enclosure: 1 -...

Enclosure: 1

Product Detail

Sr. No. Product Name Existing

(MT/Month) Proposed

(MT/Month)

Total After expansion

(MT/Month) 1 NORMAL BUTYL BROMIDE 20 40 60 2 NORMAL PROPYL BROMIDE 4 56 60 3 ETHYL BROMIDE 2 5.5 7.5 4 ISO PROPYL BROMIDE 1.5 6 7.5 5 1:3 DI BROMO 5:5 DI METHYL

HYDENTOIN 15 -- 15

6 TETRA BUTYL AMMOMIUM TRI BROMIDE -- 1 1

7 CETYL BROMIDE -- 1.5 1.5 8 OCTYL BROMIDE -- 1.5 1.5 9 SODIUM BROMIDE POWDER -- 0.5 0.5 10 SODIUM BROMIDE SOLN. -- 30 30 11 POTTASIUM BROMIDE POWDER -- 0.5 0.5 12 LIQUID BROMINE -- 25 25

TOTAL 42.5 167.5 210

Enclosure: 02

Packing & Final Use of Products

Sr. No. Name of proposed products Final application of products Type of packing

1 NORMAL BUTYL BROMIDE

Production of phase transfer

catalyst and other Pharmaceutical

industry

HDPE barrel

2 NORMAL PROPYL BROMIDE



industry

HDPE barrel

3 ETHYL BROMIDE



industry

HDPE barrel

4 ISO PROPYL BROMIDE



industry

HDPE barrel

5 1:3 BROMO 5:5 DI METHYL HYDENTOIN

Pharmaceutical industry as green brominating agent

HDPE Carboys

6 TETRA BUTYL AMMOMIUM TRI BROMIDE

Pharmaceutical industry as green brominating agent

Fibre drum

7 CETYL BROMIDE Production of phase transfer

catalyst HDPE barrel

8 OCTYL BROMIDE Production of phase transfer

catalyst HDPE barrel

9 SODIUM BROMIDE POWDER For the

pharmaceutical industries

HDPE bags

10 SODIUM BROMIDE SOLN. For the

pharmaceutical industries

HDPE barrel

11 POTTASIUM BROMIDE POWDER For the

pharmaceutical industries As above

HDPE bags

12 LIQUID BROMINE Self consumption Glass bottles in

set of six in plastic or wooden crates

Enclosure: 3

Product Wise Raw Material

Sr.No. Product Name Quantity (MT/Month)

Raw Material Name

Total Quantity MT/Batch MT/Month

1. NORMAL BUTYL BROMIDE 60 N. Butanol 0.625 37.5 Liq. Bromine 0.675 40.5 Sulfur 0.045 2.7

2. NORMAL PROPYL BROMIDE 60 N. Propanol 0.513 30.78 Liq. Bromine 0.750 45 Sulfur 0.050 3

3. ETHYL BROMIDE 7.5 Ethanol 0.510 3.825 HBr 2.060 15.45 Sulfuric Acid 1.400 10.5

4. ISO-PROPYL BROMIDE 7.5 Iso-Propanol 0.550 4.125 HBr 1.725 12.937 Sulfuric Acid 1.175 8.81

5. 1:3 DI BROMO 5:5 DI METHYL HYDENTOINE 15

DMH 0.334 5.01 Liq. Bromine 0.434 6.510 Chlorine Gas 0.200 3.00 Soda Ash 0.420 6.3

6. TETRA BUTYL AMMOMIUM TRI BROMIDE 1

TBAB 0.675 0.675 Liq. Bromine 0.350 0.350 HBr 0.100 0.100

7. CETYL BROMIDE 1.5

Cetyl Alcohol 0.810 1.215 Liq. Bromine 0.295 0.442 Red Phosphorous 0.022 0.033 Sulfuric Acid 0.130 0.195

8. OCTYL BROMIDE 1.5

Octyl Alcohol 0.870 1.305 Liq. Bromine 0.560 0.84 Red Phosphorous 0.043 0.064 Sulfuric Acid 0.150 0.022

9. SODIUM BROMIDE (POWDER) 0.5 NaOH Soln. 0.786 0.393 HBr Soln. 1.573 0.786 Charcoal 0.005 0.002

10. SODIUM BROMIDE (SOLUTION) 30

NaOH Soln. 0.334 10.02 HBr Soln. 0.669 20.07

Charcoal 0.004 0.12

11. POTTASIUM BROMIDE (POWDER) 0.5

KOH/H2O 0.945 0.472 HBr Solution 1.371 0.685 Charcoal 0.006 0.003

12. LIQUID BROMINE 25 NaBr/KBr/NH4Br/HBr 4.667 116.67

Chorine Gas 0.500 12.5

Overall list of Raw Material:

Sr. No. Raw Material Name Quantity

(MT/Month) Total (MT/Month) Existing Proposed

1 Normal Butanol 14.4 23.1 37.5 2 Normal Propanol 2.35 45 47.35 3 Iso Propanol 0.86 3.265 4.125 4 Ethanol 1.05 2.775 4.315 5 5,5 Di Methyl Hydantoin 5.01 -- 5.01 6 Liquid Bromine 25.00 68.64 93.64 7 Hydrobromic Acid 6.75 38.33 45.18 8 Octyl Alcohol -- 1.305 1.305 9 Cetyl Alcohol -- 1.215 1.215

10 Charcoal -- 0.123 0.123 11 Solution of NaBr / KBr / NH4Br -- 116.67 116.67 12 Chlorine 4.00 11.5 15.5 13 Soda Ash 6.30 -- 6.30 14 Sulfuric Acid 3.30 16.22 13.52 15 Sodium Hydroxide -- 10.41 10.41 16 Sulfur 2.50 3.2 5.7 17 Red Phosphorous 0.00 0.097 0.97 18 Tetra Butyl Ammonium Bromide -- 0.675 0.675 19 Potassium Hydroxide Flakes -- 0.472 0.472

Enclosure: 4

Chemical Name & Physical form of raw material with his storage facility

Sr. No. Name of raw material CAS NO. Physical

form Type of Packing MOC

Max. at a time

storage in MT

Max Consumption

MT/ week

1 Normal Butanol 71-36-3 Liquid HDPE barrel-165 kg HDPE barrel 10 MT 6 MT

2 Normal Propanol 71-23-8 Liquid HDPE barrel-165 kg HDPE barrel 10 MT 4.5 MT

3 Iso Propanol 67-63-0 Liquid HDPE barrel-165 kg HDPE barrel 5 MT 2 MT

4 Ethanol 64-17-5 Liquid HDPE barrel-165 kg HDPE barrel 4.5 MT 1 MT

5 5,5 Di Methyl Hydantoin 32718-18-6 Solid HDPE bag 50 kgs HDPE bag 7.5 MT 0.7 MT

6 Liquid Bromine 7726-95-6 Liquid

Glass bottle of 3 kg in pack 6 bottle in wooden or plastic

boxes- 18 kgs

Glass bottle 18 MT 8.8 MT

7 Hydrobromic Acid 10035-10-6 Liquid HDPE barrel 200 kgs HDPE barrel 10 MT 4MT

8 Octyl Alcohol 111-87-5 Liquid HDPE or galvanized iron barrel-190 kgs

HDPE or galvanised iron barrel

1 MT 0.87 MT / Month

9 Cetyl Alcohol 36653-82-4 Solid HDPE bag 25 kg HDPE bag 1 MT 0.81 MT

10 Charcoal 7440-44-0 Solid HDPE bag of 50 kgs HDPE bag 0.5 MT 0.002 MT

11 Solution of NaBr / KBr / NH4Br 7647-15-6 Liquid HDPE barrel of 220 kgs HDPE barrel 25 MT 6 MT

12 Chlorine 7782-50-5 Liquid/Gas Steel toners of 900

kgs Steel Toners 3.6 MT 1 MT

13 Soda Ash 497-19-8 Solid HDPE bag of 50 kgs HDPE bag 5 MT 0.5 MT

14 Sulfuric Acid 7664-93-9 Liquid MS tanker MS Tank 15 MT 3 MT

15 Sodium Hydroxide solution 1310-73-2 Liquid MS tanker MS tank 20 MT 4 MT

16 Sulfur 7704-34-9 Solid HDPE bag of 50 kgs HDPE bag 5 MT 0.8 MT

17 Red Phosphorous 7723-14-0 Solid Galvanised drum of 50 kgs

Galvanised drum 0.75 MT 0.5 MT/ Month

18 Tetra Butyl Ammonium Bromide 1643-19-2 Solid Fiber drum of 50 kgs Fiber Drums 1 MT 0.675 MT/ month

19 Potassium Hydroxide Flakes 1310-58-3 Solid HDPE bag of 50 kgs HDPE bag 1 MT 0.47 MT/ month

Enclosure: 5

Properties of Raw Material

Sr. No

Product

Physical & Chemical Composition B.P. F.P. LEL

TLV LD50

mg/kg Sp.Gr.

(Water=1)at

V.D. at

(air=1)

Odor Threshold Solubility

in Water Chemical Formula State MW oC oC % ppm or

mg/nm3 ppm,

mg/Nm3

1 Normal Butanol C3H9OH Liquid 74.12 117 34 1.4 152 790 0.8089 2.55 1.2 Soluble

2 Normal Propanol C3H7OH Liquid 60.1 97.2 15 2.1 200 560 0.804 2.07 5.3 Soluble

3 Iso Propanol C3H8O Liquid 60.9 82 12 2 1225 5000 0.7850 2.1 22 Miscible 4 Ethanol C2H5OH Liquid 46.08 78.5 12 3.3 1900 NA 0.790 1.59 100 Soluble

5 5,5 Di Methyl Hydantoin

C5H8N2O2 Solid 285.91 376 197 NA 0.4 542 NA NA ND Soluble

6 Liquid Bromine Br2 Liquid 159.808 58.78 NA NA 0.2 2600 3.11 7.1 0.05 Soluble

7 Hydrobromic Acid Br-H Liquid 80.92 -66.7 -

86.7 NA NA NA 1.5 2.81 NA Soluble

8 Octyl Alcohol C8H17OH Liquid 130.23 195 190 1.1 NA 1790 NA 4.5 0.1 NA 9 Cetyl Alcohol C16H33OH Solid 242.43 344 160 NA NA 3200 0.8187 8.36 NA Negligible

10 Charcoal C Solid 12.01 NA NA NA 3.5 NA 3.51 NA NA Insoluble

11 Solution of NaBr / KBr / NH4Br

NaBr Liquid 102.89 1390 NA NA NA 3500 3.208 NA NA Soluble

12 Chlorine Cl Liquid/Gas 71 - NA NA 1 146.5 1 0.62 NA Soluble

34.05

13 Soda Ash Na2CO3 Solid 106 NA NA NA NA 4090 2.532 NA NA Soluble 14 Sulfuric Acid H2SO4 Liquid 98.08 270 NA NA 3 320 1.84 3.4 NA Soluble

15 Sodium Hydroxide NAOH Liquid 40 1390 NA NA 2 NA 2.12 NA NA Soluble

16 Sulfur S Solid 16 445 188 35 NA 8437 NA 8.8 NA Insoluble

17 Red Phosphorous P Solid 30.974 416 NA NA 0.02 NA 2.36 NA NA Insoluble

18 Tetra Butyl Ammonium Bromide

C16H36NBr Solid 322.36 NA NA NA NA 9.4 1 NA NA Soluble

19 Potassium Hydroxide Flakes

KOH Solid 56.107 1384 NA NA 2 90 2.044 0.62 NA Soluble

Enclosure: 6

Details of Hazardous Chemicals

The Raw materials, which are termed as hazardous Chemicals as per the “Manufacturing, Storage and Import of Hazardous Chemicals (MSIHC) Rules, 1989” are as listed below Table:

Sr. No.

Name of Hazardous chemicals Reference in MSIHC

Threshold Quantity

(MT)

Maximum Storage Capacity

(MT) Sc-2 Sc-3 1 Liquid Bromine Sr. No. 84 (Sch-1 of MSIHC, 1989) --- --- 18 2 Chlorine Sr. No. 119 (Sch-1 of MSIHC, 1989) 50 40 3.6 3 Ethanol Sr. No. 248 (Sch-1 of MSIHC, 1989) --- --- 4.5 4 Iso Propanol Sr. No. 334 (Sch-1 of MSIHC, 1989) --- --- 5 5 Normal Butanol Sr. No. 412 (Sch-1 of MSIHC, 1989) --- --- 10

6 Potassium Hydroxide Flask Sr. No. 522 (Sch-1 of MSIHC, 1989) --- --- 1

7 Sodium Hydroxide Sr. No. 571 (Sch-1 of MSIHC, 1989) --- --- 20 8 Sulphuric Acid Sr. No. 591 (Sch-1 of MSIHC, 1989) --- 10 15

Enclosure: 7

Manufacturing Prosess & Chemical Reaction & Mass Balance

NORMAL BUTYL BROMIDE

• MANUFACTURING PROCESS:

In reaction vessel take Normal Butanol+Sulfur+Water. Stir it. Than start addition of Liquid Bromine slowly. After complete addition of Liq. Bromine reflux it for 4½ hour then distill the product on next day. Normal Butyl Bromide and Residue transfer to reactor Regenerated Spent Sulphuric Acid. Takes in HDPE drums and packed it.

• CHEMICAL REACTION:

C4H9OH + S + H2O + Br2 C4H9Br + Dil. H2SO4 + H2O

n-Butyl Bromide

• FLOW SHEET OF NORMAL BUTYL BROMIDE:

Normal Butanol-625 kgs

Sulfur-45 kg

Water-675 Kg

R1

Liq. Bromine-675kgs

Processing

Normal Butyl Bromide-1000 kgs

Spent Sulphuric Acid treated &

sent to Novel Spent -710 kgs

Normal Propyl Bromide:


In a reactor take, Normal Propanol+ Sulfur+ Water and add Liq. Bromine Slowly. After Complete addition of Liq. Bromine reflux it for 4½ hour then distill the product. Normal Propyl Bromide and Residue transfer to reactor Regenerated Spent Sulphuric Acid. Takes in HDPE drums and paked it.


C3H7OH + S + H2O + Br2 C3H7Br + Dil. H2SO4 + H2O n-Propyl Bromide

• FLOW SHEET OF NORMAL PROPYL BROMIDE:

Normal Propanol-513 kgs

Sulfur-50 kgs

Water-700 kgs

R1

Liq. Bromine-750 kgs

Processing

Normal Propyl Bromide-1000 kgs

Spent Sulphuric Acid treated & sent to Novel Spent Acid Mgmt-513 kgs

Ethyl Bromide:


In reaction vessel take, Hydro Bromine acid & ethyl alcohol Stir it. Than start addition of Sulphuric acid slowly with chilling. Complete the addition of acid. Then reflux up to complete the reaction then distilled it. Takes in HDPE drums and packed it.


CH3-CH2-OH + HBr + H2SO4 CH3-CH2-Br + Dil. H2SO4 Ethyl Bromide

• FLOW DIAGRAM:

Ethanol-510 kgs Hydro bromic acid-2060 kgs Sulphuric Acid-1400 kgs

Reactor

Reaction & Distillation

Separation

Spent Sulphuric Acid treated & sent to Novel Spent Acid Mgmt.-2970 kgs

Drying

Ethyl Bromide-1000 kgs

Iso-Propyl Bromide:


In reaction vessel take, Iso-Propyl alcohol. Stir it. Than start addition of Liquid Bromine slowly up to reflux it. Complete the reaction then distilled it. Takes in HDPE drums and paked it.


CH3-CH-CH3 + HBr+H2SO4 CH3-CH-CH3+Dil. H2SO4

OH Br Iso-propyl bromide

• FLOW DIAGRAM:

Iso- Propanol-550 kgs Hydrobromic Acid-1725 kgs Sulphuric Acid-1175 kgs

Reactor

Reaction & Distillation

Separation

Spent Sulphuric Acid treated & sent to Novel Spent Acid Mgmt.-2450 kgs

Drying

Iso-Propyl Bromide-1000 kgs

1:3 Di Bromo Di Methyl Hydentoine:


In reaction vessel take, water & add soda ash & cool it to 20°C. Then start addition of Di methyl Hydentoin and dissolve it. Then add bromine slowly then pass chlorine till the reaction complete, then centrifuge it. Wash with water and dry it.


(CH3)2C NH (CH3)2C NBr H2O+ CO + Na2CO3 + Br2 + Cl2 CO + 2 NaCl+ H2O + CO2

OC NH CO NBr 1:3 Di Bromo Di Methyl Hydentoin

• FLOW DIAGRAM:

Water -1500 kgs Soda Ash-420 kgs Liq Bromine -434 kgs Chlorine -200 kgs DMH -334 kgs

Reactor

CO2 Liberate-174 kgs

Water-1500 kgs

Centrifuge

NaCl To ETP-2800 kgs

Vaccum Drying

Moisture loss-414 kgs 1:3 Di Bromo 5:5 Di Methyl Hydentoine-1000 kgs

Tetra Butyl Ammonium Tri Bromide:


In reaction vessel take, tetra butyl ammonium bromide and then add Methylene chloride and water to it. Add Hydrobromic acid and liquid bromine slowly within 20 hr at 25- 30° C. Then centrifuge it and dried in a Vaccum dryer pack it.


( C4H9 ) 4 NBr + Br2 ( C4H9 ) 4 NBr3

Tetra Butyl Ammonium Tri bromide

• FLOW DIAGRAM:

Water-900 kgs TBAB-675 kgs Liq Bromine-350 kgs HBr-100 kgs

Reactor

DMH-50 kgs

Centrifuge

Bromine Recovery Plant-975 kgs

Vaccum Drying

Moisture loss-100 kgs Tetra Butyl ammonium tri bromide -1000 kgs

Cetyl Bromide:


In reaction vessel take, Cetyl alcohol & red Phosphorous than add Liquid Bromine slowly, stir it. Then separate the layer and wash with sulphuric acid and dry it. Pack it.


C16H33OH + Br2 + Red Phosphorous+Water C16H33Br+Dil. H3PO3

Cetyl bromide

• FLOW DIAGRAM:

Cetyl Alcohol-810 kgs Liq. Bromine-295 kgs Red Phosphorus-22 kgs

Reactor

Reg. H3PO3-80 kgs

Sulphuric Acid-130 kgs

Separation

Spent Acid treated & sent to Novel Spent Acid Mgmt -150 kgs

Drying & Packing

Moisture loss-27 kgs Cetyl Bromide-1000 kgs

Octyl Bromide:


In reaction vessel take, Octyl alcohol& red Phosphorous than add Liquid Bromine slowly, stir it. Then separate the layer and wash with sulphuric acid and dry it &Pack it.


C8H17OH +Br2+ Red Phosphorous C8H17Br+Dil. H3PO3

Octyl Bromide

• FLOW DIAGRAM:

Octyl Alcohol-870 kgs Liq. Bromine-560 kgs Red Phosphorus-43 kgs

Reactor

Reg. H3PO3-190 kgs

Sulphuric Acid-150 kgs

Separation

Spent Acid treated & sent to Novel Spent Acid Mgmt.-400 kgs

Drying

Moisture loss-33 kgs Octyl Bromide-1000 kgs

Sodium Bromide (Powder):


In reaction vessel take, Sodium Hydroxide or Sodium bromide solution than add Hydrobromic acid and till neutralization to obtain their salt and evaporate that solution to get dry salt.


NaOH/H2O + HBr (Solution) NaBr + H2O Sodium Bromide

FLOW DIAGRAM:

NaOH Soln-786 kgs HBr Soln-1573 kgs

Reactor

NaBr Sodium Bromide Solution

Charcoal-05 kgs

Centrifuge

Wet Charcoal to Solid waste-15 kgs

Heated, Cooled &

crystallised

NaBr Solid-1000 kgs Evaporated water-1349 kgs (condensed & used)

NOTE

• If we have making Sodium Bomide Solution we will use only first step of this process OR for further process we will get Sodium Bromide Powder.

Potassium Bromide (Powder):


In reaction vessel take, Potassium Hydroxide or Potassium bromide solution than add Hydrobromic acid and till neutralization to obtain their salt and evaporate that solution to get dry salt.


KOH/KBr + HBr (Solution) KBr + H2O Potassium Bromide

• FLOW DIAGRAM:

KOH/H2O-945 kgs HBr Soln-1371 kgs

Reactor

Charcoal-06 kgs

Centrifuge

Wet Charcoal to Solid waste-18 kgs

Heated, Cooled & crystallised

KBr (Powder)-1000 kgs Evaporation-1304 kgs

Liquid Bromine:


In a recovery glass tower, take Sodium bromide solution or Hydrobromic acid solution or Potassium bromide solution or Ammonium bromide solution than pass chlorine gas & steam to generate liquid Bromide.


NaBr / KBr / HBr / NH4Br Soln. + Cl2 Br2+NaCl / KCl / HCl / NH4Cl Soln.

Liq. Bromine

• FLOW DIAGRAM:

NOTE:

• When we will use NaBr/KBr/NH4Br effluent goes to ETP for treatment & We will use HBr generate HCl to acidify solution which is use in our plant.

NaBr/ KBr / HBr /NH4Br -4667 kgs Chlorine Gas-500 kgs

Bromine extraction

tower

Liquid Bromine-1000 kgs

NaCl/KCl/NH4Cl to ETP & HCl to acidify the

solution-4167 kgs

Enclosure-8

DETAILS OF WATER CONSUMPTION & WASTEWATER GENERATION

Water Consumption

(KL/Day) Waste Water Generation

(KL/Day) Existing Proposed Total Existing Proposed Total

Domestic 600 -- 600 500 -- 500 Industrial Process 2100 5268 7368 1980 3756 5736 Boiler 1500 5900 7400 150 740 890 Washing 00 150 1500 00 1500 1500 Gardening 00 500 500 00 00 00 TOTAL 4200 13.168 17368 2630 5996 8626

Domestic Wastewater Consumption is 600 L/day & Industrial Water Consumption is 16768 L/Day.

Domestic Wastewater is 500 L/day will be disposed off through Soak Pit/Septic Tank System.

Industrial effluent 8126 L/day will be treated in Effluent treatment Plant and finally @ 2390

L/day send to CETP of Vatva & @ 5736 L/Day send to MEE-Vatva to maintain our unit Zero Liquid Discharged.

Source of Water:- GIDC Water Supply

Water Balance Diagram

All the Figures are in L/Day

Water Consumption 17168

Process 7368

Domestic 600

Industrial 16568

Effluent 5736

To ETP than Send to MEE 5736

Washing Effluent 1500

Boiler 7400

Blow Down 890

Gardening 2000

Washing 1500

Domestic Effluent goes to septic tank

500

To ETP than Send to CETP 2390

Enclosure-9

Details of Effluent Treatment Plant

Detail of Effluent Treatment Plant (After Proposed):

Sr. No. Name of Unit Nos. Capacity (Liter)

1. Collection Cum Neutralization Tank 1 12000 2. Hopper Bottom Settling Tank 1 12000 3. Aeration Tank 1 100000 4. Secondary Settling Tank 1 5000 5. Sludge Drying Beds 1 -- 6. Final Collection Tank 1 8000 7. Holding Tank 1 10000

Diagram of Effluent Treatment Plant (After Proposed):

Collection Cum

Neutralization Tank

Hopper Bottom Settling

Tank

Aeration Tank

Secondary Aeration

Tank

Filtration

Overhead

Holding Tank

Sludge Drying Beds

To CETP Vatva for Further Treatment

And Disposal

Enclosure: 10

Details of Flue Gas Emission & process Gas Emission with APC system

Flue Gas Emission Details:

Sr. No. Stack Attached to Stack

Height in Meter

Parameter Permissible

Limit Existing Proposed

1. IBR Boiler IBR Boiler

(New as same quantity)

11 Particulate Matter SO2 NOx

150 mg/Nm3

100 PPM 50 PPM

2. Hot Air

Generator -- 11

NOTE: • We Remove Our Old IBR Boiler After Obtaining Environment Clearance.

Process Gas Emission Details:

Sr. No.

Stack Attached to

Stack Height in

Meter

Air Pollution Control System Parameter

Permissible Limit Existing Proposed

1. Reaction Vessel (9 Nos.) 15

Single Stage Alkali Scrubber

Two Stage Alkali

Scrubber

HBR Bromine

30 mg/Nm3 02 mg/Nm3

NOTE:

• We will remove single stage alkali scrubber after obtaining Environment Clearance.

Fuel Consumption details:

Sr. No.

Fuel Quantity

(SCM/Month) Existing Proposed Total

1. Natural Gas 3500 2445 5945

Enclosure-11

DETAILS OF HAZARDOUS WASTES GENERATION AND ITS MANAGEMENT

No Type of waste Category Quantity

Management Existing Proposed Total

1 ETP Waste, 35.3 0.4 MT/Month

0.8 MT/Month

1.2 MT/Month

Collection, Storage, Transportation, Disposal at TSDF approves by Board.

2 Used oil 5.1 10 Lit/Year

15 Lit/Year

25 Lit/Year

Collection, Storage, Transportation, Disposal by selling to Registered reprocessor.

3

Discarded Barrels Liners Discarded Drums/Barrels

33.1

--

10 Nos./Month

450 Nos./Month

350 Nos./Month

450 Nos./Month

360 Nos./Month

Collection, Storage, Transportation, Disposal by selling to authorized recycler.

4 Spent Acid D2-sch-II 11 KL/Month

104 KL/Month

115 KL/Month

Collection, Storage, Transportation, Disposal at NOVEL

5 Spent Charcoal -- -- 0.022 MT/Month

0.022 MT/Month

Collection, Storage, Transportation, Disposal at TSDF site.

Enclosure –12

LIST OF PARTNERS

Sr.No NAME OF PARTNER ADDRESS

1. Mr. Ajaybhai Mukundbhai Parikh

12,A-Vijay Colony, Nr. Sardar Patel Colony, Naranpura Ahmedabad-380013. Ph.No.:(R): 079-27680197 Mo.No.: 9825015590

2. Mr. Sureshbhai Pragjibhai Mangrolia(Patel)

12,Sardar Patel Co.Op.Soc.Ltd. P.O. Thakkar Bapanagar, Nikolgam Road, B/h. Sardar Mall, Ahmedabad-382350. Ph.No.:(R): 079-22703030 Mo. No.: 9825012856

3. Mr. Vasantbhai Ravjibhai Mangrolia

38-39,Sardar Patel Co.Op.Soc.Ltd. P.O. Thakkar Bapanagar, Nikolgam Road, B/h. Sardar Mall, Ahmedabad-382350. Ph.No.:(R): 079-22703839 Mo.No.: 9825017399

4. Mr. Bhanubhai Jinabhai Kothiya

7,Shahi Kutir Bunglows, Nr. Sardar Patel Ring Road, M.G. Road, Nikol, Ahmedabad-382350. Mo.No.:9825026570

Enclosure –13

Land Supporting Document

Enclosure –14

Site Plane & Plane Layout

Enclosure –15

CA Certificate

Enclosure –16

CETP & NOVEL Membership Certificate

Enclosure: 17

SSI Certificate

Enclosure –18

Existing Consent Copy

enclosure: 1 -...

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