PRE FEASIBILITY REPORT FOR EXPANSION FOR NEW …environmentclearance.nic.in/.../PFR/...feasibilityReport(PFR)File.pdf · PRE FEASIBILITY REPORT FOR . EXPANSION FOR NEW PRODUCTS

PRE FEASIBILITY REPORT

FOR

EXPANSION FOR NEW PRODUCTS

OF

M/s. Aries Laboratories.

18, Natraj Industrial Estate,

Village: Iyava-Vasna, Sanand, Dist:Ahmedabad.

Ashwin Patel: 9825068761

E-mail: [email protected]

Prepared By:

T. R. ASSOCIATES C-605/A, Ganesh Meridian, Opp. Kargil Petrol Pump,

S. G. Highway, Ahmedabad.

Mo. No.: 98253 71099

Email ID: [email protected];

[email protected]

June 2015

mailto:[email protected]

mailto:[email protected]

1. Executive summary M/s. Aries Laboratories is proposing Expansion to manufacture new products as

pharmaceutical drugs at 18, Natraj Industrial Estate, Village: Iyava-Vasna, Sanand,

Dist:Ahmedabad. Proposed unit will manufacture all pharmaceutical drugs for sell

purpose.

The total land area of company is 1987 m2 out of which 720 Sq. Mt. land will be

used for greenbelt area development. The Existing Cost of project is 0.45 Crore,

whereas cost of Proposed Expansion is 3.55 Crores. Therefore, Total cost of project

after Expansion will be 4 Crores. Total budget allocation towards Environmental

Management Facilities will be Rs. 10 Lacs. Total 10 persons will be employed

including skilled persons, unskilled persons and office staff.

M/s. T. R. Associates is carried out EIA/EMP studies for Environmental Clearance.

Production details are given below:

Existing Products

SR. NO.

NAME OF THE PRODUCT QUANTITY

1 Ferrous Sulphate 50 MT/M

2 Zinc Sulphate 50 MT/M

3 Potassium Iodide 10 MT/M

4 Ammonium Chloride 50 MT/M

Sr. No.

Name of Product Quantity MT/Month

1 Diethyl Carbamyzine Citrate 8

2 Diphen Hydramine Hydrochloride 5

3 Sodium Benzoate 20

4 Diclofenac Sodium 10

5 Diclofenac Potassium 5

6 Erythromycin Stearate 5

7 L-Lysine Monohydrochloride 10

8 Fluconazole 2

9 Carbomer 10

10 Disulfuram 5

11 Niacinamide 20

12 Sodium Citrate 40

13 Trimethyl Sulphoxonium Iodide 10

14 2-(7-methoxynaphthalen-1-yl)acetic acid 0.3

By-Products 1 Sodium Chloride 1.22

2 Ammonium Thiocynate 0.37

3 Sodium Bromide 1.77

Salient Features with in 10 km radius surroundings area as follows:

S.No Important Features Description

1 Location 18, Natraj Industrial Estate,

Village: Iyava-Vasna, Sanand, Dist:Ahmedabad

2 Longitude 72°20'26"E

3 Latitude 23° 0'34"N

4 MSL 34 m

5 Nearest power station GEB (Gujarat Electricity Board)

6. Proponent Name Ashwin Patel

7 Corporate office address 23, Jodhapur Park society, B/H ISRO,

Ramdevnagar, Satellite, Ahmedabad-380015

8 Temperature range 100 C to 460 C

9 Annual Rain fall 772 mm

10 Nearest Road SH 17 (0.29 Km)

11 Nearest Railway station Sanand– 4.88 Km

12 Nearest city Ahmedabad (16 km)

13 Nearest village Vasna Iyava (1.3 km)

14 National HW NO NH 8C (16 Km)

15 State HW No SH 17 (0.29 Km)

16 Seismic Zone Zone-III (Less Active)

17 National Parks / Sanctuary None within 10 Km radius.

2. Project back ground.

Diethylcarbamazine is used in the treatment of certain worm infections. This medicine works by killing the worms.

Diphenhydramine is an antihistamine used to relieve symptoms of allergy, hay fever, and the common cold. These symptoms include rash, itching, watery eyes, itchy eyes/nose/throat, cough, runny nose, and sneezing. It is also used to prevent and treat nausea, vomiting and dizziness caused by motion sickness.

As a food additive, sodium benzoate has the E number E211. It is bacteriostatic and fungistatic under acidic conditions. It is most widely used in acidic foods such as salad dressings (vinegar), carbonated drinks (carbonic acid), jams and fruit juices (citric acid), pickles (vinegar), and condiments.

Lysine is an essential amino acid in human nutrition because the body cannot produce it; therefore, it must be taken in either by diet or supplementation. Lysine has been studied for the prevention and treatment of herpes infections and cold

sores. It also increases the intestinal absorption of calcium and eliminates its excretion by the kidney, suggesting that it might be helpful in osteoporosis.

Niacinamide (nicotinamide) is a form of vitamin B3 (niacin) and is used to prevent and treat niacin deficiency (pellagra). Niacin deficiency can cause diarrhea, confusion (dementia), tongue redness/swelling, and peeling red skin. Niacinamide is often used instead of niacin because it causes fewer side effects (e.g., flushing). Unlike niacin, niacinamide does not help correct blood fat levels and cannot be substituted for niacin if you are being treated for a blood fat problem (e.g., high cholesterol).

Disulfiram is used along with counseling and support to treat alcoholism. Disulfiram works by blocking the processing of alcohol in the body. This causes you to have a bad reaction when you drink alcohol.

Fluconazole is used to prevent and treat a variety of fungal and yeast infections. It belongs to a class of drugs called azole antifungals. It works by stopping the growth of certain types of fungus.

sodium citrate is used for Treating metabolic acidosis and certain kidney problems (eg, kidney stones). It is an osmotic laxative, which induces a laxative effect (stimulating stool production). Sodium citrate is sometimes used as an acidity regulator in drinks, and also as an emulsifier for oils when making cheese.

Erythromycin is used to treat a wide variety of bacterial infections. It may also be used to prevent certain bacterial infections. Erythromycin is known as a macrolide antibiotic. It works by stopping the growth of bacteria.

Diclofenac Sodium is used to relieve pain, swelling (inflammation), and joint stiffness caused by arthritis. Reducing these symptoms helps you do more of your normal daily activities. This medication is known as a nonsteroidal anti-inflammatory drug (NSAID).

Diclofenac potassium belongs to a group of medicines called non-steroidal anti-inflammatory drugs (NSAIDs), which are used to reduce pain and inflammation in the following conditions: Sprains, strains and other injuries, Pain and inflammation following surgery, Gout.

Trimethylsulfoxonium Iodide is a sulfoxonium salt. It is used to generate dimethyloxosulfonium methylide by reaction with sodium hydride. The latter compound is used as a methylene-transfer reagent, and is used to prepare epoxides.

Carbomer is a synthetic polymer that forms a viscous eye gel. It produces a transparent, lubricating and moistening film on the surface of the eye and is used as artificial tears.

The proposed products have good market demand.

Export Possibility.

There is good possibility for export. But currently we are focused to local sale market for distribution.

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

This project will provide direct employment to 10 people whereas it will provide employment to many others indirectly.

3. Project Description

(i) Type of project including interlinked and interdependent projects.

Pharmaceutical drugs are linked to human health directly. Some of the

products will be only purified in our project and so it will be interdependent on

the companies manufacturing those crude products/raw materials.

(ii) Location

Longitude: 72°20'26"E Latitude : 23° 0'34"N

Google Image of Proposed Location.

Key Plan of proposed site

Project Site

(iii) Project description with process details

EXISTING PRODUCTS

1. Manufacturing Process of Zinc Sulphate PROCESS:- First Charge DM Water in SS Reactor. Then add Zinc Sulphate Crystal and heat the solution up to 60 °C. After Dissolution of crystals, filter the solution. Then evaporate the material and cool up to room temperature. The obtained zinc sulphate is centrifuged and dried. After drying & pulverizing the product is analyzed and packed. The Mother Liquor is recycled for next batch.

Equation

Process Flow Diagram:

SS Reactor DM Water

Heating

Filtration

Evaporation

Centrifugation

Drying

Pulverizing

Analyzing and Packing

Zinc Sulphate crystal

Mother Liquor is recycled in next batch.

2. Manufacturing Process of Ferrous Sulphate PROCESS:- First Charge DM Water in SS Reactor. Then add Ferrus Sulphate Crystal under stirring till it dissolves. Filter the solution and Start Evaporation. The obtained ferrous sulphate solution is centrifuged and dried. After drying & pulverizing the product is analyzed and packed. The Mother Liquor is recycled for next batch.

Equation


SS Reactor DM Water

Stirring till the crystals dissolves

Filtration

Evaporation

Centrifugation

Drying

Pulverizing


Ferrus Sulphate crystal

Mother Liquor is recycled in next batch

3. Manufacturing Process of Ammonium Chloride PROCESS:- Take D.M. Water In S.S Reactor. Charge Ammonium Chloride Tech in S.S. Reactor. Heat The Solution at 50°C. Then filter the Solution. The obtained filtrate is evaporated. Then Obtained Ammonium Chloride is centrifuged

and dried. Then Final product is packed. The Obtained Mother Liquor is recycled in the next batch.

Equation


SS Reactor DM Water

Heating

Filtration

Evaporation

Centrifugation

Drying


Ammonium Chloride Tech


4. Manufacturing Process of Potassium Iodide PROCESS:- First Charge DM Water in SS Reactor. Then add caustic potash at room temp. Then charge Iodine in Caustic Potash in a solution at 5-10°C temp. Iodine is slowly

dissolved in it. The material is then reduced with Formic Acid. Potassium Iodide forms naturally. Evaporate the solution. Then potassium Iodide is centrifuged & Dried at 110°C. After drying the materials are analyzed & then Packed. The Mother Liquor is recycled for next batch.


SS Reactor Formic Acid

Filtration

Concentrated

Centrifugation

Drying


Iodine Crude Caustic Potash


PROPOSED PRODUCTS FOR EXPANSION

1. Manufacturing Process of DIETHYLCARBAMAZINE CITRATE

PROCESS:- First charge Toluene, N-Methylpiperazine and Sodium Hydroxide in S S reactor. Start slowly addition Di Ethyl Carbamyl Chloride under stirring below 20°c

temperature. After addition is completed, start distillation for recovery of toluene. At the end Di Ethyl Carbamazine base are received. Then start separation of Sodium Chloride & Water. Then dissolve Di Ethyl Carbamazine base in acetone and add carbon & filter the

material. Then start addition of Citric Acid under stirrng to get pure Diethyl Carbamazine

Citrate. Then Di Ethylcarbamazine Citrate is centrifuged and dried. After drying for 4 to5 hrs material is taken for analyses and then packed. The mother liquor obtained is recycled in the next batch.

Reaction Flow

N

N

CH3

H

N

N

CH3

CON(C2H5)2

+ (C2H5)2NCOCL

TOLUENE+ +Nacl H2O

N

N

CH3

CON(C2H5)2N

N

CH3

CON(C2H5)2

+

CH3 C

HOOCH2C

CH2COOH

COOHCH3 C

HOOCH 2C

CH2COOH

COOH

NaOH

NMP

DECCL

DC Base

DC BaseCitric Acid

DCC


S.S. Reactor 385 kgs

385 kgs

Di ethyl carbamyl chloride-135 kgs

Addition Below 20°c Temp 520 kgs

520 kgs

Sepration 520kgs

Sodium chloride- 58kgs + Water-28 kgs (Sodium chloride will goes to manufacturer)

434 kgs

Distilation 434 kgs

Toluneloss-10kgs Tolune recieved-225 kgs used in next batch

199 kgs

Acetone-225 kgs Carbon-2 kgs

Diethyl carbamyzine base - 426 kgs

426 kgs

Filter 426 kgs 2 kgs carbon loss

424

Addition 841 kgs

841 kgs

Centrifuged 841 kgs

Acetone-225 kgs Citric acid-192 kgs Acetone loss-10 kgs

Acetone reci-430 kgs +Material loss-11 kgs (used in next batch)

Tolune-235 kgs N-methyl Piperazine-100 kgs Sodium Hydroxide-50 kgs

Drying 390 kgs

Acetone loss- 10 kgs

380 kgs

Diethyl carbamyzine citrate 380 kgs

390 kgs

Mass Balance SR. NO.

INPUT QTY PER BATCH (KG)

OUTPUT QTY PER BATCH (KG)

1. Toluene 235 Sodium Chloride 58 2. n Methyl Piperazine 100 Water 28 3. Sodium hydroxide 50 Toluene loss 10 4. Di ethyl carbamyl

chloride 135 Toluene Received 225 5. Acetone 450 carbon waste 2 6. carbon 2 Acetone loss 20 7. Citric acid 192 Acetone received 430 8. Material loss 11 9. DI ETHYL

CARBAMYZINE CITRATE 380

Total 1164 1164 2. Manufacturing Process Of DIPHEN HYDRAMINE HYDROCHLORIDE

PROCESS:- First charge Diphenyl Methane Bromide, Toluene & Sodium Hydroxide In S.S. reactor. Then add Di Methyl Amino Ethanol slowly under stirring & maintain 105°c temp . After addition is completed, start stirring the material for 1 hrs . Separate Toluene layer and add Carbon then filter the material. Charge Toluene layer for distillation for recovery of Toluene to get crude Diphen

Hydromine base. Charge Diphen Hydromine base and add IPA HCL slowly under stirring & maintain

10°temp till 4 to 5 hrs. Diphen Hydramine Hydrochloride is received. Then above material is taken for centrifuge, drying and pulverizing. After pulverizing material is analyzed and then pack the material. The mother liquor obtained is recycled in the next batch.

Reaction Flow

H5C6

H5C6

CHBr +CH3

CH3

NCH2CH2OHNAOH

TOLUENE

H5C6

CH2

H5C6

OCH2

C6H5

CH2

C6H5

Diphenyl methane bromide

HCl

Di methyl amino ethanol Diphen hydramine hydrochloride


Diphenyl methane bromide-235 kgs, Tolune-100 kgs Sodium Hydroxide-50 kgs

S.S.Reactor 385 kgs

385 kgs

Di methyl amino ethanol-89 kgs

Addition Below 105°c Temp 474 kgs

474 kgs

Separation 474 kgs

Sodium bromide- 103kgs + Water-28 kgs (Sodium bromide will goes to manufacturer)

343 kgs

Filter 345.5 kgs Carbon – 2.5 kgs

343 kgs

Acetone-225 kgs Carbon-2 kgs

Distillation -570 kgs

270 kgs

Di phen hydramine base

IPA HCL -211kgs Used in next batch

270

Addition 517 kgs

517 kgs

Carbon-2.5 kgs

Tolune recoverd-285kgs Toluene loss-15 kgs

IPA HCL-247 kgs

Centrifuged 517 kgs

Drying 306 kgs

306 kgs

IPA HCL loss-15 kgs

291 kgs

Pulverizing 291 kgs

291 kgs

Diphen hydramine hydrochloride 291 kgs

Mass Balance

SR. NO.



1. Diphenyl Methane Bromide 235 Sodium bromide 103

2. Toluene 100 Water 28 3. Sodium Hydroxide 50 Waste carbon 2.5 4. Dimethyl Amino

ethanol 89 Toluene recovered 285 5. Carbon 4.5 Toluene Loss 15 6. IPA HCL 247 IPA HCL Recovered 211 7. Acetone 225 IPA HCL loss 15 8.

Diphen Hydramine Dichloride 291

Total 950.5 950.5

3. Manufacturing Process Of SODIUM BENZOATE

Process First charge D M Water and benzoic acid under stirring. Then add slowly caustic soda under stirring & maintain PH 6.5 to 7.0 of this solution. Then filter the material & start evaporation of the solution. Then start sodium benzoate material is taken for centrifuge. Then start drying the material for 3 hrs. Then start pulverizing. After pulverizing, the obtained sodium benzoate is analyzed. Then pack the material.

The mother liquor obtained is recycled in the next batch.

Reaction Flow

COOH

+ NaOH

COONa

+ H2O

Benzoic Acid Di methyl amino ethanol Sodium Benzoate Water

Process Flow Diagram

D M Water 400kgs Benzoic Acid 427 kgs

S S Reactor ( 400 kgs)

400 kgs

Caustic Soda 70 kgs

897 kgs

Stirring ( 897 kgs)

Maintain Ph 6.5 to7.0

Filter (897 kgs)

897 kgs

350 KGS Water loss

897 kgs

Centrifuge (547 kgs)

547 kgs

Evaporation (897 kgs)

32 kgs Material loss 33 kgs water loss Mother liquor used in next batch

Drying (482 kgs)

482 kgs

10 kgs Water loss

472 kgs

Pulverising ( 472 kgs)

472 kgs

Packing (472 kgs)

Mass Balance

SR. NO.



1. DM awter 400 Water Loss 393 2. Benzoic Acid 427 Material Loss 32 3.

Caustic Soda 70 Sodium Benzoate 472

Total 1164 1164

4. Manufacturing Process Of DICLOFENAC SODIUM

Process First charge D M water and Diclofenec Sodium Tech in S.S. reactor and dissolved it. Then add Carbon and reflex for 1 hrs. Then filter the solution. Then start cooling when the material at room temperature. Then material is taken for centrifuge. Then start drying. After drying analysed the material. Then pack the material.


Reaction Flow


1500 kgs

1505kgs

Packing 475 kgs

475 kgs

Drying 485 kgs

485 kgs

Centrifuge 575 kgs

575 kgs

Evoparation 1300 kgs

1300 kgs

Filteration 1305 kgs

30 kgs material +60 kgs water (ml used in next batch)

Water loss 200 kgs

10 kgs Water loss

Diclo fenec Sodium Tech 500 kgs D M Water 1000 kgs

S S Reactor 1500 kgs

Treat with Carbon (1 hour) Reflux

Carbon 5 kgs

Carbon loss 5 kgs

Heating 100°

1500 kgs

Water loss 725 kgs

Mass Balance

SR. NO.



1. Diclofenac Sodium 500 Water loss 935 2. D M water 1000 Carbon Loss 5 3.

Carbon 5 Material + Water 90

4. Diclofenac Sodium 475

Total 1505 1505

5. Manufacturing Process Of DICLO FENAC POTASSIUM

Process First charge D M water and 2-6-Dichloro Phenyl in S S reactor and dissolved it. Then add carbon and reflex for 1 hrs. Then filter the solution. Then start evaporation then the material at room temperature. Then material is taken for centrifuge. Then start drying. After drying analyzed the material. Then pack the material.


Reaction Flow

Process flow diagram

1500 kgs

1305kgss

Packing 475 kgs

475 kgs

Drying 485 kgs

485 kgs

Centrifuge 1200 kgs

1200 kgs

Cooling 1200 kgs

1200 kgs

Filteration 1305 kgs

1500 kgs

Heating 1500 kgs

25 kgs Material loss 690 kgs water loss is recycled in next batch

200 kgs Water loss

10 kgs Water loss

Diclofenec Potassium Tech 500 kgs D M Water 1000 kgs


Carbon 1 hours Reflex 1505 kgs

Carbon 5 kgs

Carbon loss 5kgs Water loss 100kgs

Mass Balance

SR. NO.



1. Diclofenac Potassium Tech 500 Water loss 310

2. D M Water 1000 carbon 5 3.

carbon 5 Material + water 715

4. Diclofenac Potassium 475

Total 1505 1505

6. Manufacturing Process Of ERYTHROMYCIN STEARATE

Process First charge MDC & Erythromycin Thio Cynate in S.S. reactor. Start slowly addition of liquid Ammonia & D M water. After addition is complete, separate Methylene Di Chloride layer. Charge Methylene Di Chloride for distillation to get Erythomysin base. Then dissolve Acetone in Erythromycine base. Start addition of Stearic Acid &heat the material at 50°c for 2hrs. Start cooling in reactor when the material is at room temp. Then Erythromycin Stearate is centrifuge and dried. Pulverise the material & analysed. Then pack the material.


Reaction Flow



1396 kgs

L.Ammonia-8.5 kgs D M Water-100 kgs

Addition 1504.5 kgs

MDC loss-49.5 kgs MDC received -950 kgs (Used in next batch)

505 kgs

Seperation 505 kgs

367 kgs

Ammonium thiocynate -38 kgs Water – 100 kgs

Acetone- 250 kgs

Erythromycin Base-617 kgs

617 kgs

Stearic acid- 142 kgs

Heating at 250°C For 2 hrs 759 kgs

759 kgs

Cooling 759 kgs

759 kgs

Acetone loss-10 kgs Acetone received-238 kgs

Centrifudge 759 kgs

Drying 511 kgs

Acetone loss -2 kgs

509 kgs

Pulverising 509 kgs

509 kgs

Erythromycin stearate 509 kgs

Erythromycin thio cynate- 396 kgs MDC-1000 kgs

Mass Balance

SR. NO.



1. Erythromycin thio cynate 396 MDC Loss 49.5

2. MDC 1000 MDC received 950 3.

Acetone 250 Ammonium thiocynate 38

4. Stearic acid 142 waste water 100 5. L. Ammonia 8.5 Acetone loss 12 6.

D.M Water 100 Acetone recovered 238

7. Erythromycin Stearate 509

Total 1896.5 1896.5

7. Manufacturing Process Of L-LYSINE MONOHYDROCHLORIDE

Process First charge D M Water and L-Lysine Monohydrochloride in S S reactor. Then heat the material at 60°c to 80⁰c. Then filter the material. Then start evaporation at 100⁰c for 2 to 3 hrs. Then material is taken for centrifuge. Then material is taken for drying. Then start pulverizing. After pulverizing analyze the material. Then pack the material.


Reaction Flow

Process flow diagram:


Heating 60⁰ to 80⁰ 1005 kgs

1000 kgs

1005kgs

Filter 1005kgs

Evaporation 1000 kgs

1000 kgs

Centrifuge 550 kgs

Drying 490 kgs

Pulverising 480 kgs

550 kgs

Packing 472 kgs

Water loss 450 kgs

40 kgs Water loss 20 kgs Material loss ( M L used in next batch)

Water loss 10 kgs

D M water 500kgs L-Lysine mono 500 kgs

Activeted carbon 5 kgs

Activated carbon 5kgs

490 kgs

480 kgs

480 kgs

Mass Balance

SR. NO.



1. Water 500

Waste Activated Carbon 5

2. L-Lysine mono 500 Evaporation Loss 500 3. Activated Carbon 5 Mother Liquor 20 4. L-Lysine

Monohydrochloride 480 Total 1005 1005

8. Manufacturing Process Of FLUCONAZOLE

Process First charge D M Water and Fluconazole Tech in S S reactor. Then heat the material at 60°c for 2 hrs& then add carbon. Then filter the solution. Then start evaporation. Then material is taken for centrifuge. Then material is taken for drying. Then start pulverizing. After pulverizing analyze the material. Then pack the material. The mother liquor obtained is recycled in the next batch.

Reaction Flow


Heat the solution 60⁰C 665 KGS

660 kgs

665 kgs

Activated Carbon 5 kgs loss Filtration 665 kgs

660 kgs

Cooling 295 kgs

25 kgs Water 10 kgs Material (ml used in next batch)

295 kgs

Centrifuge 295 KGS

260kgs

10kgs Water loss Drying 260 kgs

250 kgs

Pulverizing 250 kgs

250 kgs

Packing 250 kgs

Fluconazole Tech 260 KGS D M Water 400KGS

S S Reactor 660 kgs

Evaporation 660 kgs

295 kgs

Activated Carbon 5 kgs

365 kgs Water loss

Mass Balance

SR. NO.



1. Fluconazole Technical 260

Waste Activated Carbon 5

2. Water 400 water loss 375 3.

Activated Carbon 5 Material + water 35

4. Fluconazole 250 Total 665 665

9. Manufacturing Process Of CARBOMER

Process First charge Ethyline Di Chloride in S.S. reactor. Then add slowly Acralic Acid. Heat the material about 60°c temperature for 4 hrs. Then start cooling in reactor at room temperature. Then obtain Carbomer material is centrifuge. Then material is taken for drying. After drying material is analyzed. Then pack the material.


Reaction Flow

CH2

OH

OCl

Cl+

Ethylene DichlorideAcrylic Acid


Mass Balance

SR. NO.



1. Acralic Acid 500 EDC reused 950 2. Athyline di chloride 1000 EDC loss 30 3. Material loss 20 4. Carbomer 500

Total 1500 1500

1500 kgs

Heat the Material 60⁰C 1007.5kgs

1500 kgs

Reflex 4HRS 1500 kgs

1500kgs

Cooling at RT 1500 kgs

950 kgs EDC Reused in next batch EDC loss 30 kgs loss

1500 kgs

Centrifuge 1500 kgs

520 kgs

20 kgs Material loss Drying 520 kgs

Packing 500 kgs

500 kgs

Acralic Acid 500 Ethylene Di Chloride 1000KGS


10. Manufacturing Process Of DI SULFIRAM

Process First charge Tetra Ethyl Thiorium Di Sulphide and IPA in S.S. reactor. Then heat the material at 60° c for 2 hours the material is dissolved. Then start cooling when the material is at room temp. Then material is taken for centrifuge. Then material is taken for dried. Then material is taken for pulverized. After pulverizing, the material is taken for analysis. Then pack the material. The mother liquor obtained is recycled in the next batch.

Reaction Flow


Mass Balance

SR. NO.



1. Tetra ethyl Thorium Di Sulphide 500 IPA reused 25

2. Iso Propyl Alcohol 800 IPA lost 10 3. Materials 790 4. Di Sulfuram 475

Total 1300 1300

Tetra Ethyl Thiorium Disulphide 500 kgs IPA 800 kgs

1300 kgs


Packing 475 kgs

475 kgs

Pulverising 475 kgs

475 kgs

Drying 485 kgs

485 kgs

Centrifuge 1280 kgs

1300 kgs

Cooling 1300 kgs

1300 kgs

Heating 60⁰C for 2 hours

Material 790 kgs IPA 25 kgs used In next batch

10 kgs IPA loss

11. Manufacturing Process Of NIACINAMIDE

Process First charge D M Water and 3-Cyano Pyridine in S S reactor. Then add NaOH solution of clear solution of 3-Cyano Pyridine below 80°c. Evaporate water after complete addition of Sodium Hydroxide from the solution. The reaction mass is cooled to R.T. to get Niaciamide. The obtained Niaciamide is centrifuged. The obtained Niaciamide is dry.

The obtained Niaciamide is pulverise. After getting analysed.

Material is taken for packing. The mother liquor obtained is recycled in the next batch.

Reaction Flow

N

CN

OH2

Hydrolysis

N

C

O

NH2+ OH2

3 Cyanopyridine Niacinamide

Water


Mass Balance

SR. NO.



1. Water 500 Water loss 421.5 2. 3 cyno pyridine 500 Mother liquor 36 3. NaOH 7.5 Niacinamide 550

Total 1007.5 1007.5

1000 kgs

Packing 550 kgs

5550 kgs

Drying 560kgs

560 kgs

Centrifuge 636 kgs

636 kgs

Evaporation 636 kgs

636 kgs

Evaporation 1007.5 kgs

1007.5 kgs

Addition below 80⁰C 1007.5kgs

36 kgs Material 40 kgs Water (ml used in next batch)

10 kgs Water loss

NaOH 7.5 kgs

D M Water 500kgs 3 cyno pyridine 500kgs


Water loss 371.5 kgs

12. Manufacturing Process Of SODIUM CITRATE

Process First charge D M Water and Citric Acid in S.S. Reactor. When Citric Acid should be

dissolved. Then add slowly Caustic Soda under stirring. Then maintain ph 6.0 to 6.5 of this solution. After that start evaporation of the solution. The obtained Sodium Citrate material is taken for centrifuge. Then start drying for 3 hrs. After drying, material is taken for analysis. Then pack the material. The mother liquor obtained is recycled in the next batch.

Reaction Flow

C COOH

COOH

COOH

OH + NaOH C COONa

COONa

COONa

OH + 3H2O

Citric Acid Sodium Hydroxide Sodium Citrate

Water


Mass Balance

SR. NO.



1. Water 400 Water loss 506 2. Citric Acid 410 Mother Liquor 20 3. Caustic Soda 256 Sodium Citrate 540

Total 1066 1066

D M Water 400kgs Citric Acid 410kgs

810 kgs

S S Reactor 810 kgs

Packing 540 kgs

540 kgs

Drying 550kgs

550 kgs

Centrifuge 610 kgs

610

Evaporation 1066kgs

1066

Maintain Ph 6.0 to 6.5

1066 kgs

Stirring 1066kgs

10 kgs Water loss

Caustic Soda 256 kgs

Water loss 456 kgs

Material 20 kgs Water 40 kgs (ml used in next batch)

13. Manufacturing Process Of TRI METHYL SULPHOXONIUM IODIDE

Process First charge Di Methyl Sulphoxide in reactor. Start addition of Methyl Iodide & heat the material at 40°c temp. Reflex for 60 hrs. Start cooling when the material is at room temp. Trimethyl Sulphoxonium Iodide is received. Above material is taken for centrifuged & drying After drying material is analyzed & pack the material. The mother liquor obtain is recycled in the next batch.

Reaction Flow

S+

CH3 CH3CH3

OI-

+ CH3ISCH3

CH3

O

Dimethyl sulfoxide Methyl Iodide Trimethylsulfoxonium Iodide


Mass Balance

SR. NO.



1. Dimethyl Sulphoxide 1000

Dimethyl Sulphoxide Received 570

2. Methyl Iodide 1000 Dimethyl Sulphoxide loss 30 3. Trimethyl Sulphoxonium

Iodide 1400 Total 2000 2000

Dimethyl sulphoxide-1000kgs


1000 kgs

Methyl Iodide -1000 kgs

Heating 40°c 2000 kgs

2000 kgs

Reflux 60 hrs 2000 kgs

2000 kgs

Cooling 2000 kgs

2000 kgs

Centrifuged 2000 kgs

1430 kgs

Drying 1430 kgs

1400 kgs

Trimethyl sulphoxonium iodide 1400 kgs

Dimethyl sulphoxide loss -30 kgs

Dimethyl sulphoxide received -570 kgs (Used in next batch)

14. Manufacturing Process Of 2-(7-methoxynaphthalen-1-yl)acetic acid

Process First charge 2-(7-Methoxynaphthalen-1-yl)Acetic Acid technical and Ethyl Acetate in S.S.

reactor. Then heat the material at 70°C for 2 hours. When the material is dissolved. Then start cooling when the material is at room temp. The material is taken for centrifuge. The material is taken for dried. The material is taken for pulverised. After pulverising, the material is taken for analyse. Then pack the material. The mother liquor obtained is recycled in the next batch. The solvent is recovered by distillation is reused in next batch.

Reaction Flow

CH3

OOH

O

2-(7-Methoxynaphthalen-1-yl)Acetic Acid

CH4


Mass Balance SR. NO.



1. 2-(7-methoxynaphthalen-1-yl)acetic acid TECH 55 Ethyl Acetate reused 135

2. Ethyl Acetate Recovered 135 Ethyl Acetate lost 15

3. Ethyl Acetate Fresh 15 Materials 5 4. 2-(7-methoxynaphthalen-

1-yl)acetic acid 50 Total 205 205

205 kgs

S S Reactor 205 kgs

Packing 50 kgs

50 kgs

Pulverising 50 kgs

50 kgs

Drying 50 kgs

55 kgs

Centrifuge 55 kgs

205 kgs

Cooling 205 kgs

205 kgs

Heating 70⁰C for 2 hours

Material 5 kgs used in next batch Ethyl Acetate135 kgs Recovered Ethyl Acetate Loss 10 KG

5 kgs Ethyl Acetate loss

2-(7-methoxynaphthalen-1-yl) acetic acid Technical 55 kgs Ethyl Acetate 150 kgs

BY-PRODUCTS

1. Manufacturing Process Of Sodium Chloride

Process First charge D M Water and Sodium Chloride in S S Reactor. Start heating at 60°c to 80⁰c. Filter the material. Start Evaporation at 100⁰c for 2 to 3 hrs. The material is taken for drying. After drying analyzed the material. Then pack the material.



S S Reactor 318 kgs


318 kgs

318 kgs

Filter 318 kgs

Evaporation 318 kgs

318 kgs

Drying 133 kgs kgs

133 kgs

Packing 116 kgs

Water loss 185 kgs

Water loss 17 kgs

D M water 146 kgs Sodium chloride 116 kgs + WW 56 kgs

116 kgs

Mass Balance

SR. NO.



1. Wastewater 56 Water Loss 202 2.

DM Water 146 Sodium Chloride 116

3. Sodium Chloride 116 Total 318 318

2. Manufacturing Process Of Ammonium Thiocynate

Process First charge water and Ammonium Thiocynate in S S Reactor. Start heating at 60°c to 80⁰c. Filter the material. Start evaporation at 100⁰c for 2 to 3 hrs. The material is taken for drying. After drying analyzed the material Then pack the material. The mother liquor obtained is recycled in the next batch.


S S Reactor 414 kgs

414 kgs


414 kgs

Filter 414 kgs

414 kgs

Evoparation 414 kgs

Drying 139kgs

139 kgs

Packing 114 kgs

Water loss 275 kgs

Water loss 25 kgs

Water 300 kgs Ammonium thiocynate 114 kgs

114 kgs

Mass Balance

SR. NO.



1. Waste-Water 300 Water loss 300 2. Ammonium

Thiocynate 114 Ammonium Thiocynate 114

Total 414 414

3. Manufacturing Process Of Sodium Bromide

Process First charge D M Water and Sodium Bromide in S S Reactor. Start heating at 60°c to 80⁰c. Filter the material. Start evaporation at 100⁰c for 2 to 3 hrs. The material is taken for drying. After drying analyzed the material Then pack the material.



S S Reactor 231 kgs


231 kgs

231 kgs

Filter 231 kgs

Evaporation 231 kgs

231 kgs

Drying

113 kgs

Packing 103 kgs

Water loss 118 kgs

Water loss 10 kgs

D M water 100kgs Sodium bromide 131 kgs

103 kgs

Mass Balance

SR. NO.



1. DM water 72 Water loss 128 2.

Waste water 28 Sodium Bromide 103

3. Sodium bromide 131 Total 231 231

LIST OF RAW MATERIALS (EXISTING)

SR. NO. NAME OF THE RAW MATERIAL QUANTITY

MT/M

1 Iodine crude 7.5

2 Caustic Potash 3.75

3 Formic Acid 1.65

4 Ferrous Sulphate crystal 13.62

5 Zinc Sulphate crystal 17.02

6 Ammonium Chloride Tech. 50.00

7 Distilled water 81.12

LIST OF RAW MATERIALS (PROPOSED)

Sr. No. Name of the product Name of Raw Materials

Quantity

Kg/Month

Products

1 DI ETHYL CARBAMYZINE CITRATE

Toluene 210

N-Methyl Piperazine 2100

Sodium hydroxide 1100

Di ethyl carbamyl chloride 2900

Acetone 425

Carbon 45

Citric acid 4100

2 Diphen Hydramine Dichloride

Diphenyl Methane Bromide 4100

Toluene 260

Sodium Hydroxide 900

Dimethyl Amino ethanol 1600

Carbon 100

IPA 175

HCL 620

3 Sodium Benzoate Benzoic Acid 18100


4 Diclofenac Sodium Diclofenac Sodium Technical 10500

Carbon 110

5 Diclofenac Potassium Diclofenac Potassium Technical 5300

Carbon 55

6 Erythromycin Stearate

Erythromycin thio cynate 3900

MDC 495

Acetone 120

Stearic acid 1400

L. Ammonia 85

7 L-Lysine Monohydrochloride

L-Lysine mono 10500

Activated Carbon 100

8 Fluconazole Fluconazole Technical 2100

Activated Carbon 40

9 Carbomer Acrylic Acid 10000

Ethylene di chloride 1000

10 Di Sulfuram Tetra ethyl Thorium Di Sulphide 5300

Iso Propyl Alcohol 425

11 Niacinamide 3 cyno pyridine 19000

NaOH 280

12 Sodium Citrate Citric Acid 30400


13 Trimethyl Sulphoxonium Iodide

Dimethyl Sulphoxide 7200

Methyl Iodide 7200

14 2-(7-methoxynaphthalen-1-yl)acetic acid

2-(7-methoxynaphthalen-1-yl)acetic acid TECH 330

Ethyl Acetate 90

1. Resource optimization/ recycling and reuse envisaged in the project, if any,

should be briefly outlined.

Our main raw materials are easily available from developmental city like Baroda,

Surat, etc.

2. Availability of water its source, Energy/ power requirement and source

should be given.

Water source: Bore well Energy/power requirement: 100 HP from GEB

3. Quantity of wastes to be generated (liquid and solid) and scheme for their

Management/disposal.

• Solid waste generation and disposal

Sr. No.

Name of the waste

Category Existing Quantity/

Month

After Expansion Quantity/

Month

Mode of disposal

1 Used oil /Spent Oil

5.1 0.1 MT/ Year

0.1 MT/ Year

Collection, storage and Use within premises as a lubricant/ sell to registered recycler

2 Discarded Plastic bags/Drums

33.3 0.5 MT 3.5 MT Collection, storage and decontamination or Reuse within premises/ sell to approved scrap vendor

3 Spent Carbon 28.2 -- 0.2 MT Collection, storage and Disposal at TSDF Site

4. Process Residue

28.1 -- 0.05 MT Collection, storage and Disposal at TSDF Site

5. ETP Sludge 33.4 -- 0.15 MT Collection, storage and sent to TSDF Site.

• Waste water generation and Disposal facility

200 liters waste water will be generated from the daily washing activity.

Flow Diagram of ETP.

ETP Sludge to be sent to TSDF site

SteamJacketed

Evaporator

To Atmosphere

Port Hole

Collection cum Neutralization

Tank

Nutch Filter /Filter Press

Effluent from

Washing

4. Schematic representations of the feasibility drawing which give

information of EIA purpose.

The applicability of the S.O 1533 for the proposed project was explored by considering different possibilities & provision made in the said notification. Considering the products & project location of the proposed project it is noticed that the proposed project falls under Category 5 (f) “A” of the Schedule-I of EIA Notification SO 1533. As per the provision of the SO 1533, it is necessary to get Environmental Clearance by applying to MoEF along with the Environmental Impacts Assessment Study Report for the proposed project prior to commissioning of the project activities. Therefore the EIA is required to conduct to comply with provisions of SO 1533 made for Category 5(f) “A” of schedule –I of the notification.

4. Site Analysis

(i) Connectivity.

Nearest Railway

station Sanand 4.88 Km

Nearest National

highway NH 8C 16 Km

Nearest Airport Ahmedabad 29.5 Km

Nearest State highway SH 17 0.29 Km

(ii) Land Form, Land use and Land ownership.

Fig: 1 Land use pattern

Land possession document are attached as annexure: A.

(iii) Topography (along with map).

Fig: 2 Legendry map of Ahmedabad district

(iv) Existing land use pattern.

Existing land use pattern shown in fig no: 1

Project site

(v) Existing Infrastructure.

(1) Nearest railway station: Sanand Railway station is 4.88 Km from the project site

(2) Nearest Highway: State Highway 17 is 0.29 km from the project site. (3) Nearest Airport: Ahmedabad is 29.5 km from the project site. (4) Power: 100 HP from Gujarat Electricity Board. (5) Water : Source of the water is Ground water (6) Basic amenities:

• Educational facility: - Indus University is at 11.8 km from the project site.

• Hotel: Krishna Leela Hotel is 4.6 km away from the project site.

• Post Office: - Post office, Nr NH-8A, S.G Highway is 15.9 km away from the project site.

• Hospital: - Krishna Shalby Hospital is 10.4 km away from the project site.

(vi) Soil classification of district Ahmedabad

In this region, major area falls into 'very deep' soil. However, ‘deep’ soil is in few area of

Ahmedabad district. There are 'moderately deep' soils in few area of Ahmedabad. A

major texture of the soil in the region is 'Loamy'. However, in South-West part (in

Ahmedabad and Surendranagar district) a soil texture in few areas is found to be

'Clayey'.

In few area of middle part of Ahmedabad district is 'Slightly Saline'. A considerable area

of a southern part of Ahmedabad district is representing 'Moderate’ salinity of the soil.

Very few area have 'Severe’ saline soil in Southern part of Ahmedabad district.

Slight sodicity is found in central part of the region (Ahmedabad district). In west part of

the Ahmedabad district region 'Moderate’ to ‘strong‘ sodicity of the soil is found.

(vii) Climatic data from secondary sources.

METEOROLOGICAL CENTRE, AHMEDABAD

DAILY METEOROLOGICAL DATA

STATION:- AHMEDABAD YEAR: - 2014 MONTH: - JUNE

ELEMENTS: - (1) WIND DIRECTION & (2) WIND SPEED REPORTED IN KMPH

DATE 0830 HRS IST 1730 HRS IST 0230 HRS IST 0530 HRS IST 1130 HRS IST 1430 HRS IST 2030 HRS IST 2330 HRS IST

DIR SPD DIR SPD DIR SPD DIR SPD DIR SPD DIR SPD DIR SPD DIR SPD

01 WSW 006 SW 006 CALM 000 W 004 WSW 010 SW 006 SW 016 SW 006

02 SW 006 NNE 030 SW 006 CALM 000 SW 006 SW 008 CALM 000 VRB 008

03 NW 004 CALM 000 CALM 000 CALM 000 SW 006 CALM 000 CALM 000 SW 014

04 CALM 000 SW 006 CALM 000 SW 006 CALM 000 SW 004 SW 018 S 018

05 SW 008 SW 006 SW 014 SW 008 SW 008 SW 010 SSW 018 SW 008

06 SW 006 W 008 SW 012 CALM 000 SW 006 WSW 012 SSW 018 SSW 016

07 WNW 006 SW 006 SSW 008 W 006 SW 008 SW 006 SW 006 SW 012

08 SW 008 S 012 SW 006 SW 004 SW 008 SW 016 SW 010 SW 016

09 SW 014 SW 006 SW 012 SW 010 SW 010 SW 012 SSW 018 SSW 018

10 SW 008 SW 014 SW 010 SW 006 SW 006 SW 006 SSW 018 SSW 018

11 SW 008 S 028 SSW 020 SSW 018 SW 010 S 014 SW 016 SW 014

12 S 008 S 018 S 006 S 016 S 012 SSW 018 SW 010 S 012

13 S 010 S 014 SW 010 SW 012 SSW 012 S 010 SW 018 SW 014

14 SW 010 S 012 SW 012 SW 012 SW 010 SW 010 SW 010 SW 012

15 SW 010 S 016 SW 012 SW 012 SW 010 S 012 S 016 S 014

16 SSW 010 SSE 012 SW 012 S 014 S 012 SSE 012 SW 012 SW 008

17 SSW 010 SW 012 S 012 SW 006 SSW 008 W 008 SW 010 SW 008

18 SW 008 SW 012 SW 010 SW 010 SW 008 S 006 S 016 S 016

19 SW 008 S 010 S 018 SSW 018 SW 010 SW 010 S 014 S 014

20 SW 010 SSW 016 S 014 S 012 SW 012 SW 012 SW 012 SW 016

21 SSW 014 S 014 S 016 SW 016 SSW 014 SW 010 S 016 SW 024

22 SW 012 SW 014 SW 014 SSW 014 SW 018 SW 012 SSW 022 SW 020

23 SW 010 SW 012 SW 020 SSW 018 SW 010 SW 014 SW 012 SW 010

24 SW 008 WSW 014 SW 010 SW 014 SW 012 SW 016 SW 010 W 008

25 SW 010 SW 010 SW 012 S 010 SW 010 SW 008 SW 014 SW 016

26 SW 006 W 012 SW 012 SW 018 SW 008 W 010 SSW 016 WSW 008

27 W 010 WSW 012 WSW 008 SW 010 W 010 W 012 SW 010 SW 010

28 W 012 W 008 WSW 010 WSW 008 W 010 WSW 012 SW 010 W 008

29 WSW 012 WSW 014 WSW 012 SW 010 WSW 014 WSW 012 SW 012 W 014

30 WSW 010 SW 012 WSW 012 SW 006 WSW 012 SW 012 WSW 010 W 010

METEOROLOGICAL CENTRE , AHMEDABAD.

DAILY METEOROLOGICAL DATA

STATION: - AHMEDABAD YEAR:- 2014 MONTH:- JUNE

ELEMENT: - RELATIVE HUMIDITY IN % (PERCENTAGE)

DATE 0830 HRS IST

1730 HRS IST

0230 HRS IST

0530 HRS IST

1130 HRS IST

1430 HRS IST

2030 HRS IST

2330 HRS IST

1 070 036 066 078 053 038 043 060 2 069 031 072 076 051 038 036 039 3 056 028 051 057 042 035 039 059 4 050 023 069 066 043 027 053 061 5 067 025 070 079 039 028 043 056 6 055 028 066 054 041 031 048 070 7 062 026 075 071 047 031 053 070 8 060 028 067 067 042 024 055 069 9 061 022 051 062 042 030 049 066

10 063 038 065 069 050 044 047 060 11 070 042 057 067 056 043 060 068 12 069 042 071 075 044 040 062 063 13 061 041 065 071 045 046 067 059 14 067 046 069 075 051 040 061 064 15 067 053 069 079 049 045 066 074 16 069 059 076 078 057 050 064 070 17 072 070 078 078 059 053 070 074 18 071 048 081 076 054 045 059 071 19 069 042 075 081 049 046 056 067 20 069 042 066 071 050 040 065 067 21 067 052 063 071 049 039 063 056 22 066 042 065 071 049 040 043 054 23 064 038 064 069 047 040 051 054 24 067 034 063 069 049 036 050 061 25 065 035 068 065 045 040 039 051 26 066 033 064 070 049 035 055 057 27 068 039 066 067 049 043 052 067 28 069 032 066 071 051 038 053 053 29 066 038 073 071 046 038 054 055 30 066 034 066 068 048 044 045 056

5. Planning Brief

(i) Planning Concept (type of industries, facilities transportation etc) Town

and Country Planning/Development authority Classification.

It is a Pharmaceutical Drugs manufacturing industry located in Ahmedabad

district. Total available area is 1987 sq. meter out of it 720 sq. meters area

will be provided as a greenbelt area.

(ii) Population Projection

In 2011, Ahmadabad had population of 7,214,225 of which male and female were 3,788,051 and 3,426,174 respectively. In 2001 census, Ahmadabad had a population of 5,816,519 of which males were 3,074,556 and remaining 2,741,963 were females. Ahmadabad District population constituted 11.94 percent of total Maharashtra population. In 2001 census, this figure for Ahmadabad District was at 11.48 percent of Maharashtra population.

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

Sr no. Name Area in Sq Mtr

% of Total Area

1 Process Area 180.00 9.06 2 Raw Material Godown 55.00 2.77 3 Product Godown 70.00 3.52 4 Sampling/testing and Other production area 40.00 2.01 5 Utilities - Boiler+Water 14.00 0.70 6 Electric Room +RO Dm room 8.00 0.40 7 Hazardous Waste Storage Area 20.00 1.01 8 Effluent Treatment Plant 25.00 1.26 9 Administrative Building 55.00 2.77

10 Security Cabin 10.00 0.50 11 Road 200.00 10.07 12 Parking 40.00 2.01 13 Green Belt 720.00 36.24 14 Open Space 550.00 27.68

Total 1987.00

(iv) Assessment of Infrastructure Demand (Physical & Social).

Secondary Education required in nearby Villages.

Proposed Infrastructure

(i) Industrial Area

Industry will provide 477 square meters built up area for industrial process

activity. Which provide all needed facility including proper ventilation, safe

handling system, etc.

(ii) Residential Area

Industry will provide labor quarter for some of their labors & will provide all

basic facilities to them.

(iii) Green Belt.

720 sq. meter area will be proposed for greenbelt development. Approx 360

sq. mt area will be proposed for tree cover area (approx 540 trees).

(iv) Social Infrastructure.

• The PP proposes the following social infrastructure facilities within 10.0 km periphery of the proposed project.

• Education Facilities:-Many Facilities for village schools like game kits, drawing kits, table-chairs; school construction (classroom/toilet/school boundary), ceiling fans/ coolers or books for school library are proposed.

• Health Facilities:-The PP proposes to provide assistance to existing

health facilities in Nearest Hospital, for improvement in health facilities or services.

(v) Connectivity

The nearest Town is Sanand. Approaching road state highway no 17 is 0.29 km

away from the project site.

(vi) Drinking Water Management

Existing use of water is 3.75 KL/day. After Expansion, Out of 9.41 KL/day water approx 0.9 KL/day water will be consumed for domestic purpose; 1.26 KL/day water will be consumed for green belt development and 7.25 KL/ day fresh water will be used for industrial purpose.

(vii) Sewerage System.

Domestic waste water 0.8 KL/day will be treated disposed in soak pit via septic

Tank.

(viii) Industrial Waste Management.

200 liter/day waste water will be generated from the washing activity. It will

be treated in effluent treatment plant and evaporate after treatment.

(ix) Solid Waste Management

Used oil, ETP waste, discarded bags are the main solid hazardous waste

generated from the proposed unit. Used oil will be send to register recycler,

ETP sludge will collected from sludge drying bed, stored into solid waste

storage area and disposed to authorized TSDF site. Discarded bags will be sold

to approved vendor.

(x) Power Requirement & Supply / source

Electricity will be obtained in tune of 100 HP from GEB.

6. Project Schedule & Cost Estimates

Construction already exists.

Likely to start installation of machinery in 1st week of December.

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

project.

Existing Cost: 0.45 Crore,

Proposed Expansion: 3.55 Crores,

Total after Expansion: 4 Crores.

Documents

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