Plot No. 38/10, GIDC Jhagadia Ind. Estate, Ankleshwar, Bharuch

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3 Sr. No Name of the Industry 1. Amar Pigments 2. Jay Overseas 3. Aarti Industries Limited 4. Shree Ganesh Remedies Ltd 5. Sagar Life Sciences Pvt. Ltd. 6. Subhashri Pigments 7. Gujarat State Fertilizer And Chemicals Ltd. Agenda for 194 th SEIAA Meeting (In continuation 396 th Meeting) to be held on P.M. Location Address Plot No , Phase- III, GIDC Panoli, Bharuch Plot No. A-2/4002, Nr. Crystal Crossway, GIDC Estate, Ankleshwar , Bharuch Plot No. CH-1+2/B, Dahej Ind. Estate, Vagra, Bharuch Plot No , GIDC Estate, Ankleshwar, Bharuch Plot No. 3124, 3125 & 3045, GIDC Estate, Panoli , Bharuch Plot No. J-1201, 1202, 1211, 1213, 1208, 1209 & 1209/A, GIDC Industrial Estate, Ankleshwar, Bharuch P.O. Fertilizernagar , Vadodara Category as per EIA Notification 2006 Date of Application Date of Recommendatio n issued by SEAC Page No. 5(f) (f) (f) (f) (f) (f) (e) Sun Industries Plot No. 38/10, GIDC Jhagadia Ind. Estate, Ankleshwar, Bharuch 5(f) Ambuja Intermediates Pvt Ltd Plot No. 41, Phase- II, GIDC Estate, Vatva, Ahmedabad 5(f) Cadila Healthcare Limited Plot No. 291, GIDC Estate, Ankleshwar, (Unit-1) Bharuch 5(f) Bifurcation of the project Sr. No Category as per EIA Notification 2006 Number of Project 1. Petroleum Products & Petrochemical Based Processing 5(e) 1 2. Chemical Project 5(f) 09 Total 10

4 Page 38 of 93 After detail deliberation the committee unanimously decided to recommend the proposal for grant of EC to SEIAA with following specific conditions 12 SIA/GJ/IND2/30827/2018 Shree Ganesh Remedies Ltd Plot No , GIDC Estate, Anklshwar,Bharuch Category of the unit : 5(f) Project status: Expansion Appraisal PP has submitted online application vide no. SIA/GJ/IND2/30827/2018 dated 01/02/2019 for obtaining Environmental Clearance. The SEAC had recommended TOR to SEIAA and SEIAA issued TOR to PP vide their letter dated 10/01/2019. Project proponent has submitted EIA Report prepared by Jyoti Om Chemical Research Centre Pvt. Ltd. based on the TOR issued by SEIAA. This is an existing unit engaged in Synthetic organic chemicals and now proposes for expansion as tabulated below: Sr. no. Name of the Products CAS no. / CI no. Quantity MT/Month Existing Propose Total d End-use of the products A Derivatives of Chlorination using Thionyl Chloride 1.. Bis (2Chloro Ethyl) Amine Piperazine derivative HCl (2-Chloro Ethyl)MorpholineHCl Intermediate for the synthesis of pharmaceuticals Chloro Ethyl Amine Piperazine derivative HCl. Di Methyl Amino Isopropyl Chloride HCl Piperazine derivative ChloroButyryl Chloride pyrazinamide 6. Methyl 4-Chlorobutyrate Pharmaceutical synthesis 7.. Cyclopropane Carbonyl Chloride Pharmaceutical products 8.. Cyclohexane Carbonyl Chloride Pharmaceutical products Furoyl Chloride Intermediate for the syntheses of pharmaceuticals 10. O-Acetylsalicyloyl Chloride Polymer Additive B Derivatives of Condensation Products Dimethyl Amino * API intermidiates Propyl Chloride HCl or Dimethylamino-2- methylpropyl chloride Intermediate for the syntheses of Page 38 of 93

5 Page 39 of 93 hydrochloride pharmaceuticals (Dibutylamino) Propyl Chloride Hydrochloride Pharmaceutical C Derivatives of Esterification Products 14.. Methyl Cyclopropane Carboxylate or * 7 10 Pharmaceutical 15.. Sorbyl Acetate (2, * 7 Chemical Hexadienyl Acetate) or 16.. Alkylsorbate( Methyl or 0 10 Pharmaceutical Sorbate or Butyl Sorbate) D Derivatives of Friedel Crafts Products Chloro 4-Fluro ButyroPhenone or * 2 7 Chemical 18.. Diphenylacetonitrile Intermediate for methadone, herbicide E Derivatives of Acidification Products 19. Cyclopropane Carboxylic * 3 5 Intermediate for Acid or pharmaceuticals Furoic Acid Preservative and a flavoring agent F Derivatives of Halogenation Products ChloroHexanol Pharmaceutical Chloro-5-hexanone Pharmaceutical 23. ChloroCycloHexane Pharmaceutical 24. Trityl Chloride or * 0 Pharmaceutical 25. Tyramine Hydrochloride or * 0 Pharmaceutical G Derivatives of Silicon Products 26. Sodium Bis Solution in THF or * 1 2 Pharmaceutical H Derivatives of Bromination Products Bromo-2-Methyl propane Used as synthetic reagent 28. BromofluoroBenzene Preparation of therapeutic drugs I Other Products Bromo 4-Propylheptane * 4 5 Pharmaceutical (Reduction/ Bromination) or 30. Dibenzosuberone (Reduction/ Halogenation) Pharmaceutical 31. R&D Products Total 5 * 180 In existing CCA AWH as per remark, Unit shall mfg either one product of products mentioned in sr.no. 1 with max. Quantity of 5 MT/Month. OR Unit shall mfg products mentioned in sr.no. 2, 3, & 4 with total quantity of 5 MT/Month. Unit will manufacture not more than six products at a time. Page 39 of 93

6 Page 40 of 93 The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification PP was called for presentation in the SEAC meeting dated 12/02/2019. Salient features of the project are as under: Sr. no. Particulars A Total cost of Proposed Project (Rs. in Crores): Details Existing: 3.33 Proposed: Total: EMP Cost: (I)Capital cost for EMS (Environmental Management System): 2.1Crores. (II)Recurring cost towards the environmental protection measures: 1.44 Crores per Annum. COMPONENT ADDITIONAL CAPITAL COST OF EMP RECURRING COST OF EMP (per Annum) TOTAL COST Rs. 2.1 Crore Rs Crore details of CER:CER Cost: Component As per Norms Allocation CER Rs. 15 Lakhs (1%) Rs. 15 Lakhs (1%) CER Cost: 0.15 Crore (This amount will be spent over the period of 5years after commissioning of project) Activities to be carried out under CER: As a part of up gradation of the hospital unit will up grading Truma centre make it most modern up gradation to meet the needs of the medical world. Letter for above CER activity from Ankleshwar Industrial development society is attached as annexure- XIII. B Total Plot area ( sq. meter) Existing: 14714Sq. m. Proposed: 00 Sq. m. Total: 14714Sq. m. Green belt area ( sq. meter) Existing: 1000Sq. m. Proposed: 2047Sq. m. Total: 3047Sq. m. C Employment generation Existing: 47 Proposed: 35 Total: 82 Page 40 of 93

7 Page 41 of 93 D Water i Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. GIDC water supply Water permission letter from GIDC, Ankleshwar is attached as Annexure-VI in EIA report. ii Water consumption (KLD) Existing Proposed Total after Remarks KLD (Additional) Expansion KLD KLD (F) Domestic Fresh water (G) Gardening Fresh water (H) Industrial Process Fresh + 7 recycle Washing recycle water Boiler Fresh Cooling fresh + 10 recycle Others Industrial Total Fresh + 19 Recycle Grand Total Fresh + (A+B+C) 19 Recycle 16) Total water requirement for the project: 69 KLD 17) Quantity to be recycled: 19 KLD 18) Total fresh water requirement: 50 KLD iii Waste water generation (KLD) Category Existing Proposed Total after Remarks Page 41 of 93

8 Page 42 of 93 KLD (Additional) Expansion KLD KLD (I) Domestic (J) Industrial Process Washing Boiler Cooling Others Total Industrial waste water Note:1) 10 KLD Domestic sewage water sent to septic tank/soak pit. 2) 4.7 KLD Existing quantity and quality of ETL will be maintained. 3) 21.8 KLD of treated waste water will be subjected to RO achieve reuse and recycle of treated water to its maximum. RO rejected 2.8KLD waste water sent to CMEE (BEIL), Ankleshwar for further treatment. 3) 19 KLD RO permeate water recycle in the process, washing and cooling tower within the plant premises. iv Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.. ETP: 50 KLD RO: 30 KLD v Mode of Disposal & Final meeting point Domestic: To soak pit Industrial: Treated in ETP and send to CETP (ETL) vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility CETP: Environ Technology Ltd., Ankleshwar CHWIF: Bharuch Enviro Infastructure Limited., Ankleshwar. Membership of Common facility (CF) Page 42 of 93

9 Page 43 of 93 (For waste water treatment) Effluent discharge permission letter from ETL (7.33 KLD) is attached as Annexure-VII in EIA report. Membership letter from CMEE (BEIL KLD) is attached as Annexure-VIII in EIA report. vii Simplified water balance diagram with reuse / recycle of waste water Water balance diagram after proposed expansion Total water requirement 69KLD (50 fresh + 19 Recycle) Process 23KLD (16 Fresh+ 7 Recycle) Washing 2 KLD recycle Boiler 15KLD Cooling Tower 14KLD (4 fresh + 10recycle) Domesti c 10KLD Gardenin g 5KLD Manufactur ing Process 9KLD Water from Dilute chemicals + impurity 3KLD Effluent 12KLD Scrubbing Agent Scrubb er 14KLD Scrubbed 20-35% HCl/Dil. HBr 8.5 KLD Loss 13KLD Blow down 2KLD Loss 12KLD Blow down 2KLD Sewage to Soak pit 10 KLD 4.7 KLD send to Other Scrubbed ETL solution to actual end user (5.5 KLD) ETP 26.5 KLD KLD RO 21.8 KLD RO Permeate 19 KLD RO Reject to CMEE (BEIL) 2.8 KLD Page 43 of 93

10 Page 44 of 93 Note: 1) Existing quantity & quality of ETL will be maintained. 2) For proposed expansion new ETP with RO will be installed. 3) RO reject will be sent to CMEE of BEIL. Total water requirement for the project: 69 KLD Total quantity to be recycle: 19 KLD. Total fresh water requirement: 50 KLD Existing wastewater discharge quality(4.7 KLD) Sr. After Parameters No. Treatment 1 ph T.D.S in mg/l T.S.S. in mg/l C.O.D. in mg/l Proposed wastewater discharge quality (4.7 KLD) Sr. After Parameters No. Treatment 1 ph T.D.S in mg/l T.S.S. in mg/l C.O.D. in mg/l vii Reuse/Recycle details (KLD) [Source of reuse & application area] Total reuse 19KLD Source of waste water for reuse with quantity in KLD Application area with quantity in KLD 19 KLD from RO 7 KLD in process, 2 KLD in washing and 10 KLD in cooling tower Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.) COD: <75 mg/l BOD: <30 mg/l TDS: <150 mg/l - E Air i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Page 44 of 93

11 Page 45 of 93 Existing & Proposed - Sr. no. Source of emission With Capacity Stack Height (meter) Type of Fuel Quantity of Fuel MT/Day Type of emissions i.e. Air Pollutants Air Pollution Control Measures (APCM) Existing 1 Boiler (1 TPH) 12 m 2 Thermic Fluid Heater (1 lac Kcal/Day.) (Commo n Stack) Natural Gas 45 NM 3 /Hr PM 150mg/ Nm 3 SO ppm NO 2 50ppm Adequate stack height Proposed 3 4 Boiler (3 TPH) 30 Thermic Fluid Heater (1 lac Kcal/Day.) 30 Natural Gas Natural Gas 150 NM 3 /Hr 350 kg/hour 5 D.G. Set 11 Diesel 40 Lit/Hr 6 Boiler (3 TPH) (Stand by) 30 Coal /Biocoal MT/D 11 MT/D 330 T/M -Note: 1) D.G. set will be run only in case of electricity failure. PM - 150mg/ Nm 3 SO2-100 ppm NOX - 50ppm PM - 150mg/ Nm 3 SO2-100 ppm NOX - 50ppm PM - 150mg/ Nm 3 SO2-100 ppm NOX - 50ppm Adequate stack height Adequate stack height Adequate stack height & acoustic enclosure Multi Cyclone +Bag Filter ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) Existing & Proposed - Page 45 of 93

12 Page 46 of 93 Specific Source Sr. no. of emission (Name of the Product & Type of emission Stack/Vent Height (meter) Air Pollution Control Measures (APCM) Process) Existing There is no process gas emission. - Proposed 1 Dryer PM 11 m Bag Filter Reaction vessel SO2 11 m Water Venturi 2 HCl Scrubber Followed By Caustic Scrubber Reaction vessel H2S 11 m Water Venturi 3 Scrubber Followed By Caustic Scrubber Reaction vessel HCl 11 m Water Venturi 4 HBr Scrubber Followed Br2 By Caustic Scrubber Reaction vessel NH3 11 m 5 Acid Scrubber iii Fugitive emission details with its mitigation measures. FUGITIVE EMISSION Sr. Source Probable No. 1 Solvent storage tank 2. Solvent recovery system 3 Handling of raw material bags in storage area Pollutant Emissio n Air pollutant (VOC) Air pollutant (VOC) Air pollutant (PM) Control Measures/ APCM Carry out work place area monitoring to find out concentration level in ambient air Close handling system Provision of breather valve cum flame arrester. Solvent recovery system with steam condensation system. Pumps & motors are mechanical seal type. Provision of exhaust ventilation Provision of PPE Provision of Job rotation to reduce exposure 4 Flange Air Routine & periodic inspection to check Page 46 of 93

13 Page 47 of 93 joints of pipeline, pump & motors 5 Solid raw material transferring to reactor 6 Liquid raw material transferring to reactor 7 Loading /unloading at storage area F Hazardous waste i pollutant (VOC) Air pollutant (PM) Air pollutant (VOC) Air pollutant (VOC) leakage Preventive maintenance, Follow SOP for maintenance Pumps & motors will be mechanical seal type LDAR program will be followed. Hopper will be provided with powder transfer system Feeding of liquid raw material will be carried out by closed pipeline and mechanical seal pump. Unloading through pipeline to tank in a close system. (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules Existing & Proposed Sr. n o. Type/Na me of Hazardou s waste 1. Empty Barrels/ Container s/ Liners contamina ted with hazardou s chemicals / wastes Source of generation (Name of the Activity, Product etc.) Packing of products & Raw Materials, Process Categ ory and Sched ule as per HW Rules. Existi ng Quantity (MT/Annum) Propo sed Tot al Managemen t of HW Collection, Decontamina tion, Generation & Disposal by send it to authorized decontamina tion facility/ recycler or reuse 2. Spent ion From mfg. exchange product no. 30, Collection, Storage and resin containing toxic metals 31 disposal by send to coprocessing/ Incineration at common incinerator of BEIL. 3. Chemical From ETP Collection, Page 47 of 93

14 Page 48 of 93 Sludge from waste water treatment storage, Disposal it to TSDF-BEIL Ankleshwar 4. Oily layer Collection, Storage, Transportatio n and coprocessing/ Incineration at common incinerator of BEIL. 5. Process or distillation residue 6. Spent Carbon or Filter Medium 7. Used or Spent Oil % HCl Solution 9. Dilute HBr Solution From mfg. product no. 4,5,10,15,17,22,2 4,27,28,29,30 From process/ ETP plant From Machinery From mfg. product no. 1,6,7,8,9,10 (From Scrubber) From mfg. product no. 1,6,7,8,9,10 (From Scrubber) Collection, Storage and Transportatio n and coprocessing/ Incineration at common incinerator of BEIL Collection, Decontamina tion, Disposal by sent it to Coprocessing/ common incineration at BEIL, Ankleshwar Collection, Storage, reuse in plant & machinery as lubricant or sell it to authorized re- refiners/ recycler B Collection, Storage, Transportatio n and disposal by neutralization in ETP. B Collection, Storage, Transportatio n and Page 48 of 93

15 Page 49 of % Sodium Bisulphite Solution 33-35% Sodium Bromide Solution Aluminiu m Chloride Solution From mfg. product no. 1,2,3,4,5,6,7,8,9, 10 (From Scrubber) From mfg. product no. 11,12,13 (From Scrubber) From process of Diphenylacetonitri le ii Membership details of TSDF, CHWIF etc. (For HW management) iii Details of Non-Hazardous waste & its disposal(msw and others) G Solvent management, VOC emissions etc. i B disposal by to end users having rule - 9 permission. Collection, Storage and disposal by sell out to authorized vendor under Rule 9 permission or in house disposal in ETP. B Collection, Storage and disposal by sell out to authorized vendor under Rule 9 permission or in house disposal in ETP Collection, Storage, Transportatio n and disposal by sell out to authorized vendor under Rule 9 permission or convert to PAC & sale to actual end user. TSDF: BEIL, Ankleshwar CHWIF: BEIL, Ankleshwar Not Applicable Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents Toluene, Methanol, Xylene, Aniline, Heptane, Cyclohexane, IPA, Ethylene Di Page 49 of 93

16 Page 50 of 93 Chloride, PTSA, Tetra hydro furan. Solvent recovery: 90-98% All the storage tank and day tank shall be connected to a vent system through cooling water and chilled brine condensers to prevent loss of solvents in the atmosphere. All the distillation column vents will be also connected to cooling water/chilled brine condensers for maximum possible recovery of the solvents. All the vents will be connected to a common carbon Absorber for removing traces of solvent from vent gases ii VOC emission sources and its mitigation measures To prevent losses of these solvents in atmosphere, following infrastructure shall be used in addition to LDAR program Leak Free Pumps for transfer of solvents MSW Gaskets in solvent pipelines to prevent leakage from flanges Minimum number of flanges, joints and valves in pipelines. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps. All the rotating equipment s like pumps will be installed with Mechanical Seals to arrest any sort of emissions. Condenser and scrubber post Reactor with cooling arrangement Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured. In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send to ETP. If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark. Two condenser will install with cooling water and chilled brine to recover the solvent. Primary Condenser HE-01: Cooling Tower water or Chilled water will be used to condense the solvents depend on the vapor pressure at its operating conditions and the non-condensedvapors will be condensed in a Secondary Condenser VOC Trap Condenser HE-02: Chilled Brine at -050C will be used to trap any traces of Solvent which is slipped from Secondary condenser During the meeting dated 12/02/2019, technical presentation made by project proponent. During the meeting, the project was appraised based on the information furnished in the EIA Report, details presented during the meeting. Page 50 of 93

17 Page 51 of 93 The baseline environmental quality has been assessed for various components of the environment viz. air, noise, water, biological and socioeconomic aspect. The baseline environmental study has been conducted for the study area of 10 km radial distance from project site for the period December to February Ambient Air Quality monitoring was carried out for PM 10, PM 2.5, SO 2, NO x, and VOC, NH3, HCL, CL2, CO at eight locations, including the project site. Values conform to the prescribed standards for Ambient Air Quality. The incremental Ground Level Concentration (GLC) has been computed using AERMOD. The resultant concentrations are within the NAAQS. The ambient air quality around the proposed project site will remain within the National Ambient Air Quality Standards (NAAQS). Risk assessment including prediction of the worst-case scenario and maximum credible accident scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site Emergency Plan has been covered in the RA report. During SEAC meeting on 12/02/2019, committee noted that the proposal is for expansion. This unit has valid EC & CC&A for existing unit. Copy of CC&A and EC, its compliance report is submitted. PP ensured that there are no court cases pending and no public complaints against the project. Source of water is GIDC. PP mentioned that effluent generated will be treated in primary, secondary & tertiary effluent treatment plant and treated effluent will be disposed to CETP of ETL, Ankleshwar as per existing CCA condition and additional quantity will be followed by RO, RO permeate shall be reused, while RO Reject shall be disposed in Common MEE of BEIL, Ankleshwar. PP has proposed two steam boiler, TFH & DG set. Fuel used will be Natural Gas/HSD. PP addressed Hazardous Waste as per HWR PP addressed EMP, CER with details of budgetary provisions was found satisfactory. After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant of Environmental Clearance. 13 SIA/GJ/IND2/30121/2017 Amidhara Enterprise Plot.No.80/7/2,Phase-I,GIDC,Vatva, Ahmedabad Appraisal Category of the unit : 5(f) Project status: Expansion PP has submitted online application vide no. SIA/GJ/IND2/30121/2017 dated 21/01/2019 for obtaining Environmental Clearance. The SEAC had recommended TOR to SEIAA and SEIAA issued TOR to PP vide their letter dated 01/08/2018. Project proponent has submitted EIA Report prepared by B. S. Rana based on the TOR issued by SEIAA. This is an existing unit engaged in Synthetic organic chemicals and now proposes for expansion as tabulated below: Sr. Name of the CAS no. / Quantity End-use no. Products CI no. MT/Month of the Page 51 of 93