Under Activity: 5(f), Category: B (Synthetic Organic ... · Planning Concept (Type of industries,...

ON

THE PROPOSED EXPANSION PROJECT (BY ADDITION OF NEW PRODUCTS)

(Manufacturing of Synthetic Organic Chemicals)

Under Activity: 5(f), Category: B

(Synthetic Organic Chemical Manufacturing Industry)

Of

Located at:

Plot no. 2702, 2901, 2701-2703, 2608, 731/A

GIDC, Sarigam – 396155 Tal. Umbergaon, Dist. Valsad. Gujarat (INDIA).

Prefeasibility Report M/s. Alchemie Industries

INDEX

1. Executive Summary……………………………………………………………………………………….……………………. 01

2. Introduction……………………………………………………………………………………..………….……………………. 03 i. Identification of the Project and Proponent. 03

ii. Brief Description of the project 03

iii. Need of the project and its importance to the country and or region 04

iv. Demand –Supply Gap.: 04

v. Imports vs. Indigenous production 04

vi. Export Possibility / Domestic / export Markets 04

vii. Employment Generation (Direct and Indirect) due to the project. 04

3. Project Description…………………………………………………………………………………………………………..… 05 i. Type of Project including interlinked and interdependent projects, If any 05

ii. Location (map showing general location, Specific location, and project boundary & project site layout)with coordinates

05

iii. Profile of Project site 06

iv. Site Layout Plan 07

v. Details of alternate sites considered and the basis of selecting the proposed site, particularly the environmental considerations gone into should be highlighted

10

vi. Size or magnitude of operation 10

vii. Project description with process details (a schematic diagram/ flow chart showing the project layout components of the project etc. should be given)

10

viii. Resource optimization/ recycling and reuse envisaged in the project, 32

ix. Availability of water its source, Energy/power requirement and source 32 x. Schematic representations of the feasibility drawing which give information of EIA

purpose 32

4. Site Analyses………………………………………………………………………………………………………………………. 39 i. Connectivity 39

ii. Land Form, land Use and Land Ownership 39

iii. Existing Infrastructure/ land use pattern 39

iv. Soil Classification and Land Use Classification 39

v. Climate Data from secondary source 39

vi. Social Infrastructure 39

5. Planning Description………………………………………………………………………………………………………….… 40 i. Planning Concept (Type of industries, facilities, transportation etc) 40

ii. Population Projection 40

iii. Land use planning (breakup along with green belt etc 40

iv. Assessment of Infrastructure demand ( Physical & Social) 40

v. Amenities/ Facilities 40

6. Proposed Infrastructure …………………………………………………………………………………………………….. 41 i. Industrial Area (Processing Area) 41 ii. Residential Area (Non Processing Area). 41

Proposed Expansion Project i Manufacturing: Synthetic Organic Chemicals


iii. Green belt 41 iv. Connectivity 41 v. Drinking Water management (Source& Supply of water) 41 vi. Sewerage System 41 vii. Industrial Waste Management 41

7. Rehabilitation and Resettlement (R&R) Plan…………………………………………………………………....... 41

i. Policy to be adopted (central/state) in respect of the project affected persons including home oustees, land oustees and landless laborers

41

8. Project Schedule & Cost Estimates…………………………………………………………………….................... 41

i. Likely date of start of construction and likely date of completion 41

ii. Estimated project cost along with analysis in terms of economic viability of the project 41

9. Analysis of Proposal (Final Recommendations…………………………………………………..................... 42 i. Financial and social benefits with special emphasis on the befit to the local people

including tribal population, if any, in the area 42

Proposed Expansion Project ii Manufacturing: Synthetic Organic Chemicals


1. EXECUTIVE SUMMARY 1.0 About project M/s. Alchemie Industries is an existing Company having its unit located at plot no. 2702,2901,2701-

2703,2608,731/A, GIDC, Sarigam, Tal. Umargam, Dist.-Valsad, Gujarat-396155 engaged in manufacturing

of Dyes intermediates and Chemicals in existing unit @ 2640 MT/Year and now is proposing for the

expansion of its unit by addition OF organic chemicals the existing premises.

2.0 Highlights of the project Sr. No.

Particulates Description

1. Project Location Plot no. 2702, 2901, 2701-2703, 2608, 731/A, GIDC, Sarigam, Tal. Umargam, Dist.-Valsad, Gujarat-396155

2. Project Activity, Category as per amendments

Project Activity:-5(f)- Synthetic Organic Chemicals, Category:-B

3. Project Cost 1106.17 lakhs

4. Total area of Project 14519.60 Sq.mt.

5. Products with capacity

Product details Existing: Dyes intermediates and Chemicals: 220.00MT / Month Total after proposed : Dyes intermediates and Chemicals: 1510.00 MT/Month By Product details Existing: 260.00 MT / Month Total after proposed : 938.00 MT/Month

6. Power Requirement 875 KVA (Existing 600 KVA + Proposed 275 KVA)

7. Utilities (D.G. Sets, Boilers, Thermopack etc...)

D.G. Set 1000KVA (Capacity: Existing: 750KVA + Proposed 250 KVA) Boiler : 5 TPH (Existing: 1.5 TPH + Proposed 3.5 TPH)

8. Fuel Requirements Diesel : 185 lits/hr(Existing: 100 lits/hr + proposed: 85 lits/hr )

9. Man Power 75 persons(Existing: 50 + proposed: 25 ) 10. Air pollution Control Measures Two Stage Acid –Alkali scrubber

11. Water requirement & waste water generation with mode of disposal

Water Consumption: 172.7 KL/day Domestic - 10 KL/Day (Existing: 5 KL/Day + proposed: 5 KL/Day), Industrial- 79.7 KL/Day (Existing: 53 KL/Day + proposed: 26.70KL/Day) Waste water generation: Domestic waste water – 7 KL/Day (Existing: 4 KL/Day + proposed: 3 KL/Day) 4.00 KL/day will be disposed through adequate soak pit and septic tank and 3 KL/Day mix with industrial waste water treated

Proposed Expansion Project 1 Manufacturing: Synthetic Organic Chemicals


in adequate ETP. Industrial waste water : 90.60 KL/Day (Existing: 57.4 KL/Day + proposed: 33.2 KL/Day) 42.4 KL/day will be treated in adequate Multiple Effect Evaporator with stripper and 48.2 KL/Day will be treated using adequate ETP then will be disposed off through underground drainage to CETP, Sarigam.

12. Solid / Hazardous waste Generation Will be managed as per Hazardous Waste (Management, Handling and Transboundary Movement) Rules-2008. [

13. Nearest Highway NH-8: 5.00 (Approx.)

14. Nearest Railway Station Bhilad- 4.90 (Approx.)

15. Nearest Airport Daman 16 Km NW (Approx.) Surat 90 Km N (Approx.)

16. Nearest Forest/ Sanctuary/Eco-sensitive zone.

None



2. INTRODUCTION (i) Identification of Project and proponent.

Name of the project Proponent: M/s. Alchemie Industries.

M/s. Alchemie Industries is an existing Company having its unit located at plot no. 2702,2901,2701-

2703,2608,731/A, GIDC, Sarigam, Tal. Umargam, Dist.-Valsad, Gujarat-396155 engaged in manufacturing of Dyes

intermediates and chemicals in existing unit @ 2640 MT/Year and now is proposing for the expansion of its unit

by addition Of organic chemicals the existing premises.

Alchemie industries is a chemical industries manufacturing dyes intermediates namely known as Fast Red b

base/ Fast Bordeaux Gp base, Ortho/ para nitro anisole. This unit was formed in the year 1987 and is located at

Sarigam industrial estate GIDC, Sarigam Total 50 employees skilled and unskilled work force are working in this

company. Total Turnover of the unit is around 60 crores per annum. Basically the end uses of the company

products application are for the manufacturing dyes and pigments.

The company is a Private Limited Company incorporate by the five Directors. Details related to them are given below:

Sr. No. Name of Director Residential Address Background

1. MANSUKH PREMJI GALA B-904, ADITYA TOWER, CHANDAVARKAR ROAD, BORIVALI (WEST), MUMBAI - 400092

PARTNER

2 HETAL GOGRI GALA 801, GOPAL SADAN, PLOT NO.552-B,JAME JAMSHED ROAD, MATUNGA (E) MUMBAI-400019

PARTNER

3 NIKHIL HOLDINGS PRIVATE LIMITED

A-1403-RUNWAL HEIGHTS, OPP. NIRMAL LIFESTYLE, LBS MARG, MULUND (WEST), MUMBAI - 400080.

PARTNER

4 MAHESH P. VIKAM

1001, WIMBELDON PARK, BUILDING NO.7, NEAR CADBURYS, VARTAK NAGAR, THANE - MAHARASHTRA - THANE - 400606.

PARTNER

5 MIRIK RAJENDRA GOGRI 1401, ANTRIKSHA, MURAR ROAD, MULUND WEST, MUMBAI - 400080

PARTNER

6 CHANDRAKANT VALLABHAJI GOGRI

601, ANTRIKSHA, MURAR ROAD, MULUND WEST, MUMBAI - 400080.

PARTNER

7 AARTI RAJENDRA GOGRI 1401, ANTRIKSHA, MURAR ROAD, MULUND WEST, MUMBAI - 400080.

PARTNER



(ii) Brief description of nature of the Project M/s. Alchemie Industries Proposes to establish their product manufacturing unit at plot no. 2702,2901,2701-2703,2608,731/A, GIDC, Sarigam, Tal. Umargam, Dist.-Valsad, Gujarat-396155

The proposed Expansion project involves the production of ortho and para nitro anisole, 2 5 di nitro anisole , with the base products fast red b base and fast Bordeaux gp base, 3 nitro para toludiene and sulphonation product ONCBPSA like Dyes intermediates and chemicals, which are Synthetic Organic Chemicals, for the proposed project, the company intends to procure the available latest technology for manufacturing the proposed products.

The industrial sector in the past years has seen a drastic boom and also the keeping in mind the globalization trend, we have identified the demand for the proposed products and with continuous R & D found that it can be developed in-house and produce commercially for domestic market as well as an eye more on export markets.

As per the EIA notification- 2006 as amended the proposed new project involves the production of Dyes intermediates and chemicals, which falls under item no. “5(f) – Synthetics organic Chemicals industries” as per the EIA notification- 2006, hence required Prior Environmental Clearance.

(iii) Need for the project and its importance to the country and or region The proposed new expansion project will provide a potential growth opportunity for the company. We have identified the demand for the proposed products and it can be developed in-house and produce commercially for domestic market as well as an eye more on export markets. Its export and also increase the foreign revenue. The products are now well established and acceptable in the international markets.

(iv) Demand –Supply Gap The products have very high demand for manufacturing of Dyes and dye intermediates Industries.

(v) Imports vs. Indigenous production Proposed products manufacturing in the country will be very much economical compare to Imports of the same and also the export of the same will earn extra revenue generation for our country.

(vi) Export Possibility / Domestic / export Markets There is a huge demand of the proposed products in the export market. Our products are widely used

and are in demand in the domestic Chemical industry.

(vii) Employment Generation (Direct and Indirect) due to the project There will be very good opportunity of employment generation directly and indirectly due to

proposed new project. We anticipate employing up to 50 operators and 25 office staff.



3. PROJECT DISCRIPTION (i) Type of Project including interlinked and interdependent projects, If any :

The proposed expansion project is not interlinked and interdependent project of the company.

(ii) Location (map showing general location, Specific location, and project boundary & project site layout) with coordinates:

The map showing general location, specific location and project boundary and project site layout of M/s. Alchemie Industries located at plot no. 2702, 2901, 2701-2703, 2608, 731/A, GIDC, Sarigam, Tal. Umargam, Dist.-Valsad, Gujarat-396155. The latitude and longitude of the project site is 20.303067°N and 72.851107°E.

Fig. 3.1: Location map showing the Project site within the GIDC Sarigam



(iii) Profile of Project Site:

Sr. No. Nearest Infrastructure Feature Distance from Project Site

1. Geographical Position Lat.: 20.306529° °N, Long.: 72.854118° °E

2. Elevation above Sea Level 36 Meters (Approx.)

3. Nearest Village Sarigam (2.05 km SE)

4. Nearest Town Sarigam (2.05 km SE)

5. Nearest National Highway NH 8 (5.00 Km E)

6. Nearest State Highway GJ SH 5 (0.60 Km SE)

7. Nearer RW Station Bhilad (4.90 km S)

8. Nearest Airport Daman (16 Kms NW) Surat (90 Km N)

9. Nearest Surface water Resource/Reservoir

Arabian Sea (14 Km W) Darotha River (3.18 Km NE)

10. Forest Patches --

11. Location of Archaeologically /Historically important places

--

12. National Park/Sanctuary or Ecologically sensitive Area

D & NH Wild Life Sanctuary Approx. 14 km E

13. National or State Boundary Dadra & Nagar Haveli – 8.00 Km E Daman – 7.00 km N

14. Tourist Places Dadra & Nagar Haveli – 9.50 Km E Daman – 21 km N

15. Selection of project Site and Detail of alternate Site.

Proposed project is in the GIDC Notified Industrial area having proper industrial infrastructure hence alternate site consideration is not envisaged.

16. Size or Magnitude of Operation Small scale

Plot site Area Statement:

Area Statement Area After Proposed Expansion (in m2)

Total Area 14519.60 Construction Area Factory Shed 5852.96 Open Land Area 1992.31 Greenbelt Area 6674.31



(iv) Site Layout Plan: 1. Key plan



2. Site plan -1



3. Site plan -2



(v) Details of alternate sites considered and the basis of selecting the proposed site, particularly the environmental considerations gone into should be highlighted : Land is acquired for the proposed expansion project in the GIDC Notified Industrial area having proper industrial infrastructure hence alternate site consideration is not envisaged.

(vi) Size or magnitude of operation: As per the proposed project cost the project is covered under Small Scale category of manufacturing industries, it comes under SSI.

(vii) Project description with process details (a schematic diagram/ flow chart showing the project layout components of the project etc. should be given):

Detailed project description with process details –

• LIST OF FINISHED PRODUCTS

Sr. No.

Products Name

Existing Production

Capacity (MT/M)

Proposed Production

Capacity (MT/M)

Total Production

Capacity (MT/M)

Group -A

1) Ortho Nitro Anisole &/OR 140 1060 1200

2) Para Nitro Anisole &/ OR 00 1200

3) 2,4 DI NITRO ANISOLE &/OR 00 1200

Group -B

1) 5 Nitro /4 Nitro Ortho Anisidine ( FAST RED B BASE / SCARLET R BASE ) &/OR

80 130 210

2) 2,5 DI CHLORO PARA NITRO ANISLINE ( 2,5 DCPNA ) &/OR

00 210

3) 3 Nitro Para Anisidine ( META NITRO PARA ANISIDINE ) &/OR

80 130

4) 3 NITRO PARA TOLUDIENE ( META NITRO PARA TOLUDIENE)

80 130

Group -C

1) ORTHO NITRO CHLOROBENZENE PARA SULPHONIC ACID ( ONCBPSA)

00 100 100

2) Ortho Anisidine &/OR Para Anisidine 140 -140 00

Total 220 1290 1510



Details of by products: Sr. No.

By Products Name Existing Production Capacity (MT/M)

Proposed Production Capacity (MT/M) Total Production

Capacity (MT/M)

1. Sodium acetate 85.00 113.00 198.00

2. Sodium sulphate 00.00 90.00 90.00

3. Crude ortho nitro phenol 10.00 90.00 100.00

4. Acetic acid 40.00 50.00 90.00

5. Sodium chloride 120.00 340.00 460.00

6. Spent caustic soda lye 05.00 0.00 0.00

Total 260.00 683.00 938.00

• INFRASTRUCTURE, MACHINERIES, EQUIPMENT & TECHNOLOGIES Installation of the plants and machineries and latest technology will be required to manufacturing the

products. To get the best results in terms of quality and quantity, the company will invests in the latest available

plant and machinery and leverages state-of-the-art technologies to get excellent results.

• MANUFACTURING PROCESS

Product A-1 Ortho Nitro Anisole OR Process Description: Caustic methanol solution is prepared in a reactor with approximate strength of caustic methanol solution is 15 % wt/vol. In autoclave ONCB/PNCB is charged. Also methanol is charged by indirect vacuum to obtain ONCB/PNCB solution in Methanol. Autoclave is then heated up to 78 oC. Then CM solution of 15 % strength is gradually charged over a Period of 30 hrs. During feeding temperature and pressure are controlled. After feeding CM solution the batch is maintained at 85 oC. and corresponding pressure to obtained desired set point. Ortho Nitro Anisole/ Para Nitro Anisole is cooled to room temp. and the contents are transferred to methanol recovery reboiler, where excess methanol is recovered. After recovery of methanol the organic layer i.e. Ortho Nitro Anisole/ Para Nitro Anisole is washed with water till pH becomes neutral. It is then stored in a storage tank for dispatch.



• PROCESS FLOW DIAGRAM

• Chemical reaction:

Methanol Caustic Soda Mixing

ONCB/PNCB

Methoxylation Reaction

Methanol

Washing


ONA PNA



• Mass Balance Sr. No.

INPUT QTY (Kgs) OUTPUT QTY (Kgs) REMARK

1. ONCB 2700.00 ONA 2430.00 2. Rec. Methanol 3233.00 ONP 83.00 3. Fresh Methanol 615.00 Sodium Chloride 1003.00 4. Cautic Flakes 810.00 Recovered Methanol 3233.00 5. water 500.00 Methanol Loss 192.00 6. H2SO4 20.00 Salt For Disposal 72.00 Total 7878.00 Total 7878.00

Product A-2 PARA NITRO ANISOLE

• Manufacturing process.

Caustic methanol solution is prepared in a reactor with approximate strength of caustic methanol solution is 15 % wt/vol. In autoclave ONCB/PNCB is charged. Also methanol is charged by indirect vacuum to obtain ONCB/PNCB solution in Methanol.

Autoclave is then heated up to 78 oC. Then CM solution of 15 % strength is gradually charged over a Period of 30 hrs. During feeding temperature and pressure are controlled. After feeding CM solution the batch is maintained at 85 oC. and corresponding pressure to obtained desired set point.

Ortho Nitro Anisole/ Para Nitro Anisole is cooled to room temp. and the contents are transferred to methanol recovery reboiler, where excess methanol is recovered. After recovery of methanol the organic layer i.e. Ortho Nitro Anisole/ Para Nitro Anisole is washed with water till pH becomes neutral. It is then stored in a storage tank for dispatch.

• Process Flow diagram

Methanol Caustic Soda

Mixing

PNCB

Methanol Recovery

Methoxylation

Menthol

Methanol

Washing

PNA

Methanol Caustic Soda

Mixing

PNCB

Methanol Recovery

Methoxylation



• Chemical Reaction

• Mass Balance

Sr. No.


7. ONCB 2700.00 ONA 2430.00 8. Rec. Methanol 3233.00 ONP 83.00 9. Fresh Methanol 615.00 Sodium Chloride 1003.00 10. Cautic Flakes 810.00 Recovered Methanol 3233.00 11. water 500.00 Methanol Loss 192.00 12. H2SO4 20.00 Salt For Disposal 72.00 Total 7878.00 Total 7878.00

• Product A-3

2,4 DINITRO ANISOLE

• Manufacturing process. Caustic methanol solution is prepared in a reactor with approximate strength of caustic methanol solution is 15 % wt/vol. In autoclave 2,4 DNCB is charged. Also methanol is charged by pump to obtain 2, 4 DNCB solution in Methanol.

Autoclave is then heated up to 50 °C. Then CM solution of 15 % strength is gradually charged over a Period of 4 hrs. During feeding temperature at 50 to 55°C are controlled. After feeding CM solution the batch is maintained 3 hrs at 55 °C and obtained desired set point. Charge water in Autoclave and reaction mass Filter in Agitated Nutch Filter. Filter Mixture Methanol + water transferred to methanol recovery reboiler. And 2,4 DNA remove from Agitated filter and packed in a 50 kg gunny bags as per the user's requirement.





• Mass Balance

Sr. No.


1. 2,4DNCB 101.00 crude 2,4 DNA 97.00 2. Rec. Methanol 100.00 Sodium Chloride 20.00 3. Fresh Methanol 202.00 Recovered Methanol 272.00 4. Cautic Lye 48% 43.00 Methanol Loss 14.00 5. water 50.00 filter ML 31.00 6. Recycle water Total 496.00 Total 496.00

Methanol Caustic Soda Mixing

2, 4 DNCB Methanol

Filtration 2,4 DNA

Methanol Recovery


Methanol



• Product B-1 4/5 NITRO ORTHO ANISIDINE:

• Process description

Conversion of Ortho Anisidine to 5 Nitro Ortho Anisidine is carried out in four unit process namely Acetylation, Nitration, Hydrolysis & separation.

In Acetylation Ortho Anisidine is acetylation with Acetic acid + Acetic Anhydride to obtain acetylated Ortho Anisidine. Acetic acid is recovered after reaction completion. The Nitration of acetylated Ortho Anisidine is done with Nitric acid & Sodium Nitrite as catalyst. The nitro body thus obtained is hydrolyzed with caustic soda to get the hydrobody. Which contains Fast Red B Base & Fast scarlet R Base? This hydrobody is filtrate in neutech filter & caustic spent is taken out as a filtrate & filtrate is taken for further treatment. The separation hydrobody is done by addition of Sulphuric acid. Fast scarlet R Base which gets dissolved in Sulphuric acid is separated in filter. The residue i.e. Fast Red B Base is then dried, blended, pulverized and packed in drums and bags for dispatch. The filtrate is now neutralized with soda ash and filtered to get Fast scarlet R Base which is dried, blended, pulverized and packed in drums and bags for dispatch.

The caustic spent taken out from filter of hydrobody as a filtrate taken for neutralization. It is neutralized with recovered Acetic acid from acetylation. Then carbon treatment is given to this and then followed evaporation in another vessel. After completion of evaporation the liquid mass called as liquid sodium acetate can be despatchable or make cool and centrifuge it. This solid sodium acetate is also salable.



• Flow diagram

Liq. Sodium Acetate

Ortho Anisidine Acetic Anhydride Acetic acid

Acetylation

Nitric acid Sodium nitrite

Hydrolysis Caustic spent

Separation

Nitration

Drying

Recovered Acetic acid

Evaporation

Centrifuge

Neutralization

Sodium Acetate

Caustic soda

Sulphuric acid

Fast Red - B Base

Blending

Pulverizing

Packing

Filtrate

Neutralization

Drying

Blending

Pulverizing

Packing

Fast SCR - R Base

Soda Ash



• Chemical reaction

• Mass Balance

Sr. No. INPUT QTY (Kgs) OUTPUT QTY (Kgs) REMARK

1. Ortho Anisidine 1400.00 Red B Base 1512.00 2. Acetic Anhydride 1205.00 Scarlet R Base 257.00 3. Zinc 03.00 Sodium Acetate . 1608.00 4. Hydro 03.00 Recover MDC 1380.00 5. Methylene Di Chloride 270.00 Drying Loss 370.00 6. Rec. MDC 1380.00 MDC Loss 270.00 7. Nitric Acid 1200.00 Acetic Acid 727.00 8. Sodium Nitrate 02.00 ETP water 28509.00 9. Water 27900.00 10. Caustic Flakes 650.00 11. Sulphuric Acid 420.00 12. Soda Ash 200.00 Total 34633.00 Total 34633.00



Product B- 2 2, 5 DICHLORO PARA NITRO ANILINE:

• Process Description: Acetylation: 2, 5 Dichloro aniline is acetylated with acetic anhydride to get acetylated 2,5 DCA .The acetylated mass of 2,5 DCA thus generated is taken for next nitration process

Nitration: Nitration of acetylated 2,5 DCA is carried out in the mixed acid of sulphuric acid and dilute nitric acid and the reaction is carried out at low temperature. Complete the feeding of acetylated 2,5 DCA , the nitro mass is maintained for 3-4 hrs till the reaction TLC is found ok. The nitro mass is then dumped in a ice liquid to precipitate the nitro mass and is then filtered to a nutch filter. Filtrate of nitro mass is transferred to a neutralizer for neutralization.

HYDROLYSIS : Nitro mass cake is then de acetylated with caustic soda flakes to obtained 2,5 DICHLORO PARA NITRO ANILINE. Hydrolysed 2,5 dcpna is then filtered to a notch filter and the filter mother liquid is sent for sodium acetate recovery plant. Wet cake of 2,5 dcpna is neutralized by wash water and the neutral cake is then centrifuged and dried in a dryer. Dried material of 2, 5 dcpna is packed in a 50 kg gunny bags as per the user's requirement.


2,5 DCA Acetic Anhydride

Acetylation

Acetic Acid

Hydrolysis

Sodium Acetate

2,5 DCPNA

Nitration

Drying


Caustic soda

Blending

Pulverizing

Packing




• Mass Balance

UNIT OPERATION

RAW MATERIAL

ACTUAL KGS

PRODUCT

OUT PUT QTY IN KGS

ACETYLATION

2,5 D C A 500 ACETYL 2 5 D C A 630 ACETIC ANHYDRIDE 400 SODIUM ACETATE 390 SODA ASH 252 SODIUM BICARBONATE WATER 1500 WATER 1528 CO2 104 TOTAL 2652 TOTAL 2652

NITRATION

ACETYL 2 5 D C A 630 NITROMASS OF ACETYL 2 5 D C A 769

NITRIC ACID -70 % 400 H2SO4 2500 UNREACTED NITRIC ACID 85 NITRIC ACID WATER 37 SPENT H2SO4 2583 REACTION WATER 56 FIRST WASHINGS 1000 FIRST WASHINGS 1000 TOTAL 4530 TOTAL 4530



NITRO WASHINGS

NITRO MASS 759 NITRO MASS 759 NITRIC ACID 33 SECOND WASHINGS 500

WASH WATER FROM 2ND WASH 518

THIRD WASH 500 WASH WATER FROM 3RD WASH 511

FOURTH WASH 500 WASH WATER FROM 4TH WASH 504

HOT WATER FOR SOLID NITROMASS 500

WASH WATER FROM SOLID NITROMASS 500

TOTAL 2792 TOTAL 2792

HYDROLYSIS

NITROMASS 751 CAUSTIC FLAKES 160 CAUSTIC FLAKES 39 WATER 3000 WATER 2585 OR SPENT CAUSTIC LIQUOR SODIUM ACETATE 247 REACTOR WASHING 500 REACTOR WASHING 500 HYDRO MASS 624 WATER WITH HYDRO MASS 416 TOTAL 4,411 TOTAL 4411

HYDROLYSIS WASHING

HYDRO MASS 567 HYDRO MASS 567 WATER 416 WATER WITH H-MASS 416 CAUSTIC 11 CAUSTIC 11 WASHINGS (1000 LITS X 3 ) 3000 WASHING WATER 3000 SODIUM ACETATE 60 SODIUM ACETATE 60 TOTAL 4054 TOTAL 4054

CENTRIFUGING

2,5 DCPNA WET CAKE 567 567 WATER WITH WET CAKE 100 100 WASHING 1000 1000

TOTAL 1667 TOTAL 1667



Product B-3 META NITRO PARA ANISIDINE: Process Description

Conversion of Para Anisidine to Meta Nitro Para Anisidine is carried out in unit process namely Acetylation, Nitration, Hydrolysis .

In Acetylation Para Anisidine is acetylated with Acetic acid + Acetic Anhydride to obtain acetylated Para Anisidine. Acetic acid is recovered after reaction completion. The Nitration of acetylated Para Anisidine is done with Nitric acid & Sodium bi sulphite as catalyst. The nitro body thus obtained is hydrolyzed with caustic soda to get the hydrobody. Which contains Meta nitro Para Anisidine? This hydrobody is filtrate in neutech filter & caustic spent is taken out as a filtrate & filtrate is taken for further treatment. The wet cake Meta nitro Para Anisidineis then dried, blended, pulverized and packed in drums and bags for dispatch.

The caustic spent taken out from filter of hydrobody as a filtrate taken for neutralization. It is neutralized with recovered Acetic acid from acetylation. Then carbon treatment is given to this and then followed evaporation in another vessel. After completion of evaporation the liquid mass called as liquid sodium acetate can be despatch able or make cool and centrifuge it. This solid sodium acetate is a by product.


Para Anisidine Acetic Anhydride

Acetylation

Acetic Acid

Hydrolysis

Sodium Acetate

Fast Bourdeaux Gp Base

Nitration

Drying


Caustic soda

Blending

Pulverizing

Packing




•

• Mass balance

Sr. No.


1. Para Anisidine 1125.00 MNPA 1100.00 2. Acetic Anhydride 930.00 Sodium Acetate . 1170.00 3. Hydro 2.00 Drying Loss 100.00 4. Methylene Di Chloride 250.00 MDC Loss 250.00 5. Rec. MDC 950.00 Acetic Acid 544.00 6. Nitric Acid 1800.00 Rec. MDC 950.00 7. Sodium Nitrate 2.00 ETP water 19645.00 8. Water 1830.000 9. Caustic Flakes 400.00 Total 23759.00 Total 23759.00



Product B-4 META NITRO PARA TOLUDIENE:

Process Description: Conversion of Para Toludiene to Meta Nitro Para Toludiene is carried out in unit process namely Acetylation, Nitration, Hydrolysis

In Acetylation Para Toludiene is acetylated with Acetic acid + Acetic Anhydride to obtain acetylated Para Toludiene. Acetic acid is recovered after reaction completion. The Nitration of acetylated Para Toludiene is done with Nitric acid & Sodium bi sulphite as catalyst. The nitro body thus obtained is hydrolyzed with caustic soda to get the hydrobody. Which contains Meta nitro Para Toludiene, This hydrobody is filtrate in neutech filter & caustic spent is taken out as a filtrate & filtrate is taken for further treatment. The wet cake Meta nitro Para Toludiene is then dried, blended, pulverized and packed in drums and bags for dispatch.

The caustic spent taken out from filter of hydrobody as a filtrate taken for neutralization. It is neutralized with recovered Acetic acid from acetylation. Then carbon treatment is given to this and then followed evaporation in another vessel. After completion of evaporation the liquid mass called as liquid sodium acetate can be despatchable or make cool and centrifuge it. This solid sodium acetate is a by product.

• Flow chart

Para Toludiene

Acetic Anhydride

Acetylation

Acetic Acid

Hydrolysis

Sodium Acetate

MNTP

Nitration

Drying


Caustic soda

Blending

Pulverizing

Packing




• Mass Balance

Sr. No.


1. Para Toludiene 500.00 MNPT 575 2. Acetic Anhydride 476.00 Sodium Acetate . 630 3. Hydro 01.00 Drying Loss 52 4. Methylene Di Chloride 125.00 MDC Loss 125 5. Rec. MDC 2375.00 Acetic Acid 281 6. Nitric Acid 650.00 Rec. MDC 2375 7. Sodium Nitrate 01.00 ETP water 9890 8. Water 9600.00 9. Caustic Flakes 200.00 Total 13928.00 Total 13928.00



Product C-1 ORTHO NITRO CHLORO BENZENE PARA SULPHONIC ACID:-

• Manufacturing process

First charge H2SO4 (98%) in a reactor and start stirring and charge spent and MCBPSA. Now slowly heat to 45°c and start feeding of HNO3 (98%). HNO3 feeding completed within 2 hours .Check sample for completed and if it is completed then add spent acid for dilution and cool to R.T. and filter it Ortho Nitro chloro benzene Para Sulphonic acid (ONCBPSA)



• Mass Balance

Sr. No.


10. MCBPSA 1200.00 ONCBPSA 916.00

11. Sulphuric Acid 720.00 Spent Sulphuric Acid - 70% 2718.00

12. Spent Sulphuric Acid 1460.00 Extracted MCB 476.00 13. Conc. Nitric Acid 330.00 14. MCB 400.00 Total 4110.00 Total 4110.00

MCBSA Sulphuric Acid Spent Nitration

Centrifuge

ONCBPSA

Filtration



By-products:

1. Sodium Acetate Flow diagram:

Nitro mass

Hydrolysis R3A

Coustic soda Water

Hydrolysis R3C

Hydrolysis R3B

Water

Hydromass

Sodium acetate liquid filterate

Water

Hydromass

sodium acetate liquid filterate

Hydromass Water

Hydromass

sodium acetate liquid filterate

Sodium Acetate

wet cake

CENTRIFUGE Sodium acetate packing

in gunny bags

Sodium Acetate

liq. Storage

tank

MEE

Water

ML Recycle to MEE

Conc.sod.acetate liquid

Condensate Water ST. Cooling tower water make up



Material Balance:

Sr. No.

INPUT QTY (Kgs) OUTPUT QTY (Kgs)

1. Mother Liquor 4000.00 Sodium Acetate 1818.00 2. Acetic Acid 240.00 Condensate 3538.00 3. Hypochlorite 1120.00 Carbon Solid Waste 8.00 4. Carbon 4.00 Total 5364.00 Total 5364.00

2. Sodium sulphate Process description:

• Sodium sulphate mother liquor of pH 7.5 to 8 is generated after the scarlet r base precipitator. • After checking the pH the liquor is neutralized with sulphuric acid in a PP vessel. • Neutralized rich sodium sulphate mother liquor is then transferred to a storage tank. • Sodium sulphate liquor is charged to a SS vessel for carbon treatment. • Heating is applied up to 80oC and the solution is maintained at that temperature upto two hours. • After carbon treatment at 80oC the whole mass is transferred through a pressure filter and collected to

a PP vessel. • Sodium hypo chlorite is added to the above mass for decolouring the solution. • After decolourizing the solution is transferred to a MEE for evaporation • Concentrate sodium sulphate liquid is then centrifuged and the centrifuge mother liquor obtained is

recycled back to the evaporator. • White sodium sulphate cake is removed from the centrifuge and packed in a gunny bag.

• Material Balance:

Sr. No.

INPUT QTY (Kgs) OUTPUT QTY (Kgs)

1. Mother Liquor 4000.00 Sodium Sulphate 380.00 2. HCL 40.00 Condensate 3655.00 3. Carbon 5.00 Carbon Solid Waste 10.00 Total 4045.00 Total 4045.00



• Flow diagram:

5 Nitro Ortho Anisidine. Washing

Water

HYDROMASS

Separation Vessel R4B

water SULPHURIC ACID

Precipitation vessel of 4 nitro

ortho

Precipitation vessel of 4 nitro ortho anisidne

SODIUM sulphate

liq. Storage

Tank

Sodium sulphate wet

cake

MEE

2100 LITS 5 nitro ortho anisidne washing water recycle

sodaash Conc.

Sod.sul w.w 1400 lits

5 nitro ortho ansidne

3500 lits water

Ml of 4 nitro ortho anisidine (scarlet R base)

Cooling tower water make up Condensate

water

4 nitro ortho Ani

Rich Sodium SULPHATE liquid

5 nitro ortho ani. WET CAKE

4 nitro ortho ani. Liq.

4 nitro ortho Anisidne

Dilute sodium SULPHATE

Conc.sod.sulphate

liquid

water

centrifuge

CENTRIFUGE MOTHER LIQUID

Sodium Sulphate packing Gunny bags

3500 lits washing water of 5 nitro ortho anisidine



1. Ortho Nitro Phenol Flow diagram:

ONCB

Methoxylation

Coustic soda

Methanol

Methanol Recovery

ONA Washer

Recycle Water

Crude ONA

Sodium Chloride ONA/METHAOL MIX.

Wash water W.W

CRUDE ONA

Treatment Vessel

Reaction mass of ONA

Recycle treated water

Methanol

filteration

ONA

Water

PP vessel for crude ONP

precipitation

Crude ONP wash water

Sulphuric acid

CRUDE ONP

evaporator

filteration

Evaporated Salt

PP Vessel for

Neutralizer

CENTRIFUGE Crude ONP in drums/bags



• Marketing area of final products:

The products are used for the manufacturing dyes and pigments and the product has very good potential in local market as well as the export of the same. The product can be exported to the other countries. Company has a wider customer base.

• Transport of Raw material and Finish products:

Sr. No.

Raw Material Quantity Source of supply

Means of storage

Max. Qty. to be stored at any given time i.e. storage capacity

Means of transportation

MSIHC rule applicability

1. Ortho nitro chloro benzene

20 MT AARTI INDUSTRIES

Liquid Storage tank

30 MT Tanker load No

2. METHANOL 15 MT AARTI INDUSTRIES DEEPAK FERTILIZER

Liquid Storage tank

39 KL Tanker load Sch.II, part –II,377

3. CAUSTIC FLAKES

15 MT GUJARAT ALKALI SHREE RAM CHEMICALS

Solid ware house

40 MT Truck load Sch.II, part –II,571

4. Para nitro chloro benzene

15 MT Aarti industries

Liquid storage tank

30 MT Tanker load Sch.II, part –II,427

5. Ortho Ansidine

15 MT Dragon drugs Liquid storage tank

27 KL Tanker load No

6. Acetic Anhydride

15 MT jubilant chemicals

Liquid Storage tank


7. Concentarte nitric acid-98%

15 MT Aarti industries / Rashtriya chemicals and fertilizers

Liquid Storage tank


8. Methylene di chloride

15 MT Aarti industries / Gujarat alkali

Liquid Storage tank




9. sulphuric acid 15 MT Aarti industries

Liquid storage tank


10. sodium bi carbonate

17 MT Tata chemicals

Solid Ware house

34 MT Truck Load No

11. Para anisidine 20 MT Dragon Drugs Solid Ware house

40 MT Truck load No

12. PARA TOLUDIENE

16 MT Dragon drugs Deepak nitrate

Solid Ware house

32 MT Truck load Sch.I, part –I(b)(v)

13. 2,5 di chloro aniline

15 MT Aarti industries

Solid Ware House

30 MT Truck load No

14. Magnesium oxide

15 MT Tirupali chemicals

Solid ware house

20 MT Truck load No

15. Dilute nitric acid

15 MT Deepak fertilizers

Liquid Storage tank

30 MT Tanker load Sch.II, part –II,423

16. Mono Chloro benzene sulphonic acid

6.0 MT Ganesh Polychem

Solid Ware house

12 MT Tempo load No

(viii) Resource optimization/ recycling and reuse envisaged in the project, if any , should briefly outlined : The raw materials packed in drums and stored in the warehouse. By adoption continuous improvement in technology and process the reduction in process waste

generation will be achieved. By proper and efficient handling of raw materials, wastages of raw materials will be reduced.

(ix) Availability of water its source, Energy/power requirement and source should be given: Availability of water its source, Energy/power required and its source.



Water Consumption & Waste water Generation and scheme for their Management/disposal:

Source: Fresh water requirement will be catered from GIDC water supply dept.

A. Domestic waste water – 5 KL/Day

(Existing: 3 KL/Day + proposed: 2 KL/Day)

5 .00 KL/day will be disposed through adequate soak pit and septic tank

B. Industrial waste water : 94.60 KL/Day

(Existing: 60.40 KL/Day + proposed: 34.2 KL/Day)

42.4 KL/day will be treated in adequate Multiple Effect Evaporator with stripper and 52.2 KL/Day will be treated using adequate ETP then will be disposed off through underground drainage to CETP, Sarigam.

Sr. No

Particulars Water consumption (KL/Day) Wastewater Generation (KL/Day)

Existing Proposed Total Exiting Proposed Total

A Domestic 5.00 5.00 10.00 3.00 2.00 5.00 B Industrial 1 Processing &

Washing 53.00 26.70 79.70 52.00 26.60 78.60

2 Boiler 7.00 0.00 0.00 0.00 0.00 0.00 3 Cooling 30.00 43.00 73.00 4.00 6.00 10.00 4 Others 5.00 5.00 10.00 0.00 0.00 0.00 5 Concentrated

Stream --- --- --- 4.40 1.60 6.00

Total B 95.00 74.70 162.70 60.40 34.20 94.60 Total (A+B) 100.00 79.70 172.70 63.40 36.20 99.60



• Water Balance Diagram after proposed expansion(KL/day)

EFFLUENT TREATMENT SCHEME

Design Criteria : Source of Effluent: process, washing and utility etc. Effluent Generation: 52.2 KL/Day

Discharge

MEE 42.4

5.0

6.0 78.6

36.4 42.2

10.0

Water Consumption 172.7

Domestic 10.0

Industrial 162.7

Soak pit Concentrated

Process &

Washing 79.7 Boiler

0.0 Cooling 110.0

(73 Fresh)

Others 10.0

Effluent Treatment Plant 52.2

Recycled as Cooling Tower Make up - 37

Evaporation Loss – 2.4

3 MT/day Sodium Sulphate

Recovery

37



EFFLUENT TREATMENT SCHEME

SR. NO.

PARTICULARS SIZE in m CAPACITY KL

1 Collection Pit 2 x 2.4 x 3.05 14.64

2 Neutralizer – I 1.7 x 2.1 x 2.6 9.28

3 Neutralizer - II 3 x 2.9 x 2.65 23.05

4 Ozonisation Pit 2 x 2.74 x 2.13 11.67

5 Collection Pit 1.9 x 2 x 2.7 10.26

6 Sand Filter – I 750 mm dia x 2.0 m ht --

7 Sand Filter - II 2.4 x 1.05 x 1.45 3.65

8 Carbon Filter 750 mm dia x 2.0 m ht --

9 Alkaline Pit 2.45 x 2.35 x 2.65 15.25

10 Acidic Pit 2.45 x 2.35 x 2.65 15.25

11 Oil & Grease Pond 1.4 x 1 x 1.7 2.38

12 Settling Tank 2.42 x .98 x 1.45 3.43

14 Holding Sump 5 x 2.67 x 1.45 19.35

Process Description:

The effluent coming from the plant will be initially collected into the collection pits. The effluent from the

collection pit will be taken into neutralization tank where effluent will be neutralized with hydrated lime /

caustic lye. After neutralization pH of the effluent will raised up to 9 and potassium permanganate solution will

be added to oxidize the phenol present in the effluent. After the oxidation of phenol the effluent will be

neutralized by ferrous sulphate solution. The neutral effluent will be pumped into settling tank. Clear effluent

from the top of the settling tank pass through the activated carbon bed. The primary treated effluent will be

discharged to CETP of M/s Perfect Enviro Control System ltd. for final treatment and disposal. Sludge from the

settling tank bottom will be drain into sludge drying bed. After drying, it will be collected into bags manually and

stored into solid waste storage yard. It will be disposed off through Sarigam Waste Effluent Management co. ltd.

to TSDF, Vapi. The lichates from the Sludge Drying Beds & solid waste storage area will be taken back into the

collection pit.



Process Flow Diagram:



Energy Requirements and its source: Sr. No.

Particulars Existing Proposed Total after proposed change

Source

1 Heat Requirement

1.5 TPH 3.5 TPH

5 TPH Will be sourced from sister unit M/s.

Aarti Industries (Boiler Div.)

• Power Requirements and its source:

Sr. No.

Particulars Existing Proposed Total after proposed change

Source

1 Power – Electricity requirement

600 kVA 275kVA 875 kVA GEB

• Utility Emission & Control Measures: Sr. No.

Particulars Fuel / Power & it’s Qty Probable Pollutants & Limits

Control Measures

1.

D.G. Set(2 No.) 250 KVA 125 KVA.

Diesel. 38 lit/hrs. Diesel. 18 lit/hrs

PM <150 mg/Nm3

SO2 < 100 ppm NOx < 50 ppm

Chimney Height: 11 m Diameter: 100mm

• Quantity of Solid Waste generation and its management:

Types of Waste& Category

Source of Generation Existing

Quantity/Month

Quantity (total after Proposed)/Month

Storage Method

Method of Disposal

Used oil (5.1)

Plant machineries

41.66 lits/M

84 liters/M

Stored into the closed container.

Will be sent to registered recycler /Reused

ETP Waste (34.3)

ETP 2 MT 60 MT

Will be stored at the separate area.

Disposal to TSDF site. Sarigam

Discarded containers/barrels /liners (33.3)

Consumed Raw materials and Product packaging.

84 nos

150 nos.

Stored at a specify area as per the rule.

Will be sold to GPCB scrape dealers as a scrap.

Saturated Carbon (28.2)

Mfg. Processes

0.00

1.25 MT

Stored at a specify area as per the rule

Will be send for incineration SEPPL Kutch ( Gujarat)



(x) Schematic representations of the feasibility drawing which give information of EIA purpose:

A schematic representation of the feasibility drawing

Resource requirements • Raw Material: Sourced from Manufacturer / Traders of the same. • Land: land not require for proposed project, At GIDC, Sarigam. • Water: Will be sourced through GIDC water supply. • Power: Power will be sourced through Dakshin Gujarat Vij Co. Ltd. • Fuel : Local dealer

Env. Mgt. Plan (EMP) • Air Pollution Control Measures: Air Pollution control system will be provided. • Greenbelt Area about 30% of the Total Area will be developed. • Health & Safety measures will be followed properly

• Soak pit/ Septic Tank and ETP for Industrial waste water. • No Process waste will be generated. • Flue Gas emissions: Adequate chimney height will be provided. • Fugitive emission: There is no generation of fugitive emissions.

Type of Industry Proposed mfg. unit of “Synthetic Organic

Chemicals”

Site Location: The company is located plot no. 2702,2901,2701-

2703,2608,731/A, GIDC, Sarigam, Tal. Umargam, Dist.-Valsad, Gujarat-396155

Public consultation: Not required as the project is located in

notified Industrial Zone

Submission of Form-1 and Pre-Feasibility Report & Draft TOR

Proposed Activity: The proposed expansion project involves

the production of "Synthetic Organic Compounds"

Type of category as per EIA notification: Synthetic Organic Chemicals (Activity -5(f)- Category-B)

Presentation before the SEAC for TOR



4. SITE ANALYSIS

4.0 Site Analysis (i) Connectivity:

The project is located in notified Industrial Estate of Sarigam which is very well connected to National Highway no.8 and Western Railways. And the nearest air port (Mumbai) and port are 150 KM away from the project site by road.

(ii) Land Form, Land use and Land ownership: The land is in the form of industrial shed owned by Gujarat Industrial Development Corporation. The total plot area 14519.60 Sq.m is belonging to M/s Alchemie Industries. The existing land is located in the notified industrial area of GIDC Sarigam (notification no.GHU/97/16/GID/1093/2391/G-1, dated : 5th May 1997)

(iii) Existing Infrastructure/ land use pattern Proposed project will be located within the GIDC notified industrial area of Sarigam which has available infrastructure like water, electricity, roads, rail, transportation and drainage system, CETP and TSDF Site. Surrounding area is consisting with agriculture, other industrial units.

(iv) Soil classification and Land use classification: General soil classification of the area is as under: The area, being of basaltic formation, falls under the broad soil group of red loams and black clay soils. The transmission of water through similar parent material seems to have influenced the development of different physiographic characteristics of the soils in the area. The area in between the hills with sloping lands contains dark yellowish brown to very dark grayish brown gravelly clay loam to clayey soils of shallow to moderate thickness. The dissected hill and steep slopes suffer from severe erosion hazards. The steep hill slopes are almost devoid of soil.

(v) Climate data from secondary sources:

Rainfall Data:

The climate here is tropical. The winter months are much rainier than the summer months in Valsad. This climate is considered to be as according to the Köppen-Geiger climate classification. The temperature here averages 26.9 °C. Rain fall about 1963 mm of precipitation falls annually during 2013.

(vi) Social Infrastructure available: Sarigam infrastructure owes itself largely to the initiatives of G.I.D.C., in building the Industrial infrastructure and in attracting young entrepreneurs from Gujarat and other states. Equally, the growth of the social infrastructure - School, Colleges, Hospital, vocational training - stems from the bold initiatives of the Laxmi Vidhya Peeth. National Highway No. 8 passes through Bhilad. It is connected to all major cities. Bhilad and Vapi railway stations on the Mumbai-Ahmedabad rail link of Western Railway (India) has become the direct beneficiary in terms of revenues due to daily commuters. The Union territories as well as Vapi, Bhilad, Umbergaon, and Pardi, only 12–40 km from Sarigam, There are good residential and commercial areas. Daman and Silvassa (the capital of Dadra and Nagar Haveli) attract both Indian and international tourists.



5. Planning Description 5.0 Planning Brief. (i) Planning Concept (Type of industries, facilities, transportation etc) Town and Country Planning

/Development authority Classification: There is a cluster of numerous large-scale, medium-scale and small-scale industries, engaged in

manufacture of variety of products in the Gujarat Industrial Development Corporation (GIDC) notified area of Sarigam. GIDC notified industrial area of Sarigam has the entire available infrastructure like water, electricity, roads, rail, and transportation, availability of raw material, CETP, TSDF Site and drainage system.

(ii) Population Projection: Not applicable

(iii) Land use planning (breakup along with green belt etc.): The proposed expansion project is located within the Notified Industrial Area by Government of Gujarat and due to the proposed project there will not be any change in the land use pattern of the region. Plot site Area Statement:

Area Statement Area After Proposed Expansion (in m2)

Total Area 14519.60 Construction Area Factory Shed 5852.96 Open Land Area 1992.31 Greenbelt Area 6674.31

(iv) Assessment of Infrastructure demand (Physical & Social): The proposed infrastructure to manufacture products will be built with standard engineering design considering all the relevant parameters related to environment, health and safety. Facilities like road and communication are good. Banks, ATM's and medical facilities are also adequate.

(v) Amenities/ Facilities:

Education- schools including middle, secondary and higher secondary schools, Collages, social welfare hostels. Medical and Health- Community Health Centre, & Primary Health centre are available near villages Power and water- All the villages are electrified and drinking water facilities are extended to all villages. Rail and Road- The project site is very well connected by road through State Highway no. 8, Western railways.



6. Infrastructure Details 6.0 Proposed Infrastructure: (i) Industrial Area (Processing Area).

Basic infrastructure developed already and the required plant and machineries will be installed after getting statutory clearance.

(ii) Residential Area (Non Processing Area) : No residential area is involved in the proposed project. The employs are accommodated in nearby Residential areas

(iii) Green Belt: Green belt area will be provided and maintain at the tune of about 30% of the total land area as the project site is within the developed industrial area.

(iv) Connectivity (Traffic and Transportation Road/ Rail/ Metro/ Water ways etc) : The project site is very well connected by road through National Highway no. 8 and western railways. (v) Drinking Water management (Source& Supply of water): Water requirement will be fulfilled through GIDC water supply. (vi) Sewerage System:

GIDC has provided sewerage system to dispose the sewage effluent.

(vii) Industrial Waste Management: Industrial waste water 90.06 KL/day generated mainly from the process and washing. Generated waste water will be treated by adequate effluent treatment plant and treated water will be send to CETP, Sarigam.

7. Rehabilitation and Resettlement (R&R) Plan: (i) Policy to be adopted (Central/ State) in respect of the project affected persons including home oustees,

land oustees and landless laborers (a brief outline to be given): The proposed Industry does not envisage any disturbance to local community or the village since the land is acquired and fully owned by GIDC Sarigam Notified industrial Area. The proposed project will not affect the home oustees, land oustees and landless laborers. Hence there is no R & R plan required.

8. Project Schedule & Cost Estimates: (i) Likely date of start of construction and likely date of completion (Time schedule for the project to be

given): After obtaining Environmental clearance and Consent to Establish from GPCB, the company shall start the proposed construction and commissioning of the project.

(ii) Estimated project cost along with analysis in terms of economic viability of the project: Estimated project cost along with the analysis in terms of economic viability of the project



Plant & Machinery, Pipeline & Fittings, Electrical Installation, Safety systems, etc. are the major heads considered in the Capital Cost Projection for the proposed expansion project. Environment Protection has also been considered in planning the Cost Projection, which will include Green belt development, safety systems, etc.

Sr. No.

Purpose Existing Cost (Rs. In Lakhs)

Proposed Cost (Rs. In Lakhs)

Total Cost (Rs. In Lakhs)

1. Land 38.60 - 38.60 2. Building and Civil Works 60.20 80.80 141.00

3. Plant & Machinery and other fittings

140.37

550.24 690.61

4. Environmental protection measures

60.70 175.26 235.96

TOTAL : 299.87 806.30 1106.17

The proposed investment will be made by company only.

The company will provide budgetary provision for the recurring expenses for environmental issues while planning the allocation of funds during the annual budgetary planning.

Recurring Cost per annum

Sr. No.

Component Proposed (Rs. in Lakhs/annum)

1. Environment & Safety Management System 25.45

2. Greenbelt Maintenance 7.00

3. Enterprise social contribution 5.00

Total 37.45

9. Analysis of Proposal (Final Recommendations): (i) Financial and social benefits with special emphasis on the befit to the local people including tribal

population, if any, in the area: Proposed expansion activity will provide benefits to the local people in terms of financial and social welfare.

• Local people will get direct financial benefit by way of employment. • Local people will get some contracts of supply and services to get indirect income. • Company will contribute in improving education and health facilities in nearby area.


Under Activity: 5(f), Category: B (Synthetic Organic ... · Planning Concept (Type of industries,...

Documents

Transcript of Under Activity: 5(f), Category: B (Synthetic Organic ... · Planning Concept (Type of industries,...