M/S. CLEAN SCIENCE PRIVATE LIMITED.

M/S. CLEAN SCIENCE PRIVATE LIMITED. PFR for Environmental Clearance (EC) of Proposed Greenfield project of Manufacturing of Synthetic Organic Chemicals at Plot No.: No.: D-25/1/1 MIDC, Kurkumbh, Tehsil Daund, District Pune, Maharashtra Goldfinch Environmental Engineering Systems Private Limited ( Goldfinch ), December 2017 This report is released for the use of the M/s Clean Science Pvt. Ltd. (CSPL). Regulators and relevant stakeholders solely as part of the subject EC of Proposed Greenfield project of Manufacturing of Synthetic Organic Chemicals at Plot No.: D-25/1/1 MIDC, Kurkumbh, Tehsil Daund, District Pune, Maharashtra. Information provided (unless attributed to referenced third parties) is otherwise copyrighted and shall not be used for any other purpose without the written consent of Goldfinch/Clean science. QUALITY CONTROL Name Publication of Proposed Greenfield project of Manufacturing of Synthetic Organic Chemicals, at Plot No.: D-25/1/1 MIDC, Kurkumbh, Tehsil Daund, District Pune, Maharashtra Project Number Prepared By Released By DISCLAIMER GEC/CSPLK/ 2016/11/04 Report No. 1 Version 1 Released December,2017 Rakesh Suryawanshi and Umesh Parab Mr. Anand Apte Goldfinch has taken all reasonable precautions in the preparation of this report as per its auditable quality plan. Goldfinch also believes that the facts presented in the report are based on information submitted by Clean science and based on the technical expertise of Goldfinch as on the date it was written. However, it is impossible to dismiss absolutely, the possibility of errors or omissions. Goldfinch therefore specifically disclaims any liability resulting from the use or application of the information contained in this report. The information is not intended to serve as legal advice related to the individual situation. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 1

CONTENTS 0 EXECUTIVE SUMMARY... 5 1 INTRODUCTION OF THE PROJECT... 6 1.1 IDENTIFICATION OF PROJECT... 6 1.2 PROJECT PROPONENT... 6 1.3 BRIEF DESCRIPTION OF NATURE OF THE PROJECT... 6 1.4 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE COUNTRY AND OR REGION... 6 1.5 DEMAND-SUPPLY GAP... 7 1.6 IMPORT VS. INDIGENOUS PRODUCTION... 7 1.7 DOMESTIC/ EXPORT MARKETS... 7 1.8 EMPLOYMENT GENERATION (DIRECT AND INDIRECT) DUE TO THE PROJECT... 7 2 PROJECT DESCRIPTION... 8 2.1 TYPE OF PROJECT... 8 2.2 LOCATION (MAP SHOWING GENERAL LOCATION, SPECIFIC LOCATION AND PROJECT BOUNDARY & PROJECT SITE LAYOUT) WITH COORDINATES... 8 2.3 DETAILS OF ALTERNATE SITES CONSIDERED AND THE BASIS OF SELECTING THE PROPOSED SITE... 10 2.4 SIZE OR MAGNITUDE OF OPERATION... 10 2.5 PROJECT DESCRIPTION WITH PROCESS DETAILS... 11 2.6 RAW MATERIAL REQUIRED ALONG WITH ESTIMATED QUANTITY, LIKELY SOURCE, MARKETING AREA OF FINAL PRODUCT/S, MODE OF TRANSPORT OF RAW MATERIAL AND FINISHED PRODUCT.... 18 2.7 RESOURCE OPTIMIZATION/RECYCLING AND REUSE ENVISAGED IN THE PROJECT,... 18 2.8 AVAILABILITY OF WATER ITS SOURCE, ENERGY/POWER REQUIREMENT AND SOURCE SHOULD BE GIVEN... 18 2.8.1 Water... 18 2.8.2 Power... 19 2.8.3 Fuel Requirement... 19 2.9 QUANTITY OF WASTES TO BE GENERATED (LIQUID AND SOLID) AND SCHEME FOR THEIR MANAGEMENT/DISPOSAL.. 19 2.9.1 Gaseous Emissions... 19 2.9.2 Liquid Effluent... 20 2.9.3 Details of Hazardous wastes... 22 2.10 SCHEMATIC REPRESENTATIONS OF THE FEASIBILITY DRAWING WHICH GIVE INFORMATION OF EIA PURPOSE.... 23 3 SITE ANALYSIS... 24 3.1 CONNECTIVITY... 24 3.2 LAND FORM, LAND USE AND LAND OWNERSHIP... 24 3.3 TOPOGRAPHY... 24 3.4 EXISTING LAND USE PATTERN (AGRICULTURE, NON-AGRICULTURE, FOREST, WATER BODIES (INCLUDING AREA UNDER CRZ)), SHORTEST DISTANCES FROM THE PERIPHERY OF THE PROJECT TO PERIPHERY OF THE FORESTS, NATIONAL PARK, WILD LIFE SANCTUARY, ECO SENSITIVE AREAS, WATER BODIES (DISTANCE FROM HFL OF THE RIVER), CRZ.... 25 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 2

3.5 SOIL CLASSIFICATION... 25 3.6 CLIMATIC DATA FROM SECONDARY SOURCES... 25 3.7 SOCIAL INFRASTRUCTURE AVAILABLE... 26 4 PLANNING BRIEF... 27 4.1 PLANNING CONCEPT (TYPE OF INDUSTRIES, FACILITIES, TRANSPORTATION ETC) TOWN AND COUNTRY PLANNING/ DEVELOPMENT AUTHORITY CLASSIFICATION... 27 4.2 LAND USE PLANNING... 27 4.3 ASSESSMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL)... 27 4.4 AMENITIES/FACILITIES... 28 4.5 Population Projection... 28 5 PROPOSED INFRASTRUCTURE... 29 5.1 INDUSTRIAL AREA (PROCESSING AREA/NON- PROCESSING AREA)... 29 5.2 RESIDENTIAL AREA... 29 5.3 GREEN BELT... 29 5.4 SOCIAL INFRASTRUCTURE... 29 5.5 CONNECTIVITY... 29 5.6 DRINKING WATER MANAGEMENT... 29 5.7 SEWERAGE SYSTEM... 29 5.8 INDUSTRIAL WATER MANAGEMENT... 30 5.9 SOLID WASTE MANAGEMENT... 30 5.10 POWER REQUIREMENT & SUPPLY / SOURCE... 30 6 REHABILITATION AND RESETTLEMENT (R & R) PLAN... 31 6.1 POLICY TO BE ADOPTED (CENTRAL/STATE) IN RESPECT OF THE PROJECT AFFECTED PERSONS INCLUDING HOME OUSTEES, LAND OUSTEES AND LANDLESS.... 31 7 PROJECT SCHEDULE & COST ESTIMATES... 32 7.1 LIKELY DATE OF START OF CONSTRUCTION AND LIKELY DATE OF COMPLETION... 32 7.2 ESTIMATED PROJECT COST ALONG WITH ANALYSIS IN TERMS OF ECONOMIC VIABILITY OF THE PROJECT... 32 Economic Viability... 32 8 ANALYSIS OF PROPOSAL... 33 8.1 FINANCIAL AND SOCIAL BENEFITS WITH SPECIAL EMPHASIS ON THE BENEFIT TO THE LOCAL PEOPLE.... 33 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 3

LIST OF FIGURES Figure 2-1: Satellite Image of the Site... 8 Figure 2-2: Site Photographs... 9 Figure 3-1:Topograph... 25 LIST OF TABLES Table 1-1: List of Directors and their designations... 6 Table 2-1:Size/Magnitude of Proposed Production Capacity... 13 Table 2-2: Details of Raw material Quantity, Source and Mode of Transport... 18 Table 2-3: Details of Raw water consumption... 19 Table 2-4: Details of emissions from process and flue gas... 19 Table 2-5: Details Stacks along with their mitigation method... 20 Table 2-6: Details of Effluent Generation... 20 Table 2-7: Design details and Performance Projection of ETP... 22 Table 2-8: Details of Proposed Hazardous Solid waste along with the Category and disposal method... 23 Table 4-1: Land Use Break Up... 27 Table 7-1: Cost Break-Up... 32 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 4

EXECUTIVE SUMMARY Clean Science Pvt. Ltd. (CSPL) was established in the year 2013 for manufacturing of Synthetic Organic Chemicals. Clean Science - as the name suggests is all about Clean Chemistries. CSPL is a leading producer of Mono Methyl Ether of Hydroquinone (MEHQ), Guaiacol, 4-Methoxy Acetophenone (4-MAP), Anisole and Butylated Hydroxy Anisole (BHA). CSPL is a Premium manufacturer of high quality 4- Methoxypropiophenone and Acetanisole. All the products are import substitute and over 70% of the products are exported. Now, CSPL proposes Greenfield project of manufacturing of synthetic organic chemicals at plot no. D-25/1/1, MIDC Kurkumbh, Taluka Daund, Pune, District. The promoters of the company are technocrats with vast experience in chemical industry. The Board of Directors consists of recognized personalities from academic & chemical industry background. Project Synopsys: Sr. No Parameters Description 1. Category as per EIA Notification ( 5 f) B -1 2. Proposed Production Capacity Products : 22,400 MT/A and By-products : 3700 MT/A 3. Total Plot Area 30000 sq. m. 4. Green Belt Area 9900 sq. m. 5. Fresh Water Requirement 650 CMD 6. Effluent Quantity (Trade + Domestic) 93.0 CMD + 10.5 CMD = 103.5 CMD 7. Trade Effluent Treatment High COD & TDS stream from process will be treated by anaerobic treatment separately. Treated effluent will be mixed with Low COD & TDS streams from process and utilities. Domestic wastewater will also be treated in secondary as a combined treatment. Treated effluent will be fed to RO. Permeate will be reused and reject will be fed to MEE. Thus unit will be run on ZLD scheme. The unit will be run on ZLD till proper functioning of CETP. 8. Domestic Waste water Treatment Will be treated in combine ETP 9. Type of Fuel and its requirement Coal - 43 TPD for boiler Coal - 7 TPD for Thermopack HSD - 6.5 TPD for DG PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 5

Sr. No Parameters Description 10. Power Requirement 1000 KVA 12 TPH (01 nos.) & 6 TPH (01 nos.) 11. Boiler, Stack height Stack height = 40 m common stack for both boilers 12. Thermopack, Stack height 10 lac Kcal/hr (01 nos.) & 6 lac Kcal/hr (01 nos.) Stack height = 30m common for both Thermopack. 01 no. 1000 KVA 13. DG Set, Stack height Stack Height : 6.3 m above enclosure 14. Work Force 400 nos. 15. Capital Cost the project (Cr) 70 Cr. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 6

1.0 INTRODUCTION OF THE PROJECT 1.1 Introduction of the Project The objective of this pre feasibility study is to provide information for the synthetic organic chemicals manufacturing unit by M/s. Clean Science Private. Limited proposed at Plot No.: D-25/1/1 MIDC, Kurkumbh, Tehsil Daund, District Pune, Maharashtra As per the EIA Notification No. S. O. 1533 promulgated on 14 th September 2006, proposed project has been covered under Synthetic Organic Chemicals Industry (5 (f)) and need prior environmental clearance. It is stated that industries located in a notified industrial area are classified under category B and would be appraised by State Level Expert appraisal committee/ impact assessment authority. Based on the OM dated 4 th April 2016 by Director MoEF, Public Hearing is exempted. 1.2 Introduction of the Project Proponent Mr. Ashok Boob - Managing Director Qualification: B. Chem. Engg. from ICT, Mumbai. Experience: Over 40 years of experience in the chemical industry. Mr. Krishna Boob, Executive Director Qualification: B. Pharmacy from University of Mumbai. Experience: More than 35 years in Chemical & Pharmaceutical Industry. Mr. Siddharth Sikchi, Executive Director Qualifications: M.Sc. in Organic Chemistry from University of Manitoba, Canada and B. Tech from ICT, Mumbai. Experience: 12 years in the Chemical Industry. To his credit, he has recently received a Young Entrepreneur Award for commercializing unique & eco-friendly process in India from the hands of Dr. Anil Kakodkar, Padma Vibhushan. 1.3 Brief description of nature of the project The proposed project is proposed at Plot No. : D-25/1/1 MIDC, Kurkumbh with land admeasuring 30000 Sq. Meters. The land is already demarcated as Industrial in a notified industrial area and is not a prime Agricultural land. Thus there is no change in the land use status. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 7

Proposed project is a greenfield project to manufacture Mono Methyl Ether of Hydroquinone (MEHQ), Guaiacol, 4-Methoxy Acetophenone (4-MAP), Anisole and Butylated Hydroxy Anisole (BHA) having total production capacity of 22400 MT/A & byproducts having capacity of 3700 MT/A. Company is mainly focusing on three different chemistries, namely hydroxylation, acylation & alkylation using Zeolite catalyst systems on commercial scale. The company produces its own catalyst for captive consumption. The products like MEHQ and Guaiacol are manufactured first time in the world using this technology. They produced using a novel & eco-friendly process. Butylated Hydroxy Anisole (BHA) is produced using MEHQ as a raw material & the process generates only water as an effluent. All the above products are import substitute and have very good export potential. 1.4 Need for the project and its importance to the country and or region Fragmented nature of industry makes it difficult for the companies to optimize operational costs, realize economics of scale and adopt latest technologies, making them uncompetitive globally. The industry should actively move towards investing in new capacities with scale and size matching global standards to achieve world scale of plants and reap economies of scale and adopting cutting edge technologies. Product innovations for meeting local needs rely heavily on the chemical industry for inputs and support. The areas for strengthening are R & D activities in chemical industry for the improvements in catalysis, manufacturing process, reduction in cost of production, development and design of new products relevant to the Indian market needs. In the Indian sub-continent` population growth is more than that of developed countries. Strong end use industry demand is expected to boost growth for the Indian chemical companies, both domestic & multinational. To meet the needs and comforts of evergrowing population industrialization became inevitable. The project is envisaged to meet the demand supply gap in both domestic and export market. The project meets to reduce imports in some of the intermediate products and also enhance the foreign exchange reserves in view of the exports of few products. 1.5 Demands-Supply Gap Chemical Industry is one of the oldest industries in India, which contributes significantly towards industrial and economic growth of the nation. It is highly scientific type of industry and provides valuable raw material/chemicals for various types of industries such as textiles, paper, paints and varnishes, leather, pharmaceuticals etc., which are required in almost all walks of life. The Indian PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 8

Chemical Industry forms the backbone of the industrial and agricultural development of India and provides building blocks for downstream industries. India s chemical industry is one of the largest and most diversified industries in the country and it consists of several small industries that cover hundreds of segments. Chemicals are generally used to make a wide variety of consumer goods and are also used in agriculture, manufacturing, construction, and service industries. The chemical industry itself consumes 26% of its own output. Major industrial customers include rubber and plastic products, textiles, apparel, petroleum refining, pulp and paper, and primary metals. With the chemical industry contributing indirectly to almost every sector of the economy, it plays a vital role in a country s economic growth. The domestic chemical industry contributes 3-4 % in India s GDP while India accounts for 8.3 % of the Asia-Pacific chemicals market's value. India s chemical industry s size in 2010-11 is estimated to be around $ 83 billion and is expected to reach $ 120 billion by 2013. India sales are projected to reach $ 250 billion by 2020. The total investment in Indian Chemical Sector is approx. US $ 60 billion and total employment generated is about 1 million. The Indian Chemical sector accounts for 13-14 % of total exports and 8-9 % of total imports of the country. In terms of volume, it is 12th largest in the world and 3rd largest in Asia. Currently, per capita consumption of products of chemical industry in India is about 1/10th of the world average. Over the last decade, the Indian Chemical industry has evolved from being a basic chemical producer to becoming an innovative industry. With investments in R & D, the industry is registering significant growth in the knowledge sector comprising of Synthetic Organic Chemicals, fine chemicals and pharmaceuticals. Companies in this industry manufacture basic, intermediate and Synthetic Organic Chemicals. Major companies include Dow and DuPont (both based in the US), BASF (Germany), INEOS Group (UK), Lyondell Basel (The Netherlands), Mitsubishi Chemical (Japan), and Roche (Switzerland). Per capita chemical consumption in India is low as compared to world standards (estimated to be one tenth of world average). Increasing consumption level in the domestic market would ignite the prevailing latent demand. To achieve global standards the industry needs to put efforts in critical areas so as to adopt aggressive growth and focus on exports, R & D, co-marketing alliances, up-gradation of manufacturing facility, contract manufacturing with companies having established markets, identification of areas of core competence, consolidation, collaboration by cluster development, outsourcing, environmental consciousness, cost reduction etc. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 9

1.6 Imports vs. Indigenous Production The proposed products having high demand in the export market. Also their demand is increasing in the domestic market. Production of these products are domestically reduces the need to import these in future along with significant scope for export in these products. 1.7 Domestic /Export Markets The finished goods will be sold in domestic market and would be largely exported to the Regulated International Market as per demand all over the world. 1.8 Employment Generation due to the project The project for manufacturing of Synthetic Organic Chemicals requires substantial handling of raw materials, chemicals in process and finished products. Project creates direct & indirect employment opportunities to people living in the surrounding region. The Management of the Company has always preferred to engage (employment) local people from the nearby villages depending upon skilled & unskilled man-power available and train them in the required field. Total direct employment is around 400 people. Apart from direct employment, there is substantial indirect employment to the people giving support services in various fields. It enhances the earnings due to various direct or indirect businesses in the areas. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 10

2.0 PROJECT DESCRIPTION 2.1 Type of Project proposed project is a greenfield to manufacture Mono Methyl Ether of Hydroquinone (MEHQ), Guaiacol, 4-Methoxy Acetophenone (4-MAP), Anisole and Butylated Hydroxy Anisole (BHA) having total capacity of 22400 MT/A and byproducts having capacity of 3700 MT/A. 2.2 Project Location Clean Science Private. Limited proposes manufacturing unit at Plot No. D-25/1/1 MIDC, Kurkumbh, Tehsil Daund, District Pune, Maharashtra. Kurkumbh is a well-developed industrial area of the MIDC near Daund Town. The MIDC area, adjacent to the Kurkumbh village, is one of the 13 chemical industrial areas developed by MIDC. The Kurkumbh Industrial area is under the jurisdiction of Daund Taluka (about 9 km) and under Dist. Pune (about 65 km). The area is surrounded by agriculture land. Kurkumbh area has well developed road and rail network, which is connected to Pune - Solapur National Highway 9 (on 1 km) and Central Railway (Daund Junction) on 9.8 km. No sanctuary, national park or ecologically sensitive area is situated within 10 km radius of Kurkumbh MIDC Longitude Lattitude National Highway Nearest railway station Nearest city Nearest air port Nearest water body from project site Seismic zone 74 31'26.16"E 18 24'11.06"N (NH-9) at a distance of approx. 0.75 km. Daund Junction 9 km Daund Pune Airport 66 km Daund Lake 4.0 km Northeast Patas Lake 7.2 km Northwest Warwand Dam 12 km West Shirsuphal Dam 11 km Southeast Zone- 3 ( Moderate Damage Risk Zone) PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 11

Figure 2-1 : Satellite Image of the Site Point Latitude Longotude A 18 24'12.22" 74 31'30.66" B 18 24'9.38" 74 31'29.90" C 18 24'9.52" 74 31'29.29" D 18 24'9.02" 74 31'29.12" E 18 24'9.77" 74 31'25.82" F 18 24'8.62" 74 31'25.48" G 18 24'9.46" 74 31'22.24" H 18 24'10.37" 74 31'22.51" I 18 24'10.52" 74 31'21.78" J 18 24'14.24" 74 31'22.79" PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 12

The project site is situated in MIDC, Kurkumbh. It is a notified industrial area where the land is owned by Maharashtra Industrial Development Corporation (MIDC) and leased to the Company. The land is meant for industrial activity. Land Ownership: Land is owned by Maharashtra Industrial Development Corporation (MIDC) and leased to the Company for 99 years. 2.3 Details of alternate sites considered and the basis of selecting the proposed site Since the proposed site has sufficient land available and owned by proponent. The following points were considered for selecting the proposed site: Location is within the established notified industrial estate Availability of common infrastructural facilities of the industrial estate Availability of water supply in the industrial estate Availability of un-interrupted power supply in the industrial estate Hence alternate sites were not considered. 2.4 Size or Magnitude of Operation The products manufactured and their capacities proposed are shown in below Table 2.1. Table 2-1: Size/Magnitude of Proposed Production Capacity S.No. Products Quantity (MT/A) 1 Anisole 10000 2 Butylated Hydroxy Anisole 2400 3 Mono Methyl Ether of Hydroquinone 3300 4 Guaiacol 1700 5 Phenothiazine 5000 Total 22,400 By-products S.No. Products Quantity (MT/A) 1 O-Cresol 250 2 Sodium Sulphate 3450 Total 3700 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 13

2.5 Process Description 1. Anisole Process Description: Phenol is mixed with Methanol. This mixture is pre heated to 200 deg. C using a heat exchanger. The vapours generated are then passed through catalyst bed in tubular form. The vapours at the outlet are then fed to distillation column 1. In first distillation column unreacted Methanol & Water are separated. Unreacted Methanol is sent back to reaction mixture. In second distillation column, Anisole is distilled out. In the third distillation column unreacted Phenol is recovered and sent back to reaction mixture. Chemical reaction:- Process flow diagram PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 14

Material Balance No. Input Qty in KG No. Output Qty in Kg 1 Phenol 0.92 1 Anisole 1.03 2 Methanol 0.33 2 O-cresol 0.05 3 Water 0.17 Total 1.25 Total 1.25 kg Process Description: Phenol is first treated with sodium hydroxide to form sodium salt of phenol. To this DMS is added drop wise at elevated temperature in couple of hours. After complete reaction of phenol, water is separated and organic layer is taken for distillation. On distillations pure Anisole is obtained Chemical reaction:- PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 15

Process flow diagram:- Material Balance Input Mass (kg) Output Mass (kg) Phenol 0.90 Anisole 1.00 DMS 0.70 Sodium Sulphate 0.69 NaOH 0.39 Water 0.30 Total 1.99 Total 1.99 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 16

2. Butylated hydroxyl Anisole (BHA) (Alkylation of MEHQ) Process Description: Mono-methyl ether Hydroquinone (MEHQ) is reacted with tertiary butanol in presence of an acid catalyst at elevated temperature. After the reaction the mixture is filtered off to separate the catalyst (which is then reused for next reaction). The reaction mixture is then subjected to series of distillation columns. In column 1, water is separated. In column 2, un-reacted mono-methyl Ether Hydroquinone (MEHQ) is separated & recycled back to the reaction mixture. In column 3, crude Butylated Hydroxy Anisole (BHA) is distilled out. This crude BHA is then subjected to solvent purification using Hexane. Pure BHA obtained is then flashed in a simple column to separate any traces of hexane & the molten pure BHA is flaked and packed in fiber drums Chemical reaction:- PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 17

Process flow diagram:- Material Balance Input Mass ( kg) Output Mass (kg) Mono-Methyl Ether Hydroquinone (MEHQ) 0.710 Waste Water 0.129 Tertiary Butanol 0.420 2 & 3-BHA 1.000 Residue on distillation 0.001 Total 1.13 Total 1.13 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 18

3. Mono Methyl Ether of Hydroquinone (MEHQ ) + Guaiacol (Hydroxylation of Anisole) Process Description: Anisole is hydroxylated using Hydrogen Peroxide (60%) in presence of Zeolite catalyst. Resultant mixture is subjected to series of distillation processes to separate raw materials which are then re-cycled & reused again to obtain the end products. In distillation Column 1, solvent is distilled out and reused. In distillation Column 2, un-reacted Anisole is distilled out and recycled again and again in the process. In distillation Column 3, Guaiacol is separated out which is packed in HDPE drums. The next fraction consists of pure MEHQ which is then flaked and packed in fiber drums. Material balance to produce Guaiacol and MEHQ Chemical reaction: PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 19

Process flow diagram :- Material Balance Input Mass (kg) Output Mass (kg) Anisole 0.950 Waste Water 0.712 H₂O₂ (60%) 0.800 Residue Traces 0.002 MEHQ/Guaiacol 1.036 Total 1.75 Total 1.75 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 20

4. Phenothiazine Process Description: Diphenyl amine + Sulphur + Catalytic Iodine is added to the reactor. The reactor is heated to 200 c and reaction is maintained for 5 hrs. Until Diphenyl amine is completely converted to Phenothiazine.After this reaction methanol is added to the mixture. The slurry is then centrifuged and product is dried to obtain pure Phenothiazine.H2S gas is scrubbed is caustic solution to produce NaSH which would be sold as by product. Chemical reaction:- + 2S + I 2 169 64 199 34 + H 2 S Process flow diagram:- PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 21

Material Balance:- Input Mass (kg) Output Mass (kg) Diphenyl amine 0.850 Phenothiazine 1.000 Sulphur 0.330 H2S 0.178 Iodine Catalytic Impurities/Residue 0.002 Total 1.180 Total 1.180 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 22

2.6 Raw material required along with estimated quantity, likely source, marketing area of final Product/s, mode of transport of raw material and finished product Raw Materials: The basic raw material for this key products capacity are submitted herein below and for the details are given for all reactants, solvents and work up support chemicals. Source for Raw Material Procurement: Raw Material is easily available in the local market; some of the raw materials are In-house. Sr. No. Mode of Transport of Raw Materials: Raw Material and finished goods will be transported through Trucks/ Tankers or which are in house will be transported through pipelines as per the requirements. Storage at the site: Raw Materials will be stored in storage yard at the project site. Location of storage yard is demarcated in Layout Plan. Name Nos. of storage Capacity 1 H₂O₂ - 60% 1 100 KL 2 MEHQ LOT 25 kg X 400 Nos. 3 Phenol 2 200 KL 4 Anisol 2 5 Tertiary Butanol 100 KL 1 50 KL Table 2-2: Details of Raw material Physical and Chemical Composition Colorless, liquid, slightly more viscous than water. Strong oxidizer & used as a agent & disinfectant White Solid (Flakes), Soluble in water. Colorless liquids or white solids at room temp. More soluble in water than are alcohols and have higher boiling points. Colorless liquid smells of of anise seed, insoluble, nontoxic Clear liquid (odorless solid, depending on the ambient temp) with a camphor-like odor. Soluble in water and miscible with ethanol Consumption (MT/A) Maximum Quantity of storage at any point of time 4000 100 KL 1704 25 kg X 400 Nos. 9100 200 KL Source Of Supply National Peroxide Ltd. Mumbai Captive SI group, Mumbai. 4750 100 KL Captive 1008 50 KL Aki Shokai Co. Ltd., Japan. Means of Days of transpor storage tation By Road 3-5 Self - Product 3-5 By Road 3-5 Self- Product By Sea 3-5 8-10 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 23

6 NaOH (50 %) and diethyl ether. 1 100 KL Clear liquid 1950 100 KL 7 DMS 1 100 KL Liquid, colorless, stench 3500 100 KL 8 Methan ol 1 50 KL 9 DPA 1 50 KL 10 Sulphur 1 11 Iodine LOT 25 KG Bags 25 KG Bags Liquid, colorless, Alcohol odor Solid, colorless to grayish, floral like odor Solid/liquid, yellow powder or rhomble powder, no odor Solid, sharp characteristic (strong) 1650 50 KL 4250 50 KL 1650 25 KG X 200 Bags Catalytic 25 Kgs X 200 Sachin Chemical Aarti Industry, Boisar. Chemtrade Overseas Pvt.Ltd, Sachin Chemicals and Urmi Chemicals, Mumbai Balagi Amine, Solapur, Multichem Mumbai Anand Enterprises Pune Anand Enterprises, Pune, Infiniun Pharma Chemical Pvt. Ltd. By Road 3-5 By Road 3-5 By Road By Road By Road By Road 3-5 3-5 3-5 3-5 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 24

2.7 Resource optimization/recycling and reuse envisaged in the project Total recycle water will be 179 CMD. To conserve the water, various recycle/ reuse schemes will be implemented. Most energy efficient technology is selected. 2.8 Availability of water its source, energy/power requirement and source 2.8.1 Water Requirement and Source Proposed fresh water requirement of the project for domestic and industrial activity during operation phase will be 643 CMD. The water will be supplied by MIDC. The details of water requirement with are given in Table 2-3 Table 2-3: Details of Raw water consumption Source Consumption (CMD) Loss (-) / Water reaction (+) (CMD) Effluent (CMD) Process including Floor, Rector washing 20 (+) 18 38 Cooling tower 470 (-) 418 52 Boiler 90 (-) 17 ( 70 Steam condensate for reuse) 03 Domestic 13 (-) 2.5 10.5 Gardening 50 (-) 50 00 Total 643 539.5 103.5 Recycle water 70 + 32 + 77 = 179 -- -- Net Fresh Water Requirement 464 -- -- Note: The steam condensate from boiler (70 CMD), RO permeate (77 CMD) and MEE condensate (32 CMD) will be recycled. Total 179 CMD water will be recycled to reduce fresh water requirement. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 25

2.8.2 Power Requirement Power requirement of proposed project will be made available through State Electricity Board. Power requirement of proposed plant is as below: Power requirement: 1000 KVA 01 no. of D. G. set of capacity 1000 KVA is proposed to meet emergency power requirement of the plant. 2.8.3 Fuel Requirement It is proposed to install 2 nos. of 6 TPH and 12 TPH boilers and 2 nos. of 10 Lac. Kcal/hr. and 6 Lac. Kcal/hr. thermopack will be required. Fuel required for proposed project will be around 50.2 T/day of coal. HSD will be used as fuel to run one DG set having capacity 1000 KVA. Requirement of HSD will be around 270 lit/hr. (as and when the power shortage occurs due to power failures). DG will be operated in case of emergency only. 2.9 Quantity of wastes to be generated (liquid and solid) and scheme for their management/disposal 2.9.1 Gaseous Emissions Details of gaseous emissions from Process and Flue gas are given in Table 2-4 Table 2-4: Details of emissions from process and flue gas S. No. Pollutant Source of Emission Emission rate Concentration in flue gas 1. SPM Boiler/DG 146 kg/h <150 mg/m 3 Details of stack mitigation measures are given in Table 2-5. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 26

Table 2-5: Details stacks along with their mitigation methods Attached to Boiler Thermopack DG Capacity 12 TPH 6 TPH 10 Lac. Kcal/hr. 6 Lac. Kcal/hr. 1000 KVA Fuel type Coal Coal HSD Fuel 43.2 T/Day 7.0 T/Day 6.5 KLD if run at full load MOC MS MS MS Shape Round Round Round Height m (above ground level) Mitigation Measures 40 m 30 m 6.3 m Stack,multicyclone followed by bag filter Stack, multicyclone followed by bag filter Stack 2.9.2 Liquid Effluent The quantity of effluent generated from proposed project will be 103.5 CMD out of which the trade effluent will be 93 CMD and domestic effluent will be 10.5 CMD. The process effluents and domestic sewage will be treated in Effluent treatment plant. ETP will be provided with required treatment facilities with the capacities of 125 CMD to treat the generated effluent. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 27

Proposed Treatment Scheme for Trade Effluent and Domestic Effluent Primary treatment - I: The system will be designed to treat 20 m 3 /day of waste water. Effluent will be sending to screen chamber, where coarse screen is placed to prevent coarse solids and debris from entering the tank. From Screen chamber effluent will overflow to Oil & Grease trap where floating oil & grease is removed from surface manually. The overflow from Oil and Grease trap enters the Collection cum Equalization Tank - I. The equalization tank is provided with acid & alkali dosing arrangement for ph neutralization & coarse bubble diffusers will be provided to mix the wastewater. This effluent will be pumped to Flash mixer where alum is dosed for coagulation. Flash mixer effluent will overflow to Flocculator where poly is dosed for better flocculation. Flocculator overflow to primary settling tank with hopper bottom tank provided. Suspended solids get settled at the bottom of settling tank & chemical sludge which is pumped to sludge collection tank and clear supernatant will overflow to Anaerobic Sludge blanket / Stirred Reactor (UASBR). Secondary (Anaerobic) treatment (UASBR): The system will be designed to treat 20 m 3 /day of waste water. Primary treated effluent shall enter the buffer tank. The effluent shall be overflow from the buffer tank for anaerobic treatment in the UASBR reactor. UASBR reactor consists of mainly feed distribution network at the bottom, sludge blanket at approx. mid height of reactor and the gas, liquid, solid separator at the top of the reactor. In UASBR process the bacteria responsible for digestion process are present in the form of sludge blanket. The bacteria grow and reside as bacterial flocs suspended in the Up flow effluent stream. The bacteria take upon organic content of wastewater to metabolize it and produce biogas and biomass. UASBR operates in the mesophillic range of temperature, i.e. 36 0 C 40 0 C. The ph inside the reactor is usually kept around 7.2 while proper ratio of volatile acid and alkalinity is maintained. Biogas is collected at the top of the reactor and burnt in flare stack. The anaerobically digested effluent is collected to holding tank and sent to (Aerobic) Bioreactor Tank for further treatment. Primary Treatment II: The system will be designed to treat 83.5 m 3 /day of waste water. Low COD and TDS streams from utilities and domestic effluent will be send to screen chamber, where coarse screen is placed to prevent coarse solids and debris from entering the tank. From Screen chamber effluent will overflow to Oil & Grease trap where floating oil & grease is removed from surface manually. Collected in the equalization PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 28

tank - II and air stripped. This effluent will then be pumped to the Flash Mixer where it will be dosed with alum for coagulation. This effluent will overflow into the settling tank where the solids will settle down and will be removed. Overflow of the settling tank will be mix with anaerobic treated effluent and it will be send to further treatment. Secondary (Aerobic) Treatment: The neutralized effluent will enter the bioreactor @ 103.5 (83.5 + 20) m 3 / day. In the bio reactor, dissolved organic material is degraded by the micro organisms present in the bio reactor. Oxygen required for the oxidation of organic matter will be provided by means of proposed diffuser aeration system which will mix the contents of the bioreactor also. The mixed liquor will overflow into Secondary Settling Tank (SST). In the secondary settling tank, solid-liquid separation takes place and solids i.e. biomass will settle at the bottom of the tank. Settled biomass will be recycled to the bio reactor for maintaining the MLVSS concentration by using proposed sludge recycle pumps and excess biomass will be wasted periodically to the sludge sump. Two stage treatments are proposed where the overflow from the 1 st stage clarifier will enter the 2 nd stage bioreactor where the non-degraded organics from the 1 st stage bioreactor will be treated. The clear overflow from the 2 nd stage Secondary Settling Tank will be collected in the intermediate tank. Tertiary Treatment: The clear effluent from the intermediate tank will be pumped by tertiary Feed pumps through the pressure sand filter (PSF) & activated carbon filters. The final treated effluent will be feed to Reverse Osmosis (RO). RO System Reverse Osmosis is at present a proven technology used to recover good quality water for process use. The outlet from ETP will be passed through RO where the dissolved solids are separated in the form of Reject & treated water free from dissolved solids (Permeate 77 CMD) is utilized for cooling tower and boiler feed. Reject of RO (26.5 CMD) shall be feed to the MEE to achieve Zero Liquid Discharge (ZLD) scheme. MEE salts generated (146 kg/day) will be send to CHWTSDF for disposal. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 29

Sludge Handling: Primary sludge and excess biomass from the secondary treatment will be collected in the sludge drying bed (SBD). The solid cake from the SDB will be sent for disposal to Hazardous waste disposal site. The filtrate from the SDB will be drained to the equalization tank. Trade and Domestic Effluent :To ETP Parameters Unit Design details and Performance Projection of ETP, RO and MEE Inlet to primary for anaerobic treatment ( High COD) Anaerobic Treated effluent Inlet to primary for aerobic treatment (Low COD) Flow m 3 /day 20 20 83.5 Anaerobic treated mixed with Low TDS & COD effluent 103.5 (20+83.5) ph ---- 6-7 6-7 6-7 6-7 BOD 3, 27 C mg/l 15000-20000 5000-6000 350-400 1200-1500 COD mg/l 35000-40000 12000-15000 800-1000 3000-3500 TSS mg/l 50-100 50-100 50-100 50-100 TDS mg/l 5000-6000 5000-6000 400-500 1200-1500 Parameters Unit Inlet to secondary treatment Outlet from secondary treatment Inlet to tertiary treatment Outlet from tertiary treatment Flow m 3 /day 103.5 103.5 103.5 103.5 ph ---- 6-7 6-7 6-7 6-7 BOD 3, 27 C mg/l 1200-1500 120-150 120-150 < 100 COD mg/l 3000-3500 300-350 300-350 < 250 TSS mg/l 50-100 50-100 50-100 < 100 TDS mg/l 1200-1500 1200-1500 1200-1500 1200-1500 From ETP : To RO Parameters Unit Inlet to RO Permeate Reject Flow m 3 /day 103.5 77 26.5 ph ---- 7-8 7-8 7-8 COD mg/l < 250 < 250 < 400 TDS mg/l 1200-1500 < 100 5000-5500 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 30

From RO : To MEE Parameters Unit Reject from RO Outlet from MEE Flow m 3 /day 26.5 ( 26.5 + 5.5 condensate from MEE) 32 ph ---- 6-7 6-7 BOD 3, 27 C mg/l 80-100 80-100 COD mg/l 200-250 < 100 TSS mg/l < 100 < 100 TDS mg/l 5000-5500 < 100 Treatment Scheme for Domestic Wastewater The sewage generated due to domestic activities will be treated in combined ETP. 2.9.3 Details of Hazardous wastes The types of Hazardous wastes generated from the project, method of disposal is shown in below table below Table 2-8: Details of Proposed Hazardous Solid waste along with the Category and disposal method S. No. Waste Name Unit Category Quantity Disposal Method Hazardous Waste Chemical Sludge from waste 1 water treatment T/A 34.3 20 2 MEE solids T/A 35.1 52 3 Distillation residue T/A 20.3 23 4 Spent Carbon from ETP T/A 35.3 35 5 Non-Hazardous Waste Discarded drums and containers Nos./M. 33.3 250 nos. 1 Boiler Ash T/D 3.5 E-waste CHWTSDF, Ranjangaon MPCB authorized party for reuse Send to brick manufacturer 1 Battery / e waste T/Yr. 0.2 sale to recycler PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 31

2.10 Schematic representations of the feasibility drawing which give information of EIA purpose. Project Identification what environmental impacts are normally associated with the type of project being proposed? Pre-feasibility Analysis Is the Project feasible from an environment point of view? (a) Project Design What negative environmental impacts could arise if the proposed project is implemented with proposed design? (b) Is there alternative design with less environmental impacts? Project Appraisal Have all the environmental concerns associated with the project been eliminated? Project Implementation What environmental concerns might arise at the implementation phase of the project? Preparation of an Environment Monitoring and Evaluation Plan (a) What environment monitoring indicators are required to ensure that the implementation of components of the project will be executed within environmentally Sound limits? ( Identify monitoring indicators ) (b) What is required to ensure that the recommended environmental control measures will be implemented and enforced? (c) (Prepare a comprehensive environment monitoring and management plan) Post EIA Monitoring and Environment Audit (a) Is the implementation of components of the project being executed in an environmentally sound manner? (b) Are all the recommended environmental control measures being implemented and enforced? Are there any environmental impacts that were earlier not anticipated when EIA was done? PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 32

3.0 SITE ANALYSIS 3.1 Connectivity M/s Clean Science Private Limited is located at Plot no. No.: D-25/1/1 MIDC, Kurkumbh, Tehsil Daund, District Pune, Maharashtra. The Site is 70.00 km from Pune City and 12.0 Km from nearest railway station (Daund). The land and infrastructure is made available by MIDC and the raw materials are easily available through easy transport via road connectivity. 3.2 Land Form, Land use and Land ownership Proposed unit is located in Notified Industrial Estate having plot area 30000SQM. The land is acquired by Clean Science Private Limited for establishing new manufacturing facility from MIDC on lease. 3.3 Topography The Geographical location of this industry is: Latitude - 18 24'11.06"N and Longitude- 74 31'26.16"E The activity of this project is in the midst of a study area, which is spread in Kurkumbh industrial area in district Pune. The town is mostly flat terrain, with hills rising 600 m (2,000 feet) to the south of the town near Kurkumbh. Daund is located on the southern bank of Bhīma River, a major river in Maharashtra. The river creates the Ujjani reservoir around 25 km (16 m) southeast of the town. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 33

Figure 3.1: Toposheet Showing Project site and 10Km of area PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 34

3.4 Existing land use pattern (agriculture, non-agriculture, forest, water bodies (including area under CRZ), shortest distances from the periphery of the project to periphery of the forests, national park, wild life sanctuary, eco sensitive areas, water bodies (distance from HFL of the river), CRZ. The proposed land for setting new unit is located in Notified Industrial Estate. The land is acquired by CSPL Industries. The proposed site is an undeveloped land which does not include agricultural, forestry, water bodies (including CRZ) etc. 3.5 Soil classification The basic type of soil found in the area varies from red, brown & black. The black type of soil is found in the eastern part. The fertility of the soil increases as it goes from red to black. 3.6 Climatic data from secondary sources The climate, in Daund area is characterized by hot summer and general dryness throughout the year except the south west monsoon season. The year may be divided into four seasons. The winter or cold season is from December to February, summer or hot season from March to May. The south west monsoon season is from June to September, while October and November constitute the post monsoon season. Climate Classification: Project site features a semiarid climate. Temperature: Annual maximum and minimum temperature in Kurkumbh ranges from max. 36 C and min. 16 C with the most comfortable time to visit in the winter October to February. May is the generally hottest month of the year with average temperature in between 38 to 22 deg. Cent. In cold season the area is sometimes affected by the cold waves over north India and the minimum temperature may drop to between 29 to 10 deg. Cent. The air is generally dry except during the south west monsoon season, when the relative humidity is high. Rainfall: Most of the rainfall occurs in the monsoon season from June to September. Average annual rainfall is 375 mm. Humidity: Annually relative humidity ranged from 65% 95% in winterand during summer season the humidity ranged from 35% 70%. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 35

3.7 Social Infrastructure Availability The basic amenities within the study area include primary schools, dispensaries, water supply, electric supply, public telephones, hotels, banks, post offices, petrol pumps, bus services, technical training institute and entertainment etc. 4.0 PLANNING IN BRIEF 4.1 Planning Concept Proposed plant activities will be started after getting statutory clearance from related authorities. The project will be completed within Six months. Further proposed project activities will take care of all the rules and regulation of statutory authority and provide the control measure and devices to achieve the standard norms. Kurkumbh MIDC provides many basic facilities like uninterrupted water supply, power and road network etc. the entire infrastructure, communication and manufacturing network will be manufactured after getting prior environmental clearance. This site is inside the campus of the MIDC and means safe transportation, less need of Utilities, less constructing buildings and roads, less fuel, less water with optimization of infrastructure. Government MIDC has provided all infrastructures like assured electrical power, continuous water supply with purification from water works like disinfection, the internal road network, external approach road, and networking with CHWSTDF (Common Hazardous Waste Storage Treatment and Disposal Facility), at Ranjangaon in vicinity established with support of MIDC and MPCB. 4.2 Land Use Planning The proposed project is in notified MIDC Industrial area, this is not a prime Agricultural Land. The land use is already as industrial. Thus there is no change in the status. This is flat land whereby cuttingfilling balances and there will be No/Low borrowing from nature. There will be no demolition works so debris will not be generated. The structure to be constructed is on a flat land. The total plot area is 30000m 2. 4.3 Assessment of Infrastructure Demand (Physical & Social) CSPL is proposing a Greenfield project for manufacturing of Mono Methyl Ether of Hydroquinone (MEHQ), Guaiacol, 4-Methoxy Acetophenone (4-MAP), Anisole and Butylated Hydroxy Anisole (BHA) & PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 36

byproducts which require full-fledged infrastructure; so there will be demand of physical infrastructure and social infrastructure. 4.4 Amenities/Facilities MIDC provides many basic facilities like uninterrupted water supply, Power and Road Network etc. This site is inside the campus of the MIDC and means safe transportation, less need of utilities, less constructing buildings and roads, less fuel, less water with optimization of infrastructure and networking with CHWSTDF (Common Hazardous Waste Storage Treatment and Disposal facility) at Ranjangaon in vicinity established with support of MIDC and MPCB 4.5 Population Projection Daund region has 382535 populations out of this 198269 male and 184266 female. And the density of population is 297 per square kilometer. It has a mixed population of Hindus, Muslims and Christians. The village has basically an agrarian economy and industrial workers and farming is the main occupation of the villagers. The local self-government vests with a Grampanchayat having an elected body headed by a Sarpanch. The literacy rate at present is approx. 74.12 % which is above the national average. In men the literacy rate is 79% and in females it is 69 %. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 37

5.0 PROPOSED INFRASTRUCTURE 5.1 Industrial area Industrial Area (Processing area) Utilities Cooling towers HSD unloading/storage area Boilers & Thermopac Ware house Coal Shed Non- Processing Area Administrative Buildings Security cabins Workers restroom Vehicle Shed Water reservoirs Temporary storage sites Works block etc 5.2 Residential Area In Clean Science Pvt. Ltd. there is no any residential area has been proposed. 5.3 Green Belt The project is built on an MIDC plot with plot area of 30000 sq. m. and green belt area 9900 sq. m. Green belt will be developed at proposed project site and details will be provided in EIA report. 5.4 Social Infrastructure The basic amenities within the study area include primary schools, dispensaries, water supply, electric supply, public telephones, hotels, banks, post offices, petrol pumps, bus services, technical training institute and entertainment etc. 5.5 Connectivity The proposed project is in MIDC Kurkumbh and well connected by road, rail and air ways. The site is 70 km from Pune city and 12 km. from Daund Railway station. The land and infrastructure is made available by MIDC and the raw materials are easily available through easy transport via road connectivity. Proposed project site is 75 km away from Pune Airport. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 38

5.6 Drinking Water Management The source of water supply is from MIDC Kurkumbh. The water requirement is about 13 m 3 /day for Domestic purpose. The source of water is already availability from existing water works of MIDC and the same is adequate and satisfactory. All surrounding villages are provided with drinking water from wells or Government Water Supply Schemes. Hence CSPL do not encroach upon their supply. 5.7 Sewage System The process effluents and domestic sewage will be treated in Effluent treatment plant. ETP will be provided with required treatment facilities with the capacities of 125 CMD to treat the generated effluent. 5.8 Industrial Water Management Water requirement is fulfilled through MIDC. Total water required for the proposed project will be 643 CMD out of which 179 CMD water will be recycled. From 2 nd day onward the total water requirement will be 464 CMD. Storm water drain compatible with the local hydrological pattern of the area is provided to carry - off any run - off or storm water from the premises. To compensate and mitigate impact on ground water availability in the area a comprehensive rain water recharge scheme will be developed. 5.9 Solid Waste Management Hazardous solid waste generated from the process will be collected, stored, transported and send to CHWTSDF, Ranjangaon as per Hazardous waste (Management, Handling and Transboundry Movement) Rules 2008. 5.10 Power Requirement & Supply / source Power requirement of proposed project will be made available through State Electricity Board. Power requirement of proposed plant is as below: Power requirement: 1000 KVA 01 no. of D. G. set of capacity 1000 KVA is proposed to meet emergency power requirement of the plant. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 39

6.0 REHABILITATION AND RESETTLEMENT (R & R) PLAN 6.1 Policy to be adopted (Central/State) in respect of the project affected persons including home oustees, land oustees and landless. Rehabilitation and Resettlement (R&R) plan is not applicable for the proposed project. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 40

7.0 PROJECT SCHEDULE & COST ESTIMATES 7.1 Likely date of start of construction and likely date of completion The construction is likely to start after getting Environmental Clearance and NOC/CTE from the authorized committee. Application for ToR December 2017 Finalization of EIA March 2018 SEAC meeting to finalize ToR January 2018 Application for EC March 2018 Environment Monitoring November 2017 December 2017 SEAC meeting for EC April 2018 January 2018 Collection of data from FAEs January 2018 February 2018 Consent to establish January 2018 Preparation of draft EIA February 2018 Consent to operate June 2018 7.2 Estimated project cost along with analysis in terms of economic viability of the project The total investment envisaged is Rs. 70.0 Crore with the break-up as given in table no 7.1 below S. No. Fixed Assets Table 7-1: Cost Break Up Proposed Amount (Rs in Lakhs) 1 Land 96.00 2 Building/Premises 1500.00 3 Plant, Machinery/Equipment & EMP 5304.00 4 Furniture & Fixture 50.00 5 Any other movable/ immovable fixed assets 50.00 Cost of total fixed assets 7000.00 PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 41

8.0 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS) Proposed activity will provide benefits to the local people in terms of financial and social welfare. Local people will get direct financial benefit by way of employment. Local people will get some contract of supply and services to get indirect income. Company will contribute in improving education and health facilities in nearby area. PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 42

Plant Layout PFR for M/s. Clean Science Private Limited. Prepared by Goldfinch Engineering Systems Pvt. Ltd. Page 43