PRE - FEASIBILITY REPORT

PRE - FEASIBILITY REPORT FOR PROPOSED RESIN MANUFACTURING UNIT BY SURVEY NO:- 173/1, VILLAGE PADANA, PADANA BHIMASAR ROAD, TALUKA GANDHIDHAM, DISTRICT KUTCH, GUJARAT OF M/S. MAPLE PANELS PVT. LTD.

SUMMARY M/s. Maple Panels Pvt. Ltd is planning to set up the resin manufacturing unit at Survey No. 173/1, village Padana, Padana - Bhimasar Road, Taluka Gandhidham, District Kutch, Gujarat. PROJECT COST The total project cost for the proposed resin manufacturing project would be around Rs. 13.5 crores. Total capital cost of pollution control measures will be Rs. 2.05 crores & recurring cost per annum will be 10 lacs. DETAILS OF PRODUCTS Details of existing and proposed products are given in following table. LIST OF PRODUCTS SR. NO PRODUCT QUANTITY MT/M 1 Urea Formaldehyde Resin 4000 2 Melamine Formaldehyde Resin 2000 3 Formalin 5000 4 Phenol Formaldehyde 500 5 Wax 500 TOTAL 12,000 REQUIREMENTS FOR THE PROJECT LAND No new land will be acquired for the proposed project. The proposed project will come in available open space in existing particle board unit. Out of the total land area (i.e. 41,205 m 2 ) around 1636.4 m 2 open land area will be utilized for the proposed Resin manufacturing unit. WATER Total water requirement for the proposed project would be estimated as 129 KLD, which would be sourced from Gujarat Water Infrastructure Limited (GWIL). ELECTRICAL ENERGY Total power requirement for the proposed project will be 500 KW will be sourced from UGVCL (Uttar Gujarat Vij Company Limited). During emergency purpose D. G. Set of 400 KVA will be utilized. MANPOWER For proposed project total 30 personnel will be required. SOURCES OF AIR POLLUTION AND CONTROL MEASURES EMISSIONS FROM COMBUSTION OF FOSSIL FUELS FROM STATIONARY OR MOBILE SOURCES SR. 1. 2. STACK ATTACHED TO Steam Boiler (2 TPH) X 2 Nos. Thermopack (10 Lac Kcal/hr) FUEL USED Coal/ Agro waste / Baggase 10 MT/Day STACK HEIGHT 30 meter 30 meter POLLUTION CONTROL SYSTEM Bag Filter Bag filter FINAL CONCENTRATI ON SPM 150 mg/nm 3 SO 2 100 ppm NO X 50 ppm SPM 150 mg/nm 3 SO 2 100 ppm

SR. STACK ATTACHED TO FUEL USED STACK HEIGHT POLLUTION CONTROL SYSTEM FINAL CONCENTRATI ON NO X 50 ppm 3. D.G Set (Stand By) 400 KVA HSD/LDO 35 Lit/Hr 07 meter Acoustic Enclosures SPM 150 mg/nm 3 SO 2 100 ppm NO X 50 ppm WASTE WATER GENERATION AND IT S TREATMENT: Total wastewater i.e. 30 KLD will be generated from the proposed Resin Manufacturing project, from that 1 KLD sewage wastewater shall be generated from domestic use which will be disposed off through septic tank/soak pit system, remaining 29 KLD industrial effluent shall be treated in proposed ETP after that it will be evaporated through evaporator and condensate water will be reused. Domestic wastewater: Total 01 KLD domestic wastewater will be disposed off through Septic tank/soak pit system. NOISE POLLUTION AND CONTROL MEASURES: From the proposed manufacturing unit noise pollution will be generated which will be controlled by adopting different types of noise pollution control measures. Main sources of the noise pollution - machineries, electric motors, boiler, D. G. set and TFH, etc. Following noise control measures to be adopted in the proposed manufacturing project, Encasement of noise generating equipment. Greenbelt will be developed all around the plant boundary to act as noise attenuator. In addition personnel, working near high noise level generating sources, will be provided with ear muffs. Proper and suitable acoustic barrier will also be provided around, areas generating high noise. Effective preventive maintenance and vibration measurement of all rotating equipment will help in the improvement of plant life and also noise reduction. SOLID WASTE GENERATION AND ITS DISPOSAL METHOD The sources of solid wastes, generation and its management are as given in the following table. SR. CATEGORY METHOD OF STORAGE AND NAME OF THE WASTE QUANTITY DISPOSAL 1. Used Oil 5.1 2. Discarded Containers/Barrels/plastic 33.3 3. ETP Sludge 29.2 4. Salt from Evaporator - 5. Fly ash - 3.0 Lit/Year 1500 Nos./Year 27.0 MT/Month 10 MT/Month 15 MT/Month Collection, storage and reuse as lubricants in the machineries within the premises only or send to authorized reprocessors. Collection, storage and send to authorized recycler after decontamination. Collection, storage and transport to TSDF site. Collection, storage and transport to TSDF site. Collection, storage and send to brick manufacturers. GREEN BELT DEVELOPMENT Company has proposed 33% of total land area for green belt development approx 13,597 m 2 land area.

INDEX CHAPTER 1 Introduction of the project 2 Project description 3 Site analysis 4 Planning brief 5 Proposed infrastructure CONTENT 6 Rehabilitation and resettlement (R & R) plan 7 Project schedule & cost estimates 8 Analysis of proposal

INTDOUCTION OF THE PROJECT CHAPTER-1 1.1 IDENTIFICATION OF PROJECT AND PROJECT PROPONENT M/s. Maple Panels Pvt. Ltd is proposing to manufacture Urea Formaldehyde Resin, Melamine Formaldehyde Resin, Formalin, Phenol Formaldehyde Resin and Wax as products at Survey No. 173/1, village Padana, Padana-Bhimasar Road, Taluka Gandhidham, District Kutch, Gujarat. 1.2 PROMOTERS BACKGROUND Main promoters of the project are Mr. Pradeep Lohia (B.E.) 40 years of experience business and Mr. Ankur Agarwal (MBA) 5 years of experience in business. 1.3 BRIEF DESCRIPTION OF NATURE OF THE PROJECT M/s. Maple Panels Pvt. Ltd is planning to set up the resin manufacturing unit at Survey No. 173/1, village Padana, Padana-Bhimasar Road, Taluka Gandhidham, District Kutch, Gujarat. LIST OF PRODUCTS SR. NO PRODUCT QUANTITY MT/M 1 Urea Formaldehyde Resin 4000 2 Melamine Formaldehyde Resin 2000 3 Formalin 5000 4 Phenol Formaldehyde 500 5 Wax 500 TOTAL 12,000 1.4 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE COUNTRY AND OR REGION. Industrial development in India has increased economic growth and improved living standards of people. Formaldehyde it is a colorless gas at room temperature and is soluble in water, alcohols and other polar solvents. Formaldehyde is usually produced close to the point of consumption since it is fairly easy to make, is costly to transport and can develop problems associated with stability during transport. Demand for these markets is greatly influenced by general economic conditions. As a result, demand for formaldehyde largely follows the patterns of the leading world economies. Formaldehyde resins are used predominantly in the wood products industry as adhesives. 1.5 DEMANDS-SUPPLY GAP As stated earlier the major end users of laminated sheets/ particle board are the building construction sector. Thus the demand for laminated sheets/ particle board is related to the expansion and growth of the building construction sector. The future demand for laminated sheets/ particle board is related to housing construction and the furniture industry whose future growth is related to the growth rate of the economy and urbanization. The rate of urbanization in the country is currently above 5 percent and the economy is growing on average at about 10%. In view of this real performance, a conservative assumption that demand for laminated sheet/ particle board will grow by 3 percent is considered in projecting the future demand. This indicates the presence of huge demand in the future and hence affirms the importance of establishing a plant that manufactures particle board. 1.6 EMPLOYMENT GENERATION For proposed project additional 30 personnel will be required. 1

PROJECT DESCRIPTION CHAPTER-2 2.1 TYPE OF PROJECT M/s. Maple Panels Pvt. Ltd is planning to set up the resin manufacturing unit at Survey No. 173/1, village Padana, Padana-Bhimasar Road, Taluka Gandhidham, District Kutch, Gujarat. It is for resin manufacturing unit which requires obtaining prior environmental clearance before establishing from MoEF&CC. Industrial development in India has increased economic growth and improved living standards of people. These growths are achieved through industrialization, infrastructure development. The industrialization has played a major role in development of the country. This industrialization is also has many other benefits. Although the industrial development leads to rapid consumption of natural resources, fuel etc. in day to day operational activity. To control the pollutions from industrial activity, government has framed regulations which are governed by Ministry of Environment and Forest in India. 2.2 LOCATION M/s. Maple Panels Pvt. Ltd is planning to set up the resin manufacturing unit at Survey No. 173/1, village- Padana, Padana Bhimasar Road, Taluka-Gandhidham, District- Kutch, Gujarat. Total plot area of the project is 41,205 m 2 from which around 1,636 m 2 will be required for this project. A map showing project site is given in following figure-1 & a detailed map of the project site & surrounding is showing in following figure. Latitude - 23 09'.46.41" North Longitude - 70 10'38.52" East LOCATION MAP 2

2.3 SIZE OR MAGNITUDE OF OPERATION M/s. Maple Panels Pvt. Ltd is planning to set up the resin manufacturing unit for 12,000 MT/M resin products. LIST OF PRODUCTS SR. NO PRODUCT QUANTITY MT/M 1 Urea Formaldehyde Resin 4000 2 Melamine Formaldehyde Resin 2000 3 Formalin 5000 4 Phenol Formaldehyde 500 5 Wax 500 TOTAL 12,000 2.4 PROCESS DESCRIPTION MANUFACTURING PROCESS: DETAILS OF MANUFACTURING PROCESSES 1) UREA FORMALDEHYDE RESIN: In reaction vessel urea (Technical Grade), formaldehyde and caustic are taken in desired quantity, then after it will stir and heat up to 70ºC and maintain temperature up to 1 hour. Reflux is done for 30 minutes. To control the temperature, the mixture is cooled by circulating water. ph will be adjusted up to desirable by adding Caustic. The reaction involves condensation between the nucleophilic Nitrogen of Urea with the electrophilic carbonyl Carbon of Formaldehyde. A branched copolymer is formed. Urea Formaldehyde Resin will be ready for Packing. CHEMICAL REACTION FLOW DIAGRAM Urea (T.G.) 25 Kg Formaldehyde 74.8 Kg REACTOR Condenser Caustic Soda 0.1 Kg Acetic Acid 0.1 Kg NEUTRALIZATION UREA FORMALDEHYDE RESIN 100 KG 3

2) MELAMINE FORMALDEHYDE RESIN The formaldehyde is charged into reaction vessel and raises it s up to 8.5 to 9.0 by adding caustic solution (NaOH Solution). Then add melamine into vessel thoroughly and maintained the ph upto 8.5 to 9.0. And start heating at 80 C to 90 C for melting of Melamine. After 15 to 20 minutes, check the ph of mixture and stop heating. Start reflux process for 40 to 50 minutes. In between the reflux process observe tolerance point. Once the required tolerance achieved, start immediate cooling. Finally, check viscosity, tolerance, ph, turbidity etc. to obtain the desired product property. CHEMICAL REACTION FLOW DIAGRAM Melamine 35.6 Kg Formaldehyde 64.2 Kg REACTOR Condenser Caustic Soda 0.2 Kg NEUTRALIZATION MELAMINE FORMALDEHYDE RESIN 100 KG 3) PHENOL FORMALDEHYDE RESIN Take required quantity of Phenol and Formaldehyde in the reactor. Start steam heating until the temperature reaches up to 60 C. The reaction being exothermic will liberate heat and temperature will rise without any further heating. Reflux process will be start at this point to achieve required water tolerance. After achieving required water tolerance, start cooling to decrease temperature up to 60 C. Once the temperature reach at 60 C stop cooling and start heating for distillation process for required quantity of resin. After achieving required amount of resins start cooling to obtain final product. Final product will be checked for the properties like Resin Viscosity, Resin ph, Resin gel time etc. The upper layer is of water and the bottom layer contains the resin. The product containing 70% solid is drained out from the reaction vessel and stored in a storage tank. 4

CHEMICAL REACTION FLOW DIAGRAM Condenser Phenol 44.0 Kg Formaldehyde 58.0 Kg REACTOR Caustic Soda 0.5 Kg Methanol 11.0 Kg NEUTRALIZATION Waste water to ETP 13.50 Kg PHENOL FORMALDEHYDE RESIN 4) FORMALIN (FORMALDEHYDE) The methanol in the measuring storage tank is pumped up to an elevated tank by a methanol pump. After being controlled by measuring, the methanol coming out from the elevated tank flows into an evaporator for vaporization of which the temperature is controlled within 44 ~ 47 0 C and the liquid level is controlled as 50%, then the vaporized methanol gets into a super heater. The heat for the vaporization of methanol is provided by the 70 0 C circulating fluid in the 1 st formaldehyde absorber. The air is filtered by a filter before being delivered to the evaporator by a blower. It mixes with the methanol in the evaporator and enters into then super heater together. The air flow is regulated by the blower through frequency conversion to control the flow ratio of air to methanol (A/M=1.8 ~1.95). When the pressure gets stable, the vapour (0.3 MPa) gets into a mist eliminator for dehumidification through the pipeline before entering into the superheat. The flow ratio of air to methanol shall be controlled at desired level. In the formaldehyde production technique using silver as catalysis, the water vapour is an inert gas which does not participate in chemical reactions. The added water vapour changes the explosive range of the methanol and air, the production of formaldehyde thereby becomes far from the explosive area and stays safe and reliable. After the flow 5

rates are regulated and proportioned, the methanol, air and water vapour enter into the super heater and the superheating temperature shall be controlled at 200 0 C. Then, these materials enter into a reactor. In the reactor, under the catalysis of silver at 650 0 C, the methanol is dehydrated and oxidized, generating Formaldehyde. Dehydration reaction is an endothermic reaction and oxidation reaction is an exothermic reaction, but the heat release is more than that can adsorbed, therefore the reaction system is a state of heat energy surplus. The water vapour is not involved in reactions but it can absorb a lot of heat of reaction, maintaining the temperature at 650 0 C. The 650 0 C reaction gas leaves the reaction and gets into heat exchanger. For the heat exchanger, the medium is water. The outlet temperature of heat exchanger is 160 0 C. The water absorbs heat, forming the water vapour of 0.35 MPa which will be used to arranging the raw materials for production in the super heater after its pressure stabilized. The generated gases of about 160 0 C enter into 1 st and 2 nd formaldehyde absorber in proper order and get absorbed by the cooled circulating fluid through spraying. The temperature of the circulating fluid at the bottom of 1 st absorber shall be control at 70 0 C and fluid is pumped to the evaporator by circulating pump to supply the heat for the evaporation of methanol. In the 1 st absorber, the concentration shall be controlled as 37%, and temperature of the top shall be controlled at 45 0 C to 50 0 C. The circulating fluid is also a composition of the formaldehyde product by this technique. The temperature of the top of 2 nd absorber shall be controlled at 30 0 C to 35 0 C and keep adding water from top to control the release of formaldehyde. CHEMICAL REACTION CH 3 OH CH 2 O + H 2-20Kcal -------1 CH 3 OH + ½ O 2 CH 2 O + H 2 O + 38 Kcal ------2 1-2=18Kcal 6

FLOW DIAGRAM Excess Energy Water Methanol Energy Generation Gases Gases l Silver Catalyst Second Column Scrubber Start up Heat Air Formaldehyde 37% Formaldehyde 0.2-0.5% 5) WAX In reaction vessel paraffin wax, Borax powder, Stearic Acid and aqueous ammonia are mixed. Reaction mass are continuous stirring and heated to prepare the product paraffin wax emulsion. Water will be added as to maintain solid content of emulsion. 7

FLOW DIAGRAM Paraffin Wax 43.8 kg Borax powder 1.5 kg Stearic Acid 5.8 kg REACTION VESSEL Aqueous Ammonia 1.5 kg Water 47.4 Kg PARAFFIN WAX EMULSION 100 KG 2.5 RAW MATERIALS REQUIREMENT WITH THEIR SOURCE AND TRANSPORATATION Details of Raw material consumption and Mode of Transportation are given in following table. LIST OF RAW MATERIALS SR.NO NAME OF RAW MATERIAL QUANTITY MTPM TYPE OF STORAGE MODE OF TRANSPORT 1. Phenol 220 MS Tank By Road 2. Formaldehyde 7016 MS Tank By Road 3. Caustic Soda 10.5 Bags By Road 4. Formic Acid 400 MS Tank By Road 5. Methanol 455 MS Tank By Road 6. Melamine 712 Bags By Road 7. Urea (T.G.) 1000 Bags By Road 8. Acetic Acid 4 Drum By Road 9. Paraffin Wax 219 Drum By Road 10. Borax powder 12.5 Bags By Road 11. Stearic Acid 54 MS Tank By Road 12. Aqueous Ammonia 12.5 MS Tank By Road 2.6 RESOURCE OPTIMIZATION / RECYCLING AND REUSE IN THE PROJECT Treated effluent (condensate water) will be reused in utilities and washing purpose which will reduce in fresh water intake quantity. 2.7 AVAILABILITY OF WATER ITS SOURCE, ENERGY / POWER REQUIREMENT AND SOURCE WATER Total water requirement for the proposed expansion project would be estimated as 129 KLD, which would be sourced from Gujarat Water Infrastructure Pvt. Ltd. POWER Total power requirement for the proposed project will be 500 KW. During emergency purpose D.G. Set of 8

400 KVA will be utilized. Power supply shall be full-filled by UGVCL (Uttar Gujarat Vij Company Limited). 2.7.1 WATER REQUIREMENT AND WASTE WATER GENERATION Total wastewater i.e. 30 KLD will be generated from the proposed Resin Manufacturing project, from that 1 KLD sewage wastewater shall be generated from domestic uses which would be disposed off through septic tank/soak pit system, remaining 29 KLD industrial effluent shall be treated in proposed ETP after that it will be evaporated through evaporator. Condensate water from evaporator will be reused in utilities and washing. 2.7.2 FUEL REQUIREMENT SR. DAILY FUEL SOURCE & MODE OF FUEL CONSUMPTION TRANSPORTATION Coal/ Waste wood/ From local market and transport 1. 10 MT/Day Baggase through truck 2. HSD/LDO 35 Lit/Hr From nearby petrol pump 2.7.3 AIR POLLUTION EMISSIONS FROM COMBUSTION OF FOSSIL FUELS FROM STATIONARY OR MOBILE SOURCES SR. 1. 2. 3. STACK ATTACHED TO FUEL USED Steam Boiler (2 TPH) X 2 Nos. Coal/ Waste wood/ Baggase Thermopack 10 MT/Day (10 Lac Kcal/hr) D.G Set (Stand By) 400 KVA HSD/LDO 35 Lit/Hr STACK HEIGHT 30 meter 30 meter 07 meter POLLUTION CONTROL SYSTEM Bag Filter Bag filter Acoustic Enclosures FINAL CONCENTRATIO N SPM 150 mg/nm 3 SO 2 100 ppm NO X 50 ppm SPM 150 mg/nm 3 SO 2 100 ppm NO X 50 ppm SPM 150 mg/nm 3 SO 2 100 ppm NO X 50 ppm 2.7.5 SOLID WASTE GENERATION AND THEIR DISPOSAL The sources of solid wastes, generation and its management are as given in the following table. SR. NAME OF THE WASTE CATEGORY 1. Used Oil 5.1 2. Discarded Containers/Barrels/plastic 33.3 3. ETP Sludge 29.2 4. Salt from Evaporator - 5. Fly ash - QUANTITY 3.0 Lit/Year 1500 Nos./Year 27.0 MT/Month 10 MT/Month 15 MT/Month METHOD OF STORAGE AND DISPOSAL Collection, storage and reuse as lubricants in the machineries within the premises only or send to authorized reprocessors. Collection, storage and send to authorized recycler after decontamination. Collection, storage and transport to TSDF site. Collection, storage and transport to TSDF site. Collection, storage and send to brick manufacturers. 9

SITE ANALYSIS CHAPTER-3 3.1 CONNECTIVITY 3.1.1 RAIL The nearest railway station is Gandhidham Railway station, which is around 10.6 km in South South West direction from the project site. 3.1.2 ROAD The site is well connected by road network to all the key places. The major highway passing near the project site is NH-8 -A which is around 2.4 km North direction from the project site and SH-6 around 1.7 km in south east direction. 3.1.3 AIR The nearest airport from the project site is Kandla Airport. The distance of airport from project site is around 9.42 km in South West direction. 3.1.4 COMMUNICATION Proposed project site is within existing company premises which is already well connected with telephone, telefax etc. all the communications facilities are well developed in the area. 3.2 TOPOGRAPHY Topography of the land is plane. 3.3 EXISTING LAND USE PATTERN There is no Forest, National park; Wild life sanctuary within a radius of 10 km. Details of existing land use is given in the following table: DETAILS OF EXISTING LAND USE SR. PARTICULAR NAME & ITS DISTANCE 1. Nearest National Highway NH-8 A at around 1.9 km 2. Nearest city Gandhidham city 10.5 km 3. Nearest River Gulf of Kutch at around 24.5km 4. Nearest Railway station Gandhidham Railway Station 10.6 km 5. National park/reserve Forest, Biosphere, etc. None within 20 km 3.4 EXISTING SOCIAL STRUCTURE Project site is located at a distance of around 10.5 km from Gandhidham city. All the infrastructures are available within city like Schools, Hospitals & community facilities. 10

PLANNING BRIEF CHAPTER 4 4.1 PLANNING CONCEPT Type of industries: Laminated sheets, Particle board, etc is made from Phenol Formaldehyde Resin, Melamine Formaldehyde Resin, Urea formaldehyde Resin and different type of resins which are highly shock absorbent, resistant to abrasion, excellent impact resistance, good dimensional stability, superior machinability, non conductive, heat resistant, stain resistant and cost effective. They are resistant to solvents low absorption to humidity and water. Due to these properties, the laminated sheets prepared from these resins have huge demand in market in terms of telephone castings, electric insulators, transformer tubes, and switch gear, used to surface walls, cabinets and counters and to make decorative laminated panels, household crockery such as glasses, cups, bowls and plates. 4.2 LAND USE PLANNING The Plant General Layout has been planned considering production facilities, auxiliary and ancillary facilities and plant utilities & services. The total plot area is 41,205 sq. m. Land use shall be as build up area of buildings, Storage facility, Roads, Greenbelt, open land etc., these kinds of land use will be there. 4.3 AMENTIES / FACILITIES Adequate storage facility for Chemicals, machinery spares and consumables shall be provided. A small mechanical and electrical/ instrument workshop facilities for repairs and maintenance shall be provided. Time and security offices shall be provided in the plant. To avoid fire hazard, internal fire hydrants system in all major plant unit will be provided. 11

PROPOSED INFRASTRUCTURE CHAPTER 5 5.1 INDUSTRIAL AREA The company has already acquired land area of 41,205 m 2 in which company will expand their production capacity. 5.2 GREEN BELT The main objective of the green belt is to provide a barrier between the source of pollution and the surrounding areas. The green belt helps to capture the fugitive emission and to attenuate the noise generated apart from improving the aesthetics. Development of green belt and other forms of greenery shall also prevent soil erosion and washing away of topsoil besides helping in stabilizing the functional ecosystem and further to make the climate more conducive and to restore water balance. The company has green belt area with Lawn, plants and flowers spread across about 33% of the total area. Green belt shall be developed at plant boundary, road side, around offices & buildings and Stretch of open land. The selection of tree species suitable for plantation at the industry are governed by guiding factors as stated below: The trees should be tolerant to air pollutants present in the area The trees should be able to grow and thrive on soil of the area, be evergreen, inhabitant, having minimum of leaf fall. The trees should be tall in peripheral curtain plantation and with large and spreading canopy in primary and secondary attenuation zone. The trees should posses extensive foliar area to provide maximum impinging surface for continued efficient adsorption and absorption of pollutants. The trees should be fast growing and indigenous and should maintain ecological, land and hydrological balance of the region. It is also recommended to plant few trees, which are sensitive to air pollution, as air pollution indicator. It is also recommended to carry out extensive plantation within premises. Keeping in view the climatic conditions, status of soils and vegetation types in and around the project area the species shall be selected for proposed green belt development. 5.3 SOCIAL INFRASTRUCTURE Drinking water facility, Canteen, proper sanitation, etc. will be provided to the workers working in plant. 5.4 CONNECTIVITY As discussed earlier, proposed location of the plant is already well connected with the network of road & rail. So there is no need to construct any new road or rail for the transportation. 5.5 WASTE WATER MANGAMENT Total wastewater i.e. 30 KLD will be generated from the proposed Resin Manufacturing project, from that 1 KLD sewage wastewater shall be generated from domestic uses which would be disposed off through septic tank/soak pit system, remaining 29 KLD industrial effluent shall be treated in proposed ETP after that it will be evaporated through evaporator. Condensate water from evaporator will be reused in utilities and washing. 12

5.7 INDUSTRIAL SOLID WASTE MANAGEMENT From the proposed project activity there shall be mainly Spent/Used Oil, ETP Sludge and Discarded containers. DETAILS OF SOLID & HAZARDOUS WASTE GENERATION DURING OPERATION SR. NAME OF THE WASTE CATEGORY 1. Used Oil 5.1 2. Discarded Containers/Barrels/plastic 33.3 3. ETP Sludge 29.2 4. Salt from Evaporator - 5. Fly ash - QUANTITY 3.0 Lit/Year 1500 Nos./Year 27.0 MT/Month 10 MT/Month 15 MT/Month METHOD OF STORAGE AND DISPOSAL Collection, storage and reuse as lubricants in the machineries within the premises only or send to authorized re-processors. Collection, storage and send to authorized recycler after decontamination. Collection, storage and transport to TSDF site. Collection, storage and transport to TSDF site. Collection, storage and send to brick manufacturers. 13

REHABILITATION AND RESETTLEMENT (R & R) PLAN CHAPTER 6 The project is located on private land, which is already acquired and there is no habitat. So the project proposal does not involve any Rehabilitation & Resettlement. 14

CHAPTER 7 PROJECT SCHEDULE & COST ESTIMATES 7.1 TIME SCHEDULE FOR THE PROJECT The implementation of the project will involve major activities like preparation of specification / drawings, issue of tenders, receipt of quotations, scrutiny of tenders, placing of orders, civil & structural construction, delivery & erection of equipment, test trial runs of various items of equipment and commissioning of the plant & equipment and completion of the project will take about 6 months after the necessary clearances are available, and the funding for the project has been tied up. 7.2 ESTIMATED PROJECT COST The total cost of the proposed project would be around Rs. 13.5 crores. Total capital cost of pollution control measures will be Rs. 2.05 Crore. 7.3 BUDGETORY PROVISIONS FOR EMP Adequate budgetary provisions have been made by the management for execution of environmental management plans. The details of capital and recurring (per annum) budget earmarked for pollution control / monitoring equipment; operation and maintenance of pollution control facilities, for greenbelt development and maintenance. COST OF ENVIRONMENTAL PROTECTION MEASURES SR. PARTICULATES RS. IN LACS 1. Capital Expenditure 205 2. Recurring expenditure on environmental management cell and 10 on pollution control systems per annum. 15

CHAPTER 8 ANALYSIS OF PROPOSAL 8.1 FINANCIAL AND SOCIAL BENEFITS The capital cost of the proposed Resin Manufacturing project is estimated at about Rs. 1350 lacs for the installation of plants & machinery along with required auxiliary and balancing facilities for the production capacity of 12,000 MT/Month of PF Resin, MF Resin, UF Resin, Formalin and Wax. For the coming of this project surrounding area will get developed due to this project and through the Corporate Social Responsibility (CSR) activities, socio-economic status of the region will also get developed. 16