Consultant: M/s. PVT. LTD. India. 1. Executive Summary . om Kavalam

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1 Pre - feasibility Report For DNS FINE CHEMICALS & LABORATORIES PVT. LTD., Plot No : W-, MIDC - Badlapur, Near Telephone Exchange Dist. Thane, Maharashtra, India. Consultant: M/s. SADEKAR ENVIRO ENGINEERS PVT. LTD. Accreditedd by QCI NABET Lab. Recognized by MoEF, Govt. of India NABL Accreditedd Certificate No. T- 9, Certified by ISO 9:8 Certified by BS OHSASS 8:7 4/44, Paradise Tower, Opp. Alok Hotel, Gokhale road, Naupada, Thane 4. Executive Summary Telephone : -84 / psadekar@yahoo.com / prs@sadekarenviro.com Name of the Project Web Propo onent site:- : arenviro.c Mr. Mathew om Kavalam May,

2 May Introduction DNS Fine is engaged in manufacturing and export of industrial chemicals for a variety of industrial requirements. In last years, it has grown into a highly matured and experienced company. Company's excellent growth rate over the years reaffirms a dedicated and efficient service to trade and industry will necessary make an increase in our client base who. Company always look for excellence in quality, uncompromising reliability and dependability keeping in mind efficient, effective customer service and their satisfaction as prime concern. DNS chemicals is ISO 9: certified company, company also have accreditation of Indian FDA, GMP. Description of Project Company is located at Plot no : W-, Badlapur MIDC, Near Telephone Exchange, Dist- Thane. Company have obtained consent to operatee from Maharashtra Pollution Control Board for manufacturing of Inorganic chemical products i.e.; Ammonium acetate, Monosodium phosphate, Di-Sodium phosphate, Tri Sodium phosphate, Mono Potassium Phosphate & Potassium Sulphate. The exiting production capacity of the unit is 7 MT/M, which will be increased up to 9.7 MT/M, quantitative details of both organic & inorganic products are as follows: Sr. Description No Inorganic Products Organic Products Total Existing (MT/M) Proposed (MT/M) Total (MT/M) Page

3 May Salient Features of Project Name & Address of Company M/s DNS Fine Chemicals & Laboratories Pvt. Ltd. Plot No: W-, Badlapur MIDC, Near Telephone Exchange, Dist : Thane, Maharashtra, India. Total Plot Area Total Plot Area: 9. Sq.m.. Ground Coverage Area:. Sq.m Green Belt Area: sq.m Parking Area:. sq.m Production details Existing production capacity : 7 MT/ /M ( Inorganic chemicals ) Proposed Production Capacity : 4.7 MT/M ( Organic chemicals.mt/m & Inorganic Chemicals- 4. MT/M) Total production Capacity: 9.7 MT/M ( Organic chemicals. MT/m & Inorganic Chemicals- 9. MT/M) Schedule of project as per EIA (f) Notification, Category of Project 'B' Production capacity as per schedule Existing : MT/MM (f) of EIA notification, Proposed :. MT/M Total :. MT/MM Total number of products comes Existing : Nos under schedule (f) of EIA Proposed : Nos notification, Total : Nos Total number of products does not Existing : Nos come under schedule (f) of EIA Proposed : Nos notification, Total : 7 Nos Water Requirement of Project Existing water requirement :.8 CMD Proposed additional water requirement :. CMD Total water requirement as after expansion : 7 Page

4 May Source of Electricity Power requirement of project Project Cost Effluent Details Sewage Effluent ETP Details Boiler Details Fuel Requirement for Boiler D.G. Set Fuel requirement for D.G. CMD MSEDCL Existing : Connected Load : KVA Existing Demand : 4 KVA Proposed: Proposed Connected Load : KVA Proposed Demand : KVA Existing : Cr Proposed: 7 Cr Total: Cr. Existing :. CMD Proposed :.9 CMD Total :.4 CMD. CMD Existing : CMD Proposed (After Up gradation) : CMD Existing : 8 kg/ /hr Capacity (Non - IBR Type) Proposed : Mt/hr Capacity ( IBR Type) Existing boiler will be removed Existing :. MT/D ( Wood) Proposed :.4 MT/D ( Wood/ Briquettes) KVA ( Proposed D.G.) HSD ( Lit/ Hr) Page 4

5 May Production Details Currently company is manufacturin g inorganic chemicals only, the existing production capacity of project is 7 MT/M. which will be increased upto 9.7 MT/M out of which. MT will be organic chemical products. Inorganic Products Sr.No Finished Product Ammonium Acetate Sodium Phosphate Dibasic anhydrous Existing Proposed Quantity ( Quantity ( Mt/ Mt / Month ) Month ) Sodium Phosphate Tribasic Dodecahydrate Mono Sodium Phosphate Monoo Potassium Phosphate Potassium Sulphate Ammonium Dihydrogen Phosphate Ammonium Formate Ammonium Sulphate Calcium oraoate 4 Cadmium Nitrate. Calcium Levulinate Diammonium Hydrogen Phosphate EDTA Di Potassium EDTA Disodium Dihydrate EDTA Tetra Sodium Tetra Hydrate Ferrous Sulphate Heptahydrate Ferric pyrophosphate Lead Aceate Trihydrate Lead subaceate Lead Nitrate Magnesium Acetate Tetrahydrate Manganese Acetate Tetrahydrate Manganese Sulphate Monohydrate Nickel Nitrate Hexahydrate Nickel Sulphate Hexahydrate Potassium Acetate Potassum Formate Potassium Carbonate Sesquihydrate e Potassium Dihydrogen Orthophosphate Potassium Hydrogen Phthalate Potassium Hydrogen Sulphate Total ( Mt / Month ) 4. Page

6 May 4 7 Potassium Nitrate Potassium Sulphate Di Potassium Hydrogen Orthophosph ate Anhydrous Sodium Acetate Anhydrous Sodium Acetate trihydrate 8 Sodium Dihydrogen orthro Phosphate Anhydrous 9 S odium Dihydrogen Phosphate Monohydrate Sodium Fluoride strontium Citrate Sodium Phosphate Dibasic Dihydrate Zinc Sulphate Monohydrate Sodium Thiosulphate Pentahydratee Sodium Selenate Zinc acetate Dihydrate Zinc Acetate Anhydrous Zinc Sulphate Heptahydrate Zinc Sterate. Zinc Oxide Ammonium Iodide Calcium Iodide.. Calcium Iodate Copper Iodide. Hydriodic acid ( HI acid) Iodic acid. Lead Iodide. Potassium Iodide Potassium Iodate Potassium Metaperiodate Per Iodic acid. Sodium Iodide Sodium Iodate Sodium Metaper Iodate Silver Iodide. Zinc Iodide. Stannous chloride Selenium Dioxide Sodium Selenite Sodium Selenate Selenium Sulphide Page

7 May 7 A B C Selenous acid Total Organic Products Benzoic acid. EDTA 8 Thiourea Urea Diiodo Salicyclic acid Diiodohydroxyquinoline Ethylene diamine Dihydroiodide ( EDDI) Iodo Benzene... Iodoo Methyl Benzoic acid Iodoform.. Iohexol Ioversol Iopamidol Iodophor Methyl Iodide. Povidone Iodine Thymol Iodide. Trimethyl sulphonium Iodide Trimethyl Iodo Silane Halquinol.. Total.. Grand Total A + B Page 7

8 May List of Raw Material Sr. No Raw Material Acetic acid Existing Quantity ( Mt / Month ) Formic acid 4 Iodine Phosphoric acid 7 Sulphuric acid. Hydrochloric acid 7 8 Nitric acid Sodium Hydroxide 9 Potassium Carbonate Potassium Hydroxide Urea Chlorine Gas Mangenese Metal 4 Selenium Metal Zinc Oxide Ammonia Gas 8 7 Hydrazine Hydrate 8 Ethylene Diamine 9 Mangesium Metal Activated Carbon. Hyflow Powder Hydrogen Peroxide Ammonium Chloride 4 EDTA acid Ammonium Sulphate Ammonium Bicarbonate 7 Potassium Permagnate 8 Barium Hydroxide 9 Glycerol Barium Nitrate Boric acid Borax Calcium Carbonate 4 Ammonium Carbonate Calcium hydroxide Citric acid Monohydrate 7 Cupric sulphate Proposed Quantity ( Mt / Month ) Total ( Mt / Month ) Storage details 7 Tanks T Drums ( kg) or Carbouys ( Kg) kg Fibre drums on pallets 7 Carbouys ( / kg) on pallets.. Carbouys ( kg) on pallets Carbouys ( kg) on pallets Carbouys ( 4 kg) on pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets Tonner ( kg) filled tonners Jumbo Bags ( kg ) Bags on Pallets ( kg ) Bags on Pallets 8 Cynlider ( kg) 4 cylinders Drums ( kg) ( kg ) Bags on Pallets ( kg ) Bags on Pallets.. ( kg ) Bags on Pallets.. ( kg ) Bags on Pallets Carbouys ( 4 kg) on pallets.. ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets.. Drums ( kg) ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets Page 8

9 May Pentahydrate 8 Magnesium Sulfate 9 Sodium Acetatee 4 Sodium Sulphate 4 Hydrated Lime 4 Potassium Nitrate 4 Potassium Sulphate 44 Tertaric acid D. 4 Tertaric acid L Tin Metal Calcium Chloride 48 Levualic acid 49 Methyl Benzoic acid Liquor Ammonia. Chloro 8 HQ 8 Hydroxyquinoline Copper sulphate pentahydrate 4 Diethyl Carbamazine base Citric Acid monohydrate Salicyclic acid 7 Red Phosphorous. 8 Chloro acetic acid 9 Methanol Nonyl Phenol Ethylene Oxide PHBA 8 Hydroxyquinoline sulphate sulphur Dioxide Gas. 4 7 PVP K Piperazine Propanol Silver Nitrate. 8 9 Thiourea Hexamethyl Silane Total ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) carbouy ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets kg drums kg drums ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets kg drums ( kg ) Bags on Pallets ( kg ) Bags on Pallets ( kg ) Bags on Pallets Page 9

10 May Pollution Load and Mitigation Measures Company takes the necessary precautions to protect the environment by using scrubbers & treating effluent from reactor washing in their effluent treatment plant. Company also has membership of Badlapur CETP & CHWTSDF - Taloja for disposal of treated effluent & hazardous waste respectively. The other non hazardous solid waste like bags, papers etc are sold to recyclers. Effluent Treatment Plant The existing ETP of company is comprises of Primary & Tertiary treatment, currently company is manufacturing inorganic chemicals only. No any process effluent generation is envisaged & the only source of effluent generation are reactor washing, boiler blowdown & cooling tower blowdown. After expansion company will be manufacturer of API & Inorganic chemicals. The existing effluent generation of company is around. -. CMD, after expansion the effluent quantity will be raised up to.4 CMD, to handle this additional load of effluent company will upgrade their existing ETP of CMD up to CMD. The exiting Effluent Treatment Unit Comprises of following units Sr. No Unit. Equalization Tank. Alum dosing tank 4. Poly dosing tank. Primary Settling Tank. Sludge drying bed 7. Filter feed tank 8. Activated Carbon Filter 9. Pressurized Sand Filter Quantity No. No. No. No. No. No. No. No. Size/ Capacity. M. M. M. M - -.m Dia X. M height.m Dia X. M height Page

11 May Characteristics of effluent Sr. No Parameter ph Total Dissolved Solids COD BOD( days at 7 C) Characteristics Before After Treatment Treatment. 9 Note: All the parameters are expressed in mg/l except ph MPCB Limit. to 8. B. Quantum of Waste Generated:. Non Hazardous waste: Sr.No. Type of waste Existing Bags 4 Spent oil - Fly ash from boiler ( Existing boiler will be remove) Quantity Proposed 7 UOM Total After expansion 9 Bags/M Lit/ A 7 Kg/D Mode of Disposal Sold to recycler Sold to authorized vendor Sold to brick manufacturer r. Hazardous waste Cat. No. Type 4. ETP Sludge Existing kg/m Quantity Total Mode of Disposal Proposed kg/ /A kg/m Sent to CHWTSDF, Taloja Page

12 May Air Emission Control Sr. Item No. Air Utilities Stack attached to various utilities with sufficient height Existing / Proposed to be installed Utilities Existing Proposed Boiler Capacity X 8 Existing boiler will be kg/hr replaced with new boiler of MT/Hr capacity Fuel Wood : Wood/ Briquettes :.4 kg/d MT/D Stack m m height Source of Local Local vendor fuel vendor D.G Set Capacity - X KVA Fuel - Diesel - Lit/Hr (only during power failure) Stack - m ground level height Source of - Local vendor fuel Scrubbers Plant Section & Units Process Scrubber Height form ground level 4 m above roof level Existing/Proposed. CFM alkali scrubber - Existing. CFM alkaline scrubber - Proposed Page

13 May Water Requirement Sr. No. 4 Activity / Process Domestic Process Boiler Cooling Tower Garden Total Existing CMD Proposed CMD Page

14 May (x) Schematic Representation of the Feasibility Drawing of EIA RESOURCEE CONSUMPTION (WATER) POWER CONSUMPTION RAW MATERIAL PRODUCTION ACTIVITY WASTE GENERATION FINISHED PRODUCTS POLLUTION ABATEMENT EMPLOYMENT MARKET CLEAN ENVIRONMENT ECONOMY Page 4

15 May 4. Site Analysis The industry is located in Badlapur MIDC (i) Connectivity: The project is located in Badlapur industrial area which is easily accessible from Neral - Badlapur Road further connecting to the project site by internal access roads developed by MIDC. Nearest Railway Station: Badlapur, approximately at a distance of.4 km (aerial distance). Nearest Airport: Chatrapati Shivaji International Airport approximately at a distance of 9.8 km (Aerial distance). Location and Access The industrial area is centrally located and easily accessible through all modes of transport. Road: The entire industrial area is well connected by internal roads. Available Road Network: Neral - Badlapur Road at a distance of approximately. km from the project site. (ii) Land Form, Land use and Land Ownership: The Project location & the surrounding environs being located in the notified industrial area prevails industrial land use form. (iii) Topography: Since the topographic characteristics govern a greater land mass, the topography of entire district has been taken into account. The project site falls under the district of Thane. The district Thane is in northern Maharashtra State in western India. The area of the district is 9,8 km². The district is bounded by Pune and Ahmadnagar on the east, Nashik on the east and northeast, Valsad District of Gujarat state and Union Territory of Dadra and Nagar Haveli on the north. The Arabian Sea forms the western boundary, while it is bounded by Mumbai City District and Mumbai Suburban District on the southwest and Raigad (iv) Existing land use pattern The proposed project is located in the notified industrial area which has been developedd for industrial development. The existing land use pattern in the km radial distance of the project site comprises of Industrial, human habitations/settlements, small agricultural/ crop lands, quarrying land use classes. Page