PROJECT PRE-FEASIBILITY REPORT - Environmental ...

PROJECT PRE-FEASIBILITY REPORT

For

AMENDMENT IN TORs

Of

PROPOSED PROJECT for

MANUFACTURING OF SYNTHETIC ORGANIC

CHEMICALS

(ENZYMES/PROBIOTICS/PREBIOTICS/API BY

FERMENTATION/BIOLOGICAL/CHEMICAL

ROUTES & SPECIALITY CHEMICALS FOR

PHARMA AND OTHER INDUSTRIES)

At

D-3/24/3, Dahej-III Industrial Estate, Taluka Vagara, Dist. Bharuch.

Project proponent

ROSSARI BIOTECH LTD.

Project Pre-feasibility Report

1

Project: Proposed project for manufacturing of Synthetic Organic Chemicals.

ENZYMES/PROBIOTICS/PREBIOTICS/API

CHAPTER – 1

EXECUTIVE SUMMARY The project is summarized in the below table:

Table1.1: Project Summary

PARTICULARS DETAILS

NAME OF THE UNIT

M/s. Rossari Biotech Ltd.

OCCUPIER Shri Sunil Srinivasan Chari , Shri Edward Menezes

REQUEST FOR AMENDMENT IN TORs

Request for amendment in TORs for following point:- 1. Change in Plot No in TORs Letter. 2. Change in Product list and its quantities. 3. Change in water requirement and water balance diagram. 4. Discharge of ETP treated effluent into CETP. 5. Extension in validity of TORs.

PRODUCTS The list of proposed products is provided in Chapter-2, table no. 2.1 at page no.3.

LOCATION D-3/24/3, Dahej-III Industrial Estate, Taluka Vagara, Dist. Bharuch.

NATURE OF PROJECT

Proposed project for manufacturing of Synthetic Organic Chemicals (Enzymes/ Probiotics/ Prebiotics/ API by Fermentation/Biological/Chemical routes and Speciality chemicals for Pharma and other Industries).

RESOURCES

Resource type Requirement Source

Phase1 After Phase2

Land 51218.35 m2 51218.35 m2 GIDC Dahej

Building 4334 m2 16685.61 m2 --

Raw-materials (Quantity in MT/M)

The product wise raw material consumption for each phase is attached as Annexure 2 of the pre-feasibility report.

The raw materials are available in Local/ Indian market and are also imported from foreign countries.

Water Domestic - 1.00 kl/day Industrial - 204.0 kl/day Gardening – 20 kl/day

Domestic - 2.00 kl/day Industrial - 376.00 kl/day Gardening – 20 kl/day

GIDC water supply Dept.

Power 648.87 kVA (Connected Load)

3396.06 kVA (Connected Load)

Gujarat Electricity Board

Fuel NG – 3816 Nm3/day LDO– 4095 ltr/day. Diesel- 28.1 LPH

NG – 8712 Nm3/day LDO– 9345 ltr/day. Diesel- 105.5 LPH

NG – GSPC LDO- Authorized Dealers Diesel- Authorized Local Dealers

Man-power 38 Nos 150 Nos To be employed from local area

POLLUTION POTENTIAL & MITIGATION MEASURES

Parameter Potential Mitigation

Phase1 After Phase2

Wastewater Domestic: 1.30 kl/day

Industrial: 50.00 kl/day

Domestic: 4.50 kl/day

Industrial: 130.00 kl/day

The domestic effluent will be disposed off through septic tank/ soak pit system.

Industrial wastewater is treated in ETP and treated water will be diverted to CETP inlet through GIDC underground drainage.

Letter of intent obtained from GIDC for CETP Discharge is attached herewith as Annexure-6


2



POLLUTION POTENTIAL & MITIGATION MEASURES

Parameter Potential Mitigation

Phase1 After Phase2

Air Emissions Emission norms for Boilers & DG set

PM < 150 mg/Nm3

SO2 <100 ppm

NOx < 50 ppm

Bag filters will be provided to the Spray Dryer.

The utility emissions will be from Boiler, Thermopac and D.G. Sets. We have proposed Natural Gas or LDO as fuel in boiler & thermopac and diesel as a fuel in DG set. Adequate stack height will be provided to Boiler, Thermopac and DG sets.

Minor quantity of solvents will be lost as handling losses in terms of fugitive emissions and some quantity of solvent is expected to be released in atmosphere as evaporation losses.

Raw Materials & Products are/will be stored in properly designed storage area and under good storage conditions to prevent any volatilities

Regular monitoring will be done of piping and fittings for checking of any leakages.

Good housekeeping will be maintained in the plant.

Hazardous & solid waste

ETP Waste (Cat. 34.3) : 15 TPM

Process Residue (Cat.26.1) :46.00 TPM

Used Oil (Cat. 5.1): 5 KL/Y

Discarded drums (Cat. 33.3): Not Quantified

ETP Waste (Cat. 34.3) : 43.00 TPM

Process Residue (Cat.26.1) :90.00 TPM

Used Oil (Cat. 5.1): 8 KL/Y

Discarded drums (Cat. 33.3): Not Quantified

ETP waste and Process Residue will be properly stored, transported and disposed to TSDF site.

Used oil will be sold to GPCB authorized recycler.

Discarded containers after proper decontamination will be sold to the authorized scrap dealer.

Noise Expected levels

Inside the plant: <80 dB(A)

The major sources of noise generation in plant area will be Air compressor, DG sets, Boiler room etc.

Anti-vibration pads and flexible bellows will be provided wherever applicable.

Acoustic enclosure will be provided to DG sets.

Ear plug and Ear muff will be provided.

Regular maintenance will be done.


3



CHAPTER – 2

INTRODUCTION OF THE PROJECT

2.1 IDENTIFICATION OF THE PROJECT AND PROJECT PROPONENT

2.1.1 IDENTIFICATION OF THE PROJECT

M/s. Rossari Biotech Ltd. is a Public Limited Company and established in 1996, Speciality

range of products has become a BRAND to reckon with in the Textile Industry. Today our range

of products and services has made rapid inroads in the processing world. We are one in a

million supplier who is capable of not only understanding the customer’s needs, but also able to

quickly tailor make products suitable to their requirement at no extra cost. Present capacity and

area of the plant is not sufficient to cater the market demands so, we want to increase our

production capacity at new location at Dahej-III Industrial Estate, Dist. Bharuch.

The company has obtained TORs from SEAC vide MOM dated 16th December, 2014 for

above said project, copy of MOM is attached as Annexure-5 Now, the company wants to

amendment into the granted TORs for following points.

1. Change in Product list and its quantities.

2. Change in water requirement and water balance diagram.

3. Change in Plot No in TORs Letter.

4. Discharge of ETP treated effluent into CETP.

5. Extension in validity of TORs.

The list wise product expansion is as given below:

Table 2.1: List of Proposed Products

S. No.

Name of Products Proposed

Quantity of Production in MT/annum

End use of Products/ By- products

Phase-1 Formulation Products

1 Pharmaceutical Products & Food Supplement 250 APIs used in Pharma industry.

2 Food & Breweries 175

In baking, fruit and vegetable processing, brewing, wine-making, processing of vegetable oils, cheese manufacturing, and


4



meat- and fish-processing.

3 Animal Health & Nutrition

(a) Acidifier Formulation

15000

Improve the quality of livestock.

(b) Cocktail Enzyme Products

(c) Electrolyte formulation

(d) Antibiotic powder injection formulation

(e) Antibiotic liquid injection formulation

(f) Vitamin mix formulation

4 Cosmetics

(a) After Shave Lotion 50 Enhance the appearance or odor of the human body

(b) Shampoo with protein 150

(c) Cream Hair Conditioner 50

5 Sanitizer & Disinfectants 500

Used to destroy or deactivate microbes that can cause infections, effectively reducing the risk of disease, hand sanitizers.

6 Cleaning Chemicals 10000 Soaps & detergents.

7 Textile & Laundry Chemicals

(a) Pre-Treatment Auxilliaries1

3000

Textile manufacturing industry & Laundry Industry.

Pretmt Auxillaries 2

Pre-Treatment Auxilliaries3





(b) Pre- Tretment Auxiliary-2 SPL 25000

(c) Dyeing Auxilliaries 15000

(d) Printing Auxilliaries 3000

(e) Finishing Auxilliaries 3000

(f) Speciality Chemicals 5000

(g) Optical Brightners 350

(h) Scouring Agent 900

(i) Wetting Agent 750

(j) Bleaching Agent 750

(k) Polysols 2000

(l) Surfactants 2000

(m) Silicon Oil 1000

(n) Emulsifiers 750

(o) Detergents 750

8 Enzyme Formulation (a) Enzyme for De-Sizing 250 Textile Industry, Leather


5



(b) Enzymes for Fading 1000 Industry.

(c) Enzymes for Bio-Polishing 900

(d) Enzymes for De-Gumming Agents 100

(e) Neutral Enzymes 250

9 Construction Chemicals (a) Plasticizers & Additives 2500 Various applications

during construction of infrastructure projects and renovation work.

(b) Surface Treatment Chemicals 500

(c) Adhesives & Sealants 500

(d) Flooring Chemicals 2400

(e) Tiling Chemicals 2300

(f) Protectove Coating & Wall Care Chemicals 1000

(g) Waterproofing Chemicals 2300

(h) Grout & Repair Motors 10000

10 Paper & Leather Chemicals (a) De-Inking Chemicals 250 Paper & Leather

manufacturing industry. (b) Refining Chemicals 250

(c) Bleaching Agent 500

(d) Soaking Chemicals 250

(e) Degreasing Chemicals 250

(f) Surface Treatment Chemicals 250

(g) Speciality Chemicals for Paper & Leather 1250

11 Antistatic Oil/ Mineral Oil/ Lubricant Oil/ Grease/ Coning Oil (a) Antistatic Oil 5000 Yarn manufacturing

industry. (b) De-dusting Oil 1200

(c) Sewage Thread Lubricants 1200

(d) Speciality Mineral Oils 10000

(e) Speciality Lubricant Oils/ Coning Oil 7000

12 Agro Formulation Products a)

Liquid Insecticides 225

Generally a contact as well as stomach insecticides. Broad spectrum organic chemicals, kills effectively most destructive and difficult insects.

b)

Powder Insecticides 110

Generally a contact as well as stomach insecticides. Broad spectrum organic chemicals, kills effectively most destructive and difficult insects.

c)

Liquid Herbicides 70

Broad spectrum herbicides effective on grass as well as broad leaf weeds.


6



d)

Powder Herbicides 50

Broad spectrum herbicides effective on grass as well as broad leaf weeds.

e)

Liquid Fungicides 110

Broad spectrum fungicidal, which control large number of diseases with its multisite action caused by phycomycetes, advance fungi and other groups of fungi infecting many crops.

f)

Powder Fungicides 550

Broad spectrum fungicidal, which control large number of diseases with its multisite action caused by phycomycetes, advance fungi and other groups of fungi infecting many crops.

g)

Liquid Acaricide 45

Acaricides are pesticides that kill member of the anarchnid sub class acar, which includes ticks and mites.

h) Plant Growth Regulators Supplement (PGRS)-Liquid 20 i) Plant Growth Regulators Supplement (PGRS)-

Powder 20 TOTAL 142025

Phase-2 Synthesis Products

13 Fermentation 1 (Enzymes)

a)

Pectinase 10.00

Degradation of plant material such as speeding up extraction fruit juice from fruit, wine production.

b)

Cellulase 48.00

Used in textile, laundry industry, fermentation of bio-mass into biofuel, etc

c)

Serratiopeptidase 12.00

Anti-inflammatory, cancer & tumor preventative, Efficient therapy of post-surgery.

d) Hemicellulase Products 8.00

Baking products, Food preparation technologies.

e)

Lactase 10.00

To make milk suitable for people with lactose intolerance, manufacture of ice-cream, sweetener in


7



many products

f)

Amylases (Bacterial/ Fungal) 8.00

Manufacturing of maltose, high fructose containing syrup, direct fermentation of starch ethanol, detergents-alkaline amylase.

g) Yeast Lipase 3.00

Dietary Supplements and Food & Beverages.

h)

Catalase 8.00

In food industry for cheese production, in textile industry for removal of hydrogen peroxide.

i)

Chitinase 5.00

In biocontrol of plant pathogenic fungi and insects , mosquito control.

j)

Phytase 75.00

In food processing, production of pharmaceuticals, used as animal feed additives.

k)

Glucoamylase 12.00

Manufacture of high fructose corn syrup used in baking & soft drink industry.

l) Fungal Diastase 12.00

In bakeries to improve bread quality.

14 Fermentation 2 (Probiotic)

a) Saccharomyces Boulardi 6.000

Treatment and prevention of diarrhea Cure for general digestion problems, irritable bowel syndrome, lyme disease, urinary tract infections.

b)

Probiotics/ Prebiotics 125.000

Treatment of adult & childhood infectious diarrhea, prevention of AAD, Immune response.

c) Lactic Acid Bacillus 12.000

Treatment of, Antibiotic induced diarrhea.

15 Methyl Cobal Amin 3

Supplement that decreases the risk of cancer, depression, dementia, heart diseases etc.

16 Ox Bile Extract 15

Effective digestion of food in patients with digestive complaints.

17 Protease from Animal Origin


8



a)

Pancreatin 15.000

Helpful in people suffering from food allergies. Celiac diseases, autoimmune diseases, cancer and weight loss.

b) Pepsin 12.000

Modify proteins for food, In leather industry for treatment of hides.

c)

Proteases(Trypsin/Chymotrypsin/Acid/Alkaline/Bacterial) 10.000

In laundry & dish detergents, making cheese from milk, tanning in leather industry.

18 Protease from Plant Origin

a) Papin

35 Digestive enzyme, chilling process of beer making.

b)

Bromelain

10 Used as both digestive aid and anti-inflammatory drug.

19

EO/PO Condensate 10000

Used as an intermediates for the production of chemicals , Industrial Surfactants, paper, textile etc.

20 Binders & Other Polymers 15000 Textile industry

21 Polymers for Paints & Other Industries 15000 Paint industry

22

Softner-1/Softner-2 (Textile & Laundry Chemicals) 7000

Textile manufacturing industry & Laundry Industry.

23 Organopoly Siloxane (Textile & Laundry Chemicals) 600 Textile industries

24 Blocked polyester (Textile & Laundry Chemicals) 240 Textile industries

25 Polyurethane (Textile & Laundry Chemicals) 300 Textile industries

26 Sizing Chemicals (Paper & Leather Chemicals) 2500 Paper & Leather manufacturing industry. 27 Neutralizing Chemicals 500

28 Grease (Antistatic Oil/ Mineral Oil/ Lubricant Oil/ Grease/ Coning Oil) 700

Yarn manufacturing industry.

29 Nutrient Liquid (by product) 410 Agriculture

30 Nutrient Powder (by product) 610 Agriculture

TOTAL 53314

2.1.2 PROJECT PROPONENT

The company is a limited firm and is promoted by 2 directors.

Shri Sunil Srinivasan Chari is having over two and half decades of experience in the textile

industry more than a decade of which is as an entrepreneur.

Shri Edward Menezes is having over 28 years’ experience predominately in the field of textile

processing.


9



Table 2.2: Addresses of Directors

Sr. No.

Name of Directors Addresses

1. Shri Sunil Srinivasan Chari 901/2, Valencia, Hiranandani Gardens, Powai, Mumbai- 400076.

2. Shri Edward Menezes 601/2, Gem House, Panchkutir, Lake Boulevard, Hiranandani Gardens, Powai, Mumbai- 400076.

2.2 NATURE OF THE PROJECT

The proposed project for manufacturing of Synthetic Organic Chemicals (Enzymes/ Probiotics/

Prebiotics/ API by Fermentation/Biological/Chemical routes and Speciality chemicals for

Pharma and other Industries) falls under the item no. 5(f) i.e. Synthetic Organic Chemicals

and Category B, as per the EIA notification, 2006 (as amended timely) and needs to obtain the

prior Environmental Clearance from the State Environment Impact Assessment Authority

(SEIAA), prior to commissioning of the above proposed project.

2.3 NEED OF PROJECT & DEMAND-SUPPLY GAP

M/s. Rossari Biotech Ltd. is engaged in manufacturing of Synthetic Organic Chemicals

(Enzymes/ Probiotics/ Prebiotics/ API by Fermentation/Biological/Chemical routes and

Speciality chemicals for Pharma and other Industries). Our products are contributing elements

to the fulfillment of basic needs of human being, i.e. Food, Cloth and House. Since the

population and economy is growing the demand for our products is poised to show an upward

trend.

Many enzymes which are imported at present to cater to domestic demand will be manufactured

at the present site and hence valuable foreign exchange will be saved. Continuous growth in

population is accelerating the demand of products in all segments including pharma,

construction, food & beverages, textile etc.

2.4 IMPORTS VS. INDIGENOUS PRODUCTION

Many enzymes which are imported at present to cater to domestic demand will be manufactured

at the present site and hence valuable foreign exchange will be saved.


10



2.5 EXPORT POSSIBILITY

Many foreign companies are showing interest in collaboration with us for production of various

novice products developed by them as they consider we can produce their products at an

economical cost with our pool of trained and skilled personnel. As an example we have recently

entered into an agreement with M/s. Buzil of Germany for production of sanitizers with

technology developed by them.

2.6 DOMESTIC / EXPORT MARKETS

Market for the proposed products includes not only the domestic market but also the

international market. Being Eco-friendly, the demand for our products is poised for tremendous

growth.

2.7 EMPLOYMENT GENERATION DUE TO PROJECT

The project will provide direct employment opportunity to 38 persons for Phase 1 and 150

persons after Phase 2 and indirect employment to 50 persons. The man-power required for the

project will be employed locally from the nearby areas.


11



CHAPTER – 3

PROJECT DISCRIPTION

3.1 TYPE & LOCATION OF PROJECT

3.1.1 TYPE

The proposed project is the type of new project for manufacturing of Synthetic Organic

Chemicals (Enzymes/ Probiotics/ Prebiotics/ API by Fermentation/Biological/Chemical routes

and Speciality chemicals for Pharma and other Industries).

3.1.2 LOCATION

The industry named M/s. Rossari Biotech Ltd. proposes new project in manufacturing of

Synthetic Organic Chemicals (Enzymes/ Probiotics/ Prebiotics/ API by

Fermentation/Biological/Chemical routes and Speciality chemicals for Pharma and other

Industries) at D-3/24/3, Dahej-III, Idustrial Estate, Taluka Vagara, Dist. Bharuch.

Dahej, a chemical hub and port, is situated on the Gulf of Cambay in Vagra Taluka of Bharuch

district in Gujarat. The nearest urban center for Dahej is Bharuch. Other major cities of Gujarat

are Vadodara and Ahmedabad in northern side and Surat in southern side. Dahej has been

identified as PCPIR (Petroleum Chemical and Petrochemical Invastement Region) and become

the first PCPIR approved by the Government of India. It is estimated that industries located in

Dahej contribute 15% of Gujarat’s state GDP (Gross Dometic Product). Dahej PCPIR is being

developed in Bharuch district and spread over an area of 453 km2 and is estimated to attract

investement of INR 50000 crore and provide employment to 8 lakh people. This PCPIR has

already seen committed investment of about 22930 crore.

Dahej PCPIR is one of the country’s largest chemical & petrochemical complexes having

following industrial segments:

Dahej Industrial Estate (spread across 4500 ha with large manufacturing units)

Dahej SEZ (notified and functional multi product SEZ spread over 1719 ha). Dahej SEZ,

a multiproduct SEZ, is being developed by Dahej SEZ Ltd.

Dahej Industrial Estate – Phase II (spread across 4200 ha is under development)


12



Dahej Port (for transportation of solid, liquid & LNG facilities including first LNG terminal

in the country)

Location of project site is shown in figures 3.1 & 3.2 and key plan & Layout are shown in figure

3.3 & 3.4.

Figure 3.1: Project Site


13



Figure 3.2: Satellite Image of the Project Site

Figure 3.3: key plan of the project site.


14



Figure 3.4: Project Site layout.


15



Table 3.1: Area Statement

S. No. Description Approx. Area (m2)

Phase -1 area utilization 1. Built-up area 4334.00

Phase -2 area utilization 2. Built-up area 16685.61

Other common area 3. Greenbelt area/ Common Open Plot area 8828.00

4. Road Area 23040.00

Sub – Total 31868.00 TOTAL 51218.35

3.2 DETAILS OF THE ALTERNATIVE SITE

Figure 3.5: Satellite Image of Alternate Site considered.

The alternative sites considered for the proposed project were Silvassa, Nasik and Vadodara.

The major reason for selection of the particular site is because its location in Petroleum,

Chemicals and Petrochemicals Investment Region (PCPIR) which is a specifically

delineated Investment Region planned for the establishment of production facilities for

petroleum, chemicals and petrochemicals.


16



Close proximity to Dedicated Freight Corridor being laid down between Delhi & Mumbai.

Investor friendly attitude of Gujarat Government and local administration.

Reduction in RM cost as many input suppliers like GNFC are located nearby which will

bring reduction in transportation cost.

PCPIR specific infrastructure such as effluent disposal pipelines, solid waste disposal

sites.

Also the company had submitted the application for TORs at SEAC in reference to plot no D-

II/CH/223, Dahej-II Industrial Estate, Taluka Vagra, Dist. Bharuch on 14-06-2013. However,

after submission of application, the company were informed that an ONGC underground

pipeline will pass through the allotted plot. In view of the raw-material to be used in the project,

the company approached the GIDC for re-allotment of a new site, and accordingly the GIDC

allotted a part of Plot No D-3/24 in Dahej-III estate via corrigendum order dated 14th May 2014.

The same was intimated to SEAC at the time of presentation. However, granted TORs vide

222nd minutes of meeting dated 16.12.2014 the old plot no. D-II/CH/223 was mentioned instead

of re-allotted plot no. D-3/24/3 there for one of the point of this application is to get amendment

in Plot No in granted TORs.

3.3 SIZE & MAGNITUDE OF OPERATION

The total magnitude of operation will be @ 142025 MT/Annum for Phase-1 and 53314

MT/Annum after Phase-2.

3.4 PROJECT DESCRIPTION WITH PROCESS DETAILS

The proposed products process details like Process description, Material Balance and Chemical

Reaction are given in Annexure 1.

3.5 RAW MATERIAL FOR FINISHED PRODUCTS

The raw materials for the proposed range of products will be indigenously available and will be

also imported. The product-wise raw-material consumption is given in Annexure 2.

3.5.1 HAZARDOUS CHEMICAL STORAGE & HANDLING

Hazardous chemicals will be used as raw material in the manufacturing process. The storage,

handling & transport of Haz. Chemicals is given in table 3.2.


17



Table 3.2: Storage, Handling & Transport of Haz. Chemicals

Raw Material Source Means of storage

Means of transport

Storage conditions

Max. Qty. to be stored MT

Press. Kg/m2

Temp (ºC)

Alcohol - 2-Mercaptoethanol

Local Traders

Can - 2 x 0. 5 kg

Truck AP RT 0.001

Acid - Acetic Acid Local / Highseas Purchase

Bulk 2 x 75000 kg

Tanker AP RT 150.000

Solvent- Acetone Local Traders

Drum- 1 x 200 kg

Truck AP RT 0.200

Solvent – Activated Carbon powder

Local Traders

Bags - 1 x 25 kg

Truck AP RT 0.025

Amine - Amino Ethyl Ethanol Amine

Local Traders

Drum- 4 x 200 kg

Truck AP RT 0.800

Benzyl chloride Local Traders

Drum- 2 x 200 kg

Truck AP RT 0.400

Solvent - Butyl Acrylate Monomer

Local Traders

Drum- 1 x 100 kg

Truck AP RT 0.100

Caustic Potash Local Traders

Bags - 6 x 25 kg

Truck AP RT 0.150

Caustic Soda Flake Local Traders

Bags - 120 x 25 kg

Truck AP RT 3.000

Acid – Citric acid Local / Import Purchase

Bags - 648 x 25 kg

Truck AP RT 16.200

Dimethyl sulphate Local Traders

Drum- 4 x 250 kg

Truck AP RT 1.000

Potassium phosphate dibasic

Local Traders

Bags - 1 x 50 kg

Truck AP RT 0.050

Diethanolamine Local Traders

Drum- 4 x 200 kg

Truck AP RT 0.800

Amine - Diethylenetriamine Local Traders

Drum- 4 x 200 kg

Truck AP RT 0.800

Disodium Phosphate Anhydrous

Local Traders

Bags - 2 x 50 kg

Truck AP RT 0.100

Solvent - Kerosene, Deodorized

Local Traders

Drum- 10 x 200 kg

Truck AP RT 2.000

Formaldehyde Local Traders

Drum- 4 x 200 kg

Truck AP RT 0.800

Acid – Formic Acid 85% Local / Import Purchase

Bulk 2 x 75000 kg & 1 x 50000

Tanker AP RT 200.000

Solvent - Glycerin Local Traders

Drum- 30 x 200 kg

Truck AP RT 6.000

Hydrogen Peroxide 50% Local Traders

Drum- 10 x 35 kg

Truck AP RT 0.350

Acid – Hydrochloric acid Local Traders

Drum- 57 x 35 kg

Truck AP RT 2.000


18




Means of transport

Storage conditions


Press. Kg/m2

Temp (ºC)

Ammonia Solution Local Traders

Drum- 4 x 25 kg

Truck AP RT 0.100

Solvent- Methanol Local Traders

Drum- 1 x 200 kg

Truck AP RT 0.100

Antifoam Compound Local Traders

Drum- 40 x 25 kg

Truck AP RT 1.000

Mono Sodium Phosphate Local Traders

Bags - 40 x 50 kg

Truck AP RT 2.000

Proxel GXL Local Traders

Drum- 14 x 35 kg

Truck AP RT 0.500

Solvent- Orthoxyline Local Traders

Drum- 2 x 250 kg

Truck AP RT 0.500

Acid - Oxalic acid Local Traders

Bags - 4 x 50 kg

Truck AP RT 0.200

Acid – Phosphoric Acid 85%

Local Traders

Drum- 3 x 200 kg

Truck AP RT 0.600

Solvent- Pine oil Local Traders

Drum- 10x 200 kg

Truck AP RT 2.000

Potassium persulfate Local Traders

Bags - 80 x 25 kg

Truck AP RT 2.000

Potassium hydroxide Local Traders

Bags - 1 x 25 kg

Truck AP RT 0.025

Polycarboxylic acid Local Traders

Drum- 100 x 200 kg

Truck AP RT 20.000

Hydroxy Ethelidene diphosphoric Acid 60%

Local Traders

Drum- 35 x 200 kg

Truck AP RT 7.000

Sodium Monochloroacetate Local Traders

Bags - 8 x 25 kg

Truck AP RT 0.200

Soda Ash Local Traders

Bags - 160 x 50 kg

Truck AP RT 8.000

Sodium bicarbonate Local Traders

Bags - 4 x 25 kg

Truck AP RT 0.100

Sodium hydrogen sulphate Local Traders

Bags - 38 x 25 kg

Truck AP RT 0.950

Sodium Meta-Silicate Local Traders

Bags - 128 x 50 kg

Truck AP RT 6.400

Octamethyl cyclo tetra siloxane

Local Traders

Drum- 100 x 100 kg

Truck AP RT 10

1,3 Divinyl tetra methyl disiloxane

Local Traders

Drum- 1 x 100 kg

Truck AP RT 0.09

Silanolate Local Traders

Drum- 1 x 100 kg

Truck AP RT 0.06

Di ethylene Glycol Local Traders

Drum- 10 x 50 kg

Truck AP RT 0.5

Mono ethylene Glycol Local Traders

Drum- 10 x 50 kg

Truck AP RT 0.5

Ethoxylated Glycerine Local Traders

Drum- 10 x 50 kg

Truck AP RT 0.5


19




Means of transport

Storage conditions


Press. Kg/m2

Temp (ºC)

Neo pentyl Glycol Local Traders

Drum- 10 x 50 kg

Truck AP RT 0.4

Terpthalic Acid Local Traders

Drum- 1 x 100 kg

Truck AP RT 1.0

Iso pthalic Acid Local Traders

Drum- 1 x 100 kg

Truck AP RT 1.0

polyl Local Traders

Drum- 1 x 100 kg

Truck AP RT 1.0

polyisocynate Local Traders

Drum- 1 x 100 kg

Truck AP RT 1.0

Sodium percarbonate Local Traders

Bags - 800 x 25 kg

Truck AP RT 20.000

Solvent - 1425 Local Traders

Drum- 10 x 200 kg

Truck AP RT 2.000

Solvent - C-IX Local Traders

Drum- 10 x 200 kg

Truck AP RT 2.000

Strain Remover Local Traders

Drum- 3 x 200 kg

Truck AP RT 0.600

Solvent Local Traders

Drum- 4 x 50 kg

Truck AP RT 0.200

Acid - Sulfamic acid Local Traders

Bags - 8 x 50 kg

Truck AP RT 0.400

Acid - Sulfuric Acid Local Traders

Drum- 5 x 35 kg

Truck AP RT 0.175

Solvent - Toluene Local Traders

Drum- 1 x 20 kg

Truck AP RT 0.020

Propylene oxide Import Bulk Truck AP RT 20.00

Ethylene Oxide Local Traders

Bulk Truck AP <20°C 40.00

Vinyl Acetate Monomer Local Traders

Bulk Truck AP RT 50.00

Dimethyl Lauryl amine Local Traders

Drum- 10 x 200 kg

Truck AP RT 2.000

Ethanol Local Traders

Drum- 200 x 200 kg

Truck AP RT 40.00

Alphacypermithirine Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Chlropyriphos Local Traders

Drum 10 x 200 Kg

Truck AP RT 2

Cypermithirine Local Traders

Drum 15 x 200 Kg

Truck AP RT 2.5

Ethion Tech Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Fenvelerate Local Traders

Drum 10 x 200 Kg

Truck AP RT 2

LamndaCyhalothrin Local Traders

Drum 5 x 200 Kg

Truck AP RT 1


20




Means of transport

Storage conditions


Press. Kg/m2

Temp (ºC)

Malathion Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Monochrophos Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Novaluron Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Propinophos Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Emulsifier Local Traders

Bulk Truck AP RT 50

Solvents Local Traders

Drum 25 x 200 Kg

Truck AP RT 5

Acephate Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Acetamiprid Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Cartap Hydrochloride Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Imidacloprid Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Thiamithoxam Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Fipronil Local Traders

Bags 40 x 25 kg

Truck AP RT 1

China Clay Local Traders

Bags 1000 x 50 kg

Truck AP RT 50

2,4-D Ethyl Ester Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

2,4-D Dimethyle Amine Salt Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Butachlor Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Glyphosate Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Oxyfluorfen Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Paraquat Di Chloride Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Pendimethalin Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Pretilachlor Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Propaquizafop Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Atrazine Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Isoproturon Local Traders

Bags 40 x 25 kg

Truck AP RT 1


21




Means of transport

Storage conditions


Press. Kg/m2

Temp (ºC)

Metribuzin Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Metsulfuran Methyl Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Piroxofop-Propinyl Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Hexaconazole Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Mancozeb Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Propiconazole Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Sulphur Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Captan Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Carbendazim Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Copper Oxychloride Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Cymoxanil Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Dodine Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Mancozeb Local Traders

Bags 400 x 25 kg

Truck AP RT 10

Myclobutanil Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Thiram Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Tricyclazole Local Traders

Bags 80 x 25 kg

Truck AP RT 2

Zineb Local Traders

Bags 40 x 25 kg

Truck AP RT 1

Dicofol Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Propergite Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Ethephon Local Traders

Drum 5 x 200 Kg

Truck AP RT 1

Triacontanol Local Traders

Bags 40 x 25 kg

Truck AP RT 1

AP= Atmospheric Pressure, RT= Room Temperature


22



3.6 RESOURCE OPTIMIZATION & AVAILABILITY

The major resources for the proposed project will be plant & machinery, raw-materials, power,

fuel, water, man-power, etc.

3.6.1 LAND & BUILDING REQUIREMENT

Total plot area for proposed project will be 51218.35 m2. Out of which the total built-up area will

be 4334 m2 for Phase1 and 16685.61 m2 after Phase-2 .The plot has been purchased from

GIDC, Dahej .The Plot allotment certificate from GIDC, Dahej has been attached as Annexure

3.

3.6.2 EQUIPMENTS

Based on process necessity, list of the proposed equipment and machinery for Phase1 and

Phase 2 is attached as Annexure-4.

3.6.3 POWER AND FUEL REQUIREMENT

The total power requirement for the proposed project will be 648.87 kVA (Connected Load) for

Phase1 and 3396.06 kVA (Connected Load) after Phase2, which will be sourced from Gujarat

Electricity Board. The company will install D.G. Sets @165 kVA for Phase1 and @500 kVA for

Phase2 which will act as standby facility and will be used only in case of power failure. The

details of power and fuel are provided at below table:

Table 3.3: Details of Power & Fuel

Sr. No.

Particulars Requirement Source

Phase 1 (Connected Load)

After Phase 2 (Connected Load)

Power

1 Power Requirement 648.87 kVA

D.G. Set (165 kVA) –

Standby facility

3396.06 kVA

D.G. Set – 2 no.

(165 & 500 kVA) –

Standby facility

Gujarat Electricity

Board

Fuel

1 Fuel & it’s

consumption

NG @3816 Nm3/D

LDO @4095 LPD

Diesel- 28.1 LPH

NG @8712 Nm3/D

LDO @9345 LPD

Diesel- 105.5 LPH

GSPC

Authorized Dealers

Authorized Dealers


23



3.6.4 WATER REQUIREMENT

Necessary water requirement for the proposed project will be fulfilled from GIDC water supply.

For proposed project, water will be required for domestic, process, washing and utility purpose.

Total fresh water requirement for proposed project will be 225.0 KLD for Phase1 and 398.0 KLD

after Phase 2.

The category wise bifurcation of the water requirement is given in the Water Balance Data in

Table 3.4.


24



Table 3.4: Category-wise Water Requirement (in KL/D)

S.No.

Particulars Requirement (KLD)

Phase1 After Phase2

1. Domestic 1.00 2.00

2. Gardening 20.00 20.00

3. Industrial

4. Process 120.00 225.0

5. RO Reject 31.00 60.30

6. Boiler ( Make-up) 5.00 16.20

7. Floor Washing 7.00 10.00

8. Cooling (Make-up) 35.00 35.00

9. Chilling Plant 0.20 0.015

10. Equipment Washing 5.70 29.40

11. D M Regeneration 0.02 0.02

12. Sub-Total: Industrial 204.0 376.0 13. Grand Total 225.0 398.0

3.6.5 MAN-POWER REQUIREMENT

The total number of man power required for proposed project will be 38 persons for Phase1 &

150 persons after Phase2.

The man-power required for the project will be employed locally from the nearby areas. Skilled

as well as unskilled labour will be employed for the project.

Table 3.5: Man Power Requirement

Phase of project Type of Labour

No. of workers

General 1st Shift 2nd Shift 3rd Shift

M F M F M F M F

Phase1

During operations Managerial 06 - - - - - - - Skilled 12 - - - - - - - Un-skilled 20 - - - - - - -

After Phase2 During operations Managerial 30 - - - - - - -

Skilled 50 - - - - - - - Un-skilled 70 - - - - - - -


25



3.7 QUANTITY OF WASTE TO BE GENERATED

3.7.1 WASTE WATER GENERATION & MANAGEMENT

The category wise bifurcation of the waste water generation is given in Table 3.6.

Table 3.6: Category-wise Wastewater Generation (in KL/D)

S. No. Particulars

Waste Water Generation

Phase1 After Phase2

1. Domestic 1.30 4.50

2. Gardening -- --

3. Industrial

4. Process 0.00 23.00

5. RO Reject 27.50 54.30

6. Floor Washing 10.00 13.00

7. Boiler (Blow down) 1.70 5.30

8. Cooling (Blow down) 5.00 5.00

9. Equipment Washing 5.70 29.40

10. DM Regeneration 0.02 0.02

11. Sub-Total: Industrial 50.0 130.0

12. Grand Total 51.3 134.5


26



Fig-3.6: Water Balance Diagram (in KLD) for Phase1


27



Fig-3.7: Water Balance Diagram (in KLD) After Phase2


28



3.7.2 WASTE WATER CHARACTERISTICS

Domestic wastewater generated from the plant will be disposed off through soak pit / septic

tank. Industrial effluent generated will be treated in the Effluent Treatment Plant and will be sent

to CETP through underground drainage.

The tentative wastewater characteristic of effluent before treatment in ETP is given below in

Table No. 3.7.

Table 3.7: Characteristics of Wastewater

Sr. No. Parameter

Characteristics Phase1 After Phase2

Untreated Untreated

1. pH 7 5-8.5

2. Suspended Solids (SS) 250-300 1000-1200

3. Total Dissolved Solids 1000-1200 2000-2500

4. Chemical Oxygen Demand (COD) 500-800 10000-12000

5. Biochemical Oxygen Demand (BOD) 100-200 3500-4000

6. Oil & Grease 10-20 20-30

3.7.3 WASTE WATER TREATMENT & DISPOSAL

The domestic waste water generated from the first phase will be 1.3 kl/day and after Phase2 it

will be 4.5 kl/day which will be disposed off through Septic tank/ Soak-pit system. The Industrial

effluent generated will be 50.0 kl/day for Phase1 and 130.0 kl/day after Phase2. The industrial

effluent will be treated in the proposed ETP and finally disposed to CETP through underground

drainage system after confirming the CETP inlet norms.

Phase 1:

Effluent Treatment Scheme:

The effluent from the manufacturing process plants shall be collected into the oil & grease trap

through bar screen chamber. In these trap oil, grease and floating materials shall be manually

collected into the drums. The oil free effluent shall be collected into the equalization cum

neutralization tanks. The effluent will be equalized by mixing the effluent completely by means

of air purging through coarse bubble diffusers provided at the bottom of the tank and tank also


29



takes care of shock loads of incoming effluent. Then the effluent will be neutralized by dosing

Acid / Alkali solutions depending upon the effluent characteristics.

Then, the neutralized effluent shall be pumped to the primary clarifier via flash mixer, where the

polyelectrolyte shall be added for better settling of reacted sludge, if required. The reacted

sludge shall settle at the bottom of the primary clarifier and then it shall be collected into the

sludge well by the means of clarifier mechanism. The sludge from the bottom of the primary

clarifier shall be pumped into the sludge blending tank.

The clarified water of primary clarifier will be collected in treated water tank and finally disposed

of to CETP through underground drainage system after confirming the CETP inlet norms.

After Phase 2:

Effluent Treatment Scheme:

The effluent from the manufacturing process plants shall be collected into the oil & grease trap

through bar screen chamber. In these trap oil, grease and floating materials shall be manually

collected into the drums. The oil free effluent shall be collected into the equalization cum

neutralization tanks. The effluent will be equalized by mixing the effluent completely by means

of air purging through coarse bubble diffusers provided at the bottom of the tank and tank also

takes care of shock loads of incoming effluent. Then the effluent will be neutralized by dosing

Acid / Alkali solutions depending upon the influent characteristics.

Then, the neutralized effluent shall be pumped to the primary clarifier via flash mixer, where the

polyelectrolyte shall be added for better settling of reacted sludge, if required. The reacted

sludge shall settle at the bottom of the primary clarifier and then it shall be collected into the

sludge well by the means of clarifier mechanism. The sludge from the bottom of the primary

clarifier shall be pumped into the sludge blending tank.

The overflow from the top of the primary clarifier shall be diverted into the treated water tank

which will act as buffer tank after Phase2 and after getting sufficient effluent level in the buffer

tank; the effluent shall be pumped to the Un-Anaerobic Sludge Blanket (UASB) tower at uniform

rate.


30



In anaerobic process, the biological conversion of complete organic matter to methane and

carbon dioxide in absence of oxygen depends on the combined activity of various types of

anaerobic bacteria. A minimum hydraulic detention time is provided for anaerobic biological

process.

Different types of bacteria present in the sludge carry out the anaerobic digestion of organic

compounds present in the raw effluent. While passing in the raw effluent through the reactor,

biodegradable organic matters present in the raw effluent is converted into biogas by the

biomass present in the reactor. Thus, COD is removed from the effluent. The treated effluent,

biogas and sludge travel upward through anaerobically maintained sludge blanket and are

separated and drained into atmosphere from the top of the reactor. The sludge is retained in the

reactor. The effluent overflows into anaerobic settling tank and is partially recycled to the buffer

tank.

The clear overflow from the anaerobic settling tank shall be fed into the aeration tank. The

aeration tanks provide proper mixing and supplies oxygen to the microorganisms in the

dissolved form through the fine bubble diffusers. A constant feed rate shall be maintained in the

aeration tanks. A sludge percentage of around 25 to 30 % by volume shall be maintained in the

aeration tank. Also MLSS and MLVSS ratio shall be maintained to ensure active

microorganisms growth. Various nutrients like UREA and DAP shall be added regularly so as to

ensure proper growth of the microorganisms. The Dissolved Oxygen content in the aeration

tanks shall be maintained in between 1.0 – 2.0 mg/lit.

Then the overflow of the aeration tanks shall be diverted into the Secondary Clarifier for

biomass separation. An appropriate retention time is given to the effluent to ensure proper

settling. The overflow of the aeration tanks shall be diverted to the centre of the secondary

clarifier. The sludge settles down into the hopper bottom of the secondary clarifier by means of

clarifier mechanism. Some amount of this settled sludge shall be pumped into the sludge

blending tank whereas some amount of sludge shall be recycled back into the aeration tanks to

maintain desired concentration of biomass.

The overflow of the secondary clarifier shall be collected into the clarified water tank. The

effluent from the clarified water tank shall be pumped to the Pressure Sand Filter and Activated

Carbon Filter for tertiary treatment. The effluent shall enter into the sand filter from the top and

the filtered effluent shall be further passed to the Activated Carbon Filter for colour removal. A


31



back wash facility shall be provided to the sand filter and carbon filter to wash out the

suspended solid whenever required. For backwash, the effluent from the clarified water tank

shall be pumped at the bottom of the sand filter (and / or carbon filter) and the discharge of the

sand filter (and / or carbon filter) shall be diverted into the equalization cum neutralization tank.

The outlet of the carbon filter shall be collected into the Treated Water Tank. Finally, the treated

effluent from the treated water tank shall be sent for disposal to CETP through underground

drainage system after confirming the CETP inlet norms.

The blended sludge from the sludge blending tank shall be diverted into the sludge thickener for

thickening of sludge. The sludge from the bottom of the sludge thickener shall be fed into the

decanter /filter press for sludge dewatering. Here, the polyelectrolyte dosing shall be done for

better separation of the sludge. The sludge cake shall be collected and packed into the plastic

bags and stored in the sludge storage area properly. The leachate from the decanter shall be

diverted to the equalization cum neutralization tank.


32



Fig-3.8: Schematic Diagram of Effluent Treatment Plant


33



3.7.4 AIR EMISSIONS & CONTROL

3.7.4.1 Process Emission

There will be no process emissions from Phase1 as all the manufacturing activities will be

carried out in closed condition. Process emission will be generated after Phase-2 of the

proposed project. Bag Filters will be provided to Spray Dryers to control these emissions.

Table 3.8: Details of Process Emission

S. No. Vent attached to Ht. & Dia. of Stack, (m)

Emission conc.

1. Spray Dryer H: 11m D :300mm

PM < 150 mg/Nm3

3.7.4.2 Utility Emission

The utility emissions will be from Boiler, Thermopac and D.G. Set. We have proposed Natural

Gas, LDO and diesel as fuel. The details regarding utility emissions and control measures are

mentioned in the below table no. 3.9.

Table 3.9: Details of Utility Emission

Particulars Details Fuel & its Qty Stack Details(m)

Exit gas details

Probable Pollutant

Emission Norms

Phase 1

Boiler-1

Capacity: 2 TPH

NG- 143 Nm³/Hr LDO : 157.5 LPH

H: 30 m D: 450 mm

V: 14-18 m/s T: 160-180 ºC

PM SO2 NOx

<150 mg/Nm3 < 100 ppm < 50 ppm

Thermopac 500000 Kcal/Hr

NG:69 Nm³/Hr LDO: 70 LPH

H: 22 m D: 250 mm

V: 8-10 m/s T: 180-190 ºC

PM SO2 NOx

<150 mg/Nm3 < 100 ppm < 50 ppm

D. G. Set (Stand-by)

165 kVA

Diesel: – 28.1 LPH @ 75% Load

H: 10 m D: 100 mm

V: 14-16 m/s T: 457 ºC

PM SO2 NOx

<150 mg/Nm3 < 100 ppm < 50 ppm

After Phase2

Boiler-1 (Stand-by)

Capacity: 2 TPH


H: 30 m D: 450 mm

V: 14-18 m/s T: 160-180 ºC

PM SO2 NOx

<150 mg/Nm3 < 100 ppm < 50 ppm

Boiler-2

Capacity: 6 TPH


H: 36 m D: 600 mm

V: 14-18 m/s T: 160-180 ºC

PM SO2 NOx

<150 mg/Nm3 < 100 ppm


34



Particulars Details Fuel & its Qty Stack Details(m)

Exit gas details

Probable Pollutant

Emission Norms

< 50 ppm

Thermopac 500000 Kcal/Hr

NG:69 Nm³/Hr LDO: 70 LPH

H: 22 m D: 250 mm

V: 8-10 m/s T: 180-190 ºC

PM SO2 NOx

<150 mg/Nm3 < 100 ppm < 50 ppm

D. G. Set -2 Nos. (Stand-by)

(165 & 500) kVA

Diesel: – 105.5 LPH @ 75% Load

H: 10 m D: 100 & 200 mm

V: 14-16 m/s T: 457 ºC

PM SO2 NOx

<150 mg/Nm3 < 100 ppm < 50 ppm

Note: H=Height, D=Diameter, V= Velocity, T=Temperature.

3.7.4.3 Fugitive Emission

Minor quantity of fugitive emissions will occur during handling of the raw materials. Fugitive

emissions are also likely to occur from drum storage.

Following measures will be practiced to reduce the fugitive emissions:

Raw Materials & Products will be stored in properly designated storage area and under

good storage conditions to prevent any volatilities

Raw Materials & Products will be stored in closed containers

The fugitive emissions in terms of handling losses will get reduced by proper storage

and handling.

Regular monitoring will be done of piping and fittings for checking of any leakages.

Hazardous chemicals will be stored as per standard criteria.

Good housekeeping will be maintained in the plant.

3.7.5 HAZARDOUS / NON-HAZARDOUS. WASTES MANAGEMENT

Hazardous wastes generated will be in the form of ETP waste from Effluent Treatment Plant,

Process residue from manufacturing process, Used oil from gear boxes of the machineries &

D.G. Set, discarded drums and bags from storage of raw materials. Company has provided

adequate storage area for proper storage of wastes.


35



Table 3.10: Details of Hazardous Waste Generation & Disposal

Type of waste & Category

Source Proposed Qty Disposal Method

Phase1 After Phase2

ETP Waste (Cat. 34.3)

ETP 15.00 TPM

43.00 TPM Collection, Storage, Transportation & Disposal to TSDF site.

Process residue (26.1)

Process 46.00 (TPM)

90.00 (TPM) Collection, Storage, Transportation & Disposal to TSDF site.

Used Oil (Cat. 5.1)

Maintenance 5 KL/Y 8 KL/Y Collection, Storage, Transportation & recycle to GPCB authorized recycler

Discarded drums & bags (Cat. 33.3)

Raw material storage

Not quantified

Not quantified Discarded containers after proper decontamination are being sold to the authorized scrap dealer.

3.7.6 NOISE AND ODOUR CONTROL

There will be no major activities due to which noise would be generated other than compressors

& pumps. However, Noise level generation would be limited to 80 dB within plant. The

equipments resulting in noise generation will be Air compressor, driers and Diesel generator.

Diesel generator will be provided with acoustic enclosure. Noise control devices such as anti

vibration pads with flexible bellows will be provided wherever applicable. Odour will be

generated from fermentation process.

The control measures to be taken for reduction in noise levels are as below:

Sturdy foundation to all the noise generating equipments will be provided.

D.G. Sets will be provided with acoustic enclosure and will be installed in a closed room.

Ear Plugs and Ear muffs will be provided to the workers in Utility Section.

Greenbelt will be developed.

The control measures to be taken for reduction in odour levels are as below:

Closed reactors and vessels will be provided for odour control.

Better housekeeping by regular steaming of all fermentation equipments.

Use of efficient bio-cides to control bacterial contamination.

Control of temperature during fermentation to avoid in-activation / killing of yeast.

Avoiding staling of fermented wash.

Regular use of bleaching powder in the drains to avoid generation of putrefying micro-

organisms.


36



3.7.7 HEALTH AND SAFETY MEASURES

The company is concerned about occupational health and safety among its

work force as the man power is the biggest asset to the company.

The following key safety measures shall be implemented in the proposed project:

Safety distance of 30 meters will be maintained for EO storage tanks. The tanks will be enclosed

by barbed wire fencing from all sides maintaining distance of 30 meters.

All the electrical fittings will be flameproof.

Dyke wall will be constructed around tank farm to contain acids flowing into the plant in case of

any major leakage in any of the tanks.

Provision for one underground emergency tank will also be made in due course for any

emergency transfer of material when required.

Applicable PPEs will be provided to all workers in the plant.

Standard First Aid Box will be available in each department.

Dedicated Occupation Health Centre will be provided to deal with any emergency.

List of emergency contact numbers will be displayed at all strategic locations.

Emergency alarms will be provided at each individual unit.

Emergency assembly point will be clearly marked with directional arrows from each individual

unit.

Mass Flow Meter will be installed for unloading/ loading of bulk tankers.

Maximum handling of material with the help of stacker and forklift to minimize manual handling.

Dock leveler will be installed at dispatch bay for easy loading/unloading of containers.

Safety / Health records and MSDS will be maintained.

SPECIAL SAFETY MEASURES FOR STORAGE OF EHTLENE OXIDE:

30 meter distance from the centre of the bullet for storage area will be provided.

Excess flow check valve will be provided on Ethylene Oxide tank inlet/outlet nozzles.

Design will be as per SMPV rules.

Storage under nitrogen pressure at 4 to 10 kg/cm2 will be provided.

MS tank with aluminize from inside tank will be provided.

Sprinkler will be provided on EO storage bullet.

Dyke wall will be provided.

PG and TG will be provided on bullet.

Ultrapure N2 will be used for unloading / purging.

Inlet / out let line and Ethylene Oxide tank will be insulated.


37



Double static earthing provision will be provided to EO tank and EO day tanks.

Double safety valve will be provided on EO bullet.

Magnetic level gauge will be provided on EO tank.

Safety valve outlet will be connected with water scrubber or dipped into water scrubber tank.

Nitrogen blanketing and Nitrogen pressure transfer method will be adopted for EO handling.

Road tanker unloading procedure will be prepared and fully implemented.

Static earthing provision will be made for EO road tanker unloading point.

SPECIAL SAFETY MEASURES FOR STORAGE OF PROPYLENE OXIDE:

Will be kept under N2 pressure storage.

Safety valve provided will be provided.

Dyke wall with separate fencing area will be provided.

SOP will be prepared.

Road tanker unloading procedure will be prepared.

Flame-proof area will be provided.

Water scrubber for the vent will be provided.

Vent condenser will be provided.

Flame arrester will be provided on final vent.

Work permit system will be followed.

Firefighting equipment will be provided.

PPEs will be used.

Safety shower, eye wash will be provided.

NFPA labeling system will be adopted for drums as well as storage tanks.

Level indicator will be provided at local as well as on DCS.

Alarm for high level & temperature will be provided.

Sprinkler system will be provided.

3.7.8 ENVIRONMENTAL HEALTH & SAFETY CELL

The company will have a separate environment cell in order to keep a close watch on the

performance of the pollution control equipment, emissions from the sources and the quality of

surrounding environment in accordance with the monitoring program. The cell will also entrust

with the responsibilities of regulating the safety measures inside the plant campus. The cell will

be also responsible for maintaining the records of all data, documents and information in line

within the legislative requirement.


38



3.7.9 POST PROJECT MONITORING PLAN

The company will develope in-house facilities for monitoring certain components. Where it is not

possible to establish such facilities, the same will be done by appointing external

recognized/approved agencies. The proposed post-project monitoring plan is given below:

Table 3.11: Post Project Monitoring Plan

Components Parameters Frequency of in house monitoring

Frequency of third party monitoring

Drinking water IS-10500:1991 -- Once in a month

Waste water BOD, COD, pH, TSS, TDS Daily (At all stages of ETP)

Once in a month (treated and untreated)

Air-ambient SPM, SOx, NOx -- Quarterly

Stack monitoring SPM, SO2, NOx

-- Quarterly

Noise monitoring dB (A) -- Once in a month

Workplace monitoring VOCs like Ammonia solution ,monoethyl amine, propylene oxide, mondo-PU-100, Acetone, Textile antifoam

-- Half Yearly


39



CHAPTER – 4

SITE ANALYSIS

4.1 CONNECTIVITY

This proposed project is located at D-3/24/3, Dahej-III Industrial Estate, Taluka Vagara, Dist.

Bharuch. The Site is 10.2 km from Dahej. The site is 3.2 km from National highway. The land

and infrastructure is already available. And the raw material is easily available through the easy

transport via road connectivity. The nearest Railway station is Bharuch railway station which is

33.6 km and Surat Airport is 70 km from the project site.

4.2 LAND FORM, LAND USE & LAND OWNERSHIP

4.2.1 LAND FORM

Currently it is a vacant land. It is to be developed by GIDC for Industrial purpose.

4.2.2 LAND USE PATTERN

Currently it is a vacant land. It is to be developed by GIDC for Industrial purpose.

4.2.3 LAND OWNERSHIP

The plot is located in the industrial estate. The company has purchased it from GIDC, Dahej.

4.3 TOPOGRAPHY

Relatively flat terrain with series of inlayed creeks of river forms the topography of Dahej. There

are mounds formed on the bank of river.

4.4 SALIENT FEATURES

The salient features of the project site are given in the table below:

Table 4.1: Salient Features of the Project Site

Particulars Details

Co-ordinates Approx. center 21°44'41.49"N,72°40'32.36"E

Village Galenda

Taluka/ Tehsil Vagara

District Bharuch


40



Particulars Details

Nearest Water body Gulf of Khambhat ≈ 15.0 km (E) Narmada River ≈ 5.7 km (S)

Nearest Highway NH 8 ≈ 3.2km (S)

Nearest Railway station & Railway line Bharuch Railway Station ≈ 33.6 km (ESE)

Nearest Airport/ Airbase Surat ≈ 70 km (S)

State/ National borders No within 15 km.

Protected Area/ Sanctuaries No

CRZ applicability No

Seismicity Seismic Zone – III (Moderate)

Note: All the above mentioned distances are the aerial distance from the project site.

4.5 EXISTING INFRASTRUCTURE

The plot is located in the industrial estate. Currently there is a vacant land. The entire necessary

infrastructure will be developed by GPCB.

4.6 SOIL CLASSIFICATION1

Dahej is a coastal belt covering 1732 hect. total area. Since the total land of Dahej is saline (pH

above 9.0), humidity in the environment and water is salty and is not suitable for all type of

plants to grow. Only shallow rooted plants like coconut, palm, saru, etc. can be grown. Major

land of Dahej and surrounding have Exchangeable Sodium Percentage greater than 15 and pH

between 8.5 and 10.0. The exchangeable sodium content influences the physical and chemical

properties of these soils significantly.

Saline soils are often recognized by the presence of white crust of salts on the surface.

Generally they are flocculated having good permeability. Salt must be removed from their root

zone. Leaching is the most effective procedure for removing salts. But, since water quality is not

good and water table being high, leaching is not possible in this area. A few portion of Dahej

SEZ contains Black soil also. This soil is deep clayey, impermeable. Its characteristic of swelling

and becoming sticky when wet and shrinking when dry creates crack; no doubt aerates the land.

It lacks Phosphorous and nitrogen.

1 (Source: http://www.kcgjournal.org)


41



4.7 CLIMATE & METEROLOGY

The year can be divided into four seasons. Climate is warm and dry from mid march to June,

during season of summer, climate remains warm and dry, while during rainy season, from mid

June to end of September climate is humid and pleasant. From October to November mild warm

climate prevails, and from December to February climate is cold.

The Table 4.2 indicates the summary of meteorological pattern at the nearest observatory of

IMD, Bharuch published by IMD.

Table 4.2: Summary Meteorological Data at nearest IMD Station - Bharuch

Location: Bharuch Gujarat ( Lat: N 21o42’, Long: E 73o 00’) Aerial Dist from Project Site: Approx. 36 km (SSE) Height of installation: 17 m above MSL.

Month Temperature (oC)

Relative Humidity (%)

Cloud Cover (Oktas)

Mean Wind Speed (km/s)

Pre-dominant Wind

Direction

Rainfall (mm)

Max. Min. Mor. Eve. Mor. Eve.

January 31.3 11.9 69 34 1.0 0.9 5.9 NE 1.2

February 33.8 14.4 61 29 0.8 0.6 6.2 NE 1.0

March 37.6 19.0 62 26 1.1 0.9 7.0 SW 0.8

April 40.0 23.3 63 27 1.4 1.1 8.8 SW 1.0

May 39.6 26.2 73 38 1.8 0.7 12.4 SW 12.5

June 35.6 26.5 80 59 4.4 3.2 14.7 SW 121.0

July 32.0 25.5 88 74 6.5 6.1 13.2 SW 307.6

August 31.2 25.0 90 77 6.8 6.2 11.5 SW 243.1

September 32.6 24.4 87 65 4.7 4.6 8.6 SW 197.6

October 35.9 22.0 75 44 1.7 2.1 5.7 SW 35.2

November 34.8 16.9 68 37 1.1 1.1 4.7 NE 3.7

December 32.2 13.2 70 37 1.2 1.1 5.2 NE 0.1

Seasonal Average Values

Period Temperature (oC)

Relative Humidity

(%)

Cloud Cover

(Oktas)

Mean Wind Speed

(m/s)

Avg. PDW Direction

Total Rainfall (mm)

Avg. Max.

Avg. Min.

Avg. Mor.

Avg. Eve.

Avg. Mor.

Avg. Eve.

Summer 39.1 22.8 66.0 30.3 1.4 0.9 9.4 SW 4.8

Winter 32.4 13.2 66.7 33.3 1.0 0.9 5.8 NE 0.8

Monsoon 32.8 25.4 86.3 68.8 5.6 5.0 12.0 SW 217.3

Post monsoon 35.4 19.5 71.5 20.5 1.4 1.6 5.2 SW/NE 19.5

Annual Total or Mean

34.9 20.2 72.6 38.2 2.4 2.1 8.1 SW 60.6

Note: Winter: December, January & February, Summer: March, April & May, Monsoon: June, July, August & September, Post monsoon: October & November

(Source: Book “Climatological tables of Observatories in India (1951 - 1980)” published by IMD)


42



4.7.1 TEMPERATURE

The climate of Bharuch is warm and dry during the summer months but humid and pleasant

during the monsoon months. The south-west monsoon from June to September brings copious

rain to the territory. The winter months are generally pleasant. May is generally the hottest

month with the mean daily maximum temperature recorded at 39.6 oC and mean daily minimum

temperature recorded at 26.2 oC. January is the coldest month with the mean daily maximum

temperature as 31.3 oC and mean daily minimum temperature observed as 11.9 oC .

4.7.2 HUMIDITY

Humidity is usually high during the monsoon months, generally exceeding 86.3 %. Humidity

decreases during the summer months. For rest of the year i.e. the period of October to

February, the relative humidity ranges around 66.7 - 71.5 %.

4.7.3 CLOUD COVER

During the South-west monsoon months, the skies are usually heavily clouded or overcast.

Cloud cover decreases during the post monsoon months. In the rest of the year the skies are

mostly clear.

4.7.4 RAINFALL

About 95% of the annual rainfall is received during the southwest monsoon season i.e. from

June to September, July being the month with highest rainfall. The average annual rainfall

observed from the data is 2182.8 mm.

4.7.5 WIND PATTERN

The annual predominant wind direction comes to West, followed by North and South-west.

Winds blows mostly from the West/North-West during summers and Monsoons are usually

South-west. The post-monsoon & winter seasons experience a change in the wind blowing from

North and North-east.

The wind speed is high during summer and monsoon seasons, slightly moderate during winter

and low during post-monsoon phase.


43



4.8 SOCIAL INFRASTRUCTURE

The infrastructure available in the study area denotes the economic well-being of the region.

4.8.1 EDUCATIONAL FACILITIES

Out of 13 villages, 13 villages have educational facilities, details of which are given below.

Table 4.3: Details of Educational facilities

Sr. No

Particulars Observed values in 5km radius

1. Primary Schools 12

2. Middle Schools 0

3. Secondary School 3

4. Senior Secondary School 0

5. College 0 (Source: Primary Census Abstract – Census of India, 2001)

4.8.2 MEDICAL FACILITIES

Details of medical facilities available in the study area are given below.

Table 4.4: Details of Medical facilities

Sr. No.


1 Dispensaries 1

2 Primary Health Centers 1

3 Primary Health sub centre 4

4 Allopathic Hospital 4

5 Allopathic dispensary 1

6 Maternity and Child welfare Centre 3

7 Community Health Workers 13 (Source: Primary Census Abstract – Census of India, 2001)


44



CHAPTER – 5

PLANNING BRIEF

5.1 PLANNING CONCEPT

The proposed project is located at D-3/24/3, Dahej-III Industrial Estate, Taluka Vagara, Dist.

Bharuch. The nearest city is Bharuch & Ankleshwar which is a big hub for chemical &

Pharmaceutical Products. Major raw materials will be sourced locally. RM cost as many input

suppliers like GNFC are located nearby which will bring reduction in transportation cost.

The region is well planned with all the basic infrastructural facilities like internal roads, water

supply, arrangements for power, streetlights, solid waste disposal sites etc.

The plot for proposed project is purchased from GIDC, Dahej.

5.2 POPULATION PROJECTION

The average household size is around 5 persons. The demographic profile of study area within

5 km radius is presented below.

Table 5.1: Distribution of population

Sr. No.


1 Total Population 17978.00

2 No. of Households 3803.00

3 Avg. household size (person) 5.00

4 Male population 9525.00

5 Male population (in %) 52.98

6 Female population 8453.00

7 Female population (in %) 47.07

8 Sex ratio 887.00 (Source: Primary Census Abstract – Census of India, 2001)

5.3 AREA STATEMENT

The total area of the plot is 51218.35 m2 out of which Greenbelt area of the plant is 8828.0 m2

which is 17 %. The bifurcation of the same is given Chapter 3; table no. 3.1 at page no.17.


45



5.4 ASSESMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL)

In this proposed project the company will acquire plant and machinery so there will be some

demand of change in physical infrastructure and social infrastructure. As manpower requirement

for the proposed project shall be locally fulfilled, employment generation will lead to additional

benefits to social infrastructure.

5.5 AMENITIES/FACILITIES

5.5.1 DRINKING WATER FACILITIES

As per census 2001 following drinking facilities are available in study region.

Table 5.2: Drinking Water Facilities

Sr. No.


1 Tap 10

2 Well water 11

3 Tank water 12

4 Tube well water 0

5 Hand pump 3

6 River water 3

7 Canal 0

8 Lakes 0

9 Spring 0

10 Other drinking water sources 2 (Source: Primary Census Abstract – Census of India, 2001)

5.5.2 POWER SUPPLY FACILITIES

As per census 2001, all the villages have power supply facilities in the study region.

5.5.3 COMMUNICATION & BANKING FACILITIES

Distribution of facilities such as post office, post & telegraph office, banks, telephone

connections in the study area are illustrated in table below.


46



Table 5.3: Communication & Banking Facilities

Sr. No.


1 Post Office 7

2 Post and telegraph office 1

3 Telephone connection 250

4 Commercial Bank 5 (Source: Primary Census Abstract – Census of India, 2001)

5.5.4 TRANSPORT FACILITIES

Bus service is available in all the villages of the study region within 5 km area and most

preferable mode of transport in the region. Second option for transport is railway; railway line is

available in 3 villages. Villages are connected with paved roads. There is 100% electrification in

the area.

5.5.5 APPROACH TO VILLAGES

As per census 2001, all the 13 villages have paved road, mud road and foot path.


47



CHAPTER – 6

PROPOSED INFRASTRUCTURE

6.1 INDUSTRIAL AREA

The total area of the plot is 51218.35 m2 out of which Greenbelt area of the plant is 8828.0 m2

which is 17 %.The total production capacity will be 142025 MT/annum for Phase1 and 53314

MT/annum after Phase2.

6.2 RESIDENTIAL AREA

In the said proposal no Residential area has been proposed for workers and/or for staff.

6.3 GREENBELT

Maximum open land will be allotted for green belt development. If required, experts will also be

consulted for selection of species for the development of the greenbelt. Total greenbelt area will

be 17 % of total plot area.

6.4 SOCIAL INFRASTUCURE

Existing infrastructure will be sufficient to accommodate the existing load from the proposed

project which is very low.

6.5 CONNECTIVITY

As Described in earlier chapter.

6.6 DRINKING WATER MANAGEMENT

Drinking water will be sourced from GIDC water supply for the proposed project.


48



6.7 SEWERAGE SYSTEM

Domestic waste water generated from the proposed project will be disposed off through soak pit

/ septic tank which will be @ 1.30 kl/day for Phase1 and 4.50 kl/day after Phase 2.

6.8 INDUSTRIAL WASTE MANAGEMENT

Industrial Effluent will be treated in the Effluent Treatment Plant at the site. Details are explained

in Chapter 03, Section 3.7.3

6.9 SOLID WASTE MANAGEMENT

Hazardous wastes generated will be in the form of ETP waste from Effluent Treatment Plant,

Used oil from gear boxes of the machineries & D.G. Set, Process residue from manufacturing

process, discarded drums & bags from storage of raw materials. Company will provide

adequate storage area for proper storage of wastes. Details of solid waste generation are given

in table 3.9.

6.10 POWER REQUIREMENT & SOURCE OF SUPPLY

The power requirement for the proposed project will be 648.87 kVA (Connected Load) for

Phase1 & 3396.06 kVA (Connected Load) after Phase2 which will be sourced from Gujarat

Electricity Board. The company will intall D.G. Sets of 165 kVA for Phase1 & 500 kVA for

Phase2, which will act as a standby unit and will be used only in case of power failure.


49



CHAPTER – 7

REHABILITATION & RESETTLEMENT (R &R) PLAN

7.1 POLICY TO BE ADOPTED

The proposed project is to be developed in the land designated for industrial use. Hence, no

displacement of any population is proposed for the project. Therefore, detailed Social Impact

Assessment studies or R&R action study has not been proposed.


50



CHAPTER – 8

PROJECT SCHEDULE & COST ESTIMATES

8.1 TIME SCHEDULE OF THE PROJECT

At present we are not proposing any construction at the site. It will start only after getting all the

statutory permission from respective authorities.

8.2 ESTIMATED PROJECT COST

The company has made budgetary provision for the recurring expenses for the environmental

issues while planning for the allocation of funds during the annual budgetary planning.

Environment Protection has also been considered in planning the cost projection. Green belt

development is also considered. The estimated project cost will be approximately 46.95 Crores.

Table 8.1: Total Capital Cost Projection

Sr. No.

Purpose Total Cost (Rs. in Crores)

After Phase1 After Phase2

1. Land 5.56 5.56

2. Plant & Machinery 2.00 27.00

3. Laboratory 0.50 2.05

4. Electrical Installations & Misc. 5.00 7.50

5. Furniture, Fixtures & Office Equipments 0.10 0.25

6. Green belt development 0.01 0.01

7. Effluent Treatment Plant 0.30 4.50

8. Safety Systems 0.03 0.08

Total 13.50 46.95

Table 8.2: Recurring cost provision for EHS

Sr. No.

Purpose Provision per Annum (Rs. In lacs)

After Phase1 After Phase2

1. ETP (Chemical & Electrification) 12.00 14.00

2. Greenbelt maintenance 0.50 0.50

3. Environment & Safety Management System

a. Env. Monitoring Cost 15.00 15.00

b. In-house personnel Salary 12.00 12.00

4. Expenses for disposal at TSDF site 36.00 82.00

Total 75.50 123.50


51



CHAPTER – 9

ANALYSIS OF PROPOSAL

9.1 FINANCIAL & SOCIAL BENEFITS

M/s. Rossari Biotech Ltd. is located at D-3/24/3, Dahej-II Industrial Estate, Taluka Vagara,

Dist. Bharuch. Speciality range of products has become a BRAND to reckon with in the Textile

Industry. Today our range of products and services has made rapid inroads in the processing

world. We are one in a million supplier who is capable of not only understanding the customer’s

needs, but also able to quickly tailor make products suitable to their requirement at no extra

cost.

For the proposed project, the company intends to donate Rs. 35 Lakhs in 20 years for the social

benefit as Corporate Social Responsibility.

Annexure-1 Process Details

Formulation Products

1 PHARMACEUTICAL PRODUCTS & FOOD SUPPLEMENT

1.1 MANUFACTURING PROCESS

Dispense the material required. Pass the material from the sieve. Charge the material in blender & mix for 20 min. Unload the blender. On QC approval, pack the material.

1.2 MATERIAL BALANCE

2 FOOD & BREWERIES


Dispense the material required. Pass the material from the sieve. Charge the material in blender & mix for 20 minutes. Unload the blender. On QC approval, pack the material.


3 ANIMAL HEALTH & NUTRITION PRODUCTS

3. a ACIDIFIER FORMULATION

3. a.1 MANUFACTURING PROCESS


3. a.2 MATERIAL BALANCE

3. b. COCKTAIL ENZYME PRODUCTS

3. b.1 MANUFACTURING PROCESS


3. b.2 MATERIAL BALANCE

3. c. ELECTROLYTE FORMULATION

3.c.1 MANUFACTURING PROCESS

Dispense the material required. Pass the material from the sieve. Charge the material in blender & mix for 20 min. Unload the blender. After testing. Pack the material.

3.c.2 MATERIAL BALANCE

3. d. ANTIBIOTIC POWDER INJECTION FORMULATION

3. d.1 MANUFACTURING PROCESS

Dispense the material required. Pass the material from the sieve. Charge the material in blender & mix for 20 min. Unload the blender. After testing. Pack the material.

3. d.2 MATERIAL BALANCE

3. e. ANTIBIOTIC LIQUID INJECTION FORMULATION

3. e.1 MANUFACTURING PROCESS

Dispense the material required. Pass the material from the sieve. Charge the material in blender & mix for 20 min. Unload the blender. After testing. Pack the materials in vials.

3. e.2 MATERIAL BALANCE

3. f VITAMIN MIX FORMULATION 3. f.1 MANUFACTURING PROCESS

Dispense the material required. Pass the material from the sieve. Charge the material in blender & mix for 20 min. Unload the blender. After testing. Pack the material. 3. f.2 MATERIAL BALANCE

4 COSMECTIC PRODUCTS

4. a. AFTER SHAVE LOTION

4. a.1 MANUFACTURING PROCESS

Charge ethanol in a reactor. After adding water mix for 2 minutes. Add Isopropyl C12-15 Pareth-9-Carboxylate. Mix for 15 minutes. On QC approval unload the material and pack.


4. b. SHAMPOO WITH PROTEIN

4. b.1 MANUFACTURING PROCESS

Charge SLES & Laureth-5-carboxylic acid in reactor & mix for 10 minutes. Add Water, Hydrolysed Animal Protein & Sodium Chloride & mix for 30 minutes. Add Cocoamidopropylhydroxysultaine &Preservative & mix for 30 minutes. Then add Colour & Fragrance & mix for 10 minutes. On QC approval unload the material and pack.

4. b.2 MATERIAL BALANCE

4. c. CREAM HAIR CONDITIONER

4. c.1 MANUFACTURING PROCESS

Charge water in a reactor & heat to 650C. Add Citric acid, Cetyl alcohol, Adipic acid & Dipropylene glycol and mix well for 30 minutes. Cool the mixture to room temperature and add Colour, Preservative & Fragrance & mix for 15 minutes. On QC approval unload the material, and pack.

4. c.2 MATERIAL BALANCE

5. SANITIZERS & DISINFECTANTS 5.1 MANUFACTURING PROCESS

Charge water in a Vessel. Add Ethanol & Tri Ethanol Amine & mix for 30 minutes. Add Propylene Glycol & Glycerol & mix for 30 Minutes. Then add Alpha tocopheryl acetate & Fragrance & mix for 10 minutes. On QC approval filter, unload the material and pack.


6 CLEANING CHEMICALS


Charge water in a reactor for 10 minutes. Add Sodium sulphate & mix for 10 minutes. Add SLES slowly in 45 minutes. Add Fragrance & colour in 15 Minutes. On QC approval unload the material and pack.


7. TEXTILE CHEMICALS & LAUNDRY CHEMICALS

7.a. PRE-TREATMENT AUXILLARIES

7.a.(i) PRE-TREATMENT AUXILLARY 1

7.a.(i) 1 MANUFACTURING PROCESS

Charge water in a reactor for 20 minutes. Add Citric acid & sodium Lignosulphonate & mix for 40 minutes Add sodium sulphate in 30 minutes slowly Then add Chelating agent in 30 minutes. Check specifications .If Ok, filter fill in packing Drums.

7.a.(i) 2 MATERIAL BALANCE

7. a. (ii) PRE-TREATMENT AUXILLARY 2

7. a. (ii) 1 MANUFACTURING PROCESS

Charge Sodium Alpha Olefin Sulfonate, Na salt-DETMP & Glycerin in reactor in 15 Minutes. Add Mono Propylene Glycol, Hexylene Glycol, Turkey Red Oil & Sodium Cumene Sulphonate. Mix for 10 minutes. Add Polymers Acrylic Acid Base, Dioctyl sulfo succinate, Triethanolamine 85% & Sodium Hypo

Chlorite. Mix for 10 minutes. Then add Hydrogen Peroxide 50% & Antimicrobial. Mix for 10 minutes. Check specifications .If Ok, filter fill in packing Drums.

7.a. (ii) 2 MATERIAL BALANCE

7. a. (iii) PRE-TREATMENT AUXILLARY 3

7. a. (iii) 1 MANUFACTURING PROCESS

Charge Ortho Xylene, Pine Oil, and Deodorised Kerosene in reactor in 15 Minutes. Add Polysiloxane polyol, Octanol & Benzyl Benzoate and mix for 30 minutes. Add Mono Methyl Ethanolamine, Paraffin Wax, Benzyl Chloride & Oleic Acid. Mix for 30 minutes. Check specifications. If Ok, Filter & fill in a packing Drums.

7. a. (iii) 2 MATERIAL BALANCE

7.a.(iv) PRE-TREATMENT AUXILLARY 4

7.a. (iv) 1 MANUFACTURING PROCESS

Charge Silicone polyether copolymer, Water, Polycarboxylic acid in reactor in 15 Minutes. Add Tallow fattyacid amidoethyl Eo lactate, Dimethyl Dialkyl Ammonium Chloride & Hostapur SAS 60. Mix for 30 minutes. Add Polyacrylamide polymer & UV Absorbers/ Substantive Sunscrenes. Mix for 30 minutes. Check specifications. If Ok, Filter & fill in a packing Drums.

7.a. (iv) 2 MATERIAL BALANCE

7.a.(v) PRE-TREATMENT AUXILLARY 5

7.a. (v) 1 MANUFACTURING PROCESS

Charge the Sodium Meta Silicate, Phosphonate & Resist Salt in blender/mixer. Mix for 10 minutes. Then add Ethoxylate-Steryl Amine, Sodium bicarbonate, Sodium Formate, Yellow Detergent, Sodium

perborate monohydrate & Sodium Bi Sulphite. Mix for 60 minutes. Send samples in QC check if OK then unload & pack.

7.a. (v) 2 MATERIAL BALANCE

7.a.(vi) PRE-TREATMENT AUXILLARY 6

7.a. (vi) 1 MANUFACTURING PROCESS

Charge the Starch- Modified potato Starch, Borax & Polymer Acrylic Acid base in blender/mixer. Mix for 10 minutes. Then add Polyvinylpyrrolidone K-30, Polymer - Sodium salt, Polyvinyl alcohol, cokooidal silica, Acid -

Oxalic acid & Aluminum trichloride & mix for 60 minutes. Send samples in QC check if OK then unload & pack

7.a. (vi) 2 MATERIAL BALANCE

7.b. PRE-TREATMENT AUXILLARY 2 SPL 7.b. 1 MANUFACTURING PROCESS

Charge water in the vessel. Add Lactic Acid, Formic Acid & Propionic acid mix for 30 minutes. Add Acetic Acid, 1-Hydroxy Ethylidene-1,1-Diphosphonic Acid,Hydrochloric Acid & Iso Propyl Alcohol

mix for 30 minutes. Then add Phosphoric Acid mix for 30 minutes. Then check & unload.

7.b. 2 MATERIAL BALANCE

7.c. DYEING AUXILLARIES

7.c.1 MANUFACTURING PROCESS

Charge water in a reactor Add castor oil ethoxylate & acetic acid & mix for 30 minutes Add add sodium sulphate & dispersing agent in 60 minutes slowly Then add AOS & ceto steryl alcohol ethoxylate in 30 minutes On QC approval unload the material and pack.


7.d. PRINTING AUXILLARIES 7.d.1 MANUFACTURING PROCESS

Charge water & Dimethyl Amine for 45 Minutes & heat up to 60°C. Add Epi Chloro Hydrin slowly in 120 minutes Check specs.If Ok fill in packing Drums.

7.d.2 MATERIAL BALANCE

7.e. FINISHING AUXILLARIES

7.e.1 MANUFACTURING PROCESS

Charge amino silicone oil in a reactor for 15 minutes Add Tridecyl Alcohol Ethoxylate & acetic acid & mix for 30 minutes Add polyethylene glycol slowly for 15 minutes. Then add sodium sulphate & water for 60 minutes Check specs.If Ok, Filter & fill in packing Drums

7.e.2 MATERIAL BALANCE

7.f. SPECIALITY CHEMICALS

7.f.1 MANUFACTURING PROCESS

Charge Tridecyl alcohol ethoxylate, Butyl carbitol, lauryl alcohol ethoxylate for 45 Minutes Add Acrylic copolymer & dispersing agent slowly & mix for 30 minutes Then add water & antifungal agent in 15 minutes. Check specs. If Ok fill in packing Drums.

7.f.2 MATERIAL BALANCE

7.g. OPTICAL BRIGHTNERS

7.g.1 MANUFACTURING PROCESS

Charge Optical Brightener in reactor for 15 Minutes Add Dispersing Agent & water slowly & mix for 30 minutes On QC approval unload the material and pack.

7.g.2 MATERIAL BALANCE

7.h. SCOURING AGENT

7.h.1 MANUFACTURING PROCESS

Charge water in a reactor for 15 Minutes Add sodium chloride & magnesium sulphate & mix for 30 minutes Add Lauryl Alcohol Ethoxylate in 60 Minutes slowly Then add Butyl carbitol & anti foaming agent in 15 Minutes Check specs. If Ok, filter & fill in a packing Drums.

7.h.2 MATERIAL BALANCE

7.i. WETTING AGENT

7.i.1 MANUFACTURING PROCESS

Charge OT LIQUID in reactor for 15 Minutes. Add Propylene glycol slowly and mix for 30 minutes. Check specification & filter & fill in drums.

7.i.2 MATERIAL BALANCE

7.j. BLEACHING AGENT 7.j.1 MANUFACTURING PROCESS

Charge the sodium per carbonate, sequestering agent & talcum in blender/mixer. Mix for 10 minutes. Add Lauryl alcohol Ethoxylate and antifoaming agent for 60 minutes. Send sample for QC approval. Unload and pack the material.

7.j.2 MATERIAL BALANCE

7.k. POLYSOLS

7.k.1 MANUFACTURING PROCESS

Charge PVA emulsion & softner for 30 Minutes. Add Acrylamide & mix for 30 minutes On QC approval unload the material and pack.

7.k.2 MATERIAL BALANCE

7.l. SURFACTANTS 7.l.1 MANUFACTURING PROCESS

Charge Antifoaming Agent & Tri Decyl Alcohol Ethoxylate for 30 Minutes. Add Water & Thickener mix for 30 minutes. On QC approval unload the material and pack.

7.l.2 MATERIAL BALANCE

7.m. SILICON OIL 7.m.1 MANUFACTURING PROCESS

Charge Silicon Oil, Emulsifier & Acetic acid in reactor for 15 minutes Add Water, Urea & Sodium Acetate & mix for 30 minutes. On QC approval unload the material and pack.

7.m.2 MATERIAL BALANCE

7.n. EMULSIFIERS

7.n.1 MANUFACTURING PROCESS

Charge Tridecyl Alcohol Ethoxylate, Butyl Carbitol, Lauryl Alcohol Ethoxylate for 30 minutes. Add Water & Iso Propanol slowly & mix for 15 minutes Add Acetic Acid for 10 minutes. On QC approval unload the material and pack.

7.n.2 MATERIAL BALANCE

7.o. DETERGENTS 7.o.1 MANUFACTURING PROCESS

Charge sodium sulphate & di-sodium phosphate in a blender. Add anti-dusting oil & Soda-ash and mix for 60 minutes and add sodium per carbonate, sodium ligno

sulphate & SLS powder and mix for 60 minutes. Specifications of the product to be checked in QC. On QC approval unload the material and pack.

7.o.2 MATERIAL BALANCE

8 ENZYME FORMULATION 8.a. ENZYME FOR DE-SIZING

8.a.1 MANUFACTURING PROCCES

Charge water in a reactor reactor for 15 minutes. Add sodium chloride & Caramel powder under stirring for 15 minutes. Add Tridecyl alcohol ethoxylate & butyl carbitol slowly for 30 minutes. Add enzyme & preservative for 30 Minutes.

8.a.2 MATERIAL BALANCE

8.b. ENZYME FOR FADING 8.b.1 MANUFACTURING PROCCES

Charge water in a reactor reactor for 15 minutes. Add sodium chloride & Caramel powder under stirring for 15 minutes. Add sorbitol slowly for 30 minutes. Then add enzyme & preservative for 30 minutes.

8.b.2 MATERIAL BALANCE

8.c. ENZYME FOR BIO-POLISHING 8.c.1 MANUFACTURING PROCCES

Charge water in a reactor for 15 minutes. Add sodium chloride & Caramel powder under stirring in 15 minutes. Add Sorbitol & Ceto Steryl Alcohol Ethoxylate slowly in 30 minutes. Add enzyme & preservative in 30 minutes.


8.d. ENZYME FOR DE-GUMMING 8.d.1 MANUFACTURING PROCCES

Charge sodium sulphate, mono sodium phosphate, Betonite powder & enzyme in blender/mixer. Mix for 10 minutes. Add Castor oil Ethoxylate, ceto steryl alcohol & anti-fungal agent for 60 minutes.


8.e. NEUTRAL ENZYMES 8.e.1 MANUFACTURING PROCCES

Charge di-sodium phosphate, mono sodium phosphate, bentonite powder and enzyme in mixer/ blender and mix for 10 minutes.

Add Tri Decyl Alcohol Ethoxylate, zeolite powder, acrylic co-polymer & anti-foaming agent & mix for 60 minutes.


9. CONSTRUCTION CHEMICAL 9.a. PLASTICIZERS & ADDITIVES


Charge water in a reactor in 20 minutes. Add Sodium sulphate & Dispersing agent & mix for 40 minutes. Add SLES in 10 Minutes slowly. Add Sodium Lignosulphonate & caustic soda in 60 minutes.


9.b. SURFACE TREATMENT CHEMICALS 9.b.1 MANUFACTURING PROCCES

Add white cement, additive of binder, thickner, quartz powder, hydrated lime in a blender. Mix it for 30 minutes.


9. c. ADHESIVES & SEALANT 9. c.1 MANUFACTURING PROCCES

Add in mixture / Vessel, Resin Gun grade, O-xylene and mix it for 60 mins. Hardner 731 to be kept separate. When required we have to mix both and use immediately.

9. c.2 MATERIAL BALANCE

9. d. FLOORING CHEMICALS 9. d.1 MANUFACTURING PROCCES

Add resin & resin diluent in vessel/reactor and mix it for 30 minutes. Add additive for epoxy and levelling agent and mix for 15 minutes. HARDNER 731 to be checked for quality and packed

9. d.2 MATERIAL BALANCE

9. e. TILING CHEMICALS

9. e.1 MANUFACTURING PROCCES

Add polymeric powder, additive for cement, whitener, talcum powder, binder, white cement and quartz powder in blender.

Mix it for 60 minutes.

9. e.2 MATERIAL BALANCE

9. f. PROTECTING COATING & WALL CARE CHEMICALS 9. f.1 MANUFACTURING PROCCES

Charge cement in blender in 30 minutes Add silica quartz sand & mix for 20 Minutes Add sodium Lignosulphonate & dispersing agent & mix for 20 minutes Add sodium thiosulphate & mix for 20 minutes

9. f.2 MATERIAL BALANCE

9. g. WATER PROOFING CHEMICALS 9. g.1 MANUFACTURING PROCCES

Add cement, binding agent, quartz sand and additive of cement in a blender. Mix for 30 minutes and unload. Add formaldehyde, acrylic polymer 2 and acrylic polymer 1 in a vessel containing water. Mix for 10 minutes and after obtaining white mixture unload the mixture.

9. g.2 MATERIAL BALANCE

9. h. GROUT AND REPAIR MORTARS 9. h.1 MANUFACTURING PROCCES

Add cement in a blender and start the blender. Add quartz and SNF powder and blend for 45 minutes. On QC approval unload the material and pack.

9. h.2 MATERIAL BALANCE

10. PAPER AND LEATHER CHEMICALS

10.a. DE-INKING CHEMICALS

10. a.1 MANUFACTURING PROCCES

Charge Sodium tri poly phosphate and di-potassium phosphate in the blender and blend for 30 minutes.

Add antifungal and salt and mix for 60 minutes. Add enzyme 1, enzyme 2 & enzyme 3 and mix for 60 minutes. On QC approval filter, unload the material and pack.


10.b. REFINING CHEMICALS

10. b.1 MANUFACTURING PROCCES

Charge water in a vessel Add Enzyme A, Enzyme B & Enzyme C and mix for 30 minutes Add Emulsifier M & stir for 10 minutes. Then add Salt & Antifungal and stir for 15 minutes On QC approval unload the material and pack.

10. b 2 MATERIAL BALANCE

10.c. BLEACHING AGENT

10.c.1 MANUFACTURING PROCCES

Charge water in vessel Add Magnesium chloride & mix for 30 minutes Add Chelating Agent & stir for 10 minutes. Then add Sodium Gluconate & stir for 15 minutes


10.d. SOAKING CHEMICALS

10.d.1 MANUFACTURING PROCCES

Charge the Sodium Tri Poly Phosphate, Sodium Carbonate & Sodium Conjugate in the blender & blend for 30 minutes.

Add antifungal & Sodium chloride & mix it for 30 minutes. Add Enzyme Protease & Emulsifier & mix for 30 minutes.


10.e. DEGREASING CHEMICALS

10.e.1 MANUFACTURING PROCCES

Charge water in a vessel Add Tri Decyl Alcohol Ethoxylate & Lauryl Alcohol Ehoxylate & mix for 30 minutes Add Chelating Agent & stir for 10 minutes. Then add Tri Ethanol Amine & stir for 15 minutes


10.f. SURFACE TREATMENT CHEMICALS

10.f.1 MANUFACTURING PROCCES

Charge Sodium Tri Poly Phosphate, Sodium Carbonate, Sodium Gluconate & Dicalcium Phosphate in a blender.

Blend for 30 minutes. Add antifungal & Sodium chloride & mix it for 30 minutes. Add Enzyme Protease & Emulsifier & mix for 30 minutes.

10.f.2 MATERIAL BALANCE

10.g. SPECIALITY CHEMICALS FOR PAPER AND LEATHER

10.g.1 MANUFACTURING PROCCES

Charge the Sodium Tri Poly Phosphate , Sodium Carbonate , Sodium Gluconate & Enzyme Lipase in the blender & blend for 30 minutes

Add antifungal & Sodium chloride & mix it for 30 minutes. Add Enzyme Protease & Emulsifier & mix for 30 minutes.

10.g.2 MATERIAL BALANCE

11. ANTISTATIC OIL/MINERAL OIL/ LUBRICANT OIL/GREASE/CONING OIL

11.a. ANTISTATIC OIL


Charge Mineral oils & add emulsifiers & ester & stir for 15 minutes Add water , Surfactant & Tackifier & stir for 15 minutes Total batch time is 30 minutes.


11.b. DE-DUSTING OILS

11.b.1 MANUFACTURING PROCCES

Charge Mineral oils. Add emulsifiers, ester & surfactants and stir for 15 minutes. Add water & again stir for 15 minutes


11.c. SEWING THREAD LUBRICANTS

11.c.1 MANUFACTURING PROCCES

Charge Mineral oils, IPP & Stearate & stir for 30 minutes. Add Silicon oils & stir for 75 minutes Total batch time is 105 minutes.


11.d. SPECIALITY MINERAL OILS

11.d.1 MANUFACTURING PROCCES

Charge Mineral oils 1,2,3 & 4 & stir for 30 minutes Total batch time is 30 minutes.


11.e. SPECIALITY LUBRICANT OILS/CONING OIL

11.e.1 MANUFACTURING PROCCES

Charge Mineral oils & add emulsifiers & ester & stir for 15 minutes Add water, surfactant & Tackifier and stir for 15 minutes Total batch time is 30 minutes.


12. AGRO FORMULATION PRODUCTS

12.a Liquid insecticides

12.a.1 Manufacturing process

All the RM in liquid from are inspected physically , weighed and charged to the blending vessel for homogeneous mixing for 30 minutes. Samples is withdrawn after 30 min for testing the sample for homogeneity. If not Ok then further mix for 30 minutes else the material is filtered through basket filter , over size material is recycle back to system and under sized material is filled in container for dispatch

12.a.2 Material balance

12.b Powder Insecticides

12.b.1 Manufacturing process

All the RM in powder from are inspected physically , weighed and charged to the blender for homogeneous mixing for 30 minutes. Samples is withdrawn after 30 min for testing the sample for homogeneity. If not Ok then further mix for 30 minutes else the material is sieved through sifter , over size material is recycle back to system and under sized material is packed for dispatch.

12.b.2 Material balance

12.c Liquid herbicides

12.c.1 Manufacturing process


12.c.2 Material balance

12.d Powder Herbicides

12.d.1 Manufacturing process


12.d.2 Material balance

12.e Liquid fungicides

12.e.1 Manufacturing process


12.e.2 Material balance

12.f Powder fungicides

12.f.1 Manufacturing process


12.f.2 Material balance

12.g Liquid acaricide

12.g.1 Manufacturing process

All the RM in liquid from are inspected physically, weighed and charged to the blending vessel for homogeneous mixing for 30 minutes. Samples is withdrawn after 30 min for testing the sample for homogeneity. If not Ok then further mix for 30 minutes else the material is filtered through basket filter , over size material is recycle back to system and under sized material is filled in container for dispatch

12.g.2 Material balance

12.h Plant Growth Regulators Supplement (PGRS)-Liquid

12.h.1 Manufacturing process


12.h.2 Material balance

12.i Plant Growth Regulators Supplement (PGRS)-Powder

12.i.1 Manufacturing process


12.i.2 Material balance

Synthesis Products

13. FERMENTATION PRODUCTS (ENZYMES) 13.1 MANUFACTURING PROCESS

Add Carbohydrates (carbon), Proteins (nitrogen), Mineral Salts, Additives, water and Microbial culture in seed vessel. Now add Carbohydrates (carbon), Proteins (nitrogen), Mineral Salts, Additives, water in a fermenter, followed by addition of material from seed vessel.

After 5 days of fermentation with inoculated microbes, fermentation broth is formed containing microbes, enzyme and un-hydrolyzed substrates.

Add filter aid on filter to aid filtration. Filter the broth through press filter. The residue called wet cake, consist of microbes and un-hydrolyzed substrates which is our by-product i.e. Nutrient Powder.

The filtrate consists of enzyme. Now it undergoes ultra-filtration, permeate of ultra-filtration goes to the ETP and the concentrate which consist of enzyme undergoes microfiltration. The concentrate is Spray Dried and the product i.e. Enzyme is obtained.

Acid, Alkali, Antifoam and Water from the dosing vessel is added in the fermenter as and when needed.


14 FERMENTATION PRODUCTS (PROBIOTICS) 14.1 MANUFACTURING PROCESS

Add Carbohydrates (carbon), Proteins (nitrogen), Mineral Salts, Additives, water and Microbial culture in seed vessel. Now add Carbohydrates (carbon), Proteins (nitrogen), Mineral Salts, Additives, water in a fermenter, followed by addition of material from seed vessel.

After 5 days of fermentation with inoculated microbes, fermentation broth is formed containing microbes, enzymes and un-hydrolyzed substrate.

Filter the broth through press filter. The residue left is a wet cake which further undergoes lyophilization where freeze drying of the wet cake is done. In freeze drying under vacuum water is evaporated and product is obtained.

The filtrate after filtration undergoes ultrafiltration, permeate of ultra-filtration goes to the ETP and the concentrate is our by-product i.e. Nutrient Liquid.

Acid, Alkali, Antifoam and Water from the dosing vessel is added in the fermenter as and when needed.


15. METHYLCOBALAMIN


Charge 200 litres of methanol in a reactor. Add cynocobalamine & mix for 30 minutes. Add water, cobalt chloride and monomethyl oxalate. After completion of reaction the liquid is passed through column. The solution obtain is crystallized. After QC approval pack the material.


16. OX BILE EXTRACT


Charge 200 liters of ethanol in a reactor. Add fresh bile paste & mix for 45 minutes. After complete dissolution add filter aid in solution. Take the solution for filtration. Dry the cake formed in the tray drier. Pulverize the material into fine powder. After QC approval pack the material.


17. PROTEASE FROM ANIMAL ORIGIN


Charge half quantity of water in a reactor. Add crude glands & mix for 30 minutes. Monitor for the activity. After achieving required activity add IPA. Take the mass in to centrifuge. Dry the mass obtained and pulverized & pack.


18. PROTEASE FROM PLANT ORIGIN 18.1 MANUFACTURING PROCESS

Charge half quantity of water in a reactor. Add crude Flakes & mix for 30 minutes. Add calcium chloride & Filter aid. After achieving required activity take up for filtration. Concentrate the material & spray dry. Dry the powder obtained. On QC approval pack the material.


19. ETHYLENE OXIDE / PROPYLENE OXIDE CONDENSATE

19.1 CHEMICAL REACTION

19.2 MANUFACTURING PROCCES

Ethoxylation- An alcohol is treated with ethylene oxide and potassium hydroxide (KOH) which serves as a catalyst.

The reactor is pressurized with nitrogen and heated to about 150 degree Celsius. Typically 5 to 10 units of ethylene oxide is added to each alcohol depending on the requirement. Finally pH is adjusted by acetic acid to neutral.


20. BINDERS & OTHER POLYMERS

20.1 CHEMICAL REACTION

STAGE 1

STAGE 2


Part A: (N Methyl Acrylamide derivative)

Mix water( 0.0062) and acrylamide Add formaldehyde, mix well and keep aside.

Part B:

Add urea to water (0.2679) and stir till it is dissolved. Add emulsifier, ethyl acrylate, acrylic acid and stir well till the solution is obtained. Add part A in this slowly and mix well and keep.

Part C: (Preparation of continuous catalyst)

Add catalyst 2 and Sodium Metabisulphite in water (0.0208). Make a clear solution.

Part D:

Take water (0.2679) in a reaction vessel and add emulsifier and then catalyst and stir well for 15 minutes.

Now add Part B & C slowly by controlling temperature in 2 to 3 hours. Mix well and maintain for 3 hours.


21. POLYMERS FOR PAINT & OTHER INDUSTRIES

21.1. CHEMICAL REACTION

STAGE 1

STAGE 2

STAGE 3

21.2. MANUFACTURING PROCCES

Charge Water & Acryclic Acid in reactor for 15 minutes Add hydrogen Peroxide & ferrous Sulphate & mix for 10 minutes Add Mercapto Ethanol to start the reaction & temperature goes upto 60 degree celsius. Add Sodium Hydroxide in 120 minutes & cool the material to room temperature.

22. SOFTNER1/ SOFTNER2(Textile & Laundry Chemicals)

22.(i) SOFTNER1

22.(i) 1 CHEMICAL REACTION

STAGE 1

STAGE 2

22.(i) 2 MANUFACTURING PROCESS

Charge fatty acid like Stearic acid in reactor. Heat the mass to 100 degree Celsius. Start stirrer and add tri amine. Raise the temperature to 140-150 degree Celsius and maintain for 8 hours. Collect water distillate in a receiver. Test for completion of reaction and cool it to 100 degree Celsius. Add acetic acid, maintain for 4 hrs and then add cetostearyl Ethoxylate. Drawning is done in water which contains sodium chloride and sodium lignosulphonate.

22.g. (i) 3 MATERIAL BALANCE

22.(ii) SOFTNER2 22.(ii)1 CHEMICAL REACTION

STAGE1

STAGE2

22.(ii) 2 MANUFACTURING PROCESS

Charge fatty acid Like, Stearic acid in a reactor. Heat the mass to 100 °C. Start stirrer and add Di Ethanol Amine & Amino Ethyl Ethanol Amine. Raise the temp. to 140 -150 °C Maintain for 8 hrs . Collect water distillate in a receiver. Test for

completion of reaction Cool to100 deg cent. Add Di Methyl Sulphate, maintain for 4 hrs. Then add cetostearyl Ethoxylate & sodium

lignosulphonate. Check for reaction & send to flaker

22.(ii) 3 MATERIAL BALANCE

23. ORGANOPOLY SILOXANE


The raw materials D4, DVTMDS & silanolate are charged into the clean reactor Which is agitated for 4 hours at 80° C. under nitrogen, heating up to 150° C. and stirs for 1.5 hours, and further heating-up to 185° C. in vacuum and stirs for another 1.5 hours. The primary product then circulates 2 times for eliminating low molecular Weight products via a 10 liters batch falling strand devolatilizer in 20-34 torr under 190° C. Wall temperature. After cooling to room temperature, the product’s viscosity is larger than 3000 cP, the volatile content is 1.91%, molecular Weight MW is larger than 80000, MW/Mn:1.7, and yield is 85.4%. The viscosity is measured by Brooklield DV I+ viscometer under room temperature. When the viscosity is in the range of 1,000 cp, S18 revolving pin is used at a rotational speed of 1.5~2 rpm. When the viscosity is in the range of 100,000 cp, S25 revolving pin is used at a rotational speed of5~6 rpm. The volatile content is measured by Mettler HR73 Halogen Moisture analyzer to choose 5-gram sample and to measure its Weight loss after heating 150° C. for 3 hours. The molecular weight is measured with GPC calibrated by polystyrene, While the yield is calculated by D4 as the base. 23.2 MATERIAL BALANCE

24. BLOCKED POLYSTER


Charge all glycol one by one like DEG, MEG, Ethoxylated Glycerine,Neopentyl glycol,Penta erythritol heat up to 60 deg.cen. once temperature reached up to 100 deg. Add Terpthalic acid and ISOPTHALIC ACID and raised temperature slowly up to 145-150 deg. Maintain column temperature less than 115 deg. Temperature increased slowly up to 220 deg. With maintaining column temperature bellow 115 deg. Check acid value at regular interval Once acid value reached up to below 15 Apply cooling up to 180 deg. Add PEG 6000 and heat up to 200 deg. Check water tolerance Once water tolerance achieved start discharge material in to blender containing water Add antibacterial material Dilute with water to get desired solids.


25. POLYURETHANE


Polyurethane prepolymer is prepared from the polyol and the polyisocyanate in the presence or absence of a solvent, and then the polyurethane prepolymer is mechanically dispersed in water by using a surfactant or the polyurethane prepolymer is reacted with an active hydrogen compound having an anionic or cathionic salt-forming group, to obtain a water-base product. Further, it is possible to introduce a blocked isocyanate group by reacting the polyol component with the above-mentioned polyisocyanate compound which has been partially blocked by a phenol such as phenol, o-cresol or xylenol; a lactam such as -butyrolactam or -caprolactam; an oxime such as methyl ethyl ketoxime or acetoxime; an imide such as succinic acid imide or phthalic acid imide; or a sulfite such as acidic sodium sulfite, or by reacting a terminal isocyanate prepolymer preliminarily prepared from the polyol component and the polyisocyanate compound, with a blocking compound.

The water-base polyurethane emulsion of the present invention may be used in combination with other water-base emulsions such as an acryl emulsion, a styrene-butadiene latex, a vinyl acetate emulsion, a vinyl chloride emulsion or an epx


26. SIZING CHEMICALS (Paper & Leather Chemicals) 26.1 MANUFACTURING PROCCES

Charge the reactor with Gum Rosin. Heat the reator with Gum Rosin. Raise temperature to 160 degree centigrade & add Maleic hydride & Fumeric Acid. Maintain temperature at 160 degrees for 2 hours. Check the mixture, if ok drawn slowly in 4 hours mixture of caustic flakes and water.


27. NEUTRASIZING CHEMICALS


Charge the reactor with Gum Rosin. Heat the reactor to melt Gum Rosin. Raise temperature to 160 degres Celsius. Add Maleic hydride, maintain at 160 degree celsius for I hour. Check for good mixture, if ok, drawned slowly in 4 hrs mixture of potassium hydroxide, tri-ethanol

amine, casein, formaldehyde and water.


28. GREASE (Antistatic Oil/ Mineral Oil/ Lubricant Oil/ Grease/ Coning Oil)


Charge fatty acid (Stearic acid) in special reactor. Heat the mass to 100 degree celsius. Start stirrer and add mineral oil & catalyst. Raise the temperature to 120-130 degree celsius and maintain for 4 hours. Collect water distillate in a receiver. Test for completion of reaction and cool to 100 degree celsius. Add lithium hydroxide and borax and maintain temperature between 120-130 degree celsius for 4 hours and test. If o.k. cool to room temperature.


Annexure-2 List of Raw material

Pharmaceutical Products Enzyme Conc. Powder 0.200 4.209 & Food Supplement Lactose 0.800 16.835Food & Breweries Enzyme Conc. Powder 0.200 2.946

Lactose 0.800 11.7853 Animal Health & Nutrition Products

Phosphoric Acid 0.200 252.525Formic Acid 0.100 126.263Calcium Propionate 0.040 50.505Herbal Extract 0.040 50.505Calcite 0.620 782.828

Cocktail Enzyme Cellulase Conc. Powder 0.040 50.505Products Amylase 0.012 15.152

Pectinase 0.010 12.626Phytase 0.010 12.626Protease 0.012 15.152Calcite 0.916 1156.566Sodium Chloride 0.100 126.263Calcium Lactate 0.100 126.263Calcium Gluconate 0.050 63.131Magnasium Sulphate 0.030 37.879Potassium Chloride 0.350 441.919Sodium Citrate 0.090 113.636Dextrose 0.280 353.535

Antibiotic Powder Ampicllin 0.500 631.313 injection Formulation Cloxacillin 0.500 631.313Antibiotic Liquid Albandazole 0.025 31.566injection Formulation Water 0.975 1231.061

Vit A 0.001 1.263Vit D 0.004 5.051Vit C 0.050 63.131Vit B1 0.003 3.788Vit B6 0.035 44.192Vit B12 0.090 113.636Rice Husk 0.817 1031.566

4 Cosmetic ProductsEthanol 0.700 2.917Water 0.250 1.042Isopropyl C12-15 Pareth-9-Carboxylate 0.050 0.208Citric acid 0.002 0.008Cetereth -20 0.020 0.083Cetyl alcohol 0.060 0.250Adipic acid 0.011 0.046Dipropylene glycol 0.015 0.063Water 0.883 3.679Colour 0.002 0.008Preservative 0.002 0.008Fragrance 0.005 0.021SLES 0.250 3.125Laureth-5-carboxylic acid 0.030 0.375Water 0.636 7.948Cocoamidopropylhydroxysultaine 0.020 0.250Hydrolysed Animal Protein 0.010 0.125Preservative 0.030 0.375Fragrance 0.002 0.025Colour 0.002 0.028Sodium Chloride 0.020 0.250

Ethanol 0.302 12.634Triethanol amine 0.003 0.126Propylene glycol 0.150 6.275Glycerol 0.020 0.837Alpha tocopheryl acetate 0.008 0.335Fragrance 0.002 0.084Water 0.515 21.545

Raw material RM Consumption

MT/batch

RM Consumption

MT/month

Phase-1 Formulation Products

a)

b)

c)

5

a)

b)

c)

d)

e)

f)

S. No.

1

2

Name of product

Acidifier Formulation

Electrolyte Formulation

Vitamin mix Formulation

After shave Lotion

Cream Hair Conditioner

Shampoo with Protein

Sanitizer & Disinfectants

SLES 0.234 195.783water 0.630 527.108colour 0.008 6.693sodium sulphate 0.108 90.361Fragrance 0.020 16.734

7 Textile Chemicals & Laundry Chemicalscitric acid 0.050 12.563water 0.602 151.256Chelating agent 0.100 25.126Sodium ligno sulphonate 0.109 27.387Sodium sulphate 0.139 34.925Water 0.080 20.000Lactic acid 0.210 52.500Formic acid 0.080 20.000Propionic acid 0.040 10.000Acetic acid 0.090 22.5001-Hydroxy ethylidene-1,1-Diphosphoric acid 0.050 12.500hydrochloric acid 0.350 87.500iso propyl alcohol 0.020 5.000phosphoric acid 0.080 20.000Sodium Alpha olefin sulfonate 0.221 55.346Na salt-DETMP 0.038 9.538Glycerine 0.040 10.040Mono propylene glycol 0.114 28.614Hexylene glycol 0.214 53.715Turkey red oil 0.054 13.554Sodium cumene sulfonate 0.106 26.606polymers acrylic acid base 0.054 13.554dioctyl sulfo succinate 0.114 28.614Triethanolamine 85% 0.024 6.024Sodium hypo chlorite 0.008 2.008Hydrogen peroxide 50% 0.010 2.385Antimicrobial 0.004 1.004Ortho Xylene 0.230 57.533Pine oil 0.170 42.543Deodorided kerosene 0.250 62.563Polysiloxane polyol 0.040 10.010Octanol 0.200 50.050Benzyl benzoate 0.018 4.505Mono methyl ethanolamine 0.031 7.833Parafin wax 0.031 7.758Benzyl chloride 0.000 0.025Oleic acid 0.030 7.508Silicone polyether copolymer 0.025 6.256Water 0.652 163.188polycarboxylic acid 0.017 4.204Tallow fattyacid amidoethyl Eo lactate 0.200 50.050Dimethyl dialkyl ammonium chloride 0.001 0.250hostapur SAS 60 0.005 1.251Polyacrylamide polymer 0.000 0.025UV absorbers/substantive sunscrenes 0.100 25.025Sodium meta-silicate 0.275 68.970Phosphonate 0.050 12.563Resist salt 0.064 16.080Ethoxylate-steryl amine 0.001 0.126Sodium bicarbonate 0.194 48.744sodium formate 0.154 38.693yellow detergent 0.254 63.819Sodium perborate monohydate 0.004 1.005Sodium bisulphate 0.005 1.256Starch-Modified potato starch 0.726 182.286Borax 0.050 12.563polymers acrylic acid base 0.024 6.030polyvinylpyrrolidone K-30 0.015 3.643Polymer- sodium salt 0.064 16.080Polyvinyl alcohol 0.104 26.131Cokooidal silica 0.015 3.769

6

a)

Pre-Treatment Auxilliaries-6


Cleaning Chemicals






Acid- Oxalic acid 0.002 0.503Aluminium trichloride 0.001 0.251Water 0.016 33.333Lactic acid 0.080 166.667Formic acid 0.340 708.333Propionic acid 0.020 41.667Acetic acid 0.370 770.8331-Hydroxy ethylidene-1,1-Diphosphoric acid 0.020 41.667hydrochloric acid 0.030 62.500iso propyl alcohol 0.020 41.667citric acid 0.064 133.333phosphoric acid 0.040 83.333AOS 0.304 381.910WATER 0.220 276.382CASTOR OIL ETHOXYLATE 0.179 224.874CETOSTERYL ALCOHOL ETHOXYLATE 0.017 21.357ACETIC ACID 0.030 37.688DISPERSING AGENT 0.230 288.945SODIUM SULPHATE 0.020 25.126DIMETHYL AMINE 0.264 66.265EPI CHLORO HYDRIN 0.241 60.492WATER 0.495 124.247AMINO SILICONE OIL 0.354 88.945WATER 0.264 66.332TRI DECYL ALCOHOL ETHOXYLATE 0.178 44.724SODIUM SULPHATE 0.017 4.271POLYETHYLENE GLYCOL 0.168 42.211ACETIC ACID 0.019 4.774ACRYLIC COPOLYMER 0.030 12.550TRIDECYL ALCOHOL ETHOXYLATE 0.084 35.141ANTIFUNGAL AGENT 0.002 0.837BUTYL CARBITOL 0.040 16.734HEDP 60% 0.080 33.467LAURYL ALCOHOL ETHOXYLATE 0.170 71.118WATER 0.544 227.577DISPERSING AGENT 0.050 20.917Optical Brightner 0.650 19.034Water 0.200 5.857Dispersing Agent 0.150 4.393WATER 0.244 18.355ANTIFOAMING AGENT 0.004 0.301BUTYL CARBITOL 0.007 0.527SODIUM CHLORIDE 0.057 4.288MAGNESIUM SULPHATE 0.038 2.859Lauryl alcohol ethoxylate 0.650 48.897OT LIQUID 0.850 53.338PROPYLENE GLYCOL 0.150 9.413Sequestering agent 0.050 3.141SODIUM PER CARBONATE 0.790 49.623LAURYL ALCOHOL ETHOXLATE 0.082 5.119ANTIFOAMING AGENT 0.025 1.539TALCUM POWDER 0.054 3.392PVA Emulsion 0.900 150.602Acrylamide 0.060 10.040Softner 0.040 6.693Antifoaming Agent 0.050 8.367Tri Decyl Alcohol Ethoxylate 0.340 56.894Water 0.560 93.708Thickner 0.050 8.367Silicon Oil 0.180 15.060Water 0.638 53.380Emulsifier 0.140 11.714Acetic acid 0.004 0.335Urea 0.030 2.510Sodium Acetate 0.008 0.669Acetic Acid 0.010 0.628Tri Decyl Alcohol Ethoxylate 0.143 8.982Iso Propanol 0.052 3.266Butyl Carbitol 0.205 12.877

k)

l)

m)

n)

b)

c)

d)

e)

f)

g)

h)

i)

j)

Surfactants

Silicon Oil

Emulsifier

Polysol

Pre-treatment auxiliary-2 SPL (Green acid)

Dyeing Auxilliaries

Printing Auxilliaries

Finishing Auxilliaries

Speciality Chemicals

Optical Brightners

Scouring Agent

Wetting Agent

Bleaching Agent

Water 0.100 6.281Lauryl Alcohol Ethoxylate 0.490 30.779SLS POWDER 0.020 1.256SODIUM PER CARBONATE 0.020 1.256SODA ASH 0.105 6.564SODIUM SULPHATE 0.482 30.245ANTIDUSTING OIL 0.001 0.063SODIUM LIGNO SULPHONATE 0.084 5.276DI SODIUM PHOSPHATE 0.289 18.153

8 Enzyme FormulationCARAMEL POWDER 0.008 0.168ENZYME 0.055 1.143WATER 0.677 14.175TRIDECYL ALCOHOL ETHOXLATE 0.100 2.094PRESERVATIVE 0.001 0.021BUTYL CARBITOL 0.002 0.042SODIUM CHLORIDE 0.157 3.296CARAMEL POWDER 0.010 0.838ENZYME 0.150 12.563WATER 0.498 41.709SORBITOL 0.201 16.834PRESERVATIVE 0.002 0.168SODIUM CHLORIDE 0.139 11.642CARAMEL POWDER 0.010 0.754ENZYME 0.190 14.322WATER 0.348 26.231SORBITOL 0.240 18.090CETO STERYL ALCOHOL ETHOXYLATE 0.071 5.352PRESERVATIVE 0.002 0.151SODIUM CHLORIDE 0.139 10.477

Enzymes for De-Gumming ENZYME 0.070 0.586Agents MONO SODIUM PHOSPHATE 0.150 1.256

CASTOR OIL ETHOXLATE 0.015 0.121ANTI FUNGAL AGENT 0.001 0.012SODIUM SULPHATE 0.762 6.382CETOSTYRYL ALCOHAL ETHOXYLATE 0.000 0.001BENTONITE POWDER 0.002 0.017Enzyme 0.080 1.675Mono Sodium Phosphate 0.450 9.422Di Sodium Phosphate 0.250 5.235Acrylic Co Polymer 0.021 0.448Antifoaming agent 0.002 0.042Tri Decyl Alcohol Ethoxylate 0.011 0.230Zeolite powder 0.134 2.797Bentonite powder 0.052 1.089

9 Construction ChemicalsSLES 0.054 11.307WATER 0.030 6.281DISPERSING AGENT 0.620 129.816SODIUM SULPHATE 0.109 22.822SODIUM LIGNOSUPHONATE 0.160 33.501CAUSTIC SODA 0.027 5.653Additive for Binder 0.013 0.544Thickner 0.003 0.126Quartz Powder 0.664 27.806WHITE CEMENT 0.270 11.307Hydrated Lime 0.050 2.094Resin Gun Grade 0.994 41.625O-xylene 0.001 0.042Hardner 731 0.005 0.209Additive for Epoxy 0.003 0.603Resin 0.536 107.739Leveling Agent 0.018 3.618Resin Diluent 0.093 18.693Polymeric Powder 0.005 0.968Additive for cement 0.010 1.936Whitener 0.005 0.968Talcum Powder 0.285 55.177

e)

a)

b)

c)

d)

e)

a)

b)

c)

d)

o)

Surface Treatment Chemicals

Adhesives & Sealants

Flooring Chemicals

Tiling Chemicals

Enzymes for Desizing

Enzymes for Fading

Enzymes for Bio-polishing

Neutral Enzymes

Plasticizers &Additives

Detergents

Binder 0.005 0.968White Cement 0.445 86.153Quartz Powder 0.245 47.433

Protective Coating DISPERSING AGENT 0.020 1.675& Wall Care SILICA QUARTZ SAND 0.450 37.688

SODIUM THIOSULPHATE 0.030 2.513CEMENT 0.450 37.688SODIUM LIGNO SULPHONATE 0.050 4.188Water 0.027 5.255Acrylic Polymer 0.284 55.011Cement 0.295 57.085Binding agent 0.021 4.149Quartz sand 1 0.096 18.586Additive for cement 0.021 4.149Quartz sand 2 0.252 48.788Formaldyhyde 0.002 0.415Acrylic Polymer 2 0.001 0.111Quartz Sand 3080 0.309 260.101SNF Powder 0.011 9.259Quartz Sand 1630 0.155 130.471Cement PPC 0.525 441.919

10 Paper & Leather ChemicalsEnzyme 1 0.210 4.397Enzyme 2 0.012 0.251Enzyme 3 0.040 0.838Antifungal 0.005 0.105Sodium Tri Poly Phosphate 0.200 4.188Salt 0.428 8.961Di Potassium Phosphate 0.105 2.198Enzyme A 0.665 13.938Enzyme B 0.021 0.440Enzyme C 0.060 1.258Antifungal 0.011 0.231Emulsifier M 0.200 4.192Salt 0.028 0.587Water 0.015 0.314Magnesium Chloride 0.050 2.094WATER 0.791 33.124Chelating Agent 0.050 2.094Sodium Gluconate 0.109 4.564Enzyme Protease 0.050 1.047Sodium Tri Poly Phosphate 0.100 2.094Sodium Carbonate 0.200 4.188Sodium Gluconate 0.015 0.314Emulsifier 0.050 1.047Sodium Chloride 0.580 12.144Antifungal 0.005 0.105Tri Decyl Alcohol Ethoxylate 0.050 1.047WATER 0.721 15.096Chelating Agent 0.030 0.628Tri Ethanol Amine 0.110 2.303Lauryl Alcohol Ethoxylate 0.089 1.863Enzyme Protease 0.100 2.094Sodium Tri Poly Phosphate 0.100 2.094Sodium Carbonate 0.200 4.188Sodium Gluconate 0.015 0.314Emulsifier 0.050 1.047Sodium Chloride 0.480 10.050Di Calcium Phosphate 0.050 1.047Antifungal 0.005 0.105Enzyme Protease 0.050 5.235Enzyme Lipase 0.020 2.094Sodium Tri Poly Phosphate 0.100 10.469Sodium Carbonate 0.200 20.938Sodium Gluconate 0.015 1.570Emulsifier 0.050 5.235Sodium Chloride 0.560 58.626Antifungal 0.005 0.523

c)

d)

e)

f)

g)

f)

g)

h)

a)

b)

Speciality for leather

Waterproofing chemicals

Surface Treatment Chemicals

De-inking Chemical

Refining Chemical

Bleaching Agent

Soaking chemical

Grout & Repair Mortars

Degreasing Chemicals

11 Antistatic Oil/ Mineral Oil/ Lubricant Oil/ Grease/ Coning OilMINERAL OILS 0.840 351.406WATER 0.020 8.367EMULSIFIERS/ESTERS 0.080 33.467SURFACTANT 0.020 8.367TACKIFIER 0.040 16.734MINERAL OILS 0.700 70.281WATER 0.010 1.004EMULSIFIERS/ESTERS 0.230 23.092Surfactants 0.060 6.024SILICON OILS 0.2 20.080MINERAL OIL 0.68 68.273IPP 0.06 6.024STEARATE 0.06 6.024MINERAL OILS-1 0.200 167.336MINERAL OILS-2 0.450 376.506MINERAL OILS-3 0.200 167.336MINERAL OILS-4 0.150 125.502

Speciality Lubricant Oils / MINERAL OILS 0.680 398.260Coning Oil WATER 0.080 46.854

EMULSIFIERS/ESTERS 0.200 117.135TACKIFIER 0.030 17.570SURFACTANT 0.010 5.857

12 Agro formulation productsa) Liquid insecticides Alphacypermithirine 0.01 0.188

Chlropyriphos 0.021 0.394Cypermithirine 0.01 0.188Ethion Tech 0.056 1.050Fenvelerate 0.021 0.394LamndaCyhalothrin 0.003 0.056Malathion 0.056 1.050Monochrophos 0.05 0.938Novaluron 0.01 0.188Propinophos 0.053 0.994Emulsifier 0.111 2.081Solvents 0.6 11.250

b) Powder Insecticides Acephate 0.075 0.688Acetamiprid 0.02 0.184Cartap Hydrochloride 0.05 0.459Imidacloprid 0.07 0.642Thiamithoxam 0.025 0.229Fipronil 0.003 0.028China Clay 0.757 6.946

c) Liquid Herbicides 2,4-D Ethyl Ester 0.038 0.2222,4-D Dimethyle Amine Salt 0.058 0.339Butachlor 0.03 0.175Glyphosate 0.041 0.239Oxyfluorfen 0.029 0.169Paraquat Di Chloride 0.024 0.140Pendimethalin 0.045 0.263Pretilachlor 0.055 0.321Propaquizafop 0.03 0.175Emulsifier 0.07 0.409Solvents 0.58 3.387

d) Powder Herbicides Atrazine 0.05 0.209Isoproturon 0.075 0.313Metribuzin 0.07 0.292Metsulfuran Methyl 0.02 0.083Piroxofop-Propinyl 0.015 0.063China Clay 0.77 3.212

e) Liquid Fungicides Hexaconazole 0.005 0.046Mancozeb 0.037 0.340Propiconazole 0.025 0.229Sulphur 0.04 0.367Emulsifier 0.143 1.312Solvents 0.75 6.882

f) Powder Fungicides Captan 0.05 2.294Carbendazim 0.05 2.294

e)

a)

b)

c)

d)

Antistatic Oils

De-dusting Oils

Sewing Thread Lubricants

Speciality Mineral Oils

Copper Oxychloride 0.05 2.294Cymoxanil 0.008 0.367Dodine 0.065 2.982Mancozeb 0.075 3.441Myclobutanil 0.01 0.459Sulphur 0.08 3.670Thiram 0.075 3.441Tricyclazole 0.075 3.441Zineb 0.075 3.441China Clay 0.387 17.755

g) Liquid Acaricide Dicofol 0.018 0.068Propergite 0.057 0.214Emulsifier 0.225 0.845Solvents 0.7 2.628

h) Plant Growth Regulators Ethephon 0.04 0.067Supplements (PGRS) - Liquid Emulsifier 0.28 0.467

Solvents 0.68 1.134i) Plant Growth Regulators Triacontanol 0.005 0.008

Supplements (PGRS) – Powder China Clay 0.995 1.660

Fermentation Acid 0.100 1.465Products (Enzymes) Alkali 0.050 0.733

Antifoam 0.050 0.733Water 1.300 19.049Carbohydrates (carbon) 0.003 0.044Proteins (nitrogen) 0.001 0.015Mineral Salts 0.001 0.015Vitamins 0.000 0.001Additives 0.001 0.015Water 0.050 0.733Microbial culture 1.200 17.583Carbohydrates (carbon) 2.400 35.167Proteins (nitrogen) 0.625 9.158Mineral Salts 0.500 7.326Vitamins 0.035 0.513Additives 0.340 4.982Water 35.000 512.847Filter Aid 0.500 7.326Preservative 0.005 0.073

Fermentation Acid 0.100 0.561Products (Probiotic) Alkali 0.050 0.281

Antifoam 0.050 0.281Water 1.300 7.297Carbohydrates (carbon) 0.001 0.006Proteins (nitrogen) 0.001 0.006Mineral Salts 0.001 0.006Additives 0.000 0.001Water 0.050 0.281Microbial culture 1.200 6.736Carbohydrates (carbon) 0.770 4.322Proteins (nitrogen) 0.700 3.929Mineral Salts 0.350 1.965Additives 0.050 0.281Water 35.000 196.459Cynocobalaine(Vit B12) 0.020 0.029Mehanol 0.500 0.714Water 0.400 0.571Monoethyl oxalate 0.040 0.057Cobalt Chloride 0.040 0.057Fresh Bile Paste 0.250 4.167Ethanol 0.700 11.667Filter aid 0.050 0.833

Protease from Crude Gland 0.250 12.235Animal Origin WATER 0.250 12.235

IPA 0.500 24.471Protease from Crude Flakes or powder 0.200 8.333Plant Origin WATER 0.743 30.958

Calcium Chloride 0.002 0.083

Phase-2 Synthesis Products

13

14

15

16

17

18

Methyl Cobal Amine

Ox Bile Extract

Filter aid 0.040 1.667Sodium Meta Bisulphite 0.015 0.625

Ehtylene Oxide/ Propylene Alcohol 0.771 642.417 Oxide Condensate Ethylene Oxide 0.220 183.333

Potassium hydroxide 0.000 0.333Acetic acid 0.001 0.500Water 0.563 703.463Acrylamide 0.013 16.388Formaldehyde 0.008 9.388Urea 0.020 25.375Emulsifier 0.033 40.625Acrylic Acid 0.013 15.638Catalyst 1 0.001 0.625Catalyst 2 0.001 1.000Sodium Metabisulphite 0.001 1.250Ethyl Acrylate 0.349 436.250

Polymers for Paint & Water 0.590 741.457Other Industries Acrylic Acid 0.219 275.126

Hydrogen Peroxide 0.025 30.905Ferrous sulphate 0.001 1.005Mercapto Ethanol 0.039 48.995Sodium Hydroxide 0.126 158.794Fatty Acids like Stearic acid 0.162 94.500Diethyle triamine 0.026 15.167Acetic acid 0.025 14.583Cetostearyl alcohol Ethoxylate 0.021 12.250Sodium Lignosulphonate 0.049 28.583Sodium Chloride 0.110 64.167Water 0.607 354.083Fatty Acids like Stearic acid 0.61 355.833Di ethanol amine 0.17 99.167Amino ethyl ethanol amine 0.08 46.667Di methyl sulphate 0.05 29.167Cetostearyl alcohol Ethoxylate 0.05 29.167Sopdium Lignosulphonate 0.04 23.333DVTMPS (1,3 Divinyl tetra methyl disiloxane) 0.00178 0.104TBPH (Silanolate) 0.00123 0.072D4 (Octamethyl cyclo tetra siloxane) 0.575 33.469Water 0.422 24.563Di Ethylene Glycol 0.1 2.000Mono Ethylene Glycol 0.16 3.200Ethoxilated Glycerine 0.06 1.200Penta Erythritol 0.05 1.000Neo Pentyl Glycol 0.13 2.600Terpthalic Acid 0.25 5.000Isopthalic Acid 0.2 4.000PEG 600 0.05 1.000Polyol 0.3 7.508Polyisocynate 0.2 5.005Surfactant 0.05 1.251Water 0.45 11.261Gum Rosin 0.200 41.667Maleic Anhydride 0.063 13.083Fumeric acid 0.063 13.083Caustic Flakes 0.059 12.292Water 0.613 127.708Gum Rosin 0.262 10.972Maleic Anhydride 0.019 0.812Casien 0.023 0.980Tri Ethanol Amine 0.003 0.109Formaldehyde 0.001 0.025Pottasium Hydroxide 0.004 0.159Water 0.688 28.819Fatty Acids like Stearic acid or Palmitic Acid 0.233 13.660Mineral Oils 0.148 8.677Catalyst 0.019 1.085Lithium Hydroxide 0.520 30.486Borax 0.081 4.719

28

21

19

20

27

26

24

25

23

22

Grease

Neutralizing Chemicals

Binders & Other Polymers

Sizing Chemicals

Polyurathene

Organopoly Siloxane

Blocked Polyeste

Softner-2

Softner-1

Eia1

Text Box

Annexure- 3 Corrigendum order

Annexure:3-Plot allotment certificate old

Annexure:3-Plot allotment certificate

Annexure- 4 List of Equipments

Sr No Description Capacity /

Specs Requirement

Qty

Machinery Qty

Phase 1 Phase 2

A Plant & Machinery

1 Fermenter 15 KL 2 0 2

2 Seed Vessels 1000 Ltr 2 0 2

3 Lab Seed Fermenter 50L / 100L 1 0 1

4 Media Preparation tank 10000 Ltr 1 0 1

5 Dosing Tanks 3500 Ltr 1 0 1

6 Harvester Tank 15000 Ltr 1 0 1

7 Fitter Press 3 KL/Hour 1 0 1

8 Collection Tank 10000 Ltr 2 0 2

9 Micro Filter 1000 Ltr 1 0 1

10 Sterile Tanks 1000 Ltr 1 0 1

11 Spray Drier 50 litres/min 1 0 1

12 Cold Storage 15000 MT 1 0 1

13 Air Compressor 300 cfm 2 1 1

14 Chiller 200 TR 1 0 1

15 Cooling Tower 300 TR 1 0 1

16 Chilling Tank 1 0 1

17 DG-1 165 KVA 1 1 0

18 DG-2 500 KVA 1 0 1

19 Raw Water Tank 300000 1 1 0

20 Soft Water Plant 5000 1 0 1

21 Effluent Plant 050 M³ 1 1 0

22 Effluent Plant 130 M³ 1 0 1

23 Evaporation Plant 5000 l/hr 1 0 1

24 Drying Plant 500 l/hr 1 0 1

25 Ultra Filtration 1500 l/hr 1 0 1

26 Feed pump/Pressure pumps 0 1 0 1

27 Boiler 2 Tons 2 Tons/Hour 1 1 0

28 Boiler 6 Tons 6 Tons/Hour 1 0 1

29 Octagonal Blender 3000/1250

Ltr 2 1 1

30 Rapid Mixer Granulator 800/350 Ltr 2 1 1

31 Lifting Devices 1000 Kg 2 1 1

32 Sifters 30” Dia 6 2 4

33 IPC Container & Acessories NA 6 0 6

34 AHU System NA 8 0 8

35 DM Water System NA 1 0 1

36 Tray Dryer 300 Kg 1 0 1

37 Separator 1500 Ltr/Hr 1 0 1

38 Nutch Filter 1000 Ltr 1 0 1

39 Lyophilizer / Freeze Dryer 800 Ltr 1 0 1

40 Automatic Powder Filling Machine 3000 Kg/Hr 1 0 1

41 Automatic Liquid Filling Machine 5000 Ltr/Hr 1 0 1

42 Mixing Vessels & Tanks 5000 Ltr 3 0 3

43 Hydraulic Devices 3000 Kg 2 0 2

44 Tray Filling Station 1-5 Kg 1 0 1

45 Pulverizer 1 0 1

46 Steam Generator 300 Kg/Hr 1 0 1

47 SS Reactor 20 KL 2 0 2






53 MS Reactor 20 KL 2 0 2





58 FRP Blender 16 KL 4 1 3





63 Forberg Mixer 01 MT 3 1 2

64 Ribbon Blender 03 MT 3 1 2

65 Micromotion Mass Flow Meter Nos 6 1 5

66 Flaker Machine Nos 1 0 1

67 Cold Room 10º C -15º C 1 0 1

68 MS Storage Tank 25 KL 8 2 6



71 FRP Storage Tank 25 KL 3 3 0




75 Small FRP & Sintex Vessel

0.5 KL & 1 KL 10 5 5

76 Thermopac 500000 Kcal/ Hr 1 0 1

77

Automatic Blending and Packing Plant with Silo System 1 0 1

78 SS Storage Tank 25 KL 7 0 7

79

Automatic Filling, Packing, Labeling Machine 2 0 2

80

Automation System for Reactor with Load Cell & PLC 15 2 13

81

SS 316 Reactor for EO/PO based products with accessories and automation. 05KL 3 0 3

82

Storage Tank for Ethylene Oxide with all necessary arrangements, pipe lines etc 07 KL 7 0 7

B Miscellaneous

1 Automation& Spares

2 Electrification &Installation

3 Storage Racks

4 Pump House 1 1 0

5 Transformer & Pole 2 1 0

6 Forklifts/ Stackers 6 2 4

C Pilot Plant and R&D Lab

1 Fermenter 500/100lit/30

lit 3 0 3

2 Shake Flark 20 lir 2 0 2

3 Filter Press 500 Ltr/hr 1 0 1

4 UF 200 Ltr/hr 1 0 1

5 Micro Filtration 1 0 1

6 Lab Spray drier 1 0 1

7 Gel Electrophoresis 1 0 1

8 HPL/TCL 1 0 1

9 BIO 1 0 1

10 Spectro Photometer 1 0 1

11 Miscellaneous Lab Equipment 1 0 1

12 AHN/FDV 1 0 1

13 Dehumidifier 1 0 1

14 Lab equipment - GLP 1 0 1

D Office Equipment & Furniture 1 0 1

E IT 1 1 0

Annexure-5 Minutes of Meeting

Annexure-6 Consent letter GIDC

Annexure :7 Power of Attorney

Annexure :

Annexure :7

Page | I

FORM 1

(I) Basic Information

S.No. Item Details

1. Name of the project/s Manufacturing of Synthetic Organic Chemicals by

M/s. Rossari Biotech Ltd.

(Amendment in TORs for:

1. Change in Plot no in TORs letter.

2. Change in product list and its quantities.

3. Change in water requirement and water balance

diagram.

4. Discharge of ETP treated effluent into CETP.

5. Extension in validity of TORs.)

2. S. No. in the schedule 5(f) – Synthetic Organic Chemical

3. Proposed capacity /area /

length/tonnage to be

handled/command area/

lease area/number of wells to

be drilled

(Amendment in TORs) Please refer pg no. 3, Table

2.1 of Chapter 2 of pre-feasibility report for proposed

production capacity.

4. New / Expansion /

Modernization

New Project (Amendment in TORs)

5. Existing Capacity/ Area etc. --

6. Category of Project i.e. ‘A’ or

‘B’

Category “B” Project (Amendment in TORs)

7. Does it attract the general

condition? If yes, please

specify.

No

8. Does it attract the specific

condition? If yes, please

specify

No

9. Location

Plot/Survey/Khasra No. D-3/24/3, Dahej-III Industrial Estate

Village Galenda Village

Tehsil Vagara Taluka

District Bharuch District

State Gujarat State

10. Nearest railway station/

airport along with distance in

kms.

Bharuch Railway Station ≈ 35.87 km (SEE)

Surat Airport ≈ 68 km (SSE)

11. Nearest Town, City, District

headquarters along with

distance in kms.

Dahej ~ 9.50 km

Page | II

S.No. Item Details

12. Village Panchayats, Zilla

Parishad, Municipal

Corporation, Local body

(complete postal addresses

with telephone nos. to be

given)

District Panchayat, Bharuch.

Phone No. (02792)222313 :

Fax No. (02792)222378 :

13. Name of the applicant Shri Prasad Prabhakar Gadkari

14. Registered address M/s. Rossari Biotech Ltd.

201-A & B, Ackruti Corporate Park,

LBS Marg, Next to GE Gardens,

Kanjurmarg(W),

Mumbai-400 078. 15. Address for correspondence: M/s. Rossari Biotech Ltd

Plot No10 & 11, Survey No.90/1/10 & 90/1/11/1

Old Surya Global Compound,

Kumbharwadi,Village Naroli

Dadra & Nagar Haveli-396235. Name Shri Prasad Prabhakar Gadkari

Designation (Owner/ Partner/

CEO)

General Manager

Address M/s. Rossari Biotech Ltd

Plot No10 & 11, Survey No.90/1/10 & 90/1/11/1

Old Surya Global Compound,

Kumbharwadi,Village Naroli

Dadra & Nagar Haveli-396235. Pin Code 396235

E-mail [email protected]

Telephone No. +919979874629 / +91- 0260 - 6693000 / 6693004 /

Fax No. +91-0260-2651376

16. Details of Alternative Sites

examined, if any. Location of

these sites should be shown

on a topo sheet.

Silvassa, Nasik and Vadodara were the alternative

sites considered for the project. Dahej is selected due

to the reasons provided in Project pre-feasibility report-

Section 3.2.

17. Interlinked Projects No

18. Whether separate application

of interlinked project has

been submitted?

Not Applicable

19. If yes, date of submission Not applicable

20. If no, reason Not applicable

Page | III

S.No. Item Details

21. Whether the proposal

involves approval/ clearance

under: if yes, details of the

same and their status to be

give.

(a) The Forest

(Conservation) Act,

1980?

(b) The Wildlife (Protection)

Act, 1972?

(c) The CRZ Notification,

1991?

No (Project site lies within the Industrial Estate, Dahej-

III Industrial Estate, Taluka Vagara, Bharuch.)

22. Whether there is any

Government Order/Policy

relevant/ relevant to the site?

The Gujarat Petroleum Chemical & Petrochemical

Special Investment Region declared under Gujarat

Special Investment Region Act, 2009.

23. Forest land involved

(hectares)

No.

24. Whether there is any

litigation pending against the

project and/or land in which

the project is proposed to be

set up?

(a) Name of the court

(b) Case No.

(c) Orders/ direction of the

court, if any and its

relevance with the

proposed project.

No

(II) Activity

1. Construction, operation or decommissioning of the Project involving actions,

which will cause physical changes in the locality (topography, land use, changes in

water bodies, etc.)

S. No. Information/Checklist

confirmation

Yes

/No

Details thereof (with approximate

quantities / rates, wherever

possible) with source of

Information data

1.1 Permanent or temporary change in

land use, land cover or topography

including increase in intensity of

land use (with respect to local land

use plan)

No

Open Land designated for industrial

use is proposed for the project. Please

refer the layout attached as Figure

3.4 of Project Prefeasibility Report at

page no. 16.

1.2 Clearance of existing land,

vegetation and buildings?

No --

Page | IV


confirmation

Yes

/No




Information data

1.3 Creation of new land uses? No --

1.4 Pre-construction investigations

e.g. bore houses, soil testing?

No Not carried out

1.5 Construction works? Yes (Amendment in TORs) Construction

for proposed project will include plant

area, storage area, ETP,

administrative building, laboratory, etc.

Please refer Figure 3.4 of Project

Prefeasibility Report at page no. 16.

1.6 Demolition works? No Not Applicable

1.7 Temporary sites used for

construction works or housing of

construction workers?

No Not Applicable

1.8 Above ground buildings, structures

or earthworks including linear

structures, cut and fill or

excavations

Yes Construction of building for proposed

project will include excavations for

foundation.

1.9 Underground works including

mining or tunneling?

No Not Applicable

1.10 Reclamation works? No Not Applicable

1.11 Dredging? No Not Applicable

1.12 Offshore structures? No Not Applicable

1.13 Production and manufacturing

processes?

Yes (Amendment in TORs) Please refer

Annexure 1 of Project Pre-Feasibility

report.

1.14 Facilities for storage of goods or

materials?

Yes (Amendment in TORs) All raw

materials will be received in tankers/

trucks and unloaded through fixed line

and pumps, into the designated

storage tanks/ drums & bags stored in

their designated storage area.

MS/SS/PPFRP/PPFRV/HDPE tank

will be provided for solvents storage.

Please refer Chapter-3, section

3.5.1, table no. 3.2 at page no.18.

1.15 Facilities for treatment or disposal

of solid waste or liquid effluent?


Chapter-3, section 3.7.5, table no.

3.10 at page no. 36.

1.16 Facilities for long term housing of

operational workers?

No Local personnel will be employed as

workers.

1.17 New road, rail or sea traffic during

construction or operation?

No Not Applicable

Page | V


confirmation

Yes

/No




Information data

1.18 New road, rail, air waterborne or

other transport infrastructure

including new or altered routes

and stations, ports, airports, etc.?

No Not Applicable since good road

infrastructure of Industrial Estate is

already available.

1.19 Closure or diversion of existing

transport routes or infrastructure

leading to changes in traffic

movements?

No Not Applicable

1.20 New or diverted transmission lines

or pipelines?

No Not Applicable

1.21 Impoundment, damming,

culverting, realignment or other

changes to the hydrology of

watercourses or aquifers?

No Not Applicable

1.22 Stream crossings? No Not Applicable

1.23 Abstraction or transfers of water

from ground or surface waters?

Yes (Amendment in TORs) GIDC’s piped

water supply shall fulfill site’s water

requirements.

1.24 Changes in water bodies or the

land surface affecting drainage or

run-off?

No GIDC will lay an underground drainage

line for conveyance of treated effluent

to the Common Effluent Treatment

Plant for further treatment & disposal.

1.25 Transport of personnel or

materials for construction,

operation or decommissioning?

No We shall hire personnel from local/

nearby area. The sources of raw

materials and machinery for

operations will vary based on market

driven forces which will be transported

via roads.

1.26 Long-term dismantling or

decommissioning or restoration

works?

No Not Applicable

1.27 Ongoing activity during

decommissioning which could

have an impact on the

environment?

No Not applicable

1.28 Influx of people to an area in either

temporarily or permanently?

No Not applicable

1.29 Introduction of alien species? No Not applicable

1.30 Loss of native species or genetic

diversity?

No Not applicable

1.31 Any other action? No None

Page | VI

2. Use of Natural resources for construction or operation of the Project (such as land,

water, materials or energy, especially any resources which are non-renewable or in

short supply) :

S.No. Information/ Checklist

confirmation

Yes/

No


quantities / rates, wherever possible)

with source of Information data

2.1 Land especially undeveloped or

agricultural land (ha)

No (Amendment in TORs) Not Applicable,

since the project plot is situated within the

notified GIDC, Dahej-III Industrial Estate,

Taluka Vagara, Bharuch.

2.2 Water (expected source &

competing users) unit : KLD

Yes (Amendment in TORs) About 225 kl/day

for Phase 1 and 398 kl/day after Phase 2

will be the anticipated fresh water

requirement. Water Source shall be piped

water supplied by GIDC, which is

specifically meant for industrial usage for

the occupiers within the notified GIDC.

Hence, there are no competing users.

2.3 Minerals (MT) No Not Applicable

2.4 Construction material – stone,

aggregates, and / soil (expected

source – MT)

Yes Cement, Sand, Gravel, Aggregate for

proposed project construction from local

supplier.

2.5 Forests and timber (source – MT) No Not applicable

2.6 Energy including electricity and

fuels (source, competing users)

Unit : fuel (MT), energy (MW)


Project Pre-Feasibility Report– Section

No. 3.6.3 at page no.: 24.

2.7 Any other natural resources (use

appropriate standard units)

No Not applicable

Page | VII

3. Use storage, transport, handling or production of substances or materials, which could

be harmful to human health or the environment or raise concerns about actual or

perceived risks to human health.

S.No. Information/Checklist

confirmation

Yes/

No



possible) with source of Information

data

3.1 Use of substances or materials,

which are hazardous (as per MSIHC

rules) to human health or the

environment (flora, fauna and water

supplies)

Yes Please refer section 3.5.1 of pre-

feasibility report for details of

hazardous chemicals.

3.2 Changes in occurrence of disease or

affect disease vectors (e.g. insect or

water borne diseases)

No Not applicable

3.3 Affect the welfare of people e.g. by

changing living conditions?

Yes Employment opportunities would be

created due to the project, which shall

improve the welfare and living

conditions of the employed personnel.

3.4 Vulnerable groups of people who

could be affected by the project e.g.

hospital patients, children, the

elderly

No The project is proposed in a notified

industrial estate

3.5 Any other causes No Not applicable

Page | VIII

4. Production of solid waste during construction or operation or decommissioning

(MT/Month)


confirmation

Yes/

No




4.1 Spoil, overburden or mine wastes No Not applicable

4.2 Municipal waste (domestic and or

commercial wastes)

Yes The commercial waste generated from

administration building would be

disposed through sale to scrap vendors.

4.3 Hazardous wastes (as per

Hazardous Waste Management

Rules)


Project Pre Feasibility Report. Section

3.7.5, Table no. 3.10 page no. – 36.

4.4 Other industrial process wastes Yes Same as above

4.5 Surplus product No Not applicable

4.6 Sewage sludge or other sludge

from effluent treatment

Yes (Amendment in TORs) ETP waste-

Phase-1 15.00 TPM & After Phase-2

43.00 TPM will be sent to the TSDF site.

4.7 Construction or demolition wastes No Not applicable

4.8 Redundant machinery or

equipment

No Not applicable

4.9 Contaminated soils or other

materials.

No Not applicable

4.10 Agricultural wastes No Not applicable

4.11 Other solid wastes Yes (Amendment in TORs) Discarded

containers (Bags/Drums) after proper

decontamination will be sold to the

authorized scrap dealer

Page | IX

5. Release of pollutants or any hazardous, toxic or noxious substances to air (Kg/hr)

S.No. Information/Checklist confirmation Yes/

No



possible) with source of Information

data

5.1 Emissions from combustion of fossil

fuels from stationary or mobile

sources


Project Pre-Feasibility Report. Section

3.7.4.2, Table no. 3.9, page no. - 34.

5.2 Emissions from production processes Yes (Amendment in TORs) Please refer


3.7.4.1, Table no. 3.8, page no. - 34.

5.3 Emissions from materials handling

including storage or transport



3.7.4.3, Page No. - 35.

5.4 Emissions from construction activities

including plant and equipment

No Not applicable

5.5 Dust or odours from handling of

materials including construction

materials, sewage and waste

Yes (Amendment in TORs) There is

generation of odour from fermentation

products. Appropriate mitigation

equipments have been considered as

deemed necessary

5.6 Emissions from incineration of waste No Not applicable

5.7 Emissions from burning of waste in

open air (e.g. slash materials,

construction debris)

No Not applicable

5.8 Emissions from any other sources No Not applicable

Page | X

6. Generation of Noise and Vibration, and Emissions of Light and Heat :


confirmation

Yes/

No

Details thereof (with approximate quantities /

rates, wherever possible) with source of

Information data

6.1 From operation of

equipment e.g. engines,

ventilation plant, crushers

Yes (Amendment in TORs) Please refer Project Pre-

Feasibility Report. Chapter 3, Section 3.7.6 at

page no. - 36.

6.2 From industrial or similar

processes

Yes Same as above.

6.3 From construction or

demolition

No Not applicable

6.4 From blasting or piling No Not Applicable.

6.5 From construction or

operational traffic

No Not Applicable.

6.6 From lighting or cooling

systems

No Not Applicable.

6.7 From any other sources No Not Applicable.

Page | XI

7. Risks of contamination of land or water from release of pollutants into the ground or

into sewers, surface water, ground water, coastal water or the sea :


confirmation

Yes/N

o




7.1 From handling, storage, use or

spillage of hazardous materials

Yes

(Amendment in TORs) However, the

hazardous Materials (i.e. hazardous

chemical and hazardous wastes) would

be handled as per the Guidelines

prescribed by Central Pollution Control

Board (CPCB) and MoEF.

Please refer section 3.5.1, Table no 3.2,

at page nos. 18 of the pre-feasibility

report.

7.2 From discharge of sewage or

other effluent to water or the

land (expected mode and place

of discharge)

Yes (Amendment in TORs) However, the

generated industrial wastewater will be

treated in ETP & treated effluent will be

discharged to CETP through underground

drainage as per GPCB norms. Domestic

waste water will be sent to soak pit/septic

tank. Also Please refer Project Pre-

Feasibility Report. Section 3.7.3, page

no. – 29.

7.3 By deposition of pollutants

emitted to air into the land or into

water

No No risk of contamination of land or water

from release of pollutants since Natural

Gas, a cleaner fuel has been proposed.

7.4 From any other sources No Not Applicable.

7.5 Is there a risk of long term build

up of pollutants in the

environment from these

sources?

No Not anticipated

Page | XII

8. Risk of accidents during construction or operation of the Project, which could affect

human health or the environment

S.

No.

Information/Checklist

confirmation

Yes/

No




8.1 From explosions, spillages, fire, etc.

from storage, handling, use or

production of hazardous substances

Yes (Amendment in TORs) Precautions

would be taken to alleviate such risks,

as detailed in Project Pre-feasibility

Report. Section – 3.7.7 at Page No. –

37.

8.2 From any other causes No Not Applicable.

8.3 Could the project be affected by

natural disasters causing

environmental damage (e.g. floods,

earthquakes, landslides, cloudburst

etc.)?

Yes However, the project is located in

Seismic zone III, which is a moderate

zone.

Page | XIII

9. Factors which should be considered (such as consequential development) which could

lead to environmental effects or the potential for cumulative impacts with other

existing or planned activities in the locality?

S.

No. Information/Checklist confirmation

Yes/

No

Details thereof (with

approximate quantities / rates,

wherever possible) with

source of Information data

9.1 Lead to development of supporting cities,

ancillary development or development

stimulated by the project which could have

impact on the environment e.g. :

Supporting infrastructure (roads,

power, supply, waste or waste water

treatment, etc.)

Housing development

Extractive industries

Supply industries

Others

No Not Applicable.

9.2 Lead to after-use of the site, which could

have impact on the environment

No Not Applicable.

9.3 Set a precedent for later developments No Not Applicable.

9.4 Have cumulative effects due to proximity

to other existing or planned projects with

similar effects

No Not Applicable.

Page | XIV

(III) Environmental Sensitivity

S.No. Areas Name/

Identity

Aerial distance (within

15 km.) Proposed

project location

boundary

1 Areas protected under international

conventions, national or local legislation

for their ecological, landscape, cultural or

other related value

No Not applicable

2. Areas which are imported or sensitive for

ecological reasons – Wetlands,

watercourses or other water bodies,

coastal zone, biospheres, mountains,

forests

Yes Narmada River ≈ 5.7 km

(S)

Gulf of Khambhat ≈ 12.71

km (SSW)

3 Areas used by protected, important or

sensitive species of flora or fauna for

breeding, nesting, foraging, resting, over

wintering, migration

No Not applicable

4. Inland, coastal, marine or underground

water


(S)

5. State, National boundaries No Not applicable

6. Routes or facilities used by the public for

access to recreation or other tourist,

pilgrim areas

No Not applicable

7. Defense installations No --

8. Densely populated or built-up area Yes Site is located inside the

Industrial Estate of Dahej,

Bharuch.

9. Areas occupied by sensitive man-made

land uses (hospitals, schools, places of

worship, community facilities)

No --

10. Areas containing important, high quality

or scarce resources

(ground water resources, surface

resources, forestry, agriculture, fisheries,

tourism, minerals)


(S)

11 Areas already subjected to pollution or

environmental damage. (those where

existing legal environmental standards

are exceeded)

No Ankleshwar GIDC which is

declared as a critically

polluted area is at an aerial

distance of 39.33 km (SE)

of the project site.

12 Areas susceptible to natural hazard

which could cause the project to present

environmental problems

(earthquakes, subsidence, landslides,

erosion, flooding or extreme or adverse

climatic conditions)

Seismic

Zone-III

(Moderate)

-

PROJECT PRE-FEASIBILITY REPORT - Environmental ...

Documents

Transcript of PROJECT PRE-FEASIBILITY REPORT - Environmental ...