Minutes of the 554 th meeting ofthe State Level Expert Appraisal Committee (SEAC) held on 01/10/2019 at Committee Room, Gujarat Pollution Control Board, Sector 10A,Gandhinagar.

The 554 th meeting of the State Level Expert Appraisal Committee (SEAC) was held on 1st October 2019 at Committee Room, Gujarat Pollution Control Board, Sector 10A, Gandhinagar. Following members attended the meeting:

1. Dr. Dinesh Misra, Chairman, SEAC 2. Shri S. C. Srivastav, Vice Chairman, SEAC 3. Shri Rajesh. I. Shah, Member, SEAC 4. Shri V. N. Patel, Member, SEAC 5. Dr. V. K. Jain, Member, SEAC 6. Shri A. K. Mule, Member, SEAC

The regular agenda of Appraisal, Screening & Scoping/ToR, Reconsideration cases were taken up. The Committee considered the applications made by project proponents, additional details submitted as required by the SEAC/SEIAA and details furnished in the Form-1, PFR, EIA-EMP reports.

Proposal No. Name and Address of the Unit Remarks

04 SIA/GJ/IND2/29059/2017 M/s. Dev Dyechem Industries EC – Plot No. C-1/324, Phase-I & II GIDC – Reconsideration Naroda, Ahmedabad. • PP remained absent in the EC – Appraisal presentation held on 01/10/2019. • After detailed discussion, Committee decided to defer the proposal and consider the same in one of the upcoming meeting of SEAC. 05 SIA/GJ/IND2/29678/2018 M/s. Apex Pharma EC – C-298/2/4, Saykha Industrial Estate, Reconsideration Saykha, Ta- Vagra, Dist -Bharuch.

Category of the unit: 5(f) Project status: New

• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/29678/2018 dated 30/04/19 for obtaining Environmental Clearance. • SEIAA issued ToR to PP vide their letter dated 10/01/2019.

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• Project proponent has submitted EIA Report prepared by Greenleaf Envirotech Pvt Ltd, Suratbased on the ToR issued by SEIAA.

Sr. Quantity Name of the Products CAS No. / Cl no. End-use of the Products No. MT/Month Asthma. 1. Acebrophylline 179118-73-1 Chronic obstructive pulmonary disease. Non-ulcer dyspepsia. 2. Itopride HCl 122892-31-3 Gastroparesis. Nausea and vomiting.

Fexofenadine Seasonal allergic rhinitis. 3. 153439-40-8 Hydrochloride Chronic Utricaria.

Vasodilator Prescribed for long term memory 4. Xanthinol Nicotinate 437-74-1 disorders. Lack of concentration. Colesevelam Cholesterol-lowering . 5. 182815-44-7 Hydrochloride Glycemic control in diabetes 6. Flavoxate HCl 3717-88-2 Overactive Bladder Hyperphosphatemia for chronic 7. Sevelamer HCl 152751-57-0 kidney disease 8. Fenofibrate 49562-28-9 Hypercholesterolemia for heart attack Asthma and other obstructive 9. Doxofylline 69975-86-6 diseases 10. Sucralfate 54182-58-0 Treatment of ulcers in the intestine

Feeling like the world is spinning 10.00 11. Betahistine Dihydrochloride 5579-84-0 (vertigo), ringing in the ears (tinnitus), hearing loss Hyperphosphatemia for chronic 12. Sevelamer Carbonate 845273-93-0 kidney disease Treat, bloating, swelling, feelings of 13. Pamabrom 606-04-2 fullness, in menstrual symptoms

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Depression, generalanxiety disorder, 14. Venlafaxine 93413-69-5 socialphobia, panic disorder, andvasomotor symptoms Heart attack, trauma, surgery, heart 15. Dopamine HCl 3739-02-1 failure, kidney failure, and other serious medical conditions. Dissolution of cholesterol rich gallstones. 16. Ursodeoxylic Acid 128-13-2 Primary biliary cirrhosis. Cystic fibrosis. O – Desmethyl Venlafaxine 17. 93413-62-8 Anti-depressive agent Succinate Monohydrate 1 – [Cyano – (4 – 18. Methoxyphenyl) Methyl] 93413-76-4 Intermediate product of Venlafaxine Cyclohexanol (VF – 1) Tauro Ursodeoxychloic 19. 14605-22-2 Chronic cholestatic liver diseases Acid 20. Indapamide 26807-65-8 Treat high blood pressure 21. Febuxostat 144060-53-7 Febuxostat is used to treat gout. Treatment of Epilepsy which is a 22. Oxcarbamazepin 28721-07-5 brain disorder Erectile Dysfuntion 23. Tadalafil 171596-29-5 Pulmonary arterial hypertension Benign prostatic hyperplasia Control seizures. 24. Gabapentine 60142-96-3 Relieve nerve pain Treat pain caused by nerve damage 25. Pregabalin 148553-50-8 due to diabetes Treat joint diseases such as 26. Diacerein 13739-02-1 osteoarthritis Treat a certain type of seizure 27. Esclicarbazepine Acetate 236395-14-5 disorder

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28. Benfotiamine 22457-89-2 For diabetes Treat heavy bleeding during your 29. Tranexamic Acid 1197-18-8 menstrual period 30. Amrozole HCl 23828-92-4 Treatment of respiratory diseases

10 31. R&D - Kg/Month 10.00 Total MT/Month • This is a new unit proposes for manufacturing of Synthetic Organic Chemical as tabulated below:

• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006.

• During the meeting dated 13/06/2019, technical presentation made during the meeting by project proponent.

• Salient features of the project including Water, Air and Hazardous waste management (Revised): • During the meeting, the project was appraised based on the information furnished in the EIA Report, and details presented during the meeting. • 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 October 2018 to December 2018. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, NH3, Cl2,O3,Pb, As, Ni, CO and VOC at Nine 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 ISCST – 3 model. The resultant concentrations are within the NAAQS. The modeling study proved that the air emissions from the proposed plant would not affect the ambient air quality of the region in any significant manner. 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, committee noted that the proposal is for Greenfield Project in GIDC- Saykha. PP mentioned that all the effluent generated will be treated in primary ETP and primary treated effluent further treated in solvent stripper followed by in-house spray dryer for further treatment and disposal. Committee asked for worst case scenario of effluent generation for proposed project to which PP could not explained satisfactorily.

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• Committee noted that PP has not addressed ToR No. 1 and ToR No. 2 satisfactorily.

• Committee insisted for revised details regarding safety measures and storage of Cl2 and flameproof fitting for solvents handling. Committee insisted for revised need based CER activities as per Greenfield project cost and adequacy of recovery of methanol more than 96.9%.Committee insisted for revised hazardous waste matrix as sodium hydrogen sulphide generation from scrubber is not match with process emission details and scrubbing media and MoU for selling of hazardous waste to Rule – 9 permission unit.

• Committee deliberated on ambient air baseline data and surface water data for proposed project. PP has addressed in details regarding for baseline data of proposed project. • After deliberation, SEAC unanimously decided to consider the proposal after submission of the following details. 1) Readdress water balance diagram considering worst case scenario of effluent for proposed project and adequacy with technical justification regarding proposed products in which water goes along with product 2) Readdress specific ToR no-1 regarding adequacy of in-house spray drying of effluent and its impact on surrounding area Environment and human health with technical justification and characteristic of inlet effluent to spray dryer and outlet characteristic of spray dryer gaseous emission. 3) Readdress specific ToR no-2 with technical justification regarding total reuse of spent solvent, Isopropyl alcohol, and liquor Ammonia within plant premises. 4) Revised details regarding safety measures and storage of Cl2 and flameproof fitting for solvents handling and revised need based CER activities with budgetary provision for next five years as per Greenfield project cost. 5) Submit MoU with end users who are having permission under Rule 9 to purchase the hazardous waste and revised hazardous waste matrix with justification regarding sodium hydrogen sulphide generation from scrubber. 6) Technical justification regarding methanol recovery more than 96.9%. • Project proponent made presentation for the above mentioned query dated 05/09/2019 for the above mentioned points. • PP presented replied as below: 1) PP presented revised water balance diagram considering worst case scenario of effluent for proposed project and adequacy with technical justification regarding proposed products in which water goes along with Product however there is still some mistakes observed in water balance diagram. 2) PP presented specific ToR no - 1 regarding adequacy of in-house spray drying of effluent and its impact on surrounding area Environment and human health with technical justification and characteristic of inlet effluent to spray dryer and outlet characteristic of spray dryer gaseous emission, however characteristic of

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effluent after phenton treatment was not observed satisfactory. 3) PP presented specific ToR no - 2 with technical justification regarding total reuse of spent solvent, Isopropyl alcohol, acetic acid and liquor Ammonia within plant premises. 4) PP presented details regarding safety measures and storage of Cl2 and flameproof fitting for solvents handling and revised need based CER activities with budgetary provision for next five years as per Greenfield project cost, however committee observed that safety aspects pertaining to chlorine safety measures has not been addressed satisfactorily. 5) PP presented MoU with end users who are having permission under Rule 9 to purchase the hazardous waste and revised hazardous waste matrix with justification regarding sodium hydrogen sulphide generation from scrubber. 6) PP presented technical justification regarding methanol recovery more than 96.9%. • Committee observed that reply submitted by PP is not satisfactory. • After detailed discussion, it was decided to consider the proposal only after revised submission of all the queries in the minutes dated 13/06/2019 (515 th IND2 Projects) with proper technical justification and proper safety aspects. • Project proponent made presentation for the above mentioned query dated 01/10/2019 for the above mentioned points. • PP presented replied as below: 1) PP presented revised water balance diagram considering worst case scenario of effluent for proposed project and adequacy with technical justification regarding proposed products in which water goes along with product. 2) PP presented specific ToR no - 1 1 regarding adequacy of in-house spray drying of effluent and its impact on surrounding area Environment and human health with technical justification and characteristic of inlet effluent to spray dryer and outlet characteristic of spray dryer gaseous emission. 3) PP presented specific ToR no - 2 with technical justification regarding total reuse of spent solvent, Isopropyl alcohol, acetic acid and liquor Ammonia within plant premises. 4) PP presented details regarding safety measures and storage of Cl2 and flameproof fitting for solvents handling and revised need based CER activities with budgetary provision for next five years as per Greenfield project cost. 5) PP presented MoU with end users who are having permission under Rule 9 to purchase the hazardous waste and revised hazardous waste matrix with justification regarding sodium hydrogen sulphide generation from scrubber. 6) PP presented technical justification regarding methanol recovery more than 96.9%. • Committee observed that reply submitted by PP is satisfactory. 554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 6 of 215

• Salient features of the project including Water, Air and Hazardous waste management (Revised):

Sr. Particulars Details no . A Total cost of Proposed Project 3.30 Crores (Rs. in Crores): ii EMP details (Capital cost & Recurring cost)

Brief details of EMP

COMPONENT CAPITAL COST OF EMP RECURRING COST OF EMP (per Month)

Cost Rs. 48.9 Lakhs Rs. 10.06 Lakhs

Bifurcation of EMP Cost Sr. Unit Installed Capital Operating Maintenance Total No Capacity Cost (Rs. Cost Cost Recurring (KLD) in Lakhs ) (Lacs/Month) (Lacs/Month) Cost (Lacs/Month) 1 Effluent 8 KLD 25 4.52 0.4 4.92 Treatment Plant & Spray Dryer 2. APCM -- 21.0 0.18 0.07 0.25 3. Hazardous -- 1 4.29 -- 4.29 Waste (Expense) 4. AWH -- 1 0.1 -- 0.1 Monitoring Cost 5. Greenbelt -- 0.9 0.45 0.05 0.5 Total 48.9 10.06

iii CER details (As per MoEF&CC OM dated 01/05/2018) As per OM no. 22-65/2017 on dated 01/05/2018 regarding “Corporate Environment Responsibility” (CER),

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Greenfield projects have to contribute 2% of the Capital Investment (Rs. 3.3 Crore) , the company will contribute Rs. 6.6 Lakhs as funds for CER activities Component As per Norms Allocation CER Rs. 6.6 Lakhs (2 %) Rs. 6.6 Lakhs (2 %) Activities to be carried out under CER:

CER Activities Fund (Rs.)

2020- 2021- 2022- 2023- 2024- Year 2021 2022 2023 2024 2025

As per discussion with Sarpanch, we will give contribution towards Rain Water 60,000/- 80,000/- 60,000/- -- -- Harvesting System & Plantation in community area to Sayakha Village .

As per discussion with Sarpanch, we will provide RO System (2 KLD 2 Nos.) to -- 60,000/- 60,000/- 80,000/- -- remove TDS in Drinking Water in Kothiya & Sankhwad Village .

Infrastructure facility to hospitals and education institutions. Government Primary School located in nearby area -- -- 80,000/- 80,000/- 1,00,000/- as infrastructure and other educational support. i.e. books, computers, stationaries etc. Village: Vagra

1,40,000 2,00,000 1,60,000 1,00,000 TOTAL 60,000/- /- /- /- /-

GRAND TOTAL 6,60,000/-

B Total Plot area (sq. meter) 2441.12 Sq. m. Green belt area ( sq. meter) 806.35 Sq. m. C Employment generation Direct = 49 Employees Indirect = 10 Employees D Water

554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 8 of 215 i Source of Water Supply GIDC Water Supply (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. Permission will be obtained ii Water consumption (KLD)

Category Water Consumption Remarks (KLD) (A) Domestic 2.0 -- (B) Gardening 2.5 -- (C) Industrial Maximum process water consumption Process 5.0 in product no. 29 (Tranexamic Acid) Washing 1.5 -- Boiler 15.0 -- Cooling 2.0 -- Others 2.0 WC in scrubber Industrial Total 25.5 -- Total (A + B + C) 30.0 -- 1) Total water requirement for the project: 30.0 KLD 2) Quantity to be recycled : -- KLD 3) Total fresh water requirement: 30.0 KLD iii Waste water generation (KLD)

Category Waste Water (KLD) Remarks (A) Domestic 1.8 -- (B) Industrial Maximum process waste water generation Process 3.0 from product no. 29 (Tranexamic Acid) Washing 1.5 -- Boiler 0.3 -- Cooling 0.2 -- Others 0.5 WWG from Scrubber Industrial waste 5.5 --

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water Total Industrial 7.3 waste water [A + B] - The domestic waste water will be allowed to Septic Tank/Soak Pit. - Total Industrial waste water@ 5.5 KLD WWG from process: 3 KLD will be subjected to solvent stripper for recovery of solvent (0.05 KLD). Boiler/Cooling Blow down@ 2.0 KLD + 0.5 KLD from Scrubber & Approximately 3.0 KLD from Stripper will be treated in ETP &subjected to in-house spray dryer. iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ETP (8.0 KLD): Primary treatment will be given within premises. Treatment scheme including segregation at source. • Segregation Concentrated (Process) stream will be allowed in Stripper & then to ETP. • Dilute stream from Boiler/Cooling Blow down & Scrubber will be directly treated in ETP. • High COD (3.0 KLD) ranges from 24000 mg/L (Oxcarbamazepin) to 75000 mg/L (Esclicarbazepine Acetate). • Low COD (2.0 KLD) ranges from <100 mg/L (Boiler blowdown) to 2500 mg/L (Washing section) Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP. Not Applicable Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): • Composite effluent stream will be subject to Spray Dryer after giving primary treatment in ETP followed by solvent stripper. v Mode of Disposal & Final meeting point Domestic: Domestic Wastewater of 1.8 KL/Day will be disposed through Soak Pit or Septic Tank. Industrial: Composite effluent stream will be subjected to Spray Dryer after giving primary treatment in ETP followed by solvent stripper. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , Name of CF Not Applicable Membership of Common facility (CF) (For waste water treatment)

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Not Applicable vii Simplified water balance diagram with reuse / recycle of waste water All figures are in KL/Day

viii Reuse/Recycle details (KLD) Total reuse 0 KLD Source of waste Remarks regarding feasibility to reuse water for reuse Application area with i.e. w/w characteristics (COD, BOD, with quantity in quantity in KLD TDS etc.) KLD ------

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. - Sr. Source of Stack Type of Fuel Quantity Type of Air Pollution no. emission Height of Fuel emissions i.e. Control With (meter) MT/Day Air Pollutants Measures Capacity (APCM) 1 Steam Boiler 12.0 Bio Coal / 2.5 PM MCS+ Bag

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(1 TPH) Imported MT/Day SO 2 Filter

Coal NO x 2 Thermic Fluid Bio Coal / 2.5 MCS+ Bag Heater(5.00 L Imported MT/Day Filter Kcal/Hr) Coal 3 D. G. Set (225 7.0 HSD 63 Liter/Hr Adequate Stack KVA – 01 No.) Height - ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) - Stack / Specific Source of Sr. Vent Air Pollution Control emission (Name of the Type of emission No. Height Measures (APCM) Product & Process) (meter) Reaction Vessel Two stage water + 3 1. SO 2< 40 mg/Nm 11 (Sulphonation) Alkali Scrubber

3 Reaction Vessel Cl 2 < 9 mg/Nm Two stage water + 2. 11 (Chlorination) HCl< 20 mg/Nm 3 Alkali Scrubber Reaction Vessel Two stage water + 3. HBr< 30 mg/Nm 3 11 (Bromination) Alkali Scrubber Reaction Vessel Two stage water 3 4. NH 3< 175 mg/Nm 11 (Amination) Scrubber Two Stage Water Spray Dryer PM<150 mg/Nm 3 Scrubber 5 25 3 (Effluent) NH 3< 175 mg/Nm & Cyclone Separator& carbon column - Iii Fugitive emission details with its mitigation measures. As below: Following measures will be adopted to prevent and control fugitive emissions 1. Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures.

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2. Raw materials loading and unloading will be done in covered area 3. Care will be taken to store construction material properly to prevent fugitive emissions, if any. 4. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs. 5. Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature. 6. Periodic monitoring of work area will be carried out to check the fugitive emission. 7. Breather valves will be provided on solvent tanks. 8. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps. 9. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers. 10. Minimum number of flanges, joints and valves in pipelines. 11. 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. 12. Adequate ventilation will be provided. 13. Periodic monitoring of work area will be carried out to check the fugitive emission as per the norms of Gujarat Factory Rules. F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Note: *We have submit the MOU at the time of Consent to Operate (CTO) from the Board. - Sr. Type/Name Source of Category Quantity Disposal Method no of generation and (MT / . Hazardous Schedule Annum) waste as per HW Rules.

1 Discarded Raw material & Sch-I / 33.3 8.0 Collection, Store & Transportation, Containers / Finished product & disposed by selling to registered Bags / Liners packing material recycler or Returned back to its supplier

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2 Used Oil DG Set Sch-I / 5.1 0.5 Collection, Store & Transportation, & disposed by sending to registered Re refiners or Used for lubrication of machineries at our unit

3 Chemical Effluent Treatment Sch-I / 35.3 6 Collection, Storage, Transportation Sludge from plant and Disposal at TSDF site (M/s. Waste Water BEIL Dahej) – for secured landfill Treatment

Process (Product- Sch-I / 20.2 4090 Collection, Storage, In-house Benfotiamine) recovery by distillation & reuse in 4 Spent process Solvent Stripper 18

5 Distillation Distillation Process Sch-I / 28.1 42 Collection, Storage, Transportation Residue (Many Products) and sent to co-processing industry or CHWIF for Incineration. (M/s. SEPPL/DIPL, Kutch)

6 Organic Salt Process (Product- Sch-I / 28.1 15.6 Collection, Storage, Transportation Xanthinol and sent for co-processing industry Nicotinate) or Send to CHWIF for Incineration(M/s. SEPPL/DIPL, Kutch)

7 Process (Product- SCh-I / 28.3 19.2 Collection, Storage, Transportation Waste Venlafaxine) and sent for co-processing based on CV / for reactivation OR send to CHWIF (M/s. SEPPL/DIPL, Kutch).

8 Iso Propyl Process (Product- Sch-I / 28.1 135.6 Collection, Storage and Recovered Alcohol Xanthinol /Reuse entire generation quantity Nicotinate) within premises. Required quantity in the manufacturing process of Ursodeoxylic Acid

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375.6 KL/Annum.

9 NaCl Salt Process (Product- Sch-I / 28.1 14.4 Collection, Storage, Transportation Tauro Ursodeoxy and Disposal at TSDF site – for chloic Acid) secured landfill

10 Acetic Acid Process (Product- Sch-I / 28.1 170.16 + Collection, Storage and Recovered Diacerein & 93.6 KL = /Reuse entire generation quantity Esclicarbazepine 263.76 KL within premises. Acetate) Required quantity in the manufacturing process of Benfotiamine600 KL/Annum.

11 Organic Process (Product- Sch-I / 28.1 79.2 Collection, Storage, Transportation Residue Esclicarbazepine and sent to co-processing industry Acetate) or Send to CHWIF for Incineration (M/s. SEPPL/DIPL Kutch.)

12 Barium Process (Product- Sch-I / 28.1 418.8 Collection, Storage, Transportation Carbonate Tranexamic Acid) and sell to end users having permission under Rule-9*.

13 Process (Product- Sch-I / 28.1 114 Collection, Storage, Transportation Sulphate Tranexamic Acid) and sell to end users having permission under Rule-9*.

14 Spent HCl Process (Product- Sch-I / 28.1 420 Collection, Storage, Transportation (30%) 1 – [Cyano – (4 – and sell to end users having permission under Rule-9*. Methoxyphenyl) Methyl]

Cyclohexanol (VF – 1) & Benfotiamine) 15 Spent Process (Product- Sch-I / 28.1 1800 Collection, Storage, Transportation H2SO4 (35- Tranexamic Acid) and sell to end users having

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40 %) permission under Rule-9*.

16 Sodium Scrubber (Product- Sch-I / 28.1 90 Collection, Storage, Transportation Hydrogen Itopride HCl & and sell to end users having Sulphide Tranexamic Acid) permission under Rule-9*.

17 Sodium Scrubber (Product- Sch. II 90 Collection, Storage, Transportation Bromide / Pregabalin & and sell to end users having B-36 Hydrogen Amrozole HCl) permission under Rule-9*. Bromide

18 Liquor NH 3 Scrubber (Product- Sch. I /28.1 90 Collection, Storage and Reuse Tranexamic Acid) entire generation quantity within premises (Required Quantity 111.6 MT/Year which is utilized in Product-Tranexamic Acid)

19 NaCl Salt Scrubber Sch-I / 28.1 90 Collection, Storage, Treatment in ETP & subjected to Spray dyer (15-20%) (Product- Gabapentine) 20 Scrubbing Spray Dryer Sch-I / 35.3 90 Collection, Storage, Transportation Solution & disposal by Incineration at CHWIF (M/s. SEPPL Kutch.)

21 Spray Dryer Spray Dryer Sch. I / 35.3 180 Collection, Storage, Transportation Salt and Disposal at TSDF site(M/s. BEIL Dahej) – for secured landfill

ii Membership details of TSDF, CHWIF etc. Company has membership of TSDF Facility (For HW management) of M/s. BEIL dated 07/03/2019. Unit will get membership of CHWIF/Coprocessing facility of M/s. SEPPL/DIPL Kutch. iii Details of Non-Hazardous waste & its disposal No such waste will be generated. (MSW and others) G Solvent management , VOC emissions etc.

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I Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents Maximum recovery of each solvent will be more than 90 %. Recovered solvent will be again reuse within premises.

ii VOC emission sources and its mitigation measures Sources - Charging Materials Measures

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- Enclose Process - Minimum flanges & joints - Handled by pump with double mechanical seals - Proper Ventilation - Adequate PPEs H ‹ Details regarding storage of Hazardous Chemicals Storage Name of major Hazardous chemicals Remarks details Storage Methanol Store at ATP Tanks Drum/Barrel DMF, Toluene, Thionyl chloride, Iso propyl Alcohol, Hydrochloric Acid, Storage Ethyl acetate, Epichlorohydrine, 2-Methylamino Ethanol, 1- Bromodecane, Sulphuric Acid, Bromethyl, Pyridine, Hydrobromic Acid, Epichlorohydrin, Acetone, Formic Acid, Formaldehyde, Hydrochloric Acid 20%, N – Methyl Pyrolidone, 4 – Methoxy Phenyl Acetonitrile, Cyclohexanone, Triethyl Amine, Ethyl Chloroformate, Triethyl Amine (TEA), Tetrahydrofuran (THF), Ammonium Hydroxide, Acetic Anhydride, Dimethyl Acetamide, Dichloromethane, Acetyl Chloride, Benzoyl Chloride, Acetic Acid, Methyl Anthranilate, Hydrogen peroxide, Tetrahydrofuran Cylinder Chlorine Store at Cool, Dry & well ventillated area Glass Bottle Bromine Store at dry & well ventillated area ‹ Applicability of PESO : Unit will obtain permission from peso for storage of solvent.

• After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant of Environmental Clearance with the following Specific Condition. 1. All necessary safety measures as per the prevailing guidelines shall be taken to avoid any kind of accident during use, storage and handling of Chlorine gas. 2. Unit shall provide safety precaution for storage and handling of Chlorineas per the PESO standards.

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06 SIA/GJ/IND2/36321/2018 M/s. Stermone Chemicals Pvt. Ltd. EC – Sr. No./Plot No. 34/1, Paldi-Golana Road, Paldi, Reconsideratio Khambhat, Ananad. n

Category of the unit : 5(f)

Project status : Expansion • Project proponent (PP) has submitted online application vide no. SIA/GJ/IND2/36321/2018dated 12/06/2019 for obtaining Environmental Clearance. • SEIAA issued TOR to PP vide letter dated 30/06/2018. • Project proponent has submitted EIA Report prepared by M/s: Excel Enviro tech based on the TOR issued by SEIAA. • Public Hearing was conducted by Gujarat Pollution Control Board on 03/05/2019 at project site of M/s: Stermone Chemicals Pvt. Ltd, Sr. No./Plot No. 34/1, Paldi-Golana Road, Paldi, Ta- Khambhat, Dist –Anand. • This is an existing unit engaged in Synthetic organic chemicals and now proposes for expansion as tabulated below:

Sr. CAS no. / Quantity, MT/Month End-use of the Name of the Products no. CI no. Existing Proposed Total products

1 Beclomethasone 4419-39-0 25 0 25 Healthcare Dipropionate 2 Betamethasone Diropionate 5593-20-4 50 0 50

3 Betamethasone I.P. 378-44-9 5 0 5

4 Betamethasone Sodium 151-73-5 50 0 50 Phosphate 5 Betamethasone Valerate 2152-44-5 50 0 50

6 Clobetasone Propionate 25122-46-7 40 0 40

7 Clobetasone Butyrate 25122-57-0 10 0 10

8 Dexamethasone and 2392-39-4 50 0 50 Sodium Phosphate 9 Fluticasone Propionate 80474-14-2 15 0 15

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10 Hydrocortisone 50-23-7 20 0 20

11 Hydrocortisone Acetate 50-03-3 20 0 20

12 Furoate 105102-22-5 20 0 20

13 Prednisolone Acetate 52-21-1 25 0 25

14 Prednisolone Sodium 125-02-0 25 0 25 Phosphate 15 58-22-0 0 2,260.5 2,260.5 Healthcare

16 57-85-2 0

17 5949-44-0 0

18 58-20-8 0

19 Decanoate 360-70-3 0

20 Nandrolone 62-90-8 0 Phenylpropionate 21 Acetate 10161-34-9 0

22 Trenbolone Enanthate 10161-33-8 0

23 Methandienone 72-63-9 0

24 434-07-1 0

25 10418-03-8 0

26 5630-53-5 0

27 Hydroxyprogesterone 630-56-8 0 Caproate 28 Norathisterone Acetate 51-98-9 0

29 Norathisterone Enanthate 3836-23-5 0

30 797-63-7 0

31 54024-22-5 0

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32 67392-87-4 0

33 57-83-0 0

34 432-60-0 0

35 60282-87-3 0

36 52-76-6 0

37 107868-30-4 0

38 50-28-2 0

39 Estrinol 50-27-1 0

40 Estradiol Cypionate 313-06-4 0

41 Ethinyl Estradiol 57-63-6 0

42 84371-65-3 0

43 53-39-4 0

44 Medroxy Progesterone 71-58-9 0 Acetate 45 Aceate 595-33-5 0

46 154229-18-2 0

47 Betamethasone 378-44-9 0 8,487 8,487 Healthcare

48 Betamethasone Acetate 987-24-6 0

49 Betamethasone Dipropionate 5593-20-4 0

50 Betamethasone Valerate 2152-44-5 0

51 Betamethasone Sodium 151-73-5 0 Phosphate 52 Clobetasol Propionate 25122-46-7 0

53 Clobetasone Butyrate 25122-57-0 0

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54 Dexamethasone 50-02-2 0

55 Dexamethasone Sodium 2392-39-4 0 Phosphate 56 Dexamethasone Acetate 1177-87-3 0

57 Deflazacort 14484-47-0 0

58 Hydrocortisone Acetate 50-03-3 0

59 Prednisolone 50-24-8 0

60 Prednislone Acetate 52-21-1 0

61 Prednisone 53-03-2 0

62 Prednisolone Sodium 125-02-0 0 Phosphate 63 Beclomethasone 5534-09-8 0 Dipropionate 64 Mometasone Furoate 83919-23-7 0

65 164656-23-9 0

66 Halobetasol Propionate 66852-54-8 0

67 Fluocinolone Acetonide 67-73-2 0

68 Fluocinonide 356-12-7 0

69 Triamcinolone 124-94-7 0

70 76-25-5 0

71 Triamcinolone 5611-51-8 0 Hexaacetonide 72 Difluprednate 23674-86-4 0

73 Methylprednislone 83-43-2 0

74 Methylprednisolone Acetate 53-36-1. 0

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75 Fluticasone Propionate 50-24-8 0

76 Fluromethonolone 52-21-1 0

77 Loteprednol Ethabonate 53-03-2 0

78 Diflucortolone Valerate 125-02-0 0

79 Desoximethasone 5534-09-8 0

80 Eplerenone 83919-23-7 0

81 164656-23-9 0

82 Hydrocortisone 66852-54-8 0

Total 405.0 10,747.5 10,747.5

• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 13/08/2019. • During the meeting dated 13/08/2019, technical presentation made by project proponent. • During the meeting, the project was appraised based on the information furnished in the EIA Report, various issues raised during the public hearing and details presented during the meeting. • 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 March 2018 to May 2018. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, HCl and VOC 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 model. The resultant concentrations are within the NAAQS. The modelling study proved that the air emissions from the proposed plant would not affect the ambient air quality of the region in any significant manner. 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. • This unit is having valid EC and CC&A for existing unit. Copy of EC and CC&A, its compliance report are submitted. PP ensured that there are no court cases pending and no public complaints against the project. • During SEAC meeting, Committee asked for certified compliance report by MoEF&CC, Bhopal or RO site visit

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report, PP informed about unit is fully complied EC order conditions. Committee asked about area adequacy of proposed expansion as huge expansion in proposed project, PP informed that by mistake proposed expansion is shown in MT/Month instead of Kg/Month. PP informed that one SCN issued by the Board and Compliance of SCN submitted by the unit. Committee asked about various written and oral suggestions and complaints against project during public hearing, PP informed that in presentation in briefs. Committee insisted for adequate details reply of written instruction of Akhol gram panchayat regarding bad odor and foul odor nuisance due to proposed project and water usage and its source from ground water details asked by village development Jagruti abhiyan. Committee asked about justification regarding water consumption showing 37 KL/Day and recycle of wastewater is 14 KL/Day and thus maintaining water consumption less than 25 KL/Day, PP could not satisfactorily addressed about it. Committee asked about existing and proposed waste water treatment, PP informed that the mother liquor stream generated from the manufacturing activities of 6.0 KLD shall be given primary treatment in existing ETP units and incinerated in existing incinerator of capacity 300 L / Hour. The concentrated stream of 10.0 KLD from manufacturing activity shall be taken to stripper for solvent recovery. After solvent recovery effluent of 6.0 KLD along with the dilute stream from boiler, cooling tower, RO reject, scrubber and washing of 10.5 KLD shall be given primary, secondary and tertiary treatment and then sent to in-house MEE. Committee asked about adequacy of Incinerator adequacy as per CPCB guidelines and MEE capacity with total mass balance of RO and MEE with its recycle quantity details. Committee informed about to submit proposal for adequate APCM as per CPCB guideline with incinerator and solid fired boiler for proposed project. Committee insisted for readdressed ToR no-12 regarding best available technology (BAT) adopted for proposed project in details. Committee asked to submit revised hazardous waste matrix submission with mentioning about separate spent solvent for in-house distillation disposal and outside solvent recycler selling disposal with its quantity. Committee insisted for detailed LDAR for each solvent utilize for each product with solvent recovery and solvent losses. • After deliberation, SEAC unanimously decided to consider the proposal after submission of the following details. 1. Revised product profile as per ToR in Kg/Month instead of MT/Month. 2. Submit adequate detailed reply of written representation of Akhol gram panchayat regarding bad odor and foul odor nuisance due to proposed project and adequate water usage and its source from ground water data asked by village development Jagruti abhiyan during public hearing. 3. Readdressed air details matrix considering adequate APCM as per CPCB guideline with incinerator and adequate APCM with solid fuel fired boiler instead of cyclone separator and subsequently revised EMP along with capital and recurring cost. 4. Submit justification regarding water consumption showing 37 KL/Day and recycle of wastewater is 14 KL/Day and thus maintaining water consumption less than 25 KL/Day along with adequacy of recycle

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water from RO and MEE with its mass balance of input and output of effluent from RO and MEE. 5. Adequacy of existing incinerator for proposed expansion project with its technical design details for effluent to be incinerated. 6. Readdress Tor No- 12 regarding adoption of best available technology (BAT) for proposed project in details. 7. Readdressed Hazardous waste matrix showing separate spent solvent management i.e. in-house distillation disposal and outside solvent recycler selling disposal with its quantity. 8. Readdressed detailed LDAR for each solvent utilize for each product with solvent recovery and solvent losses. • Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned points. • PP presented replied as below: 1. PP presented revised the product profile as per ToR in Kg/Month instead of MT/Month. 2. PP presented adequate detailed reply of written representation of Akhol gram panchayat regarding bad odor and foul odor nuisance due to proposed project mention that now they will use “Triethylamine” instead of “Pyridine” along with adequate water usage and its source from ground water data asked by village development Jagruti abhiyan during public hearing. 3. PP presented air details matrix considering adequate APCM as per CPCB guideline with incinerator and adequate APCM with solid fuel fired boiler instead of cyclone separator and subsequently revised EMP along with capital and recurring cost. 4. PP presented justification regarding water consumption showing 37 KL/Day and recycle of wastewater is 14 KL/Day and thus maintaining water consumption less than 25 KL/Day as follows; (1) Total Water Requirement = 37 KLD, (2) Reuse/Recycle = 14 KLD, (3) Fresh Water Requirement = 23 KLD, along with adequacy of recycle water from RO and MEE with its mass balance of input and output of effluent from RO and MEE. 5. PP presented adequacy of existing incinerator for proposed expansion project with its technical design details for effluent to be incinerated and also committed to follow CPCB guidelines. 6. PP readdressed ToR No- 12 regarding adoption of best available technology (BAT) for proposed project in details. 7. PP readdressed Hazardous waste matrix showing separate spent solvent management i.e. in-house distillation disposal and outside solvent recycler selling disposal with its quantity. (Outside CEPI area) 8. PP readdressed detailed LDAR for each solvent utilize for each product with solvent recovery and solvent losses. • Committee observed that reply submitted by PP is satisfactory. • Salient features of the project including Water, Air and Hazardous waste management (Revised): 554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 25 of 215

Sr. Particulars Details no. A Total cost of Proposed Project 9.52 crore. (Rs. in Crores): B Total Plot area 14,404 m2 ( sq. meter) Green belt area 4754.0 m 2 ( sq. meter) C Employment generation Existing : 43 Proposed:45 Total: 88 D Water i Source of Water Supply GWSSB (Gujarat Water Supply (GIDC Bore well, Surface water, Tanker supply etc...) and Sewerage Board) through pipeline. Status of permission from the concern authority. Permission Obtained. Refer Annexure VI of EIA Report ii Water consumption (KLD)

Sr. Remark Particulars Water Consumption KLD No. Total Fresh Total Existin water Reuse Proposed g After Expansion 1. Domestic 0.25 4.75 5.0 -- 2. Gardening 0.90 2.1 3.0 -- 3. Industrial 2 KLD will be reused in process a. Process 0.90 15.1 16.0 2.0 after proposed expansion

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6 KLD will be reused in boiler b. Boiler 0.20 6.8 7.0 6.0 after proposed expansion 2 KLD will be reused in Cooling c. Cooling 0.20 1.8 2.0 2.0 after proposed expansion 3 KLD will be reused in washing d. Washing 0.10 2.9 3.0 3.0 after proposed expansion 1 KLD will be reused in process e. Scrubber 0.0 1.0 1.0 1.0 after proposed expansion Total Industrial 1.4 27.6 29.0 14.0 Total (1 + 2) 2.55 34.45 37.0 -

Total Water Consumption – 37 KLD (Fresh 23 + Reuse 14) Domestic Wastewater disposed in Soak Pit – 3.0 KLD iii Waste water generation (KLD)

Sr. Remark Particulars Wastewater Generation KLD No. Propose Existing Total d 1. Domestic 0.2 2.8 3.0 2. Gardening 3. Industrial 6 KLD to MEE and a. Process 0.41 15.59 16.0 10 KLD stripper and to then to ETP

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b. Boiler 0.02 0.68 0.7 c. Cooling 0.02 0.18 0.2 d. Washing 0.10 2.9 3.0 To ETP e. Scrubber 0.0 1.0 1.0 f. RO Reject 0 6.0 6.0 Total Industrial 0.55 26.35 26.9 Total (1 + 2) 0.75 29.15 29.9

iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.. Incinerator – 300 L/Hour ETP consisting of primary, secondary and tertiary treatment of capacity 16.50 KLD MEE – 1500 kg/hour

Treatment scheme including segregation at source. • The mother liquor stream generated from the manufacturing activities of 6.0 KLD shall be given primary treatment in existing ETP units and incinerated in existing incinerator of capacity 300 L / Hour. • The concentrated stream of 10.0 KLD from manufacturing activity shall be taken to stripper for solvent recovery. After solvent recovery effluent of 6.0 KLD along with the dilute stream from boiler, cooling tower, RO reject, scrubber and washing of 10.5 KLD shall be given primary, secondary and tertiary treatment and then sent to in-house MEE. • The condensate recovered from MEE shall be reused for various industrial purposes. • Domestic wastewater is disposed through a septic tank from septic tank it would be taken by Khambhat Nagarpalika through tankers. Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ Not Applicable as it is zero discharge system Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): • The mother liquor having high COD (15,000 mg/L – 25,000 mg/L) generated from the manufacturing activities of 6.0 KLD shall be given primary treatment in existing ETP units and incinerated in existing incinerator of capacity 300 L / Hour.

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• The process stream of @ 10.0 KLD having COD (10,000 mg/L – 15,000 mg/L) shall be taken to stripper having capacity of 1000 kg/hour for solvent removal. • The wastewater stream of @6.0 KLD after solvent recovery shall be taken to ETP consisting of primary, secondary and tertiary treatment. • The dilute stream of @10.2 KLD from boiler, cooling tower, RO reject, scrubber and washing shall be treated in ETP along with wastewater stream after solvent recovery. Hence, @ 16.2 KLD of effluent shall be treated in ETP having capacity of 20.0 KLD. • The effluent of @ 16.2 KLD after giving primary, secondary and tertiary treatment shall be evaporated in MEE having capacity 1500 kg/hour. v Mode of Disposal & Final meeting point Domestic: Septic Tank Industrial: Zero Liquid Discharge – ETP, Incinerator & MEE vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF)(For waste water treatment) ‹ In-house facility Membership of Common facility (CF) (For waste water treatment) : Not Applicable vii Simplified water balance diagram with reuse / recycle of waste water

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Water Consumption 23 KL/Day

Domestic Industrial Gardening 5 KL/Day 15 KL/Day 3 KL/Day

Septic Tank Process Boiler Washing Cooling Scrubber RO 3 KL/Day 14+2 (recycle) 1+6 (recycle) 3 KL/Day 2 KL/Day 1 KL/Day Reject KL/Day KL/Day

0.2 KL/day 0.7 KL/Day 3 KL/Day 1 KL/Day 6 KL/Day

Concentrated stream / Stream MotherLiquor 10 .2 6 KL/Day 10 KL/Day 6.0 KL/Day ETP (Primary, Stripper Secondary, Tertiary) Incinerator 16.2 KL/Day

4.0 KLD MEE 2.0 KLD Losses

Recycle 14 KL/Day vii Reuse/Recycle details (KLD) [Source of reuse & application area] Total reuse 14 KLD Source of waste Remarks regarding water for reuse Application area with feasibility to reuse i.e. w/w with quantity in quantity in KLD characteristics (COD, BOD, KLD TDS etc.) Boiler 6 MEE Condensate having TDS Process 2 < 500. Washing 3 Cooling 2 Scrubber 1 Total 14.0

E Air i Flue gas emission details

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No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Existing & Proposed Height Sr. Fuel Stack attached of Revised No Fuel Consumpti APCM Parameter to Stack, APCM . on m Existing Multi Multi Boiler Briquett Dust 1. 13.0 100 kg/Hour Cyclone 1 TPH e Collector Separator * Particulate D.G. Set Adequate Matter 2. (Stand-By 125 11.0 Diesel 20 Lit./Hour stack -- <150mg/Nm KVA) height 3

Proposed SO2 < 100 D.G. Set Adequate ppm 3. (Stand-By 500 11.0 Diesel 40 Lit./Hour stack -- NOx< 50 KVA) height ppm Multi Boiler Briquett Cyclone Dust 4. 13.0 200 kg/Hour 2 TPH e Separator Collector * *Unit will install Multi Dust Collector in place of cyclone separator.

ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) Existing & Proposed

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-

Specific Air Pollution Source of Stack/Vent Control Sr. emission Type of emission Height Measures no. (Name of the (meter) (APCM) Product &

Process) SO2 <40 mg/Nm 3 NOx< 25 mg/Nm 3 3 HCl < 20mg/Nm Water Chlorine <09 mg/Nm 3 Scrubber Incinerator Ammonia <175mg/Nm 3 1 30.0 followed by (Existing) H2S <45 mg / Nm 3 Alkali 3 Mercaptan <0.5 mg/ Nm Scrubber CS2 <180 (By Volume) CO <150 mg/ Nm 3 Hydrocarbon <45 mg/ Nm 3

iii Fugitive emission details with its mitigation measures. • Regular sprinkling of water, pacca road shall be constructed & green belt shall be provided within premises to prevent fugitive emissions due to vehicular movement. Regular maintenance of vehicles. • General control measures like routine & regular inspection to identify leakage, preventive maintenance and operational maintenance, provision of leak detection and repair system (LDAR) and potable instrument for measurement of VOC etc. will be implemented by the unit. • Management to ensure proper handling of the spillages during transfer, charging operation and provision of a Dust Collection System for collection of the air borne material wherever applicable. • Preventive maintenance of flange connections and glands of pumps. • Management will also ensure proper usage of the Personnel Protective Equipment by the workers. • Closed handling system shall be provided for chemicals. • Reflux condenser to be provided over the reactor.

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• The acids shall be taken from storage tanks to reactor through closed pipeline. Storage tanks shall be vented through trap receiver and condenser operated on chilled water. • Fugitive emissions in the work zone environment, product raw material storage area shall be monitored regularly. F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Existing & Proposed i Sr Quantity . Type of Categ (MT/Annum) Source Mode of Disposal N Waste ory Propos Tot Existing o. ed al Spent Collection, Storage, Manufacturing 1. Catalyst/Spe 28.2 0.35 4.0 4.35 Transportation and Disposal at Process nt Carbon TSDF site Collection, Storage, Distillation Solvent 2. 20.3 1.0 12 13 Transportation and Disposal at Residue Distillation Rule-9 supplier or CHWIF Incineration of Collection, Storage, Incinerator 13.2 3. Concentrated 37.2 1.25 12 Transportation and Disposal at Ash 5 Stream TSDF site From Primary Collection, Storage, and Secondary 4. ETP Sludge 35.3 0 12 12 Transportation and Disposal at Treatment of TSDF site Effluent The total quantity of spent solvent will be 4800 MT/Annum, unit will be reusing Spent Manufacturing 480 4320 MT/Annum, and 480 5. 28.6 0 4800 Solvent Process 0 MT/Annum will be sent to out- side recycler/co-processing unit. MOU with M/s. Amidhara is

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already obtained.

Collection, Storage, 6. MEE Salt From MEE 35.3 0 20 20 Transportation and Disposal at TSDF site Plant Equipment 100 7. Waste Oil 5.1 0.1 0.2 Sold to authorized vendors &Machineries L/Year 200 Raw Material & 8. Empty Bags 33.1 Nos./Ye 3.8 4.0 Sold to authorized vendors Product ar 200 Barrels/ Raw Material & 9. 33.1 Nos./Ye 2.8 3.0 Sold to authorized vendors Container Product ar Collection, Storage, 10 Date Expired Product Storage 28.5 --- 3.6 3.6 Transportation and Disposal at . Product Coprocessors 11 Boiler Ash Boiler Operation ------500 500 Collection, Storage and Reuse .

ii Membership details of TSDF, CHWIF etc. The unit has got the membership of (For HW management) common facility for TSDF and incineration at Nandesari Environment Control Ltd. Membership certificate is attached as Annexure-IX in EIA Report iii Details of Non-Hazardous waste & its As per local disposal(MSW and others) G Solvent management , VOC emissions etc i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. Recover Use Losses y % Solvents Used MT/Mont MT/Mont Product Remarks MT/Mont recovery h h h Acetic Anhydride 12.43 12.18 97.99 0.1827 Hormon Recover Acetone 27.12 26.58 98.01 0.3987 es ed /

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Acetonitrile 9.94 9.74 97.99 0.1461 Reused Ethanol 169.53 166.14 98.00 2.4921 Within Ethyl Acetate 67.81 66.45 97.99 0.9968 Process Hexane 14.7 14.41 98.03 0.2162 /Disposa Iso Propyl Ether 53.46 52.39 98.00 0.7859 l at Rule- Di Chloro Methane (MDC) 169.74 166.35 98.00 2.4953 9 Methanol 65.34 64.03 98.00 0.9605 supplier N,N Dimethyl Formamide 12.43 12.18 97.99 0.1827 for co- Pyridine 5.4 5.29 97.96 0.0794 processi Tetra Hydro Furan (THF) 29.38 28.79 97.99 0.4319 ng Toluene 27.12 26.58 98.01 0.3987 Maximum Solvent (Worst 169.74 166.35 98.03 2.50 Case) Acetone 84.87 83.17 98.00 1.2476 Recover Acetonitrile 135.79 131.52 96.86 1.9728 ed / Chloroform 64.5 63.21 98.00 0.9482 Reused Di Methyl Formamide 33.94 33.26 98.00 0.4989 Within (DMF) Process Ethanol 107.36 105.21 98.00 1.5782 / Ethyl Acetate 172.28 168.83 98.00 2.5325 Disposal Ethyl Chloroformate 51.34 49.86 97.12 0.7479 at Rule-9 Iso Propyl Alcohol (IPA) 77.23 75.69 98.01 1.1354 supplier Iso Propyl Ether (IPE) 53.46 52.39 98.00 0.7859 for co- Di Chloro Methane (MDC) 169.74 166.35 98.00 2.4953 processi Methanol 65.34 64.03 98.00 0.9605 ng Pyridine 28.007 27.45 98.01 0.4118 Tetra Hydro Furan (THF) 53.04 51.98 98.00 0.7797 Maximum Solvent (Worst 172.28 168.83 98.00 2.5325 Case)

ii VOC emission sources and its mitigation measures VOC Emission sources solvent handling. Mitigation Measures: • Identification of potential areas, where possibility of flammable mixture/VOC are possible.

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• Efforts to avoid hazardous mixtures, by inert gas purging and other methods. • Declaring hazard zones & providing flame proof electrical fittings & equipment. • Providing Explosion Vents in spaces with possibility of air-vapour mixtures. • Smoke detectors or heat detectors to be provided in storage or process area. • Providing adequate fire control devices. • Providing arrangements to avoid static sparks. • Take care of adverse weather conditions. • Safe access to the top of the process and storage area car. • Adequate personal protective equipment to be provided. • Emergency shower and eye washer to be provided. • Ensure that sufficient space is available in the storage area. • Necessary training of personnel. • Avoid mixing of chemicals. Take full precautions. • Routine thorough check-up procedures. • Proper identification on discharge lines. • Solvent storage tank shall be provided with breather valve to prevent losses. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks Storage tanks Drum/Barrel storage 2-5 bistrifluro Aneline, 4 - Methyl - 1 – Cyclohexane, Acetone, Ammonium Hydroxide, Bromopropane, Butyl Lithium, Chloropropane, Chloroform, Decanoyl Chloride, Dimethylformamide, Ethy Acetate, Ethyl Chloroformate,Hexane, Iso Propyl Alcohol (IPA), Iso Propyl Ether, Di Chlor Methane, Methanol, Methyl Formate, Methyl Sulphonyl Chloride, Propionic Anhydride, Sodium hydroxide (NaOH), Triethanolamine (TEA), Toluene, Tri Ethyl Amine

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‹ Applicability of PESO : Not Applicable ‹ PESO not required. After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant of Environmental Clearance with following conditions: 1. Unit shall strictly comply the all three conditions of small units as defined in the amendment to EIA Notification, 2006 vide SO 1599 (E) dated 25/06/2014. i.e. (i) Water consumption less than 25 M3/day; (ii) Fuel consumption less than 25 TPD; and (iii) not covered in the category of MAH units as per the Management, Storage, Import of Hazardous Chemical Rules (MSIHC Rules), 1989 as per the legal undertaking submitted with EIA report. 2. Isolated storage and industrial activity at a site handling (including transport through carrier or pipeline) of hazardous chemicals shall not equal to or, in excess of the threshold quantities specified in the Management, Storage, Import of Hazardous Chemical (MSIHC) Rules, 1989 for Major Accident Hazards (MAH) installations. 07 SIA/GJ/IND2/37270/2018 M/S. HEMANI CHEMIORGANIC PVT. LTD. EC – Reconsideration Plot No. A1/301, 303, Chemical Zone, Notified Industrial Area, GIDC Sarigam. Umbergaon, Valsad. Category of the unit: 5(f) Project status: New • Project proponent (PP) has submitted online application vide no. SIA/GJ/IND2/32270/2018 on dated 20/06/2019 for obtaining Environmental Clearance. • The SEAC had recommended TOR to SEIAA and SEIAA issued TOR to PP vide their letter dated 29/01/2019. • Project proponent has submitted EIA Report prepared by Eco Chem Sales & Service, Surat based on the TOR issued by SEIAA. • This is a new unit proposes for Synthetic Organic Chemicals manufacturing as tabulated below: CAS Capacity, # Product End Use of the Product Number TPM

2,4 Di Nitro Chloro Benzene (2,4 1. 97-00-7 1000 Dyes and Dyestuff Intermediates DNCB)

2. Para Nitro Aniline (PNA) 100-01-06 500 Dyes

3. Para Chloro Aniline (PCA) 106-47-8 500 Dyes ,Basic Pharma

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4. Para Phenylene Di Amine (PPDA) 106-50-31 200 Dyes

5. P Anisidine (PA) 104-94-9 100 Azo Dyes

It is used as an solvent for 6. 2,4 Di chloro Aceto Phenone (DICAP) 2234-16-4 100 Plastics, Resins, Cellulose Ethers, and Esters

7. Para/ortho Amino Phenol (PAP/OAP) 123-30-8 500 Cosmetics

6 Nitro 2 Amino Phenol 4- Sulphonic 8. 96-93-5 200 Dyes Acid (6- NAPSA)

Total --- 3100

• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 25/07/2019. • During the meeting dated 25/07/2019, technical presentation made by project proponent. • 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 2018 to February 2019. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx 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. • 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, committee noted that the proposal is for new unit at GIDC Sarigam. Water source is GIDC. • During meeting, Committee asked for proposed production size, PP informed that proposed plot size is adequate for proposed production. Committee asked about wastewater management, PP informed that high COD effluent after ETP treatment will be evaporated in in-house MEE cum ATFD. Low COD effluent will be treated in primary, secondary and tertiary ETP units and will be discharged into GIDC drainage leading to CETP of GIDC Sarigam. Committee asked for BAT adopted for proposed project, PP informed that they will adopt BAT for proposed product but committee insisted for mentioning BAT for proposed products. PP informed about characteristic of high COD and Low COD effluent and CETP to be discharged into CETP of Sarigam. Committee insisted for separate high COD and Low COD stream at source and treated separately.

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Committee asked about APCM with coal fired boiler, PP informed that water scrubber followed by ESP as APCM with boiler. Committee asked about coal storage and its handling for huge consumption of coal, PP has not submitted details regarding coal storage handling. Committee also insisted for revised air and water balance diagram for compliance of control of coal dusting. Committee asked about LDAR for methanol handling, PP informed that adequate transferring system will be adopted for it. Committee insisted for detailed LDAR programme with mentioning about storage, handling and transferring and losses of methanol and its recovery system. Committee insisted for revised hazardous waste matrix for each bleed liquor generation and disposal and off specification product etc. details. Committee also insisted for mentioning latest technology with proper safety aspect for nitration process and hydrogenation process. PP informed about ambient air baseline

data, committee insisted for revised baseline data and EIA report for parameters like NH 3 , CO and HCl. Committee asked about need based CER activity with provision for five years and green belt development as per CPCB criteria. After deliberation, SEAC unanimously decided to consider the proposal after submission of the following details. 1. Technical details with BAT for innovative process in place of conventional process adopted for proposed project. 2. Separate high COD and Low COD stream at source and provide ETP separately for High COD and Low COD effluent. 3. Revised Air matrix and water balance considering coal dusting control as per Coal storage and handling guidelines of GPCB. 4. Revised Hazardous waste matrix with mentioning each bleed liquor from scrubber separately with its generation and disposal quantity and mentioning off specification products, spent carbon and spent resin generation. 5. Readdressed safety measures for Nitration and Hydrogenation process with mentioning adoption of BAT for it. 6. Detailed LDAR programme with flow diagram and mentioning about storage, handling, transferring and losses of methanol and its recovery system.

7. Revised Ambient air baseline data with monitoring parameters like NH 3, CO and HCl and revised EIA in this regard. 8. Revised need based CER activity with budgetary provision for five years and adequate green belt development area as per CPCB criteria. • Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned points. • PP presented replied as below:

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1. PP presented technical details with BAT for innovative process in place of conventional process adopted for proposed project product wise. 2. PP proposed to install separate Product wise plant. Based on mass balance and material balance, characteristics of effluent is worked out and segregate at source and provide separate line leading to collection tank of ETP: 1 and ETP:2 3. PP presented revised air matrix and water balance considering coal dusting control as per coal storage and handling guidelines of GPCB. 4. PP presented revised Hazardous waste matrix with mentioning each bleed liquor from scrubber separately with its generation and disposal quantity and mentioning off specification products, spent carbon and spent resin generation. 5. PP presented safety measures for Nitration and Hydrogenation process with mentioning adoption of BAT for it. 6. PP presented detailed LDAR programme with flow diagram and mentioning about storage, handling, transferring and losses of methanol and its recovery system. 7. PP presented revised ambient air baseline data with monitoring parameters like NH3, CO and HCl and revised EIA in this regard. 8. PP presented Revised need based CER activity with budgetary provision for five years and adequate green belt development area as per CPCB criteria. • Committee observed that reply submitted by PP is satisfactory. • Salient features of the project including Water, Air and Hazardous waste management (Revised): Sr. Particulars Details no. A A Total cost of Proposed Project 7.00 Crores (Rs. in Crores): EMP details (Capital cost & Recurring cost) Capital Cost Of Environment Management System S. Total Cost Particulars No. (Rs. In Lakhs) 1. Air pollution management 35.00 2. Water pollution management 182.00 3. Occupational Health and safety 5.00 4. Solid waste disposal and 2.00

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management Green belt development and rain 1.00 5. water harvesting Total 225.00 Recurring/operating Cost Per Annum Environmental & Safety Management System Proposed # Component (Rs.in Lakhs/annum) Environment (Water, Air & Hazardous Waste) & 1. 1350 Safety Management System 2. Greenbelt Maintenance 5 Total 1355

CER details (As per MoEF&CC OM dated 01/05/2018) ‹ As per latest OM No.F.No.22-65/2017-IA,dated 1 st May 2018 the fund allocation for the CER is Rs.14.00 Lakhs (2% of capital investment of Rs.700 Lakhs for undertaking the Socio Economic Activities.) Component As per Norms Actual CER to be done

CER 14.00 Lakhs 14.00 Lakhs

‹ Unit will spend total Rs.14.00 Lakhs rupees towards the CER activity in coming 5 years. ‹ CER activities will be carried out in Punat, Dehali, Malav, Dhanoli & Angam villages. ‹ Under CER activities unit will provide in Drinking water facility by infrastructure development, Education Initiatives and Health Initiatives etc. B Total Plot area ( sq. meter) 5390 Sq. m. Green belt area 1200 Sq. m. ( sq. meter) C Employment generation 150 Nos. D Water i Source of Water Supply GIDC Sarigam Water Supply. (GIDC Bore well, Surface water, Tanker supply etc...)

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Status of permission from the concern authority. Proponent has already received water permission letter from GIDC Sarigam Water Supply Dept. vid letter No. GIDC/DEE/SRG/390 dated 16/11/2018. ii Water consumption (KLD)

Category Quantity Remarks KLD (D) Domestic 7.50 (E) Gardening 6.00 (F) Industrial Process 39.63 Processing, washing and scrubber of PNA, PAP/OAP, 6 NAPSA - 26.8 KLD. Processing, washing and scrubber of PCA, 2,4 DNCB, PPDA, DICAP, PA -12.83 KLD. Washing 12.00 Floor/equip ment

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washing Boiler 140.00 Cooling 70.00 Others 10.00 Coal wetting scrubber for boiler - 7.0 KLD. Scrubber of boiler -3.0 KLD. Industrial Total 271.63 Total (A + B + C) 285.13

4) Total water requirement for the project: 285.13 KLD 5) Quantity to be recycled : 00 KLD 6) Total fresh water requirement: 285.13 KLD (Total water requirement = Fresh water + Recycled water) iii Waste water generation (KLD)

Category Waste water Remarks KLD (C) Domestic 6.00 (D) Industrial Process 136.29 Processing, washing and scrubber of PNA, PAP/OAP, 6 NAPSA - 115.5 KLD. Processing, washing and scrubber of

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PCA, 2,4 DNCB, PPDA, DICAP, PA - 20.79 KLD. Washing 12.00 Floor/equipm ent washing Boiler 15.00 Cooling 7.00 Others -- Total Industrial 170.29 waste water Total [A + B] 176.29 - iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ MEE: 125 KLD ‹ ATFD: 1.5 MT/h ‹ ETP: 170.29 KLD Treatment scheme including segregation at source. ‹ Total Industrial Waste water generation will be 170.29 KLD mainly from process, washing, scrubber, boiler blow down and cooling tower blowdown. From the process, average 115.5 KLD of high TDS/COD effluent will be segregated, neutralized, filter separately and evaporated in MEE followed by ATFD. Average 90.4 KLD of condensate will be generated from MEE/ATFD, which will be taken to ETP. Thus total 145.19 KLD of industrial effluent will be treated in proposed primary, secondary & tertiary treatment plant & discharged into underground effluent drainage line of GIDC Sarigam to CETP Sarigam for further treatment & ultimate disposal into Arabian Sea through closed pipe line. ‹ Domestic waste water (6 KLD) will be disposed off through septic tank/soak pit. Note: (In case of CETP discharge) :

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Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ Total Industrial Waste water generation will be 170.29 KLD mainly from process, washing, scrubber, boiler blow down and cooling tower blowdown. From the process, average 115.5 KLD of high TDS/COD effluent will be segregated, neutralized, filter separately and evaporated in MEE followed by ATFD. Average 90.4 KLD of condensate will be generated from MEE/ATFD, which will be taken to ETP. Thus total 145.19 KLD of industrial effluent will be treated in proposed primary, secondary & tertiary treatment plant & discharged into underground effluent drainage line of GIDC Sarigam to CETP Sarigam for further treatment & ultimate disposal into Arabian Sea through closed pipe line. ‹ Domestic waste water (6 KLD) will be disposed off through septic tank/soak pit. Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): • Not Applicable v Mode of Disposal & Final meeting point Domestic: Domestic waste water (6 KLD) will be disposed off through septic tank/soak pit. Industrial: Total Industrial Waste water generation will be 170.29 KLD mainly from process, washing, scrubber, boiler blow down and cooling tower blowdown. From the process, average 115.5 KLD of high TDS/COD effluent will be segregated, neutralized, filter separately and evaporated in MEE followed by ATFD. Average 90.4 KLD of condensate will be generated from MEE/ATFD, which will be taken to ETP. Thus total 145.19 KLD of industrial effluent will be treated in proposed primary, secondary & tertiary treatment plant & discharged into underground effluent drainage line of GIDC Sarigam to CETP Sarigam for further treatment & ultimate disposal into Arabian Sea through closed pipe line. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF

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‹ CETP Sarigam Membership of Common facility (CF) (For waste water treatment) Membership of CETP-CETP/SCI/PROCER/ on dated 16/04/2019 vii Simplified water balance diagram with reuse / recycle of waste water

Water Balance Diagram

Total Water consumption, 285.13 m 3/day source from GIDC Sarigam

Domestic: 7.5 Processing/ Processing/ Cooling: 70.0 Boiler: 140.0 Floor/equipment Gardening: 6.0 Coal wetting washing/ washing for washing: 12.0 + boiler scrubber: Scrubber for PCA,2,4 DNCB, 7 + 3 =10) Septic tank/ PNA, PAP/OAP, PPDA,DICAP, soak pit: 6.0 6 NAPSA: 26.8 PA: 12.83 Scrubber effluent: 3 7.0 15.0 12.0 recycle for coal wetting 115.51 20.79

High TDS/COD: 115.5 from Process Low TDS/COD: 20.79 COD: 15000-17000mgl, TDS: 15-20% from product washing & scrubber H Lime: 0.5 MT Primary Treatment Primary/secondary/tertiary ETP: 145.19 m3/day

Filteration Sludge: 0.75 MT CETP Sarigam ETP: 1 ETP: 2 Loss:1.0 MEE: 115.5 Condensate: 80.4 Arabian Sea

ATFD: 34.1 Loss:1.0 Condensate: 90.4,m3/day Condensate: 10.0 COD: 2000-2500 mgl, TDS: 500-600 mgl Salt: 23.1 MT viii Reuse/Recycle details (KLD) Total reuse 00 KLD Source of waste Application Characteristics of Remarks water for reuse area with waste water to be regarding with quantity in quantity in reused (COD, BOD, feasibility KLD (From KLD (Where it TDS etc.) to reuse i.e. where it is is used) coming) ------

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.

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- Air Source of Type of Stack Quantity Pollution Sr. emission Type of emissions Height of Fuel Control no. With Fuel i.e. Air (meter) Measures Capacity Pollutants (APCM) Water Steam Imported Scrubber 1 Boiler 30 2000 kg/h Coal followed by (10 TPH) ESP Steam Water Boiler Imported Scrubber 2 (5 TPH) 30 1000 kg/h PM Coal followed by (For SO x Bag filter MEE/ATFD) NO x Thermic MDC Fluid Heater Imported 3 30 250 kg/h followed by (10 Lakhs K Coal Bag filter Cal/h) D.G Set 4 11 HSD 125 kg/h Exhaust (500 kVA) Closed shed, water sprinkler, wind Coal breaking 5 Storage - - - PM wall, RCC yard flooring and dust suppression system Coal Closed 6 - - - PM Handling screening,

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system coal crushing and closed conveyer Impact blade Coal 7 - - - PM crusher, crusher closed conveyer Fly ash 8 handling - - - PM Closed Silo system Notes on coal and ash handling system: Coal received from the coal supplier through closed covered trucks. Unloaded the coal in a coal storage yard through a completely closed mechanized system. Coal storage yard provided closed shed, RCC flooring, wind breaking wall, dust suppression system. Coal transferred from coal storage yard to coal crushing unit having closed screening, closed conveyer belt. Coal crusher having inbuilt impact blade crusher, screen conveyer and closed elevator. Required size of coal is taken to bunker followed by boiler through a closed conveyer system. Fly ash and dust generated from the boiler, pre-heater, economizer is taken in a closed silo. As this is a complete closed and covered system hence there is no chimney is required for coal handling and fly ash handling system.

FLOW DIAGRAM FOR COAL HANDLING/ASH HANDLING SYSTEM

Chimney

Coal transfer COAL Truck Coal unload Coal transfer through Boiler Economizer, ESP Wet scrubber closed conveyer belt through conveyer Air Pre-heater in closed storage yard belt to Bunker to coal crusher

Fly ash

Silo

Fly ash load on truck

ii Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.)

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- Specific Source of Air Pollution Sr. emission Type of Stack/Vent Control Measures no. (Name of the emission Height (meter) (APCM) Product & Process) Two Stage Alkali 1 2,4 DNCB NO x 11 Scrubber

PNA & Storage Water followed by 2 NH 3 11 Tank Acid Scrubber

6- NAPSA & NO x Two Stage Alkali 3 11 Storage Tank SO x Scrubber - iii Fugitive emission details with its mitigation measures: As below: ‹ Concrete road will be developed within plot premises to avoid fugitive dust due to vehicle movement. ‹ Manufacturing activity will be carried out in closed reactors/vessels and ‹ Regular checking and maintenance of the same will be carried out to avoid any leakages. ‹ All the raw materials will be stored in closed containers and in sealed bags and will be handled through closed system to avoid the handling losses. F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type/Name Specific Category Quantity Management no. of Source of and (MT/Annum) of HW Hazardous generation Schedule waste (Name of the as per HW Activity, Rules. Product etc.)

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1 Used Oil D G set and Sch: I/5.1 0.02 Collection, gearbox of Storage, reactors Transportation and disposal by Selling to authorized recycler 2 Discarded Empty Sch: I/33.1 5.0 Collection, Container containers of Storage, raw materials Transportation and disposal for Utilize for packing of hazardous waste or sell to authorized recycler after de- contamination 3 ETP Waste Neutralization Sch: I/35.3 452.4 Collection, and Filtration Storage, process of Transportation effluent and disposal at Dispose off into TSDF Vapi through SIA, Sarigam OR Detox India 4 Salt from Evaporating Sch: I/35.3 7207.2 Collection, MEE/ATFD process of Storage, effluent Transportation and disposal

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at Dispose off into TSDF Vapi through SIA, Sarigam OR Detox India 5 Distillation Distillation Sch: I/26.1 66.0 Collection, Residue process of Storage, products Transportation and disposal by Selling to M/S RSPL, Panoli for co- processing OR M/S SEPPL, Kutch 6 Spent Process of Sch: I/26.3 6288.0 Collection, Sulphuric 2,4 DNCB Storage, Acid (80%) product Transportation and disposal by Selling to actual users having Rule 9 permission under H/W rules 2016 7 Spent Acetic Process of Sch: I/26.3 1284.0 Collection, Acid (30%) DICAP Storage, product Transportation and disposal by Selling to actual users having Rule 9

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permission under H/W rules 2016 8 Spent Process Sch: I/26.5 88.8 Collection, Catalyst Storage, Transportation and disposal for Recycled in next batch 9 Spent Resin D M Plant of Sch:I/35.2 2.0 Collection, from D M Boiler feed Storage, plant water Transportation and disposal at Dispose off into TSDF Vapi through SIA, Sarigam OR Detox India 10 Spent Tertiary ETP Sch:I/36.2 2.0 Collection, carbon from Storage, ETP Transportation and disposal by Selling to M/S RSPL, Panoli for co- processing OR M/S SEPPL, Kutch 11 Bleed liquor Scrubber --- 683.28 Collection, from attached to Storage and scrubber sulphonator Treated in (Sodium and Nitrator ETP followed

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sulphite and rector of 6 by MEE/ATFD sodium NAPSA nitrite soln) product

12 Bleed liquor Scrubber --- 1341.6 Collection, from attached to Storage and scrubber Nitrator of Reused for (Sodium DNCB washing of nitrite product 2,4 DNCB solution)

13 Bleed liquor Scrubber --- 1519.4 Collection, from attached to Storage and scrubber convertor of Reused in first (liquor Ammonia gas of PNA to ammonia to ammonia minimize the soln) liquid of PNA fresh liquor product ammonia soln. - ii Membership details of TSDF, CHWIF etc. • TSDF of VGEL, Vapi. (For HW management) Proponent has already applied to VGEL, Vapi for TSDF Membership. • Membership of Detox India on dated 20/05/2019 • Membership of M/s. SEPPL on dated 20/05/2019 • Membership of M/s. RSPL on dated 20/05/2019 iii Details of Non-Hazardous waste & its disposal Fly Ash-2433.6 TPA will be

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(MSW and others) disposed of by Selling to brick manufacturers. G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format) Solvent to be used in MT Name of Total % # Product the Fres Recovere Los consumptio Recover solvent h d s n per month y 1 2,4 0 0 0 0 0 0 . DNCB 2 PNA 0 0 0 0 0 0 . 3 PCA 0 0 0 0 0 0 . 4 Methano PPDA 430 10 420 10 97.6 . l 5 PA 0 0 0 0 0 0 . 6 DICAP 0 0 0 0 0 0 . 7 PAP/OA 0 0 0 0 0 0 . P 8 6- 0 0 0 0 0 0 . NAPSA Total --- 430 10 420 10 97.6

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

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• Reactor and solvent handling pumps will have mechanical seals to prevent leakages. Reactors shall also be provided with breather valve to prevent losses. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Remarks Hazardous chemicals Storage tanks Nitric Acid Sulphuric Acid

NH 4OH Methanol MDCB Acetic anhydride Caustic Lye Oleum (23%) Drum/Barrel storage ---

‹ Applicability of PESO : ‹ Unit will obtain permission from PESO for methanol and permission from prohibition department after obtaining EC. • After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant of Environmental Clearance 8. SIA/GJ/IND2/30224/2018 M/S. SANJAY INDUSTRIES EC – Plot No. C-150, At Saykha GIDC Industrial Estate Reconsideration ,Bharuch. Category of the unit : 5(f) Project status: New • Project proponent (PP) has submitted online application vide no. SIA/GJ/IND2/30224/2018 on dated 21/06/2019 for obtaining Environmental Clearance. • The SEAC had recommended TOR to SEIAA and SEIAA issued TOR to PP vide their letter dated 26/02/2019. • Project proponent has submitted EIA Report prepared by EXCEL ENVIRO TECH based on the TOR issued by SEIAA. • This is a new unit proposes for Synthetic Organic Chemicals manufacturing as tabulated below:

Sr. Name of the Product CAS no. /CI Quantity End-use of products

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No. no. (MT/Month)

1 Sulpho Tobias Acid (STA) 117-62-4 15 Manufacturing of Reactive synthesis & Dyes 2 Sulpho Vinyle Sulphone 2494-89-5 Manufacturing of Reactive (SVS) 15 synthesis & Dyes

3 Sulpho Broneer Vinyle 81417-89-2 Manufacturing of Reactive Sulphone (SBVS) 10 synthesis & Dyes

4 Aniline 2,5 Di Sulphonic Acid 98-44-2 Manufacturing of Reactive 10 synthesis & Dyes 5 G-Salt 842-18-2 Manufacturing of Reactive 20 synthesis & Dyes 6 Gama Acid 90-51-7 Manufacturing of Reactive 20 synthesis & Dyes 7 Benzadine 2-2 Di sulphonic 117-61-3 Manufacturing of Reactive Acid (BDSA) 10 synthesis & Dyes

8 Metanilic Acid 121-47-1 30 Manufacturing of Reactive synthesis & Dyes

9 4 Sulpho Anthranilic Acid 98-43-1 15 Manufacturing of Reactive synthesis & Dyes 10 DASA 16803-97-7 10 Manufacturing of Reactive synthesis & Dyes Total 155

• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 25/07/2019. • During the meeting dated 25/07/2019, technical presentation made by project proponent. • 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 2018 to February 2019. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, CO, NH3, HCL, CL2, HBr, &VOC 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. 554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 56 of 215

• 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, committee noted that the proposal is for new unit at GIDC Saykha. Water source is GIDC. • During meeting, Committee asked for proposed production size, PP informed that proposed plot size is adequate for proposed production. Committee asked about wastewater management, PP informed that high COD effluent after ETP treatment, will be evaporated in in-house MEE cum stripper. Low COD effluent will be treated in softening plant and will be completely reused back in process. Committee asked about adequacy of reuse of treated waste water after softening plant with raw and treated waste water characteristic, PP could not explained in details regarding it. Committee insisted for BAT adopted for proposed dirty products project and with correct data for adopt BAT process for manufacturing proposed products in details with specification of it. Committee asked about feasibility for total reuse of spent acid in manufacturing of Benzadine 2-2 Di sulphonic Acid (BDSA) and Metanilic acid and mentioned as raw material , PP could not explained in details regarding it . Committee insisted for technical justification for dilute HCl as Hazardous waste generation quantity only 2.3 MT/Year , SBS slurry generation quantity 93 MT/Year and Ammonia solution generation quantity 56 MT/Year and ETP sludge/ MEE salt generation. Committee asked about APCM with coal fired boiler, PP informed that MDC and bag filter as APCM with boiler. Committee asked about solvent usage and VOC control, PP has mentioned that solvent will not be used in proposed project. Committee insisted for ambient air baseline data and EIA report for parameters like NH3 , CO and HCl and revised EIA report. • After deliberation, SEAC unanimously decided to consider the proposal after submission of the following details, 1. Technical details with BAT for innovative process in place of conventional process adopted for proposed project. 2. Adequacy of reuse of treated waste water after softening plant with raw and treated waste water characteristic. 3. Feasibility for total reuse of spent acid in manufacturing of Benzadine 2-2 Di sulphuric Acid (BDSA) and Metanilic acid. 4. Technical justification for dilute HCl as Hazardous waste generation quantity only 2.3 MT/Year , SBS slurry generation quantity 93 MT/Year and Ammonia solution generation quantity 56 MT/Year. 5. Revised Hazardous waste matrix with mentioning spent sulphuric acid disposal and accurate ETP sludge/ MEE salt quantity. 6. Revised Ambient air baseline data with monitoring parameters like NH3, CO and HCl and revised EIA in this regard. 554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 57 of 215

• Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned points. • Committee noted as below: 1. Technical details with BAT for innovative process in place of conventional process adopted for proposed project submitted. 2. Adequacy of reuse of treated waste water after softening plant with raw and treated waste water characteristic submitted. 3. Feasibility for total reuse of spent acid in manufacturing of Benzadine 2-2 Di sulphuric Acid (BDSA) and Metanilic acid submitted. 4. Technical justification for dilute HCl as Hazardous waste generation quantity only 2.3 MT/Year , SBS slurry generation quantity 93 MT/Year and Ammonia solution generation quantity 56 MT/Year submitted. 5. Revised Hazardous waste matrix with mentioning spent sulphuric acid disposal and accurate ETP sludge/ MEE salt quantity submitted. 6. Revised Ambient air baseline data with monitoring parameters like NH3, CO and HCl and revised EIA in this regard submitted. • Committee observed that reply submitted by PP is satisfactory. • Salient features of the project including Water, Air and Hazardous waste management (Revised): Sr. Particulars Details No . A A Total cost of Proposed Project 10 Crores (Rs. in Crores): B Total Plot area ( sq. meter) 5000 Sq. m. Green belt area 1650 Sq. m. ( sq. meter) C Employment generation 55 nos. D Water i Source of Water Supply GIDC, Water Supply (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. GIDC Water consent obtained vide Letter No.

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GIDC/DEE(WS)/BRH/303 dated 12/04/2019 ii Water consumption (KLD)

Category Quantity, Remarks KLD (G) Domestic 5 For workers (H) Gardening 6 --- (I) Industrial Process 12.7 --- Scrubber (APCM) 5 Fresh + Recycled Boiler 60 Fresh + Recycled Cooling 5 Fresh + Recycled Laboratory 1 ---- Industrial Total 83.7 --- Total (A + B + C) 94.7 Note - **: Will include the reuse quantity of treated domestic waste water. 1) Total water requirement for the project: 94.7 KLD 2) Quantity to be recycled : 52.0 KLD 3) Total fresh water requirement: 42.7 KLD iii Waste water generation (KLD) Category Waste water KLD Remarks

(E) Domestic 4.5 Septic Tank / Soak Pit (F) Industrial Process + APCM 19 ZLD System Boiler blow down+ RO Reject 30 Treated in Cooling tower Blow down 3 softening plant and reuse in process Laboratory 1 ZLD System Spent Acid (after Gypsum 4.5 ZLD System removal)

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Total Industrial waste water 57.5 Total [A + B] 62.0 Waste water from process and APCM willbeneutralized in ETP and then evaporated in MEE. The concentrate from MEE shall be further treated in ATFD and condensate from MEE after treatment shall be reused. iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ In house ETP for primary treatment – 40 KLD ‹ MEE – 2400 kg/hour ‹ ATFD – 450 kg/hour. Treatment scheme including segregation at source. • High Concentrated Effluent: High concentrated process effluent @ 24.5 KL/Day after giving primary treatment shall be evaporated in FBMEE (Force Base Circulation System for Concentration). The concentrate from FBMEE shall be further evaporated in ATFD. • Low Concentrated Effluent: Low concentrated effluent from cooling tower, boiler and RO Plant @33 KL/Day which shall be reused after being treated in softner along with MEE condensate. • Total spent sulphuric acid generated of @ 6.2 KLD through manufacturing processes will be neutralized by using lime or shall be reused within process. Due to neutralization of spent acid, high quantity of gypsum will be produced, which will be sold to cement manufacturer or sent to TSDF. Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ Not Applicable Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ High concentrated process effluent of 24.5 KLD from process, APCM, laboratory shall be treated in effluent treatment plant consisting of stripper, collection tank and neutralizer which are adequate with respect to hydraulic load. Spent Acid generated of @6.2 KLD shall be treated in ETP consisting of collection tank and neutralizer for gypsum recovery.

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‹ The effluent @24.5 KLD shall be evaporated in FBMEE ‹ The concentrate from FBMEE of @4.5 KLD shall be further treated in ATFD of capacity 450 kg/hour. ‹ The condensate from FBMEE along with boiler, cooling tower effluent & RO reject shall be treated in softener plant of capacity 6.0 KL/hour. v Mode of Disposal & Final meeting point Domestic: Septic Tank / Soak Pit System

Industrial: High COD/TDS water treated in in-house ZLD plant & Low COD/TDS water (as such RO reject/Cooling tower Blow down/Boiler blow down) treated in softening plant and reused. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ NOT APPLICABLE. Membership of Common facility (CF) (For waste water treatment) NOT APPLICABLE. vii Simplified water balance diagram with reuse / recycle of waste water

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viii Reuse/Recycle details (KLD) Total reuse 46 KLD Source of waste Application area Remarks regarding feasibility to water for reuse with with quantity in reuse i.e. w/w characteristics quantity in KLD KLD (COD, BOD, TDS etc.) Industrial Waste water Boiler, Cooling COD – 200 mg/L @ 52 KLD Tower, TDS – 150 mg/L Gardening

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. Source Air Type of of Stack Quantity Pollution Sr. Type of emissions emission Height of Fuel Control No. Fuel i.e. Air With (meter) MT/Day Measures Pollutants Capacity (APCM)

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APH, MDC, FBC PM ≤150 Cyclone Steam Imported 12.0 1 30 mg/Nm 3 and Bag Boiler (3 coal MT/Day SO 2≤10 filter& TPH) ppm Water

NO 2≤5 Scrubber DG Set ppm 200 Acoustic 2 (250 10 Diesel L/Day enclosure KVA) - ii Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) Specific Source of Stack/Vent Air Pollution Control Sr. emission(Name of Type of Height Measures no. the Product & emission (meter) Process) (APCM)

HCl ≤35 25 m Three stage Venturi 3 1 Drowning (G-Salt mg/m scrubber( with chilled /Gamma Acid) water circulation and column,

SO 2 25 m Series of two stage ≤200 Venturi (Caustic and Isolation mg/m 3 Water 15% solution) and 2 (Gama Acid/Metanilic one stage packed Acid/DASA) column with Alkaline water circulation PM ≤150 25 m Cyclone Separator with 3 Exhaust air out let for 3 Spin flash Dryer mg/m Bag Filter

iii Fugitive emission details with its mitigation measures: ° Regular sprinkling of water, pacca road shall be constructed & green belt shall be provided within premises to prevent fugitive emissions due to vehicular movement. Regular maintenance of vehicles. ° General control measures like routine & regular inspection to identify leakage,

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preventive maintenance and operational maintenance, provision of leak detection and repair system (LDAR). ° Management to ensure proper handling of the spillages during transfer, charging operation and provision of a Dust Collection System for collection of the air borne material wherever applicable. ° Preventive maintenance of flange connections and glands of pumps. ° Management will also ensure proper usage of the Personnel Protective Equipment by the workers. ° Closed handling system shall be provided for chemicals. ° Reflux condenser to be provided over the reactor. ° The acids shall be taken from storage tanks to reactor through closed pipeline. Storage tanks shall be vented through trap receiver and condenser operated on chilled water. ° Fugitive emissions in the work zone environment, product raw material storage area shall be monitored regularly. F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type / Specific Category Quantity Management of HW No Name of Source of and (MT/Annum) . Hazardous generation Schedul waste e 2000 Nos HDPE Bags, Discarded Raw material Collection, Storage, 150 drums 1 bags / storage and 33.1 transportation, sent to (9.1 containers handling Registered recyclers. Kg/drum=136 5 Kg/annum). Collection, Storage, Plant and 2 Used oil 5.1 0.5 transportation, Sent to machinery register refiners

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Collection, storage and reuse in manufacturing process. Total generation will be 21.96 MT/Annum Dilute HCl Sh-I I 3 APCM (DASA) 21.96 and requirement in (27-30%) B15 process will be 24.48 MT/Annum. Balanced quantity will be -2.52 MT/Annum purchased. Collection, storage and treated in in-house ZLD system for Gypsum recovery or reused in Sulpho Tobias process. (in-house). Spent Acid,, Aniline Total generation will be Sulphuric 2,5 Disulphonic 1816.0 MT/Annum and 26.3 1816.0 Acid (40- Acid, G-salt, reuse in process 1380.24 45%) Gamma Acid MT/Annum. Balanced quantity will be 435.8 MT/Annum. Balance 4 quantity of spent acid will be used for generation of Gypsum. Collection, storage , transportation and Sulpho Vinyl Spent disposal by sending to Sulphone, Sulphuric unit having permission Sulpho Broneer 26.3 1285.0 Acid (20- under Rule -9. MOU has Vinyl Sulphone, 25%) been obtained from Unit, DASA or treated in the ZLD Plant.

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Collection, storage and Transportation and Manufacturing disposal by land filling at 5 Iron Sludge of Metanilic 26.1 756 TSDF. Unit has already Acid and DASA obtained Membership certificate from M/s. SEPPL obtained Collection, storage and reuse in manufacturing process. Total generation will be 112 MT/Annum APCM and reuse in process 6 SBS Slurry (DASA/Gama 26.3 112 41.37 MT/Annum. Acid) Balanced quantity will be 70.52 MT/Annum. Balance quantity of SBS will be treated in ZLD. Collection, storage and Transportation and disposal by co- processing at cement industries. Unit has from already obtained letter Neutralization from Binani Cement for Gypsum of Spent Acid 7 26.1 835 accepting their Gypsum Sludge and From sludge. Unit has already process of obtained MOU from M/s. Metanilic Acid Binani Cement for accepting Gypsum. Membership From SEPPL is obtained

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Neutralization ETP 8 of wastewater 35.3 30.0 Sludge Collection under the steel stream fabricated roof with After HDPE Liner laying under Concentration the 6 inch RCC and MEE/ATFD impervious Layer with 9 Evaporation 35.3 576 Salt PCC, send to authorized remaining Salt+ TSDF. Organic waste from ZED Collect in specially designed silo and pack in solid HDPE bags, sell to 10 Fly ash From boiler 240 waste cement industries and road construction company.

ii Membership details of TSDF, CHWIF etc. Membership of Saurashtra (For HW management) Enviro Projects Pvt. Ltd. for disposal of iron, gypsum sludge & ATFD salt. iii Details of Non-Hazardous waste & its disposal NOT APPLICABLE (MSW and others) G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format) Quantity Quantity Sr. Name of Quantity Raw Materials (Per (MT/Day) No. Products (MT/Month) Batch) 4 Sulpho Ortho Nitro Toluene 1.0 6.98 0.28 1. Anthranilic Acid

The Ortho Nitro Toluene used in the process is @6.98 MT/Month which is very minor quantity. This is highly soluble in water, so stripper shall be installed for this in ZLD,

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and the vapour pressure is 0.0213, so <= 0.2 Kpa so there is no VOC emissions.

ii VOC emission sources and its mitigation measures ‹ The Ortho Nitro Toluene used in the process is @6.98 MT/Month which is very minor quantity. This is highly soluble in water, so stripper shall be installed for this in ZLD, and the vapour pressure is 0.0213, so <= 0.2 Kpa so there is no VOC emissions. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Remarks Hazardous chemicals Storage tanks Oleum Acid --- Drum/Barrel storage Hydro Chloric Acid, Ortho --- Nitro Toluene, Sulphuric Acid

‹ Applicability of PESO : Not Applicable • During SEAC meeting, Committee asked about BAT adopted for proposed project, PP informed that catalytic hydrogenation process adopted for eliminate iron sludge reduction and installation of brine chilling plant instead of ice as part of BAT. Committee asked about reuse of softening plant, technical expert of PP informed that cooling , boiler and RO plant effluent after neutralization will be reused and also mentioning about its characteristic. Technical expert of PP informed about spent sulphuric acid reuse due to installation of brine chilling plant and due to that spent sulphuric acid will be of 45% and reuse of it in manufacturing process. • PP informed that they have submitted revised dil. HCl and SBS slurry quantity with respect to justification regarding lee generation quantity mentioned and Dilute HCl generated: 21.96 MT/Year ,SBS slurry generation: 112 MT/Year. In connection with generation of dilute Ammonia solution (concentration 15-20%); it is used Amidation stage of Gamma Acid production. The reaction is carried out under pressure by using Ammonia. Therefore, no gaseous ammonia is being librated which is not required to be sent to scrubber as per reconfirmation with process developers and hence no ammonia solution generated. Technical expert of PP submitted revised Hazardous waste matrix with accurate ETP sludge/MME salt, gypsum, spent acid etc. generation quantity and its disposal which is discussed in length. • Technical expert of PP informed that they have submitted revised EIA and baseline data with mentioning about HCl, Ammonia and Cl2 parameters detail in EIA.. • In view of above, after detailed discussion, Committee unanimously decided torecommend the project

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to SEIAA Gujarat for grant of Environmental C learance.

9. SIA/GJ/IND2/37419/2019 M/S. UNIVERSAL CHEMICALS EC – Plot No:824/26, Industrial estate Reconsideration GIDC, Jhagadia,Ta- Jhagadia, Dist - Bharuch.

Category of the unit: 5(f) Project status: New • Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/37419/2019dated 29/07/19 for obtaining Environmental Clearance. • SEIAA issued TOR to PP vide their letter dated 13/05/2019. • Project proponent has submitted EIA Report prepared by Yuva Enviro Expertbased on the TOR issued by SEIAA. • This is a new unit proposes for manufacturing of Synthetic Organic Chemical as tabulated below: Sr. Name of the Products CAS no. /CI Quantity End -use of products No. no. MT/Month 01 isobutyl 5 chloro 2,2 109232-37-3 130 MT/Month To be used in dimethylvalerate gemfibrozil (API) 02 4 NAX 1309-48-4 100 MT/Month Pharma intermediate 03 4- Methyl catechol 452-86-8 5 MT/Month Used in 4-Methyl Catechol Diacetic acid Dimethyl ester 04 Methylenedioxy Phenol 533-31-3 5 MT/Month Used in Paroxetine (SESAMOL) 05 O-Benzylhydroxylamine 2687-43-6 5 MT/Month It Isused in the Hydrochloride synthesis of hydroxylamines and hydroxyamates. 06 4-Methoxy 2186-92-7 5 MT/Month Itis used as a precursor Benzaldehyde dimethyl to 1-methoxy-1-(4- Acetal methoxyphenyl)hept-2- yne 07 PREGABELIN 148553-50-8 10 MT/Month It’s a API

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Pharmaceutical Product 08 QUETIAPINE 111974-72 5 MT/Month It’s a API FUMARATE Pharmaceutical Product 09 LERCANIDIPINE 132866-11-6 5 MT/Month It’s a API HYDROCHORIDE Pharmaceutical Product 10 ETORICOXIB 202409 -33 -4 5 MT/Month It’s a API Pharmaceutical Product Total 275 MT/Month • The projectfallsunderCategory B of project activity 5(f) asper the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 14/08/2019. • During the meeting dated 14/08/2019, technical presentation made by the Project proponent. • Committee noted that this proposal is new in GIDC Jhaghadia. Source of Water is GIDC. Committee noted that has mentioned disposal mode of generated effluent into CMEE of BEIL, Ankleshwar and disposal of Hazardous Waste into TSDF of BEIL, Ankleshwar which is Critically Polluted Area as per Honourable National Green Tribunal (NGT) order dated 10.07.2019 in Original Application No. 1038/2018. • Further Committee told PP that due to the higher CEPI score in the area were disposal of effluent and hazardous waste is going to take place this proposal cannot be considered for further appraisal until disposal mode is changed to any other common facility which does not fall in CEPI area. • In view of the above, Committee unanimously decided to defer the case and to consider the proposal only after satisfactory submission for sound management of effluent & hazardous waste. • Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned point. • PP presented replied as below: ‹ Unit submitted revised proposal of in-house evaporator and ETP units instead of CMEE and Hazardous waste disposal. • Salient features of the project including Water, Air and Hazardous waste management (Revised): Sr. Particulars Details no. A A Total cost of Proposed Project 2.75Crore (Rs. in Crores):

Details of EMP Capital Cost: 95Lacs

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Recurring Cost: Approx. 4Lacs/Annum Details of CER as per OM dated 01/05/2018 5.5Lacs (2 % of Total Project Cost) B Total Plot area ( sq. meter) 3400 Sq. m.

Green belt area 340 Sq. m. (10%) ( sq. meter) C Employment generation 10

D Water i Source of Water Supply GIDC Water supply, Jhagadia (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. Obtained

ii Water consumption (KLD) Category Quantity Remarks KLD (J) Domestic 1 (K) Gardening 1

(L) Industrial

Process 25

Boiler 25

Cooling 8

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Washing 3

Others 61 Industrial Total 63 Total (A + B + C)

1) Total water requirement for the project: 63 KLD 2) Quantity to be recycled : 22KLD 3) Total fresh water requirement: 41KLD (Total water requirement = Fresh water + Recycled water) (63 KLD = 41 KLD + 22 KLD) iii Waste water generation (KLD) Category Waste water Remarks KLD (G) Domestic 0.75

(H) Industrial

Process 18

Boiler 4

Cooling 2

Washing 1

Others

25 Total Industrial

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waste water Total [A + B] 25.75 - iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.

Sr. Name of Unit Capacity No

1 Collection tank 10 KL 2 Neutralization tank 5 KL 3 Primary Clarifier 8 KL 4 Holding tank 5 KL each 5 PSF 30 KLD 6 ACF 30 KLD 7 RO 30 KLD 8 MEE 10 KLD

Treatment scheme including segregation at source. ‹ Total Effluent Generated will be 25 KLD from which 23 KLD will go to RO and RO Permeate water(14 KLD) will be reused and RO Reject Water will send to In-House MEEfrom which 8 KLD will be reused to achieve Zero Liquid Discharge.

Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ Not Applicable Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Total Effluent Generated will be 25 KLD from which 23 KLD will go to RO and RO Permeate water 14 KLD will be reused and RO Reject Water will be sent to In-House MEE from which 8 KLD will be reused to achieve Zero Liquid Discharge.

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Domestic: Discharge Into Septic Tank/Soak Pit

Industrial: Will be Treated in ROto In-House MEE& ATFD to achieve ZLD. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ Not Applicable Membership of Common facility (CF) (For waste water treatment) Not Applicable vii Simplified water balance diagram with reuse / recycle of waste water

554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 74 of 215 viii Reuse/Recycle details (22KLD) Total reuse: 0 KLD Source of waste Application Characteristics of Remarks water for reuse area with waste water to be regarding with quantity in quantity in reused (COD, BOD, feasibility KLD (From KLD (Where it TDS etc.) to reuse i.e. where it is is used) coming) 14 KLD from RO& In Washing(3)+ COD:< 10 mg/l 8 KLD from MEE Process (19) BOD: Nil TDS: <500 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.

- Air Source of Type of Stack Quantity Pollution Sr. emission Type of emissions Height of Fuel Control no. With Fuel i.e. Air (meter) MT/Day Measures Capacity Pollutants (APCM) Boiler Natu 175 1 (3.5- 30 ral SOx, NOx SCFM TPH) Gas

RVD Adequate (Rotary Stack Vaccu Natu Height me 90 2 15 ral SOx, NOx Dryer) SCFM Gas 12 Lacs Kcal

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Thermi c Fluid 45 LDO 3 Heater 10 Litre/ SOx, NOx /FO (4 Lacs Day Kcal) - ii Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO xetc.)

- There Will be Not any process gas emission from the process. Specific Source of emission Air Pollution Stack/Vent Sr. Type of Control (Name of the no. emission Height (meter) Measures Product & (APCM) Process)

1 ------

iii Fugitive emission details with its mitigation measures: As below: Necessary precautions will be taken care like development of water sprinkling system including development of green belt. F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type/Nam Specific Category Quant Management of HW no. e of Source of and ity Hazardou generation Schedule (MT/A s waste (Name of the as per HW nnum) Activity, Rules. Product etc.)

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Collection, Storage Within Factory Premises and transportation Proces From and Final Disposal 1 s 26.1 120 Process at TSDF Sludge (Approved by GPCB and falling outside CEPI area.).

Collection, Storage Within Factory Premises, transportation and ETP From ETP 2 35.3 08 Final Disposal at Waste Plant TSDF. (Approved by GPCB and falling outside CEPI area.).

Collection, Maintenance Storage Within Used of Factory Premises 3 5.1 0.6 Oil Production and sale to area registered re- processor.

Collection, Discard Storage, ed Maintenance Transportation & 4 Bags/Li of plant and 33.1 10 Disposal by selling ners/Ba machineries to authorized rrels vendor

5 Distillati From 36.1 23 Collection

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on distillation ,Storage Residu ,transportation e ,Incineration & disposal to CHWIF (Approved by GPCB and falling outside CEPI area.).or to Coprocess Cement Plant

Collection, storage reuse in next Spent From 6 26.4 165 process/sell to end Solvent Process user having Rule 9 pemission.

Collection, Storage Within Factory Premises and transportation and Final Disposal Spent From 25. at 7 28.3 Carbon Process 9 CHWIF(Approved by GPCB and falling outside CEPI area.)./ coprocess Cement Plant.

As Will be sold to & Spent regenerators have From wh 8 Catalys 26.5 hazardous Waste Process en t Rule 2016 gen category erat

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ed

Disposal by sell Formic out to authorized acid users who is solution From having 9 26.1 90 (50 Process authorization with to 60% valid CCA and rule soln); 9 permission to receive this waste.

Disposal by sell out to authorized chloride users who is 1 Solutio From having 26.1 250 0 n (20 Process authorization with to 22% valid CCA and rule soln) 9 permission to receive this waste.

By-Product for 1 From B2 19. sale - rule 9 PoCL3 1 Process (B2040) 8 permission to receive

Sod By-Product for .Bromid 1 From B2 sale - rule 9 e 39 2 Process (B2040) permission to Solutio receive n

By-Product for Sodium 1 From B2 11. sale - rule 9 Format 3 Process (B2040) 22 permission to e receive

1 Sodium From B2 By-Product for 3 4 Carbon Process (B2040) sale - rule 9

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ate permission to receive

Collection, Evapor Storage Within ated Factory Premises, Salt transportation and 1 From From MEE 35.3 55 Final Disposal at 5 MEE as TSDF(Approved ETP by GPCB and waste falling outside CEPI area.).. - ii Membership details of TSDF, CHWIF etc. Eco Care Infrastructure Pvt. (For HW management) Ltdor BEIL, Dahej(Which is approved by GPCB and falling outside CEPI area) iii Details of Non-Hazardous waste & its disposal Other municipal solid waste (MSW and others) generated would include kitchen waste, cardboards, papers, and garden waste. Cardboard and papers wastes will be handed over to scrap dealers and kitchen & garden waste would be sent to the nearest municipal waste collection site. G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)

S Product Solvent Quantity Loss Quantity Loss/ %

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. used Kg/Kg with ton /tone with Reco N produ produ very Fres Recyc Fres Rec o ct/Fug ct, T/T h le h ycle . itive Kg/Kg

1 4-NAX Di 1 115 50 1.2 1. 0.05 95. ethyl 2 0 1 83 keton 0 5 e 0

2 4- Butan 5 545 15 0.5 0. 0.01 97. Methyl ol 6 6 5 5 32 Catec 0 4 hol 5

3 Methyl Tolue 1 161 40 1.6 1. 0.04 97. ene ne 6 0 5 6 58 Dioxy 5 1 Pheno 0

l Meth 3 290 10 0.3 0. 0.01 96. (SESA anol 0 2 67 MOL) 0 9

4 O- Meth 1 950 50 1 0. 0.05 95. Benzyl anol 0 9 00 Hydro 0 5 xyl 0

Amine Tolue 8 775 25 0.8 0. 0.02 96. Hydro ne 0 7 5 88 chlorid 0 7 e 5

5 4- Meth 7 680 20 0.7 0. 0.02 97. Metho anol 0 6 14 xy 0 8 Benza

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ldehyd e Di methyl Acetal

6 Prega IPA 8 800 20 0.8 0. 0.02 97. balin 2 2 8 56 0

7 Etoric IPA+ 9 930 20 0.9 0. 0.02 97. oxib Hexa 5 5 9 89 ne 0 3

Tolue 3 360 20 0.3 0. 0.02 94. ne 8 8 3 74 0 6

THF 3 280 20 0.3 0. 0.02 93. 0 2 33 0 8

8 Lerca Tolue 3 303 10 0.3 0. 0.01 96. nidipin ne 1 13 3 81 e 3 0 Hydro 3

chlorid Ethan 1 170 10 0.1 0. 0.01 94. e ol 8 8 1 44 0 7

Ethyl 2 230 58 2.3 2. 0.05 97. aceta 3 0 58 3 8 54 te 5 8

9 Qutiap Meth 9 880 20 0.9 0. 0.05 97. inefum anol 0 8 78 arate 0 8

Tolue 4 445 124 4.5 4. 0.12 97.

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ne 5 0 74 4 4 29 7 5 4

DMA 1 130 16 0.1 0. 0.01 95. 3 36 1 6 59 6 3

1-(2- 2 280 166 0.2 0. 0.16 97. (2- 8 86 2 6 90 hydro 6 8 xyeth oxy)e thyl) Piper azine

1 Isobut HEX 1 120 10 0.1 0. 0.01 96. 0 yl 5 ANE 2 25 1 00 chloro 5 2

2,2 THF 1 95 20 0.1 0. 0.02 95. dimeth 0 0 00 ylvaler 0 9 ate 5

IBA 2 24 10 0.0 0. 0.01 96. 5 25 0 00 2 4

ii VOC emission sources and its mitigation measures • Closed handling & charging system will be provided. • Mechanical seals to pumps will be provided to prevent leakages. • Regular monitoring of VOCs will be done. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Remarks Hazardous chemicals

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Cylinder Hydrogen

‹ Applicability of PESO : Not Applicable

• During SEAC meeting dated 01/10/2019, technical expert of PP informed about proposed project is of dyes intermediate and bulk drug product. Committee asked about wastewater management disposal to CMEE outside CPA, technical expert of PP informed that they proposed in-house MEE and ATFD instead of sending effluent to CMEE after ETP and RO treatment. Committee asked for steam requirement and change in fuel consumption in boiler, PP could not able to justify regarding steam requirement for effluent to be evaporated in in-house MEE. Committee asked about stage wise reduction of pollutant in ETP and adequacy of in-house MEE instead of CMEE, technical expert of PP could not addressed satisfactorily it during meeting. Committee asked about air matrix, technical expert of PP informed that no process emission from proposed process. Committee disagree with no process emission from proposed project as hydrogenation, chlorination and bromination process involved in proposed project and informed PP for submit revised air matrix with APCM details and bleed liquor disposal details. • After detailed discussion, it was decided to consider the proposal only after submission of the following documents: 1. Submit proposal with steam requirement for in-house MEE and ATFD in addition to production plant and subsequent change in fuel consumption. 2. Adequacy of in-house MEE in place of CMEE with stage wise reduction of pollutant in ETP and MEE. 3. Revised Air matrix with mentioning regarding APCM for bromination and chlorination process and change in EIA report. 4. Revised Hazardous waste matrix with mentioning bleed liquor from scrubber generation and disposal details. 5. Revised Ambient air baseline data with monitoring parameters like HBr and HCl and revised EIA in this regard. 10. SIA/GJ/IND2/28359/2016 M/S. NUTRAPLUS INDIA LTD.(UNIT - EC – II) Reconsideration Plot No. C-198, Saykha Industrial Estate, Vagra, Bharuch.

Category of the unit: 5(f) Project status: New

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• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/28359/2016dated 29/07/19 for obtaining Environmental Clearance. • SEIAA issued ToR& ToR – Amendment to PP vide their letter dated 29/12/2016 & 26/02/2018. • Project proponent has submitted EIA Report prepared by Aqua Air Environmental Engineers Pvt Ltd, Suratbased on the ToR& ToR – Amendment issued by SEIAA. • This is a new unit proposes for synthetic organic chemicals as tabulated below: SR. PRODUCT NAME CAS NO. PROPOSED END USE NO. CAPACITY (MT/MONTH)

1 Ibuprofen 15867-27-1 Anti-Inflammatory

2 Diclofenac Sodium 15307-79-6 Anti

3 Aceclofenac 89796-99-6 Anti

4 Nimesulide 51803-78-2 Anti

5 Chlorzoxasone 95-25-0 Anti

6 Mefenamic Acid 61-68-7 Anti

7 Mesalamine 89-57-6 Anti

8 Albendazole 54965-21-8 Anti-Worm

9 Febendazole 43210-67-9 Anti-Trematode therapeutic

10 Mebendazole 31431-39-7 Anti-Worm medication

11 Metronidazole 443-48-1 Antibiotics

12 Metronidazole Benzoate 22916-47-8 Antibiotics

13 Tinidazole 19387-91-8 Antibiotics 400 14 Ornidazole 16773-42-5 Antibiotics

15 Oxyclozanide 2277-92-1 Anthelmintic

16 Roxarsone 121-19-7 Anthelmintic

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17 Chlorpheniramine Maleate 113-92-8 Antihistamines (C.P. Maleate)

18 BromhexineHcl 611-75-6 Antioxident/Expectorant

19 AmbroxolHcl 23828-92-4 Secretolytic

20 PhenyleffrineHcl 61-76-7 Decongestant

21 DexoMetherphanHbr 6700-34-1 Antihistamines

22 Salbutemol Sulphate 51022-70-9 Antihistamines

23 Theophyllin 58-55-9 Xanthines

24 Caffein 58-08-2 Ergotamine

25 Theobromine 83-67-0 Vasodilator

26 Ciprofloxacin 85721-33-1 Antibiotics

27 Oflaxacin 82419-36-1 Antibiotics

28 Enrofloxacin 93106-60-6 Antibiotics

29 Sildinafil Citrate 171599-83-0 pulmonary arterial hypertension

30 Tramadol Hcl 27203-92-5 Analgesic

31 Lumefantrine 82186-77-4 Antimalarial

32 Hydroxide 21645-51-2 Antacid Gel/Powder

33 Ampicillin 69-53-4 Antibiotics

34 Amoxicillin 26787-78-0 Antibiotics

35 Cloxacillon 61-72-3 Antibiotics

36 Cephalexin 15686-71-2 Antibiotics

TOTAL 400 MT/MONTH

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• This is a new unit proposes for manufacturing of Synthetic Organic Chemical as tabulated below:

• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006.

• During the meeting dated 14/08/2019, technical presentation made by the Project proponent. • During the meeting, the project was appraised based on the information furnished in the EIA Report and details presented during the meeting. • During the meeting dated 14/08/2019, committee noted that PP has not submitted EIA report in Hard copy and committee asked PP to clarify the same. PP mentioned that it got delayed and CTE – Fees for the project is also yet not paid however today they have brought the EIA report. Committee noted that due to delayed submission of EIA report in Hard Copy the committee members could not scrutinized the project along with whole report immediately. • After detailed discussion, it was decided to defer the proposal and consider the same only after submission of EIA Report along with Receipt of Fees Paid to GPCB as per the circular of GPCB for EC to CTE. • Project proponent submitted reply by revised format and presentation by e-mail dated 31/08/2019. • During SEAC meeting dated 04/09/2019, committee asked about CTE fees receipt and hard copy of EIA, Technical expert of project proponent informed that they have submitted CTE fees receipt and hard copy of EIA. Committee asked about waste water treatment for proposed project, Technical expert of PP informed that High COD effluent will be treated in solvent stripper and distillation unit and MEE. MEE condensate along with low COD effluent will be treated in primary, secondary and tertiary ETP and RO plant. RO permeate will be recycled back and RO reject will be evaporated in spray dryer.Committee asked about technical details of distillation unit proposed for effluent containing solvent with solvent details, PP could not explained about it. Committee asked about clarification regarding adequacy of spray dryer salt disposal for co-processing in cement industry, technical expert of PP could not explained satisfactorily. Committee asked about ToR no-12 regarding BAT for proposed project, PP replied that they will adopt BAT for proposed project which is not considered by committee and asked them to submit revised ToR no- 12 with adequate details for BAT for proposed process mentioning about waste reduction due to BAT. Committee asked about bleed liquor from scrubber disposal, PP informed that they have shown source of bleed liquor from manufacturing process instead of scrubber hence committee asked to submit each bleed liquor from scrubber generation and its disposal details. Committee asked about LDAR for solvent stripper and distillation unit for effluent containing solvent, technical expert of PP has not addressed it and addressed about LDAR for solvent utilized in manufacturing process. • After detailed discussion on the matter, It was decided to further appraise the project only after submission of the following:

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1. Adequacy of solvent stripper and distillation unit proposed for effluent containing solvent along with technical details of distillation unit. 2. Adequacy of treatment scheme proposed for high COD effluent stream with stage wise reduction of pollutant. 3. Adequacy of reuse of spent HCl and spent sulphuric acid generated from bulk drug products utilesed in another bulk drug products. 4. Adequate LDAR programme separately for effluent stream and manufacturing process with technical details like solvent recovery and solvent losses. 5. Revised ToR no-12 regarding Best Available Technology (BAT) for proposed process considering waste reduction. • Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned points. • PP presented replied as below: 1. Adequacy of solvent stripper and distillation unit proposed for effluent containing solvent along with technical details of distillation unit. 2. Adequacy of treatment scheme proposed for high COD effluent stream with stage wise reduction of pollutant. 3. Adequacy of reuse of spent HCl and spent sulphuric acid generated from bulk drug products utilesed in another bulk drug products. 4. Adequate LDAR programme separately for effluent stream and manufacturing process with technical details like solvent recovery and solvent losses. 5. Revised ToR no-12 regarding Best Available Technology (BAT) for proposed process considering waste reduction. • Committee observed that reply submitted by PP is satisfactory. • Salient features of the project including Water, Air and Hazardous waste management (Revised): Sr. Particulars Details no. A A Total cost of Proposed Project 50.0 Crores (Rs. in Crores):

ii EMP details (Capital cost & Recurring cost) ‹

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Environment Remedial Capital Cost Component Recurring Cost Issue/ Measures of EMP (Rs.) (Rs.) Component Hazardous Proper 5,00,000/ - TSDF facility 60,72,000 per waste collection, year generation & Safe Handling, (Expense) disposal Storage within premises (Hazardous waste storage yard ) BEIL 2,00,000/ - Incineration 1,58,40,000 / -Year membership facility charges Earn from Aluminium 660000x 1.5= Hazardous Chloride 9,90,000/- waste Sodium Bromide 816000x 2.0= 16,32,000/- : Ammonium 672000x 1.5= Chloride 6,72,000/- Aluminium 2760000x 1.0= Hydroxide 27,60,000/- Effluent ETP : 85 KLD ETP – Rs. Total Treatment 27,00,000/ -year generation and R.O : 85 KLD 85,00,000/- cost/Year treatment Spray Dryer : R.O : 25 15,00,000 /- Spray Dryer : 50,00,000 Details of Air Multi-Cylcone Stack – Maintenance of 3,00,000 /- Emission separator with 10,00,000/- Cycloneseparator bag filter and with bag filter scrubber

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Adequate pollution control system and Two stage scrubber Plantation 33.0 % of the 16,50,000/- Maintenance of 2,75,000/- plant area will green belt fertilizers be developed or damage plants as greenbelt. Monitoring of Regular 10,00,000 /- monitoring of 3,50,000/- Environmental monitoring of various parameters various environmental environmental parameters parameters will be carried out to check the effectiveness of the control system. Total 1,94,00,000/ - Expense: 2,55,37,000/year

Earn from 60,54,000 / -Year 21,28,083 / - Month Hazardous waste

iii CER details (As per MoEF&CC OM dated 01/05/2018) ‹ Rs. 100,00,000 As per OM no. 22-65/2017 on dated 01/05/2018 regarding “Corporate Environment Responsibility” (CER), Brownfield projects have to contribute 2% of the Additional Capital Investment, the company will contribute Rs 100.0 Lakhs as funds for CER activities Activities to be carried out under CER: ‹ Education, ‹ Health,

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‹ Environment, ‹ Agriculture

B Total Plot area ( sq. meter) 16067.36 Sq. m.

Green belt area 5300.36 Sq. m. ( sq. meter) C Employment generation Direct : 50 Nos. Indirect : 50 Nos. D Water i Source of Water Supply GIDC water Supply

(GIDC Bore well, Surface water, Tanker supply etc...)

Status of permission from the concern authority.

ii Water consumption (KLD) Category Quantity Remarks KLD (M) Domestic 21.0

(N) Gardening 3.0

(O) Industrial

Process 50.0

Washing 8.0

Boiler 35.0

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Cooling 30.0

Others(Scrubber) 2.0

Industrial Total 125.0 Total (A + B + C) 149.0

1) Total water requirement for the project:149.0 KLD 2) Quantity to be recycled :60.0 KLD 3) Total fresh water requirement: 89.0 KLD

iii Waste water generation (KLD) Category Waste Remarks water KLD (I) Domestic 21.0 (J) Industrial Process 60.0

Washing 8.0

Boiler 6.0

Cooling 5.0

Others/Scrubber* 2.0

Total Industrial 81.0 waste water Total [A + B] 102.0 - iv Treatment facility within premises with capacity

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[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.. M/s. Nutraplus India Ltd. (UNIT-II) shall have an Effluent treatment plant consisting of primary, secondary tertiary and advanced treatment units. The effluent confirming to inlet standards of GIDC drain. The details of ETP are as follows.

First all non-toxic and biodegradable streams (low & medium COD) of wastewater shall pass through Screen Chamber (SC) where floating material shall be removed with help of Screen (S-01). Then effluent shall be passed through Oil & Grease Removal Tank (OGRT). Automatic mechanical Oil Skimmer shall be provided in the OGRT to remove floating oil and grease from the wastewater to Oil & Grease Collection Tank (OGCT). Then effluent shall be collected in Collection cum Equalization tank (CET). Pipe grid is provided at bottom of the CET to keep all suspended solids in suspension and to provide proper mixing. 2 nos. of Air Blowers (1 stand-by) shall supply air through diffusers to pipe grid. Condensate from Multiple Effect Evaporator (MEE) shall also be collected in CET.

Then after, equalized wastewater shall be pumped to Neutralization Tank (NT) where the continuous addition and stirring of lime solution is done to maintain neutral pH of wastewater from Caustic Dosing Tanks (CDT) as per requirement by gravity. Then after, neutralized wastewater shall go to Flash Mixer-1 (FM) by gravity. Alum and Polyelectrolyte shall be dosed from Flocculants Dosing Tank (FLDT) and Polyelectrolyte Dosing Tank (PEDT) respectively by gravity into FM-1 to carry out coagulation by using a Flash Mixer.

Then after, coagulated wastewater shall be settled in Primary Tube Settler (PTS).Clear supernatant from PTS shall be passed in Aeration Tank (AT-1) Here, biodegradation of organic matter of the wastewater shall be carried out by bacteria (suspended growth) in the AT-1 and for that oxygen shall be supplied by 2 nos. of air blowers (B-02) through diffusers. Air blowers also keep MLSS in suspension.

Then after, wastewater shall go to Secondary Settling Tank-1 (SST-1) from AT. Here, the suspended solids shall be settled. Sludge shall be removed from bottom of SST-1 and

554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 93 of 215 pumped to AT-1 to maintain MLSS and excess activated sludge shall be sent to Sludge Sump (SS). Clear supernatant from SST-1 shall go to Aeration Tank-2 (AT-2). Here biodegradation of left out organic matter of the wastewater shall be carried out by bacteria (suspended g rowth) and for that oxygen shall be supplied by two nos. of blowers (B-03) with help of diffusers. Then after, wastewater shall go to Secondary Tube Settler (SST-2) from AT-2. Here, the suspended solids shall be settled. Activated sludge shall be removed from bottom of SST-2 and pumped to AT-2 to maintain MLSS and remaining will be sent to SS. Nutrients will be added from NDTs to Aeration Tank-2 for growth of Bacteria. Clear effluent is the collected in of Intermediate Sump (IS) by gravity.

Thereafter, t he wastewater shall be passed through Pressure Sand Filter (PSF) to remove left out TSS and Activated Carbon Filter (ACF) for final effluent polishing. After tertiary treatment, Filter water is collected to RO Feed Tank (RFT) and then pumped to RO Unit (la rge capacity) for further treatment. Treated water from RO will be reuse in process. RO reject will be sent to SD Feed Tank (SDFT) for further treatment. Then effluent shall be sent to Spray Dryer (SD). Solid from Spray Dryer shall be collected and stored in HWSA for ultimate disposal to TSDF. Sludge settled in PTS-1 and excess sludge from SST-1 & 2 shall be collected in Sludge Sump then sludge shall be pumped to Filter Press where, dewatering shall be carried out before storage in HWSA and ultimate disposal to TSDF.

All High COD & TDS streams of wastewater shall be collected in Solvent Stripper (STR) where solvent shall be removed from effluent and collected in Reactor (RE).Mother liquid from Solvent Stripper shall be sent in CET for further treatment.

S.N Size (m x m x m) Name of unit No. MOC/ Remark . L x B x (LD+FB) Stream I (Low COD & TDS Stream) 73 m 3/D + 12 m 3/D 1 Screen Chamber (SC- 1.5 m x 0.8 m 1 RCC M25+A/A 01) (0.05 m+0.7 FB) Bk. Lining 2 Collection cum 4.0 m x3.0 m x 1 RCC M25+A/A Equalization Tank (CET- (3.0 m+1.0 FB) Bk. Lining 01)

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3 Neutralization Tank (NT- 1.0 m x 1.0 m x 1 RCC M25+A/A 01) (2.5 m +0.5 FB) Bk. Lining 4 Flash Mixer (FM-01) 1.0 m x 1.0 m x 1 RCC M25 (2.3 m +0.7 FB) 5 Primary Tube Settler 2.75 m x2.0 m x 1 RCC M25 (PTS-01) (2.0 m + 0.5 HB+0.5 FB) 6 Aeration Tank-1 (AT-01) 8.0 m x 7.5 m x 1 RCC M25 (4.0 m+0.7 m) 7 Secondary Settling 3.0 m x 2.0 m x 1 RCC M25 Tank-1 (SST-01) (2.0 m + 0.5 HB+0.5 FB) 8 Aeration Tank-2 (AT-02) 7.5 m x 6.0 m x 1 RCC M25 (4.0 m+0.7 m) 9 Secondary Settling 2.5 m x 2.0 m x 1 RCC M25 Tank-2 (SST-02) (2.0 m + 0.5 HB+0.5 FB) 10 Intermediate Sump (IS- 2.0 m x 2.0 m x 1 RCC M25 01) (2.5 m+0.5) 11 Pressure Sand Filter 5 m3/hr 1 FRP (PSF-01) 12 Activated Carbon Filter 5 m3/hr 1 FRP (ACF-01) 13 RO Feed Tank (ROFT- 4.0 m x3.5 m x 1 RCC M25 01) (2.5 m+0.5 FB) 14 RO Unit 4.25 m 3/hr 1 As per spec.

15 Sludge Sump(SS-01) 2.0 m x 2.0 m x 1 RCC M25 (2.5 m + 0.5) 16 Filter Press(FP-01) 7 m 3 / batch 1 PP

17 Drain Pit(DP-01) 1.0 m x1.0 m x 1 RCC M25 (2.0 m+0.3 FB) 18 SD Feed Tank(SDFT- 3.0 m x 2.5 m x 1 RCC M25 01) (2.5 m + 0.3 FB)

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19 Spray Dryer(SD) 21 m 3/Day 1 SS Stream II (High COD & High TDS stream) 35 m 3/D 20 Stripper Feed 4.0 m x3.5 m x 1 RCC M25+A/A Tank(SFT-01) (2.5 m+0.5 FB) Bk. Lining 21 Solvent Stripper (STR) 35 m3/D 1 SS 22 Reactor (RE) 12 m3 1 SS 23 Distillation Unit 23 m3/D 1 SS

DETAILS OF SOLVENT STRIPPER

• All the solvents shall be directly distilled from high COD effluent with the help of Solvent Stripper and Distillation. • The solvent distillation system shall be designed so as to achieve minimum 92.0 % recovery of solvent. • Pure solvent, crude solvent and distilled (recovered) solvent shall be stored only in storage tanks. • Wherever required, the solvents shall be directly pumped into day tanks from the storage tanks and shall be charged into the reactors without involving any manual handling. • All the pumps shall be mechanical seal type to avoid any leakage of solvent. • All necessary fire fighting systems shall be provided with alarm system. Flame proof wiring and flame proof electrical accessories shall be provided to avoid any mishap. • 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 are 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 Adsorber for removing traces of solvent from vent gases. • Residue generated from the distillation will be incinerated in-house or sent to BEIL incinerator site. TECHNICAL DETAILS OF SPRAY DRYER Tall Form Nozzle spray dryers form into two main categories the Standard Spray 554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 96 of 215

Dryer Chamber and the Bustle Spray Dryer Chamber. With the standard spray dryer design all the air and powder is removed from the base of the chamber and transported to a powder separator, either cyclone or bag filter. This type of machine is prevalent in the production of food and chemicals and is relatively low in cost, easy to operate and very low maintain. The bustle is used more usually employed on larger throughputs and where delicate products or multi stage drying is required. Bustle dryers are highly versatile but retain the ease of operation and low maintenance costs of the standard dryer. Bustle dryers allow powder extraction from the base of the chamber and through conveying ducts at the base of the cylindrical section that transport fine particles and air to the separation cyclones or bag filters. Far ease we have based measurements on cyclones only and plant heights do not take account of secondary processes which must be allowed for when sizing a building. Bustle chambers blend themselves to fines recycling to allow the production of agglomerated particles especially with multiple nozzles.

Air Filter Air is drawn into the system through a filter, figure . The efficiency of the filter will depend on the product being dried. In general chemicals require less filtration while the processing of some food stuffs and pharmaceuticals require very high efficiency filters. On most applications there are two banks of filters a low efficiency filter followed by a higher efficiency filter medium. Filters generally have two functions, the first to avoid contamination of product being dried and the second to stop particles passing through the hot air system and becoming a possible spark as it enters the chamber which could be a possible ignition source for fires and explosions.

Flow Diagram of Effluent Treatment Plant:

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Treatment scheme including segregation at source. ‹ Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ Not Applicable v Mode of Disposal & Final meeting point

Domestic: It will be added in biological treatment of ETP.

Industrial: • Total water requirement will be 149 m3/day (89 Fresh + 60 Recycled) which will be met through GIDC water supply. The wastewater generation will be 102 m3/day. • High COD stream (27 m 3/day) from process will be treated in solvent stripper and solvents shall be distilled in solvent

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distillation facility. Mother liquor from solvent stripper shall be sent to collection tank of ETP. Recovered solvent shall be reused and distillation residue will be sent to cement industries for co-processing or sent to CHWIF. • Low COD stream from Solvent stripper, Process, Boiler, Cooling, Washing/Scrubbing & Domestic effluent (75 m3/day) will be sent to proposed ETP consists of primary, secondary & tertiary treatments. To achieve the Zero Liquid Discharge, Treated effluent from ETP (85 m3/day) shall be treated in R.O. plant. Then R.O. permeate (60 m3/day) shall be reused in Boiler and Cooling while, R.O. reject (25 m3/day) shall be treated in spray dryer & salt will be sent to TSDF site for disposal. • Domestic wastewater will be added in biological treatment of ETP. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , Name of CF

-- Membership of Common facility (CF) (For waste water treatment) vii Simplified water balance diagram with reuse / recycle of waste water

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viii Reuse/Recycle details (KLD) Total reuse 0.0 KLD Source of waste Application area with Remarks water for reuse quantity in KLD regarding with quantity in feasibility to KLD reuse i.e. w/w characteristics (COD, BOD, TDS etc.) R.O Permeate Boiler & Cooling PH : 7.5 COD :<25.0 TDS :<150.0

E Air

554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 100 of 215 i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

- Details Of Flue Gas Emission Sr. Source of Stack Type of Quantity Type of Air No. emission Height Fuel of Fuel emissions Pollution With (meter) MT/Day i.e. Air Control Capacity Pollutants Measures 1 Steam 30. 0 M Coal/ 24 Pm<150 Multi - Boiler Briquette MT/Day Mg/Nm 3 Cylcone

6 TPH *2 s of Bio- or So 2< 100 separator Nos. Coal 15 ppm with bag MT/Day Nox< 50 filter and ppm water scrubber 2 Thermopac 30. 0 M Coal/ 24 PM<150 Multi - k Briquette MT/Day Mg/Nm 3 Cylcone

Capacity s of Bio- or So 2< 100 separator (4000 U) Coal 15 ppm with bag MT/Day Nox< 50 filter and ppm water scrubber 3 D. G Set 11. 0 M Diesel 2000 PM<150 Adequate 1000 KVA Lit/Day Mg/Nm 3 Height

So 2< 100 Provided. ppm Nox< 50 ppm - ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.)

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- Details Of Process Gas Emission Particulars Hei Emission Norms APCM ght Process Vent*-1 15 HCl < 20 mg/Nm 3 Two Stage (Product :15 : Oxyclozanide) m SO2 < 40 mg/Nm 3 Scrubber (Product :10 : Mebendazole) (Water + Alkali) Process Vent*-2 15 CL2< 9.0 mg/Nm 3 Two Stage (Product :10 : Mebendazole) (Product m Scrubber :23 : Theophylline) (Product :24 : (Water + Caffein) Alkali) Process Vent*-3 : 15 NH3< 175.0 Two Stage (Product :20 Phenylpherine) (Product m mg/Nm 3 Acid :29 Sildinafil Citrate) (Product :34 Scrubber Amoxicillin Trihydrate) Process Vent*-4 : 15 HBR< 30.0 Two Stage (Product :21 Dexometherphan) m mg/Nm 3 Alkali Scrubber

iii Fugitive emission details with its mitigation measures. As below: ‹ Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures. ‹ Care will be taken to store construction material properly to prevent fugitive emissions, if any ‹ Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs. ‹ Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature. ‹ Periodic monitoring of work area will be carried out to check the fugitive emission. ‹ Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers. ‹ Minimum number of flanges, joints and valves in pipelines.

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Enclosures to chemical storage area, collection of emission from loading of raw materials.

F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type/Name of Specific Source of Category Quantity Management of HW Hazardous generation and no. (MT/Annum) waste Schedule (Name of the as per Activity, Product HW etc.) Rules.

1 ETP Sludge From ETP plant Sch- 636 Collection, Storage, I/35.3 Transportation & MT/Year sent for co- processing in cement industries or disposal at nearest TSDF Site.

2 Discarded From raw material Sch- 36.0 Collection, Container/ I/33.1 Storage, MT/Year Transportation, Bags/Drums Decontamination & Sell to authorized vendors

3 HDPE Bags From raw material Sch- 12.0 Collection, I/33.1 Storage, MT/Year Transportation, Decontamination & Sell to authorized vendors

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4 Distillation From Solvent Sch- 360.0 Collection, Residue Recovery plan I/33.1 Storage, MT/Year Transportation & sent for co- processing in cement industries or disposal at common incineration site

5 Spent From mfg. Sch- 360.0 Collection, Solvent Process I/36.1 Storage, and in- MT/Year house solvent recovery plan & Reuse in plant premises.

6 Used Oil From plant Sch- 6.0 Collection, machinery I/5.1 Storage, MT/Year Transportation & Reuse or sale to registered re- processors

7 Process From plant Sch- 480.0 Collection, Waste machinery I/28.1 Storage, MT/Year Transportation & 8 Spent Carbon From mfg. Sch- 192 sent for co- process Product I/28.3 MT/Year processing in no.02,04,10- cement industries 16,18,19,21,25,26 or disposal at -30,36 common incineration site

9 Iron Sludge From mfg. Sch- 1200 Collection, process Product Storage,

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no.04,18,23,24,29 I/28.1 MT/Year Transportation & sent for co- processing in cement industries

1 Spent Catalyst From mfg. Sch- 24.0 Collection, 0 process Product I/28.2 MT/Year Storage, no.09,22 Transportation & return back to supplier for re- generation or Sent to nearest common Incineration Site. 1 Spray Dryer From waste water Sch- 1200 Collection, 1 Salt treatment I/35.3 MT/Year Storage, Transportation & sent for co- processing in cement industries or disposal at nearest TSDF Site. 1 HCl (32%) From mfg. Sch- 4800.0 Collection, 2 process Product I/28.1 MT/Year Storage, no.07,08 & Transportation Scrubber And Reuse in ROXARSONE (Require Quantity of HCL (32%)– 5400 MT/Annum) 1 H SO (70%) From mfg. Sch- 3840.0 Collection, 2 4 3 process Product I/28.1 MT/Year Storage, no.09,22 Transportation

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And Reuse in IBUFROFEN (Req uire Quantity of H2SO4 (70%)– 1296.0 MT/Annum) or METRONIDAZOL E (Require Quantity of H2SO4 (70%)–5520.0 MT/Annum) or TINIDAZOLE (Require Quantity of H2SO4 (70%)– 3408.0 MT/Annum) or ORNIDAZOLE (Require Quantity of H2SO4 (70%)– 7824.0 MT/Annum). 1 Sodium From mfg. Sch- 360.0 Collection, 4 Sulphite process Product I/28.1 MT/Year Storage, no.15,10 & Transportation & Scrubber sell to end user having Rule-9 Permission. 1 Sodium From mfg. Sch- 180.0 Collection, 5 hypochlorite process Product I/28.1 MT/Year Storage, no.15,10 & Transportation & Scrubber sell to end user 1 Ammonium From mfg. Sch- 672.0 having Rule-9 6 Chloride process Product I/28.1 MT/Year Permission.

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no.08,22

1 Sodium From mfg. Sch- 1800.0 7 Sulphate process Product I/28.1 MT/Year no.17,23 1 Sodium From mfg. Sch- 816.0 8 Bromide process Product I/28.1 MT/Year no.08 & Scrubber 1 KCl Salt From mfg. Sch- 288.0 9 process Product I/28.1 MT/Year no.04 2 Sodium From mfg. Sch- 1200 Collection, 0 Carbonate process Product I/28.1 MT/Year Storage, no.07,22 Transportation And Reuse in MESALMINE (Req uire Quantity of Sodium Carbonate (1200.0 MT/Annum) or SALBUTAMOL SULPHATE (Require Quantity of Sodium Carbonate (144.0 MT/Annum) Send to End users having Rule 9 permission. 2 AlCl From mfg. Sch- 660.0 Collection, 2 1 process Product I/28.1 MT/Year Storage, no.22,26 Transportation And Send to End

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users having Rule 9 permission. 2 Al(OH) From mfg. Sch- 2760.0 Collection, 3 2 process Product I/28.1 MT/Year Storage, no.01,02,10,32 Transportation & sell to end user having Rule-9 Permission. 2 NaOH From mfg. Sch- 768.0 Collection, 3 process Product I/28.1 MT/Year Storage, no.07 Transportation And Reuse in MESALMINE (Req uire Quantity of Sodium Hydroxide (864.0 MT/Annum) or Send to End users having Rule 9 permission. 2 MnO From mfg. Sch- 1920.0 Collection, 2 4 process Product I/28.1 MT/Year Storage, no.19 Transportation & 2 Methane From mfg. Sch- 2160.0 sell to end user 5 Sulfonic Acid process Product I/28.1 MT/Year having Rule-9 no.21 Permission. 2 Methyl From mfg. Sch- 3060.0 6 Sodium process Product I/28.1 MT/Year Sulphate no.24 2 MMA Solution From mfg. Sch- 624.0 7 process Product I/28.1 MT/Year no.25 2 Ether From mfg. Sch- 624.0 8 process Product I/28.1 MT/Year

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no.26

Non-Hazardous Waste

1. Fly Ash From APCM -- 360.0 Collection, MT/Year Storage, Transportation and sell to brick manufacturer

ii Membership details of TSDF, CHWIF etc. (Detox Group) (For HW management) iii Details of Non-Hazardous waste & its disposal Fly Ash : Collection, Storage, (MSW and others) Transportation and sell to brick manufacturer G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents 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 condensed vapors will be condensed in a Secondary Condenser Secondary Condenser HE-02: Chilled Brine at - 5 0C will be used to condense the non condensed vapors in the Secondary Condenser Final venting will be done after passing through carbon column. 95.0 % up of Spent solvent will be recovered ii VOC emission sources and its mitigation measures • All the solvents are directly distillate from product mix and purified in packed column with the help of reflux and therefore there is no generation of any distillation residue from the solvent distillation. • The solvent distillation system is designed so as to achieve minimum 95% recovery of solvent.

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• Pure solvent, crude solvent and distilled (recovered) solvent shall be stored only in storage tanks and we shall not be using drums at any stage in the Solvent Management System. • Wherever required, the solvents shall be directly pumped into day tanks from the storage tanks and shall be charged into the reactors without involving any manual handling. • All the pumps shall be mechanical seal type to avoid any leakage of solvent. • All necessary fire fighting systems shall be provided with alarm system. Flame proof wiring and flame proof electrical accessories shall be provided to avoid any mishap. • All the storage tank and day tank shall be connected to a vent system through chilled water condensers to prevent loss of solvents in the atmosphere. All the distillation column vents are also connected to chilled water condensers for maximum possible recovery of the solvents. Vacuum Distillation • Enclosed Processed • Minimum joints/flanges • Adequate Condenser • Brine will be utilized as chilling agent • Pumps with double mechanical seals • Proper Ventilation • PPEs • During SEAC meeting dated 01/10/2019, committee asked about Adequacy of Solvent stripper and distillation unit proposed for effluent containing solvent along with technical details of distillation unit and Adequacy of treatment scheme proposed for high COD effluent stream with stage wise reduction of pollutant., PP informed that effluent first will be passed through solvent stripper and then distilled in distillation unit. Committee disagree with high COD effluent will be treated in solvent stripper and distillation unit and insisted for revised proposal for ZLD instead of solvent stripper and distillation unit. • PP has addressed ToR 12 regarding BAT. • Committee asked about adequacy of reuse of spent HCL and sulphuric acid generated from bulk drug products utilized in another bulk drug products, PP simply mentioned spent HCl and spent sulhuric acid generation and reuse in production plant. PP informed LDAR programme for solvent in details. • After detailed discussion, it was decided to consider the project only after submission of the following

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documents. 1. Submit revised proposal of MEE(ZLD) instead of solvent stripper and distillation unit for high COD/TDS effluent stream 2. Adequacy of ETP and MEE for treatment of effluent with stage wise reduction in pollutants of effluent. 3. Readdress Adequacy of reuse of spent HCl and spent sulphuric acid generated from bulk drug products. 11. SIA/GJ/IND2/37454/2018 M/S. S. M. CHEMICALS EC – Plot No: 3103, Chemical Zone, GIDC Reconsideration Estate, Sarigam,Valsad. • PP remained absent in the EC – Appraisal presentation held on 01/10/2019. • Committee decided to defer the proposal and consider the same in one of the upcoming meeting of SEAC. 12. SIA/GJ/IND2/30806/2019 M/S. RAJPUTANA STAINLESS LIMITED ToR – Plot no- 213, Vill- Mahwas, Halol Kalol Road, Reconsideration Ta- Kalol, Dist- Panchmahal

Category of the unit: 3(a) Project status: Expansion • This office has received an application vide their online proposal no. SIA/GJ/IND2/30806/2019dated 01/04/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report. • Project proponent (PP) has submitted Form-1, PFR and relevant details/information. • This is existing unit and now proposes for products tabulated as below:

Sr. Name of the CAS no. / Quantity End -use of the no. Products CI no. MT/Annum products Existing Proposed Total 1 SS.MS & Alloy SS-65997-19-5 20000 20000 48000 SS-Chemical Steel(AS) Ingots Industries, and Billets 2 SS.MS & Alloy AS-7440-44-0 5000 31000 36000 Furniture Steel (AS) Bars Industries Engg. 3 Bright Bars MS-7429-90-5 3000 3000 6000 Utensil & Exports AS-Engg

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&Machinery Industries MS- Construction & Engineering Total 28000 62000 90000

• The project falls under Category B of project activity 3(a) as per the schedule of EIA Notification 2006. • Earlier Project Proponent remained absent during meeting on dated 15/04/2019 and 03/05/2019, hence committee decided to defer the proposal in one of the upcoming SEAC meeting. • Again PP was called for presentation in the SEAC meeting dated 04/09/2019. • Technical presentation was made by the project proponent with consultant/expert Green circle during SEAC meeting dated 04/09/2019. • Committee noted that this proposal is for expansion project located outside notified area. • During SEAC meeting, PP informed that unit is having valid CCA for existing plant and CCA compliance report submitted. Show cause notice issued by the GPCB and compliance reply of it submitted by the unit. Committee asked clarification regarding Production capacity for proposed expansion is showing in MT/Month while existing plant CCA production capacity in MT/Year, PP confessed that it is shown by mistake in MT/Month. Committee asked about waste water management and its disposal for proposed expansion project, PP could not express its view regarding existing plant and proposed plant waste water treatment and its disposal scheme. Committee asked about waste water and Hazardous waste generation from pickling section, PP is not able to explain about pickling waste water and Hazardous waste management. Committee informed PP to submit revised air and Hazardous waste matrix with mentioning about pickling section stack and APCM and ETP sludge management. • After detailed discussion, it was decided to defer the proposal and consider the same in one of the upcoming meeting with submission of following details, 1. Revised product profile with mentioning production capacity in MT/year instead of MT/Monthas per existing CCA. 2. Technical justification regarding proposed project cost with respect to mentioning existing plant project cost. 3. Submit proposal of adequate ETP with treatability report for waste water management. 4. Submit mode of disposal of treated industrial effluent for proposed project. 5. Submit proposal of adequate APCM and stack for pickling section and its bleed liquor disposal. 6. Submit revised Hazardous waste matrix with mentioning about ETP waste generation and its disposal management. 554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 112 of 215

• Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned points. • PP presented replied as below: 1. Revised product profile with mentioning production capacity in MT/year instead of MT/Month as per existing CCA. 2. Technical justification regarding proposed project cost with respect to mentioning existing plant project cost. 3. Submit proposal of adequate ETP with treatability report for waste water management. 4. Submit mode of disposal of treated industrial effluent for proposed project. 5. Submit proposal of adequate APCM and stack for pickling section and its bleed liquor disposal. 6. Submit revised Hazardous waste matrix with mentioning about ETP waste generation and its disposal management. • Salient features of the project including Water, Air and Hazardous waste management (Revised): Sr. Particulars Details no. A Total cost of Proposed Project Existing: 98.39 crore (Rs. in Crores): Proposed:3.50 crore Total:101 crore B Total Plot area Existing: 43000Sq. m. ( sq. meter) Proposed: 15800Sq. m. Total: 43000Sq. m. Green belt area Existing: 500Sq. m. ( sq. meter) Proposed: 13700Sq. m. Total: 14200Sq. m. C Employment generation Existing: 396 Proposed:150 Total:546 D Water Source of Water Supply Bore Well (GIDC Bore well, Surface water, Tanker supply etc...) i Status of permission from the concern authority. NOC Application No. 21- 4/4666/GJ/IND/2018

554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 113 of 215 ii Water consumption (KLD)

Existing Proposed Total after Remarks KLD (Additional) Expansion KLD KLD (P) Domestic 10 15 25 (Q) Gardening 5 17.5 22.5 (R) Industrial Process 5 20 25 Washing 5 10 15 Boiler - - - Cooling 10 20 30 Others - - - Industrial Total 20 50 70 Grand Total 35 82.5 117.5 (A+B+C) 1) Total water requirement for the project:117.5 KLD 2) Quantity to be recycled: 0.00 KLD 3) Total fresh water requirement:117.5 KLD (Total water requirement = Fresh water + Recycled water) Waste water generation (KLD) iii Category Existin Proposed Total after Remarks g (Additional Expansion KLD ) KLD KLD (K) Domestic 10 14 24 (L) Industrial

Process 3 20 23 Washing 5 10 15 Boiler - - - Cooling 0 0 0

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Others - - - Total Industrial 18 44 62.0 waste water

iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.

v Mode of Disposal & Final meeting point

Domestic: Soak Pit Industrial: ETP vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)

Membership of Common facility (CF) (For waste water treatment)

554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 115 of 215 vii Simplified water balance diagram with reuse / recycle of waste water

vii Reuse/Recycle details (KLD) [Source of reuse & application area] Total reuseKLD - Source of waste water Application area Characteristics of waste Remarks for reuse with with quantity in water to be reused (COD, regarding quantity in KLD (From KLD (Where it is BOD, TDS etc.) feasibility to where it is coming) used) reuse i.e.

E Air

Flue gas emission details i No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Existing & Proposed - Source Type of Air Stack Type Quantity Sr. of emissions Pollution Height of of Fuel no. emission i.e. Air Control (meter) Fuel MT/Day With Pollutants Measures

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Capacity (APCM)

Heating furnace 1 15 HSD 200LPH Bag Filter of rolling PM, SO x, mill NO x

2 D.G. Set 11 LDO 150 LPH -

- ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO xetc.) Existing & Proposed - Specific Source of emission Stack/Vent Air Pollution Control Sr. Type of (Name of the Height Measures no. emission Product & (meter) (APCM) Process)

Stack Attached So x,No x, 1 12 Bag Filter to AOD unit SPM - iii Fugitive emission details with its mitigation measures. F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Existing & Proposed i Sr. Type/Na Specific Catego Quantity Management of HW no. me of Source of ry and (MT/Annum) Hazardo generation Sched us (Name of ule as Existin Propose Total waste the per g d Activity, HW Product Rules. etc.)

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1 Used oil Machinery 5.1 500 - 500 Collection, Storage and Lubrication kg/yea kg/year sell to Authorized User r 2 Discarde From Raw 33.1 2 - 2 Collection, storage, reuse d Material MT/Ye MT/Year and disposal at containe Section ar decontamination facility or r/ Barrel/ by sent to suppliers Liner 3. Acid Pickling 12.1 100 75 175 Collection,Storage,Transp residue Section KG/Ye KG/Year KG/Year ortation and Disposal at from ar TSDF site pickling 3 Fuel gas From 11.4 12 03 15 Collection,Storage,Transp cleaning heating MT/Ye MT/Year MT/Year ortation and Disposal at residue ar TSDF site

- ii Membership details of TSDF, CHWIF etc. yes (For HW management) iii Details of Non-Hazardous waste & its disposal(MSW and others) G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents. ‹ There is no solvents recovery ii VOC emission sources and its mitigation measures ‹ No • During SEAC meeting dated 01/10/2019, Committee asked for revised product profile, PP informed that they have submitted revised product profile with change capacity of production in MT/Annum instead of MT/Month. • PP presented wastewater generation, its treatment and management. • Upon asking PP could not explained ETP with treatability report for waste water management along with reuse and mode of disposal of treated industrial effluent for proposed project. • PP has not addressed APCM for pickling section,scrubber bleed liquor disposal details and ETP sludge generation quantity.

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• After detailed discussion, it was decided to consider the project after submission of following details, 1. Submit proposal of adequate ETP with treatability report for waste water management along with reuse and mode of disposal of treated industrial effluent for proposed project. 2. Submit proposal of adequate APCM and stack for pickling section and its bleed liquor disposal. 3. Submit revised Hazardous waste matrix with mentioning about ETP waste generation and its disposal management. 14. SIA/GJ/IND2/36039/2019 M/S. MEDIKAMENT PHARMA ToR - Plot No – C/368, GIDC – Sayakha, Reconsideration Ta- Vagra, Dist: Bharuch

Category of the unit : 5(f) Project status : New • This office has received an application vide their online proposal no. SIA/GJ/IND2/36039/2019 dated 22/05/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report. • Project proponent (PP) has submitted Form-1, PFR and relevant details/information. • This is a new unit proposes for manufacturing of synthetic organic chemicals as tabulated as below: Sr. CAS no. /CI Quantity End -use of the Name of the Products No no. (MT/Month) products

Group 1

2 Bromo 4-5- Dimethoxy Pharma Intermediates 1. 53207-00-4 Benzyl Bromide AND/OR

2-(Diethylamino)ethyl Chloride Amiodarone, Hydrochloride AND/OR Bietaserpine, Butetamate, Camylofin, Ciclonium bromide, 40.00 , 2. 869-24-9 Cloricromen, DEA Dextran, Dimazole, Etafenone, Etamiphylline, Fenoxedil, Flurazepam, Gallamine triethiodine,

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Imolamine, Isothipendyl, Methadone, Myrtecaine, Naftidrofuryl, Oxitefonium bromide, Penthienate methobromide, Phenglutarimide, Promethazine, Propoxycaine, Proxymetacaine, Tiamulin, Tibezonium iodide, Tiropramide

2,3,4 Bis -o-(1 methyl)-B-D- Topiramate 3. N/A Fructopyranose AND/OR

2-Methyl-4,5-Dimethoxybenzoic Fragrance Intermediate 4. N/A Acid AND/OR

5. 3-Methoxy Phenol AND/OR 150-19-6 Aroma chemical

6. 4-Iso Propyl Catechol AND/OR 2138-43-4 Perfumery agent

4-Methyl Cathechol Diacetic Fragrance Intermediate 7. 52589-39-6 Acid Dimethyl Ester AND/OR

8. 6 chloro hexanol AND/OR 2009-83-8 Aroma Chemical

6-Chloro-5(2-Chlor Ethyl) Ziprasidone 9. 118289-55-7 Oxindole AND/OR

Benzaldehyde Dimethyl Acetal Flavor and Compounds 10. 1125-88-8 AND/OR

Bis(2-chloroethyl)amine Aripiprazole, hydrochloride AND/OR Batoprazine, 11. 821-48-7 Cyclophosphamide, Eltoprazine

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hydrochloride, phosphate, Ifosfamide, Itraconazole, , Lensiprazine, Naluzotan, Trazodone

Cetyl Pyridinium Chloride This is mainly used in AND/OR mouthwashes, toothpastes, lozenges, 12. 123-03-5 throat sprays, Breathe sprays, antiseptic towels, and nasal sprays.

13. Lasamide AND/OR 2736-23-4 Furosemide

N,N Dimethyl Form amide Imatinib,itraconazole 14. 4637-24-5 Diemthyl Acetal AND/OR

15. Sesamol AND/OR 533-31-3 Paroxetine

2-Diethylaminoethanethiol Desvenlafaxine 16. 1942-52-5 AND/OR

Guanidine AND/OR sulfamethyldiazine, 17. 50-01-1 sulfamethazine and folic acid intermediates

Analgesic

Dimethyl fumarate And/Or its Analgesic 18. 624-49-7 intermediates AND/OR

Etodolac And/Or its 41340-36-7 Analgesic 19. intermediates AND/OR /12188-02-7

Iguratimod And/Or its Analgesic 20. 149436-41-9 intermediates AND/OR

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Naproxen And/Or its Analgesic 21. 3900-45-6 intermediates AND/OR

Pregabalin And/Or its 75143-89-4 Analgesic 22. intermediates AND/OR /181289-15-6

Anti Prostatic

Naftopidil And/Or its AntiProstatic 23. 5464-78-8 intermediates AND/OR

AntiArrhythmias

Ivabradine Hcl And/Or its AntiArrhythmias 24. 148870-57-9 intermediates AND/OR

AntiAsthmatic

Doxofylline And/Or its AntiAsthmatic 25. 7252-83-7 intermediates AND/OR

AntiBiotic

Amoxicillin And/Or its Antibiotic 26. 551-16-6 intermediates AND/OR

Chloramphenicol And/Or its Antibiotic 27. 56-75-7 intermediates AND/OR

Doxycycline And/Or its Antibiotic 28. 24390-14-5 intermediates AND/OR

Erythromycin And/Or its Antibiotic 29. 114-07-8 intermediates AND/OR

Metronidazole And/Or its Antibiotic 30. 443-48-1 intermediates AND/OR

Trimethoprim And/Or its Antibiotic 31. 738-70-5 intermediates AND/OR

AntiCoagulant

Dabigatran And/Or its AntiCoagulant 32. 212322-56-0 intermediates AND/OR

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Rivaroxaban And/Or its 898543-06-1 / AntiCoagulant 33. intermediates AND/OR 446292-08-6

Warfarin And/Or its AntiCoagulant 34. 81-81-2 intermediates AND/OR

AntiConvulsants

Carbamazepine And/Or its AntiConvulsants 35. 298-46-4 intermediates AND/OR

Levetiracetam And/Or its AntiConvulsants 36. 7682-20-4 intermediates AND/OR

Topiramate And/Or its AntiConvulsants 37. 106881-35-0 intermediates AND/OR

AntiDepressant

Desvenlafexine And/Or its AntiDepressant 38. 93413-61-7 intermediates AND/OR

Venlafaxine hydrochloride AntiDepressant 39. And/Or its intermediates 93413-76-4 AND/OR

AntiDiabetic

Gliclazide And/Or its AntiDiabetic 40. 58108-05-7 intermediates AND/OR

Glipizide And/Or its AntiDiabetic 41. 5521-55-1 intermediates AND/OR

Metformin Hydrochloride AntiDiabetic 42. And/Or its intermediates 1115-70-4 AND/OR

Saxagliptin And/Or its AntiDiabetic 43. 361440-67-7 intermediates AND/OR

Sitagliptin And/Or its AntiDiabetic 44. 762240-14-6 intermediates AND/OR

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Voglibose And/Or its AntiDiabetic 45. 83480-29-9 intermediates AND/OR

AntiHypertensive AntiDiabetic

Diltiazem hydrochloride AntiDiabetic 46. And/Or its intermediates 42399-49-5 AND/OR

Irbesartan And/Or its AntiDiabetic 47. 138401-24-8 intermediates AND/OR

Metoprolol Succinate And/Or its AntiDiabetic 48. 56718-70-8 intermediates AND/OR

Perindopril And/Or its AntiDiabetic 49. 82834-12-6 intermediates AND/OR

Valsartan And/Or its AntiDiabetic 50. 482577-59-3 intermediates AND/OR

AntiLipemic

Fenofibrate And/Or its AntiLipemic 51. 42017-89-0 intermediates AND/OR

AntiPsychotic AntiLipemic

Aripiprazole And/Or its AntiLipemic 52. 119532-26-2 intermediates AND/OR

Clozapine And/Or its AntiLipemic 53. 5786-21-0 intermediates AND/OR

Escitalopram oxalate And/Or its AntiLipemic 54. 717133-25-0 intermediates AND/OR

Olanzapine And/Or its AntiLipemic 55. 138564-60-0 intermediates AND/OR

Erectile Dysfunction

Sildenafil Citrate And/Or its Erectile Dysfunction 56. 139756-21-1 intermediates AND/OR

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Proton Pump Inhibitors

Esomeprazole Proton Pump Inhibitors 57. And/Or its intermediates 73590-85-9 AND/OR

Lansoprazole And/Or its Proton Pump Inhibitors 58. 127337-60-4 intermediates AND/OR

SSRIs

Citalopram And/Or its SSRIs 59. 103146-26-5 intermediates AND/OR

Paroxetine HCl Hemihydrate SSRIs 60. And/Or its intermediates 105812-81-5 AND/OR

Sertraline And/Or its SSRIs 61. 79617-89-3 intermediates

Group 2

AntiMuscarinics

62. Tiotropium Bromide And/Or its AntiMuscarinics 85700-55-6 intermediates AND/OR

AntiOsteoporotic

63. Alendronate sodium And/Or its AntiOsteoporotic 121268-17-5 intermediates AND/OR

AntiRetroviral

64. Darunavir And/Or its 10.00 AntiRetroviral 169280-56-2 intermediates AND/OR

65. Zidovudine And/Or its AntiRetroviral 25442-42-6 intermediates AND/OR

AntiVirals

66. Valacyclovir hydrochloride AntiVirals 124832-31-1 And/Or its intermediates

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AND/OR

Benzodiazepines

67. Diazepam And/Or its Benzodiazepines 439-14-5 intermediates AND/OR

Chelating Agent

68. Deferasirox And/Or its Chelating Agent 1218-69-5 intermediates AND/OR

Corticosteroids

69. Prednisolone sodium Corticosteroids phosphate And/Or its 50-24-8 intermediates AND/OR

Hyperuricemia

70. Febuxostat And/Or its Hyperuricemia 160844-75-7 intermediates AND/OR

Immunosuppressant

71. Mycophenolate Mofetill And/Or Immunosuppressant 128794-94-5 its intermediates AND/OR

Iron Deficiency

72. Iron Sucrose Complex And/Or Iron Deficiency 8047-67-4 its intermediates AND/OR

Leukotriene Receptor

Antagonist

73. Montelukast Sodium And/Or its Leukotriene Receptor 142569-70-8 intermediates AND/OR Antagonist

Overactive Bladder

74. Solifenacin And/Or its Overactive Bladder 118864-75-8 intermediates AND/OR

Rheumatoid Arthritis

75. Baricitinib And/Or its 1187595-85-2 Rheumatoid Arthritis

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intermediates AND/OR

Vasoconstrictor

76. Phenylephrine And/Or its Vasoconstrictor 61-76-7 intermediates AND/OR

Vitamins

77. Folic acid And/Or its Vitamins 35011-47-3 intermediates AND/OR

78. Methylcobalamin And/Or its Vitamins 13422-55-4 intermediates AND/OR

79. (+_)3-(Carbamoyl methyl)-5- Pregabaline 181289-33-8 methyl hexanoic acid Intermediate

Group 3

Alzheimer's Disease

80. Memantine HCL And/Or its Alzheimer's Disease 941-37-7 intermediates AND/OR

Analgesic

81. Etoricoxib And/Or its Analgesic 221615-75-4 intermediates AND/OR

82. Flurbiprofen And/Or its Analgesic 5104-49-4 intermediates AND/OR

83. Gabapentin And/Or its Analgesic 64744-50-9 5.00 intermediates AND/OR

84. Lidocaine HCL And/Or its Analgesic 1131-01-7 intermediates AND/OR

AntiArrhythmias

85. Amiodarone And/Or its AntiArrhythmias 19774-82-4 intermediates AND/OR

AntiArthritis

86. Apremilast And/Or its 608141-41-9 AntiArthritis

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intermediates AND/OR

AntiAsthmatic

87. Salbutamol And/Or its AntiAsthmatic 16475-90-4 intermediates AND/OR

AntiBiotic

88. Ciprofloxacin HCL And/Or its AntiBiotic 85721-33-1 intermediates AND/OR

AntiDiabetic

89. Teneligliptin And/Or its AntiDiabetic 401566-79-8 intermediates AND/OR

AntiFungals

90. Fluconazole And/Or its AntiFungals 86404-63-9 intermediates AND/OR

91. ketoconazole And/Or its AntiFungals 67914-60-7 intermediates AND/OR

AntiHistaminic

92. Desloratidine And/Or its AntiHistaminic 31255-55-7 intermediates AND/OR

93. Levocetirizine dihydrochloride AntiHistaminic And/Or its intermediates 42137-88-2 AND/OR

AntiHypertensive

94. Bisoprolol And/Or its AntiHypertensive 177034-57-0 intermediates AND/OR

95. Ramipril And/Or its AntiHypertensive 93779-29-4 intermediates AND/OR

96. Rosuvastatin Calcium And/Or AntiHypertensive 147118-37-4 its intermediates AND/OR

AntiLipemic

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97. Niacin And/Or its intermediates AntiLipemic 59-67-6 AND/OR

98. Simvastatin And/Or its AntiLipemic 5856-77-9 intermediates AND/OR

AntiPsychotic

99. Quetiapine And/Or its AntiPsychotic 07-07-3159 intermediates AND/OR

Erectile Dysfunction

100. Tadalafil And/Or its Erectile Dysfunction 14907-27-8 intermediates AND/OR

Receptor Antagonist

101. Varenicline tartrate And/Or its 230615-51-7 intermediates AND/OR

Vertigo

102. Betahistine Dihydrochloride Vertigo 5579-84-0 And/Or its intermediates

Group 4

AntiHypertensive

103. Telmisartan And/Or its AntiHypertensive 144702-27-2 intermediates AND/OR

Proton Pump Inhibitors

104. Omeprazole And/Or its 2.50 Proton Pump Inhibitors intermediates AND/OR 86604-75-3

105. Pantoprazole sodium And/Or Proton Pump Inhibitors 97963-62-7 its intermediates

Group 5

AntiGlaucoma 1.00 106. Travoprost And/Or its 1204185-88-5 AntiGlaucoma1.00

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intermediates AND/OR

Alzheimer's Disease

107. Donepezil hydrochloride Alzheimer's Disease And/Or its intermediates 22065-85-6 AND/OR

Analgesic

108. Celecoxib And/Or its Analgesic 720-94-5 intermediates AND/OR

AntiBiotic

109. Azithromycin monohydrate AntiBiotic And/Or its intermediates 83905-01-5 AND/OR

110. Cefixime And/Or its AntiBiotic 79349-82-9 intermediates AND/OR

AntiCancer

111. Capecitabine And/Or its 161599-46-8 AntiCancer intermediates AND/OR

112. Imatinib Mesylate And/Or its AntiCancer 106261-64-7 intermediates AND/OR

AntiCoagulant

113. Apixaban And/Or its AntiCoagulant 503614-91-3 intermediates AND/OR

AntiConvulsants

114. Lacosamide And/Or its AntiConvulsants 880468-89-3 intermediates AND/OR

115. Oxcarbamazepine And/Or its AntiConvulsants 28721-09-7 intermediates AND/OR

AntiDepressant

116. Mirtazapine Hemihydrate 61337-89-1 AntiDepressant

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And/Or its intermediates AND/OR

AntiDiabetic

117. Vildagliptin And/Or its AntiDiabetic 207557-35-5 intermediates AND/OR

AntiHistaminic

118. Loratidine And/Or its AntiHistaminic 31251-41-9 intermediates AND/OR

AntiHypertensive

119. Amlodipine And/Or its AntiHypertensive 88150-62-3 intermediates AND/OR

120. Carvedilol And/Or its AntiHypertensive 1836-62-0 intermediates AND/OR

121. Clopidogrel Bisulphate And/Or AntiHypertensive 141109-19-5 its intermediates AND/OR

122. Lisinopril And/Or its AntiHypertensive 16652-71-4 intermediates AND/OR

123. Losartan potassium And/Or its AntiHypertensive 114798-26-4 intermediates AND/OR

124. Olmesartan medoxomil And/Or AntiHypertensive 80841-78-7 its intermediates AND/OR

AntiLipemic

125. Atorvastatin And/Or its AntiLipemic 125971-95-1 intermediates

Group 6

Benign Prostatic Hyperplasia

126. Silodosin And/Or its Benign Prostatic 1375180-30-5 0.15 intermediates Hyperplasia

Hormonal Therapy

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127. And/Or its Hormonal Therapy 4584-46-7 0.08 intermediates

Insomia

128. Zopiclone And/Or its Insomia 43200-81-3 11.00 intermediates

Analgesic

129. Cyclosporine And/Or its 59865-13-3 Analgesic 0.35 intermediates

AntiArrhythmias

130. Digoxin And/Or its 20830-75-5 AntiArrhythmias 0.02 intermediates

Group 7

131. R & D development 0.50 ---

Total (Group 1 to 7) 70.60

• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 13/06/2019. • Technical presentation was made by the project proponent with consultant/expert Environ during SEAC meeting dated 13/06/2019. • Committee noted that this proposal is new bulk drug and its intermediate manufacturing unit located at GIDC, Saykha. Committee asked clarification regarding product profile shown 130 products of bulk drug and its intermediates hence production plant adequacy and reason for such huge products proposed to which PP has not satisfactorily addressed about it .Committee also insisted for R and D products shall be in Kg/Month instead of MT/Month. Committee asked for waste water treatment, PP submitted simple conventional ETP without segregation of effluent hence committee insisted for revised treatment scheme with segregation of Low COD and High COD stream and proposed RO and ZLD for effluent instead of conventional ETP in addition to proposed conventional ETP. PP informed that washing effluent proposed nil and cooling blow down and boiler blow down only 0.5 KLD which is not feasible looking to proposed project hence committee insisted for revised water balance diagram with adequate quantity of washing, cooling blow down, boiler blow down generation with considering worst case scenario. Committee also asked for readdressed adequate characteristic of effluent discharge to CETP and also mentioning about inlet norms of CETP. Committee disagree with waste water treatment scheme proposed by technical experts of PP looking to the proposed bulk drug products

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profile. Committee insisted for revised air matrix and hazardous waste matrix considering revised advance effluent treatment scheme like ZLD and RO system. • After deliberation, committee asked PP to come prepared with all the details pertaining to project and defer the proposal in one of the upcoming SEAC meeting with submission of following details, 1. Revised adequate proposal for bulk drug product profile with area adequacy with mentioning about production plant machinery and its utility inventory and inventory justification with proposed products and plant size. 2. Revised product profile with mentioning of bulk drug intermediate chemical name and R & D product in Kg/Month. 3. Revised treatment scheme with segregation of Low COD and High COD stream and proposed RO and ZLD for effluent in addition to proposed conventional ETP. 4. Revised water balance diagram with adequate quantity of washing, cooling blow down, boiler blow down generation with considering worst case scenario. 5. Readdressed adequate characteristic of effluent discharge to CETP, Saykha and also mentioning about inlet norms of CETP, Saykha. 6. Revised air matrix and hazardous waste matrix considering revised advance effluent treatment scheme like ZLD and RO system for effluent. 7. Revised process gas emission stack and its APCM for each process reactor separately. 8. Technical justification regarding proposed 57 hazardous waste generation from proposed bulk drug and its intermediate sector considering Hazardous Waste ( M & H & T/M ) Rules’2016. 9. Technical justification regarding feasibility report from schedule-! Auditor regarding various hazardous waste generated from plant reuse within plant and solid waste generated from product no- 130 namely Digoxin And/Or its intermediates, reuse as fuel in boiler within plant. • PP has submitted revised proposal with curtails of production capacity with subsequent change in salient features of Water, Air and Hazardous Waste Management and this case reconsidered in SEAC meeting dated 01/10/2019. • Revised product profile of proposed project as above and revised salient features of Water, Air and Hazardous waste management as below: Sr. Particulars Details no. A A Total cost of Proposed Project 3.65 Crores (Rs. in Crores):

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B Total Plot area ( sq. meter) 5,000.00 Sq. m.

Green belt area 1,655.00 Sq. m. ( sq. meter) C Employment generation 26 Nos.

D Water i Source of Water Supply GIDC

(GIDC Bore well, Surface water, Tanker supply etc...)

Status of permission from the concern authority. In process

ii Water consumption (KLD)

Category Quantity Remarks KLD (S) Domestic 1.50

(T) Gardening 6.50

(U) Industrial

Process 43.00 Including APCM Washing 5.00

Boiler 5.00

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Cooling 5.00

Others 0.00

Industrial Total 58.00

Total (A + B + C) 66.00

7) Total water requirement for the project: 66.00 KLD 8) Quantity to be recycled : 0.00 KLD 9) Total fresh water requirement: 66.00 KLD

iii Waste water generation (KLD)

Category Waste water Remarks KLD (M) Domestic 1.00 ---

(N) Industrial

Process 54.00 --- Washing 4.00 --- Boiler 0.50 --- Cooling 0.50 --- Others 0.00 --- Total Industrial waste water 59.00 --- Total [A + B] 60.00 ---

- iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.

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‹ Proposed ETP – 100 KLD ‹ Proposed MEE – 55 KLD Treatment scheme including segregation at source. ‹ Wastewater generation from the proposed production activity will be treated in MEE and ETP having capacity of 55 KLD and 100 KLD respectively. Then send to the CETP, Saykha for further treatment. Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ Assurance letter from GIDC, vide Letter no. GIDC/BRH/ DEE(DRG)/259 dated 1 st May, 2019. Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Wastewater generation from the proposed production activity will be treated in MEE and ETP having capacity of 55 KLD and 100 KLD respectively. Then send to the CETP, Saykha for further treatment. v Mode of Disposal & Final meeting point

Domestic: Sewage generated during operation phase shall be treated in soak pit/septic system. Industrial: Wastewater generation from the proposed production activity will be treated in MEE and ETP having capacity of 55 KLD and 100 KLD respectively. Then send to the CETP Saykha for further treatment. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ Assurance letter from GIDC, vide Letter no. GIDC/BRH/ DEE(DRG)/259 dated 1 st May, 2019. Membership of Common facility (CF) (For waste water treatment) GIDC Letter no. GIDC/BRH/DEE(DRG)/259 dated 1 st May,2019. vii Simplified water balance diagram with reuse / recycle of waste water

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viii Reuse/Recycle details (KLD) Total reuse 0.00 KLD Source of waste Application Characteristics of Remarks water for reuse area with waste water to be regarding with quantity in quantity in reused (COD, BOD, feasibility KLD (From KLD (Where it TDS etc.) to reuse i.e. where it is is used)

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coming) ------

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.

- Stack Quantit Type of Air Pollution Source of Sr. Height Type of y of emissions Control emission No. (meter Fuel Fuel i.e. Air Measures With Capacity ) MT/Day Pollutants (APCM)

Coal 3.0 Multi Cyclone Boiler – 600 kg/Hr – 1. 30 m OR MT/Day Separator, Bag 1 No. Agro OR Filter and briquette 3.4 PM < 150 Scrubber s MT/day 3 Thermic Fluid mg/Nm Multi Cyclone OR OR SO 2< 100 Separator, Bag 2. Heater – 2 lacs 30 m 3 Natural 400 m Kcal/Hr. ppm Filter and Gas /day NOx< 50 ppm Scrubber

32 Stack Height, 3. D.G. Set – 200 KVA 5 m HSD Lit/hr. Acoustic Enclosure

Steam requirement :- Maximum Steam Required Sr. No. Group/MEE (kg/hr) 1. Group 1 230 2. Group 2 3. Group 3 142 4. Group 4 5. Group 5 123 6. Group 6 102 Total (Group 1 to 6) 597

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7. MEE 800 Total Steam Requirement 1,397 We have proposed Boiler 600 kg/hr and Thermic fluid heater 2 lacs Kcal/hr which is sufficient as per above said steam requirement. - ii Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.)

- Stack/Vent Air Pollution Sr. Specific Source of emission Type of Height Control Measures No. (Name of the Product & Process) emission (meter) (APCM) Scrubber 1. (2-(Diethylamino)ethyl Chloride Hydrochloride) Scrubber 2. (Lasamide) SO 2 Scrubber 3. (Sildenafil Citrate And/Or its intermediates) Scrubber 4. (Tadalafil And/Or its intermediates) Water Scrubber Scrubber followed by Alkali 5. 20 (Lasamide) Scrubber Scrubber 6. (Clozapine And/Or its intermediates) Scrubber 7. (Sildenafil Citrate And/Or its HCl intermediates) Scrubber 8. (Bisoprolol And/Or its intermediates) Scrubber 9. (Tadalafil And/Or its intermediates)

10. Scrubber NH 3 Water Scrubber

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(Naproxen And/Or its intermediates) followed by Acid Scrubber Scrubber 11. (Pregabalin And/Or its intermediates) Scrubber 12. (Zidovudine and/or Its Intermediates) Scrubber 13. (Atorvastatin And/Or its intermediates) Scrubber 14. (Niacin And/Or its intermediates) Scrubber 15. (Simvastatin And/Or its intermediates) Scrubber 16. (Omeprazole And/Or its intermediates) Scrubber 17. (2-Diethylaminoethanethiol hydrochloride) - iii Fugitive emission details with its mitigation measures: As below: ‹ Process plant building will open on all sides to provide adequate ventilation in the work areas. ‹ Third party ambient air monitoring will be regularly carried out for the proposed expansion. ‹ Adequate sprinkling system and firefighting arrangements will be provided. ‹ Storage tanks of raw materials and finished products will be provided with dyke walls to hold any unforeseen spillage/leakage. ‹ Unit will be developed road for prevention of dust during vehicular movement. ‹ Use of vehicles with PUC will be made compulsory for transportation vehicles entering the premises. ‹ Adequate greenbelt area will be developed to minimize the impact of fugitive dust due to vehicular movement.

F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i

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Specific Source of Category Type/Name generation and Sr. of Quantity Management of (Name of the Schedule as No. Hazardous (MT/Annum) HW Activity, Product per HW waste etc.) Rules.

Process Process (Maximum residue from Group no. 1 – Product - Sitagliptin And/Or its intermediates, Maximum from Group no. 2 – Product - Valacyclovir hydrochloride And/Or its intermediates , Maximum from Group no. 3 – Collection, Product - Varenicline Storage and send 1. 28.1 (Sch. I) 1,389.71 tartrate And/Or its to Incinerator for intermediates, further treatment. Maximum from Group no. 4 – Product - Omeprazole And/Or its intermediates, Maximum from Group no. 5 – Product -Amlodipine And/Or its intermediates, From Group no. 6 – Product - Tamoxifen

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And/Or its intermediates , Zopiclone And/Or its intermediates, Cyclosporine And/Or its intermediates)

Distillation Process (Maximum residue from Group no. 1 – Product - Aripiprazole And/Or its intermediates, Maximum from Group no. 2 - Product - Valacyclovir hydrochloride And/Or its intermediates, Maximum from Group no. 3 – Collection, Product - Simvastatin Storage, 2. And/Or its 20.3 (Sch. I) 1,747.34 Transportation & intermediates, send to CHWIF or Maximum from co-processing. Group no. 4 – Only from product - Telmisartan And/Or its intermediates, Maximum from Group no. 5 – Product - Mirtazapine Hemihydrate And/Or its intermediates, From Group no. 6 – Product -

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Cyclosporine And/Or its intermediates, Digoxin And/Or its intermediates)

Spent carbon Process (Maximum from Group no. 1 – Product – Levetiracetam And/Or its intermediates, Maximum from Group no. 2 – Product - Solifenacin And/Or its intermediates, Maximum from Collection, Group no. 3 – Storage, Product - Tadalafil Transportation & 3. 28.3 (Sch. I) 516.20 And/Or its send to CHWIF or intermediates , co-processing. Maximum from Group no. 5 – Product - Vildagliptin And/Or its intermediates, From Group no. 6 – Product - Tamoxifen And/Or its intermediates , Zopiclone And/Or its intermediates , Digoxin And/Or its

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intermediates)

ETP Sludge Collection, Storage, 4. ETP 35.3 (Sch. I) 300.00 Transportation & send to TSDF site.

Used Oil Collection, Storage, Transportation, Disposal by 250.00 5. Machinery 5.1 (Sch. I) selling to GPCB/ kl/Month MoEF approved recycler/ reuse as lubricant within premises.

Discarded Collection, Container/ Storage, Raw Material Storage barrels/ liners Transportation, area and Finished 750.00 6. 33.1 (Sch. I) Decontamination, product packing Nos./Month Disposal by send Material to the GPCB authorized dealer.

MEE Salt Collection, Storage, 7. ATFD 35.3 (Sch. I) 1,460.00 Transportation & send to TSDF site.

Allumina Collection, Process (Group no. 6 Powder Storage, - only from product - 8. 28.1 (Sch. I) 1.08 Transportation & Digoxin And/Or its send to TSDF intermediates) site.

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Lanata leaves Process (Group no. 6 Collection, - only from product - Storage and send 9. 28.1 (Sch. I) 175.70 Digoxin And/Or its to Incinerator for intermediates) further treatment.

Spent Solvent Process (Group no. 1 – Only from Product - N,N Dimethyl Form amide Diemthyl Acetal, Maximum from Group no. 3 – Product - Ramipril Collection, And/Or its Storage and Sold intermediates , 1,704.00 to actual users Group no. 5 – Only 10. 20.2 (Sch. I) having from Product - permission of Azithromycin Rule – 9 from monohydrate And/Or SPCB/CPCB. its intermediates , Group no. 6 – Only from Product - Digoxin And/Or its intermediates)

250.00 Stripper KL/Annum

Ammonium Collection, Sulphate Storage and Sold to actual users 11. Scrubbing Media 35.1 (Sch. I) 180.00 having permission of Rule – 9 from SPCB/CPCB.

12. Ammonium Scrubbing Media 35.1 (Sch. I) 14.93 Collection,

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Chloride Storage and Sold to actual users having permission of Rule – 9 from SPCB/CPCB.

Sodium Collection, sulphate Storage and Sold to actual users Scrubbing Media 35.1 (Sch. I) 30.00 having permission of Rule – 9 from SPCB/CPCB.

Collection, Storage, reused as raw material (Product - Levetiracetam Process (Maximum And/Or its 13. from Group no. 1 – intermediates, Product - Escitalopram Levetiracetam oxalate And/Or its And/Or its intermediates, 28.1 (Sch. I) 1,202.00 intermediates, Group Darunavir And/Or no. 3 - only from its intermediates, product - Quetiapine Solifenacin And/Or its And/Or its intermediates) intermediates, Apremilast And/Or its intermediates, Desloratidine And/Or its

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intermediates, Quetiapine And/Or its intermediates, Capecitabine And/Or its intermediates, Tamoxifen And/Or its intermediates)

Hydrogen Collection, Chloride Storage and Sold (30%) to actual users Scrubbing Media 35.1 (Sch. I) 38.40 having permission of Rule – 9 from SPCB/CPCB. 14. Collection, Process (Maximum Storage, reused from Group no. 1 – as raw material Product - Bis(2- 28.1 (Sch. I) 327.60 (Product - 4- chloroethyl)amine Methyl Cathechol hydrochloride) Diacetic Acid Dimethyl Ester).

Aluminium Collection, hydroxide Storage and Sold Process (Only from to actual users 15. Group no. 1 – 28.1 (Sch. I) 645.80 having Product - Guanidine) permission of Rule – 9 from SPCB/CPCB.

16. Potassium Process (Group no. 1 28.1 (Sch. I) 38.96 Collection,

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sulphate - only from product - Storage and Sold Trimethoprim And/Or to actual users its intermediates) having permission of Rule – 9 from SPCB/CPCB.

Boric acid Collection, Process (Group no. 2 Storage and Sold - only from product - to actual users 17. Phenylephrine 28.1 (Sch. I) 16.74 having And/Or its permission of intermediates) Rule – 9 from SPCB/CPCB.

Triphenyl Collection, Carbinal Storage and Sold Process (Group no. 1 to actual users - only from product - 18. 28.1 (Sch. I) 180.00 having Zidovudine And/Or its permission of intermediates) Rule – 9 from SPCB/CPCB.

Piperazine Collection, Hydrochloride Process (Group no. 3 Storage and Sold - only from product - to actual users 19. Ciprofloxacin HCL 28.1 (Sch. I) 24.80 having And/Or its permission of intermediates) Rule – 9 from SPCB/CPCB.

Tert. Butyl Collection, Process (Group no. 1 alcohol Storage and Sold - only from product 20. 28.1 (Sch. I) 90.72 to actual users Saxagliptin And/Or its having intermediates) permission of

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Rule – 9 from SPCB/CPCB.

P - Toluene Collection, Sulfonic acid Process (Group no. 5 Storage and Sold - only from product - to actual users 21. Clopidogrel 28.1 (Sch. I) 5.11 having Bisulphate And/Or its permission of intermediates) Rule – 9 from SPCB/CPCB.

Sulphuric acid Collection, Storage, reused Process (Maximum as raw material from Group no. 1 – (Product 2 Bromo 22. Product - 28.1 (Sch. I) 242.00 4-5- Dimethoxy Trimethoprim And/Or Benzyl Bromide, its intermediates) 2,3,4 Bis -o-(1 methyl)-B-D- Fructopyranose).

Sodium Collection, Nitrate Storage, reused Process (Group no. 1 as raw material - only from product - 23. 28.1 (Sch. I) 115.90 (Product - 4-Iso Trimethoprim And/Or Propyl Catechol, its intermediates) Apixaban And/Or its intermediates).

Potassium Collection, Carbonate Storage, reused Process (Group no. 1 as raw material - only from product - 24. 28.1 (Sch. I) 343.80 (Product - 6- Lansoprazole And/Or Chloro-5(2-Chlor its intermediates) Ethyl) Oxindole, Doxofylline

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And/Or its intermediates)

Sodium Collection, Chloride Storage, reused as raw material (Product -. Topiramate And/Or its intermediates, Sitagliptin And/Or its intermediates, Process (Maximum Paroxetine HCl from Group no. 1 – Hemihydrate Product - 2- And/Or its Diethylaminoethanet intermediates, hiol , Group no. 2 - Darunavir And/Or Only from product - its intermediates, Phenylephrine 25. 28.1 (Sch. I) 427.00 Zidovudine And/Or its And/Or its intermediates, intermediates, Maximum from Fluconazole Group no. 3 – And/Or its Product - intermediates, Fluconazole And/Or Capecitabine its intermediates) And/Or its intermediates, Vildagliptin And/Or its intermediates, Carvedilol And/Or its intermediates, Lisinopril And/Or its intermediates).

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Zinc Chloride Collection, Storage, reused Process (Maximum as raw material 26. from Group no. 1 - 28.1 (Sch. I) 594.00 (Product - 6- Product - Sesamol) Chloro-5(2-Chlor Ethyl) Oxindole, Sesamol)

Aluminium Collection, Chloride Storage, reused Process (Only from as raw material Group no. 1 - Product (Product - 2- 27. - 2-Methyl-4,5- 28.1 (Sch. I) 475.00 Methyl-4,5- Dimethoxybenzoic Dimethoxybenzoi Acid) c Acid , Guanidine)

Sodium Collection, Hydroxide Storage, reused as raw material (Product 4-Iso Propyl Catechol, 2- Diethylaminoetha Process (Maximum nethiol ,Etodolac from Group no. 1 – And/Or its 28. product - 28.1 (Sch. I) 60.00 intermediates, Trimethoprim And/Or Naproxen And/Or its intermediates) its intermediates, Pregabalin And/Or its intermediates, Trimethoprim And/Or its intermediates).

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Sodium Collection, Acetate Storage, reused as raw material 9.26 (Product - Apixaban And/Or Process (Group no. 1 its intermediates). - only from product - 29. 28.1 (Sch. I) Collection, Naproxen And/Or its Storage and Sold intermediates) to actual users 330.50 having permission of Rule – 9 from SPCB/CPCB.

Ammonium Collection, acetate Storage, reused as raw material (Product - Lansoprazole 187.85 And/Or its intermediates, Process (Group no. 1 Omeprazole - only from product - 30. 28.1 (Sch. I) And/Or its Trimethoprim And/Or intermediates). its intermediates) Collection, Storage and Sold to actual users 74.23 having permission of Rule – 9 from SPCB/CPCB

Sodium Process (Only from Collection, 31. 28.1 (Sch. I) 24.90 Bisulfate Group no. 1 – Storage, reused

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Product - 2-Methyl- as raw material 4,5- (Product - Dimethoxybenzoic Bisoprolol And/Or Acid) its intermediates, Digoxin And/Or its intermediates)

Collection, Storage and Sold to actual users 510.10 having permission of Rule – 9 from SPCB/CPCB.

Sodium Collection, Bromide Storage, reused Process (Maximum as raw material 1.20 from Group no. 1 – (Product - Product - 4-Iso Silodosin And/Or Propyl Catechol , its intermediates) 32. Group no. 2 - Only 28.1 (Sch. I) Collection, from Product - Storage and Sold Phenylephrine to actual users And/Or its 701.80 having intermediates) permission of Rule – 9 from SPCB/CPCB.

- ii Membership details of TSDF, CHWIF etc. BEIL, Dahej. (For HW management) iii Details of Non-Hazardous waste & its disposal NA

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(MSW and others)

G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)

Sr. Quantity (kg/Batch) Recovery Name of Product Name of Solvent No. In Out (%)

2 Bromo 4-5- Dimethoxy 1. Methanol 0.20 0.198 99.00 Benzyl Bromide

MDC 1.06 1.044 98.86

HBr 0.45 0.441 98.00

Cyclohexane 0.45 0.445 98.89

2,3,4 Bis -o-(1 methyl)-B- 2. Acetone 1,000.00 981.00 98.10 D-Fructopyranose

Toluene 300.00 295.00 98.33

2-Methyl-4,5- 3. Toluene 1,500.00 1,472.00 98.13 Dimethoxybenzoic Acid

MDC 1,500.00 1,473.00 98.20

4. 3-Methoxy Phenol Toluene 1,000.00 981.00 98.10

5. 4-Iso Propyl Catechol MDC 1,000.00 983.00 98.30

CuSO4 1,000.00 982.00 98.20

N-Butanol 1,400.00 1,375.00 98.21

4-Methyl Cathechol

6. Diacetic Acid Dimethyl Methanol 2,500.00 98.20 2,455.00 Ester

Toluene 1,000.00 981.00 98.10

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7. 6 chloro hexanol Toluene 14,681.50 14,400.00 98.08

6-Chloro-5(2-Chlor Ethyl) 8. DMSO 1,000.00 981.00 98.10 Oxindole

MDC 700.00 687.00 98.14

Methanol 1,000.00 982.00 98.20

Acetic acid 600.00 589.00 98.17

Benzaldehyde Dimethyl 9. Methanol 700.00 687.00 98.14 Acetal

Bis(2-chloroethyl)amine 10. EDC 0.00188 0.00185 98.40 hydrochloride

11. CetylPyridinium Chloride Pyridine 0.000464 0.000455 98.06

Methyl Ethyl Ketone 0.0040 0.0039 98.00

Acetone 0.0040 0.0039 98.00

12. Sesamol MDC 800.00 785.00 98.13

Toluene 1,650.00 1,620.00 98.18

Methanol 300.00 295.00 98.33

Formic acid 620.00 610.00 98.38

Dimethyl fumarate 13. Methanol 7.00 6.87 98.14 And/Or its intermediates

Etodolac And/Or its 14. Methanol 2,000.00 1,963.00 98.15 intermediates

Pregabalin And/Or its 15. n-Hexane 450.00 441.10 98.02 intermediates

Chloroform 5,100.00 5,005.00 98.14

Diethylmalonate 50.00 49.00 98.00

Ivabradine Hcl And/Or its 16. Methanol 0.21 0.21 98.10 intermediates

DMSO 0.533 0.531 99.62

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Chloramphenicol And/Or 17. Methanol 1,300.00 98.15 its intermediates 1,276.00

Erythromycin And/Or its 18. MDC 9.02 8.85 98.07 intermediates

Trimethoprim And/Or its 19. Methanol 700.00 687.50 98.21 intermediates

Dimethyl Sulfoxide 150.00 147.00 98.00

Rivaroxaban And/Or its 20. THF 9.07 98.02 intermediates 8.89

Ethanol 9.67 98.04 9.48

Warfarin And/Or its 21. Toluene 20.00 19.61 98.05 intermediates

Carbamazepine And/Or 22. Methanol 150.00 147.50 98.33 its intermediates

Levetiracetam And/Or its 23. Ethyl acetate 16.16 15.87 98.21 intermediates

Dichloromethane 38.75 38.10 98.32

Topiramate And/Or its 24. Acetone 2,100.00 2,060.00 98.10 intermediates

n-Hexane 1,370.00 1,344.10 98.11

Toluene 1,600.00 1,570.00 98.13

Ethyl acetate 1,610.00 1,580.00 98.14

Isopropyl alcohol 1,415.00 1,389.00 98.16

Desvenlafexine And/Or 25. DCM 8.50 8.34 98.11 its intermediates

DMF 5.00 4.91 98.2

Methanol 2.05 2.01 98.04

Acetone 5.652 5.54 98.01

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Ethanol 7.81 7.67 98.20

Venlafaxine 26. hydrochloride And/Or its Ethyl acetate 328.00 328.00 100.00 intermediates

Glipizide And/Or its 27. Methanol 246.00 242.10 98.41 intermediates

Acetone 100.00 98.00 98.00

Saxagliptin And/Or its 28. DMF 625.00 613.00 98.08 intermediates

Isopropyl alcohol 350.00 343.00 98.00 (IPA)

Methylene 470.00 461.00 98.09 dichloride(MDC)

Ethyl acetate 620.00 607.90 98.05

Sitagliptin And/Or its 29. MDC 250.00 245.10 98.04 intermediates

IPA 200.00 196.10 98.05

Methanol 350.00 343.10 98.03

Voglibose And/Or its 30. DMSO 0.0050 0.0049 98.00 intermediates

Diltiazem hydrochloride 31. Methanol 400.00 392.000 98.00 And/Or its intermediates

Toluene 750.00 737.400 98.32

Ethylacetate 500.00 490.000 98.00

IPA 93.00 92.60 99.57

Irbesartan And/Or its 32. o-Xylene 2,500.000 2,450.000 98.00 intermediates

Toluene 3,800.000 3,729.000 98.13

Isopropyl Alcohol 1,600.000 1,570.000 98.13

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Ethyl acetate 450.000 442.000 98.22

Tributyltin Chloride 220.000 216.000 98.18

Valsartan And/Or its 33. Methanol 17.03 16.70 98.06 intermediates

Toluene 2.48 2.44 98.39

MDC 67.11 65.90 98.20

Acetonitrile 9.45 9.28 98.20

O-Xylene 25.74 25.30 98.29

Hexane 16.70 16.40 98.20

Acetone 12.91 12.69 98.30

EA 21.06 20.70 98.29

Olanzapine And/Or its 34. Dimethysulphoxide 1500.00 1470.000 98.00 intermediates

EA 1600.00 1570.000 98.13

TIOTROPIUM BROMIDE 35. Toluene 105.00 103.00 98.10 and/or Its intermediates

Acetonitrile 260.00 255.00 98.08

Ethanol 280.00 275.00 98.21

Zidovudine and/or Its 36. Toluene 4800.00 4752.000 99.00 Intermediates

EA 500.00 490.000 98.00

Diazepam and/or Its 37. Methanol 629.20 620.00 98.54 Intermediates

Toluene 520.20 510.00 98.04

Deferasirox And/Or its 38. Toluene 3.18 3.13 98.43 intermediates

Methanol 0.80 0.79 98.75

Ethanol 18.08 17.80 98.45

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Prednisolone Sodium 39. Phosphate And/Or its Tetra Hydro Furan 435.00 427.00 98.16 intermediates

Acetone 175.00 172.00 98.29

Febuxostat And/Or its 40. IPA 3.95 3.88 98.23 intermediates

Mycophenolate Mofetill 41. Xylene 1400.00 1375.00 98.21 And/Or its intermediates

Isobutyl Acetate 600.00 589.00 98.17

Montelukast Sodium 42. Toluene 300.00 295.00 98.33 And/Or its intermediates

Methanol 400.00 393.00 98.25

Folic acid And/Or its 43. Acetonitrile 1400.00 1372.00 98.00 intermediates

EA 1750.00 1718.00 98.17

Donepezil hydrochloride 44. Methanol 438.00 430.10 98.20 And/Or its intermediates

Toluene 133.00 130.50 98.12

DMF 46.00 45.10 98.04

IPA 165.00 163.00 98.79

Celecoxib And/Or its 45. Toluene 24.00 23.60 98.33 intermediates

IPA 2.59 2.54 98.03

Cyclosporine And/Or its 46. Toluene 4,666.67 4,578.33 98.11 intermediates

Acetone 33.33 32.70 98.10

Methanol 33.33 32.73 98.20

Cyclohexane 33.33 32.70 98.10

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Lidocaine HCL And/Or 47. Acetone 129.88 128.73 99.11 its intermediates

Toluene 77.30 75.86 98.14

Digoxin And/Or its 48. Chloroform 10,057.50 9,857.50 98.01 intermediates

Isopropylether 39.09 38.35 98.11

Salbutamol And/Or its 49. IPA 180.00 178.00 98.89 intermediates

Ethy Acetate 105.00 103.00 98.10

Retarder 105.00 103.00 98.10

Toluene 12.00 11.80 98.33

Methanol 696.00 683.00 98.13

Acetone 300.00 294.50 98.17

Cefixime And/Or its 50. MDC 133.82 131.18 98.02 intermediates

MeOH 373.16 367.78 98.56

TPPO 20.12 19.74 98.10

DMF 36.09 35.38 98.03

NBA 388.24 384.12 98.94

Phenol 92.65 90.88 98.10

Acetone 47.06 46.18 98.13

NaBr 8.64 8.47 98.06

Ciprofloxacin HCL 51. N-Butanol 333.33 327.50 98.25 And/Or its intermediates

Apixaban And/Or its 52. Ethyl acetate 157.14 154.21 98.14 intermediates

Tetrahydrofuran 75.00 73.61 98.14

Dichloroethane 71.43 70.07 98.10

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Morophine 57.14 56.07 98.13

Toluene 85.71 84.07 98.08

Lacosamide And/Or its 53. Tetrahydrofuran 1,411.90 1,385.00 98.09 intermediates

Methyl Tertiary Butyl 1028.64 1020.00 99.16 Ether

Methanol 1,550.00 1,520.00 98.06

Toluene 1159.28 1152.00 99.37

Methylene chloride 3,608.60 3,550.00 98.38

Acetone 1,147.00 1,125.00 98.08

ethyl acetate 220.50 216.50 98.19

Oxcarbamazepine 54. Toluene 21.19 20.80 98.16 And/Or its intermediates

N-Propanol 13.17 12.95 98.33

Acetone 2.23 2.19 98.21

Mirtazapine And/Or its 55. Ethyl acetate 1,162.70 1,142.86 98.29 intermediates

Teneligliptin And/Or its 56. EDC 862.07 845.98 98.13 intermediates

MIBK 275.86 271.26 98.33

Vildagliptin And/Or its 57. Methanol 35.48 34.8 98.083 intermediates

Methylene Chloride 267.37 262.5 98.17 (MDC)

Ethyl acetate 24.3 23.85 98.14

IPA 2.8 2.75 98.21

Fluconazole And/Or its 58. Toluene 10.52 10.32 98.10 intermediates

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Hexane 1.40 1.38 98.36

IPA 10.52 10.32 98.10

MDC 14.73 14.45 98.11

Desloratidine And/Or its 59. Ethyl acetate 450.00 441.00 98.00 intermediates

Di Isopropyl ether 610.80 598.90 98.05

Levocetirizine 60. dihydrochloride And/Or Toluene 555.56 546.30 98.33 its intermediates

Cyclohexane 601.85 592.59 98.46

MDC 1,481.48 1,452.31 98.03

Ethyl acetate 1,851.85 1,818.52 98.20

Acetone 1,250.00 1,226.85 98.15

Carvedilol And/Or its 61. EDC 6.37 6.24 98.02 intermediates

MeOH 19.01 18.70 98.35

Chloroform 37.76 37.10 98.25

Acetone 22.68 22.25 98.11

Acetic acid 12.27 12.05 98.18

DNS 7.00 6.88 98.29

IPA 7.46 7.32 98.12

Ethyl acetate 13.26 13.00 98.07

Lisinopril And/Or its 62. MDC 335.00 329.00 98.21 intermediates

MTBE 35.00 34.40 98.29

Ethyl alcohol 180.00 178.00 98.89

Ethanol 443.70 438.50 98.83

63. Losartan potassium Methanol 34.13 33.50 98.15

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And/Or its intermediates

Acetonitrile 2.40 2.36 98.33

Olmesartan medoxomil 64. Acetone 276.22 272.73 98.73 And/Or its intermediates

Ramipril And/Or its 65. Methyldichloride 239.50 235.00 98.12 intermediates

DIPE 44.10 98.00 45.00

Diethyl ether 100.70 98.90 98.21

Rosuvastatin Calcium 66. Acetone 556.52 549.28 98.70 And/Or its intermediates

Toluene 1375.65 1356.52 98.61

Methanol 847.25 840.58 99.21

MIBK 333.62 331.88 99.48

EA 264.06 262.32 99.34

IPA 262.03 260.87 99.56

BHT 65.22 65.22 100.00

Niacin And/Or its 67. Toluene 30.95 30.36 98.08 intermediates

Quetiapine And/Or its 68. Toluene 1251.09 1227.91 98.15 intermediates

DCM 2739.30 2692.33 98.29

Ethanol 1850.12 1813.97 98.05

Tadalafil And/Or its 69. Methanol 533.20 526.60 98.76 intermediates

IPA 266.60 263.30 98.76

Acetic Acid 333.30 330.00 99.01

70. Pantoprazole sodium Acetone 444.44 435.56 98.00

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And/Or its intermediates

IPA 833.33 816.67 98.00

Zopiclone And/Or its 71. IPA 444.60 435.91 98.05 intermediates

MDC 2292.25 2248.64 98.10

EA 2281.50 2238.25 98.10

Varenicline And/Or its 72. Methanol 80.00 78.55 98.19 intermediates

n-Hexane 25.60 25.15 98.24

MDC 28.00 27.50 98.21

Betahistine 73. Dihydrochloride And/Or Toluene 2307.69 2294.87 99.44 its intermediates

IPA 1666.67 1639.74 98.38

Capecitabine And/Or its 74. Dichloromethane 347.60 341.00 98.10 intermediates

Pyridine 1,966.00 1,930.00 98.17

n-pentyl 1,914.00 1,880.00 98.22 chloroformate

Methanol 16.72 98.39 16.45

Imatinib Mesylate And/Or 75. Pyridine 160.00 156.90 98.06 its intermediates

DiChloro Methane 38.00 37.27 98.08

Methanol 2.00 1.96 98.00

Ethanol 3.60 3.53 98.06

Iguratimod And/Or its 76. Dimethyl formamide 2.22 2.20 99.09 intermediates

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Amoxicillin And/Or its 77. Enzyme 10.00 9.85 98.50 intermediates

Sr. Quantity (kg/day) Recovery Name of Product Name of Solvent No. In Out (%)

Naproxen And/Or its 1. Toluene 0.0032 0.0031 98.025 intermediates

Naftopidil And/Or its 2. Methanol 1.52 1.50 98.14 intermediates

Ethyl acetate 1.83 1.80 98.15

Doxofylline And/Or its 3. Methanol 8,750.00 8,586.00 98.13 intermediates

DMF 4,141.80 3,628.80 87.61

Toluene 3,270.00 3,210.20 98.17

Dabigatran And/Or its 4. Ethanol 80.00 78.40 98.00 intermediates

Acetone 40.00 39.21 98.03

Gliclazide And/Or its 5. DMF 0.00074 0.00073 98.65 intermediates

Toluene 0.000294 0.000289 98.30

Metformin Hydrochloride 6. Isopropyl alcohol 2,400.00 2,352.00 98.00 And/Or its intermediates

Methanol 1,650.00 1,618.00 98.06

Dimethylformamide 1,800.00 1,764.00 98.00 (DMF)

Metoprolol Succinate 7. Toluene 400.00 392.00 98.00 And/Or its intermediates

Acetone 1,500.00 1,477.50 98.50

Perindopril And/Or its 8. Toluene 665.00 652.00 98.05 intermediates

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EA 13795.00 13530.00 98.08

Ethanol 2925.00 2870.00 98.12

Fenofibrate And/Or its 9. Acetone 77.34 75.95 98.20 intermediates

Chloroform 27.77 27.25 98.15

IPA 101.39 99.50 98.14

Toluene 450.00 441.50 98.11

Aripiprazole And/Or its 10. Toluene 1162.5 1140 98.06 intermediates

Methanol 135 132.75 98.33

IPA 687.5 675.2 98.21

Chloroform 400 392 98.00

MDC 612.5 600.45 98.03

Clozapine And/Or its 11. DMF 120.00 117.80 98.17 intermediates

Ethanol 1032.00 1017.80 98.62

Toluene 628.00 616.10 98.11

Anisole 55.00 54.00 98.18

IPA 165.00 162.40 98.42

Escitalopram oxalate 12. Acetonitrile 220.00 215.80 98.09 And/Or its intermediates

Toluene 80.00 78.50 98.13

EA 50.00 49.00 98.00

Sildenafil Citrate And/Or 13. Toluene 800.00 785.000 98.13 its intermediates

MDC 1550.00 1520.000 98.06

Methanol 1050.00 1029.000 98.00

Acetone 500.00 490.000 98.00

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Esomeprazole 14. magnesium And/Or its Acetone 100.00 98.10 98.10 intermediates

Methanol 62.50 61.25 98.00

MDC 120.00 118.05 98.38

Toluene 90.00 88.20 98.00

Lansoprazole And/Or its 15. Methanol 1351.60 1325.00 98.03 intermediates

Diisopropyl ether 371.65 365.00 98.21

Ethyl acetate 3051.75 3000.00 98.30

Acetone 7820.60 7780.45 99.49

Ethanol 1252.80 1252.80 100.00

Citalopram HBr And/Or 16. Acetic Acid 500.00 490.00 98.00 its intermediates

Acetonitrile 1000.00 982.60 98.26

Diisopropylether 1100.00 1079.90 98.17

IPA 550.00 540.00 98.18

THF 750.00 735.00 98.00

Toluene 2000.00 1969.80 98.49

Paroxetine HCl 17. Hemihydrate And/Or its EA 2254.30 2210.20 98.04 intermediates

Propan-2-ol 1170.00 1148.20 98.14

Heptane 1860.00 1824.60 98.10

Toluene 8935.00 8768.30 98.13

THF 145.00 142.50 98.28

Acetone 4865.00 4780.40 98.26

MDC 3255.00 3194.80 98.15

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IPA 3,160.00 3,103.20 98.20

Sertraline And/Or its 18. MDC 500.000 493.700 98.740 intermediates

Methanol 85.000 83.600 98.353

IPA 900.000 888.900 98.767

Alendronate Sodium 19. Methanol 375.00 368.000 98.13 and/or Its Intermediates

Darunavir Ethanolate 20. Ethyl Acetate 560.00 550.00 98.21 and/or Its Intermediates

Tetrahydofuran 150.00 147.00 98.00

MDC 640.00 630.00 98.44

Cyclohexane 450.00 443.30 98.51

Valacyclovir HCl and/or 21. Dimethyformamide 600.00 589.00 98.17 Its Intermediates

Methanol 1915.00 1878.00 98.07

Acetone 1330.00 1304.00 98.05

Solifenacin Succinate 22. Methanol 6.00 5.890 98.17 And/Or its intermediates

Toluene 15.40 15.120 98.18

Pyridine 0.05 0.053 98.15

THF 3.00 2.940 98.00

IPA 8.40 8.240 98.10

(+_)3-(Carbamoyl 23. methyl)-5-methyl Toluene 800.00 785.00 98.13 hexanoic acid

Memantine HCL And/Or 24. Formic acid 150.00 147.20 98.13 its intermediates

Methanol 150.00 147.10 98.07

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Etoricoxib And/Or its 25. Methanol 25.00 24.55 98.20 intermediates

Gabapentin And/Or its 26. Methylene dichloride 3,950.00 3,875.00 98.10 intermediates

Acetone 750.00 735.00 98.00

Methylene Dichloride 135.00 132.50 98.15

Acetone 1,035.00 1,015.00 98.07

Methanol 1,810.00 1,775.00 98.07

Methylene Dichloride 1,740.00 1,706.00 98.05

Amiodarone And/Or its 27. Toluene 600.00 589.00 98.17 intermediates

IPA 859.20 842.30 98.03

Apremilast And/Or its 28. Acetic acid 875.00 859.00 98.17 intermediates

Ethyl acetate 1,000.00 981.00 98.10

n- Hexane 250.00 245.50 98.20

Ethanol 350.00 343.50 98.14

Azithromycin 29. monohydrate And/Or its MDC 5,373.50 5,275.00 98.17 intermediates

Acetone 1,597.00 1,567.50 98.15

DCM 2,139.00 2,100.00 98.18

Methanol 8,315.50 8,175.00 98.31

ketoconazole And/Or its 30. Methanol 550.00 540.00 98.18 intermediates

Ethyl acetate 4,345.00 4,260.00 98.04

Acetone 1,970.00 1,933.00 98.12

Dimethyl Sulfoxide 815.00 800.00 98.16

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Loratidine And/Or its Xylene 31. 50.00 49.10 98.20 intermediates

Tetrahydrofuran(THF) 35.00 34.40 98.29

Acetonitrile 50.00 49.10 98.20

Amlodipine And/Or its 32. Toluene 8,401.30 8,250.00 98.20 intermediates

Methanol 345.90 340.00 98.29

Cyclohexane 10,088.10 9,890.00 98.04

Ethyl acetate 2,920.20 2,890.00 98.97

Acetic acid 13,630.90 13,400.00 98.31

Bisoprolol And/Or its 33. Toluene 1,500.00 1,471.00 98.07 intermediates

Methanol 2,000.00 1,962.00 98.10

Acetone 3,000.00 2,945.00 98.17

Clopidogrel Bisulphate 34. MDC 310.00 303.80 98.00 And/Or its intermediates

EA 165.00 161.80 98.06

Methanol 60.00 58.80 98.00

Telmisartan And/Or its 35. Methanol 3,337.70 3,272.50 98.05 intermediates

Dimethyl formamide 969.60 952.00 98.18

Acetone 295.10 290.00 98.27

Acetic acid 470.60 462.00 98.17

Atorvastatin And/Or its 36. Methanol 14953.00 14686.50 98.22 intermediates

Cyclohexane 9261.90 9096.60 98.22

IPA 21112.50 20739.70 98.23

Methyl ethyl ketone 2300.00 2258.00 98.17

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Simvastatin And/Or its 37. Methanol 11023.00 10835.90 98.30 intermediates

Toluene 11311.30 11111.30 98.23

EA 14709.90 14509.90 98.64

MDC 11862.60 11688.10 98.53

Cyclohexane 12180.20 11994.40 98.47

Omeprazole And/Or its 38. Methanol 24106.92 23632.21 98.03 intermediates

Dichloro Methane 13765.58 13490.10 98.00

Acetone 667.69 654.52 98.03

Phenylephrine And/Or its 39. Iso-propyl alcohol 856.00 839.00 98.01 intermediates

Ethyl Acetate 500.00 491.00 98.20

ii VOC emission sources and its mitigation measures

‹ Mentioned in the EIA report.

H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Remarks Hazardous chemicals Storage tanks Toluene --- Methanol Drum/Barrel storage N-propanol --- Tri ethyl Amine Fresh IPA Ethanol Acetonitrile Thionyl chloride HCl Glass Bottle Liquid Bromine Liquid Bromine should be stored in a cool,

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dry, well-ventilated area away from sources of moisture. Keep glass container tightly closed and in a well-ventilated place. Store at +5°C to +30°C.

‹ Applicability of PESO : Will be Apply after getting permission

• During SEAC meeting dated 01/10/2019, Committee asked for revised product profile with area adequacy, technical expert of PP informed that they have reduced production capacity almost 40% i.e. from 120.50 MT/Month to 70.60 MT/month and submitted Revised Product profile as above. PP informed that at a time they will manufacture only seven (7) nos. of products at a one time between group 1 to 7 and total plot area is 5,000.00 m2 , which is sufficient for the production of 70.60 MT/month and R and D products in Kg/Month with its utility. Committee asked regarding querry of adequate waste water treatment scheme with segregation of effluent, its stage wise characteristic and CETP saykha details, Technical expert of PP informed that they have submitted revised water balance diagram considering worst case scenario for production group no-1 to 7. They will segregate low COD stream and high COD stream at source and high COD stream after primary treatment and solvent stripper will be evaporated in in-house MEE and ATFD while MEE condensate along with Low COD stream will be treated in ETP and treated effluent will sending to CETP, Saykha for further treatment and disposal. PP informed about revised air matrix for flue gas and process emission details in length.MCS , Bag filter and water scrubber as APCM will be provided separately with coal fired boiler and thermo pack. Committee asked about bleed liquor disposal of process gas scrubber, PP informed that exhausted scrubbing media like spent Hcl, Ammonium chloride etc. will be sold to end-users having Rule- 9 permission. • Committee asked about clarification regarding some products mentioned in Hazardous waste is hazardous waste or by product and clarification regarding 57 products mentioned in Hazardous waste matrix, PP informed that they have reduced 57 Hazardous waste to 32 Hazardous waste as previously they have mentioned each solvent as Hazardous waste and also sending process waste from Product no-130 namely Digoxin and/or its intermediate for incineration to CHWIF instead of reuse as fuel.

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• Considering the above project details, after detailed discussion, the terms of reference (ToR) were prescribed as below and as per the standard TOR for the Synthetic Organic Chemical projects recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and approved by SEIAA in its 12 th meeting dated 16/09/2017 for the EIA study to be done covering 10 Km radial distance from the project boundary. 1. Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP report. 2. Explore the use of renewable energy to the maximum extent possible. Details of provisions to make the project energy-efficient through energy efficient devices and adoption of modes of alternative eco-friendly sources of energy like solar water heater, solar lighting etc. Measures proposed for energy conservation. 3. Technical justification of ETP sludge and MEE salt quantity against treatment of industrial effluent. 4. Separate ETP for High COD effluent stream and Low COD effluent stream in plant. 5. PP shall furnish status of all the applicable rules, acts, regulation, clearances in a tabular form. 6. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during unloading, storage, transportation, handling and processing of Solvents and bromine, oleum, ammonia etc. 7. Adequacy of in house ETP and in-house MEE along with stage wise effluent characteristic and feasibility report by third party NABL accredited academic institute regarding adequacy of ETP and in-house MEE. 8. Segregation of waste water streams based on characteristics and its proper management keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . (COD, BOD, TDS etc. of each stream shall be given) 9. Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent proposed for use in-house with detailed chemical properties including vapor pressure. LDAR shall endeavor prevention of losses of solvents to the best minimum extent with each chapter for each solvent. 10. MoU with actual end-users for sending Hazardous waste streams under Rule 9 as per the HW Rules 2016. 11. Adequacy of reuse of Hazardous waste generated from bulk drug product is utilize for different bulk drug products as per HWR Rules’2016. • The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs

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available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be considered as generic TORs for preparation of the EIA report in addition to all the relevant information as per the generic structure of EIA given in Appendix III in the EIA Notification, 2006. • Further Project Proponent may be advised to submit final EIA Report with EC application within 100 days from the date of issuance of this ToR to expedite processing of Environment Clearance application. • The project proponent shall have to apply for Environmental clearance through online portal http://environmentclearance.nic.in/ along with final EIA report. 15. Offline Application M/s. Mirash Indu stries Pvt. Ltd (Unit - Screening and 1) scoping PLOT NO. D2/14, GIDC Dahej-II, Ta:- Vagra, Dist:-Bharuch . • PP submitted the E-mail to delist the application as the project falls in B1 category. • Committee decided to withdraw the proposal and permanently close the file. 16. Offline Application M/s. H. P. Mineral s EC -Reconsideration S.No-943 , Nr. GMDC colony, Rajpardi, Ta- Jhagadia, Dist- Bharuch • PP submitted withdrawal letter for EC – Appraisal presentation held on 01/10/2019. • Committee decided to withdraw the proposal and permanently close the file. 16 SIA/GJ/IND2/38906/2019 M/S. RUCHI PETROCHEMICALS LIMITED Screening & Plot no- 42/2, GIDC Dahej, Ta- Vagra, Dist- Scoping Bharuch Category of the unit: 5(f) Project status: Expansion • This office has received an application vide their online proposal no. SIA/GJ/IND2/38906/2019 dated 29/07/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report. • Project proponent (PP) has submitted Form-1, PFR and relevant details/information. • This is an existing unit for inorganic chemicals and now proposes for expansion in manufacturing of new synthetic organic chemicals as tabulated as below:

Total SR. Existing Proposed PRODUCT NAME Proposed NO MT/Month MT/Month MT/Month Existing Non EC Product

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1. Calcium Chloride 333.33 5666.67 6000 Equivalent Sulfuric Acid (a) Sulphuric Acid 30000 NIL 30000 2. (b) Oleum 23% and 65 % 6000 NIL 6000

(c) Liq. SO 3 15000 NIL 15000 3. Chloro Sulphonic Acid 12000 NIL 12000 4. Thionyl Chloride 6000 NIL 6000 5. Sodium Bi sulphate 3000 NIL 3000 6. Sulphur Dioxide 2400 NIL 2400 7. Sulphur Mono Chloride 400 NIL 400 8. Sulphuryl Chloride 400 NIL 400 9. Di Calcium Phosphate 3000 3000 6000 10. Poly Aluminum Chloride -- 4000 4000 Proposed EC Product Chlorination of HC Such as MCB, DCB, ODCB, 11. -- 5000 5000 PDCB,MDCB &TCB) Nitro derivatives of Hydro such as 12. NCB/PNCB/ONCB/NT/NX/EHX/EHN/NB/Nitro Methane/ -- 15000 15000 ONT/PNT/MNT/MDNB/DCNB Hydrogenation of HC, Nitro Hydrocarbon & Chloro 13. Hydrocarbon Like Aniline, OA/PA, DCA/PCA/MCA, -- 5000 5000 MPD/OPD/PPD, Toludine, Cumidiene, Xylidine, 3, 3 DCB 14. ONA/PNA -- 3000 3000 15. H Acid -- 1500 1500 16. Vinyl Sulphone -- 3000 3000 17. Di Methyl Sulphate -- 5000 5000 18. Di Methyl Aniline -- 3000 3000 19. Acetanilide -- 2500 2500 20. Triphosgene -- 8000 8000 21. Benzyl Sulphonyl Chloride - 3000 3000 22. Sulphonation of substituted HC such as DASDA/Metanilic 2000 2000

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Acid/ MPDSA/PNTOSA/ C acid 23. Red B(FR B – fast red B) 1500 1500 78533.33 70166.67 148700 24. Power Plant (Waste Heat Recovery Boiler) 4.2 MW -- 4.2 MW 25. Power Plant (Steam turbine) -- 4.9 MW 4.9 MW • The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 14/08/2019. • During the meeting dated 14/08/2019, technical presentation made by the Project proponent. • Committee noted that this proposal is for expansion in GIDC Dahej. Committee discussed in detailed about category of the project as per EIA Notification 2006. Committee asked PP about production of Sulphuric Acid in the Existing Plant along with Manufacturing of Single Super Phosphate in the expansion stage. PP could not reply satisfactorily about the proposed project in line with the EIA Notification 2006. Committee deliberated in detailed about list of projects or activities requiring prior environmental clearance as per the schedule of EIA Notification 2006 and concluded that the proposed project is covering under 5(a) “Chemical Fertilizer” and the production of Single Super Phosphate is going to take place in expansion stage along with production of Sulphuric Acid in the Existing Plant which attracts “Category A”. Committee asked PP to clarify the same. PP mentioned that they will drop the production of “Single Super Phosphate” in the Expansion stage and submit revised proposal as per the schedule of EIA Notification 2006 considering “Category B”. • After detailed discussion, committee decided to consider the project only after submission of revised proposal with revised Form-1, PFR, and Format and consider the project in one of the upcoming meeting of SEAC after satisfactory submission of the following documents. • Project Proponent remained absent during meeting on dated 04.09.2019, hence committee decided to defer the proposal in one of the upcoming SEAC meeting. • Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned point. • Salient features of the project including Water, Air and Hazardous waste management (Revised): Sr. Particulars Details no. A Total cost of Proposed Project Existing: 150 Cr. (Rs. in Crores): Proposed: 310 Cr. Total: 460 Cr. B Total Plot area Existing: 540000 Sq. m. ( sq. meter) Proposed: NIL

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Total : 540000 Sq m Green belt area Existing: 162000 Sq. m ( sq. meter) Proposed : NIL Total : 162000 Sq. m C Employment generation 195 D Water i Source of Water Supply GIDC Water (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. ii Water consumption (KLD)

Water Consumption in KL/Day Remarks Sr Category PROPOSED No EXISTING Additional TOTAL

1. Domestic Purpose 15 NIL 15

2. Gardening NIL 50 50

INDUSTRIAL

Process & Washing 265 2091 2356

Cooling 2400 100 2500 3. RO Plant/Softening Plant 1090 (P) 1090 We will install RO/Softening plant for *Boiler 390 (240** E + 150 P) 390 existing as well as *Scrubber NIL 400 400 proposed utility

Total water Consumption 15.0 NIL 15.0 Domestic

Total water Consumption 2905 3041 5946 (Industrial)

Total Water Consumption (1 + 2 2920 3091 6011

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+ 3)

Total Reuse Water - 3499 3499

Fresh Water After Reuse 2512

Note *The RO Permeate water will be utilized in Boiler feed and in scrubbing system ** The proposed RO/softening system will satisfy existing water utilization in boiler and proposed total includes the same. The details elaborated in water balance diagram.

Note: The wastewater from the process is higher than the consumption due to ice utilization in each process.

1) Total water requirement for the project: 6011 KLD 2) Quantity to be recycle: 3499 KLD 3) Total fresh water requirement: 2512 KLD iii Waste water generation (KLD)

Wastewater Generation in KL/Day Sr Category EXISTIN Addition PROPOSE No G al D TOTAL 1. Domestic Purpose 13 NIL 13 INDUSTRIAL Process & Washing 56 4408 4464 Boiler 25 10 35 2. Cooling 20 5 25 Scrubber* - 593 * 593* RO REJECT -- 300 300 Total Waste Water Generation 13 NIL 13.0 (Domestic) Total Waste Water Generation 101 4723 4824 (Industrial) Reuse Water -- 3499 3499 Waste Water Discharge in vilayat 101 409 510

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pipeline for disposal Wastewater Disposal through captive --- 815 815 Spray Drier

Note: Domestic: The sewage generated from domestic activity will send to septic tank and over flow of the same will convey to activated sludge process to maintain the MLSS/MLVSS ratio in the tank. Industrial: • Total Industrial 4824 KLD Waste Water Generation from Manufacturing Process and Other Ancillary Operation, • From which 233 KLD condensate water reuse in Process • The 4081 KLD Waste water generation form H and Vs Plant and other Sulphonation of HC and Fast red B Effluent will be discharge though MEE followed by In house Spray Dryer. • The 3266 KLD MEE condensate Reuse in Process and 815 KLD MEE Reject will be Discharge though In-house Spray dryer. • The remaining 510 KLD Other ancillary operation which is Treated in In house ETP Plant for dilute stream and after achieving the norms it will be Send to Dispose into GIDC Sewer line –Dahej Vilayat Pipeline/Common Disposal System up to the sea. iv Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. High Concentrated Effluent plant Sr Nos Name of unit Capacity NO 1 Collection Tank 6 500 KL Each 2 Neutralization Tank 6 200 KL Each 3 Filter press 12 1600 X 1600 X 48 Plates 4 Crystallization 5 200 KL Each 5 MEE 1 200 KLPH 6 MEE Condensate Collection Tank 3 500 KL Each 7 MEE Reject 2 500 KL Each 8 High Temperature Spray Dryer 4 10 KLPH Each

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Low Concentrated Effluent plant Sr.

No Name of unit Volume in KL Nos. .

1 Collection cum Equalization Tank 250 KL 2 2 Neutralization Tank (NT) 25 KL 2 3 Flash Mixer (FM) 10 KLPH 1 4 Flocculator (FL) --- 1 5 Lime Dosing Tank (LDT) 5 KL 1 6 Alum Dosing Tank (ADT) 5 KL 1 7 Polyelectrolyte Dosing Tank (PEDT) 5 KL 1 8 Nutrient Dosing Tanks (NDTs) 2 KL 2 9 Primary Clarifier (PCL) 30 KL 1 10 Aeration Tank (AT) 300 KL 1 11 Secondary Clarifier (SCL) 30 KL 1 12 Intermediate Sump (IS) 40 KL 1 13 Pressure Sand Filter (PSF) 10 KLPH 1 14 Activated Carbon Filter (ACF) 10 KLPH 1 15 Treated Effluent Sump (TES) 250 KL 2 16 Sludge Sump (SS) 50 MT 1 17 Filter Press (FP) 1250 X 1250 1

Treatment scheme including segregation at source. High Concentrated Effluent

Low Concentrated Effluent

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Collection cum Neutralization Flash Primary Flocculator Equalization tank Tank Mixer clarifier

Activated Secondary Intermediat Pressure Aeration Carbon Clarifier e Sump Sand Filter Tank Filter

Treated Efflunet Sump Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP .

Domestic: The sewage generated from domestic activity will send to septic tank and over flow of the same will convey to activated sludge process to maintain the MLSS/MLVSS ratio in the tank.

Industrial : • Total Industrial 4824 KLD Waste Water Generation from Manufacturing Process and Other Ancillary Operation, • From which 233 KLD condensate water reuse in Process • The 4081 KLD Waste water generation form H and Vs Plant and other Sulphonation of HC and Fast red B Effluent will be discharge though MEE followed by In house Spray Dryer. • The 3266 KLD MEE condensate Reuse in Process and 815 KLD MEE Reject will be Discharge though In-house Spray dryer. • The remaining 510 KLD Other ancillary operation which is Treated in In house ETP Plant for dilute stream and after achieving the norms it will be Send to Dispose into GIDC Sewer line –Dahej Vilayat Pipeline/Common Disposal System up to the sea. Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Not applicable v Mode of Disposal & Final meeting point Domestic: The sewage generated from domestic activity will send to septic tank and over flow of the same will convey to activate sludge process to maintain the MLSS/MLVSS ratio in the tank. Industrial: • Total Industrial 4824 KLD Waste Water Generation from Manufacturing Process

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and Other Ancillary Operation, • From which 233 KLD condensate water reuse in Process • The 4081 KLD Waste water generation form H and Vs Plant and other Sulphonation of HC and Fast red B Effluent will be discharge though MEE followed by In house Spray Dryer. • The 3266 KLD MEE condensate Reuse in Process and 815 KLD MEE Reject will be Discharge though In-house Spray dryer. • The remaining 510 KLD Other ancillary operation which is Treated in In house ETP Plant for dilute stream and after achieving the norms it will be Send to Dispose into GIDC Sewer line –Dahej Vilayat Pipeline/Common Disposal System up to the sea. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility -Not Applicable Membership of Common facility (CF) (For waste water treatment) vii Simplified water balance diagram with reuse / recycle of waste water

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Exisiting

After Expansion Water Balance Diagram

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vii Reuse/Recycle details (3499 KLD) [Source of reuse & application area] Total reuse 3499 KLD Source of waste water Application area Remarks Characteristics of waste water for reuse with quantity with quantity in regarding to be reused (COD, BOD, TDS in KLD (From where it KLD (Where it is feasibility to etc.) is coming) used) reuse i.e. Product Condensate and 3266 KLD reuse in pH 7-8 It will be feasible MEE Condensate process COD 400-500 to reuse in TDS 700-800 process with fresh water

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. Stack Stack Sr. height Type of attached Fuel Consumption APCM Remark no in Emission to meter Steam Boiler (10 MTPH) ESP + Water 1 30 Existing (Replace Scrubber Imported with 15 50 MT/Day Coal TPH) PM Steam SOx ESP + Water 2 Boiler (15 30 NOx Proposed Scrubber TPH) Thermic ESP + Water Fluid Imported 3 30 30 MT/Day Scrubber Proposed Heater I Coal

(20 Lac

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Kcal/hr)

Thermic Fluid Imported 4 Heater II 30 MT/Day Proposed Coal (20 Lac Kcal/Hr) HAG (20 Imported ESP + Water 5 Lac 30 25 MT/Day Proposed Coal Scrubber Kcal/hr) D.G Set PM Acoustic 6 (AS Stand 11 HSD 25 lit/hr SO x Proposed enclosures By) NO x Stack for PM Power Imported ESP + Water 7 22 30 MT/Day SO x Proposed plant (4.9 Coal Scrubber NO x MW)

ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) Existing & Proposed - Stack Sr. Stack attached to height in APCM Type of Emission Remark no meter

Two stage Alkali HCl 1 Reaction Vessel 11 Existing Scrubber Cl2

Two stage Alkali SO2 2 Sulphuric Acid Plant 50 Existing Scrubber Acid Mist/Sulphur

Two stage Alkali Cl2 3 Thionyl Chloride 20 Existing Scrubber SO2

4 Sulphur Mono 20 Two stage Alkali Cl2 Existing

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Chloride Scrubber

Two stage Alkali 5 Sulphuryl Chloride 20 Cl2 Existing Scrubber Liq. SO3 Storage 6 22 H2SO4 Scrubber SO2 Existing tanks of CSA Plant

CSA Storage Tank of HCl 7 22 Dilute CSA Scrubber Existing CSA Plant SO2

Two stage Alkali HCl 8 Reactor of CSA Plant 22 Existing Scrubber SO2

Multi cyclone Spray Dryer for H acid 9 11 Separator with Two PM Proposed Plant Stage water Scrubber Isolator for H Acid Two stage Alkali 10 12 SO 2 Proposed 5 Nos. Scrubber Neutralizer for H Acid Two stage Alkali 11 12 NO x Proposed 5 Nos. Scrubber Water Absorber Glass Chlorinator of Chloro HCl 12 15 Water Scrubber with Proposed Benzene Plant Cl 2 Caustic Scrubber Alkali Scrubber + HF 13 DCP Plant 15 Proposed Water Scrubber HCl Two Stage Alkali + SO2 14 Vinyl Sulphone Plant 15 Proposed Water Scrubber HCl Alkali Scrubber + 15 Triphosgene 15 HCl Proposed Water Scrubber Multi cyclone Spray Drier for water 16 15 Separator with Two PM Proposed Evaporation Stage water Scrubber

iii Fugitive emission details with its mitigation measures.

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ó The entire manufacturing activities will be carried out in the closed reactors and regular checking and maintenance of reactors will be carried out to avoid any leakages. ó The tank vents will be equipped with either a carbon filter or an oil trap to prevent water vapor from entering the tank as it breathes. ó All the motors of pumps for the handling of hazardous chemicals will be flame proof and provided with suitable mechanical seal with stand-by arrangement ó Control of all parameters on a continuous basis will be done by adequate control valves, pressure release valves and safety valves etc. ó All the flange joints of the pipe lines will be covered with flange guards. ó All the raw materials will be stored in isolated storage area and containers tightly closed. ó There will also be provision of adequate ventilation system in process plant and hazardous chemical storage area F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Existing & Proposed i Hazardo Sr Existin Propo Type of us Quantit . g sed Mode of Hazardous Sources Waste y MT/ N MT/ MT/ Disposal Waste Categor Year o. Year Year y Collection , Storage, Transport ETP ation & 1 ETP Sludge 35.3 600 1200 1800 Plant Disposal to nearest TSDF at Dahej Collection Spray Dryer , Storage, Spray 2 evaporation - - 11520 11520 Transport dryer salt ation and sell to

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actual users or Disposal to nearest TSDF at Dahej Collection , storage, Used Plant Reuse 3 Oil/Spent Machine 5.1 12 24 36 within Oil ry premises/ authorizer Recycler. Collection , storage, and Empty Material Dispose Drums/Cont Storage 4 33.1 600 1200 1800 by selling ainer and to Empty Bags Handling authorize d Reuse /Recycler Nitro Collection Derivativ , Storage, es Transport Product, ation and Spent H Acid, in which Sulphuric 51037 5 Vinyl 26.3 NIL 510372 334752 Acid (35 to 2 Sulphon MT/Year 75%) e, DMS, reuse DMA, with in Benzyl Plant Sulphon Premises

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yl (i.e Chloride 162500 Sulphon MT/Year ation of Spent HC Sulphuric Product Acid(Fro and Fast m VS) B Reuse in H Acid, 97200 MT/Year will be reuse in DCP, 45072 MT/Year will be reuse in CSA and 30480 MT/Year will be Reuse in Metanilic Acid) and remaining 175620 MT/Year Spent Sulphuric Acid send to industry

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having permissio n under Rule 9. Collection , Storage and Reuse in as raw Material Chlorinat in of Calcium HC, Chloride Vinyl Process, Sulphon Chloro Spent HCl e, 17796 Sulphonic 6 Acid (30% - 26.3 NIL 177960 Benzyl 0 Acid and 32%) Sulphon Poly yl Aluminum Chloride, Chloride Triphosg against ene total requireme nt of Spent HCl Acid 379140 MT/Year Collection , Storage, Sodium 7 OA/PA - NIL 76800 Transpirat Chloride 76800 ion and send to

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industry having permissio n under Rule 9 Collection , Storage, and Process 8 DCP 26.1 NIL 18000 18000 Dispose Sludge to Co processin g/ TSDF Collection, Storage, and Gypsum 13860 9 H Acid 26.1 NIL 138600 Dispose to Sludge 0 Co processing / TSDF H Acid C Acid Collection, and Storage, other and sulphona 14220 Transporta 10 Iron Sludge tion 26.1 NIL 142200 0 tion for co- product processing and or Send to DCA, TSDF Site MCA, PCA Collection, Activated Fast B 11 - NIL 270 270 Storage, carbon red and

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Dispose to Co processing / TSDF Collection, Storage, and Reuse Sodium Bi 12 H Acid - NIL 17820 17820 within Sulphite plant premises in H Acid Collection, Storage, Transporta tion and reuse 20520 MT/Year in H Acid Manufactu H Acid, ring Glauber Vinyl 13 - NIL 91080 91080 process Salt Sulphon and e Remaining 70560 MT/Year send to industry having permission under Rule 9.

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Collection, Storage Transporta tion and Hydrofluosili send to 14 DCP - 720 720 1440 cic Acid industry having permission under Rule 9. Collection, Storage Transporta tion and Sodium Scrubbing send to 15 -- NIL 3060 3060 Nitrate Media industry having permission under Rule 9. Collection, Storage Transporta tion and Sodium Scrubbing send to 16 Hypo - NIL 7320 7320 Media industry chloride having permission under Rule 9. Spent Vinyl Collection, 17 Acetic Acid Sulphone, 26.3 Nil 22500 22500 Storage, (45 % to 55 Acetanilid Total

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% e reuse with plant premises in Acetanilide process against total requireme nt of Acetic Acid 2362.5 MT/Year. Collection, Storage, Spent H Acid, Distilled 18 26.1 NIL 14352 14352 Solvent TCB out and reuse in process Collection, Storage, and Solvent Distillation Transporta 19 26.1 NIL 4032 4032 Residue Unit tion for co- processing or Send to CHWIF Note : • We have consider neutralization quantity of ETP waste in gypsum waste to easily send for co- processing hence the quantity of ETP waste is not reflecting much quantity with respect to wastewater generation. • The spent generation from products pertaining to GPCB circular 03.11.2018 will utilized in house in the manufacturing process. The spent generated from other sources will disposed by sending to actual

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users having permission of Rule 9 ii Membership details of TSDF, CHWIF etc. Not Applicable (For HW management) iii Details of Non-Hazardous waste & its disposal(MSW and others) No G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents Qty of Total Qty of of Sr. Name of Solvent Solvent Solvent Losses % recovery % Losses No Product Recycled Input (Kg) (Kg) (Kg) 1 TCB ODCB 5379 5354 25 99.50 0.5 2 H acid Methanol 938 919 19 98.50 1.5

ii VOC emission sources and its mitigation measures • Sources of fugitive emissions include storage of chemicals, solvents storage, loading and unloading section, raw material handling and, hazardous waste storage area Measures : • The fugitive emissions in terms of handling losses will get reduced by proper storage and handling. • Hazardous chemicals will be stored as per standard criteria. • Periodically monitoring will be carried out as per the post project monitoring plan. • All materials must be stored in suitable packing to prevent contamination of air. • Enclosed system & efficient procedures for materials charging shall be ensured. H ‹ Details regarding storage of Hazardous chemicals Name of major Hazardous Storage details Capacity Nos. chemicals Sulphuric Acid 100 4 Chlorine - 500 Tonner Benzene 100 5 Mono Chloro Benzene 100 2 Storage tanks PNCB 100 2 ONCB 100 1 Dichloro Benzene 100 1 Nitric Acid 100 3

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PNT 100 2 ONT 100 2 Ammonia Anhydrous 50 1 Bullet Nepthanol 50 2 Oleum 250 KL 5 Ethylene Oxide 100 2 Hydrogen - Bank OR Pipeline Methanol 100 2 Catalyst Drum / Barrel storage Acetic Acid Nitric Acid

‹ Applicability of PESO : Not Applicable. • During SEAC meeting dated 01/10/2019, Committee asked this case is category “A” project or not, technical expert of PP informed that they have drop single super phosphate product from product list and submitted revised proposal as category ‘B project with revised product profile as above. Committee asked about proposed captive power production, technical expert of PP informed that proposed captive power production is 4.9 MW hence public hearing is not applicable to the unit. Committee asked about existing plant compliance, PP informed that they have obtained CTE for existing in-organic products and still not commissioned existing plant. Committee asked about waste water management for dirty products, technical expert of PP informed that high concentrated effluent from dirty production will be treated in primary ETP and treated effluent will be evaporated in in-house MEE. MEE condensate will be reused back while MEE reject will be evaporated in in- house spray dryer. Low COD effluent from other organic products except dirty products along with utilities will be treated in ETP units and will be discharged into GIDC Dahej pipeline. Committee asked about domestic sewage disposal, PP informed that domestic effluent disposal in septic tank and overflow of domestic effluent taken into aeration tank of secondary ETP for MLSS development.Committee insisted for spare oleum storage tank and safety measures for nitration, hydrogenation and Cl2 handling as per PESO standards. Committee asked about APCM with coal fired boiler, ESP and water scrubber as APCM will be provided with coal fired boilers. Committee deliberated in length regarding Hazardous waste management and its disposal. Committee insisted for compliance of conditions stipulated in GPCB circular dated 03/11/2018. • Considering the above project details, after detailed discussion, the terms of reference (ToR) were prescribed as below and as per the standard TOR for the Synthetic Organic Chemical projects recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and approved by SEIAA in its 12th meeting dated

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16/09/2017 for the EIA study to be done covering 10 Km radial distance from the project boundary. 1. Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be made as per MoEF&CC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP report. 2. Details with respect to justification for proposed expansion: (1) To address proportionate availability of space for production plant. (2) To address proportionate availability of storage area for raw materials finished goods, utilities considering fire-safety norms & PESO standards and goods carrier movement within premises. (3) To address proportionate captive/common infrastructure available to accommodate additional load due to proposed expansion. (4) Environment impact and its mitigation measures for common/ captive infrastructure due to proposed production. 3. PP shall install online TOC/Ammonical nitrogen meter at final outlet of ETP and shall install online CEMS with flue gas emission stack. 4. Explore the use of renewable energy to the maximum extent possible. Details of provisions to make the project energy-efficient through energy efficient devices and adoption of modes of alternative eco- friendly sources of energy like solar water heater, solar lighting etc. Measures proposed for energy conservation. 5. PP shall address adequacy of reuse of various spent acid and bleed liquor with details of storage, handling and re-use under the Hazardous and other Waste (Management and Transboundary Movement) Rules 2016 with its stoichiometric mass balance. 6. Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent proposed for use in-house with detailed chemical properties including vapor pressure. LDAR shall endeavor prevention of losses of solvents to the best minimum extent. 7. PP shall furnish status of all the applicable rules, acts, regulation, clearances in a tabular form. 8. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during unloading, storage, transportation, handling and processing of Solvents 9. Submit adequacy of proposed process APCM attached for process gas emission reactor like sulphonation and nitration etc. process for dirty products. 10. Treatability & adequacy report for complete ZLD for wastewater. Feasibility report for complete reuse treated waste water for industrial purpose like in boiler feed and sodium sulphate recovery. 11. Technical justification of quantity of ETP sludge and MEE salt against treatment of effluent. 12. Compliance of all the conditions stipulated in GPCB circular dated 03/11/2018 and subsequent circulars/orders in this regard. 13. Submit compliance of Coal storage and handling guideline of GPCB in spirit

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14. Submit adequacy report of third party NABL accredited academic institute like NEERI regarding in – house ETP,in-house MEE and spray dryer considering proposed dirty products production. 15. Detailed SOP for safe handling of hydrogenation and hydrogenation process proposed to be implemented for product where hydrogenation and nitration process is involved. 16. Provision of spare tank as a safety precaution for Oleum storage and emergency transfer facility for Oleum as per the prevailing Rules/ guidelines. • The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be considered as generic TORs for preparation of the EIA report in addition to all the relevant information as per the generic structure of EIA given in Appendix III in the EIA Notification, 2006.

• Further Project Proponent may be advised to submit final EIA Report with EC application within 100 days from the date of issuance of this ToR to expedite processing of Environment Clearance application. • The project proponent shall have to apply for Environmental clearance through online portal http://environmentclearance.nic.in/ along with final EIA report. 17. SIA/GJ/IND2/31289/2019 M/S. FERROX CHEMICAL PVT. LTD ToR – Plot no-1665, GIDC Sarigam, Ta- Reconsideration Umbergaon, Dist- Valsad Category of the unit: 5(f) Project status: Expansion • This office has received an application vide their online proposal no. SIA/GJ/IND2/31289/2019dated 12/06/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report. • Project proponent (PP) has submitted Form-1, PFR and relevant details/information. • This is an existing unit and now proposes for expansion of manufacturing plant of synthetic organic chemicals as tabulated below: SR. CAS Existing Proposed TOTAL PRODUCTS END USE REMARK NO NO. (MT/M) (MT/M) (MT/M) 7782- 300.00 0.00 1 Ferrous Sulphate 300.00 Pharma 63-0 Not in Pesticides 7758- 10.00 0.00 & Fungicides 2 Copper Sulphate 10.00 Pharma 99-8 1 2, 4 DI-CHLORO NITRO 609-89- 0.00 35.00 35.00 Feed additive Organic Product

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PHENOL 2 & Intermediate 2,4 DI-CHLORO 6 AMINO 5930- for 5 chloro Organic Product PHENOL 28-9 4 CHLORO 2 AMINO PHENOL 95-85-2 Organic Product 5-CHLORO 8-HYDROXY 130-16- Feed additive Organic Product QUINOLINE 5 & 5, 7 DI-IODO-8-HYDROXY 130-26- Intermediate Organic Product QUINOLINE 7 for halquinol 130-26- Feed additive 5-CHLORO 7-IODO 7 & Organic Product HYDROXYQUINOLINE Intermediate for Albedazole 141-01- FERROUS FUMARATE Organic Product 5 FERROUS GLYCINE 17169- Organic Product SULPHATE 60-7 Food minerals 299-29- 2 FERROUS GLUCONATES 0.00 80.00 80.00 and Iron Organic Product 6 Premix 24808- FERROUS ASCORBATE Organic Product 52-4 299-29- FERRIC GLUCONATE Organic Product 6 METHYL IODIDE 74-88-4 Organic Product Used in Mfg of 593-71- CHLOROIODOMETHANE Statins Organic Product 5 DI-IODOMETHANE 75-11-6 Organic Product 591-50- Catalyst 3 IODOBENZENE 0.00 20.00 20.00 Organic Product 4 TRI METHYL SULFOXONIUM 1774- Flucanazole Organic Product IODIDE 47-6 3240- Custom IODOBENZENE DIACETATE Organic Product 34-4 Synthesis

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2 IODO BENZOIC ACID 88-67-5 Organic Product 610-97- 2 IODO METHYL BENZOATE Organic Product 9 516-12- N-IODO SUCCINIMIDE Organic Product 1 133-91- Pharma 4 3:5 DI-IODO SALISYLIC ACID 0.00 05.00 05.00 Organic Product 5 Intermediate 14639- CHROMIUM PICOLINATE Organic Product 5 25-9 0.00 05.00 05.00 Mineral Premix PICOLINIC ACID 98-98-6 Organic Product 30123- 4-AMINO 1,2,4 TRIZOLE Organic Product 90-2 6 0.00 05.00 05.00 Flucanazole 288-88- 1-H 1,2,4 TRIZOLE Organic Product 0 657-27- L-LYCINE MONO HCL USP Organic Product 2 7 0.00 15.00 15.00 Excepient 110-17- FUMARIC ACID Organic Product 8 118-48- Isatoic Anhydride Organic Product 9 Fragrance & 8 0.00 75.00 75.00 134-20- Cosmatics Organic Product Methyl Anthranilate 3 TOTAL 310.00 240.00 550.0 • The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 23/07/2019. • Technical presentation was made by the project proponent with consultant/expert Aditya Environ during SEAC meeting dated 23/07/2019. • Committee noted that this unit is Greenfield project at GIDC Sarigam. • During SEAC meeting, committee asked for area adequacy for proposed production capacity, PP informed that area of proposed project is only 1000 square metre. Committee asked justification regarding process reactor, R/M storage, finished product storage, green belt, utility and ETP in proposed area, PP could not satisfactorily addressed about it. Committee asked to submit revised product profile with mentioning end use of proposed

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product is not for pesticide and fungicide. • PP informed that raw material storage mentioning in tank which committee marked that tank storage is not adequate for proposed project area. • After detailed discussion, Committee decided to defer the proposal and consider the same in one of the upcoming meeting of SEAC after submission of following details, 1. Revised product profile with technical justification regarding process reactor, R/M storage, finished product storage, green belt, utility and ETP in proposed area. 2. Revised product profile with notarized undertaking regarding end use of proposed product is not for pesticide and fungicide products. 3. Details with respect to justification for proposed expansion : (1) To address proportionate availability of space for production plant. (2) To address proportionate availability of storage area for raw materials finished goods, utilities considering fire-safety norms & PESO standards and goods carrier movement within premises. (3) To address proportionate captive/common infrastructure available to accommodate additional load due to proposed expansion . (4) Environment impact and its mitigation measures for common/ captive infrastructure due to proposed production . • During the SEAC meeting dated 04/09/2019, Committee asked about reply of above query, PP informed that they have submitted revised prescribed format for technical details and product profile. Committee asked clarification regarding product profile as new products while mentioning expansion project, technical expert of PP informed that unit is having CTE of the Board for Non- EC products like ferrous sulphate and applied for new EC applicable products. Committee disagrees with proposal as new product and submit revised proposal with Prefeasibility report (PFR) as expansion project. Committee asked about existing plant legal compliance, Technical expert of PP hide details of legal and CCA status of existing plant in presentation. • After detailed discussion, it was decided to defer the proposal and consider the same in one of the upcoming meeting of SEAC after submission of following details, 1. Revised product profile as expansion project instead of new project along with revised Prefeasibility report(PFR) with adequate water consumption, waste water generation, flue/process gas emission and Hazardous waste details. 2. Compliance status of existing plant CCA and legal action taken against unit by the Board in last three years. 3. Clarification from technical expert of PP regarding hide details of existing plant CCA, Court case & public litigation against unit and legal notices of GPCB compliance status in presentation. • Project proponent made presentation for the above mentioned query dated 01.10.2019 for the above mentioned points. • PP presented replied as below: 554 th meeting of SEAC-Gujarat, dated 01.10.2019 Page 201 of 215

1. Revised product profile as expansion project instead of new project along with revised Prefeasibility report (PFR) with adequate water consumption, waste water generation, flue/process gas emission and Hazardous waste details. 2. Compliance status of existing plant CCA and legal action taken against unit by the Board in last three years. 3. Clarification from technical expert of PP regarding hide details of existing plant CCA, Court case & public litigation against unit and legal notices of GPCB compliance status in presentation. • During SEAC meeting dated 01/10/2019, committee asked about reply of above information, PP informed that they have revised product profile as above. Also Salient features of the project including Water, Air and Hazardous waste management (Revised) submitted as below: Sr. Particulars Details no. A A Total cost of Proposed Project 2.25 Crores (Rs. in Crores):

B Total Plot area ( sq. meter) 1000.00 Sq. m.

Green belt area 250.00 Sq. m. ( sq. meter) C Employment generation 15

D Water i Source of Water Supply GIDC Water supply

(GIDC Bore well, Surface water, Tanker supply etc...)

Status of permission from the concern authority.

Ii Water consumption (KLD)

Category Quantity Remarks KLD Existing Propose Total

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(V) Domestic 3.0 1.00 4.00 (W) Industrial Process 1.70 95.40 97.10 Washing 1.00 16.00 17.00 Boiler 1.00 5.00 6.00 Cooling 1.20 3.40 4.60 Scrubbing 0.00 1.00 1.00 Others (Gardening) 1.00 0.50 1.50 Industrial Total 5.90 121.30 127.20 Total (A + B) 8.90 122.30 131.20 1) Total water requirement for the project: 131.20 KLD 2) Quantity to be recycled : 0.00 KLD 3) Total fresh water requirement: 131.20 KLD (Total water requirement = Fresh water + Recycled water)

Iii Waste water generation (KLD) Category Waste water KLD Remarks Existing Propose Total (O) Domestic 2.0 1.0 3.00 (P) Industrial Process 0.0 9.50 9.50 Washing 0.0 16.00 16.00 Boiler 0.1 0.90 1.00 Cooling 0.0 1.00 1.00 Scrubbing 0.0 0.50 0.50 Others(Gardening) 0.0 0.0 0.00 Total Industrial 0.10 27.90 28.00 waste water Total [A + B] 2.10 28.90 31.00

Iv Treatment facility within premises with capacity ‹ MEE, In-house ETP Treatment scheme including segregation at source. ‹ High COD concentrated effluent treated by MEE.

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Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ CETP Sarigam Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Not Applicable V Mode of Disposal & Final meeting point

Domestic: Soak pit/ Septic Tank

Industrial: Through underground pipeline of CETP Sarigam

Vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ CETP Sarigam Membership of Common facility (CF) (For waste water treatment) Sarigam CETP Vii Simplified water balance diagram with reuse / recycle of waste water

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Viii Reuse/Recycle details (KLD) Total reuse - NIL

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.

Source of Air Pollution Stack Quantity of Type of Sr. emission Type of Control Height Fuel emissions i.e. no. With Fuel Measures (meter) MT/Day Air Pollutants Capacity (APCM)

Evaporator 3 PM 150MG/NM Agro 1 (Existing) 10 m 0.5 MT/Day 100 ppm waste SO 2 NO 50 ppm For Inorganic x

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Stream

Boiler (600 150MG/NM 3 Natural 100 PM 2 kg/hr) 12 m 100 ppm Gas SCM/Day SO 2 (Existing) 50 ppm NO x

3 Boiler 150MG/NM Natural 500 PM 3. (2TPH) 20m 100 ppm Gas SCM/Day SO 2 (Proposed) 50 ppm NO x

DG Set 3 PM 150MG/NM (Capacity: 4. 11 m L.D.O 14 lit/hr SO 100 ppm 125 KVA) 2 50 ppm (Existing) NO x

Ii Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) Specific Source of emission Stack/Vent Air Pollution Sr. Type of Control (Name of Height no. emission Measures the (meter) (APCM) Product & Process)

Process 2 Stage water 1 NH 3 11 Vent- 1 scrubber

Process 2 Stage alkali 2 SO 2 11 Vent- 2 Scrubber

Iii Fugitive emission details with its mitigation measures: As below: Fugitive emission could occur from the storage yard of raw materials and finished products. Mitigations measures: • Proper storage of Raw materials and Products. • Ensuring closed feeding and sampling.

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• Proper Ventilation system. • Establishing SOPs for start-up, Shutdown and maintenance operational procedures. • Regular workplace monitoring and ambient air quality monitoring as per post project monitoring plan.

F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.

I Sr. Quantity (MT/Month) Source of No Type of waste Propose Total Disposal Method Generation Existing . d Collection, Storage, Discarded Decontamination. Return to Drums/ Raw Material & Raw material Suppliers. Reuse 1. 1.00 1.00 2.00 Bags/ Liners Storage for packing of Product or (Sch-I/ 33.3) Disposed through common decontamination facility. Collection, Storage, Used Oil Equipment & 2. 0.010 0.99 1.00 Transportation & Sale to GPCB (Sch-I/ 5.1) Machinery registered re-processor. Collection, Storage, Process Waste 3. Process 25.00 27.50 52.50 Transportation, disposal at (Sch-I/ 28.1) TSDF site. Process ( 5- Collection, Storage and reuse HCl Chloro 7-Iodo 462.0 within premises. Remaining 4. - - (Sch-II/ B-15) Hydroxyquinoli 0 sent to end user with ne) permission under Rule – 9. Collection,Storage, ETP Sludge 5. ETP - - 25.00 Transportation and Disposal at (Sch-I/ 34.3) common TSDF site.

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Recovered Process (2, 4 Collection, Storage and Reuse 525.0 6. Nitric Acid Di-Chloro Nitro - - within premises 0 (Sch-II/ B-15) Phenol) Process ( 2, 4 Collection, Storage & Sold to Sodium Sulfite 7. Di-Chloro 6 - - 84.00 re-processors or end users (Sch-I/ 28.1) Amino Phenol) having permission under Rule- Process (5- 9. Chloro 8- Ammonium Hydroxy 120.0 8. Sulphate - - Quinoline + 0 (Sch-I/ 28.1) Ferrous Fumarate) Liq. Ammonia 9. Scrubber - - 60.00 (Sch-II/ A-10) Process (L- Collection, Storage, Spent Carbon 10 Lycine Mono - - 1.50 Transportation & sent to (Sch-I/ 35.3) Hcl Usp) cement industries for co- Distillation processing or common 100.0 11. Residue Distillation - - incineration facility. 0 (Sch-I/ 36.1) Collection, Storage, Re- Spent Solvent 600.0 12. Process - - process and Reuse within (Sch-I/ 36.3) 0 premises Collection, Storage & Sold to MEE Salt re-processors or end users 13. MEE - - 72.00 (Sch-I/ 34.3) having permission under Rule- 9

Ii Membership details of TSDF, CHWIF etc. TSDF (For HW management) Iii Details of Non-Hazardous waste & its disposal Stationary waste. (MSW and others)

G Solvent management , VOC emissions etc.

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I Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format) Methanol, Toluene and Acetone Type of Solvent Recovery % Use of Recovered Solvent Methanol 98% Reused in next batch Toluene 98% Reused in next batch Acetone 98% Reused in next batch

Ii VOC emission sources and its mitigation measures Source: Process ‹ Enclosed processes. ‹ Minimum Joints and Flange ‹ Pumps with double mechanical seals ‹ Proper Ventilation ‹ PPEs ‹ Main heat exchanger cooling water, vent heat exchanger brine, product cooler chilled water.

H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks Drum Caustic Lye MSIHC Sch I, Part II (571) Tank HCl MSIHC Sch I, Part II (313) Tank Liq. Ammonia MSIHC Sch I, Part II (31) Tank H2SO4 MSIHC Sch I, Part II (591) Drum Acetone MSIHC Sch I, Part II (4) Drum Nitric Acid MSIHC Sch I, Part II (423) Tank Toluene MSIHC Sch I, Part II (628) Carboy Formic Acid MSIHC Sch I, Part II (287) Drum EDC MSIHC Sch I, Part II Drum Aniline MSIHC Sch I, Part II (37) Tank Methanol MSIHC Sch I, Part II (377) ‹ Applicability of PESO : Not Applicable

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• During SEAC meeting dated 01/10/2019, Committee asked about existing plant CCA and legal compliance, technical expert of PP informed that GPCB issued closure direction and after compliance of closure order conditions, GPCB issued revocation order to unit. Committee asked regarding area adequacy for proposed expansion, PP informed that proposed plot is of sufficient area for accommodate proposed expansion in plant. Committee asked about end use of product as pesticide, PP informed that end use of proposed product is not for pesticide.Committee asked about revised water balance diagram and treatment of effluent , PP informed that high COD effluent after primary treatment will be evaporated in in-house MEE while low COD effluent will be treated in ETP and treated effluent will be sent to CETP, Sarigam for further treatment and disposal. Committee insisted for install online TOC and flow meter at final outlet of ETP leading to CETP.Committee also suggested for explore possibility for reuse of boiler and cooling effluent instead of discharge. PP informed that two stage scruberr prosed for process gas emission and Natural gas will be used as fuel in boiler. Committee deliberated regarding Hazardous waste management and disposal. • Considering the above project details, after detailed discussion, the terms of reference (ToR) were prescribed as below and as per the standard TOR for the Synthetic Organic Chemical projects recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and approved by SEIAA in its 12th meeting dated 16/09/2017 for the EIA study to be done covering 10 Km radial distance from the project boundary. 1. Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be made as per MoEF & CC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP report. 2. Details with respect to justification for proposed expansion: (1) To address proportionate availability of space for production plant. (2) To address proportionate availability of storage area for raw materials finished goods, utilities considering fire-safety norms & PESO standards and goods carrier movement within premises. (3) To address proportionate captive/common infrastructure available to accommodate additional load due to proposed expansion. (4) Environment impact and its mitigation measures for common/ captive infrastructure due to proposed production. 3. PP shall install online TOC/flow meter at final outlet of ETP leading to CETP. 4. Explore the use of renewable energy to the maximum extent possible. Details of provisions to make the project energy-efficient through energy efficient devices and adoption of modes of alternative eco- friendly sources of energy like solar water heater, solar lighting etc. Measures proposed for energy conservation. 5. PP shall address adequacy of reuse of various spent acid and bleed liquor with details of storage, handling and re-use under the Hazardous and other Waste (Management and Transboundary Movement) Rules 2016 with its stoichiometric mass balance.

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6. Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent proposed for use in-house with detailed chemical properties including vapor pressure. LDAR shall endeavor prevention of losses of solvents to the best minimum extent. 7. PP shall furnish status of all the applicable rules, acts, regulation, clearances in a tabular form. 8. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during unloading, storage, transportation, handling and processing of Solvents 9. Submit notarized undertaking regarding end use of existing and proposed product shall not be sold as pesticide and its intermediates. 10. Treatability & adequacy report for in-house MEE and ETP with stage wise reduction of pollutants. 11. Technical justification of ETP sludge and MEE salt quantity against treatment of trade effluent. • The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be considered as generic TORs for preparation of the EIA report in addition to all the relevant information as per the generic structure of EIA given in Appendix III in the EIA Notification, 2006. • Further Project Proponent may be advised to submit final EIA Report with EC application within 100 days from the date of issuance of this ToR to expedite processing of Environment Clearance application. • The project proponent shall have to apply for Environmental clearance through online portal http://environmentclearance.nic.in/ along with final EIA report. 18. SIA/GJ/IND2/17426/2019 GUMANDEV CHEMICALS PVT. LTD. Reconsideration (EC– Plot No. D-2/CH-82, GIDC Estate- Amendment) Dahej-II, Taluka Vagra, District- Bharuch

Category of the unit : 5(f) Project status: Amendment – EC

• SEIAA, Gujarat has accorded Environment Clearance to M/s. Gumandev Chemicals Pvt. Ltd vide letter no. SEIAA/GUJ/EC/5(f)/1038/2018 vide dated: 01/10/ 2018. • Now, project proponent has applied online vide proposal no. SIA/GJ/IND2/17426/2019vide dated 01/02/2019 for Amendment in EC. • PP has applied for Amendment in EC as mentioned below: Sr. Condition As per EC As per proposed Justification no. no. in which amendment changes

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proposed.

1 Total water Total water requirement: Due to availability of requirement: 186 KLD 186 KLD RO permeate of 40 Cond. 8 Fresh: 150 KLD Fresh: 146 KLD KLD Reuse : 36 KLD Reuse : 40 KLD 2 Process effluent to Industrial effluent shall ° Higher capital treat in stripper (Cap. be treated in ETP cost but lower 200KLD) followed by comprising of advance operation cost. MEE (Cap. 200KLD) physico-chemical ° Better and other effluent shall treatment followed by treatability of effluent Cond. 11, be treated in advance biological and easy to achieve 12 & 13 conventional ETP (MBR) process followed discharge norms for (Cap. 200KLD) along by tertiary treatment and disposal into GIDC with MEE condensate. reverse osmosis. pipeline Cap. of RO : 60 KLD Cap. of ETP: 200 KLD Cap. of RO : 70 KLD 3 Cond. 31 ETP sludge: 20 TPA ETP sludge : 120 TPA There will be no MEE MEE Salt : 650 TPA salt generation. • During the meeting dated 30/07/2019, technical presentation made during the meeting by project proponent. • As per existing EC, entire quantity of effluent will be treated in ETP followed by RO and stripper followed by MEE.Treated effluent will be partially reused and balance quantity will be disposed to common disposal system of GIDC after achieving prescribed norms. • Now, as per EC amendment, entire quantity of effluent will be treated in proposed advanced ETP followed by RO.Treated effluent will be partially reused and balance quantity will be disposed to common disposal system of GIDC after achieving prescribed norms. • Committee noted that there will be no change in total water consumption, wastewater generation, flue gas emission, process gas emission and product profile. • Committee deliberated on the proposed advanced ETP, characteristics of stream wise effluents. • After deliberation, SEAC unanimously decided to consider the proposal after submission of the following details. 1. Technical feasibility and treatability of ETP to remove COD, Ammonical nitrogen, etc. considering high TDS of effluent.

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2. ETP stage wise reduction of pollutants. • PP submitted reply of above query and this case was reconsidered in SEAC meeting dated 01/10/2019. • During SEAC meeting dated 01/10/2019, technical expert of PP informed that they have submitted feasibility report to remove COD and Ammonical nitrogen considering high TDS effluent. Committee asked about stage wise reduction of pollutants in ETP and its adequacy, technical expert of PP informed that they will install advanced primary treatment and MBR for secondary treatment scheme for reduction of COD parameters in case of high TDS effluent with 99% efficiency. PP deliberated in details regarding stage wise characteristicc of reduction of pollutant like COD and TDS. Committee asked about Ammonical nitrogen reduction, PP informed that anoxic tank in ETP provided for reduction of ammonical nitrogen.PP also informed regarding change in ETP sludge and MEE salt generation quantity and revised detail showing only ETP sludge generation quantity increase from 20 MTA to 120 MTA and MEE salt generation is nil.

• In view of the facts stated above, Committee decided to recommend the project to SEIAA Gujarat for grant of above mentioned amendment in EC issued to this unit vide letter no. SEIAA/GUJ/EC/5(f)/1038/2018 vide dated: 01/10/ 2018.

19. SIA/GJ/IND2/36957/2019 M/S. DHARTI ENTERPRISE EC -Corrigendum Plot No. D-2/CH-326 of GIDC Dahej - II ,Taluka: Vagra, District: Bharuch .

Category of the unit : 5(f) Project status: EC-Corrigendum

• SEIAA, Gujarat has accorded Environment Clearance to M/s. Dharti Enterprise vide letter no. SEIAA/GUJ/EC/ 5(f)/639/2019 Dt. 03/05/2019. • Now, project proponent has applied online vide proposal no. SIA/GJ/IND2/36957/2019dated 01/02/2019 for corrigendum in EC. • PP has applied for Amendment in EC as mentioned below: Sr. Conditio As per EC As per Justification no. n no. in proposed which amendment changes propose d. 1 Cond. 12 “Total water requirement “Total water Fresh water : 113.5 KLD

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for the project shall not requirement for Reuse water : 30 KLD exceed 113.5 KLD . Unit the project shall Total water requirement: 143.5 KLD shall reuse 30 KLD, not exceed 143.5 Hence, fresh water KLD. Unit shall requirement shall not reuse 30 KLD, exceed 113.5 KLD and it Hence, fresh shall be met through water GIDC water supply only. requirement shall Prior permission from not exceed 113.5 the concerned authority KLD and it shall shall be obtained for be met through withdrawal of water.” GIDC water supply only. Prior permission from the concerned authority shall be obtained for withdrawal of water.”

To install Cyclone To install Cyclone Moreover, TFH to be installed is equivalent separator followed by separator with to 0.83 TPH, hence, no venture scrubber venture scrubber with TFH TFH of 5.0 Lac is required to install. of 5.0 Lac Kcal/Hour as an Kcal/Hour as an APCM. APCM.

• During the meeting dated 01.09.2019, technical presentation made during the meeting by project proponent along with technical expert. • PP presented justification for above mentioned points. • Total water requirement for the project was shown 143.5 KLD in original application. • Committee noted that fuel consumption in TFH is coal – 2.4 MT/Day or Biofuel (Agrowaste) – 2.6 MT/Day. • In view of the facts stated above, Committee decided to recommend the project to SEIAA Gujarat for grant of above mentioned amendment in EC issued to this unit vide letter no. SEIAA/GUJ/EC/ 5(f)/639/2019 Dt. 03/05/2019.

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Meeting ended with thanks to the Chair. Minutes approved by:

1. Dr. Dinesh Misra, Chairman, SEAC

2. Shri S. C. Srivastav, Vice Chairman, SEAC

3. Shri Rajesh. I. Shah, Member, SEAC

4. Shri V. N. Patel, Member, SEAC

5. Dr. V. K. Jain, Member, SEAC

6. Shri A. K. Mule, Member, SEAC

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