For TOR Expansion Case

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1 SEAC, Gujarat: Page 1 of 12 For TOR Expansion Case 1. Basic Information of the Project: i. Name & Address of the Project site (Complete details with plot no. /Survey no., Landmark etc.) Sanhi Chemicals Plot No: 1712, Phase III, Notified Industrial Area, GIDC-Vapi, , Tal.: Pardi, Dist.: Valsad (Gujarat) ii. Name of the Applicant Mr. Sanjay Desai (Partner) iii. Address for correspondence Plot No: 1712, Phase III, Notified Industrial Area, GIDC-Vapi, , Tal.: Pardi, Dist.: Valsad (Gujarat) iv. Contact no. and ID of the Applicant Mob. No.: v. Aerial distance of nearest Habitat (KM) Chhiri 0.80 km in N direction vi. Longitude & Latitude of the Project Site: (4 corners of the site) vii. Category as per the Schedule to the EIA Notification 2006 i.e. 1(d), 2(b), 5(f) etc. viii. Applicability of General Conditions of EIA Notification 2006: i.e. Ensure that I. Protected areas notified under the Wildlife (Protection) Act, 1972; II. CEPI areas III. Eco-sensitive areas and IV. Inter-state boundaries and international boundaries; are not located within 5 km or 10 km (as the case may be) area from the boundary of the proposed site. Corner Latitude Longitude A 20 o N 72 o E B 20 o N 72 o E C 20 o N 72 o E D 20 o N 72 o E 5(f) -B as per EIA Notification 2006 General conditions are Not Applicable.

2 SEAC, Gujarat: Page 2 of Online application proposal No. : SIA/GJ/IND2/25878/ Date of application for TOR: 21/04/ Project status: Expansion 5. Product profile: # Product Name CAS Number Qty. MT/Month Existing Proposed Total Naphthylamine 4,6,8 tri Sulfonic acid (Sulpho G Acid) Nitro 2 amino phenol 6 Sulfonic acid (4 NAPSA) Nitro 2 amino phenol 4 Sulfonic acid (6 NAPSA) Amino Phenol 4- Sulfonamide (OPSAMIDE) Naphthyl amine 3,6,8 tri Sulfonic acid (KOCH ACID) M-Amino Phenol (MAP) Naphthol 3,6 di Sulfonic Acid (Violet Acid) Naphthol 3,8 di Sulfonic acid (EPSILONE ACID) Amino 8 Naphthol 4,6 Di Sulfonic Acid (European K Acid) Naphthylamine 4,8 Di Sulfonic Acid (C Acid) Chloro 5 - Toludine 4 - Sulphonic Acid (CLT Acid) Naphthylamine 8- Hydroxy 2,4 Di Sulfonic Acid (Chicago Acid) Amino Benzene Sulphonic Acid (Metanilic Acid) ,3 Di Nitro Di Phenyl Sulphone (3 3 DDS) Meta Nitro Benzene Sulphonic acid (Resist Salt) OR ,3 Di Nitro Di phenyl Sulphone Nitro 1-Di-Azo 2-Napthol 4-sulfonic Acid (6 Nitro 1,2,4 Diazo) Amino 5- Hydroxy Naphthalene-1,7 Di Sulphonic Acid (K Acid) Nitro Benzene Meta di Nitro Benzene N-Ethyl-N-Benzyl Aniline m-sulphonic Acid (EBAMSA) Para Phenylene Di Amine (PPD) Meta Nitro Para Toludine (MNPT) Di phenyl Epsilon Acid Naphthol 8- Sulfonic Acid

3 SEAC, Gujarat: Page 3 of Naphthol 4, 8 sulfonic Acid , 5 Di Nitro Benzoic Acid (3,5 DNBA) ,5 Di Amino Benzoic Acid (3,5 DABA) ,4,5 Tri Chloro Aniline Ortho Amino Phenol Meta Nitro Chloro Benzene (MNCB) N-N Di Ethyl -m- Amino Phenol (DEMAP) P-AMINO BENZOIC ACID DI Calcium Phosphate Total The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification Product wise Raw Material Consumption: Consumption in MT # Raw Materials CAS No. After MT/Tone Existing Proposed Expansion 1.0 For 2- Naphthylamine 4,6,8 tri Sulfonic acid (Sulpho G Acid) 1.1 Sulphuric Acid Oleum (65%) G-Acid Salt For 4-Nitro 2 amino phenol 6 Sulfonic acid (4 NAPSA) 2.1 Oleum (23%) PNCB Nitric Acid Caustic soda Salt NaHS For 6-Nitro 2 amino phenol 4 Sulfonic acid (6 NAPSA) 3.1 Oleum (23%) ONCB Nitric Acid Salt Caustic NaHS For 2- Amino Phenol 4- Sulfonamide (OPSAMIDE) 4.1 Chloro Sulfonic acid ONCB ONCB PSA Ammonia Caustic lye Iron Powder HCI For 1 Naphthyl amine 3,6,8 tri Sulfonic acid (KOCH ACID) 5.1 Naphthalene Sulphuric acid (98%) Oleum Nitric Acid

4 SEAC, Gujarat: Page 4 of Lime Stone Soda Ash Caustic Iron powder HCI For M-Amino Phenol (MAP) 6.1 Metanilic acid Caustic lye For 1-Naphthol 3,6 di Sulfonic acid (Violet Acid) 7.1 Naphthalene Sulphuric Acid 98% Oleum 65 % Lime Stone Sodium sulphate Caustic Flaks HCI Caustic lye For 1-Naphthol 3,8 di Sulfonic acid (EPSILONE ACID) 8.1 Oleum 65 % Sulphuric Acid (98%) Naphthalene Nitric Acid (98%) Lime Stone MgO Iron powder HCI Caustic lye Sodium Nitrite For 1- amino 8 naphthol 4,6 di sulfonic acid (European K Acid) 9.1 Naphthalene Sulphuric Acid (98%) Oleum 65 % Nitric Acid Lime stone Soda ash HCl Iron Caustic lye For 2- Naphthylamine 4,8 di Sulfonic acid (C Acid) 10.1 Naphthalene Sulphuric acid Oleum Nitric acid MgO HCl Iron Powder Caustic lye For 2 - Chloro 5 - Toludine 4 - Sulphonic acid (CLT acid) 11.1 Toluene Sulphuric acid Chlorine gas Ferric chloride Nitric acid

5 SEAC, Gujarat: Page 5 of % Dedanol OT Common salt Soda ash Iron HCl (30%) Caustic lye For 1- naphthylamine 8- hydroxy 2,4 di sulfonic acid (Chicago Acid) 12.1 Peri acid Oleum 65 % Sulphuric Acid (98%) Oleum (23%) Lime Soda Ash Caustic flaks Caustic lye HCI For 3- Amino Benzene Sulphonic acid (Metanilic Acid) 13.1 Nitro Benzene Oleum 65% Hydrated lime Soda ash CI Powder HCl Sulphuric acid For 3,3 Di Nitro Phenyl Sulphone (3 3 DDS) 14.1 Wet cake of 3,3 DDS For Meta Nitro Benzene Sulphonic acid (Resist salt) 15.1 Nitro Benzene Oleum 65% Hydrated lime Soda ash For 6-Nitro 1-Di-Azo 2-Napthol 4-sulfonic acid (6 Nitro 1,2,4 Diazo) 16.1 Caustic Lye Beta Naphthol Sodium Nitrate Sodium bi-sulfite Sulphuric acid Ice Oleum 23% Nitric acid For 4- Amino 5- Hydroxy Naphthalene-1,7 Di Sulphonic acid (K Acid) 17.1 B Naphthol Sulphuric Acid (98%) Oleum (65%) Ice Sodium Sulphate % Ammonia Sodium Bicarbonate Caustic lye For Nitro Benzene 18.1 Sulphuric acid Nitric acid Benzene

6 SEAC, Gujarat: Page 6 of Caustic soda For Meta di Nitro Benzene 19.1 Nitro Benzene , Nitric Acid Sulphuric acid Caustic lye For EBAMSA 20.1 EBA Oleum Sulphuric Acid Caustic lye For Para Phenylene Di amine (PPD) 21.1 PNA Iron HCl For Meta Nitro Para Toludine (MNPT) 22.1 P- Toluene Acetic Acid Nitric Acid Caustic lye For Di phenyl Epsilon Acid 23.1 Epsilon Acid Aniline Sulphuric Acid Naphthol 8- Sulfonic acid 24.1 Peri acid Sulphuric Acid NaNO Caustic lye For 1 Naphthol 4, 8 sulfonic acid 25.1 Peri acid Sulphuric Acid NaNO Caustic lye For 3, 5 Di Nitro Benzoic Acid (3,5 DNBA) 26.1 Benzoic Acid Sulphuric acid (98%) Nitric Acid (63%) Oleum (23%) For 3,5 Di Amino Benzoic Acid (3,5 DABA) 27.1 DNBA Iron HCl For 2,4,5 Tri Chloro Aniline 28.1 TCB Sulphuric acid Nitric acid Soda ash Iron HCl Sodium Nitrite Caustic lye

7 SEAC, Gujarat: Page 7 of For Ortho Amino Phenol 29.1 PNCB Caustic Fe HCI For Meta Nitro Chloro Benzene (MNCB) 30.1 Nitrobenzene , Chlorine Ferric Chloride Lime N-N Di Ethyl -m- Amino Phenol (DEMAP) 31.1 Matanilic acid Caustic Flakes Di Ethyl Sulphate ; Sulphuric acid For P-Amino Benzoic acid Nitro Benzoic acid Pd/C NaOH HCl H N For DI Calcium Phosphate 33.1 Rock Phosphate Spent Sulphuric Acid Lime Compliance Status of the Existing Project: S. No. Particulars Brief Information/Details Remarks 1. Earlier EC details Not Applicable Sanhi Chemicals was started in 2. Compliance of EC the year of 2010.Earlier the unit 3. Status of inspection by RO- MoEFCC, Bhopal. was known as M/S Solar Dyestuff Pvt. Limited and manufactured 4. Status of submission of half Dyes intermediates which was yearly return to concern started before We have authorities. purchased said premises in the year of 2010 along with land, plant, building and machineries and amend the existing CCA of the board. Hence, Environmental Clearance is not applicable for Existing Plant. 5. Compliance of existing CC&A We are complying with all CC&A Conditions Legal actions/closure No legal or closure order directions/scn etc. Issued issued by the board for last -- by GPCB. two years. 7. Any Public Complaints No Public Complaints Is there any litigation pending No Court Cases are before any court of Law against the Project? pending against the project --

8 SEAC, Gujarat: Page 8 of Water, Air and Hazardous Waste Management: S. No. Particulars A. Total cost of Proposed Project (Rs. in Crores): Capital cost for EMS: B. Total Plot Area (sq. meter) Existing: 4.08 Crores Proposed: 3.50 Crores Total: 7.58 Crores Existing: 0.10 Crores Proposed: 0.65 Crores Total: 0.75 Crores Details Recurring cost towards the environmental protection measures 4.10 Crores per Annum Existing: 5,000 m 2 Proposed: 0 m 2 Total: 5,000 m 2 Green belt area,/tree Plantation area (sq. meter) Existing: m 2 Proposed: m 2 Total: m 2 C. Employment Generation 1. Direct Existing: 20 Nos. Proposed: 30 Nos. Total:50 Nos. 2. Indirect Existing: Nos. Proposed: Nos. Total: Nos. D. Water i ii Source of Water Supply GIDC, Vapi Water Supply (GIDC, Bore Well, Surface water etc.) Status of permission from the concern authority. Permission issued by GIDC Vapi vide letter No. GIDC/DEE(W/S)/NA/VAPI/1285 on 09/04/2018 Water Consumption (KL/day) # Particulars Water Consumption, KLD Existing Proposed Total Remark Treated in A. Domestic septic tank/soak pit B. Industrial 1. Processing Cooling Boiler Washing Others C. Total Industrial D. Total (A+B+C) E. Condensate from MEE Net Fresh Water (D-E) ) Total water requirement for the project: 150 KLD 2) Quantity to be recycle: KLD 3) Total fresh water requirement: KLD Recycled in process iii Waste Water Generation (KL/day)

9 SEAC, Gujarat: Page 9 of 12 # Particulars Effluent generation, M 3 /day Existing Proposed Total Low High Low High Low High TDS/COD TDS/COD TDS/COD TDS/COD TDS/COD TDS/COD A. Domestic B. Industrial 1. Processing, product washing and scrubber Cooling Boiler Floor/container/equipment washing Total Industrial Total (A+B) Mode of treatment ETP - ETP MEE ETP MEE Net Discharge to CETP iv Treatment facility with capacity (ETP, CETP, MEE, STP etc) KLD ETP for Normal effluent KLD ETP for Concentrated effluent. v Mode of Disposal & Final meeting point Domestic: Domestic waste water (5.00 KLD) will be disposed-off through Septic Tank. Industrial: Total industrial Waste Water Generation will be 45.5 KLD, out of which 27.5 KLD of process water will be evaporated in proposed multi effect evaporator and balance 18 KLD of industrial effluent will be treated in existing primary & tertiary effluent treatment plant and finally treated effluent will be disposed off into CETP Vapi for further treatment and disposal into Arabian Sea. vi Reuse/Recycle details (KL/day) KLD vii Details of Rain water harvesting Shall be continued after proposed expansion B Air (Existing and Proposed) i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/h, MT/h, KVA etc. - # Type of Source of Emission Stack Quantity of Name of the emissions Emission With Capacity e.g. Height Fuel MT/h & APCM fuel i.e. Air Standard Boiler (8 TPH) (meter) MT/Day Pollutants EXISTING <PM: Thermopak: I (20 Lacs K Cal) PROPOSED Steam Boiler: II 1. (2 TPH) 2. Thermopak: II (25 Lacs K Cal) 30 Coal 500 kg/h 30 Coal 400 kg/h 30 Coal 550 kg/h PM SOx NOx PM SOx NOx Multi Cyclone & Bag Filter MDC & Bag Filter Multi Cyclone & Bag Filter 3. DG Set 11 HSD 115 kg/h Adequate Stack mg/nm 3, <SOx:100 ppm <NOx: 50 ppm <PM: 150 mg/nm 3, <SOx:100 ppm <NOx: 50

10 SEAC, Gujarat: Page 10 of 12 ii v C i (500 KVA) Height ppm Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) (Existing and Proposed) # Particulars Existing After Proposed Expansion Remarks 1.0 Expected Pollutants from Sulphonation Reaction & Sulphonation Reaction & Oleum Storage Oleum Storage 1.1 Pollutants SO 2, SO 3 SO 2 Existing will be utilized 1.2 APC Provided Two Stage Acid followed by Two Stage Acid followed by Alkali Alkali Scrubber Scrubber 1.3 Height of vent 11 m 11 m 2.0 Expected Pollutants from --- Chlorination Reactor Two Stage Water followed by 2.1 APC Provided 0 Alkali Scrubber Proposed 2.2 Height of Vent 0 11 m 2.3 Expected Emission 0 HCl: <20 mg/m 3 Cl2: < 5 mg/m Stack attached to --- Nitrator 3.1 Pollutant 0 Nox 3.2 APC Provided 0 Two Stage Alkali Scrubber Proposed 3.3 Height of Vent 0 11 m 3.4 Expected Emission 0 NOx: <25 mg/m Stack attached to --- Amidator 4.1 Pollutant 0 NH APC Provided 0 Two Stage Water Scrubber followed by Acid Scrubber Proposed 4.3 Height of Vent 0 11 m 4.4 Expected Emission 0 NH3: <175 mg/m 3 Fugitive emission details with its mitigation measures. (Existing and Proposed) Concrete road is already developed within plot premises to avoid fugitive dust due to vehicle movement. Manufacturing activity is being/will be carried out in closed reactors/vessels and Regular checking and maintenance of the same is being/will be carried out to avoid any leakages. All the raw materials are being /will be stored in closed containers and in sealed bags and will be handled through closed system to avoid the handling losses. Hazardous Waste (As per the Hazardous and Other Wastes (Management and Tran s boundary Movement) Rules (Existing and Proposed) # Type Quantity, TPA Existing Proposed Total Disposal 1. Used Oil (Sch: I /5.1) Discarded Containers (Sch: I /33.1) Sell to registered recycler 3. Waste from ETP (Sch: I/ 35.3) Dispose off into TSDF, Vapi 4. Process Waste Sell to cement industries or (Sch: I/26.1) dispose off into TSDF, Vapi Utilize for manufacturing of 5. in-house di calcium Spent Acid (45-78%) phosphate or sell to actual (Sch: I/26.3) users under hazardous waste rules Hydro Chloric Acid (30%) Recycle in the process or sell

11 SEAC, Gujarat: Page 11 of (Sch: I/26.3) Sodium Bi Sulphite Soln. (48%) (Sch: II/B23) Ammonium Sulphite (40%) Soln. (Sch: II/B1) Sludge from Wet Scrubber (Sch: (I/37.1) Salt from MEE (Sch: I/35.3) to actual users under hazardous waste rules 2016 Sell to actual users under hazardous waste rules 2016 Sell to actual users under hazardous waste rules 2016 Dispose off into ETP/MEE for treatment Dispose off into TSDF, Vapi 11. Fly Ash Sell to Brick manufacturers Quantity of discarded containers must be in MT/Annum. ii Membership details of CETP, TSDF, CHWIF, VWEMCL certificate for CETP for acceptance of additional Common MEE etc. effluent vide letter No. CETP_Member.Certi/1944/17486 dated:21/04/2012 & Common Solid waste disposal membership No. 516 dated 21/04/2012 ii Details of Non-Hazardous waste & its disposal (MSW and others) Fly Ash 1160 TPA will be generated after expansion and sold to brick manufacturer. D i Spent Solvent Management (If any) No use of Solvent ii VOC emission sources and its mitigation measures Source: Process Reactor Raw material Handling & Storage Mitigation Measures: The raw materials will be stored in closed containers and will be handled through closed system to avoid the handling losses Reactor and solvent handling pumps will have mechanical seals to prevent leakages. Reactors shall also be provided with breather valve to prevent losses. Details of Environmental Consultants: S. No. Particulars Details i. Name of the Consultant Eco Chem Sales and Services ii. Validity of Certificate of accreditation issued by the NABET, QCI The accreditation certificate number NABET/EIA/1720/RA 051 is valid up to 3 rd February 2020 iii. Accreditation for the categories 22 sectors including 5(f) - A iv. Any other details -- Name & Designation of the Applicant: Mr. Sanjay Desai (Partner) Stamp & Signature of the Applicant:

12 SEAC, Gujarat: Page 12 of 12 Date: 20/04/2018 General Instructions: Format shall be in WORD Format (Page size-a4, Font type- Arial, Font size- 11) Provide authenticated (with stamp & Signature) hard copy during presentation. Kindly mail to: and copy to all members. Above data should be as per application Form-1 & PFR. Incorporate relevant details in respective column of the above format. Do not attach as Annexure in Format.

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