LIST of ANNEXURES SR. NO. NAME of ANNEXURE I List of Products with Their Production Capacity II Layout Map of the Plant III Brie
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LIST OF ANNEXURES SR. NO. NAME OF ANNEXURE I List of products with their production capacity II Layout Map of the Plant III Brief Manufacturing Process Descrip tion with Chemical and Mass Balance IV Details of Water Consumption Wastewater Generation V Effluent Treatment Scheme VI Details of Hazardous /Solid Waste Generation, Handling and Disposal VII Details of Air pollution Control System (Stack & Vent) VI II Details of Hazardous Chemicals Storage & Handling IX Socio-economic Impacts X Proposed Terms of Reference for EIA studies ANNEXURE – 1 LIST OF PRODUCTS WITH THEIR PRODUCTION CAPACITY Production (MT/Month) LD Sr. Product Name CAS No. Proposed Proposed 50(mg/Kg) No. Existing Total Nytrosyl Sulphuric Acid (from 7782-78-7 467.92 2140 1 132.08 600 Sulfur) * Nytrosyl Sulphuric Acid (from 7782-78-7 00 2140 2 Sodium Thio Sulphate Solution and 468 468 Spent Acid (H2SO4)) ** 3.1 4-Met hyl Acetophenone 122 -00 -9 1400 00 60 3.2 Acetyl Furan 1192-62-7 60 1130 4.0 Diethyl Ketone 96 -22 -0 00 179 179 2737 5.1 Methyl Propyl Ketone 107 -87 -9 20001 5.2 Dipropyl Ketone 123-19-3 00 100 100 20001 5.3 Propiophenone 93-55-0 4500 6 Alpha Nitro Napthalene 86-57-7 00 100 100 2560 7 Alpha Napthylamine 134 -32 -7 00 165 165 2000 Phenyl Alpha Naphthylamine 90-30-2 90 90 2000 8 00 (PANA) Epichlorohydrin Based Polyamide 106-89-8 116 116 1580 9 00 resin 10 2,4-Dichloro Acetophenone 2234-16-4 00 60 60 1800 98-86-2 60 60 815 11 Acetophenone 00 IGBA - 3-(2- 75143-89-4 68.2652 68.2652 3580 12.1 methylpropyl)pentanedioic acid 00 KSM - 3-(2-amino-2-oxoethyl)-5- 181289-15- 12.2 methylhexanoic acid 6 5000 13 Anisole 100 -66 -3 00 100 100 3700 Pesticide Interemdiates 13 3, 5 Dichloro aniline 626-43-7 00 50 50 2870 14 D- Allethrollone 43917 -8-56 00 10 10 5000 3-Methyl 4- Nitro Imino Per 153719-38- 20 20 2000 15 00 hydro1,3,5 Oxidiazine 1 118712-89- 30 30 5000 16 Transfluthrin Acid Chloride 00 3 17 1,2,4 Triazole 288-88-0 00 50 50 1750 18 2- Chloro 5 - Chloromethyl Pyridine 70258 -18 -3 00 30 30 1289 19 4-Methoxy Acetophenone 100-06-1 00 60 60 1720 Total 600.08 1787.82 2387.9 List of Raw Materials RAW MATERIAL CONSUMPTION , PRODUCTION MT/M ONTH SR. NO. DESCRIPTION CAPACITY NAME CONSUMPTION Oleum Or 448.23 Or Sulphuric Acid 390.00 Nitric Acid Or 127.03 NytrosylSulphuric Acid 600 1 (from Sulfur or SO Gas) MT/Month 2 104.17 Sulphur Or 24.80 Or SO2 Gas 105.83 Spent H 2SO 4 285.17 Thio Solution 499.05 NytrosylSulphuric Acid H2SO 4 326.16 (from Sodium ThioSulphate 468 2 Solution and Spent Acid MT/Month HNO 3 71.08 (H2SO4)) Soda Ash 6.17 Charcoal 3.35 Anisol 207.57 Acetic 43.40 3.1 4-Methoxy Acetophenone 60 MT/Month anhydride catalyst 3.60 Toluene 1441.79 3.2 4-Methyl Acetophenone 60 MT/Month Catalyst 3.60 Acetic 159.85 Anhydride Furan 46.18 Furan 6.41 (Recycle) Catalyst 0.05 3.3 Acetyl Furan 60 MT/Month Catalyst 0.88 (Recycle) Acetic 69.33 Anhydride 179 Propionic Acid 4 Diethyl Ketone 315.04 MT/Month Butyric acid 103 100 5.1 Methyl Propyl Ketone MT/Month Acetic Acid 69 100 Butyric Acid 154 5.2 Dipropyl Ketone MT/Month Benzoic acid 91.07 100 5.3 Propiophenone MT/Month Propionic acid 135.71 Naphthalene 74.93 Nitric Acid 245.86 100 60% 6 Alpha Nitro Napthalene MT/Month Ethylede Dichloride 224.78 [EDC] [Fresh + Recycle] Naphthalene 156.90 Nitric Acid 515.25 Ethylene 470.71 Dichloride Alpha Napthylamine - 165 7 IPA/Methanol 287.48 Through Continuous Process MT/Month Aniline /ODCB 391.75 Hydrogen 7.32 Catalyst 21.26 Naphthalene 157.43 Nitric Acid 258.25 IPA/Methanol 287.61 OR Alpha Napthylamine - 165 7 Through Batch wise Process MT/Month Aniline /ODCB 393.58 Hydrogen 8.78 Catalyst 21.19 Aniline (Fresh) 41.79 An iline 56.25 (Recovered) Phenyl Alpha Naphthylamine 8 90 MT/Month (PANA) Alpha 64.29 Napthylamine Catalyst 1.61 DETA 5.85 Epichlorohydrin Based 116 Adipic Acid 7.8 9 Polyamide resin MT/Month EPI 3.51 1,3 - Dichlorobenze 56.34 ne [Fresh + Recycled] 2,4-Dichloro Acetophenone Catalyst 10 60 MT/Month (Fresh + 0.98 Recycled) Acetic 34.02 Anhydride Benzene [Fresh + 47.10 Recycle] Catalyst Acetophenone 11 60 MT/Month [Fresh + 0.82 Recycle] Acetic 53.53 Anhydride CyanoAcetami 47.25 de Water 300.00 IGBA - 3-(2- 28.2652MT/M methylpropyl)pentanedioic Sulphuric Acid 247.50 12.1 onth acid Toluene 117.00 3-Methyl 24.00 Butanal CyanoAcetami 47.37 de Sulphuric Acid 248.12 Sulphuric Acid 30.70 - Recycle KSM - 3-(2-amino-2- Toluene 117.29 oxoethyl)-5-methylhexanoic 40MT/Month 12.2 3- acid 24.06 methylbutanal Ammonium 17.59 Carbamide Caustic Lye 19.55 Charcoal 2.25 Phenol 100.04 100MT/Mont Dimethyl Anisol 95.79 13 h Carbonate Catalyst 1.96 PNA 69.81 Chlorine 71.80 MCB 349.06 NSA 167.71 3, 5 DCA 50MT/Month 14 NSA - 43.50 Recovered HCHO 51.89 Sulfur 42.45 Caustic Lye 110.59 2- Methyl Furan 1.109 EDC 0.080 DMF 0.060 POCl3 1.524 Allyl Chloride 0.661 D- Allethrollone 10 15 Toluene 0.050 THF 0.060 Mg Metal 0.205 Sodium Acetate 0.170 Acetic Acid 0.534 3-Methyl 4 - Nitro Imino Per 16 hydro1,3,5 Oxidiazine Formic Acid 0.16 N-Methyl Nitro Guanidine 0.78 20 Methane Sulphonic Acid 0.05 Caustic Lye 48% 0.39 DMF 0.09 Trans Cypermethrin Acid 3.000 Transfluthrin Acid Chloride 30 17 EDC 0.050 3.742 Caustic Lye 48% HCl 30% 3.663 n-Hexane 0.040 DMF 0.006 Thionyl Chloride 0.610 Formic Acid 1.94 1,2,4 Triazole 50 Ammonia 0.87 18 Hydrazine Hydrate 0.07 Benzyl Amine 0.912 Propanaldehy de 0.494 Toluene 0.075 Acetic Anhydride 0.802 2-Chloro 5-Chloromethyl 30 DMF 0.050 19 Pyridine (CCMP) Tri ethyl amine 0.048 EDC 0.130 Acetonitrile 0.100 Phosphorus Oxy Chloride 2.125 Chlorine 0.330 Caustic Lye 47% 1.000 ANNEXURE – 2 PLANT LAYOUT ANNEXURE – 3 MANUFACTURING PROCESS, CHEMICAL REACTION WITH MASS BALANCE 1. NITROSYL SULFURIC ACID (NSA) FROM SULFUR (OR SULFUR DIOXIDE GAS) Process Description: First make mix acid of Oleum 23 % and concentrate Nitric Acid . Charge Sulfur in to the mix acid from this process reaction takes place and generation SO 2 Gas (or charge Sulphur Dioxide gas in to the mix acid). SO 2 react with concentrate Nitric Acid and Oleum convert in to Sulphuric A cid after this reaction product will be Nitrosyl Sulfuric Acid (NSA). Reaction Mechanism 6 HNO3 + 2S 3N 2O3 + 2SO 3 + 3H 2O N2O3 + 2SO 3 + H 2O 2NOHSO 4 6HNO 3 + 8H 2SO 4 + 4SO 3 + 2S 6NOHSO 4 + 8H 2SO 4 OR H2SO 4 + HNO 3 + SO 2 NOHSO 4 + H 2SO 4 Flow Chart Oleum 23 % (7590 Kg) or Sulphur [420 kg] Or Sulphuric Acid 98% [6604 kg] Sulphur Dioxide Gas [1792 kg] MIX ACID Nitric Acid 98 % [7590 kg] Or Nitric Acid 98 % [1764 kg] 10160 kg NSA Nytrosyl Sulphuric Acid from Sulfur INPUT KG PROCESS KG OUTPUT Oleum 23 % or 7590 or 6604 10160 NSA Sulphuric Acid 98 % 2151 or 1764 Nitric Acid 98 % Mix Acid Vessel 1 SO 2 Sulphar or SO2 Gas 420 or 1792 Total 10161 10161 Total PRODUCT [2] NITROSYL SULPHURIC ACID (NSA) AND SULPHUR RECOVERY FROM SODIUM THIOSUIPHATE SOLUTION 1. Process Description with Chemical Reaction: Nytrosyl Sulphuric Acid from the spent sodium thio solution shall be manufactured only after getti ng permission from the Central Pollution Control Board [i. e. utilization of the hazardous wastes under Rule 11 of the Hazardous Waste (Management, Handling & Transboundary) Rules, 2008]. Sulfur and Sodium Sulphate shall be generated, only from the man ufacturing of Nytrosyl Sulphuric Acid from Sodium Thio Sulphate Solution (used as a raw material). Take Sodium Thiosuiphate Solution. Now take this solution in one vessel and add spent acid in it, Reaction takes place and SO 2 librates, Scrub this gas in another vessel which is having mix acid of H 2SO 4 and HNO 3. Mix Acid Vessel which has scrubbed SO 2 gas will make NITROSYL SULFURIC ACID [NSA]. SO 2 + HNO 3 NOHSO 4 [NSA] After completion of Spent Addition heat the solution till SO 2 librates then cool the mass and filter. Dry the residue to obtain SULPHUR. Filtrate will be collected separately, neutralize this solution and make concentrate by distillation water, then cool the mass, and Filter it. Residue will be dried and Product will be SODIUM SULPHATE, Filtrate will be used again. Na 2S2O3 + H 2SO 4 SO 2 + S + H 2O + NA 2SO 4 Flowchart: Nytrosyl Sulphuric Acid INPUT KG PROCESS KG OUTPUT INPUT KG PROCESS KG OUTPUT Thio 13097. Solutio SO 2633.56 NSA 40 % 2 48 n 14000 2633.56 SO 2 Spent NSA H SO H SO Acidifica 19366.4 Reaction 2 4 7862.32 ScruBBer 2 4 98 % (40 %) 8000 tion 4 Mass Vessel HNO 3 2601.6 98 % 13097.4 13097. Total Total Total 22000 22000 Total 8 48 Reacti Sulfur on 19366. Sulfur 1800 1420 Sulfur Dry W/C Mass 44 1800 W/C Dryer 17566.4 Reaction Water 380 4 Mass Evaporated Filtration Total 1800 1800 Total 19366.