Minutes of the 575Thmeeting Ofthe State

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Minutes of the 575th meeting ofthe State Level Expert Appraisal Committee(SEAC) held on 17/12/2019 at Committee Room, Gujarat Pollution Control Board, Sector 10A,Gandhinagar.

The 575th meeting of the State Level Expert Appraisal Committee (SEAC) was held on 17 th December 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 V. N. Patel, Member, SEAC 4. Shri. R. J. Shah, Member, SEAC 5. Shri Rajesh. I. Shah, Member, SEAC 6. Shri A. K. Muley, Member, SEAC

The regular agenda of Appraisal, Screening & Scoping/ToR – reconsideration, EC – Amendment, EC – Corrigendum 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

6 SIA/GJ/IND2/45092/2019 M/s. Krufren Pharma Appraisal Plot No: C/251, GIDC Saykha, Vagra, Bharuch. Category of the unit : 5(f) Project status: Expansion

• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/45092/2019dated 13/11/2019 for obtaining Environmental Clearance. • SEIAA issued TOR to PP vide their letter dated 24/05/2019. • Project proponent has submitted EIA Report prepared by Aqua Air Environmental Engineers Pvt Ltd, Ahmedabad based on the TOR issued by SEIAA. • This is an expansion project for manufacturing of synthetic organic chemical as tabulated below. Sr. Name of the Products CAS no. /CI no. Quantity End -use of the products No. MT/Month 1 Nabivilol 152520-56-4 1.0 Beta-Blocker 2 Zonisamide 68291-97-4 10.0 Anti Depression 3 Fluconazole 86386-73-4 10.0 Antifungal Medication

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4 Loratadine 79794-75-5 1.0 Anti Depression 5 Glimepride 93479-97-1 1.0 Anti Diabetic Amiodarone 6 1951-25-3 10.0 Irregular Heartbeats Hydrochloride

7 Cilostazol 73963-72-1 10.0 Intermittent Claudication

8 Apripitant 170729-80-3 10.0 Antiemetic

Sevelamer 9 152751-57-0 10.0 A Noncalcemic Phosphate Binder Hydrochloride

Nicardipine 10 54527-84-3 1.0 Calcium Channel Blockers. Hydrochloride

11 Amlodipine Besilate 111470-99-6 10.0 Calcium Channel Blockers.

12 Glibenclamide 10238-21-8 10.0 Anti Diabetic

13 Desloratadine 100643-71-8 1.0 Antihistamine

Venlaflaxine 14 99300-78-4. 10.0 Antidepressant Hydrochloride

15 Telmisartan 144701-48-4 10.0 Anti Hypertension

16 Pregabalin 148553-50-8 10.0 Anxiety Disorders

17 Febuxostat 144060-53-7 10.0 Hyperuricemia.

18 Vildagliptin 274901-16-5 10.0 Anti Diabetic

19 Valsartan 137862-53-4 10.0 Anti Hypertensive

20 Topiramate 97240-79-4. 1.0 Antiepileptic

21 Ropivacine 132112-35-7 1.0 Local Anesthetic

22 Pedotimode 121808-62-6 1.0 Anti Neoplastic

-- 23 R&D 1.0 For R & D Purpose

Total 149 • The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.

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• PP was called for presentation in the SEAC meeting dated 17/12/2019. • Salient features of the project are as under: Sr. no. Particulars Details A A Total cost of Proposed Project 4.0 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 (2019-20) Month)

Cost Rs. 234.4 Lakhs Rs. 29.71 Lakhs

Bifurcation of EMP Cost Sr. Unit Installed Capital Operating Maintenance Total No Capacity Cost Cost Cost Recurring (KLD) (Rs. in (Lacs/Month) (Lacs/Month) Cost Lakhs ) (Lacs/Month) 1 Effluent 42.05 KLD 200.0 18.73 0.35 19.08 Treatment Plant 2. APCM -- 11.0 -- 0.1 0.1 3. Hazardous -- 8.75 10.36 -- 10.36 Waste (Expense) 4. AWH -- 10.0 -- 0.125 0.125 Monitoring Cost 5. Greenbelt -- 4.65 -- 0.041 0.041 Total 234.4 29.09 0.616 29.706

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), greenfield projects have to contribute 2% of the Additional Capital Investment, the company

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will contribute Rs. 8.0 Lakhs as funds for CER activities Component As per Norms Allocation CER Rs. 8.0 Lakhs (2 %) Rs. 8.0 Lakhs (2 %)

Activities to be carried out under CER: CER Activities Fund (Rs.) Provision & Installation of Water Cooler at Saykha Village 4,00,000 Provision & Installation of Water Cooler at Argama Village 4,00,000 Total 8,00,000/-

B Total Plot area ( sq. meter) 4000 Sq. m. Green belt area 1200.0 Sq. m. ( sq. meter) C Employment generation 30 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/DEE/(WS)/BRH/561 ii Water consumption (KLD) Category Quantity Remarks KLD (A) Domestic 2.0 (B) Gardening 1.5 (C) Industrial Process 28.0 Washing 2.0 Boiler 15.0 Cooling 5.0 Scrubber 2.0 R&D 0.026 Industrial Total 52.026 Total (A + B + C) 55.526

1) Total water requirement for the project: 55.526 KLD 2) Quantity to be recycled : 34 KLD 3) Total fresh water requirement: 21.526 KLD

575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 4 of 178 iii Waste water generation (KLD) - Category Waste water Remarks KLD (A) Domestic 1.5 (B) Industrial Process 33 Low COD & TDS: 23 KLD High COD & TDS: 10 KLD Washing 1.5 Boiler 1.5 Cooling 0.5 Scrubber 2.8 Reuse and sell under rule-9 permission (C) R&D 0.025 Total Industrial 39.325 waste water Total [A + B + C] 40.825

iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ ETP (Primary, Secondary, Tertiary) & RO: 26.525 KLD ‹ MEE + Solvent Stripper : 15.525 KLD Treatment scheme including segregation at source. ‹ Low COD & TDS effluent from Process, Boiler, Cooling and Washing will be treated in ETP (Primary, Secondary, Tertiary & RO treatment. ‹ High COD & TDS effluent from process will be treated in-house MEE. 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 water requirement will be 55.526 KLD. Total reuse water will be 34.0 KLD from RO

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Permeate and MEE Condensate. Hence approximately 61.0% treated water will be reuse. v Mode of Disposal & Final meeting point Domestic: Disposal through soak pit/ septic tank Industrial: For Low COD & TDS: ETP consisting of Primary, Secondary, Tertiary & RO treatment. Treated effluent will be reuse. For High COD & TDS: ETP consisting of Primary treatment followed by MEE+ Solvent Stripper treatment. MEE condensate will be reuse. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF NA Membership of Common facility (CF) (For waste water treatment) Ref No.: BEIL/ANK/2019, dated 18/03/2019 vii Simplified water balance diagram with reuse / recycle of waste water

viii Reuse/Recycle details (KLD) Total reuse: 0 KLD

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Source of waste water for Application area with Characteristics of waste water to be reuse with quantity in KLD quantity in KLD (Where reused (COD, BOD, TDS etc.) (From where it is coming) it is used)

RO Permeate: 21.0 KLD Process: 21.0 KLD COD: 80 mg/l BOD: 25 mg/l TDS: 200 mg/l MEE Condensate: 13.0 KLD Boiler: 13.0 KLD COD: 150 mg/l BOD: 50 mg/l 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. -Proposed Source of Air Pollution Stack Quantity of Type of Sr. emission Control Height Type of Fuel Fuel emissions i.e. no. With Measures (meter) MT/Day Air Pollutants Capacity (APCM) SPM Multi Cyclone Briquettes of Boiler (2.0 3/2/2000 SO 2 Separator with 1 30 Biocoal/Coal/Nat TPH) SCM /Day NO x Bag Filter + ural Gas water Scrubber SPM Multi Cyclone

Thermo Briquettes of SO 2 Separator with 3/2/2000 2 Pack (1.0 30 Biocoal/Coal/Nat NO x Bag Filter + SCM /Day lakhs kcal/hr) ural Gas Water Scrubber SPM D. G Set Adequate stack 3 11 HSD 0.05 SO 2 (100 KVA) Height 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 Air Pollution Control Sr. emission Type of Stack/Vent Measures no. (Name of the emission Height (meter) (APCM) Product &Process)

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Process Vent 1 (Source: Loratadine HCl 11 Two stage Water scrubber Process) Process Vent

2 (Source: Loratadine SO 2 11 Two stage Alkali scrubber Process) Process Vent

3 (Source: Topiramate NH 3 11 Two Stage Acid Scrubber Process)

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. 2. Adequate ventilation will be provided. 3. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions. 4. Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature. 5. Periodic monitoring of work area will be carried out to check the fugitive emission. 6. Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with online pH meter with hooter system for better operational control. 7. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers. 8. Minimum number of flanges, joints and valves in pipelines. 9. Regular inspection of floating roof seals and proper preventive maintenance of roofs and seals for tanks. 10. Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area will be collected through hoods and ducts by induced draft and controlled by scrubber/ dust collector. 11. Dedicated scrubber will be provided are used for fugitive emissions to control. 12. For dust emissions bag filter will be provided. 13. 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. F Hazardous wastes

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(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type/Name of Specific Source Category Quantity Management of HW no. Hazardous waste of generation and (MT/Annum (Name of the Schedule as ) Activity, per HW Product etc.) Rules. Collection, Storage, Transportation and sent for co- Glibenclamide Schedule-(I)- 1 Process Waste 37.56 processing in Process (28.1) cement industries or Disposal at common incineration site. Collection, Storage, Transportation and Schedule-(I)- 2 ETP Sludge ETP Treatment 84.0 Disposal at common (35.3) TSDF Site of M/s. BEIL, Dahej. Collection, Storage, Discarded Decontamination, Raw Material and Schedule-(I)- 3 Drums/Containers/B 2880 Reuse, Transportation Storage (33.1) ags and sale to authorized vendor. Collection, Storage, From Moving Schedule-(I)- Transportation, Reuse 4 Used Oil 9.6 Machineries (5.1) and sale to authorized recycles. Collection, Storage, Transportation and Ropivacaine Schedule-(I)- 5 Spent carbon 24.0 Disposal to TSDF Process (28.3) site of M/s. BEIL, Dahej.

Schedule-(I)- Collection, Storage 6 Spent Solvent Process 9120 (28.6) and reuse within

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premises after distillation.

Collection, Storage, Transportation and sent for co- Schedule-(I)- 7 Distillation Residue Distillation plant 432 processing in (20.3) cement industries or sent to common incineration site. Collection, storage and reuse in Schedule - 8 Dil. HCl (30%) Scrubber 414.2 Zonisamide process (II)-B15 (Reqd. qty 900 MT/Annum) Collection, Storage, Transportation and Sodium Sulphite Schedule - 9 Scrubber 500.0 Sell to end users (28%) (II)-B36 Having permission Rule-9

Collection, Storage, Transportation and Schedule -(I)- 10 Salt from MEE MEE Process 360 Disposal to TSDF (35.3) site of M/s. BEIL, Dahej.

Solvent Stripper Schedule-(I)- Collection, Storage, 11 Solvent Stripper 288 Residue (35.3) Transportation and sent for co- processing in Off Specification Schedule-(I)- cement industries or 12 Batch fail 12 Product (28.4) Disposal at common incineration site.

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Collection, storage and reuse in Liq. Ammonia Schedule - 13 Scrubber 102 Zonisamide process (20%) (II)-B36 (Reqd. qty 750 MT/Annum)

Topiramate Schedule-(I)- Collection, Storage, 14 Sodium sulphate 57.24 Process (28.1) Transportation and Sell to end users Ropivacine Schedule-(I)- 15 Sodium chloride 74.28 Having permission Process (28.1) Rule-9

- ii Membership details of TSDF, CHWIF etc. BEIL, Dahej (For HW management) 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.

Boiling Vapor Input Output Solvent Loss % Recovery % Loss Point ( 0C) Pressure (MT) (MT) 400 mm Hg Acetone 56.5 86.54 85.38 1.16 98.66 1.34 @ 39.5 0C 100 mm Hg EDC 83.47 122.5 117.89 4.61 96.24 3.76 @ 30 0C Ethyl 91 mm Hg 77.1 100 96.45 3.55 96.45 3.55 Acetate @ 25 0C 44 hPa @ IPA 82 316.67 305.8 10.87 96.57 3.43 20 0C 400 mm Hg MDC 39.6 620.4 595.32 25.08 95.96 4.04 @ 24.1 0C 128 hPa @ Methanol 64.5 200 195.56 4.44 97.78 2.22 20 0C 22 mm Hg Toluene 111 612.5 585.05 27.45 95.52 4.48 @ 20 0C Xylene 138.4 8.3 mm Hg 132.31 127.87 4.44 96.64 3.36

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@ 25 0C

ii VOC emission sources and its mitigation measures During operation stage, leakage through valves/pumps, leakage and emission from open drum containing chemicals, open feeding, storage tanks, etc. will be major sources of fugitive emissions and VOCs. Excess use of solvent/s may also results fugitive emission from the process vessels. • Solid raw material charging will be done through closed system. • Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature. • Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers. • Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area, will be collected through hoods and ducts by induced draft and controlled by scrubber/dust collector. • Emphasis will be given to solvent management/solvent loss prevention. • Control by having proper scrubbing system. • Condenser to trap VOC. • 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. • Proper maintenance schedule will be adhered to avoid emissions through flange joints, pump seals etc. • Minimum number of flanges, joints and valves in pipelines. • Proper gland packing will be maintained for pumps and valves and to the extent possible pumps with mechanical seal. • All the raw materials will be pneumatically transfer to the reactor. • All rotating equipments like pumps will be installed with mechanical seals to arrest any sort of emissions. • A regular preventive maintenance schedule will be in place to replace or rectify all gaskets and joints etc. as a part of ISO systems to ensure no fugitive emissions take place. • Periodic monitoring of work area will be carried out to check the fugitive emission. • Solvent tank vents will be connected to vent chillers. • Adequate ventilation will be provided. • Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures.

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• Breather valves will be provided on solvent tanks. • During the meeting dated 17/12/2019, 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. • The baseline environmental quality has been assessed for various components of the environment viz. air, noise, water, biological and socioeconomic aspect for the study area of 10 km radial distance from project site for the period October 2018 to December2018. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOX, O3, Pb, NH3, CO, C6H6, BaP, As, Ni, HCL, CO & VOCs 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 ISCST – 3. 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 on 17/12/2019, committee noted that the proposal is for expansion. This unit has valid CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP ensured that there are no court cases pending and no public complaints against the project. Source of water is GIDC. Committee noted that PP has not addressed CER properly as per Specific ToR granted. Further referring to the EIA report it was noted that PP has not covered water sampling as per Water Quality Monitoring Guidelines, 2017 of CPCB. Further committee noted that PP has omitted Specific ToR No. 5 & 6 in the EC – Appraisal Presentation presented before the Committee. Committee noted that EIA consultant has taken very casual approach for EC – Appraisal presentation. • After detailed discussion, Committee unanimously decided to defer the proposal and call back the project proponent for the presentation with all the proper technical details and justification related to Air, Water & Hazardous Waste and with proper compliance of all ToR granted by SEIAA, Gujarat 7 SIA/GJ/IND2/44632/2018 M/s. Jaksh Castor Products Pvt Ltd Appraisal Survey No. 1242, At- Gajera, Opp. Savana Ceramic, Jambusar, Bharuch. Category of the unit : 5(f) Project status: New

• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/44632/2018 dated 13/11/2019 for obtaining Environmental Clearance. • SEIAA issued TOR to PP vide their letter dated 19/06/2019.

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• Public Hearing of the Project was carriedout by Gujarat Pollution Control Board on 25/09/2019at Project Site of M/s. Jaksh Castor Products Pvt Ltd , Survey No. 1242, At- Gajera, Opp. Savana Ceramic, Ta: Jambusar, Dist: Bharuch. • Project proponent has submitted EIA Report prepared by Shree Green Consultancy, Surat based on the TOR issued by SEIAA. • This is a new unit proposes for manufacturing of Synthetic Organic Chemical as tabulated below:

Sr. CAS no. /CI Quantity End-use of Name of the Products No. no. MT/Month product

Hydrogenated Vanaspati oil (530 as per (Hydrogenated castor oil or other granted Manufacturing of 1 8001-78-3 hydrogenated Vanaspati oil) CCA+ 670) Grease = 1200.00

12-Hydroxy Stearic Acid Manufacturing of 2 106-14-9 Grease 1000.00 Ricinolic Acid Manufacturing of 3 141-22-0 Lubricating oil

Dehydrated Castor Oil Manufacturing of 4 64147-40-6 500.00 Paint

2700.00

• 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 17/12/2019. • Salient Features of the project including Water, Air and Hazardous waste management:

Sr. Particulars Details no.

A Total cost of Proposed Project 4.50 Crores (Rs. in Crores):

EMP details (Capital cost & Recurring cost)

Brief details of EMP

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

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Total Cost Rs. 50 Lakhs Rs. 12 Lakhs

Bifurcation of EMP Cost

Sr. Unit Capital Cost Operating Maintenance Total No. (Rs. in Lakhs) Cost Cost Recurring Cost

(Lacs/Month)

1 Air Pollution Control 10 2.5 0.5 3

2 Water Pollution Control 25 4.15 0.83 4.98

3 Noise Pollution Control 1 0.5 0.1 0.6

4 Environment Monitoring and waste 5 1.25 0.25 1.5 Management

5 Rain Water Harvesting 2 0.2 0.04 0.24

6 Occupational Health 3 0.5 0.1 0.6

7 Green Belt 2 0.4 0.08 0.48

8 Fire Safety & 2 0.5 0.1 0.6 Equipment

TOTAL 50 10 2 12

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), Greenfield projects have to contribute 2% of the Additional Capital Investment, the company will contribute Rs. 10.0 Lakhs as funds for CER activities Year wise budget (Rs. in Lacs) for CER Sr. CER – Proposed planned Identified Activities No. Activities villages 1st 3rd Grand 2nd Year Year Year Total Free Note book and stationary Nearby schools accessories and smart Board 1 of Gajera 1.7 1.5 1.6 4.8 facilities distribution in nearby village.. schools of Gajera village.

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Drinking water facility and In Uchachhad 2 0.8 0.8 0.6 2.2 sanitation village Free medicines to needy patients coming to the health 3 In Masar village 1.3 0.9 0.8 3.0 centre at Masar Charitable Hospital.

Year Wise Total (Rs in Lacs) 3.8 3.2 3.0 10.0

B Total Plot area (sq. meter) 5128.02

Green belt area 1692.00 (sq. meter)

C Employment generation 40

D Water i Source of Water Supply Tanker and bore well (GIDC Bore well, Surface water, Tanker supply etc...)

Status of permission from the concern authority. Application has been made to CGWA ii Water consumption (KLD)

Category KL/day Remark (D) Domestic 2.0 (FW) TW: Treated Water (E) Gardening 0.5 (TW) FW: Fresh Water (F) Industrial 10.0 (4.50 TW + 5.50 FW) Process 3.50 (FW) Washing 2.00 (FW) Boiler 4.00 (TW) Cooling 0.50 (TW) Others 0.0 Total (A+B+C) 12.5 (5.00 TW + 7.50 FW) 1) Total water requirement for the project: 12.5KLD 2) Quantity to be recycled: 5.0 KLD 3) Total fresh water requirement: 7.5 KLD

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iii Waste water generation (KLD)

Category Existing KL/Day Remarks

(D) Domestic 1.60 - (E) Industrial 22.90 - Process 20.50 - Washing 2.00 - Boiler 0.40 - Cooling 0.00 - Others 0.00 - Total Industrial waste water 24.50 - - iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ Domestic waste water (1.6 KLD) will be disposed off through septic tank followed by soak pit ‹ Industrial effluent (22.9 KLD) will be neutralized in a neutralization tank with caustic lye to increase the pH level to the range of 7 – 8 and it will be sent in-house MEE plant and MEE condensate (5.0 KLD) will be reused. Neutralization tank for 22.9KLD will be constructed, working capacity of neutralization tank shall be 35 KLD.

Treatment scheme including segregation at source. ‹ Domestic waste water (1.6 KLD) will be disposed off through septic tank followed by soak pit ‹ Industrial effluent (22.9 KLD) will be neutralized in a neutralization tank with caustic lye to increase the pH level to the range of 7 – 8 and it will be sent in-house MEE plant and MEE condensate (5.0 KLD) will be reused. Neutralization tank for 22.9KLD will be constructed, working capacity of neutralization tank shall be 35 KLD.

Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ v Mode of Disposal & Final meeting point

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Domestic: Generated domestic waste water will be treated through soak pit followed by septic tank.

Industrial: Generated effluent will be send to in-house MEE and MEE condensate will be reused. vi In case of Common facility (CF) like CETP, Common SSpraypray dryer, Common MEEMEE etc. Name of CF ‹ None

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

vii Simplified water balance diagram with reuse / recycrecyclele of waste water

viii Reuse/Recycle details (KLD)

Total reuse 5.00 KLD Source of waste water Application area with Remarks regarding feasibility to

575 th meeting of SEAC -Gujarat, dated 17.12.2019 Page 18 of 178 for reuse with quantity quantity in KLD reuse i.e. w/w characteristics in KLD (COD, BOD, TDS etc.) 1,2-hydroxy stearic acid Generated effluent will be send to or Ricinolic acid MEE and MEE condensate shall be 3.5 KLD reused in the manufacturing of 1,2- pH 6.5-85 hydroxy stearic acid or Ricinolic TDS (mg/l) < 600 acid COD (mg/l) < 100 From washing: Generated effluent will be send to BOD (mg/l) < 30 2.0 KLD MEE and MEE condensate shall be SS (mg/l) < 25 reused for washing and gardening purpose Boiler: 0.4 KLD Generated effluent will be send to MEE and MEE condensate shall be reused for cooling purpose

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 Quantity of Type of SR. Stack Name of emission Fuel MT/hr & APCM emissions i.e. no. Height (meter) the fuel With Capacity MT/Day Air Pollutants

1 Boiler 1 (2 TPH) SPM Thermopack (4 11 Coal 10 MTPD Bag Filter SO2 2 lac Kcal) NOx

SPM D.G.SET Adequate 3 9 LDO/HSD 2.0 KLD SO2 (250 KVA) Height NOx

- 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 Control emission Type of Stack/Vent Sr. no. Measures (Name of the Product & emission Height (meter) (APCM) Process)

1 - - - -

iii Fugitive emission details with its mitigation measures: As below: • Minimum number of flanges, joints and valves in pipelines • Selection / use of state-of-the art leak proof valves • Provision of mechanical seals in pumps • Proper preventive maintenance of roofs and seals for tanks Monitoring and preventive maintenance of valves, flanges, joints, etc. • Fugitive emission over reactors, formulation areas , centrifuges, chemical loading, transfer area, shall be collected through hoods and ducts by induced draft and controlled by dust collector. • For particulate / dust emissions from the coal handling system: Water will be sprinkled to control particulate / dust emission from coal storage area.

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

Category and Type/Name of Sr. Source of Schedule as Management Hazardous Quantity no. generation per HW of HW waste Rules.

Used or spent oil will be collected, stored and reuse as lubricants in Equipment’s and 1 Used Oil 5.1 0.003 the machineries within plant machineries the premises or sent to authorized re- processors.

Discarded Raw material Discarded barrels/ 2 34.3 180 Bags storage containers/ liners will be

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collected, stored, transported & sent to authorized GPCB vendors after decontamination

Collection, Storage, 3 Fly Ash Boiler 33.1 35 transportation to brick manufacturing.

will be sold or sent to 4 Glycerin 12-Hydroxy 42.2 authorized vendor Stearic acid or 34.3 Will be sold or sent to 5 Sodium salt Ricinolic acid 85.2 authorized vendor

Hydrogenated Spent Nikel castor oil or other Will be sold or sent to 6 28.1 3.6 Catalyst hydrogenated authorized vendor vanspati oil

Collection, Storage, 7 MEE Salt MEE plant 33.1 280 transportation and sent to TSDF site.

ii Membership details of TSDF, CHWIF etc. Will be obtained (For HW management) iii Details of Non-Hazardous waste & its disposal None (MSW and others)

G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.

‹ No Solvent shall be used in the process ii VOC emission sources and its mitigation measures

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• Solid raw material charging will be done through closed system. • Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature. • Proper maintenance schedule will be adhered to avoid emissions through flange joints, pump seals etc. • Minimum number of flanges, joints and valves in pipelines. • Proper gland packing will be maintained for pumps and valves and to the extent possible pumps with mechanical seal.

H Details regarding storage of Hazardous Chemicals

Storage details Name of major Hazardous chemicals Remarks Storage Tanks Sulphuric acid

Bank Hydrogen gas

 Applicability of PESO: NA

• During the meeting dated 17/12/2019, technical presentation made by the Project proponent. • During the meeting, the project was appraised based on the information furnished in the EIA Report, Public hearing proceedings 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 for the study area of 10 km radial distance from project site for the period March 2019 to May 2019. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, CO & VOCs at eightlocations, including the project site. Values conform to the prescribed standards for Ambient Air Quality. The incremental Ground Level Concentration (GLC) has been computed using ISCST3. 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. • Committee noted that unit is located outside GIDC, Complying the three conditions as per the amendment with EIA Notification, 2006 vide SO 1599 (E) dated 25/06/2014. [The Water consumption less than 25 m3/day (12.5 KLD); Fuel consumption is less than 25 TPD (10 MT/day); and not covered in the category of MAH units

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as per the Management, Storage Import of Hazardous Chemical Rules (MSIHC Rules), 1989]. • Committee noted that this proposal is new in Village: Gajera.PP mentioned that source of Water is Bore well/Tanker. Committee noted that the project proponent has obtained ToR as New Project however the proposal is for expansion as unit has obtained valid CC&A from GPCB and asked PP to clarify the same. • PP mentioned that they had applied for ToR dated 20/10/2018. • Presentation was made before SEAC dated 18/12/2018. The deliberation in the meeting dated 18/12/2018 is as follows: ‹ “Committee felt that these products does not falls under the 5(f) category i.e. Synthetic organic chemicals industry (dyes & dye intermediates; bulk drugs and intermediates excluding drug formulations; synthetic rubbers; basic organic chemicals, other synthetic organic chemicals and chemical intermediates) ‹ Referring to the product profile, committee noted that the proposal does not attract provision of EIA Notification 2006 and hence unanimously decided to recommend for delisting of the proposal as it does not attract provision of EIA Notification 2006. ‹ In view of the above, Committee decided to delist the proposal from the list of pending applications & to close the file.” ‹ The case was referred back by SEIAA, Gujarat vide Letter No. SEIAA/GUJ/ToR/212/2019 dated 29/01/2019 for the following reasons: “To verify the applicability of EIA Notification, 2006.” ‹ PP made reply to the above mentioned query dated 11/03/2019 as follows. ‹ “PP submitted expert opinion on product profile by Dharmsinh Desai University stating that all proposed product involved simple unit operations where castor oil along with hydrogen, caustic soda and sulphuric acid is used. The operations involved simple mixing and blending at certain temperatures followed by drying and packing. In view of the above all it is confirmed that characteristic of the proposed product does not come under any category of the schedule/list of projects or activities requiring prior environmental clearance.” ‹ The deliberation in the SEAC meeting dated 10/04/2019 is as follows: ‹ “Committee noted that the process involves synthesis, however, no any carbon molecule transfer takes place, but bond breakage takes place and a new molecule and external heat are also supplied and pressure is also maintained in the reaction chemistry hence the process involves synthesis which comes 5 (f) category of EIA Notification, 2006. After deliberation, Committee was of the view that the expert opinion given by Dharmsinh Desai University is not acceptable.” ‹ PP was accorded ToR by SEIAA, Gujarat vide Letter No. SEIAA/GUJ/TOR/5(f)/925/2019 dated 19/06/2019. ‹ PP mentioned that CC&A for Hydrogenated Vanaspati Oil with Quantity 530 MT/Month was granted by GPCB dated 28/12/2018 which is Non EC Product.

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• In view of the above, as the ToR application was done before CC&A was applied and granted by GPCB this project was considered as new project instead of expansion. • PP mentioned that effluent generated from process, washing, boiler blow down & cooling tower blow down will be treated in proposed in-house Primary ETP followed by MEE, and Condensate of MEE will be reused by mixing with fresh water while Reject/Salt will be disposed at approved TSDF. Committee asked PP to Justify direct salt generation from MEE without ATFD however PP could not satisfactorily explain the same. Committee asked PP to submit application status made to CGWA for withdrawal of Ground Water along with Recharge & Rain Water Harvesting Plan however PP was not able to submit the same. Committee noted that PP has not presented proper reply to the issue raised during Public Hearing and asked to submit the same in tabular form. PP has proposed one steam boiler & one Thermic Fluid Heater. Fuel used will be Coal. PP has not addressed Hazardous Waste as per HWR – 2016. • After detailed discussion, it was decided to consider the project only after satisfactory submission of the following details. 1. 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. 2. Compliance of issues raised during Public Hearing in Tabular Form and current status of compliance. 3. Proper Justification as to why this Proposed Project should be considered as “New Project/Activity” instead of “Expansion” 4. Technical Justification of MEE Salt Generation without ATFD by Justifying the Quantity of MEE Salt in Hazardous Waste Matrix. 5. Need Based CER & EMP along with Fixed Capital Cost and Recurring Cost. 6. Compliance of CC&A granted by GPCB with Consent Order No. AWH-33560 dated 28/12/2018. 8 SIA/GJ/MIS/38296/2019 M/s. Bio Waste Management Service ToR – Reconsideration Plot No: 1, S.No.368 at Tupani , Devbhoomi – Dwarka. Category of the unit: 7(da) Project status: New

• This office has received an application vide their online proposal no. SIA/GJ/MIS/38296/2019 dated 26/07/2019 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.

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• This is new unit proposes for Common Bio-Medical Waste Treatment Facility (CBWTF) tabulated as below: Sr. no. Name of the Activity at CBWTF Quantity Remarks MT/Day

1 Incineration Plant 2500 125 Kg/Hr 2 Autoclave 2000 100 Kg/Hr/Cycle(20 Cycle) 3 Shredder 3000 150 Kg/Hr. • The project falls under Category B of project activity 7(da) as per the schedule of EIA Notification 2006. • PP was called for presentation in the SEAC meeting dated 01/08/2019. • Salient features of the project including Water, Air and Hazardous waste management: Sr. Particulars Details no. A Total cost of Proposed Project 2.70 Crores (Rs. in Crores): B Total Plot area ( sq. meter) 4057.00 Sq. m.

Green belt area,/Tree Plantation area 1340.00 Sq. m. ( sq. meter) C Employment generation 24 Nos

D Water i Source of Water Supply Bore Well

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

Status of permission from the concern authority. CGWA Permission Applied

ii Water consumption (KLD)

Category KLD

(G) Domestic 1.5 (H) Gardening 4.0 (I) Industrial

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Process 4.47 Washing 2.0 Boiler 0.0 Cooling 0.0 Others 0.0 Industrial Total 6.47

Total (A + B + C) 11.97

1) Total water requirement for the project: 11.97 KLD 2) Quantity to be recycle: 2.97 KLD 3) Total fresh water requirement: 9.0 KLD

iii Waste water generation (KLD)

Category Waste water Remarks KLD (F) Domestic - 1.4 (G) Industrial

Process 1.0 - Washing 2.0 - Boiler 0.0 - Cooling 0.0 - Others 0.0 - Total Industrial waste 3.0 - water Total [A + B] 4.4 - - iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..

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In-House ETP (Primary &Tertiary): 4 KL/Day Treatment scheme including segregation at source. Streams are segregated as follows: • Domestic waste 1.4 KL/Day will be generated & it will be send to septic tank/soak pit system. • Industrial waste water 3.0 KL/Day generated will be treated in in-house effluent treatment plant having primary treatment facilities. The treated water will be reused for lime slurry preparation along with fresh water to make the whole system Zero discharge. The salt generated from the bottom of reactor and ETP sludge will be sent to nearby TSDF site for final disposal. 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 (Unit is ZLD) Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Domestic waste 1.4 KL/Day will be generated & it will be send to septic tank/soak pit system. ‹ Industrial waste water 3.0 KL/Day generated will be treated in in-house effluent treatment plant having primary treatment facilities. The treated water will be reused for lime slurry preparation along with fresh water to make the whole system Zero discharge. The salt generated from the bottom of reactor and ETP sludge will be sent to nearby TSDF site for final disposal. v Mode of Disposal & Final meeting point

Domestic: Septic tank/ Soak pit

Industrial: Zero Liquid Discharge 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) TSDF – Saurashtra Enviro Projects Pvt. Ltd. (SEPPL), Kutch. vii Reuse/Recycle details (KLD) 2.97 KLD After In-House ETP Treatment will be reused in Lime Slurry Preparation 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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Source of Air Pollution Stack Quantity Sr. emission Type of Type of emissions Control Height of Fuel no. With Fuel i.e. Air Pollutants Measures (meter) MT/Day Capacity (APCM) 1 Incineration 30 LDO/ 50 - 60 SPM ≤ 50 mg/Nm3 Lime Reactor, 125 KG/HR Meter HSD lit/hr NOx ≤ 400 mg/Nm3 Air HCl ≤ 50 mg/nm3 cooled gas Hg ≤ 0.05 mg/Nm3 cooler, Total dioxins and Sodium Furans Carbonate ≤ 0.1 ng TEQ/Nm3 injection, Activated carbon injection system and Bag Filter with adequate stack height 2 D.G. Sets 11 Diesel 55 In case of emergency Adequate Stack (125 KVA- 01 Meter Liter/Hr only. height and No.) Acoustic enclosures - ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) - No any process gas emission - iii Fugitive emission details with its mitigation measures. As below: • Green belt will be developed which will help to reduce fugitive emission. • All pumps, Compressors and Agitator must be mechanically sealed. • All process pumps must be provided trays to collect probable leakage. • More weightage on selection of MOC of piping must be given to avoid leakage/spillage. • Proper system must be provided for decontamination and effective cleaning of drums. • Face mask must be provided to all workers to avoid odor nuisance. • Developing appropriate green belt.

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• Vehicular speed will be limited to reduce airborne fugitive dust. F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type/Name of Source of Category and Quantity Disposal Method no. Hazardous waste generation Schedule as per (MT/Annum) (Name of the HW Rules. Activity. Product etc.)

1 From DG Sets, Pumps, 100.0 Used as lubricant/ Used oil 5.1 Compressors Lit/Annum Burnt in Incinerator etc

2 Incineration of Authorized Land BMW Waste 110.0 filling site of M/s. Incinerator Ash 37.2 flue gas MT/Annum Detox India cleaning residue Pvt.Ltd., Kutch

3 Authorized Land Wastewater 9.0 filling site of M/s. ETP Sludge 35.3 Treatment MT/Annum Detox India Pvt.Ltd., Kutch

4 Authorized Land 64.0 filling site of M/s. Sludge Salt Reactor 37.3 MT/Annum Detox India Pvt.Ltd., Kutch

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5 Plastic Waste will be given to authorized recycler Treatment of approved by Treated 1870 Biomedical - GPCB. Biomedical Waste MT/Annum Waste Glass waste will be given to authorized recycler approved by GPCB.

6 Needle / Sharp Treatment of 0.9 waste will be Sharp Waste Biomedical - MT/Annum disposed to in- Waste house Sharp Pit.

- ii Membership details of TSDF, CHWIF etc. Detox India Pvt.Ltd., Kutch

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

• Not Applicable ii VOC emission sources and its mitigation measures

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• Not Applicable

• Technical presentation was made by the project proponent with consultant/expert En-vision Environmental Services during SEAC meeting dated 01/08/2019. • Committee noted that this proposal is for setting up of new CBWTF in Devbhoomi Dwarka district. • Aerial distance of nearest residential area of village Tupani is @ 800 m in SSW direction. • No National Parks & Reserve forests within 10 km radius. • Committee deliberated on CPCB guidelines regarding Criteria for development of a new Common Bio- Medical Waste Treatment and Disposal Facility, waste water management, Hazardous waste management, APCM etc. • While discussing regarding coverage area of the proposed CBWTF, PP informed that proposed CBWTF site will be collecting BMW from the entire western Gujarat Region i.e. Dwarka, Jamnagar & Porbandar districts will be covered for collecting, transporting, storing and disposal of Bio-Medical Waste. District wise beds booked are presented shown is following table. • Committee noted that there are two existing CBWTF in the region which are located at a distance more than 75 Km. • Referring to the revised guidelines for CBWTF published by CPCB and CPCB letter no. F. NO. B-31011/BMW (50)/2018/WM-I/18169 dated 08/03/2019, Committee was of the view that PP shall submit authentic data of available nos of Beds for the proposed CBWTF and list of member units. Committee felt that PP shall submit gap analysis done by SPCB w.r.to coverage area of the bio-medical waste generation. • After deliberation, SEAC unanimously decided to consider the proposal only after satisfactory submission of the following details. 1) Gap analysis w.r.to coverage area of the bio-medical waste generation by GPCB for assessing additional BMW treatment capacity requirement. 2) Authentic data of available nos of Beds for the proposed CBWTF. List of member units to whom your proposed CBWTF will cater. • Project proponent was called for presentation for the above mentioned query dated 04/11/2019 for the above mentioned points. • Committee during the meeting dated 04/11/2019 noted that a complaint has been received against this project/activity in SEAC vide inward no 2313 dated 04/11/2019 from MS Office SEIAA, Gujarat Vide Letter No. SEIAA/GUJ/GEN/1305/2019 dated 26/09/2019. • Committee deliberated on the complaint received and after referring to its content decided to give the copy of the complaint to the project proponent (PP) for its compliance and schedule the proposal for presentation of the project only after PP submit the compliance report of the complaint and query by SEAC in 537th Meeting dated 01/08/2019. • Project proponent was called for presentation of compliance for complaint received from CBWTF Association

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of India and Dev Bio Medical Waste Management Service along with Appeal No. 03/2013 in Appellate Authority, Forest & Environment Department, Government of Gujarat with Appellant CBWTF Association of India Versus Gujarat pollution Control Board along with query by SEAC in 537 th Meeting dated 01/08/2019 dated 17/12/2019. • PP mentioned that they have only obtained information on nos of beds and nos of health care units from GPCB in three district viz (1) Dwarka – 1488 beds in 139 health care units, (2) Jamnagar – 4156 beds in 549 health care units, (3) Porbandar – 1057 beds in 259 health care units vide letter no. GPCB/BMW-JMN- 307/528376 dated 29/11/2019 however they have not obtained Gap analysis w.r.to coverage area of the bio- medical waste generation by GPCB for assessing additional BMW treatment capacity requirement as per CPCB guidelines, 2016 for CBWTF. • Committee noted that as PP is not able to produce Gap analysis w.r.to coverage area of the bio-medical waste generation as per CPCB guidelines, 2016 for CBWTF so it cannot proceed further with this application and informed PP to obtained gap analysis from GPCB as per guidelines of CBWTF, 2016 and make a presentation of ToR after that. • After detailed discussion, it was decided to consider the project only after satisfactory submission of the following details. 1) Gap analysis w.r.to coverage area of the bio-medical waste generation by GPCB for assessing additional BMW treatment capacity requirement. 2) Compliance for complaint received from (a) CBWTF Association of India and (b) Dev Bio Medical Waste Management Service along with (c) Appeal No. 03/2013 in Appellate Authority, Forest & Environment Department, Government of Gujarat with Appellant CBWTF Association of India Versus Gujarat pollution Control Board. 3) Authentic data of available nos of Beds for the proposed CBWTF. List of member units to whom your proposed CBWTF will cater. 9 SIA/GJ/IND2/45512/2019 M/s. Prima Chemicals Screening & Scoping Plot No. C-232 to C-234, Saykha Industrial Estate Vagra, Bharuch.

Category of the unit: 5(f) Project status: New • This office has received an application vide their online proposal no. SIA/GJ/IND2/45518/2019 dated 22/11/2019 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 new unit proposes for manufacturing of synthetic organic product as tabulated below:

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Proposed SR. NO PRODUCT NAME End Use MT/Month 1. Solvent Yellow 14 2. Solvent Yellow 18 3. Solvent Yellow 72 4. Solvent Yellow 33 5. Solvent Yellow 43 6. Solvent Yellow 82 7. Solvent Yellow 107 8. Solvent Yellow 114 9. Solvent Yellow 124 10. Solvent Yellow 172 11. Solvent Blue 35 12. Solvent Blue 36 13. Solvent Blue 58 14. Solvent Blue 79 15. Solvent Blue 98 16. Solvent Blue 104 Printing and Paint Industries 17. Solvent Blue 122 250

18. Solvent Green 3 19. Solvent Green 33 20. Solvent Red 195 21 . Solvent Red 135 22. Solvent Red 111 23. Solvent Red 161 24. Solvent Red 164 25 . Solvent Red 207 26. Solvent Red 23 27. Solvent Red 24 28. Solvent Orange 60 29. Solvent Orange 63 30. Solvent Violet 13 31. Solvent Violet 14 32. Solvent Yellow 16 33. Solvent Yellow 2

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34 . Solvent Yellow 56 35. Solvent Orange 98 36. Solvent Red 19 E 37. Solvent Orange 105 38. Solvent Red 52 39. Solvent Yellow 157 40. Solvent Yellow 163 41. Solvent Yellow 93 42. 1 phenyl 3 Methyl 5 Pyrazolone 43. Para Toyl 3 Methyl 5 Pyrazolone 160 44. 1, 4 Sulpho phenyl 3 Methyl 5 Pyrazolone 45. 1,3 Metachloro 3 Methyl 5 Pyrazolone 46. 1,3 Sulpho Phenyl 3 Methyl 5 Pyrazolone 40 47. 3 Hydroxy Quinaldine 4 carboxylic Acid 25 48. Quanizarine 50 Dyes industries 49. Fast Red B/Scarlet R 25

50. 4 NAP 10 51. 5 NAP 1-Amino Anthraquinone / 1,5 Dichloro Amino Anthraquinone / 52. 30 1,8 Dichloro Amino Anthraquinone/ 1 sulpho Anthraquinone 53. Di Amino Naphthalene 30 Liquid Dyes Yellow Dyes Cherry Red PG 54. 200 Red Brown PR Printing and Paint Industries Rubine PB

Orange PR Disperse Orange 44 55. Disperse Red 167 50 Disperse Yellow 79 Total 870 • 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 17/12/2019. • Salient features of the project including Water, Air and Hazardous waste management: 575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 34 of 178

Sr. Particulars Details no. A Total cost of Proposed Project Proposed: 12.0 Cr. (Rs. in Crores): B Total Plot area Proposed: 22680.056 Sq. m ( sq. meter) Green belt area Proposed : 7485 Sq. m ( sq. meter) C Employment generation 50 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) Sr Category Water Consumption No 1. Domestic Purpose 10.0 2. INDUSTRIAL Process 235 Washing & Scrubbing 10.0 Boiler 80.0 Cooling 25.0 Total water Consumption & Generation (Domestic) 10.0 Total water Consumption & generation (Industrial ) 350.0 Total Water Requirement 360.0 Total Reuse Water 338.0 Fresh Water Requirement after Reuse 22.0

1) Total water requirement for the project: 360.0 KLD 2) Quantity to be recycle: 338 KLD 3) Total fresh water requirement: 22.0 KLD iii Waste water generation (KLD)

Sr Waste Water Category No Generation 1. Domestic 7.00

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2. INDUSTRIAL Process water 430 Washing & Scrubbing 10.0 Boiler 8.0 Cooling 5.0 Total sewage Generation (Domestic) 10.0 Total wastewater generation (Industrial) 453

Note: The generated sewage will be disposed through soak pit/septic tank. Total industrial 453 KLD Waste water generation from manufacturing Process and other ancillary operation, from which 160 KLD waste water generation from Dyes intermediates treated with primary effluent treatment ETP-1 plant followed by MEE and 120 KLD MEE Condensate Reuse and 40 KLD Discharge though in house Spray Dryer Remaining 293 KLD Waste water generation From Primary, Secondary treatment ETP-2 plant followed by MEE and in house Spray Dryer, by which is discharge though in House Spray Dryer, Hence unit has achieved ZERO LIQUID DISCHARGE iv Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ETP-1 Sr. Name of Unit Capacity Nos. No. 1 Collection Tank 100 KL 1 2 Collection Tank 80 KL 1 3 Solvent Striper 4 KLPH 1 4 Equalization tank 50 KL 2 5 Filter Press 48”(PP) 48”(PP) 1 6 Filter Press 36” (PP) 36” (PP) 1 7 Holding Tank 200 KL 2 8 MEE Plant 160 KLD 1 8 Spray Dryer 2500 LPH 1

ETP-2 Sr. Name of Unit Capacity Nos. No. 1 Collection Tank 200 KL 1

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2 Collection Tank 100 KL 1 3 Solvent Stripper 8KLPH 1 4 Primary Settling Tank 100 m 3 2 5 Aeration Tank 100 m 3 2 6 Secondary Settling Tank 100 m 3 1 7 Sludge Drying Bed 50 m 3 1 8 Filter Feed Tank 20 m 3 1 9 Activated Carbon Filter 20 m 3 1 8 MEE 300 KLD 1 9 MEE Reject Tank 80 KL 1 10 In house Spray Dryer 4000 LPH 1

Treatment scheme including segregation at source. ETP-1

ETP-2

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 . ‹ Total industrial 453 KLD Waste water generation from manufacturing Process and other ancillary operation, from which 160 KLD waste water generation from Dyes intermediates treated with primary effluent treatment ETP -1 plant followed by MEE and 120 KLD MEE Condensate Reuse

575 th meeting of SEAC -Gujarat, dated 17.12.2019 Page 37 of 178 and 40 KLD Discharge though in house Spray Dryer ‹ Remaining 293 KLD Waste water generation From Primary, Secondary treatment ETP-2 plant followed by MEE and in house Spray Dryer, by which is discharge though in House Spray Dryer, Hence unit has achieved ZERO LIQUID DISCHARGE Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Not applicable v Mode of Disposal & Final meeting point Domestic: The generated sewage will be disposed through soak pit/septic tank. Industrial: Total industrial 453 KLD Waste water generation from manufacturing Process and other ancillary operation, from which 160 KLD waste water generation from Dyes intermediates treated with primary effluent treatment ETP-1 plant followed by MEE and 120 KLD MEE Condensate Reuse and 40 KLD Discharge though in house Spray Dryer Remaining 293 KLD Waste water generation From Primary, Secondary treatment ETP-2 plant followed by MEE and in house Spray Dryer, by which is discharge though in House Spray Dryer, Hence unit has achieved ZERO LIQUID DISCHARGE 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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vii Reuse/Recycle details (338 KLD) [Source of reuse & application area] Total reuse 338 KLD Source of waste Application Characteristics of waste Remarks water for reuse area with water to be reused regarding with quantity in quantity in KLD (COD, BOD, TDS etc.) feasibility to KLD (From where (Where it is reuse i.e. it is coming) used) MEE Condensate Manufacturing of pH = 6.5 to 8.00 Reuse in 120 KLD Intermediates COD = 250-350 manufacturing TDS = 700-800 process MEE Condensate Manufacturing of pH = 6.5 to 8.00 218 KLD Dyes and Other COD = 100-150 ancillary TDS = 300-400

E Air i Flue gas emission details

575 th meeting of SEAC -Gujarat, dated 17.12.2019 Page 39 of 178 No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

Sr. Stack height Consumptio Stack attached to Fuel APCM no in meter n

ESP +Water 1 Steam Boiler (7.5 TPH) 25 Coal 15 MT/Day Scrubber Thermic Fluid Heater (6 Lac 2 Coal 5 MT/Day Kcal/h) ESP +Water 25 Thermic Fluid Heater (10 Lac Scrubber 3 Coal 8 MT/Day Kcal/h) Hot Air Generator (10 Lac 4 Coal 12 MT/Day Kcal/Hr ) for Spray Dryer Hot Air Generator (15 Lac ESP +Water 5 25 Coal 15 MT/Day Kcal/Hr ) for Spray Dryer Scrubber Hot Air Generator (10 Lac 6 Coal 12 MT/Day Kcal/Hr ) for Spray Dryer

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

Sr Stack height Stack attached to APCM Pollutant no in meter

Spray Dryer ( 2500 Multi Cyclone Followed By 1. 15.0 PM LPH) Two Stage Water Scrubber Spray Dryer ( 4000 Multi Cyclone Followed By 2. 15.0 PM LPH) Two Stage Water Scrubber Spray Dryer ( 1500 Multi Cyclone Followed By 3. 15.0 PM LPH) for product Two Stage Water Scrubber

4. Isolation (4 NAP) 11.0 Two Stage Alkali scrubber H2S Gas

iii Fugitive emission details with its mitigation measures. 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

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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 Types of Sr. Categor Propose Hazardous Sources Disposal No y MT/Year Waste Collection, storage, 1 ETP Sludge ETP Area 35.3 1200 Transportation and Dispose to Active TSDF Site Collection, storage, Reuse 2 Used Oil Plant Machinery 5.1 12 within premises. Material Collection, storage, Discarded 3 handling and 33.1 80 Transportation and Dispose by Container Storage selling to Registered Recycler 1-3 Sulpho Collection, storage, Spent Sulphuric Phenyl 3 methyl transportation and send to 4 26.3 5520 Acid 5 pyrazolone, (Rule -9) authorized agencies Fast Red B or actual users Solvent Yellow 14, Yellow 18, Yellow 72, Yellow 33, Collection, storage, Yellow 43, transportation and send to 5 Spent Acid Yellow 82, 26.3 33.6 (Rule -9) authorized agencies Yellow 107, or actual users Yellow 114, Yellow 124, Yellow 172, Blue 35, Blue

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36, Blue 58, Blue 98, Blue 104, Blue 122, Green 3

Collection, Storage, and reuse Sodium hydro 6 4 NAP - 60 in 4 NAP Process or sell to bisulphite (25%) authorize industries Rule-9

Solvent Dyes Yellow 33, Yellow 43, Yellow 114, Yellow 172, Yellow 157, Yellow 163, Yellow 93, Blue 35, Blue 36, Blue 58, Blue 98, Blue 104, Collection, Storage, And 7 Spent Solvent Blue 122, Green 26.4 16680 Reuse With in Plant Premises 3, Red 135, Red in Process After Distillation 111, Red 207, Red 52 orange 60, orange 63, Violet 13, Violet 14 phenyl 3 Methyl 5 Pyrazolone, Para Toyl 3 Methyl 5 Pyrazolone Collection, Storage, And Send 8 Solvent Residue Distillation Unit 26.1 636 For Co-Processing Collection, storage, 9 Evaporation Salt MEE 35.3 2700 Transportation and Dispose to Active TSDF Site Note: The unit will select disposal facility of other hazardous waste outside the CEPI area to comply 575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 42 of 178

with the order dated 10.07.2019 and 23.08.2019 from Hon’ble Tribunal. 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 Qty of Total Sr. Name of Solvent of % % Solvent Solvent No Product Recycled Losses recovery Losses Input (Kg) (Kg) (Kg) ODCB 838 821 17 98.5 1.5 Solvent dye 1 Methanol 2222 2177 45 98.0 2.0 s Butanol 2474 2424 50 98.0 2.0 1 phenyl 3 2 Methyl 5 Metanol 285 277 8 96.0 4.0 Pyrazolone Para Tolyl 3 3 Methyl 5 Metanol 300 288 12 96.0 4.0 Pyrazolone

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 Sr . Capacity in Spare Storage tanks Name of Chemical Nos. N MT Tank o.

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1 HCL 20 2 - 2 Methanol 10 2 - 3 Xylene 5 2 - 4 Sulphuric Acid 20 2 - 5 Oleum 23% 5 1 1 6 Oleum 65% 8 1

Liq. Ammonia Acetic Anhydride Drum/Barrels H Acid VS

‹ Applicability of PESO : Not Applicable. • Technical presentation was made by the project proponent with consultant/expert M/s. Satva Enviroment Consultancy, Ahmedabad during SEAC meeting dated 17/12/2019. • Committee noted that this proposal is for new unit located in GIDC Saykha. Source of water is GIDC. PP mentioned that effluent generated from process viz dyes intermediate will be treated in proposed in-house Primary ETP – 1 followed by MEE – 1, Condensate of MEE -1 will be reused by mixing with fresh water while Reject of MEE – 1 will be treated in Spray Dryer – 1 followed by ATFD – 1 and salt/residue generated will be disposed in approved TSDF. PP mentioned that effluent generated from process viz dyes along with washing & scrubbing, boiler blow down & cooling tower blow down will be treated in proposed in-house Primary & Secondary ETP – 2 followed by MEE – 2, Condensate of MEE – 2 will be reused by mixing with fresh water while Reject of MEE – 2 will be treated in Spray Dryer – 2 followed by ATFD – 2 and salt/residue generated will be disposed in approved TSDF. PP has proposed one steam boiler; two TFH and three HAG. Fuel used will be Coal. PP has addressed Hazardous Waste as per HWR – 2016. • After detailed discussion, it was decided to recommend the project to SEIAA, Gujarat for grant of Terms of Reference. • 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

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sources of energy like solar water heater, solar lighting etc. Measures proposed for energy conservation. 3. 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. 4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during unloading, storage, transportation, handling and processing of Solvents. 5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form. 6. Adequacy of ZLD for Proposed in-house ZLD for High COD/TDS stream along with its treatability & feasibility. 7. MoU for all the hazardous waste to be disposed under rule – 9 of the HWR – 2016. 8. Technical Specification of In-house MEE, Spray Dryer & ATFD shall be provided at the time of Appraisal presentation along with its reuse/recycle for specific purpose shall be provided along with its characteristic. • 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. 10 SIA/GJ/IND2/45450/2019 M/S. Hemani Intermediates Pvt. Ltd. Screening & Scoping Plot No: 1246, 1247, 1248, Chemical zone, Notified Industrial Area, GIDC Sarigam, Umbergaon, Valsad.

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intermediates

2 Ortho Chloro Aniline 95-51-2 18.46 Dyes intermediates 3 4B Acid 88-44-8 150 Pigment intermediates 4 2B Acid 88-51-7 50 Pigment intermediates 5 Ortho/Para Nitro Anisole 91-23-6/ 121-87-9 150 Dyes intermediates 6 Ortho /Para Anisidine 90-04-4/ 104-94-9 300 Dyes intermediates 7 Tetra Chloro Benzidine.2HCl 15721-02-5 30 Dyes intermediates 8 Pigment Violet 23 6358-30-1 20 Plastic, printing, ink, coating 9 Organic Yellow pigment 100 Ink, Plastic, Paint ( Pigment Yellow 12 6358-85-6 Pigment Yellow 13 5102-83-0 Pigment - Yellow 14 5468-75-7 Pigment - Yellow 83 5567-15-7 Pigment - Yellow 147 4118-16-5 Pigment - Yellow 155 68516-73-4 Pigment - Yellow 180 77804-81-0 Pigment - Yellow 188) 23762-68-9

Organic Orange pigment 6253-10-7 (Orange 13) 10 2,5 Di Chloro Aniline 95-82-9 150 Dyes and pigments 11 Ortho dianisidine-2HCl 20325-40-0 50 Dyes intermediates Total 1218.46 • 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 17/12/2019. • Salient features of the project including Water, Air and Hazardous waste management: Sr. no. Particulars Details A Total cost of Proposed Project Rs. 20 Crores (Rs. in Crores):

B Total Plot area 10745 Sq. m. ( sq. meter)

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Green belt area 3760 Sq. m. C Employment generation 50 D Water i Source of Water Supply GIDC Sarigam water supply (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. Permission issued by GIDC Vapi vide letter No. NAO/SRG/573 dated 14/10/2019

Water consumption (KLD) ii Category Quantity Remarks KLD (J) Domestic 7.5 (K) Gardening 6.0 (L) Industrial Process 524.15 Processing, washing and scrubber Washing 12.0 Floor/equipment Washing Boiler 140.0 Cooling 70.0 Others 10.0 Coal wetting and boiler scrubber Industrial Total 756.15 Total (A + B + C) 769.65

1) Total water requirement for the project: 769.65 KLD 2) Quantity to be recycled:30 KLD 3) Total fresh water requirement: 739.65 KLD (Total water requirement = Fresh water + Recycled water) iii Waste water generation (KLD)

Category Waste water Remarks KLD

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(H) Domestic 6.0 (I) Industrial Process 528.17 Processing, washing and scrubber Washing 12.0 Floor/equipment Washing Boiler 15.0 Cooling 7.0 Others 3.0 Coal wetting and boiler scrubber Total Industrial waste water 565.17 Total [A + B] 571.17

iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ ETP – 530 KLD ‹ MEE & ATFD – 40 KLD ‹ RO – 35 KLD Treatment scheme including segregation at source. ‹ Total Industrial Waste water generation will be 565.16 m 3/day mainly from process, washing, scrubber, boiler blow down and cooling tower blowdown. From the process, product washing and common scrubber, average 528.17 m 3/day of waste water is generated. Out of which 39.43 m3/day of concentrated effluent will be segregated, neutralized and treated in solvent stripper followed by MEE and ATFD. 32 m3/day of condensate from MEE will be treated in ETP. Balance 488.74m3/day of normal effluent will be treated in ETP. Average 34 m3/day of boiler blow down, cooling tower blow down and floor/container washing will be treated in RO Plant. 27 m3/day of RO permeate will be recycled and 7 m3/day of RO rejection will be treated in ETP. 3 m3/day of effluent from scrubber attached to boiler will be directly utilized for coal wetting. Thus total 527.74 m 3/day 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. 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, there is no 18(1) b condition imposed by CPCB to Sarigam CETP. Total Industrial Waste water generation will be 565.16 m3/day mainly from process, washing, scrubber, boiler blow down and cooling tower blowdown. From the process, product washing and

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common scrubber, average 528.17 m3/day of waste water is generated. Out of which 39.43 m3/day of concentrated effluent will be segregated, neutralized and treated in solvent stripper followed by MEE and ATFD. 32 m3/day of condensate from MEE will be treated in ETP. Balance 488.74m3/day of normal effluent will be treated in ETP. Average 34 m3/day of boiler blow down, cooling tower blow down and floor/container washing will be treated in RO Plant. 27 m3/day of RO permeate will be recycled and 7 m3/day of RO rejection will be treated in ETP. 3 m3/day of effluent from scrubber attached to boiler will be directly utilized for coal wetting. Thus total 527.74 m3/day 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. Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Not Applicable ‹ Total Industrial Waste water generation will be 565.16 m3/day mainly from process, washing, scrubber, boiler blow down and cooling tower blowdown. From the process, product washing and common scrubber, average 528.17 m3/day of waste water is generated. Out of which 39.43 m3/day of concentrated effluent will be segregated, neutralized and treated in solvent stripper followed by MEE and ATFD. 32 m3/day of condensate from MEE will be treated in ETP. Balance 488.74m3/day of normal effluent will be treated in ETP. Average 34 m3/day of boiler blow down, cooling tower blow down and floor/container washing will be treated in RO Plant. 27 m3/day of RO permeate will be recycled and 7 m3/day of RO rejection will be treated in ETP. 3 m3/day of effluent from scrubber attached to boiler will be directly utilized for coal wetting. Thus total 527.74 m3/day 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. v Mode of Disposal & Final meeting point Domestic: Domestic waste water (6 m3/day) will be disposed off through septic tank/soak pit. Industrial: Total Industrial Waste water generation will be 565.16 m3/day mainly from process, washing, scrubber, boiler blow down and cooling tower blowdown. From the process, product washing and common scrubber, average 528.17 m3/day of waste water is generated. Out of which 39.43 m3/day of concentrated effluent will be segregated, neutralized and treated in solvent stripper followed by MEE and ATFD. 32 m3/day of condensate from MEE will be treated in ETP. Balance 488.74m3/day of normal effluent will be

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treated in ET P. Average 34 m3/day of boiler blow down, cooling tower blow down and floor/container washing will be treated in RO Plant. 27 m3/day of RO permeate will be recycled and 7 m3/day of RO rejection will be treated in ETP. 3 m3/day of effluent from scrubber att ached to boiler will be directly utilized for coal wetting. Thus total 527.74 m3/day of industrial effluent will be treated in proposed primary, secondary & tertiary treatment plant & discharged into underground effluent drainage line of GIDC Sarigam to CE TP 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, CHWIF etc. Name of Common facility (CF) (For waste water treatment) ‹ Treated Waste water will be sent to CETP for further treatment and disposal into Arabian Sea. Membership of Common facility (CF) (For waste water treatment) Proponent has already applied to CETP Sarigam for effluent discharge. vii Simplified water balance diagram with reuse / recycle of waste water

vii Reuse/Recycle details (KLD)

575 th meeting of SEAC -Gujarat, dated 17.12.2019 Page 50 of 178 [Source of reuse & application area] Total reuse: 30 KLD - Source of waste Application area Remarks water for reuse with Characteristics of waste with quantity in regarding quantity in KLD water to be reused (COD, KLD (Where it is feasibility to (From where it is BOD, TDS etc.) used) reuse i.e. coming) Reuse in boiler COD:100-150 mg/l RO Permeate-27 KLD - and cooling TDS:50-60 mg/l Reuse in coal COD:10-15 mg/l Boiler scrubber-3 KLD - wetting TDS:500-600 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. - Type of Air Pollution Source of Stack Quantity Type of emissions Control Sr. no. emission Height of Fuel Fuel i.e. Air Measures With Capacity (meter) Pollutants (APCM) ESP Followed Steam boiler Imported 1. 30 2000 Kg/h by wet (10 TPH) Coal scrubber MDC followed Steam boiler (5 Imported by bag filter 2. 15 1000 Kg/h TPH) Coal and wet PM scrubber SO X Thermic Fluid MDC, bag NO X Heater Imported 250 filter followed 3. 15 (10 Lakhs k Coal Kg/h by wet cal/h) scrubber 125 D G set 4. 11 HSD kg/h Chimney (500 kVA)

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Closed shed, water sprinkler, wind Coal Storage breaking wall, 5. - - - PM yard RCC flooring and dust suppression system Closed screening, Coal Handling 6. - - - PM coal crushing system and closed conveyer Impact blade crusher, 7. Coal crusher - - - PM 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.

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FLOW DIAGRAM FOR COAL HANDLING/ASH HANDLING SYSTEM

Chimney

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

Fly ash

Silo

Fly ash load on truck

ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) Specific Source of Air Pollution Control Sr. emission Type of Stack/Vent Measures No. (Name of the Product emission Height (meter) (APCM) & Process) Storage tanks of Nitric Two stage alkali 1. acid, Sulphuric acid, Acidic vapour 11 scrubber hydro chloric acid Particulate Cyclone separator & 2. Pulveriser 11 Matter pulse jet bag filter

Particulate Cyclone separator & 3. Spin Flash Dryer 11 Matter pulse jet bag filter

iii Fugitive emission details with its mitigation measures. ‹ 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 waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.

575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 53 of 178 i Sr. Type/Name of Specific Source Category and Quantity Management of no. Hazardous of generation Schedule as (MT/Annum) HW waste (Name of the per HW Activity, Product Rules. etc.) 1. Used oil D G set and Sch: I/5.1 0.1 Collection, gearbox of storage, reactors transportation and selling to authorized recycler 2. Discarded Empty containers Sch: I/33.1 50.0 Collection, container of raw materials storage and Utilize for packing of hazardous waste or selling to authorized recycler after decontamination 3. ETP waste Neutralization and Sch: I/35.3 200.0 Collection, Filteration storage, process of transportation effluent and Dispose off into TSDF SEPPL, Kutch 4. Spent Resin D M plant Sch: I/35.2 2.0 Collection, from D M plant regeneration storage, transportation and Dispose off into TSDF SEPPL, Kutch 5. Used filter cloth Filter Press Sch: I/36.2 2.0 Collection, storage, transportation

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and Dispose off into TSDF SEPPL, Kutch 6. Spent solvent purification Sch:I/26.4 913.0 Recycled in process process after distillation 7. Mix solvent Solvent stripper Sch:I/26.4 46.8 Collection, storage, transportation and sell to authorized distillatory 8. Salt from MEE Evaporation of Sch: I/35.3 1840.8 Collection, liquid effluent in storage, MEE transportation and Dispose off into TSDF SEPPL, Kutch 9. Process Distillation Sch:I/26.1 468.48 Collection, Residue process storage, transportation and sent for co- processing to cement industries 10. Spent Acid (20- From process of Sch:I/26.3 30726 Collection, 25%) 3,3 DCB & ortho storage, di Anisidine transportation (450 TPA will be recycled in ODA, and balance 30276 TPA sell to actual users having Rule 9 permission under hazardous waste

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rules 2016 11. Spent Catalyst From process of Sch:I/26.5 34.59 Collection, 3,3 DCB, OA/PA storage, & ortho di transportation Anisidine and sent to authorized regenerator 12. Bleed liquor From common - 156 Collection, from scrubber scrubber attached storage, mainly salts storage tanks treatment in MEE/ETP - ii Membership details of TSDF, CHWIF etc. (For HW • We will apply for membership of TSDF management) after obtaining ToR iii Details of Non-Hazardous waste & its disposal(MSW Fly Ash:- 1703 TPA and others) It will be sold to brick manufacturer. 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 Total Recovery, MT Loss, MT % No to be Consumption, Recover . used MT y Per Per Per Per Per Per tone month tone month tone month 1 3,3 Toluene 3.494 698.8 3.40 680.4 0.092 18.4 97.3 dichlorobenzidin 2 e-2 HCl 2 4B Acid ODCB 3.5 525 3.43 514.95 0.067 10.5 98.0 3 3 2B Acid ODCB 6.281 314.05 6.20 310.3 0.075 3.75 98.8 6 4 Ortho/Para Methan 1.063 159.45 0.83 124.8 0.231 34.65 78.2 Nitro Anisole ol 2 5 Tetra Chloro Toluene 1.333 39.99 1.26 38.01 0.066 1.98 95.04 Benzidine.2HCl 7 6 Pigment Violet MCB 3.775 75.5 3.45 69 0.325 6.5 91.39

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23 ODCB 25.88 517.7 24.7 495.2 1.125 22.5 95.6 5 6 DEG 1.818 36.36 0.90 18.18 0.909 18.18 50 9 7 Yellow/orange Xylene 0.55 55 0.54 54 0.01 1 98.18 pigment 8 2,5 Di Chloro Methan 0.766 114.98 0.75 113.7 0.085 1.278 98.8 Aniline ol 8 2 9 Ortho Toluene 0.66 33 0.63 31.68 0.026 1.32 96 dianisidine-2HCl 3 4 Total 2569.8 2450.2 120.05 3 2 8

ii VOC emission sources and its mitigation measures Source: • Process Reactor • Raw material Handling & Storage Mitigation Measures: • The raw materials will be stored in closed containers and will be handled through closed system to avoid the handling losses • Reactor and solvent handling pumps will have mechanical seals to prevent leakages. Reactors shall also be provided with breather valve to prevent losses H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous Remarks chemicals Storage tanks 48 % Caustic lye, Acetic Acid, Caustic lye, Hydro chloric acid, Methanol, Mono chloro Benzene, Nitric acid (60%),Ortho Di Chloro Benzene, Sulphuric acid, Toluene, Xylene Drum/Barrel storage 2- Chloro Para Toludine, Benzene Sulfonyl Chloride, Carbazole, Caustic Flakes, Chloranil, Di ethyl Glycol, Di

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Ethyl Sulphate, Emulsifier, Para Toludine,

‹ Applicability of PESO : Will be obtained after obtaining EC/CTE

• Technical presentation was made by the project proponent with consultant/expert M/s. Eco Chem Sales & Service, Surat during SEAC meeting dated 17/12/2019. • Committee noted that this proposal is for new unit located in GIDC Sarigam. Source of water is GIDC. Committee noted that in the Product profile PP has proposed to Manufacture 3,3 DCB & Ortho di Anisidine in which Dilute Spent Acid Stream (20-25 %) is generated having Quantity 30,726 MT/Year and PP has proposed to reuse only 450 MT/Year and difference in quantity 30,276 MT/Year is going to be disposed under Rule – 9. Committee noted that considering the location of the unit there are no such actual end users on Dilute Spent Acid (20-25%) with such huge quantity which PP is going to generate in its proposed project. Further Committee also noted that Dilute Spent Acid Stream is also mismanaged considering its low cost and there are handling, transportation & disposal problems of the same. • After detailed discussion, Committee decided to call back the Project Proponent after submission of revised proposal in Product Profile along with Form-1 & Project details Considering Sound Management of Hazardous Waste as per HWR – 2016. 11 SIA/GJ/IND2/41723/2019 M/S. Savakashi Industries Llp ToR – Reconsideration Plot No. C-12 & 13, GIDC Saykha Ind. Estate, Saykha, vagra, Bharuch. Category of the unit: 5(f) Project status: New

• This office has received an application vide their online proposal no. SIA/GJ/IND2/41723/2019 dated 01/10/2019 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 new unit proposes for manufacturing of synthetic organic product as tabulated below: SR. QUANTITY PRODUCT NAME CAS NO. NO. (MT/MONTH) 1. DISPERSE YELLOW 10 GN 164578-37-4 450 2. DISPERSE YELLOW SGL 83249-52-9

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3. DISPERSE YELLOW SG 61968-66-9 4. DISPERSE YELLOW C4G H/C 86836-02-4 5. DISPERSE YELLOW CXG ---- 6. DISPERSE GOLDEN YELLOW 2GD 54077-16-6 7. DISPERSE GOLDEN YELLOW 2GN H/S 54077-16-6 8. DISPERSE YELLOW 5RX 54077-16-6 9. DISPERSE ORANGE RL 31482-56-1 10. DISPERSE SCARLET RR 12217-86-6 11. DISPERSE SCARLET RRS 6657-37-0 12. DISPERSE SCARLET BR H/C 61703-11-5 13. DISPERSE SCARLET GS 78564-87-1 14. DISPERSE SCARLET 3R 12223-35-7 15. DISPERSE YELLOW BROWN 2RFL 12223-23-3 16. DISPERSE YELLOW BROWN 2RFL 150% 12223-23-3 17. DISPERSE YELLOW BROWN 2RFL 200% 12223-23-3 18. DISPERSE PINK RBSF ---- 19. DISPERSE LUMINOUS RED G 70294-19-8 20. DISPERSE DARK RED 2B - 100% 26850-12-4 21. DISPERSE DARK RED 2B - 200% 26850-12-4 22. DISPERSE RED F3BS 9931-78-6 23. DISPERSE RED F3BL ---- 24. DISPERSE RED F3B ---- 25. DISPERSE RED BS 78564-86-0 26. DISPERSE RUBINE GFL 16889-10-4 27. DISPERSE RED 60 H/S 17418-58-5 28. DISPERSE RED VIOLET FBL ---- 29. DISPERSE PINK 5B 522-75-8 30. DISPERSE VIOLET 3R (Concentrated) ---- 31. DISPERSE BLUE 3R ---- 32. DISPERSE BLUE 2R (Concentrated) 2309-94-6 33. DISPERSE BLUE 2RXN 31810-89-6 34. DISPERSE BLUE 2RX - 100% ---- 35. DISPERSE BLUE ER ---- 36. DISPERSE BLUE 79 12239-34-8 37. DISPERSE BLUE BRS ----

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38. DISPERSE BRILLIANT BLUE BG 12217-80-0 39. DISPERSE BLUE SR 104137-27-1 40. DISPERSE BLUE GSL 41642-51-7 41. DISPERSE BLUE EXSF - 300% ---- 42. DISPERSE BROWN 3BS - 150% ---- 43. DISPERSE BROWN 3REL H/Concentrated ---- 44. DISPERSE BROWN SFH ECO ---- 45. DISPERSE RED RGL 3089-17-6 46. DISPERSE BROWN 3RSF H ---- 47. DISPERSE BROWN FRL - 150% ---- 48. DISPERSE BLACK EXSF - 300% ---- 49. DISPERSE BLACK CCR ---- 50. DISPERSE BLACK R Concentrated ---- 51. DISPERSE LIQUID BLACK RULTRA R ---- 52. DISPERSE BLACK BSL H/C. (For Printing) ---- 53. DISPERSE BLACK RLS (For Printing) ---- 54. DISPERSE BLACK HLS H/C. (For Printing) ---- 55. DISPERSE WHITE RLC ---- 56. DISPERSE WHITE RCT ---- 57. DISPERSE WHITE RBF ---- 58. DISPERSE WHITE RX ULTRA Concentrated ---- 59. DISPERSE BLACK MIX ---- 60. DISPERSE BLUE 183 2309-94-6 61. DISPERSE BLUE MIX ---- 62. DISPERSE BLUE 366 84870-65-5 63. DISPERSE BLUE 79:1 3618-72-2 64. DISPERSE NAVY BLUE ECO ---- 65. DISPERSE ORANGE 80 70210-10-5 66. DISPERSE RED 92 72363-26-9 67. DISPERSE RED 343 ---- 68. DISPERSE YELLOW 211 86836-02-4 TOTAL PRODUCTION 450 • 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 17/10/2019. • Salient features of the project including Water, Air and Hazardous waste management:

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Sr. Particulars Details no. A A Total cost of Proposed Project 16.45 Crores (Rs. in Crores):

B Total Plot area ( sq. meter) 11345.56 Sq. m.

Green belt area 3403.66 Sq. m. ( sq. meter) C Employment generation 45

D Water i Source of Water Supply GIDC-Saykha

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

Status of permission from the concern authority. GIDC

ii Water consumption (KLD) Water Consumption Application (KLD) Domestic [A] 4.0 Gardening [B] 5.0 Industrial [C] Process 250 Washing 2.0 Boiler 10.0 Scrubber 1.0 Cooling 3.0 Total Industrial 266 TOTAL 275 [A+B+C]

1) Total water requirement for the project: 275 KLD

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2) Quantity to be recycled : 0.0 KLD 3) Total fresh water requirement: 275 KLD (Total water requirement = Fresh water + Recycled water) iii Waste water generation (KLD) Waste water generation Application (KLD) Domestic [A] 3.6 Gardening [B] 0.0 Industrial [C] Process 310 Washing 2.0 Boiler 1.0 Scrubber 1.0 Cooling 0.3 Total Industrial 314.3 TOTAL 317.9 [A+B+C] Domestic waste water 3.6 KLD – Discharged to Soak pit via Septic Tank Effluent Generation from Industrial Activity: 314.3 KLD Generated industrial effluent will be treated in proposed in house Effluent Treatment Plant having primary & tertiary units. treated effluent will be discharged to Common CETP of Saykha Industrial Estate iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ In house ETP and having primary and tertiary ETP treatment Treatment scheme including segregation at source. ‹ No stream segregation as all the effluent will be discharge to CETP of Saykha Industrial Estate after ETP 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 . ‹ Generated industrial effluent 314.3 KLD will be treated in proposed in house Effluent Treatment Plant having primary & tertiary units. treated effluent will be discharged to Common CETP of Saykha Industrial Estate Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ No zero liquid discharge.

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Domestic: To Soak pit via septic tank.

Industrial: Generated industrial effluent 314.3 KLD will be treated in proposed in house Effluent Treatment Plant having primary & tertiary units. treated effluent will be discharged to Common CETP of Saykha Industrial Estate vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ No membership of common facility (ZLD) Membership of Common facility (CF) (For waste water treatment)

No membership of common facility (ZLD) vii Simplified water balance diagram with reuse / recycle of waste water

viii Reuse/Recycle details (KLD) Total reuse 0.0 KLD Source of waste Application area Characteristics of waste Remarks water for reuse with with quantity in water to be reused (COD, regarding quantity in KLD KLD (Where it is BOD, TDS etc.) feasibility to (From where it is used) reuse i.e. coming) ------

575 th meeting of SEAC -Gujarat, dated 17.12.2019 Page 63 of 178 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 Stack Quantity of Type of Air Pollution Sr. emission Type of Height Fuel emissions i.e. Control Measures no. With Fuel (meter) MT/Day Air Pollutants (APCM) Capacity Multi Cyclone Dust Imported SPM Steam Boiler collector followed by 1 30 Coal/Agr 4.0 SO2 (4 TPH) Bag Filter & Wet o Waste NOX Scrubber Hot Air Generator Imported SPM Multi Cyclone Dust 2 (2.0 Lac k 15 (Each) Coal/Agr 8.0 SO2 collector followed by cal/hr) o Waste NOX Bag Filter (2 Nos)

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

Spray Dryer-1 Particulate Multi Cyclone Dust (2 KL/Hr) Matter Collector followed by 1 30 Bag Filter & Wet Scrubber

Spin Flash Dryer Particulate Cyclone separator & 2 20 Matter Bag filter

iii Fugitive emission details with its mitigation measures: As below: Sources of fugitive emissions include storage of chemicals, loading and unloading section, raw material handling, hazardous waste storage area.

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Mitigation Measures - Water shall be sprinkled during the construction - Mechanical seals for pumps etc. should be used and maintained. - Closed unloading, conveying and packing system - All the reactors shall be closed. - Safety devices shall be provided to workers - Raw material storage in closed storage area

F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type of Hazardous Source of Cat. Quantity Management No. Waste Generation No. (per Annum) From treatment of Collection, Storage, low concentrated 1080.0 Transportation & 1. ETP Waste 35.3 effluent MT Disposal by sent to TSDF site. Collection, Storage, Transportation & Disposal by reuse in 2. Used Oil 5.1 10 Liter Plant & machinery plant machineries as lubricant or selling to registered refineries. Raw material/ Collection, Storage, Discarded Production Transportation & 3. 33.1 18.0 MT Containers/Bags Section Disposal by selling to registered recyclers. Collection, Storage, Distillation of Transportation & 720.0 4. Distillation residue Solvent 20.3 Disposal by send to MT common incineration facility.

ii Membership details of TSDF, CHWIF etc. ------(For HW management) iii Details of Non-Hazardous waste & its disposal No any hazardous 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 and DMF will be used as solvent in the process and its is recovered through separate distillation. ii VOC emission sources and its mitigation measures ‹ There will not occur any VOC emission in premises

H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous Remarks chemicals Storage tanks HCl (Hydrochloric acid) 8.0 Drums

Drum/Barrel storage ------

‹ Applicability of PESO : ‹ Not applicable PESO. Unit is not covered under MAH category as per Hazardous Chemicals as per the "Manufacturing, Storage and Import of Hazardous Chemicals Rules, 1989", • Technical presentation was made by the project proponent with consultant/expert M/s. Bhagwati Enviro Care Pvt. Ltd. During SEAC meeting dated 17/10/2019. • Committee noted that this proposal is for new unit located in GIDC- Saykha. Source of water is GIDC. PP mentioned that effluent generated from process, washing boiler blow down, cooling tower blow down & scrubber will be treated in proposed in-house Primary & Tertiary ETP and treated effluent will be discharged into CETP, Saykha for final treatment & disposal. Committee asked PP to clarify about discharge permission from CETP, Saykha. PP mentioned that they have applied for the same but till yet they have not obtained the Permission Letter. In view of the above Committee decided to appraise the project only after discharge permission is obtained from CETP, Saykha or PP submit revise proposal as ZLD. • After detailed discussion, Committee decided to defer the proposal and consider the same only after Assurance Letter from CETP, Saykha is obtained by Project Proponent (PP) or Project Proponent (PP) submit the revise proposal for discharge considering it as ZLD Project. • Project proponent was called for presentation for the above mentioned query dated 17/12/2019 for the above mentioned points. • PP mentioned that they have obtained membership certificate from CETP, Saykha for disposal of effluent dated 23/10/2019. PP mentioned that they have proposed one steam boiler & one HAG. Fuel used will be Imported Coal/Agro Waste. PP has addressed Hazardous Waste as per HWR – 2016. • Committee noted that PP has submitted the compliance of the query dated 17/10/2019.

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• After detailed discussion, it was decided to recommend the project to SEIAA, Gujarat for grant of Terms of Reference. • 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. 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. 4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during unloading, storage, transportation, handling and processing of Solvents. 5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form. 6. Characteristic of effluent to be disposed in CETP of Saykha along with its discharge norms. • 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. 12 SIA/GJ/IND2/45524/2019 M/S. Sahydri Organics Screening & Scoping Plot. No. 830/7/1 & 2, Nr Saint Gobin, GIDC Jhagadia ,Bharuch.

Category of the unit: 5(f) Project status: New • This office has received an application vide their online proposal no. SIA/GJ/IND2/45518/2019 dated 13/11/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.

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• Project proponent (PP) has submitted Form-1, PFR and relevant details/information. • This is new unit proposes for manufacturing of synthetic organic product as tabulated below: Sr. Name of the Products CAS no. / Quantity End-use of the products no. CI no. (MT/Month) Total 1 Benzoyl Chloride 98-88-4 40 Pharma Intermediate 2 Benzotrichloriide 98-07-7 30 Dyes 3 Acetyl Chloride 75-36-5 10 Dyes and Pigment 4 Propionyl Chloride 79-03-8 10 Pharma Total 90 • 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 17/12/2019. • Salient features of the project including Water, Air and Hazardous waste management: Sr. no. Particulars Details A A Total cost of Proposed Project 0.5 Crores (Rs. in Crores): B Total Plot area ( sq. meter) 2498.84 m 2 Green belt area ( sq. meter) 825.0 Sq. m. C Employment generation 30 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. Applied ii Water consumption (KLD)

Category Quantity Remarks KLD (M) Domestic 1.0 (N) Gardening 2.0 (O) Industrial Process 0.0 Washing 0.0 Boiler 0.0

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Cooling 10.0 Other/Scrubber 2.5 Industrial Total 12.5 Total (A + B + C) 15.5 1) Total water requirement for the project: 15.5 KLD 2) Quantity to be recycled : 0.4 KLD 3) Total fresh water requirement: 15.1 KLD iii Waste water generation (KLD)

Category Waste water Remarks KLD (J) Domestic 0.5 (K) Industrial Process 0.0 Washing 0.0 Boiler 0.0 Cooling 0.5 Scrubber 2.5* Reuse and sell under rule-9 permission Total Industrial waste water 3.7 Total [A + B + C] 4.2 - Iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Collection Tank 1.0 KLD Treatment scheme including segregation at source. R.O Plant 0.5 KLD 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 1.0 KL/day (0.5 KL/day Industrial + 0.5 KL/day domestic) of effluent shall be generated. ‹ Scrubbing Media Sell to end user having Rule-9 permission. ‹ 0.5 KLD waste water from cooling blow down will be treat in R.O plant.

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‹ 0.5 KLD Domestic waste water send to soak pit or septic tank system. ‹ R.O Permeate 0.4 KLD will be Reuse in Cooling purpose and R.O reject 0.1 KLD will be evaporated inreactor vessel and salt will be sent TSDF Site. v Mode of Disposal & Final meeting point Domestic: Domestic waste water (0.5 KL/day) will be disposed by septic tank or soak pit system Industrial: ‹ Total 1.0 KL/day (0.5 KL/day Industrial + 0.5 KL/day domestic) of effluent shall be generated. ‹ Scrubbing Media Sell to end user having Rule-9 permission. ‹ 0.5 KLD waste water from cooling blow down will be treat in R.O plant. ‹ 0.5 KLD Domestic waste water send to soak pit or septic tank system. ‹ R.O Permeate 0.4 KLD will be Reuse in Cooling purpose and R.O reject 0.1 KLD will be evaporated inreactor vessel and salt will be sent TSDF Site. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ N.A Membership of Common facility (CF) (For waste water treatment) N.A vii Simplified water balance diagram with reuse / recycle of waste water

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viii Reuse/Recycle details (KLD) Total reuse: 0.4 KLD Source of waste Application area Characteristics of waste Remarks water for reuse with with quantity in water to be reused (COD, regarding quantity in KLD KLD (Where it is BOD, TDS etc.) feasibility to (From where it is used) reuse i.e. coming) R.O Cooling COD :50.0 R.O Permeate BOD3 :20 TDS :300

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. Flue gas emission details

Sr. Source of Stack Type of Quantity of Type of Air Pollution no. emission Height Fuel Fuel emissions Control (m) Measures Thermic Fluid Briquettes SPM Multi-cyclone 0.9 MT/Day 1 Heater - 2 Nos. 30 of Bio-Coal SO 2 Separator + bag / (2 Lac KL/hr.) /Coal NOx filter SPM D.G. Set* 25 Adequate Stack 2 11 HSD SO 2 (55 KVA) Liter/Hour Height NOx

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

Sr. no. Source of Type of Stack/Vent Air Pollution Control emission emission Height (m) Measures Process Vent-1 1 HCl 11 Two Stage Water Scrubber (Chlorination ) - iii Fugitive emission details with its mitigation measures: As below:

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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. 2. Adequate ventilation will be provided. 3. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions. 4. Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature. 5. Periodic monitoring of work area will be carried out to check the fugitive emission. 6. Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with online pH meter with hooter system for better operational control. 7. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers. 8. Minimum number of flanges, joints and valves in pipelines. 9. Regular inspection of floating roof seals and proper preventive maintenance of roofs and seals for tanks. 10. Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area will be collected through hoods and ducts by induced draft and controlled by scrubber/ dust collector. 11. Dedicated scrubber will be provided are used for fugitive emissions to control. 12. For dust emissions bag filter will be provided. 13. 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. F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Name of Source of Category Total Disposal Method no. Hazardous generation and Quantity/ waste Schedule Annum 1 Used Oil Machineries & SCH-I/5.1 100 Collection, Storage, Utilities lit Transportation and sell to GPCB registered reprocessor/ Refiner

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2 Discarded Raw Materials & SCH-I/33.1 600.0 Nos. Collection, Storage, Drums/Bags Products Decontamination, Transportation & given to GPCB authorized Vendor 3 Dil.HCL From mfg. SCH-I/28.1 312.0 Collection, Storage, Process MT/Annum Transportation and sell to end user Having Rule-9 Permission. 4 Distillation Distillation SCH-I/36.1 6.0 MT/Annum Collection, Storage, Residue Transportation and sent to Co- processing or common Incineration site for disposal. 5 Evaporate Salt Evaporation SCH-I/35.3 1.08 Collection, Storage, MT/Annum Transportation and sent to Co- processing or TSDF for disposal site Dahej. - ii Membership details of TSDF, CHWIF etc. Unit has applied for (For HW management) membership iii Details of Non-Hazardous waste & its disposal There will be no generation of (MSW and others) Non-Hazardous waste. G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format) -- ii VOC emission sources and its mitigation measures During operation stage, leakage through valves/pumps, leakage and emission from open drum containing chemicals, open feeding, storage tanks, etc. will be major sources of fugitive emissions and VOCs. Excess use of solvent/s may also results fugitive emission from the process vessels.

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• Solid raw material charging will be done through closed system. • Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature. • Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers. • Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area, will be collected through hoods and ducts by induced draft and controlled by scrubber/dust collector. • Emphasis will be given to solvent management/solvent loss prevention. • Control by having proper scrubbing system. • Condenser to trap VOC. • 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. • Proper maintenance schedule will be adhered to avoid emissions through flange joints, pump seals etc. • Minimum number of flanges, joints and valves in pipelines. • Proper gland packing will be maintained for pumps and valves and to the extent possible pumps with mechanical seal. • All the raw materials will be pneumatically transfer to the reactor. • All rotating equipments like pumps will be installed with mechanical seals to arrest any sort of emissions. • A regular preventive maintenance schedule will be in place to replace or rectify all gaskets and joints etc. as a part of ISO systems to ensure no fugitive emissions take place. • Periodic monitoring of work area will be carried out to check the fugitive emission. • Solvent tank vents will be connected to vent chillers. • Adequate ventilation will be provided. • Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures. • Breather valves will be provided on solvent tanks. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks Storage tanks --

Drum/Barrel storage Toluene, Acetic Anhydride, Benzoic Acid,

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Propionic Acid

Cylinder, Bottle or Tonner Chlorine gas

‹ Applicability of PESO : If Applicable, company will take permission. • Technical presentation was made by the project proponent with consultant/expert M/s. Aqua Air Environmental Engineers Pvt Ltd, Surat during SEAC meeting dated 17/12/2019. • Committee noted that this proposal is for new unit located in GIDC Jhagadia. Source of water is GIDC. PP mentioned that effluent will be generated from only from boiler blow down which will be treated in in-house RO, RO – Permeate will be used in cooling tower while RO – Reject will be evaporated in reactor vessel and salt will be disposed at approved TSDF. PP has proposed one thermic fluid heater. Fuel used will be briquettes of bio-coal/Coal. PP has addressed hazardous Waste as per HWR – 2016. • After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant of Terms of Reference. • 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. 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. 4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during unloading, storage, transportation, handling and processing of Solvents. 5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form. 6. Adequacy of Reactor Vessel to be utilized in both Product Manufacturing & Evaporation of RO – Reject. 7. MoU for all the hazardous waste to be disposed under rule – 9 of the HWR – 2016. 8. Safety precautions pertaining to chlorine shall be addressed along with its SOP for storage, transport & handling along with its process safety. • 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. 13 SIA/GJ/IND2/40232/2019 M/S. Intech Healthcare Screening & Scoping Plot No. 38/5-2, GIDC Jhagadia, Bharuch.

Category of the unit: 5(f) Project status: New • This office has received an application vide their online proposal no. SIA/GJ/IND2/45254/2019 dated 13/11/2019 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 new unit proposes for manufacturing of synthetic organic product as tabulated below: SR. NAME OF PRODUCTS CAS NUMBER TOTAL END USE NO. MT/ MONTH GROUP-I ANTI HYPERTENSIVE Losartan Potassium & Intermediates AND/OR 124750-99-8 2 Anti- 4-{[2-butyl-4chloro-5-(hydroxymethyl)-1H-imidazol-1- Hypertensive 114772-55-3 yl]methyl}biphenyl-2-carbonitrile (Stage – A) 2-n-butyl-4-chloro-5hydroxymethyl-1-{[2”-(1H- 1. tetrazole-5-yl)-biphenyl-4-yl]methyl]imidazole (Stage – 124751-00-4 B) 2-n-butyl-4-chloro-5hydroxymethyl-1-{[2”-(1H- tetrazole-5-yl)-biphenyl-4-yl]methyl]imidazole 124750-99-8 potassium (Stage – Final) Metoprolol Tartrate & Intermediates AND/OR (2-{[4-(2-methoxyethyl)phenoxy]oxirane) (Stage – A) 56718-70-8 (1-[4-2-methoxyethyl)phenoxy]-3-(propane-2- 2. 51384-51-1 ylamino)propan-2ol) (Stage – B) (±)1-(Isopropylamino)-3-[p-(β-methoxyethyl)phenoxy]- 37350-58-6 2-propanol (+)-tartrate salt,

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Metoprolol Succinate & Intermediates AND/OR (2-{[4-(2-methoxyethyl)phenoxy]oxirane) (Stage – A) 56718-70-8 (1-[4-2-methoxyethyl)phenoxy]-3-(propane-2- 3. 51384-51-1 ylamino)propan-2ol) (Stage – B) 1-[4-(2-methoxyethyl)phenoxy]-3-[(1-methylethyl)amino]- 98418-47-4 2-propanol succinate, Telmisartan & Intermediates AND/OR 4’-methylbiphenyl – 2- carbonitrile (Stage – A) 114772-53-1 4-Bromomethyl 2-cyano biphenyl (Stage – B) 114772-54-2 4'-[[4-methyl-6-(1-methyl-1H-benzimidazol-2-yl)-2- 4. propyl-1H-benzimidazol- 1-yl] biphenyl-2- carbonitrile.(Stage – C) 144702-27-2 4'-[[4-Methyl-6-(1-methyl-2-benzimidazole)-2-propyl-1- benzimidazol -1-yl] methyl] biphenyl-2-carboxylic acid. (Stage - Final) 144701-48-4 Bosentan Monohydrate & Intermediates AND/OR 4,6 dihydroxy-5-(2-methoxy phenoxy )-2,2’- 329923-15-1 bipyridine(Stage – A) 4, 6 dichloro-5-(2-methoxy phenoxy )-2,2’-bipyridine 150728-13-5 (Stage – B) P-t-butyl-N-(6-chloro-5-(o-methoxy phenoxy)-4- 150727-06-3 5. pyrimidinyl) benzene sulphonamide (Stage – C) 4-tert-butyl-N-(6-(2-hydroxy ethoxy)-5-(2-methoxy- phenoxy)-[2,2’]-bipyrimidin-4-yl]-benzene 147536-97-8 sulphonamide (Stage – D) 4-tert-butyl-N-(6-(2-hydroxy ethoxy)-5-(2-methoxy- phenoxy)-[2,2’]-bipyrimidin-4-yl]-benzene 157212-55-0 sulphonamide Monohydrate (Stage – Final) GROUP-II ANTI HYPERTENSIVE

Nebivolol & Intermediates 0.05 Anti- [6-fluoro-3,4-dihydro-2H-chromene-2- Hypertensive carbaldehyde](Stage – A) 409346-73-2 6. [6-fluoro-2-(oxiran-2-yl)-3,4-dihydro-2H- chromene](Stage – B) 99199-90-3 [6-fluoro-2-(oxiran-2-yl)-3,4-dihydro-2H- 99199-90-3

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chromene](Stage – C) [ 2-(benzylamino)-1-(6-fluoro-3,4-dihydro-2H-chromen- 2-yl)ethanol](Stage – D) 1322622-97-3 1-(6-fluoro-3,4-dihydro-2H-chromen-2-yl)-2-[[2-(6- fluoro-3,4-dihydro-2H-chromen-2-yl)-2- hydroxyethyl]amino]ethanol;hydrochloride (Stage – F) 169293-50-9 1-(6-fluoro-3,4-dihydro-2H-chromen-2-yl)-2-[[2-(6- fluoro-3,4-dihydro-2H-chromen-2-yl)-2- hydroxyethyl]amino]ethanol;hydrochloride (Stage – Final) 169293-50-9 [2-(6-fluoro-3,4-dihydro-2H-chromen-2-yl)ethyl acetate] (NV -2A) 129101-36-6 [2-(6-fluoro-3,4-dihydro-2H-chromen-2-yl)-2-{[(4- methylphenyl)sulfonyl]oxy}ethyl acetate] (NV -2B) 1345202-53-0 [6-fluoro-2-(oxiran-2-yl)-3,4-dihydro-2H-chromene](NV- 99199-90-3 2C) GROUP-III ANTI-HYPERTENSIVE

Pentoxifyline (Final Stage) 6493-05-6 1 Anti- Hypertensive 7. 3,7-Dihydro-3,7-dimethyl-1-(5-oxohexyl)-1H-purine-2,6-dione(stage – Final) 6493-05-6

GROUP-IV ANTI DEPRESSANT

Paroxitine HCl & Intermediates 0.5 ANTI (3 S)-4-(4-fluorophenyl)-1-methylpiperidin-3-yl]-methyl DEPRESSAN 317323-77-6 4-methylbenzenesulfonate (stage - A) T 8. (3 S,4 R)-3-[(1,3-benzodioxol-5-yloxy)methyl]-4-(4- 110429-36-2 fluorophenyl)-1-methylpiperidine(Stage – B) (3S-trans)-3-[(1,3-Benzodioxol-5-yloxy)methyl]-4-(4- 78246-49-8 fluorophenyl)piperidine Hydrochloride(Stage – Final)

GROUP- V ANTIVIRAL

Topiramate & Intermediates 1 ANTI VIRAL 2,3:4,5-bis-O-(1-isopropylidene)-β-D- 9. 20880-92-6 fructopyranose(Stage - A 3:4,5-Bis-O-(1-methylethylidene)- β -D- 97240-79-4

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fructopyranose sulfamate (Stage – B)

3:4,5-Bis-O-(1-methylethylidene)- β -D- fructopyranose sulfamate 97240-79-4 (Stage – Final)

GROUP- VI ANTIEMITIC

Granisetron 0.5 ANTIEMITIC

10. 1-Methyl-N-(1S)-9-methylbicyclo(3.3.1)non-3-yl]- 1H-indazole-3-carboxamide HCl ( Stage – Final) 107007-99-8

Granisetrone Base 1-Methyl-N-(1S)-9-methylbicyclo(3.3.1)non-3-yl]- 11. 1H-indazole-3-carboxamide Base 109889-09-0 (Stage – Final)

GROUP- VII HYPOGLCEMIC

Repaglinide & Intermediates 0.1 ((S)-3-Methyl-1-[(2-(1- 147769-93-5 piperidinyl)phenyl]butylamine))(Stage – A) ((S)-2-Ethoxy-4-[2-[[3-methyl-1-[(2-(1- piperidinyl)phenyl] 147770-06-7 butyl]amino]-2-oxoethyl benzoic acid ethyl ester) 12. (Stage – B) ((S)-2-Ethoxy-4-[2-[[(1S)-3-methyl-1-[(2-(1-piperidin-1- yl)phenyl]butyl]amino]-2-oxoethyl] benzoic acid) (Stage 135969-54-9 – C) ((S)-2-Ethoxy-4-[2-[[(1S)-3-methyl-1-[(2-(1-piperidin- 1-yl)phenyl]butyl]amino]-2-oxoethyl] benzoic acid) 135969-54-9 (Stage – Final)

GROUP- VIII ANTI-DEPRESSANT

Riluzole & Intermediates 0.1 13. 6-(Trifluoro methoxy)-2-Benzothiazoleamine 1744-22-5 (Stage – Final)

GROUP- IX ANTI-DEPRESSANT

14. Lithium Carbonate 554-13-2 0.5

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GROUP - X PHOSHATE BINDING (KINDNEY DEASISE) Sevelamer Carbonate & Intermediates 845273-93-0 2 Polly Allylamine Hydrochloride (Stage – A) 71550-12-4 2-(chloromethyl)oxirane;prop-2-en-1- 15. 152751-57-0 amine;hydrochloride(Stage – B) carbonic acid;2-(chloromethyl)oxirane;prop-2-en-1- 845273-93-0 amine (Stage – Final)

GROUP- XI ANTIHYPERLIPIDEMIC

Colesevelam HCl & Intermediates 182815-44-7 0.5 Polly Allylamine Hydrochloride (Stage – A) 71550-12-4 16. 2-(chloromethyl)oxirane;prop-2-en-1- 152751-57-0 amine;hydrochloride(Stage – B) Cosevelamer HCl (Stage – Final) 182815-44-7

GROUP- XII – ANTIHISTAMINE

17. Desloratidine 100643-71-8 0.5 Levocetrizine di hydrochloride & Intermediates (R)-2-[2-[4-[(4-chlorophenyl)phenylmethyl]piperazine- 130018-87-0 1-yl]ethoxy]acetamide dihydrochloride(Stage – A) 18. (R)-2-[2-[4-[(4-chlorophenyl)phenylmethyl]piperazine- 1-yl]ethoxy]acetamide dihydrochloride(Levocetrizine 130018-87-0 Final)

GROUP- XIII – ANTI-INFLAMMATORY

Fluticasone Propionate & Intermediates 0.05 (6a,9a-difluoro 11β-hydroxy-16 α-Methyl-3-oxo 17 α(Hydroxy) androsta 1,4 dien-17 β-carboxylic acid] 28416-82-2 (Stage – A) [6a,9a-difluoro 11β-hydroxy-16 α-Methyl-3-oxo 17 α(propionyloxy) androsta 1,4 dien-17 β-carboxylic 65429-42-7 19. acid](Stage – B) [17 β{(N,N dimethylcarbomoyl)thio}carbonyl-6a,9a- difluoro 11β-hydroxy-16 α-Methyl- 17 α(propionyloxy)- 105638-31-1 3-oxondrosta-1,4-diene](Stage – C) 6α,9α-Difluoro-11β-hydroxy-16α-methyl-3- 80474-45-9 oxo-17α-(propionyloxy)-androsta-1,4-diene-

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17β -carbothioic Acid (Stage – D) [S-fluoromethyl 6a,9a-difluoro 11β-hydroxy-16 α- Methyl- 17 α(propionyloxy)-3-oxondrosta-1,4-diene 17 80474-14-2 β-carbothioate](Stage – E) [S-fluoromethyl 6a,9a-difluoro 11β-hydroxy-16 α- Methyl- 17 α(propionyloxy)-3-oxondrosta-1,4-diene 17 80474-14-2 β-carbothioate](Stage – Final) GROUP- XIV – ANTICONVULSANT Zonisamide & Intermediates 1.5 1, 2-Benzisoxazole -3-methane sulfonyl chloride 73101-65-2 20. (Stage – A) 1, 2-Benzisoxazole -3-methane sulfonamide(Stage – 68291-97-4 Final) Lacosamide & Intermediates (R )-N-Boc-D- serine (Stage – A) 6368-20-3 Boc-D-Serine Benzylamide (Stage – B) 1253790-58-7 (R )-N-Benzyl-2-N-Bocamino-3-methoxy 21. 880468-89-3 propionamide(Stage – C) (R )-2-Amino-N-Benzyl-3-methoxy- 196601-69-1 propionamide(Stage – D) Lacosamide (Stage – Final) 175481-36-4 Oxcarbazepine & Intermediates 10-oxo-10,11-dihydro-5H-dibenzo[b,f]azepine-5- 28721-07-5 22. carboxamide (Stage –A) 10-oxo-10,11-dihydro-5H-dibenzo[b,f]azepine-5- 28721-07-5 carboxamide (Stage –Final)

GROUP- XV - ANTIDOTES

Deferasirox & Intermediates 0.5 2-(2-(2-hydroxyphenyl)Benz(e)[1,3]oxazine -4- 1218-69-5 0ne(Stage – A) 23. 4-[3,5-Bis(2-hydroxyphenyl)-1H-1,24-triazole-1-yl 201530-41-8 benzoic acid (Stage –B) 4-[3,5-Bis(2-hydroxyphenyl)-1H-1,24-triazole-1-yl 201530-41-8 benzoic acid (Stage –Final)

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GROUP- XVI - PEPTIC ULCER DISEASES

Esomeprazole Magnassium & Intermediates 4 5-Methoxy-2-(4-methoxy-3,5-dimethylpyridine-2-yl- 113713-24-9 methylthio)1H-benzimidazole(Stage – A) 24. methoxy -2-{(S)-[(4-methoxy-3,5-dimethyl pyridine -2- yl)methyl sulfinyl) 1H – benzimidazole magnesium, 217087-09-7 trihydrate (Stage- Final) Pentaprazole sodium & Intermediates (RS )-6-(Difluoromethoxy)-2-[(3,4-dimethoxypyridin-2- 25. yl)methylsulfinyl]-1H-benzo[d]imidazole(Stage – A) 102625-64-9 (RS )-6-(Difluoromethoxy)-2-[(3,4-dimethoxypyridin-2- yl)methylsulfinyl]-1H-benzo[d]imidazole(Stage – Final) 164579-32-2 GROUP- XVII –ANTI HYPERTENSIVE Lercadipine Hydrochloride & Intermediates 0.2 1,4-Dihydro-2,6-dimethyl-4-(3-nitrophenyl)-3,5- pyridinedicarboxylic Acid 3,5-Dimethyl Ester(Stage – 21881-77-6 A) 5-Methoxycarbonyl-2,6-Dimethyl-4-(3-Nitrophenyl)-1,4- 74936-72-4 Dihydrpyridine-3-Carboxylic Acid(Stage – B) 1,4-Dihydro-2,6-dimethyl-4-(3-nitrophenyl)-2-[(3,3- diphenylpropyl)methylamino]-1,1-dimethylethyl methyl 132866-11-6 ester 3,5-pyridinedicarboxylic acid hydrochloride(Stage 26. – C) 1,4-Dihydro-2,6-dimethyl-4-(3-nitrophenyl)-2-[(3,3- diphenylpropyl)methylamino]-1,1-dimethylethyl methyl 132866-11-6 ester 3,5-pyridinedicarboxylic acid hydrochloride(Stage – D) 1,4-Dihydro-2,6-dimethyl-4-(3-nitrophenyl)-2-[(3,3- diphenylpropyl)methylamino]-1,1-dimethylethyl methyl 132866-11-6 ester 3,5-pyridinedicarboxylic acid hydrochloride(Stage – Final)

GROUP- XVIII - CARDIOVASCULAR DISEASE

Rosuvastatin Calcium & Intermediates 1.5 27. (+)-(3R, 5S)-7-[4-(4-FLUOROPHENYL)-6- 147098-18-8 ISOPROPYL-2-(N-METHYL-N-

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METHANESULFONYLAMINO)PYRIMIDIN -5- YL]-(3, 5)-DIHYDROXY-6(E)-HEPTENOATE, tert-Butyl rosuvastatin (+)-(3R,5S)-7-[4-(4-fluorophenyl)-6-isopropyl-2-(N- methyl-N-methanesulfonyl amino)pyrimidin-5-yl]3,5- 147098-20-2 dihydroxy-6(E)-heptenoic acid calcium salt (Stage – Final) Atorvastatin & Intermediates (4R,6R)-tert-Butyl-6-(2-aminoethyl)-2,2-dimethyl-1,3- 125995-13-3 dioxane-4-acetate tert-Butyl (4R,6R)-2-[[[6-(2-4-fluorophenyl)-5-isopropyl- 3-phenyl-4-(phenylcarbamoyl)pyrrol-1-yl]ethyl]-2,2- 125971-95-1 28. dimethyl-1,3-dioxan-4-yl]acetate [R-(R*, R*)]-2-(4-fluorophenyl)-β, δ-dihydroxy-5-(1- methylethyl)-3-phenyl-4-[(phenylamino)carbonyl]- 134523-03-8 1Hpyrrole-1-heptanoic acid, calcium salt (2:1)trihydrate.

GROUP- XIX - ANTIDIABATIC

Sitagliptin Phosphate & Intermediates 0.2 5-[1-hydroxy-2-(2,4,5-trifluorophenyl)ethylidene]- 2,2- 764667-64-3 dimethyl-1,3-dioxane-4,6-dione (Stage – A) Tert –butyl-3[(1R]-1-phenylethyl (amino)-4-(2,4,5- 1345822-93-6 trifluorophenyl)-but-2-enoate (Stage –B) (Z)-3-[[(1R)-1-phenylethyl)amino]-4-(2,4,5- --- trifluorophenyl)but-2-enoic acid(Stage – D) (2z)-3-{[(1r)-1-phenylethyl]amino}-1-[3- 29. (trifluoromethyl)-5,6-dih Ydro[1,2,4]triazolo[4,3- 1169707-29-2 a]pyrazin-7(8h)-yl]-4-(2,4,5-trifluorophe Nyl)-2-buten-1- one (Stage – E) (3 R)-3-amino-1-[3-(trifluoromethyl)-6,8-dihydro-5H- [1,2,4]triazolo[4,3-a]pyrazin-7-yl]-4-(2,4,5- 654671-77-9 trifluorophenyl)butan-1-one;phosphoric acid;hydrate(Stage – F) (3 R)-3-amino-1-[3-(trifluoromethyl)-6,8-dihydro-5H- 654671-77-9 [1,2,4]triazolo[4,3-a]pyrazin-7-yl]-4-(2,4,5-

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trifluorophenyl)butan-1-one;phosphoric acid;hydrate(Stage – Final)

GROUP- XX ANTIDIABATIC

30 . Canagliflozin 928672-86-0 1 Teniligliptine & Intermediates

3-((2S,4S)-4-[4-(3-methyl-1-phenyl-1H-pyrazol-5- 1572583-29-9 yl)piperazine-1-yl]pyrrolidine-2-ylcarbonyl)thiazolidine Hydrobromide hydrate

31. (Stage – A)

3-((2S,4S)-4-[4-(3-methyl-1-phenyl-1H-pyrazol-5- 1572583-29-9 yl)piperazine-1-yl]pyrrolidine-2-ylcarbonyl)thiazolidine Hydro bromide hydrate

(Stage – Final)

Glimipiride & Intermediates N-{2-[4-(aminosulfonyl)phenyl]ethyl}-3-ethyl-4-methyl- 2- oxo-2, 5-dihydro-1H-pyrrole-1-carboxamide (Stage – B) 119018-29-0 32. 3-ethyl-4-methyl-N-{2-[4-({[(4- 93479-97-1 methylcyclohexyl)carbamoyl]aminosulfonyl)phenyl]eth yl}-2-oxo-2,5-dihydro-1H-pyrrole-1-carboxamide(Stage – Final) GROUP- XXI ANTI KERATOSIS

Adapelene & Intermediates 0.05 2-(1-admantyl)-4-bromophenol(Stage – A) 104224-68-2 3-(5-bromo-2-methoxyphenyl) tricycle [4.3.1.0] 104224-63-7 decane(Stage – B) Methyl 6-[3-(1-adamantyl)-4-methoxyphenyl]-2- 33. 106685-41-0 naphthoate (Stage – C) 6-(4-methoxy-3-tricyclo [3.3.1.1] dec-1-yl phenyl) 106685-40-9 napthalene-2-carboxylic acid(Stage – D) 6-(4-methoxy-3-tricyclo [3.3.1.1] dec-1-yl phenyl) 106685-40-9 napthalene-2-carboxylic acid(Stage – Final)

GROUP- XXII ANALGESIC(PAIN RELIEVING), ANTI-

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INFLAMMATORY AND ANTIPYRETIC (FEVER REDUCING) Etoricoxib & Intermediates 3 1-(6-Methyl-3-pyridinyl)-2-(4-methyl sulfonyl)phenyl- 34. ethanone(Ketosulphone, stage – A) 221615-75-4 5-chloro-6'-methyl-3-[4-(methylsulfonyl)phenyl]-2,3'- bipyridine (Stage – Final) 202409-33-4 Lornoxicam & Intermediates 6-chloro-4-hydroxy-3- Methoxycarbonyl-2H- 70374-51-5 Thieno[2,3,e]-1,2-Thiazine-1,1-Dioxide(Stage –A) 6-chloro-4-hydroxy-2-methyl-3-Methoxycarbonyl-2H- Thieno [2,3,e]-1,2-Thiazine-1,1-Dioxide(Stage – B) 70415-50-8

35. 6-chloro-4-hydroxy-2-methyl-N-(2-pyridinyl)-2H- thieno[2,3,e]-1,2-Thiazine-3-carboxamide- 1,1- 70374-39-9 dioxide(Stage – C) 6-chloro-4-hydroxy-2-methyl-N-(2-pyridinyl)-2H- thieno[2,3,e]-1,2-Thiazine-3-carboxamide- 1,1- 70374-39-9 dioxide(Stage – Final) Maloxicam & Intermediates methyl (1,1-dioxido-3-oxo-1,2-benzothiazol-2(3 H)- yl)acetate(Stage – A) 6639-62-9 methyl 4-hydroxy-2-methyl-2H-1,2-benzothiazine-3- carboxylate 1,1-dioxide (stage-B) 35511-15-0 36. 4-hydroxy-2-methyl-N-(5-methyl-1,3-thiazol-2-yl)-2H- 1,2-benzothiazine-3-carboxamide 1,1-dioxide (Stage- 1027136-06-6; C) 71125-38-7 4-hydroxy-2-methyl-N-(5-methyl-1,3-thiazol-2-yl)-2H- 1,2-benzothiazine-3-carboxamide 1,1-dioxide (Stage- 1027136-06-6; Final) 71125-38-7 Fluconazole & Intermediates 2-(2, 4-diflurophenyl)-1, 3-bis (1H-1, 2,4-triazol-1-yl)- 37. propan-2-ol.(Stage – A) 89429-59-4 2-(2, 4-diflurophenyl)-1, 3-bis (1H-1, 2,4-triazol-1-yl)- propan-2-ol.(Stage – Final) 89429-59-4 Sertaconazole & Intermediates 38. (RS)-1-[2-[(7-chloro-1-benzothiophen-3-yl)methoxy]-2- 99592 -32 -2

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(2,4,-dichlorophenyl) ethyl]-1H-imidazole(Stage – A) 1-[2-[(7-chloro-1-benzothiophen-3-yl)methoxy]-2-(2,4- dichlorophenyl)ethyl]imidazole;nitric acid(stage – Final) 99592-39-9 Terbinafine HCl & Intermediates trans-N-(6,6-Dimethyl-2-hepten-4-ylyl)-N-methyl-1- 39. naphthylmethylamine (stage – A) 91161-71-6 trans -N-(6,6 -Dimethyl -2-hepten -4-ylyl) -N-methyl -1- naphthylmethylamine hydrochloride(stage – Final)

GROUP- XXIII (USED TO TREAT EPILEPSY, NEUROPATHIC PAIN, FIBROMYALGIA, AND GENERALIZED ANXIETY DISORDER) Pregabalene & Intermediates 4 (3-(2-amino-2-oxoethyl)-5-methylhexanoic acid(Stage – A) 181289-15-6 (3 R)-3-(2-amino-2-oxoethyl)-5-methylhexanoic 40. acid(Stage – B) 181289-33-8 (3 S)-3-(aminomethyl)-5-methylhexanoic acid(Stage – C) 148553-50-8 (3 S)-3-(aminomethyl)-5-methylhexanoic acid(Stage – Final) 148553-50-8

GROUP- XXIV- ANTI HYPERTENSIVE Olmesartanmedoxomil & Intermediates 1 Ethyl-4(1-hydroxy-1-methylethyl)-2-propyl-1-{4-[2-(trityl tetrazol-5-yl-) -phenyl] phenyl} methyl imidazole-5-carboxylate.(Stage – A) 189400 – 21 - 3 1H-Imidazole-5-carboxylicacid,4-(1-hydroxy-1-methyl ethyl)-2-propyl -1-[2'-[1-(triphenylmethyl)-1-H-tetrazole- 5-yl][1,1'-biphenyl]-4-yl]methyl]-(5-methyl-2-oxo-1,3- 41. dioxol-4-yl)methyl ester.(Stage – C) 144690 – 92 - 6 4-(1-Hydroxy-1-methylethyl)-2-propyl-1-[[2'-(1H- tetrazole-5- yl)[1,1'-biphenyl]-4-yl]-methyl]-1H-imidazole-5- carboxylic acid (5-methyl-2-oxo-1, 3- dioxol-4-yl) methyl ester (Stage – D) 144689 – 63 - 4 4-(1-Hydroxy-1-methylethyl)-2-propyl-1-[[2'-(1H- tetrazole-5- 144689 – 63 - 4

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yl)[1,1'-biphenyl]-4-yl]-methyl]-1H-imidazole-5- carboxylic acid (5-methyl-2-oxo-1, 3- dioxol-4-yl) methyl ester (Stage – Final) Frucemide & Intermediates 4-Chloro-N-furfuryl-5-sulfamoylanthranilic acid, 5- 42. (Aminosulfonyl)-4-chloro-2-([2- furanylmethyl]amino)benzoic acid 54-31-9

GROUP- XXV ANTI-ALERGATIC Phenyl ephrine HCl & Intermediates 1 2-bromo-1-(3-hydroxyphenyl)ethanone(Stage - A) 2491-37-4 2-[benzyl(methyl)amino]-1-(3- 43. hydroxyphenyl)ethanone(stage – B) 56917-44-3 3-[1-hydroxy-2-(methylamino)ethyl]phenol(Stage – C) 1477-63-0 1R)-1-(3-Hydroxyphenyl)-2-(methylamino)ethanol hydrochloride(Stage – Final) 61-76-7

GROUP- XXVI ANTI DIABETIC Vildagliptine & Intermediates 0.5 (2 S)-1-(chloroacetyl)pyrrolidine-2-carboxamide(Stage – A) 214398-99-9 (2 S)-1-(chloroacetyl)pyrrolidine-2-carbonitrile(Stage – 44. B) 207557-35-5 (2 S)-1-{[(3-hydroxytricyclo[3.3.1.1 3,7 ]dec-1- yl)amino]acetyl}pyrrolidine-2-carbonitrile(Stage – C) 274901-16-5 (2 S)-1-{[(3-hydroxytricyclo[3.3.1.1 3,7 ]dec-1- yl)amino]acetyl}pyrrolidine-2-carbonitrile(Stage – Final) 274901-16-5

GROUP- XXVII ANTIFUNGAL Luliconazole 0.7 1H-imidazol-1-ylacetonitrile(Stage – A) 98873-55-3 (2 E)-[(4 R)-4-(2,4-dichlorophenyl)-1,3-dithiolan-2- ylidene](1 H-imidazol-1-yl)ethanenitrile HCl(stage – B) 187164-19-8 45. (2 E)-[(4 R)-4-(2,4-dichlorophenyl)-1,3-dithiolan-2- ylidene](1 H-imidazol-1-yl)ethanenitrile(Stage – C) 187164-19-8 (2 E)-[(4 R)-4-(2,4-dichlorophenyl)-1,3-dithiolan-2- ylidene](1 H-imidazol-1-yl)ethanenitrile(Stage – Final) 187164-19-8

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GROUP- XXVIII ANTIMALARIAL Atovaquone & Intermediates 2 2-chloro-3-[trans -4-(4- chlorophenyl)cyclohexyl]naphthalene-1,4-dione(Stage – A) 153977-22-1 46. 2-[trans -4-(4-chlorophenyl)cyclohexyl]-3- hydroxynaphthalene-1,4-dione(Stage – B) 95233-18-4 2-[trans -4-(4-chlorophenyl)cyclohexyl]-3- hydroxynaphthalene-1,4-dione(Stage – Final) 95233-18-4

GROUP- XXIX ANTI-DIABETIC Linagliptine & Intermediates 0.5 8-Bromo-7-(but-2-yn-1-yl)-3-methyl-3,7-dihydro-1H- purine-2,6-dione (Stage –A) 666816-98-4 (2-(Chloromethyl)-4-methylquinazoline) (Stage-B) 109113-72-6 (3R)-piperidin-3-amine dihydrochloride (Stage-C) 334618-23-4 (5-methyl-2-[(3R)-piperidin-3yl]-1H-isoindole-1,3(2H)- dione) (Stage-D) 4667-76-9

47. (8-bromo-7-(But-2-yn-1-yl)-3-methyl-1-[(4- methylquinazolin-2-yl)methyl]-3,7 dihydro-1H-purine- 2,6-dione) (Stage-E) 853029-57-9 (8-[(3 R)-3-Aminopiperidin-1-yl]-7-(but-2-yn-1-yl)-3- methyl-1-[(4-methylquinazolin-2-yl)methyl]-3,7-dihydro- 1H-purine-2,6-dione) (Stage-G) 668270-12-0 (8-[(3R)-3-Aminopiperidin-1-yl]-7-(but-2-yn-1-yl)-3- methyl-1-[(4-methylquinazolin-2-yl)methyl]-3,7-dihydro- 1H-purine-2,6-dione) (Stage-Final) 668270-12-0 0.55 R & D PRODUCTS 31 TOTAL • 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 17/12/2019. • Salient features of the project including Water, Air and Hazardous waste management: Sr. Particulars Details no.

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A A Total cost of Proposed Project 4 Crores (Rs. in Crores):

B Total Plot area ( sq. meter) 2972.86 Sq. m.

Green belt area 746.44 sq. m. ( sq. meter) C Employment generation 45

D Water i Source of Water Supply GIDC Bharuch.

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

Status of permission from the concern authority. Will be obtained.

ii Water consumption (KLD) Category Quantity Remarks KLD Domestic 5 Unit will use fresh water for it. Gardening 4 Unit will use fresh water for it. Industrial Process 25 Fresh water :- 3 KLD + Recycled water:- 22 KLD Washing 3 Fresh water from GIDC Boiler 8 Fresh water from GIDC Cooling 18 Fresh water from GIDC Scrubber 2 Fresh water from GIDC Water Scrubber 8 Unit will use 5 KLD Boiler Blow Down for water scrubber of boiler. In which 2 KLD water will be getting evaporated. Remaining 3 KLD saturated scrubber solution will be used for coal handling & Ash Quenching. Industrial Total 64 Fresh water:- 34 KLD + Recycled

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water:- 30KLD Total 73 Fresh water:- 43 KLD + Recycled water:- 30KLD

1) Total water requirement for the project: 73 KLD 2) Quantity to be recycled : 30 KLD 3) Total fresh water requirement: 43 KLD

iii Waste water generation (KLD) Category Waste water Remarks KLD (L) Domestic 5 Treated along with industrial effluent.

(M) Industrial Process 30 Unit will bifurcate industrial effluent into 2 steamsbased oncharacteristics. STEAM 1:- HighAmmonical Nitrogen Steam + High COD Steam (10 KLD). 1 KLD strip solvent will be removed. Remaining 9 KLD will be subjected to in house ETP. STEAM 2:- LOW COD steam (20 KLD) - treated in unit’s own effluenttreatment plant. Washing 3 3 KLD WASHING WATER will be treated in unit’s own effluent treatment plant. Boiler 5 Total 5 KLD Boiler Blow Down will be generated. Unit will use this BoilerBlow Down water in the water scrubber of Boiler. Total 2 KLD effluent will be lost into atmosphere. Remaining 3 KLD saturated Water will be used in Coal Handling and Ash quenching. So unit will use entire BOILER BLOW DOWN water

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with in premises. Cooling 3 3 KLD Cooling Tower Blow Down water will be used for the washing purpose. Other 2 2 KLD scrubber solutions will be subjected to unit’s own effluent treatment plant.

Total Industrial waste 43 -- water Total [A + B] 48 --

iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ Unit will develop primary, secondary and tertiary treatment. Treatment scheme including segregation at source.

➢ HighCODandHighAmmonicalnitrogenstreamwillbesegregatedatthe sourceandsenttoin- houseMEEafterneutralizationandLOWCODand LOWAmmonicalnitrogensteamwillbetreatedinunitsowneffluent treatment plant and subjected to M/s. NCT.

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 . ‹ It is new project, then 18 (1) (b) is not applicable. Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Not Applicable. v Mode of Disposal & Final meeting point

Domestic: Treated along with industrial effluent. Industrial: M/s. NCT vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ M/s.NCT Membership of Common facility (CF) (For waste water treatment) Unit has obtained membership certificate of M/s. NCT.

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vii Simplified water balance diagram with reuse / recycle of waste water

Equalization Cum After Tertiary After M/s. Sr. Collection Neutralization Treatment/ Parameter Unit Secondary NCT No. Tank Tank, Sand filter & Clarifier norms coagulation & Carbon Filter clarification

1 pH - 6.5-7.5 6.0- 8.5 6.0- 8.5 6.0- 8.5

2 TDS mg/lit 4000-5000 <10000 <10000 <10000 --

3 SS mg/Lit <100 <50 <50 <50 100

4 COD mg/lit <5000 <3500 <500 <250 250

575 th meeting of SEAC -Gujarat, dated 17.12.2019 Page 92 of 178 5 BOD mg/lit <1500 <1000 <100 <100 100

viii Reuse/Recycle details (KLD) Total reuse 10 .KLD Source of waste Application area Characteristics of waste Remarks water for reuse with with quantity in water to be reused (COD, regarding quantity in KLD KLD (Where it is BOD, TDS etc.) feasibility to (From where it is used) reuse i.e. coming) RO Permeate 22 KLD into MFG pH – Neutral Reusable in TDS :-<300 mg/l MFG COD :- < 100 mg/l Boiler Blow down- 5 5 KLD into Boiler pH – Basic Reusable in KLD scrubber TDS :-2000-2500 mg/l Boiler scrubber

Scrubber saturated 3 KLD for ash pH – Basic Reusable in solution- 3 KLD quenching TDS :-4000-6000 mg/l ash quenching.

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.

Type of emissi Air Pollution Sr. Stack Quantity of Source of emission Type of ons i.e. Control No. Height Fuel With Capacity Fuel Air Measures (meter) MT/Day Polluta (APCM) nts 600 Kg/Hr Multi Cyclone + Steam Boiler Coal/Bri 1. 30 OR Bag Filter + 5 TPH quette PM 750 Kg/Hr Water Scrubber SO 2 Natural Adequate stack Steam Boiler NO X 2. 11 Gas 140 Nm3/Hr height 2 TPH

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Adequate stack Diesel 3. TFH (4 Lakhs Kcal/Hr) 12 50 Nm3/Hr height

Adequate stack 4. D.G.Set (250 KVA) 12 Diesel 40 Lit/Hr height

ii Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) - Sr. APCM attached to Stack APCM Pollutant No. Height Water Scrubber followed HCl 1 Reaction Vessel 12 by Alkali Scrubber SO 2

Cl 2 2 Reaction Vessel 12 2 Stage Caustic Scrubber Br 2

3 Reaction Vessel 12 2 stage Acid scrubber Ammonia

iii Fugitive emission details with its mitigation measures: As below: Sr. Source Probable Pollutant Control Measures/ APCM No. Emission 1. Solvent storage Air pollutant i) Carry out work place area monitoring to find tank (VOC) out concentration level in ambient air. ii) Provision of breather valve cum flame arrester. 2. Solvent recovery Air pollutant i) Solvent recovery system with steam system (VOC) condensation system. ii) Pumps & motors are mechanical seal type. 3 Handling of raw Air pollutant i) Provision of exhaust ventilation material bags in (PM) ii) Provision of PPE. storage area iii) Provision of Job rotation to reduce exposure. 4 Flange joints of Air pollutant i) Routine &periodic inspection to check pipeline, pump & (VOC) leakage. motors ii) Preventive maintenance, Follow SOP for maintenance. iii) Pumps & motors will be mechanical seal type.

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iv) LDAR program will be followed. Provision of Flange guard.

5 Solid raw material Air pollutant Hopper will be provided with powder transfer transferring to (PM) system. reactor 6 Liquid raw Air pollutant Feeding of liquid raw material will be carried out material (VOC) by closed pipeline and mechanical seal pump. transferring to reactor 7 Loading Air pollutant Unloading through pipeline to tank in a close /unloading at (VOC) system. storage area

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

1. ETP Waste From ETP plant 35.3 185 Collection, Storage, Transportation, Disposal at TSDF site at M/s. BEIL- Dahej.

2. MEE salt From MEE 35.3 185 Collection, Storage, Transportation and disposal at TSDF site at M/s. BEIL-Dahej

3. Used Oil From Lubrication 5.1 1 Collection, Storage & Reused within the premises.

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4 Discarded 33.1 Packing 5 Collection, storage, Drums/Empty of raw transportation & disposal Barrels/ materials. by selling to GPCB Containers / authorized recycler Bag/Liners

5. Spent Caron/ Production process 28.3 36 Collection, Storage, of product No. Transportation & send to Hyflow Incineration/ Co- 1,2,3,4,7,9,10,17,18, processing. 20,24,25,27,30,32,4 1,43

6. Spent Generated from 28.2 30 Collection, Storage, and Catalyst product sell to regenerator unit.

No.6,29,43,46,47

7. Distillation From Solvent 28.1 125 Collection, storage, Residue Recovery Unit Transportation & Send to incineration./Co- processing unit.

8 Date expired From Manufacturing 28.5 0.5 Collection, storage, Product activity transportation, incineration in common 9 Off- From Manufacturing 28.4 1 incinerator/ Co- specification activity processing. Product

10 Spent From process no:- B15 2250 Collection, Storage and Sulfuric acid 46 Sell to those units who

(30% to 40%) are having permission of

rule-9 or who have

applied under rule-9.

11. Liquor From manufacturing B15 1080 Collection, Storage and Ammonia activity : Sell to those units who

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(10% to 15%) 12,17,32,34,43,45 are having permission of rule-9 or who have applied under rule-9.

12. Recoverable From manufacturing 28.6 2500 Collection, Storage and Solvent activity distil the solvent by in house distillation and reused within the process.

13. Stripped From Stripper 28.6 365 Collection, storage, and Solvent send to GPCB authorized distillation units.

14. Scrubber From Scrubber -- 100 Collection, storage, and Solution – send to ETP. (Sodium Bromide solution (low concentration )

15. Scrubber From Scrubber -- 330 Collection, storage and Solution – send into ETP. (Hcl solution )(10% to 12%)

16. Scrubber From Scrubber -- 200 Collection, storage, and Solution – send to ETP. (SBS solution) (low concentration )

17. Scrubber From Scrubber -- 100 Collection, storage, and Solution – send to ETP. (Ammonium sulphate

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solution (low concentration )

ii Membership details of TSDF, CHWIF etc. Unit will obtain membership of TSDF and (For HW management) incineration after getting TOR. iii Details of Non-Hazardous waste & its disposal MSW waste will be collected by notified (MSW and others) authority of GIDC.

Sr. Waste Quantity Mode Of Disposal No.

1. Glass Waste ( Z13) 0.01 MT/month To TSDF.

2. Paper waste (Z44) 0.1 MT/month At notified area facility.

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

Name of Name of Solvent Representative used Solvent Solvent Product Quantity recover Solvent used in Quantity Recovered Percentage ton per in Ton per Quantity in Recovery ton of ton of MT/Month product product

Dimethyl 40 38 1.92 96% Sulfoxide

Acetone 82 79 3.93 96%

Acetonitrile 29 28 1.40 96%

Luliconazole Hexane 8 7.7 0.38 96%

Methylene 259 249 12.43 96%

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Chloride

Ethyl Acetate 207 199 9.95 96%

Acetone 16 15.36 7.68 96%

Methylene 55 52.8 26.4 96% Dichloride

Isopropyl alcohol 10 9.6 4.8 96% Olmesartan Toluene Medoxomil0 8 7.68 3.84 96%

Ethyl Acetate 30 28.8 14.4 96%

Tetrahydrofuran 7 6.72 3.36 96%

1,2- 30 29 2.88 96% Dichloroethane

Hexane 11 10.56 1.06 96%

Methylene 23 22.08 2.21 96% Nebivolol Hcl Dichloride Dimethyl 4.2 4.03 0.40 96% Sulfoxide

Tetrahydrofuran 15 14 1.44 96%

Methanol 3.6 3 0.35 96%

Ethyl Acetate 0.14 0.13 0.013 96%

Methanol 1.27 1.20 0.12 96%

Linagliptin Toluene 0.83 0.79 0.079 96%

Methyl tertary butyl ether 0.44 0.4 0.04 96%

Toluene 8 7.68 0.77 96% Levalbuterol Hcl Ethanol 1.2 1.15 0.12 96%

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Methanol 0.4 0.37 0.04 96%

Isopropyl alcohol 3 2.89 0.29 96%

Methylene chloride 38 36.48 36.48 96%

Ethyl acetate 6 5.4 5.4 96%

Fluconazole Toluene 2 1.93 1.93 96% Acetone 2 1.9 1.9 96%

Methanol 0.07 0.06 0.06 96%

Isopropyl alcohol 0.07 0.06 0.06 96%

ACETONE 17.3 16 16 96%

Ethylene dichloride 8 7.96 7.96 96% Telmisartan

Isopropyl alcohol 5 4.8 4.8 96%

Methanol 24 23.04 23.04 96%

Acetone 8 7.68 1.53 96%

Methanol Glimperide 20 19.2 3.84 96%

Toluene 2 1.92 0.38 96%

Isopropyl Alcohol 10 9.6 9.6 96% Etoricoxib

Methanol 10 9.6 9.6 96%

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Toluene 55 52.8 52.8 96%

THF 23 22.08 22.08 96%

ii VOC emission sources and its mitigation measures ‹ Provision of mechanical seal in pump. ‹ Regular inspection of tank roof seals. ‹ Adequate measures for the minimization/prevention of the fugitive emission. ‹ Regular maintenance of valves, pumps and other equipment to prevent leakage. ‹ Entire process to be carried out in the closed reactor with proper maintenance of temperature. ‹ Regular periodic monitoring of work area to check the fugitive emission. ‹ Adequate stack heights as per the GPCB estimation will be provides at all locations to reduce GLCs of pollutants. ‹ Air Pollution Control System will be installed in the plant. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks (Storage Tank,HDPE Storage Tank,Cylinderetc) Acetone --- U/G MS TANK Methanol -- Toluene --

‹ Applicability of PESO : Not Applicable

• Technical presentation was made by the project proponent with consultant/expert M/s. Jyoti Om Chemical Research, Surat during SEAC meeting dated 17/12/2019. • Committee noted that this proposal is for new unit located in GIDC Jhagadia. Source of Water is GIDC. Committee noted that PP has proposed product profile which has 29 groups and 47 products. Further Committee noted that PP has mentioned project cost of 4 crore which is too less if compared with product profile and groups to be manufactured and asked PP to clarify the same. PP clarified that they are only going to manufacture 4 to 5 products at a time however they could not clarify on the number of glass line vessel & reactor that they are going to install. Further Committee asked PP to clarify the storage facility to sell all the intermediates in each groups however PP was not able to clarify the same. Further Committee asked PP to give proper justification pertaining to area adequacy for storage of huge raw material which is going to be

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manufactured in area of 2972 sq.mt which is having 747 sq.mt of green belt area however PP was not able to justify the same. • After detailed discussion, it was decided to defer the proposal and call back the project proponent for presentation only after satisfactory submission of following details with revised PFR & Project Details: 1. Revised Proposal with proper bifurcation of Project Cost viz (1) Plant & Machinery, (2) Building & Construction & (3) Land Cost along Technical Details of Number of Glass Line Reactors, Reaction vessels and Input of Fixed Cost for Plant & Machinery like Piping, Boiler, storage vessels etc. 2. Revised Product Profile with Intermediates Groups Manufacturing in line with area available for storage of Raw Material and Products within premises considering all the safety aspects. 14 SIA/GJ/IND2/43086/2019 M/S. Delta Finochem Pvt Ltd ToR – Reconsideration Plot No. C-192, Saykha Indu. Estate, Sr. No.276/P,277/P, Saykha, Vagra, Bharuch.

Category of the unit: 5(f) Project status: New • This office has received an application vide their online proposal no. SIA/GJ/IND2/43086/2019 dated 24/10/2019 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 new unit proposes for manufacturing of synthetic organic product as tabulated below: Sr. Name of the CAS no. /CI no. Quantity End-use of the products No. Products MT/Month Group A 1. Quaternary Compound (Use in Tetra Butyl Ammonium 1643-19-2 pharma, dyes & chemical Bromide industries) 2. Quaternary Compound (Use in Tetra Butyl Ammonium 32503-27-8 pharma, dyes & chemical Hydrogen Sulphate industries) 3. Quaternary Compound (Use in Tetra Butyl Ammonium 311-28-4 pharma, dyes & chemical Iodide industries) 4. Ethyl Quaternary Compound (Use in TriphenylPhosphoniu 1530-32-1 pharma, dyes & chemical m Iodide industries)

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5. 1250 Quaternary Compound (Use in Tetra Ethyl Ammonium 71-91-0 pharma, dyes & chemical Bromide industries) 6. Quaternary Compound (Use in Tetrabutyl Ammonium 3109-63-5 pharma, dyes & chemical Hexafluoro Phosphate industries) 7. Quaternary Compound (Use in Tetrapropyl 1941-30-6 pharma, dyes & chemical Ammonium Bromide industries) 8. Ethyl Quaternary Compound (Use in TriphenylPhosphoniu 1530-32-1 pharma, dyes & chemical m Bromide industries) 9. Quaternary Compound (Use in TetraphenylPhosphoni 2751-90-8 pharma, dyes & chemical um Bromide industries) 10. Methyl Quaternary Compound (Use in TriphenylPhosphoniu 1779-49-3 pharma, dyes & chemical m Bromide industries) 11. Quaternary Compound (Use in Phenyl Trimethyl 16056-11-4 pharma, dyes &chemical Ammonium Bromide industries) 12. Quaternary Compound (Use in Phenyl Trimethyl 4207-56-1 pharma, dyes & chemical Ammonium Tribromide industries) 13. Quaternary Compound (Use in Tetrabutyl Ammonium 38932-80-8 pharma, dyes & chemical Tribromide industries) 14. Methyl Quaternary Compound (Use in TriphenylPhosphoniu 2065-66-9 pharma, dyes & chemical m Iodide industries) 15. Butyl Quaternary Compound (Use in TriphenylPhosphoniu 13371-17-0 pharma, dyes & chemical m Chloride industries) 16. Benzyl Quaternary Compound (Use in TriphenylPhosphoniu 1100-88-5 pharma, dyes & chemical m Chloride industries)

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17. Quaternary Compound (Use in Tetra Methyl 75-57-0 pharma, dyes & chemical Ammonium Chloride industries) 18. Quaternary Compound (Use in Tetra Ethyl Ammonium 56-34-8 pharma, dyes & chemical Chloride industries) 19. Quaternary Compound (Use in Methyl Trioctyl 63393-96-4 pharma, dyes & chemical Ammonium Chloride industries) 20. Quaternary Compound (Use in Methyl Tributyl 56375-79-2 pharma, dyes & chemical Ammonium Chloride industries) Total (Group A) 1250 Group B 21. Tetra Butyl Ammonium Quaternary Compound (Use in Bromide Solution In 1643-19-2 25 pharma, dyes & chemical Water 50% industries) 22. Tetra Butyl Ammonium Quaternary Compound (Use in Hydrogen Sulphate 32503-27-8 10 pharma, dyes & chemical 55% Solution I Water industries) 23. Quaternary Compound (Use in Tetraethylammonium 429-06-1 5 pharma, dyes & chemical Tetrafluoroborate industries) Total (Group B) 40 Group C Bromide 24. N-Hexyl Bromide 111-25-1 200 (Use in pharma & dyes Industries)

Alpha Bromo 2 Bromide 25. Chlorophenyl Acetic 29270-30-2 10 (Use in pharma & dyes Industries) Acid Methyl Alpha-Bromo- Bromide 26. 2-Chlorophenyl 85259-19-4 30 (Use in pharma & dyes Industries) Acetate Bromide 27. 4 Bromo Anisole 104-92-7 150 (Use in pharma & dyes Industries)

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Bromide 28. Decyl Bromide 112-29-8 30 (Use in pharma & dyes Industries) Bromide 29. 1 4 Dibromobutane 110-52-1 80 (Use in pharma & dyes Industries) Bromo Acetaldehyde Bromide 30. Dimethyl Acetal 7252-83-7 5 (Use in pharma & dyes Industries) (BADIMA) Bromoacetaldehyde Bromide 31. 2032-35-1 2 Diethyl Acetal (Use in pharma & dyes Industries) 3 Bromide 32. 2142-63-4 2 BromoAcetophenone (Use in pharma & dyes Industries) BromoTrichloro Bromide 33. 21928-51-8 1 Benzene (Use in pharma & dyes Industries) Chloroacetaldehyde Bromide 34. 97-97-2 30 Dimethyl Acetal (Use in pharma & dyes Industries) 2-Chloromethyl-1,3- Bromide 35. 2568-30-1 5 Dioxolane (Use in pharma & dyes Industries) 4 Bromo Bromide 36. 1122-91-4 10 Benzaldehyde (Use in pharma & dyes Industries) Bromide 37. N-Propyl Bromide 106-94-5 150 (Use in pharma & dyes Industries) Bromide 38. N-Butyl Bromide 109-65-9 150 (Use in pharma & dyes Industries) Bromide 39. Cyclopentyl Bromide 137-43-9 20 (Use in pharma & dyes Industries) Bromide 40. N- Pentyl Bromide 110-53-2 10 (Use in pharma & dyes Industries) Bromide 41. Cetyl Bromide 57-09-0 20 (Use in pharma & dyes Industries) Bromide 42. Isobutyl Bromide 78-77-3 20 (Use in pharma & dyes Industries) 1 Bromo 5 Chloro Bromide 43. 54512-75-3 10 Pentane (Use in pharma & dyes Industries) Bromide 44. 1,3 Dibromopropane 627-15-6 40 (Use in pharma & dyes Industries) 45. 4bromo phenetole 588-96-5 16 Bromide

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(Use in pharma & dyes Industries) Bromide 46. Lauryl Bromide 143-15-7 20 (Use in pharma & dyes Industries) Bromide 47. Myristyl Bromide 112-71-0 3 (Use in pharma & dyes Industries) Bromide 48. N- Octyl Bromide 111-83-1 20 (Use in pharma & dyes Industries) Bromide 49. N- Octyl Chloride 111-85-3 40 (Use in pharma & dyes Industries) Total (Group C) 1074 Group D 50. 2 Amino Diphenyl Intermediate 1134-94-7 Sulfide 15 (Use in pharma industries) 51. 25 Intermediate Dibenzothiazepinone 03159-07-7 (Use in pharma industries) 52. 60 Intermediate Amino Propanediol 61278-21-5 (Use in pharma industries) 53. Tri Ethyl Phosphono 40 Intermediate 867-13-0 Acetate (Use in pharma industries) 54. Tri Methyl Phosphono 10 Intermediate 5927-18-4 Acetate (Use in pharma industries) 55. Dimethyl Amino 20 Intermediate Isopropyl Chloride 4584-49-0 (Use in pharma industries) Hydrochloride 56. 20 Intermediate Thioanisole 100-68-5 (Use in pharma industries) 57. 10 Intermediate Phenetole 103-73-1 (Use in pharma industries) 58. 5 Intermediate Net Acid 42017-89-0 (Use in pharma industries) 59. 2 Intermediate Flavone Acid 525-82-6 (Use in pharma industries) 60. LSP Amine (S)-2- 2 Intermediate (Aminomethyl)-1- 22795-99-9 (Use in pharma industries) ethylpyrrolidine 61. Anisole 100-66-3 30 Intermediate

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(Use in pharma industries) 62. Dimethylamino 10 Intermediate 42751-79-1 Ethylene Diamine (Use in pharma industries) 63. 40 Intermediate Methoxy (Use in pharma industries) 593-56-6 Hydroxylamine HCl

64. 20 Intermediate 2-(Furan-2-Yl)-2-(Syn- (Use in pharma industries) Methoxyimino) Acetic 39684-61-2 Acid

65. 50 Intermediate Dihydroxy Dithiane 40018-26-6 (Use in pharma industries)

66. 30 Intermediate Orotic Acid 50887-69-9 (Use in pharma industries)

67. 2 Amino Benzyl 2 Intermediate 5344-90-1 Alcohol (Use in pharma industries)

68. 8 Intermediate 1 Amino 4 Cyclopentyl (Use in pharma industries) 61379-64-4 Piperazine

Total (Group D) 399

Total (Group A+B+C+D) 2763

Note: • Unit will manufacture any of the products from Group A on either/or basis and total production capacity of Group A shall not exceed 1250 MT/Month. • Unit will manufacture any of the products from Group B, C and D as per individual quantity prescribed. • Products from Group A, B, C & D will be manufacture at the same time. Total production capacity shall not exceed 2763 MT /month. • 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 17/12/2019.

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• Salient features of the project including Water, Air and Hazardous waste management: Sr. Particulars Details no. A A Total cost of Proposed Project Rs. 22.4264 Crores (Rs. in Crores):

B Total Plot area ( sq. meter) 28146.66Sq. m.

Green belt area 7000 Sq. m. ( sq. meter) C Employment generation 132

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

ii Water consumption (KLD) Category Quantity KLD (P) Domestic 6.00 (Q) Gardening 28.0 (R) Industrial Process 91.0 Washing 10.0 Boiler 120.0 Cooling 15.0 Others (scrubber) 5.0 Industrial Total 241.0 Total (A + B + C) 275.0

1) Total water requirement for the project: 275.0 KLD 2) Quantity to be recycled : 79.20 KLD 3) Total fresh water requirement: 195.80 KLD

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iii Waste water generation (KLD) Category Waste water Remarks KLD (N) Domestic 5.0 (O) Industrial Process 64.0 Washing 10.0 Boiler 6.0 Cooling 1.0 Others (Scrubber) 2.0 Total Industrial waste 83.00 water Total [A + B] 88.00 - iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ Unit will install in-house ETP of capacity 25.0 KLD having Primary, Secondary and Tertiary treatment. ‹ In house MEE (Capacity: 5 KL/hr)

Treatment scheme including segregation at source.

‹ Industrial wastewater generated from manufacturing process and other ancillary operation shall be segregated in two different streams like low COD and high COD stream.

Low COD stream of effluent generated from utility and washing will be treated into ETP having primary, secondary & tertiary treatment and then treated effluent will be sent to RO plant from where RO permeate water will be again reused in process and RO rejected water will be allowed into in-house MEE.

High COD stream of effluent generated from process will be collected in separate collection Tank. After pH adjustment, it will be sent to stripper followed by MEE from where water will be concentrated to recover mixed solvent, salt and condensed water will be reused for washing & Boiler. Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water

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(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):

‹ Industrial wastewater generated from manufacturing process and other ancillary operation shall be segregated in two different streams like low COD and high COD stream.

v Mode of Disposal & Final meeting point

Domestic: Domestic effluent shall be disposed in to Septic tank / Soak pit system.

Industrial: Industrial wastewater generated from manufacturing process and other ancillary operation shall be segregated in two different streams like low COD and high COD stream for which two separate collection tanks will be provided. Low COD stream of effluent generated from utility and washing will be treated into ETP having primary, secondary & tertiary treatment and then treated effluent will be sent to RO plant from where RO permeate water will be again reused in process and RO rejected water will be allowed into in-house MEE. High COD stream of effluent generated from process will be collected in separate collection Tank. After pH adjustment, it will be sent to stripper followed by MEE from where water will be concentrated to recover mixed solvent, salt and condensed water will be reused for washing & Boiler. Unit will maintain Zero Liquid Discharge (ZLD) System for Proposed Project.

575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 110 of 178 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

viii Reuse/Recycle details (KLD) Total reuse – 79.20 KLD Source of waste Application area Characteristics of waste Remarks water for reuse with with quantity in water to be reused (COD, regarding quantity in KLD KLD (Where it is BOD, TDS etc.) feasibility to (From where it is used) reuse i.e. coming) RO Permeate – 11.50 Process – 11.50 COD <100 mg/L Feasible for KLD KLD BOD <30 mg/L Reuse TDS <100 mg/L MEE Recovered Boiler – 57.7 KLD COD <500 mg/L Feasible for Water – 67.7 KLD Washing – 10.0 BOD <200 mg/L Reuse KLD TDS <500 mg/L

E Air

575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 111 of 178 i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

- Type of Air Pollution Source of Stack Quantity of Sr. Type of emissions Control emission Height Fuel no. Fuel i.e. Air Measures With Capacity (meter) MT/Day Pollutants (APCM) Adequate Steam Boiler PM 1 Natural 4800 stack height (Capacity – 12.0 m SO Gas SCM/Day 2 will be 3 TPH) NO x provided Adequate Steam Boiler PM 12.0 m Natural 3200 stack height 2 (Capacity – & Gas SCM/day SO 2 will be 2 TPH) 0.15 m NO x provided

Adequate Thermopack PM 3 Natural 2900 stack height (Capacity 2 12.0 m SO Gas SCM/day 2 will be Lac Kcal/Hr.) NO x provided Adequate D.G Set (Stand PM 4 3600 stack height By) (Capacity 5.0 m HSD SO Lit/day 2 will be 550 KVA) NO x provided Adequate D.G Set (Stand PM 5 1632 stack height By) (Capacity 5.0 m HSD SO Lit/day 2 will be 250 KVA) NO x provided - ii Specific Source of emission Type of Stack/Vent Air Pollution Control Sr. no. (Name of the Measures emission Height (meter) Product & (APCM) Process)

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Process Vent – 1 (Product No. 12,13,24, 25, 27 Br 2 Two stage Alkali 1 to 31, 33, 36 to 10.0 m HBr Scrubber 42, 44 to 48, 59, Process – Bromination) Process Vent – 2 (Product No. 34, 49, 59, 65 HCl Two stage Alkali 2 10.0 m Process – Cl 2 Scrubber Friedelcraft reaction) Process Vent – 3

3 (Product No. 26 Two stage Alkali SO 2 10.0 m Process – Scrubber Esterification)

Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) - - iii Fugitive emission details with its mitigation measures: As below: - Sources of fugitive emissions will be from raw material storage area, handling of chemicals, manufacturing process and from vehicle movement on internal road. - To minimize fugitive emission, powder material will be allowed in a vessel through closed loop while liquid material will be charged through pipeline. - Transportation of raw materials & products will be carried out by trolley within premises and minimum manual material handling will be carried, so the fugitive emission due to process activity and material handling will be negligible.

F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type/Name of Specific Source Category and Quantity Management of

575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 113 of 178 no. Hazardous of generation Schedule as (MT/Annum) HW waste (Name of the per HW Activity, Rules. Product etc.) 1 ETP Sludge Effluent 35.3 25.00 Collection, Treatment Plant (Sch. I) MT/year Storage, Transportation and Disposal at TSDF site – for secured landfill 2 MEE Salt MEE 35.3 657.00 Collection, (Sch. I) MT/year Storage, Transportation and Disposal at TSDF site – for secured landfill 3 Used / Spent Oil D. G Set & 5.1 1.0 MT/year Collection, Thermopack (Sch. I) Storage, Transportation and Disposal by selling to Registered Re- refiners approved by GPCB / CPCB / reuse for lubrication 4 Discarded Raw material & 33.1 200 MT/year Collection, Containers / Finished product (Sch. I) Storage, Bags / Liners packing material Transportation and Disposal by selling to registered recycler approved by GPCB / CPCB / reuse within premises 5 Distillation Distillation 20.3 192.12 MT/year Collection, Residue Process (Sch. I) Storage,

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(Product No. 1, 3 Transportation and to 5, 7 to 20, 44, Disposal for co- 46, 47, 48, 49, processing. 58, 59, 62, 63) Solvent 322.00 Recovery Plant MT/year

6 Process Process 28.1 583.00 MT/Year Collection, Residue (Product No. 6, (Sch. I) Storage, 24, 28, 29, 37 to Transportation and 42, 52 to 54, 56, Disposal for 57, 61) incineration OR for co-processing as per CV. 7 Spent Solvent Process 28.6 22068.00 Collection, storage, (Product no. 1 to (Sch. I) MT/year recovered through 5, 7 to 20, 25, in-house distillation 26, 30 to 36, 50, and reuse within 51, 60, 64, 65, premises 67, 68) OR Collection, Stripper (MEE) 0.22 storage and MT/year disposal by selling to distillation unit having valid CTO from GPCB and rule 9 permission to receive this waste 8 Sodium Process 28.1 10000.00 Collection, Bromide (Product no. 6) (Sch. I) MT/year Storage, Solution Transportation & (30-35 %) Disposal by selling to authorized users who are having authorization with valid CCA and rule

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9 permission to receive this waste 9 Hydrogen Process 28.1 23292.50 Collection, Bromide (Product no. 2, (Sch. I) MT/year Storage, Solution 25, 27, 30, 31, Transportation & (30-35%) 33, 36, 45, 59) Disposal by selling to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste 10 Spent Sulfuric Process 28.1 1041.70 Collection, Acid (Product no. 24, (Sch. I) MT/year Storage, (50-55 %) 26, 37 to 42, 48, Transportation & 49) Disposal by selling to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste 11 Phosphoric Acid Process 28.1 2267.13 MT/year Collection, (20 %) (Product no. 28, (Sch. I) Storage, 29, 44, 46, 47, Transportation & 51) Disposal by selling to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste 12 Methyl Acetate By Product 28.1 29.50 Collection, (85 to 90 %) (Product no. 30) (Sch. I) MT/year Storage, Transportation & Disposal by selling

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to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste 13 Dil. HCl Solution Process 28.1 1097.14 Max. quantity (20-25 %) (Product no. 34) (Sch. I) MT/year (500.00 MT/year) will be reuse within premises & balance quantity (597.14 MT/year) will be disposed by selling to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste 14 Liquor Ammonia Process 28.1 112.70 MT/year Collection, Storage (15-20 %) (Prod. No. 62) (Sch. I) & entire quantity (100 %) will be reuse as raw material in Process within premises. 15 Sodium By product 28.1 857.14 MT/year Collection, Chloride (Prod. No. 63) (Sch. I) Storage, (30-35 %) Transportation & Disposal by selling to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste

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16 Methanol Process 28.1 444.0 MT/year Collection, (80 - 85%) (Product no. 35, (Sch. I) Storage, 63) Transportation & Disposal by selling to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste 17 2 Bromo By Product 28.1 33.00 Collection, Phenetole (Product no. 45) (Sch. I) MT/year Storage, (92 - 95%) Transportation & Disposal by selling to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste 18 Off Specification Mfg. Process 28.4 28.0 MT/Year Collection, Products (Batch failure) (Sch-I) Storage, Transportation and sent for co- processing. - ii Membership details of TSDF, CHWIF etc. Unit will get Membership of TSDF (For HW management) site. iii Details of Non-Hazardous waste & its disposal (MSW and others)

Sr. Source of Category Type of Waste Disposal No. Generation of Waste

1. Domestic Waste Employees MSW Collected in separate bin

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(Food waste, Plastic, working in the and disposed to bin of Paper etc.) premises GIDC.

Industrial Waste Steam Pipe & 2. (Glass wool [Insulating ISW Sell to local scrap vendor Vessels Material, Scrap])

From Raw Industrial Waste 3. Material & Product ISW Sell to local scrap vender (Wooden pellets) storage area

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

Product Name of Product Name of the Generation Recovered Recovery No. Solvent Quantity (MT/Month) Efficiency % (MT/Month) 1 Tetra Butyl Ammonium Ethyl Acetate 585.94 574.22 98.00 Bromide 2 Tetra Butyl Ammonium Methyl 1388.89 1354.17 97.50 Hydrogen Sulphate Isobutyl Keton 3 Tetra Butyl Ammonium Ethyl Acetate 1453.49 1431.69 98.50 Iodide 4 Ethyl Triphenyl Methanol 563.06 554.62 98.50 Phosphonium Iodide 5 Tetra Ethyl Ammonium Ethyl Acetate 559.21 555.92 99.41 Bromide 7 Tetrapropyl Ammonium Ethyl Acetate 651.84 648.01 99.41 Bromide 8 Ethyl Triphenyl Methanol 625.00 606.25 97.00 Phosphonium Bromide 9 Tetraphenyl Methanol 769.23 756.41 98.33 Phosphonium Bromide 10 Methyl Triphenyl Methanol 789.47 776.32 98.36 Phosphonium Bromide

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11 Phenyl Trimethyl Methanol 455.93 450.23 98.75 Ammonium Bromide 12 Phenyl Trimethyl Methanol 454.55 446.97 98.33 Ammonium Tribromide 13 Tetrabutyl Ammonium Methanol 528.17 519.37 98.33 Tribromide 14 Methyl Triphenyl Methanol 761.42 748.73 98.33 Phosphonium Iodide 15 Butyl Triphenyl Methanol 1000.00 983.33 98.33 Phosphonium Chloride 16 Benzyl Triphenyl Methanol 654.76 642.86 98.18 Phosphonium Chloride 17 Tetra Methyl Ammonium Ethyl Acetate 441.18 430.15 97.50 Chloride 18 Tetra Ethyl Ammonium Ethyl Acetate 508.47 495.76 97.50 Chloride 19 Methyl Trioctyl Ethyl Acetate 728.16 709.95 97.50 Ammonium Chloride

20 Methyl Tributyl Ethyl Acetate 454.55 443.18 97.50 Ammonium Chloride 25 Alpha Bromo 2 Toluene 10.13 9.95 98.25 Chlorophenyl Acetic Acid 26 Methyl Alpha-Bromo-2- MDC 23.08 22.77 98.67 Chlorophenyl Acetate Methanol 9.23 9.08 98.33 30 Bromo Acetaldehyde MDC 6.14 5.96 97.14 Dimethyl Acetal (Badima) 31 Bromoacetaldehyde Methylene 2.11 2.05 97.16 Diethyl Acetal (Badiea) Dichloride 32 3 Bromo Acetophenone Methanol 1.28 1.26 98.33 33 Bromo Trichloro Benzene Methanol 0.57 0.55 96.25 34 Chloroacetaldehyde Methanol 35.71 35.0 98.00 Dimethyl Acetal Methylene 50.00 48.93 97.86 Dichloride 35 2-Chloromethyl-1,3- Cyclohexane 5.71 5.50 96.25 Dioxolane

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36 4 Bromo Benzaldehyde Methanol 10.0 9.86 98.57 50 2 Amino Diphenyl Sulfide Methanol 13.33 12.89 96.67 51 Dibenzothiazepinone Methanol 57.14 55.71 97.50 Toluene 71.43 69.64 97.50 60 LSP Amine Methanol 5.12 5.01 98.00 64 2-(Furan-2-Yl)-2-(Syn- Acetone 14.46 14.22 98.33 Methoxyimino) Acetic Acid 65 Dihydroxy Dithiane Methanol 44.44 43.52 97.92 67 2 Amino Benzyl Alcohol Methanol 7.79 7.64 98.00 68 1 Amino 4 Cyclopentyl Methanol 8.59 8.40 97.81 Piperazine

ii VOC emission sources and its mitigation measures ‹ VOCs generation will be from storage and usage of raw materials. ‹ VOC analysers will be provided to detect any solvent leakages during storage and handling. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks Storage tanks Acetone, Bromine, Methanol, Ethyl Acetate, Methylene Dichloride, N- Butanol , N- Decanol, N- Hexanol , N- Propanol , Tri Butyl Amine, Tri Ethyl Amine Drum/Barrel storage Acetic Acid, Acetonitrile, Benzyl Chloride, Butyl Chloride, Chloroform, Cyclohexane, Cyclopentanol , Diethyl Sulphate, Dimethyl amino Ethanol, Ethyl Bromide, Ethyl Iodide, Iso Butanol, Liquid Ammonia, Methyl Chloro Acetate, Methyl Iodide, Methyl Isobutyl Keton, Methylene Glycol, N-Butyl Iodide, N-Octanol, Pentanol , Phenol, Sulfuric Acid, Thionyl Chloride, Thiophenol

‹ Applicability of PESO : Applicable, Permission will be taken. • Technical presentation was made by the project proponent with consultant/expert M/s. Jyoti Om Chemical Research, Surat during SEAC meeting dated 14/11/2019. • During SEAC meeting, committee noted that the proposal is for Greenfield Project in GIDC Saykha. PP mentioned that treated effluent will be sent to CETP Saykha after in-house ETP treatment. Committee asked about scale of the unit, PP informed that it is large scale unit. Committee disagree with disposal of effluent in CETP Saykha as SEIAA accorded EC to CETP Saykha with specific condition of CETP is for only SSI units and submit revised proposal with disposal of effluent other than CETP Saykha. • After detailed discussion, it was decided to defer the proposal and consider the same in one of the upcoming

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meeting of SEAC only after submission of the following documents. 1. Submit revised proposal for waste water disposal other than CETP Saykha as CETP Saykha is only for SSI units. • Project proponent was called for presentation for the above mentioned query dated 17/12/2019 for the above mentioned points. • PP mentioned that they have revised their proposal to ZLD by proposing stripper & MEE in High Concentrated Stream while ETP & RO for low concentrated stream. Committee noted on the changes made by PP and asked them to clarify worst case scenario for all the products group wise for which changes have been incorporated however PP mentioned that they have not brought the excel sheet in which worst case scenario has been calculated for all the products group wise. Committee asked PP to clarify High & Low COD stream for which they have made segregation however PP was not able to clarify the same. Further Committee noted that PP has selected range for High & Low COD/BOD/TSS/TDS for segregation of effluent stream which is not addressed satisfactorily. Further PP has not properly justified decrease in water consumption and generation in line with their earlier proposal. Committee noted that there is huge decrease in quantity of some waste in Hazardous Waste Matrix due to change in Product profile and their group and asked PP to clarify the same with worst case scenario however PP was not able to clarify or justify the same. • After detailed discussion, it was decided to consider the proposal only after satisfactory submission of following documents: 1. Worst Case Scenario for all the Products Group Wise along with Comparison with Original Proposal and Increase or Decrease in Production (If any). 2. Water Consumption & Waste Water Generation Table with Input of Segregation Stream for all the Parameters along with Comparison with Original Proposal mentioning Increase or Decrease in Water Consumption or generation (If any). 3. Justification of Decrease in Hazardous Waste as Compared to Original Proposal along with Worst Case Scenario for Hazardous Waste Matrix in Present Proposal for all the Hazardous Waste Generated. 15 SIA/GJ/IND2/43968/2019 M/S. M R Chemicals Screening & Scoping Plot No. 141, Phase No. II, GIDC, Naroda, Ahmedabad.

Category of the unit: 5(f) Project status: New • This office has received an application vide their online proposal no. SIA/GJ/IND2/43968/2019 dated 13/11/2019 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 new unit proposes for manufacturing of synthetic organic product as tabulated below:

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Sr. CAS No. / CI Quantity, MT/Month End-use of Name of the Products No. Name. Existing Additional Total product 6 Acetyl OAPSA 1. (Ortho Amino Phenol 4 40306-75-0 15 0 15 Sulfonic Acid) 2. Formazane Blue FR and/or -- 20 65 4,4 Diamino, 2,2, 3. Disulphanic Acid (DDSA) 81-11-8 -- 85 and/or 4, Sulfo Anthranilic Acid 4. 98-43-1 -- 85 and/or Hydrazone of 4-Sulfo 5. Anthranilic Acid 77734-52-2 -- 85 and/or 6. Metanilic Acid and/or 121-47-1 -- 85 Aniline 2,5 DSA (Di 7. 98-44-2 -- 85 Manufacturi Sulphonic Acid) and/or ng of Aniline 2,4 DSA (Di 8. 137-51-9 -- 85 Reactive Sulphonic Acid) and/or 85 synthesis & Sulpho Formazone Blue 9. -- -- 85 Dyes and/or 4,5 Nitro Ortho Anisidine 10. 97-52-9 -- 85 and/or Amino Azo Benzene 4 11. Sulphonic acid (AABS) 104-23-4 -- 85 and/or 12. Bourdex GP and/or 96 - 96 - 8 -- 85 4,4 Dinitro Stilbene 2,2, 13. Disulphonic Acid (Sodium 128-47-7 -- 85 Salt) (DNSDA) and/or Meta Nitro Para Toluidine 14. 119-32-4 -- 85 (MNPT) and/or 15. Sodium Acetate 127-09-3 -- 85 Total 35 *65 / *85 100 Note:Out of existing two products, production capacity of 6-Acetyl OAPSA will remain unchanged. The product Formazone Blue FR will be put in blend of product and total of 14 products will never cross 85

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MT/month. Thus, total production will be 100 MT/month after the proposed expansion. Where *65 is for Formazane Blue FR and *85 is for other remaining products except 6-Acetyl OAPSA . • 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 17/12/2019. • Salient features of the project including Water, Air and Hazardous waste management: Sr. Particulars Details no Existing:1.0 Crore Total cost of Proposed Project A Proposed: 2.0 Crores (Rs. in Crores): Total: 3.0 Crores Existing: 2816 Sq. m. Total Plot area B Proposed: 0 Sq. m. ( sq. meter) Total: 2816Sq. m. Existing: 100 Sq. m. Green belt area Proposed: Nil. ( sq. meter) Total: 100 Sq. m. Existing: 25 C Employment generation Proposed: 25 Total: 50 D Water Source of Water Supply GIDC water supply dept. i (GIDC Bore well, Surface water, Tanker supply etc...) Permission for proposed expansion to Status of permission from the concern authority. be taken. Water consumption (KLD) Existing Proposed Total after Category Remarks KLD (Additional) Expansion (A) Domestic 3.0 KLD 4.0 KLD 7.0 (B) Industrial Boiler 2.0 5.0 7.0 ii Cooling 1.0 1.0 2.0 Manufacturing 8.0 31.5 39.5 Washing 1.5 3.0 4.5 Others (APCM) 0 0.5 0.5 Industrial Total 12.5 41.0 53.5

Grand Total (A+B) 15.5 45.0 60.5

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1) Total water requirement for the project: 60.5 KLD 2) Quantity to be recycled: 0.0 KLD

3) Total fresh water requirement: 60.5 KLD (Total water requirement = Fresh water + Recycled water) Waste water generation (KLD) Existing Proposed Total after Category Remarks KLD (Additional) Expansion

(A) Domestic 3.0 KLD 3.0 KLD 6.0 To CETP (After Soak Pit) (B) Industrial Boiler 1.0 0.5 1.5 iii Cooling 1.0 0.0 1.0 Primary treatment Manufacturing 10.0 18.7 28.7 in ETP Washing 4 0.3 4.3 Others (APCM) 0 0.5 0.5 Total Industrial waste 16.0 20.0 36.0 water Grand Total (A+B) 19.0 23.0 42.0

Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Sr. Description Volume (in m 3) No. A Treatment for weak (Dilute) stream (max 16 KLD)) 1. Collection tank-1 20 2. Collection tank-2 20 3. Neutralization Tank 20 4. Nutsche Filter 20 iv 5. Filter press 36” x 36 “ 6. Holding Tank 20 B Treatment for concentrated stream (min 16 KLD) (max 36 KLD) 1. Collection tank 20 2. Neutralization Tank 20 3. Holding tank 20

Treatment scheme including segregation at source. ‹ The effluent coming out from the process is taken to collection tank. ‹ The effluent is pumped to the equalization tank where sufficient retention time should be provides

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for Collection Cum Neutralization Tank of pH and other characteristics of incoming effluent. If required dosing of chemicals will be carried out in this tank as per requirement of pH Correction. The wastewater after chemical treatment shall be taken to filter press. The filtrate from the filter press shall be sent to NEPL CETP by tanker. ‹ The sludge from the filter press shall be sent to TSDF facility. 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 . ‹ The Total Industrial waste water generated from manufacturing process will be 36 KLD, out of which 16 KLD will be discharged to CETP of NEPL and remaining 20 KLD will be sent to common Spray drier for the Evaporation. The spent acid 40 KLD will be sent to the Common facility Management units or to the actual user (M/s Shree Cements Ltd.) ‹ The domestic effluent 6 KLD shall be discharged in the CETP (After Soak Pit). Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Not Applicable

Mode of Disposal & Final meeting point

The domestic effluent 6.0 KLD shall be discharged in the CETP (After Soak Domestic: Pit). v The Total Industrial waste water generated from manufacturing process will be 36 KLD, out of which 16 KLD will be discharged to CETP of NEPL and Industrial: remaining 20 KLD will be sent to common Spray drier for the Evaporation. The spent acid 40 KLD will be sent to the Common facility Management units or to the actual user (M/s Shree Cements Ltd.)

In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF)(For waste water treatment)

‹ CETP and common MEE vi Membership of Common facility (CF)

(For waste water treatment) ‹ Common Evaporation Facility – Society for Clean Earth (Vatva) and Society for clean and Green Environment (Naroda) ‹ CETP – NEPL (Naroda Enviro Project Ltd.) vii Simplified water balance diagram with reuse / recycle of waste water

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Total Water Consumption 60.5 KLD

Industrial Domestic 53.5 KLD 7.0 KLD

6.0 KLD to CETP(After Soak Pit)

Process Boiler Cooling APCM 39.5 KLD 7.0 KLD 2.2 KLD Washing 0.5 KLD 4.5 KLD

28.7 1.5 1.0 4.3 0.5

40 KLD spent acid to actual user (M/s Shree Cements Ltd.)

CETP of ETP (Primary Evaporation NEPL, 16 Treatment) 36 (Common KLD KLD MEE), 20 KLD

Reuse/Recycle details (KLD) [Source of reuse & application area]

Total reuse 0 KLD - vii Source of waste water Application area Remarks Characteristics of waste for reuse with quantity with quantity in regarding water to be reused (COD, in KLD (From where it KLD (Where it is feasibility to BOD, TDS etc.) is coming) used) reuse i.e. None

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

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

Boiler - 1 TPH 2700 (SCM/ Day) PM < 150 1. 12 Natural Gas Not (Existing) = mg/Nm3 Applicable 900 SCM/ Day SO2< 100 other than Boiler (1 TPH) (existing) + ppm 2. 12 Natural Gas adequate (Proposed) 1800 SCM/ Day NOx< 50 stack Height (Proposed) ppm

PM < 150 Not mg/Nm3 D.G. Set - 125 Applicable SO2< 100 3. KVA 5 HSD 120 Litre/day other than ppm (Proposed) adequate NOx< 50 stack Height ppm

Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) ii Existing & Proposed - None - Specific Source of Air Pollution Type of emission Stack/Vent Control Sr. No emissions i.e. Air (Name of the Product & Height (meter) Measures Pollutants Process) (APCM) Reactor-1 Two Stage Alkali 3 1 SO 3< 40 mg/Nm 12 m (Proposed) Scrubber Reactor-2 Two Stage Alkali 3 2 SO 3< 40 mg/Nm 12 m (Proposed) Scrubber

iii Fugitive emission details with its mitigation measures. During operation stage, leakage through valves, pumps, emission from open drum containing chemicals, open feeding; storage tanks, etc. are the major sources of fugitive emissions of organic chemicals and VOCs. Excess use of solvent may also results fugitive emission from the process vessels. Mitigation

Measures given below: The proposed activity would be taken in the building and hence the emissions would be limited to the premised.

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° 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. ° 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, produce raw material storage area shall be monitored regularly. Hazardous waste F (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Existing & Proposed

Specific Quantity Category Type/Name Source of (MT/Annum) and Sr. of generation Schedule Management of HW no. Hazardous (Name of the as per HW Existing Proposed Total waste Activity, Rules. Product etc.) Collection, Storage, Transportation, i Effluent 1 ETP Waste 35.3 60 1190 1250 Disposal at TSDF treatment approved by the Board. Collection, Storage, Process Area transportation, (Metanilic Acid, disposal by Co- 2 Iron Sludge 26.1 300 900 1200 6-Acetyl processing or at OAPSA) CHWIF approved by the board

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Collection, Storage, Manufacturing transportation, Gypsum Process 3 26.1 0 3000 3000 disposal by Co- Sludge (DDSA, processing at CHWIF Metanilic Acid) approved by the board Collection, Storage and dispose to Manufacturing 4 Spent Acid 26.3 0 14400 14400 common facility or sell Process to authorized end user. Collection, Storage, Decontamination, Raw materials Discarded 1800 3000 4800 Transportation, 5 & waste 33.1 Container Nos. Nos. Nos. Disposal by selling to storage authorized recycler or reuse. Collection, Storage Plant & 6 Used Oil 5.1 0.12 0.004 0.124 and sell to registered Machineries recycler

Collection, storage Process gas 7 Bleed liquor 35.1 0 180 180 and reuse or scrubbing disposed in ETP

• The unit has taken membership of TSDF from SEPPL (Saurashtra Enviro Projects Pvt. Ltd) • MOU with M/s Shree Cements Ltd. and Membership details of TSDF, CHWIF etc. ii Membership from Novel Spent Acid Management (For HW management) for Supply of Spent Sulphuric Acid has been obtained. • Gypsum Sludge – Ambuja Cements Ltd. Details of Non-Hazardous waste & its disposal iii Not Applicable (MSW and others) G Solvent management , VOC emissions etc. Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in i Table Format) Name of the Name of the Solvent Solvent Recovery % Loss, %

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Product Solvent Used recovery MNPT (Meta Methylene Di nitro para 870 849 98 2 Chloride (MDC) toluidine) Methylene Bourdex GP 2000 1980 99 1 Dichloride

The unit would recover the solvents through distillation process and would reuse them in the process. ii VOC emission sources and its mitigation measures Mitigation Measures: • Identification of potential areas, where possibility of flammable mixture/VOC are possible. • 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. ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks

1. Acetic Acid These chemicals will H 2. Aniline be stored in the tank Storage tanks 3. Benzaldehyde considering all safety 4. Caustic Lye measures 5. Formaldehyde

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6. Hydrochloric Acid 7. Hydrochloric Acid (30%) 8. Nitric Acid 9. Methylene Di chloride 10. Nitrobenzene 11. Oleum 12. Oleum (65%) 13. O.N.T (Ortho Nitro Toluene) 14. Ortho Anisidine 15. Ortho nitro Benzene 16. Sodium Hydroxide (48%) 17. Sulphuric Acid ((98%) All liquid raw material shall be stored in Drum/Barrel storage -- drum / barrel,

‹ Applicability of PESO : ‹ Not Applicable • Technical presentation was made by the project proponent with consultant/expert M/s. Excel Enviro Tech, Ahmedabad during SEAC meeting dated 17/12/2019. • Committee noted that this proposal is for expansion of unit located in GIDC Naroda. PP mentioned that there is no any court case or litigation pending. PP ensured that there is no any Public Complaint pending. PP mentioned that unit has valid CC&A and has submitted compliance of the same. Committee noted that unit has received four SCN in last three years viz 17/01/2017, 29/07/2017, 11/01/2019 & 24/06/2019 and asked PP justify the same w.r.to expansion scenario however PP could not clarify the same properly. Further committee noted that unit has not addressed product profile clearly. Committee also noted that the spent acid generation from the proposed project is very high @ 14400 MT/Month and disposal method shown is actual users however no any information pertaining to actual users under rule – 9 is shown by PP. Committee also noted that PP has not addressed Hazardous Waste Matrix as per HWR – 2016. • After detailed discussion, it was decided to reconsider the proposalonly after satisfactory submission of the following details along with revised Project details, PFR. 1. Address the Product Profile clearly in such a way that disposal of Hazardous Waste takes in Environmental Sound Manner. 2. Justify your expansion scenario w.r.to SCN received from GPCB in last three years along with Compliance of the same. 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

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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. 16 SIA/GJ/IND2/41158/2019 M/s. Dharti Industries Screening & Scoping Plot No. 57/1, Survey No. 453, Katosan road, Detroj, Ahmedabad. • PP remained absent in the EC – Amendment presentation held on 15/10/2019. • After detailed discussion, Committee decided to defer the proposal and consider the same in one of the upcoming meeting of SEAC. 17 SIA/GJ/IND2/43204/2019 M/s. Yahska Polymers Pvt Ltd Screening & Scoping S. No. 407, Plot No. 15/A, new Ahmedabad Industrial Estate, Moraiya, Sanand, Ahmedabad.

Category of the unit: 5(f) Project status: New • This office has received an application vide their online proposal no. SIA/GJ/IND2/43204/2019 dated 22/11/2019 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 new unit proposes for manufacturing of synthetic organic product as tabulated below: Sr. Quantity End-use of the No. NameofProduct CASNo. (MT/Month) products 1. Admixture(Liquid) ---- 2. Admixture(Powder) ---- Used Phenol

Formaldehyde Condensation as 3. Product 9003-35-4 900.0 Intermediates 4. PolyCarboxylateEther 27599-56-0 forbuildingconstruc Total 900.0 tio n. • 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 17/12/2019. • Salient features of the project including Water, Air and Hazardous waste management: Sr. Particulars Details no.

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A A Total cost of Proposed Project 2.5 Cr (Rs. in Crores): B Total Plot area ( sq. meter) 3080 Sq. m. Green belt area 1020 Sq. m. ( sq. meter) C Employment generation 40 D Water i Source of Water Supply Borewell (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. -- ii Water consumption (KLD) Category Quantity Remarks KLD (S) Domestic 2.0 (T) Gardening 2.0 (U) Industrial

Process 13.6 Boiler 0.5 Cooling 1.0 15.1 Industrial Total 19.1 Total (A + B + C)

1) Total water requirement for the project: 19.1 KLD 2) Quantity to be recycled : 0.15 KLD 3) Total fresh water requirement:18.95 KLD iii Waste water generation (KLD) Category Waste water Remarks KLD (P) Domestic 1.7

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(Q) Industrial Process 0.0 Boiler 0.05 Cooling 0.10 Total Industrial waste water 0.15 Total [A + B] 1.85 - iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ Not applicable Treatment scheme including segregation at source. ‹ Not applicable 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): ‹ Zero Liquid Discharge. v Mode of Disposal & Final meeting point

Domestic: 1.7KLPDdomesticwaste waterwillgotosoakpit viaseptictank.

Industrial: Industrialeffluentgenerationwill be0.15KLPDwhichwill be reusedintheprocessagain. 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.KLD Source of waste Application area Characteristics of waste Remarks water for reuse with with quantity in water to be reused (COD, regarding quantity in KLD KLD (Where it is BOD, TDS etc.) feasibility to (From where it is used) reuse i.e. coming) Industrialeffluentgener Reusedintheproces COD:<10 ationwill sagain. BOD:<2 be0.15KLPDwhichwill TDS:1800-2000 be treatedinprimaryETPan d thenit will bereused

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)

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SteamBoiler(C 228.63SCM/ AdequateStackh 1 apacity;0.5To 12 PNG Day SPM eight n/Hr.)

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

‹ -TherewillbenoanyProcessGasEmission. iii Fugitive emission details with its mitigation measures: As below: • Proper storage of raw materials, products and fuels. • Ensuring closed feeding and sampling. • Establishing SOPs for start-up, shut down and maintenance operational procedures. • Regular work place 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. Type/Name of Specific Category Quantity Management of HW no. Hazardous waste Source of and (MT/Annum) generation Schedule (Name of the as per HW Activity, Rules. Product etc.) 1 Plant Collection,Storage,Tran UsedOil machinery 5.1 10Lit/Year sportation &Disposalbyselling toRegistered ReprocessesorReu seatlubricant.

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2 Raw material Collection, Discarded storage area 2.5 MT Storage, container/ 33.1 Decontamination,Tra Liner/Bags nsportation, andDisposalbyreturnb ackto supplier. - ii Membership details of TSDF, CHWIF etc. We will became a member of (For HW management) TSDF side 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 etc. (Details in Table Format) ‹ There will be no use of solvent. ii VOC emission sources and its mitigation measures ‹ There will be no any VOC emission source. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous Remarks chemicals Storage tanks: 20KL SulfuricAcid Storage tanks:20 KL Oleum Storage tanks: 20 KL SodiumHydroxide Storage tanks:5 KL Formaldehyde

‹ Applicability of PESO : not applicable • Technical presentation was made by the project proponent with consultant/expert M/s. Bhagwati Enviro Care Pvt Ltd, Ahmedabad during SEAC meeting dated 17/12/2019. • Committee noted that this proposal is for new unit located in Village: Moraiya. Source of water is bore well. Committee asked PP to justify criteria of small units for unit located outside GIDC, Complying the three conditions as per the amendment with EIA Notification, 2006 vide SO 1599 (E) dated 25/06/2014. PP mentioned that the Water consumption less than 25 m3/day (19.1 KLD); Fuel consumption is less than 25 TPD (PNG is used as fuel); and not covered in the category of MAH units as per the Management, Storage Import of Hazardous Chemical Rules (MSIHC Rules), 1989] however justification for storage of formaldehyde & Oleum with proper quantity was not shown by PP. Committee asked PP to submit legal undertaking for not

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covered in the category of MAH units as per amendment with EIA Notification, 2006 vide SO 1599 (E) dated 25/06/2014. Committee noted that PP has also not addressed Product Profile correctly and instructed to address the Product Profile correctly with proper CAS No. PP mentioned that effluent generated from boiler blow down & cooling tower blow down will be treated in in-house Primary ETP and treated effluent will be reused back in process by mixing with fresh water. PP has proposed one steam boiler. Fuel used will be PNG. PP has addressed Hazardous Waste as per HWR – 2016. • After detailed discussion, Committee decided to consider the proposal only after submission of the following documents: 1. Legal Undertaking of Complying the three conditions as per the amendment with EIA Notification, 2006 vide SO 1599 (E) dated 25/06/2014. [The Water consumption less than 25 m3/day; Fuel consumption is less than 25 TPD; and not covered in the category of MAH units as per the Management, Storage Import of Hazardous Chemical Rules (MSIHC Rules), 1989]. 2. Address the Product Profile correctly by mentioning Name of product along with its respective CAS No. 18 SIA/GJ/IND2/40359/2019 M/s. Overseas Enterprise ToR – Reconsideration Plot No. 53/5, GIDC Estate, Odhav, Ahmedabad. Category of the unit: 5(f) Project status: Expansion • This office has received an application vide their online proposal no. SIA/GJ/IND2/40359/2019 dated 17/09/2019 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 expansion of existing unit proposes for manufacturing of synthetic organic product as tabulated below: Quantity (MT/Month) Sr. Name of Product CAS No Total after No. Existing Proposed expansion EXISTING PRODUCTS

1. REACTIVE YELLOW M4G 12226-49-2 1.5 --- 1.5 2. REACTIVE ORANGE H2R 12225-85-3 2.5 --- 2.5 PROPOSED PRODUCTS

3. REACTIVE ORANGE HE2R 91261-29-9 --- 4. REACTIVE ORANGE ME2RL 12220-12-1 --- 5. REACTIVE RED ME4BL 93050-79-4 --- 6. REACTIVE YELLOW H4G 12226-48-1 --- 7. REACTIVE YELLOW M8G 61-79-35-0 --- 8. REACTIVE GOLDEN YELLOW MR 12270-91-6 --- 21.0 21.0

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9. REACTIVE GOLDEN YELLOW HR 35642-64-9 --- SOLVENT DYES 10. SOLVENT RED 23 85-86-9 --- 11. SOLVENT RED 24 85-83-6 --- 12. SOLVENT YELLOW 2 60-11-7 ---

13. SOLVENT YELLOW 14 842-07-9 --- 14. SOLVENT YELLOW 56 2481-94-9 --- TOTAL 4.0 21.0 25.0 • 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 17/10/2019. • Salient features of the project including Water, Air and Hazardous waste management: Sr. Particulars Details no. A Total cost of Proposed Project Existing: 0.119 (Rs. in Crores): Proposed: 0.506

Total: 0.625 B Total Plot area Existing: 650.5 Sq. m. ( sq. meter) Proposed: 0.0 Sq. m.

Total: 650.5 Sq. m. Green belt area Existing: 0.0 Sq. m. ( sq. meter) Proposed: 150 Sq. m. (Outside Premises) Total: 150 Sq. m. C Employment generation Existing: 5 Proposed: 7 Total: 12 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

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ii Water consumption (KLD)

Water Consumption (KLD) Application Existing Proposed After expansion

Domestic [A] 0.7 2.5 3.2 Gardening [B] 0.0 0.5 0.5 Industrial [C] Process 3.0 4.9 7.9 Washing 1.0 4.0 5.0 Boiler 0.5 4.0 4.5 Total Industrial [C] 4.5 12.9 17.4

TOTAL 5.2 15.9 21.1 [A+B+C]

1) Total water requirement for the project: 21.1 KLD 2) Quantity to be recycled: 8.83 KLD 3) Total fresh water requirement: 8.57 KLD (Total water requirement = Fresh water + Recycled water) iii Waste water generation (KLD)

Waste water generation (KLD) Application Existing Proposed After expansion

Domestic [A] 0.5 2.0 2.5 Gardening [B] 0.0 0.0 0.0 Industrial [C] Process 2.45 8.17 10.62 Washing 1.0 4.0 5.0 Boiler 0.05 0.45 0.5 Total Industrial [C] 3.5 12.62 16.12

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TOTAL 4.0 14.62 18.62 [A+B+C] Industrial Low concentrated effluent from Boiler blow-down, and plant/floor washing 3.5 KLD will be treated in primary ETP to achieve all the norms in permissible limit and then after send to CETP-OEPL.

Industrial High concentrated effluent from Process and Vessel washing 12.62 KLD will be collected in collection tank and after primary treatment including R.O. treatment 8.83 KLD R.O. permeate will be reused for industrial use and 3.79 KLD of R.O. rejected will be discharge to Common Spray Dryer of OEPL after achieving all norms in permissible limits. iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.. ‹ In-house ETP having Primary treatment units Treatment scheme including segregation at source. ‹ Low concentrated effluent (Including Boiler blow down, plant & floor washing) Treated in existing ETP plant & discharged to CETP after achieving all norms in permissible limits. ‹ High concentrated effluent (Including process effluent & vessel washing) Treated in proposed ETP plant having primary treatment units & it will be discharged to Common Spray dying facility OEPL. 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 . ‹ No additional effluent will discharge to CETP-OEPL, Odhav, Ahmedabad. Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Proposed effluent will be discharged to common spray drying facility to achieve ZLD only after expansion. v Mode of Disposal & Final meeting point

Domestic: To soak pit via septic tank

Industrial: Industrial Low concentrated effluent from Boiler blow-down, and plant/floor washing 3.5 KLD will be treated in primary ETP to achieve all the norms in permissible limit and then after send to CETP-OEPL.

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Spray Dryer of OEPL after achieving all norms in permissible limits. 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) ‹ CETP –Odhav Enviro Projects Limited, Odhav, Ahmedabad ‹ Common Spray Dryer – OEPL common spray dryer, Odhav, Ahmedabad Membership of Common facility (CF) (For waste water treatment) ‹ CETP-OEPL, Odhav ‹ Common Spray dryer of OEPL, Odhav. vii Simplified water balance diagram with reuse / recycle of waste water Total Reuse of water is 8.83 KLD vii Reuse/Recycle details (KLD) [Source of reuse & application area] Total reuse 8.83 KLD Source of waste Application area Characteristics of waste Remarks water for reuse with with quantity in water to be reused (COD, regarding quantity in KLD KLD (Where it is BOD, TDS etc.) feasibility to (From where it is used) reuse i.e. coming) Industrial process 6.5 KLD (in ------(8.83 KLD) process)

2.33 KLD (in Washing)

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. Existing & Proposed

Existing Stack Air Pollution Sr. Permissible Stack attached To /Proposed Height Control Parameter No. Limit (m) System

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Small Boiler Existing Multi-cyclone 1. (Capacity: 800 11 Dust Kg/hr) collector Hot Air Generator-I Existing Multi-cyclone Particulate 150 mg/Nm 3 2. (Capacity: 3.5 Lac 11 Dust Matter 100 ppm Kcal) collector NOx 50 ppm Hot Air Generator- Existing SO 2 Multi-cyclone II (Dismantled) 3. 11 Dust (Capacity: 3.5 Lac collector Kcal) Hot Air Generator- Proposed III Adequate 4. 11 (Capacity: 3.5 Lac Stack Height Particulate 150 mg/Nm 3 Kcal) Matter

IBR Boiler Proposed Adequate 5. (Capacity; 1.5 11 Stack Height TPH)

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

Spin Flash Dryer Particulate Matter 1 (Capacity: 200 11 Adequate Stack Height

Litre/Hr)

iii Fugitive emission details with its mitigation measures. Sources of fugitive emissions include storage of chemicals, loading and unloading section, raw material handling and hazardous waste storage area. Mitigation Measures - Water shall be sprinkled during the construction - Mechanical seals for pumps etc. should be used and maintained. - Closed unloading, conveying and packing system

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- All the reactors shall be closed. - Safety devices shall be provided to workers - Raw material storage in closed storage area F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Existing & Proposed i

Type of Quantity Sr. Cat. Hazardous After Management No. No. Existing Proposed Waste Expansion Collection, Storage, 35.3 1.2 2.8 4.0 Transportation, 1. ETP Sludge (Sch.1) MT/Annum MT/Annum MT/Annum Disposal by send to TSDF site. Collection, Storage, 5.1 8.0 Transportation, 2. Used oil 5.0 Liter/Year 3.0 Liter/Year (Sch.1) Liter/Year Disposal by reused lubricant. Collection, Storage, Discarded Decontamination, 33.1 0.125 1.875 2.0 3. Bags & Transportation, and (Sch.1) MT/Year MT/Year MT/Year Containers Disposal by return back to supplier.

ii Membership details of TSDF, CHWIF etc. TSDF- Eco Care Infrastructure Ltd., - (For HW management) Surendranagar iii Details of Non-Hazardous waste & its No any non hazardous waste disposal(MSW and others) G Solvent management , VOC emissions etc. No any kind of solvent will be used in existing as well as proposed manufacturing activity, i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format) ‹ No solvent use.

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ii VOC emission sources and its mitigation measures

‹ There will be no occur VOC emission in premises

H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous Remarks chemicals Storage tanks HCl (Hydrochloric acid) MS Tank of 10 KL

Drum/Barrel storage Aniline/Aniline Oil HDPE Carboys

Liq. Ammonia HDPE Carboys/Drums

‹ Applicability of PESO : Not applicable PESO. Unit is not covered under MAH category as per Hazardous Chemicals as per the "Manufacturing, Storage and Import of Hazardous Chemicals Rules, 1989", • Technical presentation was made by the project proponent with consultant/expert M/s. Bhagwati Enviro care Pvt Ltd. during SEAC meeting dated 17/10/2019. • Committee noted that this proposal is for expansion of unit located at GIDC- Odhav. Committee asked PP to clarify the distance from Critically Polluted Area (CPAs) Vatva, GIDC. PP mentioned that unit is at a distance of more than 5 KMS from CPAs area however they have not incorporated the exact distance for the same. PP mentioned that earlier EC was not applicable and they have submitted compliance of CC&A. PP further mentioned that there is no any court case or any public complaint pending against this unit. Committee asked PP to clarify about area adequacy for such a small plot area of 650.5 Sq. mt. and expansion to the tune of 54 MT/Month from 4 MT/Month, which is almost 13 times then the present capacity. PP mentioned that they will only manufacture 25 MT/Month dyes in either of the group. Committee told PP that as they will only manufacture 25 MT/Month at a time they need to submit revised proposal for the same considering all the aspects of Air, Water & Hazardous Waste. • After detailed discussion, Committee unanimously decided to defer the proposal and call the project proponent only after submission of revised proposal with the production capacity not exceeding 25 MT/Month along with exact distance of the unit from Critically Polluted Area (CPAs) i:e: Vatva, GIDC on Google Map. • PP made presentation of the above mentioned query dated 17/12/2019. • During technical presentation dated 17/12/2019 PP mentioned that they have reduced their production 54 MT/Month to 25 MT/Month and also submitted revised proposal along with it. Committee asked PP to clarify the exact distance from Critically Polluted Area (CPAs) i:e; Vatva, GIDC. PP presented google map of their project site from Vatva, GIDC however did not mention Latitude & Longitude of the unit as well as the boundary of Vatva, GIDC. Committee took the note of Map and asked PP to superimpose the map with the 575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 146 of 178

exsitng 5 KMs boundary of Vatva, GIDC from unit along with Latitude & Longitude of the unit as well as Vatva GIDC. Committee further noted that PP has not properly addressed treatability of effluent along with stream segregation and treatment methodology and asked them to properly address the same. PP has proposed one steam boiler & one Hot Air Generator. Committee noted that PP did not mention the fuel used for the same and asked to address the same. PP has addressed Hazardous Waste as per HWR – 2016. • After detailed discussion, Committee decided to consider the proposal only after submission of the following documents: 1. Super imposing the 5 KMs satellite Map of Vatva, GIDC CEPI area with the Proposed Project/Activity along with Latitude & Longitude of Both Project Site & Vatva, GIDC. 2. Address treatability of effluent along with stream segregation and treatment methodology as per the characteristic of effluent generated. 3. Details of Fuel used in Proposed Steam Boiler & Hot Air Generator with Quantity. 19 SIA/GJ/IND2/45442/2019 M/s. Shree Harikrishna Pharmaceuticals Screening & Scoping Plot.No. C-1/510 & C-1/511, Kerala GIDC area, Kerala, Bavla, Ahmedabad.

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

• This office has received an application vide their online proposal no. SIA/GJ/IND2/45442/2019 dated 13/11/2019 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. Name of the CAS no. /CI no. Quantity End-use of the products No. Products MT/Month 1 Deflazacort 14484-47-0 6 It is a glucocorticoid used as an anti-inflammatory and immuno suppressant. 2 Acebrophylline 179118-73-1 It is used to treat blockage, swelling, and irritation associated with bronchial asthma and chronic obstructive pulmonary disease (COPD) 3 Thiocolchicoside 602-41-5 It is a muscle relaxant with anti-

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inflammatory and analgesic effects 4 Solifenacin Succinate 242478-38-2 It is used to treat overactive bladder. It may help with incontinence, urinary frequency, and urinary urgency. 5 Anagliptin 739366-20-2 It is used for the treatment of type 2 diabetes mellitus. 6 Atazanavir sulphate 229975-97-7 It is an antiretroviral medication used to treat and prevent HIV/AIDS. 7 Esclicarbazepine 236395-14-5 It is an anticonvulsant Acetate medication approved for use as monotherapy or as additional therapy for partial-onset seizures epilepsy 8 Febuxostat 144060-53-7 It is used long-term to treat gout due to high uric acid levels. 9 Flupirtine maleate 75507-68-5 It is used as an analgesic for acute and chronic pain 10 Methylcobalamin 13422-55-4 It is a cobalamin, a form of vitamin B12 11 Mirabegron 223673-61-8 It is used to treat overactive bladder. 12 Pidotimod 121808-62-6 It is used for the prevention and treatment of respiratory and urinary tract infections in patients with a compromised immune system. 13 Tenaligliptine 906093-29-6 It used for the treatment of type 2 hydrobromide diabetes mellitus 14 Valsartan 137862-53-4 It is used to treat high blood pressure, heart failure, and diabetic kidney disease. 15 Pirfenidone 53179-13-8 It is used for the treatment of idiopathic pulmonary fibrosis

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16 N-Boc Amino acid NA Intermediate for Bulk drug preparation 17 Fluconazole 86386-73-4 It is an antifungal medication used for a number of fungal infections. 18 Losartan Potassium 124750-99-8 It is mainly used to treat high blood pressure. It is also used for diabetic kidney disease, heart failure, and left ventricular enlargement 19 Clopidogrel Sulphate 120202-66-6 It is an antiplatelet medication used to reduce the risk of heart disease and stroke in those at high risk. 20 Sertraline HCl 79559-97-0 It is an antidepressant of the selective serotonin reuptake inhibitor (SSRI) class. 21 Oxcarbazepine 28721-07-5 It is a medication used to treat epilepsy and bipolar disorder. 22 Nebivolol 99200-09-6 It is a beta blocker used to treat high blood pressure and heart failure. 23 Telmisartan 144701-48-4 It is used to treat high blood pressure, heart failure, and diabetic kidney disease. 24 Clomipramine HCl 17321-77-6 It is used for the treatment of obsessive–compulsive disorder, panic disorder, major depressive disorder, and chronic pain. 25 Bisoprolol Fumarate 104344-23-2 It is most commonly used for heart diseases. This specifically includes high blood pressure, chest pain from not enough blood flow to the heart, and heart failure. 26 Tadalafil 171596-29-5 It is used to treat erectile

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dysfunction (ED), benign prostatic hyperplasia (BPH), and pulmonary arterial hypertension. 27 5-(4'-Bromomethyl- 124750-51-2 Intermediate for Bulk drug 1,1'-biphenyl-2-yl)-1- preparation triphenylmethyl-1H- tetrazole (Trityl tetrazole bromomethyl biphenyl) (TTBB) 28 Derivatives of 6- 99199-90-3 Intermediate for Bulk drug fluoro-3,4-dihydro-2- preparation oxiranyl-2H-1- benzopyran (NB-V) 29 4-Bromomethyl-2- 114772-54-2 5 Intermediate for Bulk drug cyanobiphenyl (4'- preparation Bromomethyl- biphenyl-2- carbonitrile) (Bromo OTBN) 29 4'-Methyl-2- 114772-53-1 Intermediate for Bulk drug cyanobiphenyl (2- preparation tolylbenzonitrile) (OTBN) 30 2-Chlorobenzonitrile 873-32-5 Intermediate for Bulk drug (Ortho preparation chlorobenzonitrile) (OCBN) 31 6-Fluoro-3,4-dihydro 129050-20-0 Intermediate for Bulk drug 2H-1-Benzopyran-2- preparation carboxylic acid (NB- III) 32 Ticagrelor 330808-88-3 0.1 It is a platelet aggregation inhibitor 33 Vardenafil 134523-03-8 0.2 It is used for treating erectile Hydrochloride dysfunction Trihydrate

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34 Atorvastatin Calcium 147098-20-2 0.2 It is used to prevent cardiovascular disease in those at high risk and treat abnormal lipid levels. 35 Rosuvastatin calcium 86386-73-4 0.1 It is used to prevent cardiovascular disease in those at high risk and treat abnormal lipid levels. Total 11.6 • 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 17/12/2019.

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

Sr. Particulars Details no. A A Total cost of Proposed Project 4.35 Crores (Rs. in Crores):

B Total Plot area ( sq. meter) 1406 Sq. m.

Green belt area 471 Sq. m. ( sq. meter) C Employment generation 15

D Water i Source of Water Supply GIDC

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

Status of permission from the concern authority. Application has been made.

ii Water consumption (KLD) Category Quantity Remarks

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KLD (V) Domestic 1 (W) Gardening 2.1

(X) Industrial

Process 11.90 Washing 2 Boiler 5 Cooling 1.5 Others-process scrubber 11.20 Others-Boiler Scrubber 1.00 32.60 Industrial Total 35.70 Total (A + B + C)

1) Total water requirement for the project: 35.7 KLD 2) Quantity to be recycled : 0 KLD 3) Total fresh water requirement: 35.7 KLD (Total water requirement = Fresh water + Recycled water) iii Waste water generation (KLD) Category Waste water Remarks KLD (R) Domestic 0.9 to Septic tank followed by soak pit (S) Industrial

Process 12.95 High COD wastewater to common

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incineration facility of SEPL, Sanand after primary treatment 10.4 Low COD Washing 2 wastewater to Boiler 1 common MEE of Cooling 0.3 SEPL, Sanand Others-process scrubber 13.30 after primary Others-Boiler Scrubber 0.5 treatment 40.45 Total Industrial waste water Total [A + B] 41.35 - iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ Primary ETP for Low COD wastewater 28 KL/d ‹ Primary ETP for High COD wastewater 13 KL/d Treatment scheme including segregation at source. ‹ High COD process wastewater to common incineration facility of SEPL, Sanand after primary treatment ‹ Low COD process and utility wastewater to common MEE of SEPL, Sanand after primary 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 . ‹ Not applicable Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Not applicable v Mode of Disposal & Final meeting point

Domestic: to Septic tank followed by soak pit

Industrial: High COD process wastewater to common incineration facility of SEPL, Sanand after

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primary treatment Low COD process and utility wastewater to common MEE of SEPL, Sanand after primary treatment vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ Common MEE & common incineration facility of Sanand Eco Project Limited Membership of Common facility (CF) (For waste water treatment) Application has been made. vii Simplified water balance diagram with reuse / recycle of waste water

GIDC 35.7

1.0 2.1 3 Domestic Gardeni Industria 3

0. 1 2.0 11 5 1 11 Soak pit/ Cool Washi Proce Boil Boil Proc ing ss er

0.3 2. 13 1 0 10

27 Note: All Values are in Pri High

Water 27 12. Common Common Wastew Incineration MEE or facility after viii Reuse/Recycle details (KLD) Total reuse 0 KLD Source of waste Application area Characteristics of waste Remarks water for reuse with with quantity in water to be reused (COD, regarding quantity in KLD KLD (Where it is BOD, TDS etc.) feasibility to (From where it is used) reuse i.e. coming)

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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 Type of Air Pollution Stack Quantity Sr. emission Type emissions Control Height of Fuel no. With of Fuel i.e. Air Measures (meter) MT/Day Capacity Pollutants (APCM) Multi cyclone separator PM -150 followed by Boiler (1 Coal/ 3 mg/NM bag filter, 1 TPH x 1 30 Briquett 2.28 SO2 -100 water No.) es ppm scrubber and NOx -50 ppm adequate stack height

PM -150 D.G.Set mg/NM 3 Adequate 2 11 Diesel 0.23 (100 kVA x SO2 -100 stack height 1 No.) ppm NOx -50 ppm - 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 emission Sr. Type of Control Height no. (Name of the Product emission Measures (meter) & Process) (APCM)

Stack attached to HCl - 20 Caustic scrubber 3 reaction vessel used mg/NM followed by 1 11 for manufacturing of adequate stack SO 2 - 40 5-(4'-Bromomethyl- 3 mg/NM height

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1,1'-biphenyl-2-yl)-1- Br 2 - 2 triphenylmethyl-1H- mg/NM 3 tetrazole (Trityl tetrazole bromomethyl biphenyl) (TTBB) & Derivatives of 6- fluoro-3,4-dihydro-2- oxiranyl-2H-1- benzopyran (NB-V)

Stack attached to reaction vessel used for manufacturing of 4-Bromomethyl-2- cyanobiphenyl (4'- Bromomethyl- biphenyl-2- carbonitrile) (Bromo HCl - 20 OTBN); mg/NM 3 Caustic scrubber 4'-Methyl-2- SO 2 - 40 followed by 2 11 cyanobiphenyl (2- mg/NM 3 adequate stack tolylbenzonitrile) height Br - 2 (OTBN); 2- 2 mg/NM 3 Chlorobenzonitrile (Ortho chlorobenzonitrile) (OCBN) & 6-Fluoro- 3,4-dihydro 2H-1- Benzopyran-2- carboxylic acid (NB- III)

Stack attached to Caustic scrubber reaction vessel used HCl - 20 followed by 3 11 3 for manufacturing of mg/NM adequate stack Vardenafil height

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Hydrochloride Trihydrate

- iii Fugitive emission details with its mitigation measures: As below: To control fugitive emissions in form of particulate matter following measures shall be adopted to ensure compliance and further reductions wherever possible: • The coverage of greenbelt around the plant consisting of air pollution capturing species. • The drums shall be stored in separate storage area. Manual handling shall be avoided as far as possible. • Proper ventilation shall be provided for dispersion. • Good housekeeping shall be maintained in the plant. • The open area shall be covered with either greenbelt or paved surface to avoid dust during transportation within plant. F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. i Sr. Type/Name Specific Source of Category Quantity Management of no. of generation and (MT/Annum) HW Hazardous (Name of the Activity, Schedule waste Product etc.) as per HW Rules. 1 Used/spent Plant machinery Sch.-I & 0.1 Collection, Oil Cat. -5.1 storage, transportation, reuse/selling to registered refiners. 2 Discarded Raw material storage area Sch.-I & 8760.00 Collection, Containers Cat. -33.1 storage, decontamination sent to authorized recycler. 3 Process Inorganic salts of potassium Sch.-I & 247.20 Collection, residue hydroxide & sodium sulphate Cat. -28.1 Storage and sent

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from manufacturing process to TSDF for Land of Lostaran Potassium, filling. Valsatarn, Clomipramine HCl and Bisoprolol Fumarate 4 Spent Manufacturing Process of Sch.-I & 79.80 Collection, Catalyst & Esclicarbazepine Acetate, Cat. -28.2 Storage and sent Spent TeneligliptinHydrobromide, & 28.3 to CHWIF for Carbon Anagliptin, Flupirtine Incineration. maleate, Mirabegron, Pirfenidone, NB-V, NB-III and Atorvastatin Calcium 5 Spent From manufacturing of Sch.-I & 1281.60 Collection, Solvent Flupirtine maleate, Methyl Cat. -28.6 Storage and sent cobalamine, Clopidogril to CHWIF for Sulphate, Sertraline HCl, Incineration. Bromo OTBN, NB-V and TTBB From manufacturing of 2301.00 Collection, Acebrophylline, Lostaran Storage and sent Potassium, Telmisartan, to authorized Thiocolchicoside, Solifenacin recycler. Succinate, Esclicarbazepine Acetate, Pidotimod, Tenaligliptine hydrobromide, Anagliptin, Valsartan, N-Boc Amino acid, Fluconazole, Pirfenidone, Nebivolol, Bisoprolol Fumarate, Bromo OTBN, OTBN, NB-V, NB-III, Ticagrelor, Vardenafil Hydrochloride Trihydrate, Atorvastatin Calcium, Rosuvastatin calcium, Tadafil and TTBB 6 Recovered Solvent recovery unit - 2567.40 Collection, Solvent attached with reactor utilised Storage and

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in manufacturing of Lostaran reuse in next Potassium, Thiocolchicoside, batch Solifenacin Succinate, Esclicarbazepine Acetate, Tenaligliptine hydrobromide, Deflazacort, Anagliptin, Fluconazole, OCBN, Pirfenidone, Clomipramine HCl, Bromo OTBN, OTBN, NB-V, Ticagrelor, Vardenafil Hydrochloride Trihydrate, Atorvastatin Calcium, Rosuvastatin calcium, Tadafil and TTBB 7 Distillation Solvent recovery unit Sch.-I & 673.20 Collection, Residue attached with reactor utilised Cat. -20.3 Storage and sent in manufacturing of to CHWIF for Thiocolchicoside, Incineration. Esclicarbazepine Acetate, Teneligliptin Hydrobromide, , Deflazacort, Anagliptin, NB- III, Atorvastatin Calcium and Rosuvastatin Calcium 8 ETP Sludge ETP Sch.-I & 33.0 Collection, Cat. -35.3 Storage and sent to TSDF for Land filling. 9 Scrubber From stack equipped with -- 748.2 To ETP for further Bleed scrubber attached with Treatment Containing reactor utilized in Sodium manufacturing of TTBB, NB- Chloride, V, Bromo OTBN, OTBN, Sodium OCBN, NB-III and Vardenafil Sulphite and Hydrochloride Trihydrate Sodium Bromide

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- ii Membership details of TSDF, CHWIF etc. Will be obtained after obtaining (For HW management) EC. iii Details of Non-Hazardous waste & its disposal Fly ash from boiler to the tune of (MSW and others) 46.8 MT/Annum will be sold to brick manufacturer. G Solvent management , VOC emissions etc. i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)

Name of Product Input (MT/Month) Spent Solven Distilla % Mode of Solven t tion Reco disposal t/ Recov Residu very of Spent ered e spent/rec ML (MT/Mo (MT/Mo overed (MT/Mo nth) nth) solvent nth) Deflazacort Ethyl acetate 27. 19.09 6.55 70.00 Reuse in 27 % process Acebrophylline Toluene 13. 12.48 To 04 authorized recycler Thiocolchicoside Acetonitrile 16. 15.33 5.00 92.00 Reuse in 67 % process Methanol 16. 20.00 To 67 authorized recycler Diethyl amine 10. 67 Solifenacin Succinate Toluene 22. 20.45 90.00 Reuse in 73 % process 68. 72.73 To 18 authorized recycler Acetone 20. 18.18 To

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00 authorized recycler Isopropyl alcohol 38. 38.73 To 77 authorized recycler Anagliptin Methylene 22. 13.64 10.96 61.71 Reuse in dichloride 11 % process Isopropyl alcohol 9.4 15.79 To 7 authorized recycler Ethyl Acetate 4.7 4 Atazanavir sulphate Methylene 25. 19.13 To dichloride 50 authorized recycler Methanol 39. 9.99 25.04 Reuse in 89 % process 53.18 To authorized recycler Acetone 26. 59 Esclicarbazepine Isopropyl alcohol 82. 58.29 To Acetate 86 authorized recycler Methylene 27. 20.57 2.06 75.79 Reuse in Dichloride 14 % process Flupirtine maleate Isopropyl alcohol 30. 87.98 To CHWIF 61 Methylcobalamin Acetone 6.9 14.14 To CHWIF 0 Mirabegron Pidotimod Methylene 25. 37.10 To dichloride 00 authorized recycler Tenaligliptine Dysol 44. 47.68 To

575 th meeting of SEAC-Gujarat, dated 17.12.2019 Page 161 of 178 hydrobromide 84 authorized recycler Methylene 12. 11.68 0.63 92.50 Reuse in dichloride 63 % process Valsartan Toluene 15. 27.03 To 79 authorized recycler Methylene 28. 27.79 To dichloride 42 authorized recycler Pirfenidone Toluene 33. 31.43 93.11 Reuse in 75 % process 4.13 To authorized recycler Ethylacetate 26. 24.94 95.00 Reuse in 25 % process 3.75 To authorized recycler N-Boc Amino acid Methylene 13. 13.85 To dichloride 85 authorized recycler Ethyl Acetate 13. 20.77 To 85 authorized recycler Fluconazole Dimethyl 12. 11.52 96.00 Reuse in Formamide 00 % process Ethyl Acetate 14. 16.20 To 40 authorized recycler Isopropyl alcohol 9.0 7.80 To 0 authorized recycler Losartan Potassium Dimethyl 13. 13.08 93.97 Reuse in formamide 92 % process

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Methanol 16. 29.94 To 74 authorized recycler Clopidogrel Sulphate Isopropyl Alcohol 6.0 14.88 To CHWIF 0 Methanol 7.2 9.66 To CHWIF 0 Sertraline HCl Methanol 52. 29.40 To CHWIF 20 Oxcarbazepine Isopropyl Alcohol 13. 10.50 To CHWIF 50 Nebivolol Toluene 18. 22.80 To 00 authorized recycler Methanol 31. 30.00 To 20 authorized recycler Telmisartan Toluene 25. 62.06 To 71 authorized recycler Clomipramine HCl Toluene 40. 39.20 98.00 Reuse in 00 % process Bisoprolol Fumarate Isopropyl Alcohol 24. 24.00 To 55 authorized recycler Tadalafil Methylene 37. 33.75 90.00 Reuse in dichloride 50 % process Isopropyl Alcohol 26. 27.86 To 79 authorized recycler 5-(4'-Bromomethyl- Thionyl chloride 26. 10.52 39.45 Reuse in 1,1'-biphenyl-2-yl)-1- 68 % process triphenylmethyl-1H- Toluene 13. 25.38 To tetrazole (Trityl 85 authorized tetrazole bromomethyl recycler biphenyl) (TTBB) Tetrahydrofuran 25.

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38 Isopropyl alcohol 31. 11.54 36.23 Reuse in 85 % process

35.82 To authorized recycler 22.57 To CHWIF Acetonitrile 13. 12.92 93.33 Reuse in 85 % process Derivatives of 6- Ethyl acetate 70. 51.25 72.89 Reuse in fluoro-3,4-dihydro-2- 31 % process oxiranyl-2H-1- 6.19 To benzopyran (NB-V) authorized recycler Acetic acid 70. 37.50 53.00 Reuse in 75 % process Toluene 90. 84.50 93.89 Reuse in 00 % process t-Butanol 15. 12.50 To 00 authorized recycler Isopropyl alcohol 20. 20.00 To CHWIF 00 4-Bromomethyl-2- Thionyl chloride 22. 8.77 39.45 Reuse in cyanobiphenyl (4'- 23 % process Bromomethyl- Toluene 11. 21.15 To biphenyl-2- 54 authorized carbonitrile) (Bromo recycler OTBN) Tetrahydrofuran 21. 15 Isopropyl alcohol 11. 11.58 To 54 authorized recycler 18.81 To CHWIF Acetonitrile 11. 10.77 93.33 Reuse in

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54 % process 4'-Methyl-2- Thionyl chloride 28. 11.40 39.45 Reuse in cyanobiphenyl (2- 90 % process tolylbenzonitrile) Toluene 15. 27.50 To (OTBN) 00 authorized recycler Tetrahydrofuran 27. 50 Isopropyl alcohol 10. 15.05 To 00 authorized recycler 2-Chlorobenzonitrile Thionyl chloride 31. 12.26 39.45 Reuse in (Ortho 08 % process chlorobenzonitrile) (OCBN) 6-Fluoro-3,4-dihydro Ethyl acetate 35. 25.63 72.89 Reuse in 2H-1-Benzopyran-2- 16 % process carboxylic acid (NB- 3.09 To III) authorized recycler Acetic acid 19. 18.75 97.40 Reuse in 25 % process Ticagrelor Toluene 7.3 7.02 95.00 Reuse in 9 % process 8.2 8.52 To 0 authorized recycler Ethyl acetate 1.9 2.62 To 3 authorized recycler Cyclohexane 0.9 2 Vardenafil Methylene 2.3 2.05 87.10 Reuse in Hydrochloride dichloride 5 % process Trihydrate Toluene 0.7 0.79 To 6 authorized

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recycler Isopropyl Alcohol 2.0 1.91 To 0 authorized recycler Atorvastatin Calcium Isopropyl Alcohol 2.9 2.13 0.56 71.97 Reuse in 6 % process

Cyclohexane 2.2 2.12 95.38 Reuse in 2 % process 2.0 3.87 To 0 authorized recycler MTBE (methyl-t- 2.0 butyl ether) 0 Methanol 7.4 4.83 64.65 Reuse in 7 % process Rosuvastatin calcium Methylene 0.7 0.64 0.17 81.82 Reuse in dichloride 9 % process Toulene 1.0 0.70 66.22 Reuse in 6 % process Methanol 3.1 0.86 Reuse in 7 process 0.35 Reuse in process 1.86 To authorized recycler MTBE (methyl-t- 0.4 0.44 96.88 Reuse in butyl ether) 6 % process

ii VOC emission sources and its mitigation measures The VOC emission in unit at different stages of solvent handling such as solvent storage, loading, unloading & recovery units. The fugitive emissions of organic chemicals and VOCs mainly occur due to leaking pipe fitting and valves, during maintenance operations. Following measures shall be followed to ensure compliance and further reductions wherever possible. ‹ The fugitive emissions in terms of handling losses shall be reduced by proper storage and handling. ‹ Hazardous chemicals shall be stored as per standard criteria.

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‹ Periodically monitoring shall be carried out as per the existing monitoring plan. ‹ Proper ventilation in storage & production area shall be provided and all materials shall be stored in suitable packing to prevent contamination of air due to particulates & volatile emissions from storage container & area. ‹ Enclosed system & efficient procedures for materials charging shall be provided. ‹ SOP’s for start-up, shut down, operation & maintenance shall be established & maintained in all relevant area of works. ‹ Brine chilled condensers shall be provided in solvent recovery units (SRU). These SRU shall be closed system. H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks Storage tanks None

Drum/Barrel storage • Potassium hydroxide, Sodium • HDPE Bags azide, Sodium Hydroxide • Acetic Anhydride, Chlorosulphonic • HDPE Acid, Ethyl chloroformate, Sulphuric Carboy Acid • Acetic acid, DIPEA (N,N-

Diisopropylethylamine), Ethanol, • HDPE Drum Formic acid, Liq. Ammonia, Thionyl

chloride

• Acetone, Acetonitrile, Cyclohexane,

Diethyl amine, Ethyl acetate,

Ethylene dichloride (EDC), • MS Drum Isopropyl alcohol, Methanol, Methylamine, Methylene dichloride, MTBE (methyl-t-butyl ether), t- Butanol, Tetrahydrofuran, Toluene, Triethyl amine

‹ Applicability of PESO : Not applicable • During the meeting dated 17/12/2019, technical presentation made by the Project proponent. • Committee noted that this proposal is new in Kerala GIDC. Source of Water is GIDC. PP mentioned that high

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COD/TDS effluent generated from process will be treated in proposed in-house Primary ETP – 1 and treated effluent will be sent to Common Incineration Facility of Sanand Enviro Project Ltd, Sanad while Low COD/TDS effluent generated from process will be treated along with washing, cooling tower blow down, boiler blow down, boiler scrubber & process scrubber effluent in proposed in-house Primary ETP – 2 and treated effluent will be sent to Common MEE/ Spray Dryer of Sanand Enviro Project Ltd, Sanaand for final treatment & disposal. PP has proposed one steam boiler. Fuel used will be briquettes/coal. PP has addressed Hazardous Waste as per HWR – 2016. • After detailed discussion, it was decided to recommend the project to SEIAA, Gujarat for grant of Terms of Reference.

• 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. 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. 4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during unloading, storage, transportation, handling and processing of Solvents. 5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form. 6. Stream Segregation of High COD/TDS & Low COD/TDS effluent along with its characteristic treatability & feasibility. 7. Justification of Quantity of ETP Sludge from both the ETP’s 1 & 2 along with its bifurcation. • 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

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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.

20 SIA/GJ/IND2/19755/2015 M/s. Yashashvi Rasayan Private Limited EC – Amendment & Plot No. 765, GIDC Jhagadia, Bharuch. Transfer

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

• SEIAA, Gujarat has accorded Environment Clearance to M/s. Yashashvi Rasayan Private Limited vide letter no. SEIAA/GUJ/EC/5(f)/941/2018; Date: 11September 2018. • Now, project proponent has applied online vide proposal no. SIA/GJ/IND2/19755/2015 dated 04/12/2019 for change of name in EC& transfer of EC. • This proposal was considered in the SEAC meeting dated 17/12/2019. During the meeting, Committee noted that SEIAA, Gujarat has issued Environment Clearance [EC] granted to M/s. Yashashvi Rasayan Private Limited for setting up of ‘Synthetic Organic Chemical’ plant at Plot No. 765, GIDC Jhagadia, Taluka: Ankleshwar, Dist: Bharuch. • Committee asked PP to explain the reason for transfer of EC along with change of name with chronology. • PP mentioned that Asset Transfer agreement made on 26/05/2015 by Yashashvi Rasayan Pvt. Ltd. With Privi Organics Ltd. for transfer of moveable assets. • PP further explained that transfer of business of Privi Organics Ltd. to Adi Aromatics Ltd., through scheme of arrangement approved vide National Court of Law & Tribunal (NCLT) order dated.22/02/2017. • PP mentioned that change of name of the company from Adi Aromatics Ltd. to Privi Organics India Ltd. approved & registered in Ministry of Corporate Affairs dated15/03/2017. • PP clarified that Land & Building of Yashashvi Rasayan Pvt. Ltd. located at Plot no.765, Industrial Estate, Jhagadia, Dist.-Bharuch, Gujarat – 394116assigned in favor of Privi Organics India Ltd. vide Deed of Assignment dated 16/11/2017. • Committee deliberated that the unit has obtained letter from “Ministry of Corporate Affairs” for change of name from M/s. Adi Aromatics to M/s. Privi Organics India Ltd dated 15 th March 2017 and also submitted NOC Letter from M/s. Adi Aromatics. Further Committee delibrated that Privi Organics India Ltd. has purchased all the assets of Yashashvi Rasayan Pvt. Ltd. located at Plot no.765, Industrial Estate, Jhagadia, Dist.- Bharuch & not the company as a whole of Yashashvi Rasayan Pvt. Ltd. • Committee further noted that PP has submitted “Affidavit” along with “Article of Memorandum” for change of Director for transfer of Environment Clearance and have also transferred their name in GIDC Plot allotment letter.

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• In view of the facts stated above, Committee decided to grant necessary change of name in Environment Clearance along with transfer of Environment Clearance with new name as “M/s. Privi Organics India Ltd” instead of “M/s. Yashashvi Rasayan Private Limited” and other conditions remain unchanged in Environment Clearance issued vide letter no. SEIAA/GUJ/EC/5(f)/941/2018; Date: 11September 2018. 21 SIA/GJ/IND2/43391/2019 M/s. Borax Morarji Limited EC – Corrigendum in Plot No. Ch -5/1, GIDC Estate, Dahej, Amendment Vagra, Bharuch. Category of the unit: 5(f) Project status: New

• This is an existing unit engaged in manufacturing of “Synthetic Organic Chemicals” which was accorded Amendment in Environmental Clearance vide letter no. SEIAA/GUJ/EC/5(f)/1099/2019 dated: 30/07/2019. • Now, project proponent has applied online vide proposal no. SIA/GJ/IND2/43391/2019 dated 24/10/2019 for EC-Corrigendum in EC-amendment letter no. SEIAA/GUJ/EC/5(f)/1099/2019 dated 30/07/2019 as mentioned below: Based on the above request for change in EC conditions. Point of EC Sr. Details as per the issued by To be revised Justification/Reasons No. EC SEIAA

1 Condition Unit shall not Unit can manufacture Boron In our product list, SEIAA No. 8 manufacture Products, Sulphonated Products has approved Boron Sulfuric Acid and Benzene Sulfonyl Chloride Products, Sulphonated Products along with CPP. products & Benzene Sulphonyl Chloride product, in which Sulfuric Acid is key raw material. Sulfuric Acid product is including all of these products. So, this condition has to be changed 2 Condition No any solvent As per condition in old EC vide letter As we are using number of No. 11 shall be used in no solvents as a Rea ctant, project SEIAA/GUJ/EC/1(d)&5(f)/155/2013 Dilution, decolorizing Agent to dated 15-July-2013, “Measures shall manufacture Existing be taken to reduce process vapors Sulphonated Products &

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emissions as far as possible. Use of Benzene Sulfonyl Chloride toxic solvents shall be minimum. All (Reactant). This condition venting equipment shall have vapour has to be as per condition in recovery system.” old EC vide letter no SEIAA/GUJ/EC/1(d)&5(f)/155 /2013 dated 15-July-2013. • Project proponent (PP) presented for the EC – Corrigendum presentation in SEAC meeting dated 26/11/2019 by technical expert M/s Aqua-air Environmental Engineers Pvt. Ltd of PP. • During SEAC meeting dated 26/11/2019, Committee asked for justification regarding change in condition no. 8 and condition no. 11. PP informed that condition no. 8 revised for reason of Boron Products, Sulphonated products & Benzene Sulphonyl Chloride product, in which Sulfuric Acid is key raw material. Sulfuric Acid product is including all of these products. PP informed that condition no. 11 revised for reason of are using number of solvents as a reactant to manufacture existing Sulphonated Products & Benzene Sulfonyl Chloride. Committee asked for clarify regarding you had applied EC-amendment proposal showing condition was already given in earlier EC order dated 15/07/2013 for which corrigendum in condition no. 11 required, PP could not able to address satisfactorily it during meeting. • After detailed deliberation, Committee unanimously decided to consider the proposal only after submission of proper technical presentation matching with the EC – Corrigendum criteria as per the EC – Amendment granted vide letter no. SEIAA/GUJ/EC/5(f)/1099/2019 dated 30/07/2019 by SEIAA, Gujarat. • PP replied for the above mentioned query dated 11/12/2019. • PP was called for presentation in the SEAC meeting dated 17/12/2019. • The project proponent along with their expert/consultant Aqua Air Environmental Engineers Pvt Ltd, Surat attended the meeting and made presentation before the committee. • PP presented clarification of condition No. 8 & 11 in line with the EC – Corrigendum as proposed is tabulated as below. Point of EC Sr. Details as per EC – issued by Justification/Reason No. Amendment SEIAA

1 Condition No. 8 Unit shall not • As per the 504 th SEAC meeting dated 08/05/2019, we (as per EC manufacture Sulfuric intended to convert our by-products list to hazardous waste Amendment) Acid Product list as per Hazardous and Other Wastes (Management & Trans boundary Movement) Rules, 2016. We also proposed for in-house captive consumption and also planned to sell the Dilute Sulphuric Acid and Dilute Hydrochloric Acid under

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Rule -9 permission to authorized end users because of delay in installation of manufacturing plant of Sulfuric Acid & Chloro Sulfonic Acid . But since there was urgency on our side for survival by selling sulphonated based products, out of which Dilute Sulphuric Acid and Dilute Hydrochloric Acid is generated and we are unable to do captive consumption as our above plants are delayed and hence our focus was to sell the sulphonated & BSCL based products for which we have valid CC&A. • Since query was raised in SEAC Minutes of Meeting dated 08/05/2019, with reference to product profile that without change in product profile , there was increase in Hazardous waste so we decided that Sulphuric Acid, Oleum 23% & 65%, Liquid Sulphur Trioxide and CSA are inorganic products and as per EIA notification 2006, EC is not applicable for the inorganic products . • That’s why we proposed for the change in above said product profile. • Further while submitting justification of EC Amendment for change in conditions dated 21/05/2019, we made mistake in view of product profile, utility and hazardous waste management by stating in Condition No. 8 that unit will surrender sulfuric acid product and that the condition to be removed from the EC Letter SEIAA/GUJ/EC/1(d) &5(f)/86/2010 dated 26-May-2010. • If the condition remains as Unit shall not manufacture Sulfuric Acid Products, then during the application for NOC & CC&A , we will not be able to apply for Sulfuric Acid Plant in future as per the condition mentioned in EC Amendment Letter vide no. SEIAA/GUJ/EC/5(f)/1099/2019 dated 30/July/2019 because we have to submit the EC Compliance and in EC letter the condition stand still. • As per the EC Amendment letter vide no. SEIAA/GUJ/EC/5(f)/1099/2019, it is stated that Unit shall not manufacture sulfuric acid product which states that the approved Boron products, Sulphonated products &

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benzene sulfonly chloride product cannot be manufactured as Sulfuric Acid is a key raw material & main chemical in initiating chemistry in all of these products which further restricts us to manufacture of granted CC&A products. • Therefore, we applied for EC Corrigendum. 1 Condition No. 8 Requisite measures • Majorities of our products are sulphonation based products. (To be revised) shall be taken to There are chances of traces of SO2 emission(if any) during control any SO2 manufacturing. emission during • As Sulphuric Acid is our basic raw material for Sulphonated manufacturing based products, there is addition or subtraction of sulphur process. bonds, during reaction phase, if total conversion of bond does not occur due to process parameters like temperature range from 160 oC to 180 oC which we have provided , there are chances or traces of SO2 emission. • To prevent the emission of SO2 in air in the worst case scenario, we will trap SO2 in alkali media through So2 Trapper and sodium sulfite will be formed which will be used as decolurizing agent in the sulphonated products. 2 Condition No. No any solvent shall • We considered that there is no change in use of solvent while 11 (As per EC be used in project applying for EC Amendment because the application was Amendment) for addition of utilities & addition of hazardous waste , hence we wrote that there is no use of solvent in the proposed amendment scenario. • Further while submitting justification of EC Amendment for change in conditions dated 21/05/2019, we made unintended mistake in view of product profile, utility and hazardous waste management Condition No. 11 that no solvent will be used to manufacture for proposed project . So this point has to be removed from the EC Letter SEIAA/GUJ/EC/1(d) &5(f)/86/2010 dated 26-May-2010. 2 Condition No. Measures shall be • Sulphonated Products and Benzene Sulfonyl Chloride include 11 (To be taken to reduce the solvents like Mesitylene, MEG, Phenol and Benzene revised) process vapors and these solvents are used as reactants, for dilution and emissions as far as decolorizing and washing. possible. Use of • Therefore we propose the condition as per Earlier EC vide

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toxic solvents shall letter no. SEIAA/GUJ/EC/1(d)&5(f)/86/2010 dated 26 -May - be minimum. All 2010 , Measures shall be taken to reduce process vapors venting equipment emissions as far as possible. Use of toxic solvents shall be shall have vapor minimum. All venting equipment shall have vapor recovery recovery system. system, shall remain the same. • Committee noted that If the condition remains unit will not be allowed to manufacture Sulfuric Acid Products, with in premises in future as per the condition mentioned in EC Amendment Letter and PP wants to eliminate this restriction. • Further Committee noted that as the application was for addition of utilities & addition of hazardous waste for amendment in EC, PP wrote that there is no use of solvent in the proposed amendment scenario however there is use of solvent viz Mesitylene, MEG, Phenol and Benzene in the manufacturing process. • Committee noted that PP will take control measures for SO2 emission during manufacturing process & also take necessary steps to reduce process vapour emission as far as possible. • After detailed deliberation, Committee unanimously decided to recommend grant of EC – Corrigendum to SEIAA, Gujarat with change in “Condition No. 8 & 11” as follows and with remaining condition unchanged in EC – Amendment granted by SEIAA, Gujarat vide Letter No. SEIAA/GUJ/EC/5(f)/1099/2019 dated 30/07/2019. • Condition No. 8 shall now be read as under: 8. Requisite measures shall be taken to control any SO2 emission during manufacturing process. • Condition No. 11 shall now be read as under: 11. Measures shall be taken to reduce process vapors emissions as far as possible. Use of toxic solvents shall be minimum. All venting equipment shall have vapor recovery system. 22 SIA/GJ/MIS/131436/2019 M/s. Gujarat Industrial Development EC – Amendment Corporation Saykha Part-1 E-9 to E-13, E-15 to E17, GIDC Saykha, Ta. Vagra, Dist. Bharuch.

Category of the unit : 7(h) Project status : New

• This is a new “Common Effluent Treatment plant” of GIDC-Saykha which was accorded EC vide letter No. SEIAA/GUJ/EC/7(h)/68/2019 dated: 10/01/2019. • Now, project proponent has applied online vide proposal no. SIA/GJ/MIS/131436/2019 dated 16/12/2019 for amendment in specific condition no. 1 & 5. • EC was granted with a condition as mentioned below: (For which amendment sought): Based on the above request for change in EC conditions

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S. Point of EC Details as per To be revised Justification/Reasons No. issued by the EC SEIAA

1 A.1 (1) CETP shall CETP shall 1). 7.2 % units have plot area above 50000 m2, 11% only accept accept waste units have plot area between 25000 - 50000 m2, and, 18 wastewater water only from % units have plot area above 10000- 25000 m2 which from the SSI those industrial show the presence of large and medium scale chemical units. Units Which are and dyes and pigment industries and about 63 % units authorized. have below 10000 m2 plot area.

2). In Saykha A, there are only 7 % Engineering units, rest (93%) being chemical, dyes and pigments and textiles.

3). In Saykha B, there are 12 % chemical and 88 % Engineering Industries.

Thus there is majority of chemical / dyes pigment industries mainly in medium and large category.

2 A.1 (5) CETP It is our humble GIDC proposed an effluent collection system for receiving Authority shall request that of effluent from member industries. lay above GIDC has Details of effluent collection system are as under: ground already laid pipeline down • Effluent collection system for member industry will network with underground be above ground with 48 hour retention period. adequate piping network • Connected to TOC, online flow meter connected capacity to for the entire with PLC scada system and high COD (High receive raw GIDC saykha TOC) effluent shall not be allowed into the effluent from area. drainage system but returned to the member unit. the member The underground pipeline shall have effluent only industries. meeting CETP inlet norms.

• PP was called for presentation in the SEAC meeting dated 17.12.2019. • The project proponent along with their expert/consultant Aqua Air Environmental Engineers Pvt. Ltd., Surat attended the meeting and made presentation before the Committee • PP mentioned that they have been granted Environmental Clearance for 40 MLD CETP and 0.5 MLD Evaporation systems for concentrated effluent, having a specific condition A.1 (1): CETP shall only accept

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waste water from the SSI Units. • PP mentioned that they proposed to amend the specific condition for the following reasons: ‹ CETP Saykha has mainly chemical, dyes and pigment, textile units having much large scale, medium scale units. ‹ Bifurcation of the same is as follows: Saykha -A Size of Estate 1017 Ha, Allotable Land 708 Ha.

Sr. No. Category Area in Ha. Nos of plot % of units

1 Chemical 295 341 50.5

2 Textiles 148 116 17.2

3 Engineering 52 47 7.0

4 Dyes & Pigments 213 171 25.3

Total Plot 708 675 100.0

Saykha -B Size of Estate 852 Ha, Allotable Land 624 Ha.

Sr. No. Category Area in Ha. Nos of plot % of units

1 Chemical 132 95 12.15

2 Engineering 492 687 87.85

Total Plot 624 782 100

• PP further mentioned that Saykha A has nearly 50.5 % chemical Industries, 25 % dyes and pigments and 17 % textile industries having higher water consumption and hence effluent generation. Also Dyes and Pigments units contribute to BOD, COD, ammonical Nitrogen load to the CETP and CETP has been designed to take this load. Saykha B has about 12 % chemical industries, whereas @ 88% are engineering industries. • The area wise table for GIDC Saykha for the units who have taken possession. Sr. No Zone No of units/ Area in m2 Total No of units

Above 50000 25000 to 50000 10000 to 25000 Below 10000

1 E1-1 4 1 1 9 15

2 E1-2 3 7 6 13 29

3 E2-1 2 2 11 18 33

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4 E2-2 1 5 23 134 163

5 E3-1 4 10 15 25 54

6 E3-2 5 10 6 19 40

7 Aragam 7 5 4 12 28

8 Total 26 40 66 230 362

Per cent 7.2 11.0 18.2 63.5 100.0

• PP mentioned that as per the table 7.2 % units have plot area above 50000 m2 , 11% units have plot area between 25000 - 50000 m2, and about 18 % units have plot area between 10000 m2 to 25000 m2, which show the presence of large and medium scale chemical and dyes and pigment industries. About 63 % units have below 10000 m2 plot area. • Committee deliberated on the presentation made by PP for change in “Specific Condition” and after observing the Plot Area Table, Size of Plot, and Type of Industries & Purpose of CETP designed to handle BOD, COD & ammonical Nitrogen in CETP. Committee decided to make necessary amendment in “Specific Condition”. • Further committee noted that PP wants to amend condition no. 5 pertaining to laying of above ground pipeline network as underground piping network. Committee deliberated on the circular written by Member Secretary, GPCB to Secretary, SEAC vide Letter No. MS/GPCB/09/2017 dated 23/04/2018 and noted that the pipeline for conveyance of effluent to CETP shall be kept above ground as per the circular. Committee told PP that this condition cannot be amended in the present scenario due to circular of MS-GPCB written to Secretary, SEAC to which PP agreed. • After detailed deliberation, Committee unanimously decided to recommend grant of EC – Amendment to SEIAA, Gujarat with change in “Specific Condition” as follows and with remaining condition unchanged in Environmental Clearance granted by SEIAA, Gujarat vide Letter No. SEIAA/GUJ/EC/7(h)/68/2019 dated 10/01/2019. • Specific Condition A.1 (1) shall now be read as under: 1. CETP shall accept waste water only from authorized industrial Units. Meeting ended with thanks to the Chair. Minutes approved by:

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1. Dr. Dinesh Misra, Chairman, SEAC

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

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

4. Shri. R. J. Shah, Member, SEAC

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

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

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