Pre - Feasibility Report

PRE - FEASIBILITY REPORT

FOR

PROPOSED 35 KLPD MOLASSES BASED DISTILLERY PLANT

M/S. SHREE MAROLI VIBHAG KHAND UDYOG SAHAKARI MANDLI LTD. SURVEY NO.: 71, 72 & 80 AT-KOLASARA (KALYAN NAGAR) P.O- MAROLI BAZAR, TALUKA JALALPORE, DISTRICT NAVSARI-396436 GUJARAT

SUMMARY

M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd is an existing sugar mill located, at Survey No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O- Maroli Bazar, Taluka Jalalpore, District Navsari, Gujarat. Capacity of the existing Sugar Industry is 3000 TCD producing 11200 MT/Month of White Crystal Sugar. Now Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd has proposed 35 KLPD Molasses based distillery unit within existing company premises.

PROJECT COST The total cost of the project will be around Rs. 30.0 crores. Total capital cost of pollution control measures will be Rs. 3.0 crores & recurring cost per annum will be 1.0 crores.

DETAILS OF PRODUCTS Details of existing and proposed products are given in following table.

LIST OF EXISTING AND PROPOSED PRODUCTS AND PRODUCTION CAPACITY

SR. EXISTING ADDITIONAL NAME OF THE PRODUCTS TOTAL NO. QUANTITY QUANTITY (A) PRODUCTS 1 White Crystal Sugar 11200 MT/Month -- 11200 MT/Month Captive Power Plant (In 2 5.85 Mw/Hr. -- 5.85 Mw/Hr. House During Crushing Season) Rectified Spirit/Anhydrous 3 -- 35 KLPD 35 KLPD Alcohol (B) BY PRODUCTS 4 Molasses 5,200 MT/Month -- 5,200 MT/Month 5 Bagasse 33,500 MT/Month -- 33,500 MT/Month 6 Press Mud 4,200 MT/Month -- 4,200 MT/Month 7 Bio Compost 4,200 MT/Month -- 4,200 MT/Month

REQUIREMENTS FOR THE PROJECT

LAND No new land will be acquired for the proposed project. Out of total land area (i.e. 1,53,262 m2) around 8,000 m 2 open land area will be utilized for the proposed distillery unit.

WATER For the proposed project additional 506 m3/Day water will be required. Existing water required of the sugar plant is 428.7m3/Day, after proposed project total water required will be 934.7m3/Day. Source of water for existing unit is Borewell/ Canal and for the proposed distillery unit surface water (i.e canal water) will be utilized.

ELECTRICAL ENERGY For proposed project additional power requirement will be 400 KW/Hr. Existing connected Power load is 299.10 KWH/MT. Power supply shall be full-filled by Dakshin Gujarat Vij Company Limited.

MANPOWER At present, 237 personnel are working in the sugar industry. For proposed project additional 24 personnel will be employed who will come from local area. Total manpower after proposed project will be 261 personnel.

FUEL For the proposed project, energy requirement will be met from existing boiler (2 Nos.) having capacity of 50 and 30 TPH, for the proposed project Baggase (1.9 MT/Hr) will be used as fuel in existing boiler.

SOURCES OF AIR POLLUTION AND CONTROL MEASURES

EMISSIONS FROM COMBUSTION OF FOSSIL FUELS FROM STATIONARY OR MOBILE SOURCES

Sr. Stack Height Air Pollution Control Stack Attached To Parameter No. In Meter Devices EXISTING PM < 150 Mg/Nm3 Boiler No. 1 Ventury Type Wet 1. SO < 100 ppm (Bidrum Water Tube 50t/Hr) Scrubber 2 45.0 (common NO 2 < 50 ppm stack) PM < 150 Mg/Nm3 Boiler No. 2 Ventury Type Wet 2. SO < 100 ppm (Bidrum Water Tube 30t/Hr) Scrubber 2 NO 2 < 50 ppm PM < 150 Mg/Nm3 D. G. Set 3. 11.0 -- SO 2 < 100 ppm (500 KVA – Stand By) NO 2 < 50 ppm PROPOSED: No any additional utilities are required for the proposed project.

WASTE WATER GENERATION AND IT’S TREATMENT: Wastewater generated from the sugar factory is being treated in existing ETP unit and treated water is being used in bio-composting. Waste water generated from the proposed distillery unit in the form of spent wash will be concentrating in multi effective evaporator and then sent for bio-composting. Condensate from MEE will be recycled back to the process, while spent less and other waste water will be treated in ETP units and treated water will be used for the bio-composting. Thus achieve the’ Zero Liquid Discharge’.

NOISE POLLUTION AND CONTROL MEASURES: From the existing and proposed manufacturing unit noise pollution will generate which will be controlled by adopting different types of noise pollution control measures. Main sources of the noise pollution are machineries, Electric motors, etc. Following noise control measures to be adopted in the existing and proposed project, ‹ Encasement of noise generating equipment. ‹ Greenbelt all around the plant boundary. ‹ 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 details of solid/Hazardous waste generation and its management are given in the following table.

Sr. Name of the Cat Existing Additional Total Method of Storage & Disposal No. Waste No. (MT/Year) (MT/Year) (MT/Year) 58 58 Collection, Storage and used as 1. ETP Waste 34.3 -- (MT/Year) (MT/Year) Manure. Collection, Storage, transportation

1.45 0.55 2.0 and disposal by selling to GPCB 2. Used Oil 5.1 (MT/Year) MT/Year (MT/Year) approved registered recyclers /

reuse. Discarded Collection, Storage and disposal by 150 150 3. Container/Barrel 33.3 -- selling to GPCB approved Nos./Year Nos./Year s/ Linear registered recyclers.

GREEN BELT DEVELOPMENT Company is having total 1,53,262 m2 land area is available. The company has green belt area with Lawn, plants and flowers spread across about 33% of the total area. Further it will be developed at plant boundary.

INDEX

CHAPTER CONTENT NO. 1 Introduction of the Project 2 Project Description 3 Site Analysis 4 Planning Brief 5 Proposed Infrastructure 6 Rehabilitation and Resettlement (R & R) Plan 7 Project Schedule & Cost Estimates 8 Analysis of Proposal

CHAPTER-1 INTRODUCTION OF THE PROJECT

1.1 IDENTIFICATION OF PROJECT M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd. is a sugar industry located at Survey No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O-Maroli Bazar, Taluka Jalalpore, District Navsari, Gujarat. Molasses is produced as a by-product during manufacturing of sugar. Maroli sugar industry is planning to set up 35 KLPD distillery plant within existing premises using molasses as a basic raw material.

1.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd is planning for installation of the molasses based distillery unit at Survey No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O-Maroli Bazar, Taluka Jalalpore, District Navsari, Gujarat.

LIST OF PRODUCTS AND PRODUCTION CAPACITY

Sr. Existing Additional Name of the Products Total No. Quantity Quantity (a) Products 1 White Crystal Sugar 11,200 MT/Month -- 11,200 MT/Month Captive Power Plant (In House 2 5.85 Mw/Hr. -- 5.85 Mw/Hr. During Crushing Season) Rectified Spirit / Anhydrous 3 -- 35 KLPD 35 KLPD Ethanol (b) By Products 4 Molasses 5,200 MT/Month -- 5,200 MT/Month 5 Bagasse 33,500 MT/Month -- 33,500 MT/Month 6 Press Mud 4,200 MT/Month -- 4,200 MT/Month 7 Bio Compost 4,200 MT/Month -- 4,200 MT/Month

1.3 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE COUNTRY AND OR REGION. In India economy many industries are dependent over agriculture produce for production of luxury and need based committees. Alcohol is used in chemical industry as well as for preparation of beverages. The use of alcohol for the purpose of potable liquor is as high as its use for industrial purpose. As a source of income to the government, the potable liquor units get assured quota of alcohol. This trend is continuing and will continue in view of the fact that potable liquor has larger revenue generating potential. Denatured sprits are Rectified Sprit made unfit for drinking by addition of chemicals which have strong disagreeable odor and which cannot be easily separated from sprit. Ethyl alcohol is important feedstock for manufacture for basic carbon base products like Acetic Acid, Butanol, Butadiene, Acetic anhydride, Vinyl acetate, PVC etc. which are needed in pharmaceuticals, paints and other important industries as they are value added products. Ethyl alcohol has been a source of large amount of revenue by way of excise duty levied by Government on alcoholic liquor. Fermented ethyl alcohol has also great demand in countries like Japan, United state, Canada, Sri Lanka etc. as synthetic alcohol produced by these countries from Naphtha of Petroleum Crude is not suitable for beverages. Ethylene, Ethylene oxide and mono-ethylene glycol can be manufactured from petrochemical route. However, latest technological development and taking into account increasing cost of petrochemical raw material the above mentioned chemicals can be easily manufactured from ethyl alcohol.

1.4 DEMANDS-SUPPLY GAP The gap between the availability of alcohol and the requirement by the industry has been widening. The existing requirement of alcohol by the industries is around 600 million liters annually. In 1992-93, alcohol consumed for industrial purpose was 450 million liters and utilization for potable purpose was 434 million liters. The trend is expected to continue over last 9-10 years.

1.5 EMPLOYMENT GENERATION: For the proposed project additional 24 nos. of personnel (existing 237 nos.) will be employed.

CHAPTER-2 PROJECT DESCRIPTION

2.1 TYPE OF PROJECT M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd is an existing sugar mill located, at Survey No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O-Maroli Bazar, Taluka Jalalpore, District Navsari, Gujarat. Molasses is produced as a by-product during manufacturing of sugar. Maroli sugar factory is planning to set up distillery plant within existing premises of sugar plant to manufacture 35 KLPD Rectified Spirit and/or 35 KLPD Anhydrous Alcohol using molasses as a basic raw material.

2.2 LOCATION M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd located at Survey No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O- Maroli Bazar, Taluka Jalalpore, District Navsari Gujarat. It is situated at 21°01'.18.24" North latitude and 73°54'59.47" East longitude. A map showing location of the presentated in figure-1and detailed plan layout in shown in figure- 2.

FIGURE- 1 LOCATION MAP

FIGURE-2 PLAN LAYOUT

2.3 PROCESS DESCRIPTION MANUFACTURING PROCESS OF DISTILLERY UNIT

The manufacturing process of rectified spirit/ anhydrous alcohol involves two major steps. Molasses is the basic raw material. Generally sulphuric acid is not required, nutrients like yeast, anti-foam agent etc, will be used.

Following steps are required for the Ethanol Production.

1) Fermentation Section Molasses handling: Molasses from the own sugar factory will be utilized for the proposed production. Molasses is then after weighted, sent for storage or to the process diluter tank.

Yeast Propagation: Best strain of yeast is required for the production of alcohol, yeast is bought from nearby vendor and is developed further in propagation section and maintain the viable cell population of about 300 million cells/ml by yeast recycling and continuous aeration of the fermenter.

Fermentation: When Yeast is added in container, yeast works on sugar present in molasses, break down the sugar into alcohol and carbon-dioxide, required temperature controlled to be 30-32°C (by circulating cooling

water). From Fermenter CO 2 collected and directed to scrubber. Remaining content is “wash”.

2) Distillation Section The “wash” from the fermentation enters into distillation section. The hardware contains columns basically for two functions, namely Stripping and Rectification. Thus, 1) Analyser column – Operated under vacuum and 2) Rectifier cum Exhaust Column – operated under pressure. (Additional columns only for refinement).

The “wash” from fermentation is first preheated in heater and fed to analyser column. Alcohol from the wash in form of vapour from the analyser column is fed to pre-rectifier column (under vaccum). The impure spirit drawn from the top of column were collected at bottom which is fed into the rectified cum exhaust column (under pressure). Alcohol is enriched towards the top and drawn out as Rectified Spirit about 95% v/v concentrations. Fusel oil generated is drawn out to tank, washed with water, decanted, layers separated and alcohol layer returned as recovery.

3) Molecular Sieve Dehydration Molecular sieve dehydration is to produce anhydrous alcohol from rectified spirit. Water molecules are absorbed on the pore surface and the larger alcohol molecules are excluded and exit from the sieve unit. The absorption is a vapour phase process and hence, rectified spirit, vaporized and super heated in a vaporizer/column is passed through sieve unit. Generally there are two sieve units. One is under adsorption while the other is under regeneration. The cycle time for adsorption and regeneration varies from 5 to 10 minutes. Thus forms Absolute Alcohol of desired 99.8% v/v purity. There is alternate Sieve Bed 2 ready for next operation.

4) Multi-Effect Evaporation Spent wash from the process is fed into bio-digester thus result in recovery of bio-gas and also reduce the COD and BOD. Then after spent wash will be sent in multi effective evaporator. Whole process is under vacuum and vapor generated are compressed and used as steam. Condensate water generated from evaporation will be recycled back into the process.

PROCESS FLOW DIAGRAM OF MOLASSES BASED DISTILLERY AFTER PROPOSED

Molasses Storage and Handling

Fermentation

Multi-Pressure Rectified spirit/ Anhydrous Alcohol Distillation

Spent wash

Bio - Bio-gas Methanation recovered

Multi-Effect Evaporator Sent for Bio -

Condensate composting

Process/Cooling

Water requirement and waste water generation for 35 KLPD molasses distillery WATER CONSUMPTION KLD WASTE WATER GENERATION KLD Drift + Evaporation + pure from For Fermentation 263 93 cooling from tower For Dilution 21 Spent Lees 4 For Cooling Tower 187 Spent Wash 373 For Boiler 28 Steam condensate Evaporation Losses 28 Miscellaneous 5 Miscellaneous 5 Domestic 2 Domestic 2 TOTAL 506* TOTAL 506

*Above table represents maximum fresh water requirement.

2.4 RAW MATERIALS REQUIREMENT Details of raw material consumption are given in following table.

LIST OF RAW MATERIALS

Sr. Name of the Raw Existing Quantity Additional Quantity Total No. Material (MT/Month) (MT/Month) (MT/Month) 1. Sugar Cane 93,000 -- 93,000 2. Lime 205 -- 205 5

Sr. Name of the Raw Existing Quantity Additional Quantity Total No. Material (MT/Month) (MT/Month) (MT/Month) 3. Sulphur 47 -- 47 4. Phosphoric Acid 4.5 -- 4.5 5. Hydrochloric Acid 0.01 -- 0.01 Caustic Soda (Sodium 6. 1.11 10.5 11.61 Hydroxide) 7. Urea -- 0.8 0.8 8. Antifoam Agent -- 1.74 1.74 Molasses (From own 9. -- 4,200 4,200 Sugar factory) Yeast (Active Dry 10. -- Own Propagation Yeast/Distiller’s Yeast)

2.5 RESOURCE OPTIMIZATION / RECYCLING AND REUSE IN THE PROJECT Water as a resource is recycled at each possible step of the process and latest technology and methodology will be adopted to conserve and reuse the resources. Waste water generated from the process goes to ETP and treated water after pH corrections is used back again into the various processes and remaining is used for the horticulture purposes.

2.6 AVAILABILITY OF WATER ITS SOURCE, ENERGY / POWER REQUIREMENT AND SOURCE 2.6.1 WATER REQUIREMENT For the proposed project additional 506 m3/Day water will be required. Existing water required of the sugar plant is 428.7m3/Day, after proposed project total water required will be 934.7m3/Day. Source of water for existing unit is Borewell/ Canal and for the proposed distillery unit surface water (i.e canal water) will be utilized.

2.6.2 POWER REQUIREMENT For proposed project additional power requirement will be 400 KW/Hr. Existing connected Power load is 299.10 KWH/MT. Power supply shall be full-filled by Dakshin Gujarat Vij Company Limited.

2.6.3 FUEL REQUIREMENT SR. DAILY FUEL CONSUMPTION SOURCE & MODE OF FUEL NO. EXISTING PROPOSED TOTAL TRANSPORTATION 1. Diesel 15 Lit / Hr -- 15 Lit / Hr From Nearest Petrol Pump Within own sugar factory 2. Baggase 40 MT / Hr 1.9 MT/Hr 41.9 MT/Hr premises

2.7 QUANTITY OF WASTES TO BE GENERATED (LIQUID, AIR AND SOLID) AND THEIR MANAGEMENT / DISPOSAL 2.7.1 WASTE WATER GENERATION For the proposed project additional 506 m 3/day water will be generated. Existing waste water generation of the sugar plant is 563.71m 3/day, after proposed project total waste water generation will be 1069.71m3/Day.

Waste water generated from the proposed distillery unit in the form of spent wash will be concentrating in multi effective evaporator and then sent for bio-composting. Condensate from MEE will be recycled back to the process, while spent less and other waste water will be treated in ETP units and treated water will be used for the bio-composting. Thus achieve the’ Zero Liquid Discharge’.

2.7.2 AIR POLLUTION EMISSIONS FROM COMBUSTION OF FOSSIL FUELS FROM STATIONARY OR MOBILE SOURCES STACK AIR POLLUTION SR. STACK ATTACHED TO HEIGHT IN CONTROL PARAMETER NO. METER DEVICES EXISTING PM < 150 mg/nm3 Boiler No. 1 Ventury Type Wet 1. SO < 100 ppm (Bidrum Water Tube 50t/Hr) Scrubber 2 45.0 (common NO 2 < 50 ppm stack) PM < 150 mg/nM3 Boiler No. 2 Ventury Type Wet 2. SO < 100 ppm (Bidrum Water Tube 30t/Hr) Scrubber 2 NO 2 < 50 ppm PM < 150 mg/nM3 D. G. Set 3. 11.0 -- SO < 100 ppm (500 KVA – Stand By) 2 NO 2 < 50 ppm PROPOSED: No any additional utilities are required for proposed project.

2.7.3 SOLID WASTE GENERATION AND THEIR DISPOSAL The sources of solid wastes, generation and its management are as given in the following table.

EXISTING PROPOSED TOTAL SR. WASTE QUANTITY QUANTITY QUANTITY DISPOSAL NO. (MT/M) (MT/M) (MT/M) 58.0 58.0 Collection, Storage and used as 1. ETP Waste -- (MT/Year) (MT/Year) Manure. Collection, Storage, transportation 1.45 0.55 2.0 2. Used Oil and disposal by selling to G PCB (MT/Year) MT/Year (MT/Year) approved registered recyclers. Discarded Collection, Storage and disposal 150.0 150.0 3. Container/Barrels/ -- by selling to GPCB approved Nos./Year Nos./Year Linear registered recyclers.

CHAPTER-3 SITE ANALYSIS

3.1 CONNECTIVITY

3.1.1 RAIL The nearest railway station is Maroli Railway station, which is around 2 km in 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 which is approximately 6 km East direction from the project site.

3.1.3 AIR The nearest airport from the project site is Surat Airport. The distance of airport from project site is around 21 km in North West.

3.1.4 COMMUNICATION Project Site is well connected with telephone, telefax etc. all the communications facilities are well developed in the district.

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. For the proposed project existing infrastructure land will be utilized.

3.4 EXISTING SOCIAL STRUCTURE Project site is located at a distance of around 9 km from Navsari city. All the infrastructures are available within city like Schools, Hospitals & community facilities.

CHAPTER – 4 PLANNING BRIEF

4.1 PLANNING CONCEPT Molasses is the by-product in processing sugar cane for production of sugar. In general the molasses production is about 4.5% on cane crushed. The Carbohydrates in Molasses are already in the form of Sugars. Hence molasses does not need any pretreatment for production of Alcohol. Repeated evaporation and Centrifugation decreases the sugar content of molasses and increases the viscosity and concentration of salts and other impurities. The residual syrup thus becomes thick, viscous and brown in colour and is very heavy. The concentration of molasses is normally measured in Brix.

Molasses Scenario of India

Details of Molasses Production in India (Source-Indian Sugar Mills Association)

Season 2008-09 2009-10 2010-11 2011-12 2012-13 2013-14 Molasses 6.542 8.40 10.97 11.824 11.744 10.881 Production

4.2 LAND USE PLANNING The plant general layout has been planned considering production facilities, auxiliary and ancillary facilities and plant utilities & services. Out of the total plot area (1,53,262 m2) around 8000 m 2 of open area from the existing unit will be utilized for the distillery plant.

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 unit will be provided.

CHAPTER – 5 PROPOSED INFRASTRUCTURE

5.1 INDUSTRIAL AREA No new land will be acquired for the proposed project. Out of total land area (i.e. 1,53,262 m2) around 8,000 m2 open land area will be utilized for the proposed distillery unit.

5.2 RESIDENTIAL AREA There is no provision of housing for the employees at site.

5.3 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. Further it will 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.

5.4 SOCIAL INFRASTRUCTURE Drinking water facility, proper sanitation, etc. will be provided to the workers working in plant.

5.5 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.

5.6 WASTE WATER MANGAMENT Waste water generated from the proposed distillery unit in the form of spent wash will be concentrating in multi effective evaporator and then sent for bio-composting. Condensate from MEE will be recycled back to the process, while spent less and other waste water will be treated in ETP units and treated water will be used for the bio-composting. Thus achieve the’ Zero Liquid Discharge’.

5.7 INDUSTRIAL SOLID WASTE MANAGEMENT From the proposed project activity detail for the solid/hazardous waste generation are given in below table.

DETAILS OF SOLID & HAZARDOUS WASTE GENERATION DURING OPERATION NAME OF TOTAL METHOD OF SR. CAT EXISTING ADDITIONAL THE (MT/YEAR STORAGE & NO. NO. (MT/YEAR) (MT/YEAR) WASTE ) DISPOSAL 58.0 58.0 Collection, Storage 1. ETP Waste 34.3 -- (MT/Year) (MT/Year) and used as Manure. Collection, Storage, transportation and

1.45 0.55 2.0 disposal by selling to 2. Used Oil 5.1 (MT/Year) MT/Year (MT/Year) GPCB approved

registered recyclers / reuse. Collection, Storage Discarded 150.0 150.0 and disposal by selling 3. Container/Ba 33.3 -- Nos./Year Nos./Year to GPCB approved rrels/ Linear registered recyclers.

CHAPTER – 6

REHABILITATION AND RESETTLEMENT (R & R) PLAN

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.

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 project after proposed project will be around Rs. 30 crores. Total capital cost of pollution control measures will be Rs. 3 crores & recurring cost per annum will be 1 crores.

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 CRORE NO. 1. Capital Expenditure 3.0 2. Recurring expenditure on environmental management cell and on pollution control systems per annum. 1.0

CHAPTER – 8

ANALYSIS OF PROPOSAL

8.1 FINANCIAL AND SOCIAL BENEFITS The capital cost of the distillery unit in existing premises is estimated about Rs. 30.0 Crores for the installation of plants & machinery along with required auxiliary and balancing facilities for the production.

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.