy remains present in the

meeting and made presentation before committee.


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



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.


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:



(Rs. in Crores):


1.5Crores 0.50Crores 2.0Crores


of 357


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


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


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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


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


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-1 Plot area


6300 Sq. m. NIL 6300 Sq. m.


Sr No.

Description of Area Existing After Expansion

Sq. m Sq. m For API Plant

1 Manufacturing Area - 650


of 357

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


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



5 10 15

D WATER

D-1



Own Bore well



of 357


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


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


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i.e. A = B + C

Reuse/Recycle details (2.5 KLD) with feasibility.


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.


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


of 357

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


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)


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

-


In house evaporator



Capacity of STP: 2.5



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 -


of 357

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


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.


➢ 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.


➢ 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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Existing Water Balance

After Expansion Water Balance

E AIR


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


of 357



(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:



➢ 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.


➢ 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


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


Note:




➢ Quantification of hazardous waste shall be based on mass balance

and calculations shall be incorporated in EMP details separately.



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


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


of 357

Recycler

4. Solvent residue

Distillation Unit

26.3 NIL 0.8 0.8


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


Transportation, sell to Authorized

Party having permission of

Rule -9

7. Sodium Sulfate

Pregabline 28.4 NIL 22.56 22.56


Transportation, sell to Authorized

Party having permission of

Rule -9


(For HW management)

We have membership of TSDF


➢ Not Applicable


(MSW and others)

Sr. no.



Quantity (MT/Annum)



1 NA NA NA NA NA NA


G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of


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


➢ 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.


• 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



-

There is no storage Tank


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


➢ 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


Type of Safety measures


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:


Reaction etc.)

-

Type of

Process


NO NO


-

Total Plot Area: 6300


of 357

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

-


We will obtained after getting NOC from GPCB


-



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


✓ 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


of 357

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.



condition:















WATER

6. Total water requirement for the project shall not exceed 9.88 KLD. Unit shall reuse 2.5KLD


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.


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


of 357

be no drainage connection from the premises and no wastewater discharge outside

premises by any means.



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.


waste water during any shut down of in-house MEE.


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.







advanced treatment.

AIR


flue gas matrix.








respective items.

GREENBELT AREA

23. The PP shall develop green belt within premises (2079 Sq. m i.e. 33 % of the total plot area)


of 357




GPCB.





chemicals.



















applicable.


together.


chemicals.


of 357

8 SIA/GJ/IND2/190249/2

020

VRS LAB

PLOT NO - 621-P/39, GIDC INDUSTRIAL

ESTATE, PANOLI Anklesvar, Bharuch

EC

Reconsi

deration


Project status: New








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


of 357

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


Sr. No.

Name of the Product

CAS No. (Product)

Type/ Category

of Product (API/

Intermediate)

Stage of

Intermediate

n-1, n-2, etc


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


(n-2) Intermediate of Levocetirizine

130018-77-8

Antihistamine

3 Para Chloro Benzhydryl Piperazine


(n-2) Intermediate of Cetirizine

83881-51-0

Antihistamine

4 10-Methoxy Iminostibene


(n-1) Intermediate of Oxcarbazep

28721-07-5

Anticonvulsants


of 357

ine

5 4-Amino-1,2,4 –Triazole


(n-3) Intermediate of Fluconazole

86386-73-4

Anti fungal

6 2,4-Difluoro-Alpha-(1H-1,2,4-Triazole) Acetophenone


(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


(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


of 357

3 sant

2-Azaspiro [4.5]decan-3-one

64744-50-9 Intermediate (n-3)

Intermediate of Gabapentin

60142-96-3

Anticonvulsant



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)


(n-4) Intermediate of Diclofenac Sodium

15307-79-6

Anti Flammatory

(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)



15307-79-6

Anti Flammatory

(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)



15307-79-6

Anti Flammatory

18

Clarithromycin 81103-11-9 API -- -- -- Anti Biotic

Erythromycin oxime


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


(n-2) Intermediate of Oxcarbazepine

28721-07-5

Anticonvulsants

21

Metformin 657-24-9 API -- -- -- Used to control


of 357

high blood sugar

22

Losratan 114798-26-4



114772-54-2

Intermediate

(n-4) Intermediate of Losratan

114798-26-4

Antihypertensive

2-butyl-4-chloro-5-formylimidazole



114798-26-4

Antihypertensive




114798-26-4

Antihypertensive


114798-36-6

Intermediate


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


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


130018-77-8

Antihistamine


of 357

ne (2-chloroehtyl)-chloromethyl amine

1-[((4-chlorphenyl)phenyl- methyl]-4-(toluene-4-sulfonyl)-piperazine

163837-56-7

Intermediate


130018-77-8

Antihistamine

1-(4-[((4-chloorphenyl)phenyl- methyl]- piperazine-1-yl)-ethanol

164726-80-1

Intermediate


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.


2021.

• Project proponent (PP) and their Technical Expert from M/s. Ozone Enviro Tech remained


• Revised Salient features of the project submitted as under:



3.5 Crores


of 357


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


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


6.0 86.73 -- 86.73

4 Fire & Safety 15.0 -- 3.20 3.20

5 AWH Monitoring

1.0 -- 1.00 1.00


2.10 -- 1.80 1.80


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…


of 357

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-1 Total Plot area ( sq. meter) 1787.50 Sq. m.


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


GIDC Water Supply




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


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)


KLD Remarks

Total water requirement for the project (A) 37

Quantity to be recycled (B) 11.9



(37.0 = 25.1 + 11.9)






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. --



KLD Remarks

(G) Domestic 1.5


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(H) Industrial

Process 16.2

Washing 2.0

Boiler 0.8

Cooling 0.5


R&D 0.3


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


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.




of 357

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. --


-

Sr. no.

Source of emission

With Capacity


Type of Fuel


Type of emissions i.e.

Air Pollutant

s


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


of 357

-

E-3 Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx

etc.)

-

Sr. no.



Type of emission



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.




Sr. no.



(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


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


26)


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.


R&D SCH-I/28.4 0.5 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.

-


Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Ankleshwar for Common TSDF & CHWIF


Not Applicable


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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➢ 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


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


-

Type of Process


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.

--


-

Total Plot Area: 1787.50





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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


-



Area provided for OHC: 15 Sq. Meter provided in Ground Floor at Admin Building


Nearest General Hospital : Welcare Hospital – 3.00 KM

Name of Antidotes to be store in plant :

--


✓ 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.



condition:




dated 10/07/2019 & 14/11/2019.




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WATER

8. Total water requirement for the project shall not exceed 37.0KLD. Unit shall reuse 11.9 KLD


exceed 25.1KLD and it shall be met through GIDC only.


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..





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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advanced treatment.

AIR


flue gas matrix.



20. Two Stage water and alkali Scrubber shall be provided to control process gas emission.






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.





chemicals.






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applicable.


together.


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


Project status: New








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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


114772-54-2

Intermediate of Losratan


83857-96-9


11477-55-3

2-Butyl-5-chloro-3-[2’(2H- 114798-

file:///C:/Users/ICON/Desktop/OET/Overx%20Pharmachem/PRODUCT%20LIST%20API%20-%2050%20to%2060%20MT-10KL-BEIL.xlsx%23RANGE!A1


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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


15307-93-4

Intermediate of Diclofenac Sodium


15308-01-7


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.


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


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


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


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


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


144701-48-4

Antihypertensive

7 Losartan Potassium & it’s intermediate

114798-26-4



114772-54-2

Intermediate

(n-4) Intermediate

of Losratan

11479

8-26-4

Antihyperte

nsive

file:///C:/Users/ICON/Desktop/OET/Overx%20Pharmachem/PRODUCT%20LIST%20API%20-%2050%20to%2060%20MT-10KL-BEIL.xlsx%23RANGE!A1


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83857-96-9

Intermediate

(n-3) Intermediate

of Losratan

11479

8-26-4

Antihyperte

nsive


11477-55-3

Intermediate


11479

8-26-4

Antihypertensive


114798-36-6

Intermediate


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


(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


(n-2) Intermediate

of

Tranexamic

Acid

1197-

18-8

Used to

treat heavy

bleeding

during your

menstrual

period

4(Aminomethyl)cyclohexanecar boxilic acid


(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


(n-4) Intermediate of Cetirizine Dihydrochloride

83881

-52-1

Antihistamin

e

19 P- chloro Benzhydryl chloride


(n-3) Intermediate of Cetirizine Dihydrochloride

83881

-52-1

Antihistamin

e

20 P-chloro benzhydryl piperazine


(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


(n-3) Intermediate of Nebivolol HCI

12020

2-66-6

Antiplatelet

23 Bis-(2-chloroethyl amine)hydrochloride


(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


(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


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


14709

8-20-2


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


14709

8-20-2


26 Atorvastatin Calcium & it’s intermediate

134523-00-5


[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


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


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


72956

-09-3

Antihypertansive

4-(2,3-Epoxypropoxy) carbazole

51997-51-4

Intermediate


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


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


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


(n-3) Intermediate of Nimesulide

51803-78-2


O- Phenoxy Aniline



51803-78-2


O- Phenoxy Methane

N/A Intermediate


51803-78-2


31 Diclofenac Sodium & it’s intermediate

15307-79-6

API -- -- -- Anti Flammatory


15307-93-4

Intermediate


15307

-79-6

Anti Flammatory


15308-01-7

Intermediate


15307

-79-6

Anti Flammatory


15362-40-0

Intermediate


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


54965

-21-8

Anthelmintic

1,2,diamine-5-propyl thio benznene

66608-52-4

Intermediate


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






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• 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.


2021.




Sr. no.

Particulars Details

A


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


(KLD)


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


-- 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


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…


CER Rs. 7.80 Lakhs (2 %) Rs. 15.6 Lakhs (4 %)


-


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 /-




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 -- --


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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. --


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



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


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).


KLD Remarks



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(104.0 = 41.5 + 62.5)







Gardening Purposed

BOD-30 --

In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. --


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


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)


➢ Not Applicable


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.

-


For Domestic waste water: Capacity of STP – 3.0 KLD.


[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ➢ In-house ETP @ 30 KLD


CHARACTERISTICS BEFORE & AFTER TREATEMENT OF EFFLUENT

Sr. No.

Parameter



Boiler 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

--


➢ 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.



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➢ Common MEE Ms/ BEIL, Ankleshwer


➢ M/s. BEIL, Ankleshwar for Common MEE vide letter no BEIL/ANK/2021 dated 21/07/2021


E Air


SR. NO.

NAME OF FUEL QUANTITY


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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-

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.


(Product wise and Total).


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




F Hazardous waste management matrix (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:





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


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




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)


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%)


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.



159 Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 13 – 593.16 MT/Year)



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.


Raw Materials/Pr

oducts

33.1 0.2 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.


R&D 28.4 1.0 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.


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


Not Applicable




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



requirement MT/Month

Total quantity of solvent recovered MT/Month


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

--






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


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


➢ 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




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



Type of Process


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.




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.

--









Nearest Fire Station : Panoli GIDC – 0.91 Km


-



-



Area provided for OHC: 15 Sq. Meter provided in Ground


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Floor at Admin Building


Nearest General Hospital : Welcare hospital – 3.0 KM


--


✓ 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.



condition:


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.


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.


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


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.


advanced treatment.

AIR

18. Unit shall not exceed fuel consumption and provide APCM and Stack height as

mentioned in flue gas matrix.



21. Two stage Alkali Scrubber shall be provided for control of Process gas emission.






respective items.

GREENBELT AREA

27. The PP shall develop green belt within premises (908 Sq. m. i.e. 40 % of the total plot area)




GPCB.





chemicals.



of 357


















applicable.


together.


chemicals.


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



of 357

Project status: New








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


of 357

SOLUTION

8 DI-ETHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE


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


20 1-(3-CHLOROPHENYL) PIPERAZINE

65369-76-8


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


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


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


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


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


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


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


Sr. No.

Name of the Product CAS No. (Product)

Type/ Category of

Product (API/

Intermediate)


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


Intermediate of Imipramine

50-49-7 Antidepressants

https://www.webmd.com/allergies/picture-of-the-sinuses







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)


19794-93-5

Antidepressant

7 DI-METHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE OR DI-METHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE SOLUTION


Intermediate of Chlorpheniramine


8 DI-ETHYL AMINO ETHYL CHLORIDE HYDROCHLORIDE


Intermediate of Amiodarone

1951-25-3

Anti-arrhythmic

9 4- HYDROXY BENZYL ALCOHOL


Intermediate of Bisoprolol Fumarat

104344-23-2


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


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



19794-93-5

Antidepressant

20 1-(3-CHLOROPHENYL) PIPERAZINE

65369-76-8

Intermediate (n-2)


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

https://www.sigmaaldrich.com/catalog/search?term=111470-99-6&interface=CAS%20No.&N=0&mode=partialmax&lang=en&region=IN&focus=product

https://www.sigmaaldrich.com/catalog/search?term=111470-99-6&interface=CAS%20No.&N=0&mode=partialmax&lang=en&region=IN&focus=product


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


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


32 1-[2-[(7-CHLORO-1-BENZOTHIOPHEN-3-YL)METHOXY]-2-(2,4-DICHLOROPHENYL)ETHYL]IMIDAZOLE OR SERTACONAZOLE

99592-32-2


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


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


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


41 (8S,9S,10R,13S,14S,17 57-83-0 API -- -- Hormon


of 357

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


of 357

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














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• 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.


2021.






3.5 Crores


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


Details of EMP

Sr. No


(KLD)


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


6.0 46.47 -- 46.47

4 Fire & Safety 15.0 -- 3.20 3.20

5 AWH Monitoring

1.0 -- 1.00 1.00


1.41 -- 1.20 1.20


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


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…


CER Rs. 7.0 Lakhs (2 %) Rs. 14 Lakhs (4 %)



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 /-

-




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

--


470 Sq. m.(40% of total area) Inside - 256 Se. Meter Outside - 214 Sq. meter

C Employment generation 25 Nos

D Water

D-1


GIDC Water Supply



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


Scrubber 2.8

R&D 0.2


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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KLD Remarks





(44.4 = 29.1 + 15.3)







Gardening Purposed

BOD-30 --




KLD Remarks

(I) Domestic 2.5

(J) Industrial

Process 12.2

Washing 1.0

Boiler 1.0

Cooling 0.6


Scrubber 4.4

R&D 0.2


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)


➢ Not Applicable



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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.

-


For Domestic waste water: Capacity of STP: STP is not provided because domestic effluents send to low COD steam ETP.


[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ➢ ETP (Primary ) : 20 KLD


Sr. No.

Parameter



Boiler 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

--


➢ 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)



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➢ M/s. BEIL, Ankleshwar for Common MEE


E Air


SR. NO. NAME OF FUEL QUANTITY


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. --


-


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Sr. no.

Source of emission

With Capacity


Type of Fuel


Type of emissions i.e.

Air Pollutant

s


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.



Type of emission



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




F Hazardous waste management matrix (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:





Sr. no.




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




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


22)


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


31)


13 Aluminum chloride


11)


14 Phosphoric acid


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%)


7)

SCH- II / B 15


17 Sodium Bromide (25%)


6) +


34)

SCH- II / B 15

630 +

4 = 634

Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.



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%)


21)

SCH- II / B 15




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.


Raw Materials/Pro

ducts

33.1 0.2 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.


R&D 28.4 1.0 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.

-


Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Ankleshwar for Common TSDF & CHWIF


Not Applicable




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



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


EDC 40.80 39.45

IPA 70.65 68.20

--






condenser. --

G-3 VOC emission sources and its mitigation measures (Brief note on LDAR)



➢ 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


Storage details Name of major Hazardous chemicals

Remarks

Storage tanks (If any) --


of 357

Drums/Bags Acetone/ Liquid Ammonia/ MDC/ Hexane/ Acetonitrile/ THF/ Ethyl Acetate

Cylinder Ammonia, Hydrogen,

Bottle Bromine


➢ 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




-

Type of Process


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




--


-








Nearest Fire Station : Panoli GIDC - 0.91 Km


-




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-



Area provided for OHC: 15 Sq. Meter provided in Ground Floor at Admin Building


Nearest General Hospital : Welcare Hospital – 3.00 KM


--


✓ 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 .



condition:


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.


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


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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



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.



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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.







advanced treatment.

AIR





21. Two stage Scrubber (Water + Alkali) shall be provided for control of Process gas

emission.



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.




of 357



chemicals.



















applicable.


together.


chemicals.


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


of 357


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


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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


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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.


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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.






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


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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


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


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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


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


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3.04mX2.13m

Treatment scheme including segregation at source.


➢ 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


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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)


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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


Type of Fuel Quantity of

Fuel MT/Day



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)


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.


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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


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


Transportation and

Dispose to Registered

Recycler

4 Iron sludge

Mfg.

Process

(metanilic

Acid)

26.1 165.0


Transportation and Send

for co-processing or TSDF

5 Gypsum

sludge

Mfg.

Process

(Resist

Salt)

26.1 657


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


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.


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




• Project proponent (PP) and their Technical Expert from M/s. Green Circle remain present

during video conference meeting.


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➢ 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


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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 .



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 .


2021.

• Project proponent (PP) and their Technical Expert from M/s. Green Circle, INC remained



✓ 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.



condition:


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.


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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.


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.


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.







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AIR








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


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.


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


c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the



d) Unit shall adopt functional operations/process automation system including


e) PP shall carry out mock drill within the premises as per the prevailing guidelines of



f) PP shall install adequate fire hydrant system with foam trolley attachment within


g) PP shall take all the necessary steps for control of storage hazards within premises


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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.

12 SIA/GJ/IND2/59728/2020

M/s. Biosynth Industries

Plot No 1713 1715 1716 GIDC Sarigam, Taluka Umbergam, District Valsad

EC Reconsideration



• 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


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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




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


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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.




• 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.



technical expert/consultant from M/s Green Circle Incremains present in the meeting and

made presentation before committee.


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Existing

Proposed

Total

0.7226 Crores 1.5413 Crores 2.2639 Crores


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


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


- 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


- 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 %



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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.)


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”)



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.


Category

Existing 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


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





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.


Category Existing 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


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.


-

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.


For Domestic waste water: Capacity of STP: Not applicable as domestic water will be treated in in house ETP.


➢ 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


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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


➢ Sarigam clean Initiative CETP


➢ M/s. SARIGAM CLEAN INITIATIVE – CETP Sarigam for effluent, Membership Letter no SCI/CETP/2019-20/051 dated 12/10/2019



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E AIR


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.


Sr. no.

Source of emission

With Capacity


Type of Fuel

Quantity of Fuel

MT/Day

Type of emissions i.e. Air

Pollutants


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



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:





-

Sr. no.



Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Management of HW

Existing

Proposed Total


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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.


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-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.


➢ 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




➢ Controlled by having proper scrubbing system. ➢ VOCs detectors will be installed.

H SAFETY details


-

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


• 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


• FLP type light fittings will be provided.

• Proper ventilation will be available in Drum storage area.


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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:


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


Manufacturing of proposed products involve various unit operations like distillation, condensation, purification, filtration, drying, reduction, coupling and esterification.


Total Plot Area: 2829.07 m2




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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Unit will get Fire NOC after obtaining Environment Clearance.


-



Area provided for OHC: 15 sq.m


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.




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).


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.


✓ Fire load calculation mentioning fire water storage (Cap: 500 KL) and 4 Nos of foam


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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.


✓ Scrubbing liquor will be reused within premises or sold as per Hazardous waste Rules.



(Management and Transboundary Movement) Rules 2016. Also submitted area

adequacy for storage of raw material, products and machineries.



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.


in the upcoming SEAC meeting only after satisfactory submission of the following:


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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.


2021.

• Project proponent (PP) and their Technical Expert from M/s. Green Circle, INC remained



✓ 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



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condition:



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


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


and it shall be treated in ETP and ultimately disposed to CETP Sarigam. It shall not

be disposed off through soak pit/ septic tank.






AIR




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14. All hazardous solid waste shall be managed as mentioned in hazardous waste

matrix.



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


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.


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


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



f) PP shall install adequate fire hydrant system with foam trolley attachment within


g) PP shall take all the necessary steps for control of storage hazards within premises




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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


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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.


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


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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.




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.)


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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.


✓ 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.


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


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the competent authority.

10. Valid Certificate of accreditation issued by the NABET, QCI.




• 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


(Rs. in Crores): Six Hundred

Total Project Cost

Phase I -180 Crores

Phase II -420 Crores

Total -600 Crores



(Rs. In Crores)

Land -

Building 86.58

Machinery 94.02


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)


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1 Waste Water

No industrial effluent

generation

- - - -

2 Air - 0.02 - - 0.01


- 0.005 0.002

4 Fire & Safety - 0.15 - - 0.015

5 AWH Monitoring

- 0.5 - - 0.3


- 0.515 - - 0.025


Covered under sr.

no. 4 - - - -

Total 1.19 - - 0.352

Summary

Phase - I Phase - II

Cost of Project in Crores per Annum: 180 420


Percentage:

1.19

(0.4 %)


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


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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.


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.


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,


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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


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. -


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)


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 -


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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



(Whichever is applicable): Not Applicable

Proposed project is for development of jetty and auxiliary facilities. Hence, no industrial

wastewater generation.


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.



Capacity of STP: Septic tank/soak pit.



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.


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.


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• Not Applicable


• 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


E AIR


thereof:Not Applicable


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


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.


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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


(For HW management)

• Not Applicable


• Not Applicable


(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


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Product etc.)

1 Domestic and

operational

waste

Canteen

40 kg/day Through Municipality/ authorized

vendors


G-1

• Not Applicable


• Not Applicable


• Not Applicable

H SAFETY details



• There is no hazardous chemicals storage on site, however fire hydrant system as a part

of safety requirement will be provided.



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


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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.


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

04.%20GMB%20NOC%20Application%20Ack%20copy.pdf


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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

05.%20Application%20to%20Department%20for%20Industrial%20Land.pdf


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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;


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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


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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

01.%20Ack%20copy_GCZMA_19.02.2020.pdf


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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

03.%20GMB%20Permission_Oceanographic.pdf

03.%20GMB%20Permission_Oceanographic.pdf

04.%20GMB%20NOC%20Application%20Ack%20copy.pdf


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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:


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

12.%20Nirma%20Port%20-%20EIA%20Report%20-%2017.07.2021.pdf


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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


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Corporation Sewage Treatment Plant, opp. Cargo Motors, Munjmahuda, Tal & Dist: Vadodara

deration

Category of the unit: 7 (da)


• 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


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. - -


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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,


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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


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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.


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Proposed: 581

Sq. m.

Total: 741 Sq.

m.

C Employment generation Existing: 22

Proposed: 15

Total: 37

D Water

i


(GIDC Bore well, Surface water, Tanker supply etc...)

Ground water


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


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


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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


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,


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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)


Total reuse 3.2 KLD

Source of waste water for reuse with quantity

Application area with quantity

Characteristics of waste water to be



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.


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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


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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


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.


waste


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


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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)


i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents

• Not any

ii VOC emission sources and its mitigation measures


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• 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.


Report, issues raised during public hearing and details presented during the meeting.




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


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➢ Incineration ash is stored in designated closed area


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


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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.


✓ 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.




• 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.


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


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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


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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


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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.


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


Type of

Fuel

Quantity of

Fuel



Measures (APCM)

HSD 2,500 lit/day

PM

NOX

HCl

Hg


(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.


waste


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.


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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



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


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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.


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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

SIA/GJ/IND2/152395/2 020 PI Industries Limited Plot No. 237 ...

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