INDEX. ANNEXURE : 6 Details of Manufacturing Process and Mass Balance. ANNEXURE : 10 Flue Gas Emission and Process Gas Emission

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1 INDEX ANNEXURE 1 Land Passaion Letter ANNEXURE : 2 Location Map ANNEXURE : 3 Layout ANNEXURE : 4 Break up of Land Area ANNEXURE : 5 Details of Product and Raw Material ANNEXURE : 6 Details of Manufacturing Process and Mass Balance ANNEXURE : 7 Water Consumption and Water Generation ANNEXURE : 7A Water Balance Diagram ANNEXURE : 8 Waste Water Treatment Facility ANNEXURE : 9 Flue Gas Consumption ANNEXURE : 10 Flue Gas Emission and Process Gas Emission ANNEXURE : 11 Details of Haz Waste Generation and Mode of Disposal ANNEXURE : 12 List Of Partners

2 Annexure -1 Land Possession Letter

3 ANNEXURE : 2 Location Map

5 ANNEXURE :3 LAYOUT PLAN

6 ANNEXURE :4 AREA BREAK-UP Description Area Squ.Meter Process Area 100 Storage Area( Product and RM) Storage of Water 40 Storage of Haz Waste 60 ETP area 100 Road 100 Office and Security Cabin 40 Utility area* Boiler, Cooling Tower and 30 maintenance dept and Parking Green Belt Total 845

7 ANNEXURE 5 List of Products and Raw Materials Consumption: A.Products : Group Sr No : Product Name MT/MONT H A 1 6 Acetyle OAPSA and or CAPSA & 6 CAPSA and or 3 COPPER FORMAZONE BASE and or 4 Brodex GP and or 5 MNPT and or 6 MSPG ACID and or 7 NDMT and or 8 4 NAPSA and or B 9 MCA ( MonoChloro Aniline) and or Chloro Metanilic Acid and or 11 2 Amino Phenol 4 Methyl Sulphonamide and or 12 2 Amino phenol 4 Methyl Sulphone and or 13 2 Choloro PPD ( 2 Chloro Phenylene Di Amine) and or 14 Methoxy OPSAmide ( 2 Amino -4-( sulphonamide-nethyl,2 Methoxy ) Chlorohydrate) and or 15 2'5 Di methyl Aniline and or 16 2 Amino Di Methyl Terphthalate C 17 Eather Amine 5 Sr NO Byproducts T/M 1 Hydrochloric Acid (Scrubber ) Sodium Sulphite ( Scrubber) Dilu. Acetic Acid 7.5 * Entire quantity of byproducts will be utilized in plant further.

8 B. Raw Materials : Product Cap MT/M Raw Material T/T T/M 6 Acetyl OAPSA 10 4 CAPSA/6 CAPSA 10 Copper Formazone 10 Bordeaux GP 10 MNPT 10 Caustic NAPSA Acetic Anhydride Spent Acid Iron Powder HCL PCP/OCA Sulphuric Acid WNA Salt Caustic Soda Ash Acetic Acid SBS Iron Powder PCP/OCP Nitro Spent Acid Hydro Acetyle OAPSA HCL NaNO Caustic Copper Sulphate Sulphamic Acid Caustic Salt Soda Sulpho Hydrazone Para Anisidine Acetic Acid Acetic Anhydride HNO Para Anisidine Acetic Anhydride NaOH HNO MSPG Acid 10 Gamma Acid

9 NDMT 10 4 NAPSA Meta Chloro Aniline 10 6 chloro Metalinic Acid 2 Amino Phenol N Methyl 4 Sulphonamide 2 Amino Phenol 4 Methyl Sulphone 2 Chloro Para Phenylene Di amine Soda Ash Metalinic Acid Sodium Bisulphite Dmt Oleum Sulphuric acid Nitric acid PNCB Oleum Methoxy OPSAmide 15 2:5 Di Methyl Aniline 15 Sulphuric acid HNO Lime NaHS Meta Chloro Nitro Benzene NaHS ONCBPSA Iron powder Caustic Acetic acid Nitromethyl opsamide Iron powder Caustic Acetic acid Nitro pms Iron powder Caustic Acetic acid Ocpna Iron powder Caustic Acetic acid Nitro methoxy OPSAmide Iron powder Caustic Acetic acid :5 Di Methyl Nitrobenzene Caustic iron powder Acetic Acid Amino Dimethyl 15 Nitro dmt

10 Terphthalate Iron powder Ether Amine 10 Caustic Acetic acid Mcb(solvent) (2 Chloroethylsulphonyl)-butyrylchloride Thionyl Chloride

11 Process Description and mass balance Meta Chloro Aniline: Annexure : 6 NO 2 Reduction NaHS Water NH 2 Cl Cl Meta Chloro Nitro Benzene (157.5) Meta Chloro Aniline (MCA) (127.5) Meta Chloro Nitro benzene is reduced by NaHS in presence of water. After completion of reaction the reduction product Meta Chloro Aniline is obtained by separation.effluent, send for evaporation at TEE. 6-Chloro Metanilic Acid: ` Cl NO 2 Reduction Iron Powder HCl Cl NH 2 SO 3 H -Fe 2 O 3 SO 3 H Ortho Nitro Chloro Benzene Sulphonic Acid (ONCBPSA) (237.6) Ortho Amino Chloro Benzene Sulphonic acid (6-Chloro Metanilic acid) (207.6) Ortho Nitro Chloro Benzene Sulphonic Acid is reduced by Fe/HCl and filter through filter press & product is isolated by chilling, filtered and C/F to get Ortho Amino Chloro Benzene Sulphonic Acid (6-Chloro Metanilic Acid).

12 2-Amino Phenol-N-methyl-4-Sulphonamide: OH NO 2 Reduction Iron Powder (Fe) HCl OH NH 2 -Fe 2 O 3 ` SO 2 NHCH 3 2-nitro phenol-n-methyl-4-sulphonamide (232.2) SO 2 NHCH 3 2-Amino phenol-n-methyl-4-sulphonamide (202.2) The cake of 2-Nitro phenol-n-methyl-4-sulphonamide is reduced with Fe/Acid and clarified through filter press. The product is isolated by chilling, filtered and centrifuged. The resultant is dried in FBD to get 2-Amino Phenol-N-methyl-4-Sulphonamide. ` 2-Amino Phenol-4-Methyl Sulphone: OH NO 2 Reduction Iron Powder (Fe) HCl OH NH 2 -Fe 2 O 3 SO 2 CH 3 2-Nitro Phenol-4-Methyl Sulphone (Nitro PMS) (217) SO 2 CH 3 2-Amino Phenol-4-Methyl Sulphone (187) 2-Nitro phenol-4-methyll sulphone is reduced by Fe/HCl, filtered through filter press and isolated by Chilling. The product is filtered and centrifuged that gives 2-Amino Phenol-4-Methyl Sulphone.

13 2-Chloro Para Phenylene Diamine [Cl-PPD]: NH 2 Cl Reduction Iron Powder HCl NH 2 Cl -Fe 2 O 3 ` NO 2 2-chloro para nitro aniline (172.5) NH 2 2-Chloro Para Phenylene Diamine (Cl-PPD) (142.5) 2-nitro para nitro aniline is reduced by Fe/HCl and filter through filter press & product is isolated by chilling, filter and C/F to get 2-Chloro Para Phenylene Diamine (Cl-PPD). ` Methoxy Opsamide: OH NO 2 Reduction Iron Powder (Fe) HCl OH NH 2 -Fe 2 O 3 SO 2 NHCH 2 CH 2 OCH 3 2-Nitro-4-(sulphonamide-N-ethyl,2'-methoxy)chlorohydrate (276) SO 2 NHCH 2 CH 2 OCH 3 2-Amino-4-(sulphonamide-N-ethyl,2'-methoxy)chlorohydrate Or Methoxy Opsamide (246) The cake of 2-Nitro-4-(sulphonamide-N-ethyl,2 -methoxy) chlorohydrate is reduced by Fe/HCl and filter through filter press & product is isolated by chilling, filtered and centrifuged and dried in FBD to get 2-Amino-4-(sulphonamide-N-ethyl,2 -methoxy) or Methoxy opsamide.

14 2,5-Dimethyl Aniline: NO 2 CH3 Reduction Iron Powder HCl NH 2 CH3 H 3 C -Fe 2 O 3 H 3 C ` 2,5-Dimethyl Nitro benzene (151) 2,5-Dimethyl Aniline (121) 2,5-Dimethyl Nitro benzene is reduced by Fe/HCl and filter through filter press & dried in FBD to get the product 2,5-Dimethyl Aniline. Recover the solvent and reuse for the next batch. 2-Amino Dimethyl Terphthalate: ` COOCH 3 Reduction Iron Powder HCl COOCH 3 COOCH 3 NO 2 2-Nitro Dimethyl Terpthlatate (239) -Fe 2 O 3 COOCH 3 NH 2 2-Amino Dimethyl Terpthlatate (209) 2-Nitro Dimethyl Terpthlate is reduced by Fe/HCl and filter through filter press & dried in FBD to get the product 2-Nitro Dimethyl Terpthlate. Recover the solvent and reuse for the next batch.

15 ` O 2 N 6-Acetyl OAPSA: OH NH 2 Acylation Acetic Anhydride Caustic Lye O 2 N OH NHCOCH 3 Reduction Iron Powder HCl Filteration Isolation & Drying H 2 N OH NHCOCH 3 Ice/Water SO 3 H SO 3 H SO 3 H 6-NITRO 2-AMINO PHENOL 4-SULPHONIC ACID (6-NAPSA) (234.19) 6-ACETYL 2-NITRO PHENOL 4-SULPHONIC ACID (276.22) 6-ACETYL ORTHO AMINO PHENOL 4-SULPHONIC ACID (6-ACETYL OAPSA) (246.24) 6-Nitro 2-Amino Phenol 4-Sulphonic acid is acetylated with Acetic anhydride followed by reduction with iron powder Fe/HCl, filtered through filter press and product is isolated by chilling. The resultant product is filtered, centrifuged and dried in FBD to get 6-Acetyl Ortho Amino Phenol-4-Sulphonic Acid (6-Acetyl OAPSA). MSPG Acid: HO 3 S OH NH 2 + N H 2 SO 3 H Reduction Soda Ash Isolation with Sodium Bisulphite Filteration Drying HO 3 S OH NH SO 3 H GAMMA ACID (239) METALINIC ACID (173) META SULPHO PHENYL GAMMA ACID (MSPG ACID) (395) Gamma acid and Metalinic acid are reduced in presence of soda ash to get the product which is isolated with sodium bisulphate and filtered in filter press. Dry in FBD to get MSPG Acid.

16 2-Nitro Dimethyl Terphthlate [NDMT]: COOCH 3 + H 2 SO 4 + HNO 3 Nitration -H 2 O COOCH 3 NO 2 -H 2 SO 4 ` COOCH 3 Dimethyl terphthalate [DMT] (194) (98) (63) COOCH 3 2-Nitro dimethyl terphthalate [NDMT] (239) Dimethyl terpthalate [DMT] is nitrated by mix acid of Nitric acid & Sulphuric acid drowning in ice, filtered and centrifuged to get 2-Nitro Dimethyl Terphthlate[NDMT]. Spent acid, sale to users. 4-nitro-2-aminophenol-6-sulphonic acid [4-NAPSA] ` Cl NO 2 + H 2 SO 4 + HNO 3 Nitration & Sulphonation HO 3 S Cl NO 2 NO 2 Hydrolysis & Partial Reduction NaHS, NaOH -NaCl -Na 2 S 2 O 3 HO 3 S OH NO 2 NH 2 p-nitro chlorobenzene (157.5) 2-chloro-3,5-dinitro benzene sulphonic acid (282.5) 4-nitro-2-aminophenol-6-sulphonic acid [4-NAPSA] (234) p-nitro chlorobenzene is sulphonated with oleum (23%) & Sulphuric acid followed by nitration with Nitric acid to get 2-chloro-3,5-dinitro benzene sulphonic acid. The above product is hydrolyzed in alkaline medium & partially reduced by adding NaHS to get 4-NAPSA (Na salt). Filter it and C/F. Dissolve the 4-NAPSA (Na salt) in sulphuric acid and clarify through filter press & isolated by sulphuric acid, filter and centrifuge to get pure 4-NAPSA.

17 Copper Formazone/4-Sulpho F Base: OH H 2 N NHCOCH 3 Diazotization NaNO 2 HCl Copper Sulphate Sulphamic Acid Coupling 4 Sulpho Hydrazone COOH NH N SO 3 H 6-ACETYL ORTHO AMINO PHENOL 4-SULPHONIC ACID (6-ACETYL OAPSA) Mol. Wt Ice/Water Caustic Caustic Ice Soda Hydrolysis Caustic/Salt Filteration SO 3 - O H 2 N O - O - Cu 2- N C - N + N + N 3H + SO 3 - COPPER FORMAZONE / 4-SULPHO F BASE Mol. Wt Acetyl OAPSA is first diazotized with NaNO2/HCl and copper sulphate in presence of Sulphamic acid. The resultant product is coupled with 4-Sulpho Hydrazone to get crude product which is then filtered followed by hydrolysis with caustic lye and filtration to get pure Copper Formazone/4-Sulpho F Acid.

18 4CAPSA: OH Sulphonation H 2 SO 4 Nitration Weak Nitric Acid HNO 3 O 2 N OH SO 3 H Dumping Caustic Lye Soda Ash Reduction Iron Powder Acetic Acid SBS -SO 2 -NO 2 PCP Reuse Cl PARA CHLORO PHENOL (PCP) (128.56) Cl 4-CHLORO 2-NITRO PHENOL 6-SULPHONIC ACID ( ) Filteration Isolation & Drying OH H 2 N SO 3 H Cl 4-CHLORO 2-AMINO PHENOL 6-SULPHONIC ACID (4-CAPSA) (223.63) 6-CAPSA: OH Cl Sulphonation H 2 SO 4 Nitration Weak Nitric Acid HNO 3 O 2 N OH Cl Dumping Caustic Lye Soda Ash Reduction Iron Powder Acetic Acid SBS -SO 2 -NO 2 PCP Reuse SO 3 H ORTHO CHLORO PHENOL (OCP) (128.56) 6-CHLORO 2-NITRO PHENOL 4-SULPHONIC ACID (253.62) Filteration Isolation & Drying OH H 2 N Cl SO 3 H 6-CHLORO 2-AMINO PHENOL 4-SULPHONIC ACID (6-CAPSA) (223.63) Para Chloro Phenol(PCP)/Ortho Chloro Phenol (OCP) is nitrated & sulphonated with Weak nitric acid and Sulphuric acid to get chloro nitro phenol sulphonic acid which is then reduced with iron powder Fe/HCl, filtered through filter press and product is isolated by chilling. The resultant product is filtered, centrifuged and dried in FBD to get 4-Chloro 2-Amino Phenol 6- Sulphonic Acid (6-CAPSA) OR 6-Chloro 2-Amino 4-Sulphonic acid (6-CAPSA).

19 6 Acetyl OAPSA Water 400 Caustic NAPSA 1700 Acetic Anhydried 400 Ice 1150 Acetylation water 400 Iron Powder 1200 HCL 200 Caustic 200 Reduction Water 1500 FIltration Iron Sludge 2000 Spent Acid 550 Isolation Filtration Waste Water 5000 Drying Loss Acetyl OAPSA Product Input T/T T/M Output T/T T/M 6 Acetyl OAPSA Water Iron Sludge Caustic Waste Water NAPSA Loss Acetic Anhydride Acetyl OAPSA Ice Spent Acid Iron Powder HCL Total Total

20 4 CAPSA/6 CAPSA PCP/OCA 1100 SO2 100 Sulphuric Acid 3000 NO2 80 Water 440 Sulphonation WNA 400 Caustic 550 Soda Ash 500 Water 2700 Salt 400 Dumption Spent Acid 4000 Water 1500 Acetic Acid 160 SBS 20 PCP/OCP Nito Reuse 1000 Reduction Iron Powder 1650 PCP/OCP Nitro 1000 Caustic 400 Water 5000 Waste Water 5000 Filtration Sludge 4965 Spent Acid 1900 Hydro 10 Isolation Filtration waste water 3210 drying Losss CAPSA/6 CAPSA Product Input T/T T/M Output T/T T/M 4 CAPSA/6 CAPSA PCP/OCA SO Sulphuric Acid NO WNA Spent Acid Salt PCP/OCP Nito Reuse

21 Caustic Waste Water Soda Ash Sludge Acetic Acid Loss SBS CAPSA/6 CAPSA Iron Powder PCP/OCP Nitro water Spent Acid Hydro Total Total

22 Copper Formazone/4 Sulpho F Base Water Acetyle OAPSA 700 Ice 3850 HCL 475 NaNO2 180 Caustic 275 Copper Sulphate 670 Sulphamic Acid 5 Diazo Water Sulpho Hydrazone 1150 Caustic 275 Ice 4000 Soda 780 Coupling Fitration Sludge 860 Caustic 1550 Salt 775 Hydrolysis Fitration Waste Water Wet Cake of 1450 Copper Formazone/4 Sulpho F Base Product Input T/T T/M Output T/T T/M Copper Formazone/4 Sulpho F Base Water Sludge Acetyle OAPSA Waste Water Ice Copper Formazone HCL NaNO Caustic Copper Sulphate Sulphamic Acid Caustic Salt Soda Sulpho Hydrazone Total Total

23 MSPG Acid Gamma Acid 400 Soda Ash 60 Metalinic Acid 310 Reduction Sodium Bisulphite 300 Water 800 Isolation Filtration Waste Wate 750 Drying Loss 120 MSPG Acid Product Input T/T T/M Output T/T T/M MSPG Acid Gamma Acid Waste Water Soda Ash Loss Metalinic Acid MSPG Acid Sodium Bisulphite Water Total Total

24 NDMT DMT 1400 OLEUM 350 SULPHURIC ACID 1100 NITRIC ACID 380 Nitration ice 2000 Dumping Filtration Spent Acid 4000 Sulphuric 1000 Isolation Filtration Waste Water 1000 Drying Loss 230 NDMT Product Input T/T T/M Output T/T T/M NDMT DMT Spent Acid OLEUM Waste Water SULPHURIC ACID Loss NITRIC ACID NDMT ice Total Total

25 4 NAPSA PNCB 1000 OLEUM 1200 SULPHURIC ACID 100 HNO3 120 REACTION LIME 500 Water 800 NaHS 600 REDUCTION Filtration Sudge 1900 H2SO4 100 Isolation Water 600 Waste Water 2000 Filtration drying Loss NAPSA Product Input T/T T/M Output T/T T/M 4 NAPSA PNCB Sludge OLEUM Waste Water SULPHURIC ACID Loss HNO NAPSA LIME Water NaHS Total Total

26 Reduction Products Acetic Acid Fe Intermediate-B Reduction Filtration Iron Sludge Caustic Isolation and ph Adjust Filtration Waste Water Drying Loss Product Product Input T/T T/M Output T/T T/M Meta Chloro Aniline Meta Chloro Nitro Benzene Sludge NaHS Waste Water Water Meta Chloro Aniline Total total chloro Metalinic Acid ONCBPSA Iron Sludge IRON POWDER Loss CAUSTIC chloro Metalinic Acid ACETIC ACID Waste Water Water Total Total AMINO PHENOL N METHYL 4 SULPHONAMIDE NITROMETHYL OPSAMIDE Iron Sludge IRON POWDER Loss AMINO PHENOL N METHYL CAUSTIC SULPHONAMIDE ACETIC ACID Waste Water WATER Total Total

27 2 AMINO PHENOL 4 METHYL SULPHONE NITRO PMS Iron Sludge IRON POWDER Loss AMINO PHENOL 4 METHYL CAUSTIC SULPHONE ACETIC ACID Waste Water WATER Total Total CHORO PARA PHENYLENE DI AMINE OCPNA Iron Sludge IRON POWDER Loss CHORO PARA PHENYLENE DI CAUSTIC AMINE ACETIC ACID Waste Water WATER Total Total METHOXY OPSAMIDE NITRO METHOXY OPSAMIDE Iron Sludge IRON POWDER Loss CAUSTIC METHOXY OPSAMIDE ACETIC ACID Waste Water WATER Total Total :5 Di Methyl Aniline 2:5 Di Methyl Nitrobenzene Iron Sludge Caustic Loss iron powder :5 Di Methyl Aniline Acetic Acid Waste Water Total Total AMINO DIMETHYL TERPHTHALATE NITRO DMT Iron Sludge IRON POWDER Loss AMINO DIMETHYL CAUSTIC TERPHTHALATE ACETIC ACID Waste Water MCB(SOLVENT) MCB RECO Total Total

28 Fast Bordeaux GP Base Para Anisidine 848 Acetic Acid 763 Ace.Anhydride 15 Acetylation Distillation Acetic Acid 753 Loss 10 HNO3 200 Nitration FIltratio n w.w 2543 Water 2800 Washing Water 1000 Hydrolysis Loss 120 FIltration waste water 1000 Drying Loss 200 Bordeaux GP Product Input T/T T/M Output T/T T/M Bordeaux GP Para Anisidine Acetic Acid Acetic Acid Loss Acetic Anhydride Bordeaux GP HNO Waste Water Water Loss Total Total

29 MNPT Para Anisidine 500 Ace.Anhydride 440 Acetylation Acetic Acid 240 HNO3 450 Water 2500 Nitration NaOH 200 Water 1000 Hydrolysis Water 1500 Waste Water 5300 Filtration Drying Loss 450 MNPT Product Input T/T T/M Output T/T T/M MNPT Para Anisidine Acetic Acid Acetic Anhydride Waste Water NaOH Loss HNO MNPT Water Total Total Ether Amine 4-(2 Chloroethylsulphonyl)-butyrylchloride 376 Thionyl Chloride 256 Chlorination Liquid Product -Ether Amine Ether Amin 632 Product Input T/T T/M Output T/T T/M 4-(2 Chloroethylsulphonyl)- Ether Amine butyrylchloride Ether Amine Thionyl Chloride Total Total

30 Details of Water Consumption Annexure : 7 Water Consumption and Water Generation Sr. No. Description KL/Day A Domestic 3.00 Industrial Process 3.82 Washing 5.00 B Boiler 2.50 Cooling 3.00 Scrubber 1.00 Total B C Gardening 2.00 Total A+B+C WASTE WATER GENERATION Sr. No. Description KL/Day A Domestic 3.00 B Industrial Process Washing Boiler Cooling Total B C Gardening 0 Total A+B+C

31 Annexure : 7 A Water Balance Diagram

32 WASTEWATER TREATMENT & DISPOSAL Annexure ; 8 Waste Water Treatment Facility The source of water for the proposed expansion project shall meet through GIDC Naroda. Total water requirement for the proposed expansion project will be KLD KLD Domestic effluents shall be disposed through septic tank & Soakpit. The effluent generation from the proposed expansion project shall be KL/day. The effluent will be segregated as follows: High Concentrated Effluent: High concentrate process KL/Day will be sent to ETP for Primary treatment and then it will be sent for evaporation at Naroda. Low Concentrated Effluent: Low concentrated effluent from Washing and Boiler 6.4 KL/Day will be sent to ETP for Primary and Tertiary treatment and then it will be CETP Naroda for further treatment and disposal. Treatment of Concentrated Stream: Concentrated stream generated from process shall be collected in Collection Tank, then it shall be transferred to Neutralization tank in which it shall be neutralized with Lime / FeSO4 and finally it shall be sent to common MEE of NEPL Naroda (after Neutralization) for further evaporation. Sr No Item Capacity 1 Collection cum Neutralization Tank m3 2 Nutch Filter 2 m3 MOC : PP 3 Dosing Tank 2 1 KL (each) 4 Storage Tank 1 20 KL Treatment of Dilute Stream: Dilute stream generated from process, scrubber, boiler & washing will given primary treatment and then sent to CETP of M/s. NEPL for further treatment and final disposal.

33 Details of Proposed treatment units for Dilute Stream : Sr No Item Dimension Capacity Collection Tank m x 2.5 m x 2.13 m m3 Equalization Tank m x 2.28 m x 2.43 m m3 Storage Tank m x 2.43 m x 3.05 m m3 Neutralisation Tank m x 2.43 m x 3.20 m m3 Settling Tank m x 1.98 m x 3.05 m m3 Storage Tank m x 2.43 m x 2.43 m m2 Centrifuge m x 1.2 m x 1.2 m 1.72 m3 Sludge Drying Bed 2.43 m x 3.96 m x 1.82 m m3 Assumed characteristics of Concentrated stream ( R & D Base) Parameter Composite Sample (Concentrated) ph 4-5 Oil and Grease mg/l 3.1 COD mg/l BOD mg/l 4500 S.S 300 TDS Assumed characteristics of dilute stream ( R & D Base) Parameter Composite Sample After (Concentrated) treatment ph Oil and Grese mg/l COD mg/l BOD mg/l S.S TDS primary

34 Annexure : 9 Flue Gas Consumption Power and Fuel Requirement Sr. No. Particulars Remarks FUEL 1. Type of Fuel Di Oil Cake, N.G and Diesel 2. Consumption rate Di Oil Cake (0.7 T/Day) N.G (15000 SCM /Month and Diesel (50 Lit/Hr) 3. Source of supply local purchase ENERGY Type of Energy Electricity Connected Load 450 HP Source of supply DGVCL/Torrent

35 FLUE GAS EMISSIONS Annexure : 10 Flue Gas Emission and Process Gas Emission : Flue Gas Emission Stack Attached to Stack(m) Fuel and Consumption Pollutants TFH Height: 11 Meter DOC-200 Kg/Day PM< 150 mg/nm3 Cap 100 U Dia: 280 mm SOx<100 ppm Boiler (2T/Hr) Height :11 meter DOC- 500 Kg/Day NOx<50 ppm Dia: 280 meter D.G Set( 50 KVA) Height :11 meter Deisel-50 Lit/Hr Dia: 280 meter PROCESS EMISSIONS AND CONTROL MEASURES Stack Attached to Stack(m) Air Pollution Control Measures Pollutants Reaction Vessel ( Sulphonator and Isolation 22 meter Common Water Scrubber Followed by Alkali Scrubber SOx <40 mg/nm3 and HCL< 20 mg/nm3

36 Details of Water Scrubber Followed by Alkali Scrubber : Two numbers of counter current packed bed two stage scrubbing system will be provided with Sulphonation and Isolation vessel. The details of scrubber will be as under Diameter : 600 mm Packed Height : 3000 mm Type of Packings : PP Pail Rings Total Height : 4000 mm MOC : MS Scrubbing Media : Caustic And Water FIGURE : 10 A PROCESS GAS EMISSION CONTROL MEASURES

37 Annexure 11 Details of Haz Waste Generation and Mode of Disposal Type of Waste Quantity Mode of Disposal Spent Sulphuric Acid 40 KL/Month Partally reuse and remaining sent to NOVEL,Vatva ETP Sludge 20 T/Month Authorised nearest TSDF Process Waste T/Month Authorised nearest TSDF Iron Sludge 21 T/Month TSDF/Cement industries Discarded Containers/Liners etc 1.5 T/year Sell to recycler used Oil T/Year Sell to recycler In addition to the provision of above, we will ensure proper management for hazardous waste as below: Transportation of hazardous waste to the TSDF Site will be governed as per the guidelines and accompanied with Form-13. Annual returns of the disposal of wastes in Form-4 will be uploaded online and submitted regularly to the local office of the GPCB.

38 Annexure : 12 Umiya Industries Partner List Details Sr.No. Partner Name Address Contact No. 01. AnkurbhaiHasmukhbhai Patel 15,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad HasmukhbhaiKalidasPatel 15,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad KrunalbhaiHasmukhbhai Patel 15,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad KalpeshbhaiPramukhbhai Patel 11,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad ManojbhaiPramukhbhai Patel 11,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad Hem Kalpeshbhai Patel 11,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad MiteshbhaiVishnubhai Patel 15,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad NikujbhaiPankajbhai Patel 15,Ramaykunj Society,Opp-Galaxy Cinema, Naroda,Ahmedabad For, Umiya Industries Partner Ankur H Patel

Annexure-I List of Products. List of Raw Materials

Annexure-I List of Products. List of Raw Materials Sr. o. Annexure-I List of Products Sr. ame of Product o. 1. 2 mercapto 2. 5 methoxy 2 mercapto 3. 5 methyl 2 mercapto 4. 5 difloromethoxy 2 mercapto 5. 4 hydroxy 3 amino chlorobenzene 6. 4 hydroxy 3 chloro