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Project details
• Synthetic Organic Chemicals 5(f)
• For Terms of Reference [ToR]
• New Project
1. Basic Information of the Project: i Name & Address of the Project site M/s. Paras Pharma Chem Plot No.C-235, Saykha Industrial (Complete details with plot no./Survey Estate, Tal: Vagra, Dist: no., Landmark etc. ) Bharuch-392140, Gujarat ii Name of the Applicant Mr.Paras Ram Choudhary iii Address for correspondence Plot No.C-235, Saykha Industrial Estate, Tal: Vagra, Dist: Bharuch-392140, Gujarat iv Contact no . and e-mail ID of the Mo. no. : 9414120806 e-Mail: Applicant [email protected] [email protected] v Aerial distance of nearest Habitat (KM) SaykhaVillage: 1.15 km Name of village vi Longitude & Latitude of the Project Site: 21°46'21.81"N & 72°48'58.85"E 21°46'21.86"N & 72°49'1.69"E (4 corners of the site) 21°46'18.52"N & 72°49'1.64"E 21°46'18.52"N & 72°48'58.87"E vii Category as per the Schedule to the EIA 5 (f) Synthetic Organic Chemicals Notification 2006 i.e. 1(d), 2(b), 5(f) etc.
viii Applicability of General Conditions of Not Applicable 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. Note: If located in Vapi-Sarigam region, kindly give exact aerial distance from the interstate boundary i.e. Boundary with Maharashtra state & U.T. of Daman, Diu and Dadra Nagar
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Haveli. viii In case of unit located outside the Not Applicable Notified area: Complying the three conditions as per the amendment to EIA Notification, 2006 vide SO 1599 (E) dated 25/06/2014. [i.e. water consumption less than 25 M3/day; Fuel consumption 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] (Storage details of all the hazardous chemicals shall be submitted in tabular form for justification.)
2. Online application& PH reg.: a) Online application proposal no . : To Be Appraised b) Date of online acceptance for ToR by - SEAC : c) Date of presentation for ToR: To Be Appraised
3. Product profile: Sr. Product Name CAS No. Proposed End Use Of Product No Quantity (MT/Month) 1. 1,3 DICHLORO DIMETHYL 112-36-7 Pharma & Water Treatment HYDANTOIN 2. 1,3 Dibromo-5,5- Dimethyl 77-48-5 Pharma Industries Hydantion 3. 5,5 Dimethyl Hydantion 77-71-4 Pharma Industries 4. 2,2-Azobisisobutyronitrile 78-67-1 Pharma, Polymer,Paint And Pesticides Industries 5. Benzoyl Peroxide 94-36-0 Paint & Polymer Industries 6. MEK Peroxide 1338-23-4 Paint & Polymer Industries 750 7. LABSA 27176-87-0 Use In Detergents Industries 8. Methyl Methacrylate (MMA) 80-62-6 Acrylic Resin, Paint & Plastic Industries 9. Acrylic Emulsion 25067-01-0 Textile , Paper & Leather Industries, 10. VAM Emulsion 108-05-4 Textile, Paint Industries 11. Sodium Hypochlorite 7681-52-9 Textile & Paper Bleaching 12 Calcium Chloride 7440-70-2 Paint & Dyes Industries 13 Benzalkonium Chloride (BKC -50) 8001 -54 -5 Clinical Products 14 Benzalkonium Chloride (BKC-80) 8001-54-5 Clinical Products 15 Amine Oxides 1643 -20 -5 Clinical Products 16 Pearl Essence 8039-79-0 Used in Paint and Plastic Industries 17 Cobalt Octate 13586-82-8 350 Paint & FRP Plastic Industries
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18 TRO Turky Red Oil 8002-33-3 Antifoaming Agent & Textile Industries 19 Coco Diethanolamide 68603-42-9 Cosmetic & Toiletries 20 Solvent Based Paints ---- Use in Wooden,Metal, Household & Industrial Use TOTAL: 1100
The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.
4. Product wise Raw materials consumption:
Sr No. Name of the Products Name of raw materials CAS No. of Quantity Raw MT/MONTH Material 1 1,3 DICHLORO DIMETHYL 5,5 Dimethyl Hydantoin 77-71-4 787.5 HYDANTOIN Caustic Lye 1310-73-2 75 Chlorine 7782-50-5 225 2 1,3 Dibromo-5,5- Dimethyl 5,5 Dimethyl Hydantoin 77-71-4 787.5 Hydantion Caustic Lye 75 Chlorine 7782-50-5 225 Bromine 7726-95-6 150 3 5,5 DIMETHYL HYDANTOIN Acetone Cyanohydrin 75-86-5 750 Ammonium Bicarbonate 1066-33-7 187.5 Liquid Ammonia 7664-41-7 112.5 4 2,2- Acetone Cyanohydrin 75-86-5 450 AZOBISISOBUTYRONITRILE Hydrazine Hydrate 7803-57-8 337.5 Chlorine 7782-50-5 225 Caustic Soda 1310-73-2 37.5 5 Benzoyl Peroxide Benzoyl Chloride 98-88-4 450 Hydrogen Peroxide 7722-84-1 225 Caustic Lye 1310-73-2 37.5 Benzoic Acid 65-85-0 75 6 MEK Peroxide Methyl Ethyl Ketone 78-93-3 450 Hydrogen Peroxide 7722-84-1 150 Dibuthyl Phthalate 131-11-3 150 7 LABSA Linear alkylbenzene 67774-74-7 637.5 Sulphuric Acid 7664-93-9 300 8 Methyl Methacrylate (MMA) Acetone Cyanohydrin 75-86-5 375 Sulphuric Acid 7664-93-9 187.5 Methanol 67-56-1 375 9 Acrylic Emulsion Butyl Acrylic Monomer 141-32-2 112.5 Styrene Monomer 100-42-5 187.5 MMA Monomer 80-62-6 37.5 Acrylic Acid 79-10-7 15 Acrylamide 79-06-1 18.75
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Catalyst - 1.5 2 Ethyl Hexyl Acrylate 103-11-7 37.5 10 VAM Emulsion Vinyl Acetate Monomer 108-05-4 300 Poly Vinyl Alcohol 9002-89-5 75 Plasticizer ----- 37.5 Catalyst ----- 1.5 11 SODIUM HYPOCHLORITE Caustic Lye 1310-73-2 87.5 Chlorine 7782-50-5 70 12 Calcium Chloride Lime Stone 1317-65-3 315 Hydrochloric Acid 7647-01-0 210 13 Benzalkonium Chloride Dimethyl lauryl Amine 111-42-2 113.75 (BKC-50) Benzyl Chloride 112-18-5 61.25 14 Benzalkonium Chloride Dimethyl lauryl Amine 111-42-2 182 (BKC-80) Benzyl Chloride 112-18-5 98 Solvents ----- 17.5 15 Amine Oxides Dimethyl lauryl Amine 111-42-2 108.5 Hydrogen peroxide 7782-84-1 31.5 16 PEARL ESSENSE Lead Carbonate 598-63-0 87.5 MICA 12001-26-2 35 Titanium Dioxide 13463-67-7 52.5 Nitrocelluolose 9004-70-0 17.5 Butayl Acetate 123-86-4 43.75 Benzophenone 119-61-9 8.75 Bismuth Oxychloride 7787-59-9 35 IPA 67-63-0 35 Acetone 67-64-1 35 17 Cobalt Octate 2-Ethyl Hexnoic Acid 149-57-5 88.9 Cobalt Sulphate 10026-24-1 70 Sodium Hydroxide 1310-73-2 23.1 Toulene 108-88-3 420 18 TRO Turky Red Oil Castor Oil 8001-79-4 245 Sulphuric Acid 7664-93-9 87.5 Caustic Lye 1310-73-2 17.5 19 Coco Diehthanolamide Coconut Oil 8001-37-8 210 (CDEA) Diethylamine 10-89-7 105 Casutic Potash 1310-58-3 35 20 SOLVENT BASED PAINTS NC Thinner ---- 140 Nitrocellulose 9004-70-0 35 Benzophenone 119-61-9 17.5 Titanium Dioxide 13463-67-7 70 Pigment Dyes ----- 3.5 Butayl Acetate 123-86-4 35 Acetone 67-64-1 24.5 IPA 67-63-0 24.5
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5. Salient features of the project including Water, Air and Hazardous waste management: Sr Particulars Details . n o. A A Total cost of Proposed Project 9.50 Crores (Rs. in Crores): B Total Plot area ( sq. meter) 8304.338 Sq. m. Green belt area ( sq. meter) 2689.11 Sq. m. C Employment generation 80 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. Unit has obtained the permission letter from GIDC. Ref No:GIDC/EE(W/D)/BRH/58 5 ii Water consumption (KLD)
Category Quantity Remarks KLD (A) Domestic 3.0 (B) Gardening 10.0 (C) Industrial Process 37.0 Washing 30 .0 Boiler 9.5 Cooling 8.5 Scrubber 2.0 Industrial Total 87.0 Total (A + B + C) 100.0 1) Total water requirement for the project: 100 KLD 2) Quantity to be recycled : 68 KLD 3) Total fresh water requirement: 32 KLD iii Waste water generation (KLD)
Category Waste water Remarks KLD (A) Domestic 2.0
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(B) Industrial Process 40.0 Stream-I: Low COD & TDS: 69 KLD Stream-II:Utilites: 2 KLD Washing 29.0 Boiler 1.0 Cooling 1.0 Scrubber 2.795 Reuse and sell end users having permission under rule-9 Total Industrial waste 73.795 water Total [A + B + C] 75.795 - Iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ‹ ETP (Primary,Secondary& Tertiary): 69 KLD
Treatment scheme including segregation at source. Stream I (RAW EFFLUENT Stream) (69 KLD)
First all non-toxic and biodegradable (streams I) of wastewater shall pass through Oil & Grease Removal Tank (OGRT-01) where floating O & G shall be removed manual from top and collected in O & G Collection Tank (OGCT-01). Then effluent shall be collected in Equalization cum Neutralization Tank (ENT-01) where the continuous addition and stirring of Lime solution is done to maintain neutral pH of wastewater from Lime Dosing Tanks (LDT-01-A/B) as per requirement with help of Lime Dosing Pumps. Then after, neutralized wastewater shall go to Flash Mixer (FM-01) by gravity. Alum shall be dosed from Alum Dosing Tanks (ADT-01-A/B) with help of Dosing Pumps. Then after, coagulated wastewater shall be settled in Primary Settling Tank-1 (PST-01). Clear supernatant from PST-01 shall be passed in Aeration Tank (AT-01). Here, biodegradation of organic matter of the wastewater shall be carried out by bacteria (suspended growth) in the AT-01 and for that oxygen shall be supplied by 2 nos. of air blowers (B-02) through diffusers. Air blowers also keep MLSS in suspension.
Then after, wastewater shall go to Secondary Settling Tank (SST-01). Here, the suspended solids shall be settled at bottom. Sludge shall be removed from bottom of SST 01 and pumped to AT-1 to maintain MLSS and excess activated sludge shall be sent to Sludge Sump (SS-01). Clear supernatant from SST-01 shall be collected in Intermediate Sump (IS-01) by gravity.
Thereafter, the wastewater shall be passed through Pressure Sand Filter (PSF-01) to remove left out TSS and Activated Carbon Filter (ACF-01) for final effluent polishing. After tertiary treatment, effluent shall be collected in Treated Effluent Sump (TES-01) before sent to RO-01 for further treatment. RO-01 permeate water shall be collected in RO Treated Water Tank (ROTWT-01) before reuse in plant. RO-01 reject shall be sent to Single Stage Evaporator (SSE-01). Condensate water from SSE-01 shall be reuse/recycle in boiler or cooling for future treatment.
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Sludge settled in PST-01 and excess sludge from SST-01 shall be collected in Sludge Sumps (SS-01) then sludge shall be pumped to Centrifuge (CF-01) where poly shall be mixed from poly Dosing Tank-2 (PDT-02) with sludge to increase efficiency of centrifuge sludge dewatering. Then, dewatered sludge shall be stored in in HWSA and then ultimate disposal to TSDF. Leachate from CF-01 and backwash from PSF- 01 and ACF-01 shall be collected in Drain Pit and pumped back to ENT-01 for further treatment.
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP . ‹ Not Applicable Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): ‹ Source of water will be met through Saykha GIDC Water Supply.Total water requirement will be 100 KL/Day (Fresh Water: 32 KL/Day +RO Permeate: 60 KL/Day +Condensate Water:8 KL/Day). ‹ Total 75.795 KL/Day (73.795 KL/Day: Industrial + 2.0 KL/Day: Domestic) of effluent shall be generated. ‹ Stream-I: 69 KL/day low COD & TDS stream (from process & Washing) will be treated in ETP giving primary, secondary & Tertiary treatment then sent to RO for further process. ‹ Stream-II: 2 KL/day utilities stream ( from Boiler, cooling) will be send to RO. Total 71 KL/day ( from Boiler, cooling & Treated effluent from ETP ) will be treated in RO & 60 KL/day RO permeate will be reused in Industrial Water requirement & RO reject will be sent to Inhouse Single Stage Evaporator and than pass through condense. Condensate water shall be reuse/recycle in boiler or cooling. ‹ 2.795 KL/Day Scrubber wastewater Will be reused or sold to end users having permission under Rule-9. ‹ 2 KL/Day Domestic waste water will be sent to Septic Tank & Soak Pit.
v Mode of Disposal & Final meeting point Domestic: Domestic waste water (2.0 KL/day) will be disposed by septic tank or soak pit system Industrial: ‹ Stream-I: 69 KL/day low COD & TDS stream (from process & Washing) will be treated in ETP giving primary, secondary & Tertiary treatment then sent to RO for further process. ‹ Stream-II: 2 KL/day utilities stream ( from Boiler, cooling) will be send to RO. Total 71 KL/day ( from Boiler, cooling & Treated effluent from ETP ) will be treated in RO & 60 KL/day RO permeate will be reused in Industrial Water requirement & RO reject will be sent to Inhouse Single Stage Evaporator and than pass through condense. Condensate water shall be reuse/recycle in boiler or cooling. ‹ 2.795 KL/Day Scrubber wastewater Will be reused or sold to
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end users having permission under Rule-9. vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF ‹ Not Applicable, Unit has Zero Liquid Discharge. vi Simplified water balance diagram with reuse / recycle of waste water i
Raw Water: 100
Dom: 3.0 Ind: 87 Gardening: 10
Septic Tank & Soak
Pit: 2
Process Washing Boiler Cooling Other : 2
40 29 1 1 2.795
Steam -I 69 KLD Low COD & TDS Steam Will be reused or Steam: II 2 sold to end users ETP ( 69) KLD Utilities having permission
under Rule -9.
RO:71 RO Permeate :60
RO Reject : 11 Reuse/recycle
Single Stage Evaporator
Condensate water: 8 Condenser Reuse/Recycle in
Salt to sludge drying
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vii Reuse/Recycle details (KLD) i Total reuse: 34.0 KLD Source of waste Application Characteristics of Remarks water for reuse area with waste water to be regarding with quantity in quantity in reused (COD, BOD, feasibility KLD (From KLD (Where it TDS etc.) to reuse i.e. where it is is used) coming) RO Permeate: 60 Industrial COD: >40 mg/l KLD Water: 60 KLD BOD: >20 mg/l TDS: 120 mg/l
Condensate Boiler & COD: >80 mg/l Water:8 KLD Cooling:8 KLD BOD: >80 mg/l TDS: -
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 Type of Air Pollution Sr. emission Type of of Fuel emissions Control Measures no. Height Fuel i.e. Air With (meter) MT/Day Pollutants (APCM) Capacity
Boiler 18 Solid 1 SPM Multi-cyclone (Capacity: Fuel- MT/Day / Separator with Bag 500 White 1 SO 2 Filter + Scrubber KG/PH) Coal, Fire MT/Day 1 NOx Wood/ Briquettes of Bio- Coal
Boiler 18 Briquettes 5 SPM Multi-cyclone (Capacity: of Bio- MT/Day separator with bag 2 1 TPH) Coal/ SO 2 filter + Scrubber Coal / 4 MT/Day NOx
Thermic 18 Briquettes 4 SPM Multi-cyclone 3 fluid of Bio- MT/Day / separator with bag heater Coal/ 3 SO 2 filter + Scrubber
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(Capacity: Coal MT/Day NOx 1 Lakh Kcal/ Hr)
D. G. Set 11 HSD 150 SPM Adequate Stack (65 KVA) Lit/Day Height 4 SO 2
NOx
D. G. Set 11 HSD 300 SPM Adequate Stack (125 Lit/Day Height 5 KVA) SO 2 NOx
-
ii Process gas emission details i.e. Type of pollutant gases (SO 2, HCl, NH 3, Cl 2, NO x etc.) - Specific Source of emission Stack/Vent Air Pollution Control Sr. Type of Measures no. (Name of the emission Height Product & (meter) (APCM) Process)
Process Vent Cl 2 11 Two Stage Caustic 1 (Chlorination) Scrubber (Product Name: HCl AIBN, DDH, DCDH)
Process Vent SO 2 11 Two Stage Water + Caustic 2 (Sulphonation) scrubber (Product Name: MMA and LABSA)
Process Vent NH 3 11 Two Stage Acid scrubber 3 (Ammoniation) (Product Name: DMH) - 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.
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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 on-line 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. Type/Name Specific Source of Category & Quantity Management of HW no. of Hazardous generation (Name Schedule as waste of the Activity, per HW (MT/ Product etc.) Rules. Annum)
1 Discarded Raw Material and Sch-I/ 45 Collection, Storage, Drums/Bags Storage and sell to Register Re 33.1 after decontamination.
2 Used / Spent Equipment & Sch-I/ 200 Lit/ Collection, Storage, Transportation Oil Machinery Year 5.1 and sell to registered recycler.
3 ETP Sludge ETP Sch-I/ 216 Collection, Storage, Transportation and sent to common TSDF of M/s. 35.3 BEIL.
4 Distillation Distillation Sch-I/ 100.68 Collection, Storage, Transportation Residue and sent for 20.3 cement industries common incineration of M/s. BEIL.
5 Spent Process (Product Sch-I/ 5 Collection, Storage, Transportation Catalyst No:9,10) and sent to registered regenerator 28.3 under Rule-9 permission.
6 NaCl (15%) Scrubber SCH-1/26.1 280 Collection, Storage, Transportation and sold to end user having permission under rule
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7 NaOCl (12%) Scrubber SCH-1/26.1 270 Collection, Storage & convert to product and than sell as main product.
8 Sodium Scrubber Sch-II/ 316.8 Collection, Storage, Transportation Sulphite and sold to end user having (25%) B36 permission under rule-9.
9 Spent Process Sch-I/ 2529 Sulphuric Acid (50%) (Product No:7,8) 26.3
10 Ammonium Scrubber + Sch-II/ 1350 sulphate Process (15%) B15 (Product No:8)
11 Spent Solvent Process (Product Sch-I/ 3045 Collection, Storage, Distillation and No;17) Reuse within premises. 28.6
12 Off From mfg. Sch-I/ 20 Collection, Storage, Transportation Specification Process and sent for co-processing in Products 28.4 cement industries or Disposal at (Batch failure) common incineration site.
13. Salt Condeser SCH-1/26.1 1080 Collection, Storage, Transportation and send to slude drying bed.
- 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 Non-Hazardous waste. (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) Only one solvent is Used in process. Other Solvent is to be used as reactant. Boiling Vapor Input Output % % Solvent Point Pressur (MT/mont (MT/mont Loss Recover Loss (0C) e h) h) y 3.8 110.6° kPa 420 Toluene 400 39 95.25 1.85 C (@ 25°C)
ii VOC emission sources and its mitigation measures During operation stage, leakage through valves/pumps, leakage and emission from
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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. • Breather valves will be provided on solvent tanks.
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H ‹ Details regarding storage of Hazardous chemicals Storage details Name of major Hazardous chemicals Remarks Acetone cynohydrin, Liquid Ammonia, Storage tanks Benzoyl Chloride, Hydrogen peroxide, Dibuthyl Phthalate, Acetone,IPA,
Diethylamine2-Ethylhexanoic acid, Hydrochloric Acid, Hydrazine Hydrate Drum/Barrel storage Sulphuric Acid , Methanol, Toluene
Cylinder, Bottle or Bromine & Chlorine Tonner
‹ Applicability of PESO : If Applicable, company will takepermission.
6. Details of Environmental Consultant: Sr. no. Particulars Details i Name of the Consultant Aqua Air Environmental Engineers Pvt. Ltd. ii Contact no. and e-mail ID of the Mo. no. :9099069611 Consultant e-Mail: [email protected] iii Accreditation for the categories Stay Order against NABET/QCI and Validity iv Any other details No Any other details
Name & designation of the Applicant: Mr.Paras Ram Choudhary
Stamp &Signature of Applicant: Date: 07/08/2019
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 e-mail to : [email protected] • 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.
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