Project details. Synthetic Organic Chemicals 5(f) For appraisal - Environmental Clearance[EC] EC Amendment

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1 SEAC, Gujarat Page 1 of 15 Project details Synthetic Organic Chemicals 5(f) For appraisal - Environmental Clearance[EC] EC Amendment 1. Basic Information of the Project: i Name & Address of the Project site (Complete details with plot no./survey no., Landmark etc. ) M/s. Icon Pharma Chem Plot No. D-2/CH/146, GIDC-Dahej-2, Tal. Vagara, District: Bharuch, Gujarat. ii Name of the Applicant Mr. Ashish Dobariya (Authorized Person) iii Address for correspondence Plot No. D-2/CH/146, GIDC-Dahej-2, Tal. Vagara, District: Bharuch, Gujarat. iv Contact no. and ID of the Applicant Mo. no. : iconpharmachem@gmail.com v Aerial distance of nearest Habitat (KM) 1.7 km Vadadala (NE) vi Longitude & Latitude of the Project Site: (4 corners of the site) A 21 43'8.41"N, 72 37'11.10"E B 21 43'8.58"N, 72 37'15.16"E C 21 43'5.90"N 72 37'15.29"E D 21 43'5.41"N 21 43'05.41"N vii viii Category as per the Schedule to the EIA Notification 2006 i.e. 1(d), 2(b), 5(f) etc. Sub Category: i.e. Dyes, Dyes Intermediates, Specialty chemicals, Bulk Drugs etc. Applicability of General Conditions of EIA Notification 2006: i.e. Ensure that (1) Protected areas notified under the Wildlife (Protection) Act, 1972; (2) CEPI areas (3) Eco-sensitive areas and (4) Inter-state boundaries and international boundaries; are not located within 5 km or 10 km (as the case may be) area from the boundary of the proposed site. 5 (f) Synthetic Organic Chemicals Sub-Category: Bulk Drugs and Bulk Drug Intermediates Not Applicable as unit is located in Notified Industrial Area- G.I.D.C, Dahej-2 Page 1 of 15

2 SEAC, Gujarat Page 2 of Online application& PH reg.: a) Date of SEAC meeting for 14 th August, 2012 recommendation to grant TOR: b) Online application proposal no. : Not Available c) Date online acceptance of EC application Not Available by SEAC: d) TOR issued by SEIAA: Letter no & date. EIA E/1287 dated: 12 Dec 2012 e) Date of Public Hearing 17/07/2013 (If applicable): f) Date of presentation for Appraisal: 03/08/ Product profile: SR. NO. PRODUCT NAME (As per EC) CAS No PROPOSED CAPACITY (MT/MONTH) End Use 1. 1 Acetyl 4 (4 Hydroxyphenyl) ketoconazole Piperazine 2. 2 Amino 5 Methyl Thiazole Meloxicam 3. 2 Chloro Ethyl Amine Pharma Hydrochloride (Powder 99%) 4. N,N Bis (2 Chloro Ethyl) Amine Itraconazole HCl 5. 1 ( 4 Methoxy phenyl) Itraconazole Piperazine 6. 1 (2,3 Dichlorophenyl) Piperazine Aripiprazole HCl 7. 1 (2 Proponyl) 2 Benzimidazolidin Pharma one 8. 1 (3 Chlorophenyl) Piperazine Trazadole 9. p Chloro Benzhydryl Piperazine Citrazine 10. Trans 4 (4 Floro Phenyl) N Methyl 3 Hydroxy Methyl Piperidine (Bis Carbinole) BY PRODUCT Paroxitine 1. Sodium Sulphite End User 2. HCl End User The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification Page 2 of 15

3 SEAC, Gujarat Page 3 of Product wise Raw material consumption: SR. PRODUCT NO. NAME CAS No. PROPOSED CAPACITY (MT/MONTH) 1 Acetyl 4 (4 Hydroxyphenyl) Piperazine 3 MT 1. P Amino Phenol Bis HCl 65% (as 100%) 5 3. Acetic Chloride Acetone Caustic Lye 48% Sodium Carbonate Sodium Hydrosulfite Charcoal HCl Solution 30% Amino 5 Methyl Thiazole 4 MT 1. Propionaldehyde Sulphuryl Chloride NaOH Thiourea , Chloro Ethyl Amine Hydrochloride 3 MT 1. Monoethanolamine Thionyl Chloride NaOH EDC N,N Bis (2 Chloro Ethyl) Amine HCl 20 MT 1. Diethanolamine Bis HCl Thionyl Chloride NaOH EDC ( 4 METHOXY PHENYL) PIPERAZINE 10 MT 1. 4 Methoxy Aniline Bis HCl Caustic Lye 48% Sodium Carbonate Sodium Hydrosulfite Charcoal HCl Solution 30% (2,3 Dichlorophenyl) Piperazine HCl 2 MT 1. O Xylene for reaction Bis HCl ,3 Dichloro Aniline DM Water Hi flow for Acidic layer Filtration Toluene for extraction of aq. Layer Caustic Lye Page 3 of 15

4 SEAC, Gujarat Page 4 of Conc. HCl (37%) IPA HCl (2 Proponyl) 2 Benzimidazolidinone 1 MT 1. O Xylene for Reaction O Phynelene Diamine Methyl Aceto Acetate Catalyst for D O Xylene for Crude wet cake washing (3 Chlorophenyl) Piperazine (T1) 15 MT 1. Meta Chloro Aniline Bis HCl ,2 Dichloro Benzene for Reaction (F+R) Caustic Lye for Basification. 5 p Chloro Benzhydryl Piperazine 8 MT 1. p Chlorobenzophenone Sodium Borohydride Caustic Lye (48%) Cat D Toluene Dilute HCl (15%) 2.3 Trans 4 (4 Floro Phenyl) N Methyl 3 Hydroxy Methyl Piperidine (Bis Carbinole) 1 MT 1. Ethyl Acetate Sodium Methoxide p Fluorobenzaldehyde (P. F. BA) ; C. S. Lye 48% Acetic Acid DM Water IPA Brine NaBH Tetra Hydrofuran (THF) Page 4 of 15

5 SEAC, Gujarat Page 5 of Compliance status of the existing project: Sr. no. Particulars Brief Information/Details Remarks 1 Earlier EC details Not Require during -- In case of EC not obtained, Copy of CTE &CCA obtained before EC Amendment 2 Compliance of EC conditions -- 3 Status of inspection by RO- -- MoEF&CC, Bhopal. i.e. CCR-Certified Compliance Report 4 Status of submission of half -- yearly returns to concern authorities. 5 Copy of CC&A and -- Compliance of existing CC&A Conditions. 6 Legal actions/closure -- directions/scn etc. Issued by GPCB and its current status. For last 3 years 7 Any Public Complaints No Public Complaints -- 8 Is there any litigation pending before any court of Law against the Project? No -- Page 5 of 15

6 SEAC, Gujarat Page 6 of Salient features of the project including Water, Air and Hazardous waste management: Sr. Particulars Details no. A Total cost of Proposed Project 5.0 Cr (Rs. in Crores): B Total Plot area 9862 Sq. m. ( sq. meter) Green belt area 2958 Sq. m. ( sq. meter) C Employment generation 15 Nos. D Water i Source of Water Supply GIDC Water Supply (GIDC Bore well, Surface water, Tanker supply etc...) Status of permission from the concern authority. Yes, Granted GIDC water supply letter ii Water consumption (KLD) As per EC Total KLD Remarks (A) Domestic 4.0 (B) Gardening 1.0 (C) Industrial Process 7.5 Washing 1.0 Boiler 1.5 Cooling 2.0 Others Nil Industrial Total 12.0 Grand Total (A+B+C) ) Total water requirement for the project :17.0 KLD 2) Quantity to be recycled: 4.5 KLD 3) Total fresh water requirement: 13.0 KLD Note: Quantum of Fresh Water consumption will remain unchanged during EC Amendment. iii Waste water generation (KLD) Page 6 of 15

7 SEAC, Gujarat Page 7 of 15 Category Total KLD (A) Domestic 3.0 (B) Industrial Process 7.0 Washing 1.0 Boiler 0.3 Cooling 0.7 Others Nil Total Industrial 9.0 waste water Remarks Note: Quantum of Waste Water Generation will remain unchanged during EC Amendment. iv Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.. As per EC In House Primary Treatment for Concentrated Stream (12 KLD Capacity) As per EC Amendment In House ETP comprise of Primary & Secondary units (12 KLD Capacity) v Mode of Disposal & Final meeting point Domestic: Domestic Waste water 2 KL/day will be disposed by septic tank or soak pit system. Note: Mode of Domestic Waste Water discharge will remain unchanged during EC Amendment. Industrial: As per EC Entire quantity of effluent shall be evaporated with the help of Multiple Effect Evaporator after primary treatment. Condensate water will be reused back in scrubber, cooling tower & boiler. Hence, there shall be no discharge of effluent in any case. No effluent from the plant shall be discharged outside the factory premises and Zero effluent discharge concept shall be followed. As per EC Amendment 6.8 KLD from steam stripper along with dilute stream (Washing & Boiler/cooling blow 2.0 KLD) = Total 8.8 KLD will be allowed in ETP comprising of primary & Page 7 of 15

8 SEAC, Gujarat Page 8 of 15 secondary units finally sent to CETP (M/s. GIDC-Dahej) after achieving CETP inlet norms. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility As per EC - Zero Liquid Discharge Unit As per EC Amendment Common CETP facility of M/s. GIDC-Dahej) Membership of Common facility (CF) (For waste water treatment) Common CETP (12 KLD) facility of M/s. GIDC-Dahej) vii Simplified water balance diagram with reuse / recycle of waste water As per EC Page 8 of 15

9 SEAC, Gujarat Page 9 of 15 As per EC Amendment vii Reuse/Recycle details (KLD) [Source of reuse & application area] As per EC Total reuse 4.5 KLD Page 9 of 15

10 SEAC, Gujarat Page 10 of 15 Source of waste water for reuse with quantity in KLD MEE Condensate Application area with quantity in KLD Boiler Cooling & Washing Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.) COD <250 (mg/l) BOD3 < 90 (mg/l) TDS< 2100 (mg/l) Note: No waste water will be recycled as effluent will go to CETP after EC Amendment. E i Air Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. - As per EC Sr. no. Source of emission With Capacity Stack Height/Dia (meter) Type of Fuel Quantity of Fuel MT/Day Emissions Norms Air Pollution Control Measures (APCM) 1 Steam Boiler (Capacity=1.5 T/Hr) 15 m/0.3 m Natural Gas/LDO* 2 D.G. Set 8 m/0.1m Diesel SPM < 150 mg/nm 3 SO 2 < 100 Adequate stack height 50 Lit/hr ppm Adequate stack NOx < 50 height ppm Note: Flue Gas Emission will remain unchanged during EC Amendment ii Process gas i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) As per EC Specific Source of Stack/Vent emission Sr. no. (Name of the Product & Process) Type of emission Height/Dia (meter) Air Pollution Control Measures (APCM) 1 Reaction vessel-1 SO 2 10 m/0.3 m Alkali Scrubber & Water Scrubber Page 10 of 15

11 SEAC, Gujarat Page 11 of 15 2 Process Vent - 2 HCl 11 m/0.3 m Alkali Scrubber & Water Scrubber - EC Amendment require Sr. no. Specific Source of emission (Name of the Product & Process) Type of emission Stack/Vent Height/Dia (meter) Air Pollution Control Measures (APCM) 1 Reaction vessel-1 SO 2 10 m/0.3 m Alkali Scrubber & Water Scrubber 2 Process Vent - 2 HCl 11 m/0.3 m Alkali Scrubber & Water Scrubber 3 Solvent Stripper VOCs 15 m/-- Primary & Secondary Condenser & Carbon absorber During proposed amendment Process 7.0 KLD concentrated Stream is subjected to proposed solvent stripper. There will be provision of primary & secondary condenser to trap the VOCs. Finally passing through carbon absorber before venting out in atmosphere. iii Fugitive emission details with its mitigation measures. 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 of VOCs. 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. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps. 7. Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with on-line ph meter with hooter system for better operational control. 8. Close feeding system will be provided for centrifuges 9. Minimum number of flanges, joints and valves in pipelines. 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. 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 Page 11 of 15

12 SEAC, Gujarat Page 12 of 15 F i materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured. Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules Existing & Proposed Sr. No. Hazardous waste Source of generation Category Quantity (MT/Month) EC Proposed Amend nt After Amend nt Disposal Mode 1 Discarded Containers Storage & handling of Raw Materials Sch-I/ 33.1 Bag: 250 Drums: Bag: 250 Drums: 500 Collection, Storage, Transportation, Decontamination & Disposal By Selling To Registered Recycler 2 Used/ Spent Oil Equipment & Machineries Sch-I/ Collection, Storage, Transportation & Disposal By Selling To Registered Recycler 3 ETP Sludge Inhouse ETP Sch-I/ Collection, Storage, Transportation and Disposal in Common TSDF Site Of BEIL, Ankleshwar 4 Spent Carbon Mfg. Process of Intraconazole Sch-I/ Collection, Storage, Transportation & Sent To Cement Industries for Co- Processing or Incineration In CHWIF of BEIL, Ankleshwar. 5 Spent Solvent Mfg. Process + Solvent Stripper Sch-I/ Collection, Storage, Management & Recovery Within the Premises. 6 Distillation Residue Solvent Recovery SCH-I/ Collection, Storage, Transportation & Sent To Cement Page 12 of 15

13 SEAC, Gujarat Page 13 of 15 Industries for Co- Processing or Incineration In CHWIF of BEIL, Ankleshwar. 7 MEE Salt MEE Sch-I/ Nil -- As total effluent will be sent to CETP(GIDC-Dahej) 8 HCl Mfg. Process Collection, Storage, Transportation and Disposal by selling to authorized end user registered under Rule-9. 9 Sodium Sulphite Mfg. Process Collection, Storage, Transportation and Disposal by selling to authorized end user registered under Rule-9. ii iii G i Membership details of TSDF, CHWIF etc. (For HW management) Membership of TSDF / Common Hazardous Waste Incineration Facility (CHWIF) that is M/s BEIL, Ankleshwar. There is no generation of any nonhazardous waste. Details of Non-Hazardous waste & its disposal(msw and others) Solvent management, VOC emissions etc. Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents SOLVENT MANAGEMENT PLAN All the solvents shall be directly distilled from product mixes and; if required shall be purified in packed column with the help of reflux. The solvent distillation system shall be designed so as to achieve minimum 95.0 % recovery of solvent. All the pumps shall be mechanical seal type to avoid any leakage of solvent. All necessary fire fighting systems shall be provided with alarm system. Flame proof wiring and flame proof electrical accessories shall be provided to avoid any mishap. All the distillation column vents are also connected to cooling water/ chilled brine condensers for maximum possible recovery of the solvents. All the vents will be connected to a common carbon Adsorber for removing traces of solvent from vent gases. Residue generated from the distillation will be incinerated in-house or sent to BEIL incinerator site. Two condenser will install with cooling water and chilled brine to recover the solvent. Page 13 of 15

14 SEAC, Gujarat Page 14 of 15 ii Primary Condenser HE-01: Cooling Tower water or Chilled water at 10 0 C -will be used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser VOC Trap Condenser HE-02: Chilled Brine at C will be used to trap any traces of Solvent which is slipped from Secondary condenser VOC emission sources and its mitigation measures Volatile Organic Content Measures: To prevent losses of these solvents in atmosphere, following infrastructure shall be used in addition to LDAR program Leak Free Pumps for transfer of solvents MSW Gaskets in solvent pipelines to prevent leakage from flanges Minimum number of flanges, joints and valves in pipelines. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps. All the rotating equipments like pumps will be installed with Mechanical Seals to arrest any sort of emissions. Condenser and scrubber post Reactor with cooling arrangement Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured. In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send to ETP. If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark. Two condensers will install with cooling water and chilled brine to recover the solvent. Primary Condenser HE-01: Cooling Tower water or Chilled water at 5 0 C will be used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser VOC Trap Condenser HE-02: Chilled Brine at C will be used to trap any traces of Solvent which is slipped from Secondary condenser. 7. Details of Environmental Consultant: Sr. no. Particulars Details i Name of the Consultant Greenleaf Envirotech Pvt Ltd 302,3rd Floor Kankavati Complex, Singanpor- Cauzway Road, Katargam, Surat ii Contact no. and ID of the Consultant Mo. no. : shailendrab.umrigar@yahoo.com iii Accreditation for the categories and Validity Stay Order against NABET/QCI iv Any other details -- Page 14 of 15

15 SEAC, Gujarat Page 15 of 15 Name & designation of the Applicant: Mr. Ashish Dobariya (Authorized Person) Stamp &Signature of Applicant: For Icon Pharma chem Mr. Ashish Dobariya (Authorized Person) Date: 09/03/2019 General Instructions Format shall be in WORD Format (Font type- Arial, Font size- 11) Do not change Format. Fill up your details / information in prescribed tables. Provide authenticated (with stamp & Signature) hard copy during presentation. Kindly send to : seacgujarat@gmail.com Above data shall be as per application Form-1 & PFR. Incorporate relevant details in respective column in the Format. Do not attach Annexure except copy of Certificates etc. Page 15 of 15