Post on 01-Jul-2018
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: aries_lab2013@yahoo.in
Prepared By:
T. R. ASSOCIATES C-605/A, Ganesh Meridian, Opp. Kargil Petrol Pump,
S. G. Highway, Ahmedabad.
Mo. No.: 98253 71099
Email ID: trassociates@hotmail.com;
trassociates@ymail.com
June 2015
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
Process Flow Diagram:
SS Reactor DM Water
Stirring till the crystals dissolves
Filtration
Evaporation
Centrifugation
Drying
Pulverizing
Analyzing and Packing
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
Process Flow Diagram:
SS Reactor DM Water
Heating
Filtration
Evaporation
Centrifugation
Drying
Analyzing and Packing
Ammonium Chloride Tech
Mother Liquor is recycled in next batch.
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.
Process Flow Diagram:
SS Reactor Formic Acid
Filtration
Concentrated
Centrifugation
Drying
Analyzing and Packing
Iodine Crude Caustic Potash
Mother Liquor is recycled in next batch.
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
Process Flow Diagram:
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
Process Flow Diagram:
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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
The mother liquor obtained is recycled in the next batch.
Reaction Flow
Process Flow Diagram
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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
The mother liquor obtained is recycled in the next batch.
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
S S Reactor 1500 kgs
Carbon 1 hours Reflex 1505 kgs
Carbon 5 kgs
Carbon loss 5kgs Water loss 100kgs
Mass Balance
SR. NO.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
The mother liquor obtained is recycled in the next batch.
Reaction Flow
Process Flow Diagram
S S Reactor 1396 kgs
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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
The mother liquor obtained is recycled in the next batch.
Reaction Flow
Process flow diagram:
S S Reactor 1000 kgs
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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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
Process Flow Diagram
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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
The mother liquor obtained is recycled in the next batch.
Reaction Flow
CH2
OH
OCl
Cl+
Ethylene DichlorideAcrylic Acid
Process Flow Diagram
Mass Balance
SR. NO.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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
S S Reactor 1500 kgs
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
Process Flow Diagram:
Mass Balance
SR. NO.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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
S S Reactor 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
Process Flow Diagram
Mass Balance
SR. NO.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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
S S Reactor 1000 kgs
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
Process Flow Diagram:
Mass Balance
SR. NO.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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
Process Flow Diagram:
Mass Balance
SR. NO.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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
S S Reactor 1000 kgs
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
Process Flow Diagram:
Mass Balance SR. NO.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
The mother liquor obtained is recycled in the next batch.
Process Flow Diagram:
S S Reactor 318 kgs
Heating 60⁰ to 80⁰ 318 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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
Process Flow Diagram:
S S Reactor 414 kgs
414 kgs
Heating 60⁰ to 80⁰ 414 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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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.
The mother liquor obtained is recycled in the next batch.
Process Flow Diagram:
S S Reactor 231 kgs
Heating 60⁰ to 80⁰ 231 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.
INPUT QTY PER BATCH (KG)
OUTPUT QTY PER BATCH (KG)
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
Sodium hydroxide 3000
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
Sodium hydroxide 19000
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.