PRE-FEASIBILITY REPORT

Transcription

1 PRE-FEASIBILITY REPORT FOR PROPOSED 30 KLD GRAIN BASED DISTILLERY PROJECT WITH 5 MW POWER CO-GENERATION PLANT At Vill. Kirna Tehisl : Mungeli Dist. Bilaspur (Chattisgarh) Proposed By :- AEGIS BEVERAGES PVT. LTD. Regd. Office : 23, Sarat Bose Road, Annapurna Building, 3 rd Floor, Flat 3A, Kolkata, WB , India

2 INDEX Contents Page Nos. 1. Executive Summary Introduction of the Project / Background Information Project Description Site Analysis Planning Brief Proposed Infrastructure Rehabilitation and Resettlement (R& R) Plan Project Schedule & Cost Estimates Analysis of Proposal 18

3 1. EXECUTIVE SUMMARY : The proposed distillery & power co-generation project of Aegis Beverages Pvt. Ltd.., is for setting up of manufacturing facilities to produce Extra Neutral Alcohol (ENA). It is based on primarily agricultural products (grain based). The project will be equipped with fully diversified processing facilities and will have a capacity of producing 30 KL of ENA per Day alongwith 5 MW Power Co-generation. As per EIA Notification 2006 and amendments thereof, the proposed distillery project is B category project and listed in Schedule of EIA Notification 2006 at Sl. No. 5(g). Project proponent of has acquired Total 10 Acres (4.05 Ha.) of land for establishment of its proposed distillery and co-generation project at Vill. Kirna, Block Mungeli, Dist. Bilaspur in the state of Chattisgarh. The major raw material and inputs will be 75 MT/Day, enzymes 60 kg/day, sodium hydroxide 30 kg/day, urea 150 kg/day, anti-foam agent 15 kg/day, yeast 15 kg/day. All the industrial effluent of proposed distillery unit will be treated by evaporation in Multi Effect Evaporator (MEE) to achieve zero discharge. The generated waste water after fermentation, send to Decantation for separation of solids. The thin slopes, after evaporation in 4 stage Multi-Effect Evaporator, produce wet cake to use as cattle feed. The condensate is being recycle & reuse in the process. This treated water is non polluting in nature and it contains mainly micro nutrients. Effluent generation from other misc. streams will be approx. 125 m 3 /day. The mixed effluent would be collected in a collection tank. Thereafter it would be treated through anaerobic biofilteration, aeration and clarification. The treated effluent would be recycle and reuse within premises for various integral purposes. The slope or stillage coming out as effluent of distillation column is used to make Distillers Wet Grains [DWG], & Dry Distillers Grain soluble [DDGS] a high value cattle feed which will be a boon for farmers & cattle. 1 P a g e

4 To control air pollution from proposed distillery project ESP will be installed in the Boiler Stack. Total Cost of the Project is 44 Crores. 2. INTRODUCTION OF THE PROJECT/BACKGROUND INFORMATION : (i) Identification of Project & Project Proponent Project ; M/s Aegis Beverages Private Limited, (ABPL) is a company incorporated on 26 th July having CIN No. U51109WB1996PTC and Registration No. is Project Proponent ; Mr. H S Ahuja President Aegis Beverages Pvt. Ltd , 7th floor Ambience Mall, NH 8, Gurgaon (Haryana) (ii) Brief description of nature of project : The proposed distillery project of Aegis Beverages Pvt. Ltd., is for setting up of manufacturing facilities to produce Extra Neutral Alcohol (ENA). It is based on primarily agricultural products (grain based). The project will be equipped with fully diversified processing facilities and will have a capacity of producing 30 KL of ENA per Day alogwith 5 MW Power Co-generation. (iii) Need for the project and its importance to the country and or region Due to abundant available of raw materials being used in the grain based distilleries there has been a huge demand for grain based extra neutral alcohol for the fast growing IMFL Industries and for blending in Foreign Liquor outside India which has been a multi-fold surge in demand. Due to substantial deficiency in supply of grain based ENA and potentiality of the national & international market Aegis Beverages Pvt. Ltd.. have planned to establish 30 KLD grain based distillery in the major grain producing area of Chattisgarh. 2 P a g e

5 The proposed distillery project will play an important role in upliftment of the socio economic condition of the region particularly nearby villages. (iv) Demand Supply Gap: The total requirement of ENA / IMFL / Ethanol in India is 600 crores litres (25% ENA from grain & 75 % from molasses) and 350 Crore Litres for Ethanol as Fuel whereas, in India, total production of ENA from molasses and grain is 148 crores litres per annum. Next five year projected ENA from grain 40 % & from molasses 60 %. 275 Crore Litres of alcohol produced from molasses were used by oil companies in the year of Projection for the year is crores litres by the oil companies. Post 2017 India will require 6.30 billion litres of alcohol mainly from molasses for the use in petrol by the oil companies. Therefore, the huge demand of ENA made out of grain will arise. (v) Imports vs. Indigenous Production: Indian producers are not able to meet present alcohol demand. Approx 5-7% of total demand of alcohol is being imported from other countries. As far as ENA production is concerned, Indian market play a vital role at both domestic & international level. In this context, there is major requirement of indigenous grain based alcohol production to reduce the import load and save the revenue. (vi) Domestic/Export Market: There is a huge demand of Indian made grain based alcohol in the national and international market. (vii) Employment Generation (Direct & Indirect) Due to establishment of proposed distillery project in the region direct and indirect employment avenues will be created in the nearby areas. Approx. 50 nos. of manpower including officers, management personnel and workers etc. will be employed after the establishment of the distillery project. 3. Project Description: (i) Type of project including interlinked and inter dependent project: 3 P a g e

6 The proposed distillery project of Aegis Beverages Pvt. Ltd., is for setting up of manufacturing facilities to produce Extra Neutral Alcohol (ENA). It is based on primarily agricultural products (grain based). The will be equipped with fully diversified processing facilities and will have a capacity of producing 30 KL of ENA per Day. 5 MW Cogeneration power plant is interlinked and interdependent on proposed grain based distillery project. (ii) Location: Village : Kirna Block : Mungeli District : Bilaspur State : Chattisgarh Refer Project Location Map of Aegis Beverages Pvt. Ltd. distillery project on next page. (iii) Details of alternate sites Considered and the basis of selecting the proposed site, particularly the environment consideration gone into should be highlighted. No alternate sites have been considered for the proposed distillery project as the land was easy available and area is rich in raw material sources with ease of accessibility. (iv) Size or magnitude of operation: 30 KLD of ENA will be produced & 5 MW Power will be cogeneration in the proposed grain based distillery project of AB Grains Ltd. 4 P a g e

7 AEGIS BEVERAGES PROJECT LOCATION MAP Howrah Delhi Main Line Project Location :- AEGIS BEVERAGES PVT. LTD. VILL. KIRNA MUNGELI BILASPUR (CHATTISGARH) LONGITUDE: 21 52'49.19"N LATITUDE : 81 56'54.29"E MSL : 249 M. 5 P a g e

8 (v) Project description with process details: (a schematic diagram/flowchart layout, components of the project) Alcohol is produced by the fermentation of saccharine or oligo-saccharide materials by yeast under suitable conditions. Sugar available in grains is recovered in the process of distillation. Reactions ; Sugar present in grains is disaccharide, which can be hydrolyzed. This hydrolysis is brought about by certain enzymes called invertase, found in yeast. The chemical reaction involved in process is as under ; C 12 H 22 O 11 + H 2 O (Sucrose) Yeast Enzyme Invertase 2C 6 H 12 O 6 (1) (Glucose Fructose) The mixture of sugars after hydrolysis of sucrose is called invert sugars. This sugar is utilized by yeast to produce ethyl alcohol with the liberation of CO 2 according to the following exothermic reaction :- Yeast C 6 H 12 O 6 2 C 2 H 5 OH + 2 CO Cal... (2) Grain based alcohol (ENA) manufacturing Process is described as under ; Before the milling quality of the grain is being checked. After the quality check grain is cleaned for removal of dust, lumps, sand, stone, iron etc. and finally store in Silo s. Milling ; The cleaned grain is sent to milling machines for grinding grain flour (size µ) is conveyed to pre-masher for slurry preparation. In pre-masher, flour & required water of ratio 1:2 are mixed by agitator. Uniform grain slurry is made and transferred to another low shear tank (slurry tank) for proper mixing. In slurry tank required ph of is maintained by using lime if required and temperature as 550 C to 600 C. An enzyme called α-amylase is added here in small (20-25%) dose before the cooking process starts. Cooking : The grain slurry is pumped to Jet Cooker (Hydro Heater) through open impeller centrifugal pump. In jet cooker steam is applied at 8 to 10 kg/cm2 pressure to cook the 6 P a g e

9 starch slurry to break down the chemical structure of starch in presence of enzymes. The temperature of grain slurry at outlet of jet cooker is maintained between 115 to 1200 C. After cooking the grain slurry is passed through the holding coil, which has several U bends in series and sufficient capacity to provide desired retention time at a given flow rate to convert starch into dextrin. In this step slurry pressure & viscosity reduces. The slurry which is hot is transferred into the flash tank to reduce the temperature of the slurry to C before sending to saccharification tank. Flash tank is attached to flash condensers where vapours are condensed and condensate is sent to slurry tank. Liquefaction ; Grain slurry is transferred to liquefaction tank from flash tank where remaining 75 to 80% of enzymes of α-amylase is added which convert starch to dextrin and 1-4 α-glycosidase linkages are hydrolyzed into amylose and amylo pectin. Enzymatic activity rapidly breakdown the starch to soluble dextrins and oligosaccharides. To have good conversion of starch to dextrin retention time should be about 2 hrs Saccharification and Fermentation Many distilleries have Partial PreSaccharification tanks for saccharification process. Whereas conducting saccharification and fermentation together is another process adopted. The liquefied slurry pumped through Plate Heat Exchanger (PHE) to the fermenters. The outlet temperature of grain slurry from PHE is 32 to 350 C. In fermenters saccharification & fermentation takes place simultaneously by adding glycol-amylase enzyme and yeast culture. Fermentation of starch from grain is somewhat more complex than fermentation of molasses sugars because starch must first be converted to sugar and then to ethanol. Starch is converted enzymatically to glucose either by diastase presents in sprouting grain or by fungal amylase. The resulting dextrose is fermented to ethanol with the aid of yeast producing CO2 as coproduct. A second co-product of unfermented starch, fiber, protein and ash known as distillers grain (a high protein cattle feed) is also produced. Glucoamylase hydrolise dextrin into maltose. In this complete conversion of dextrin takes place and to reduce the viscosity further spent wash after decanter is mixed to save water. Maltose further breaks into glucose & fructose. Yeast i.e. Saccharomyces cerevisiae which produce invertase and zymase enzyme convert glucose & fructose into alcohol. Above both processes takes 7 P a g e

10 place in a fermenter. Glucose is converted into ethyl alcohol and carbon dioxide evolved is let out. The total duration required is 60 to 65 hours. The entire material is sent for distillation and yeast sludge in continuous process is settled at bottom is mixed with water and used for fresh batch whereas in Batch process the entire yeast sludge was let out. Due to more fermentation time side byproducts i.e. acids & higher alcohols are high as compared to molasses which affects proper alcoholic fermentation. Distillation Multiple-pressure vacuum distillation system: Vacuum distillation is defined as that in which the operating pressure in the system is either less than atmospheric pressure or more than atmospheric pressure. Vacuum is nothing but sub-atmospheric pressure (negative gauge pressure). Fermented wash to extra neutral alcohol (ENA): Multi-pressure vaccum distillation system for production of Extra Neutral Alcohol consists of distillation columns namely- 1. Degasifying-cum-analyzer column- Operation under vaccum 2. Pre-rectification-cum-Exhaust column- Operation under vaccum. 3. Extractive Distillation Column- Operation under pressure 4. Rectifier-cum- Exhaust column- Operated under pressure 5. Recovery/Fused Oil Column- Operated under pressure 6. Simmering Column- Operated under atmospheric or Vaccum Pre-heated fermented wash is fed at the top of the Degassifier column. Analyzer Column is provided with reboiler. Top vapours of analyzer column containing all the alcohol in the wash are sent to Pre-rectifier column and are taken out as spent wash from Analyzer column bottom. Low Boiling impurities are concentrated in the Pre-rectifier column. A draw of impure alcohol is taken out from the top of the Pre-rectifier column. RS draw is taken from the top of Pre-rectifier column, which further is sent to Extractive Distillation (Purifier) column. Dilution water in the ratio of 1:8 to 1:9 is fed to this column. The Extractive Column operates on the principle of inversion of relative volatility. 8 P a g e

11 Low boiling impurities are separated in the purifier column & bottom is sent to Rectifiercum-Exhaust column. The Rectifier/Exhaust Column concentrates the alcohol to 96% v/v. The high- grade spirit is drawn from upper trays of the rectification column. Fusel oil build up is avoided in the Rectifier-cumexhaust column by withdrawing side streams (Fusel oils). Purifier condensates, Degasifier condensates & fusel oil draw from Rectifier/Exhaust column are sent to Recovery column where these fusel oils are concentrated and then sent to decanter where these streams are diluted with water and fusel oil rich layer is separated. Washings are sent back to the column to recover alcohol. The high spirit draw from the Rectifier column is sent to the Simmering column where methanol is separated in the form of a cut from the top and ENA is taken out from the bottom. ENA draw from the simmering column is taken to the receiver after cooling in ENA cooler. The steam consumption of this set up would be of about 6.5% of total spirit production. Distillation with integrated evaporation system: Integrated evaporation or standalone evaporation systems are now getting installed in few distilleries with an intension to concentrate the spent wash as per their requirement. It helps to reduce the final quantity of spent wash generation. Integrated evaporation system uses alcohol vapours as heating media for heating the spent wash. Thus, good amount of steam saving can also be achieved in integrated evaporation systems. Integrated evaporation is expected to concentrate the spent wash to about 22-30% solids concentration depending on the type of fermentation system used and final alcohol concentration in wash. Manufacturing process flow sheet is shown on next page ; 9 P a g e

12 MANUFACTURING PROCESS FLOW SHEET OF AEGIS BEVERAGES PVT. LTD.. ENA 10 P a g e

13 (vi) Raw Material required along with estimated Quantity, likely source, marketing area of final products, mode of Transport of raw material & finished product. Raw Materials Requirement Source of Raw Materials Transportation GRAIN (Broken Rice, Wheat, Maize, Bajra, Jowar etc.) 75 TPD From local markets By Trucks Chemicals Sodium Hydroxide (Caustic) Urea Antifoam Agent Enzymes Liquefying Enzyme Saccharifying Enzyme Yeast 30 Kg / Day 150 Kg / day 15 Kg / Day 22 Kg. / day 38 Kg / Day 15 Kg / Day From Kolkata & Bilaspur From Suppliers Kolkata & Bilaspur By trucks By Trucks (vii) Resources optimization/recycling and reuse envisaged in the project, if any, should be briefly outlined. Aegis Beverages Pvt. Ltd. will make optimum utilization, recycling and reuse. These resources include Land, Fuel (Rise husk and coal), Grain, Water and Electricity. Wastewater generated from Boiler and cooling tower blow down will be treatment in polishing unit and recycled for further process, domestic & green belt development uses. (viii) Availability of Water its source, Energy/Power requirement and source should be given Water requirement of the proposed Grain Based Distillery Project will be approx. 525 KLD. 517 KLD water will be utilized for industrial and allied purposes and 8 KLD water will be for domestic purposes. Total Fresh Water requirement will be 239 KLD and 286 KLD treated water will be recycle and reuse for various purposes. The Details are as under ; (A) Total Water Input (Total Water Requirement) Water Requirement Quantities 1. Process Water in Liquefaction 1.0 M 3 / day 2. Process Water in Fermentation 46.0 M 3 / day 3. DM Water for RS Dilution & Vaccum Pump 30.0 M 3 / day 11 P a g e

14 4. Moisture in Grains 8 M 3 / day 5. Total Steam Input to Process Plant M 3 / day 6. Soft Water as Cooling Tower Make up M 3 / day 7. Water for Domestic Use 8.0 M 3 / day 8. Green Belt Water Requirement 10.0 M 3 / day GRAND TOTAL M 3 / day (B) Total Water Output Water Requirement Spent lees PR Spent lees rectifer Steam condensate recycle Water in product Water in DDGS (by-product) Spent lees recovery column Moisture vented through dryer Moisture vented with co 2 Cooling tower drift losses Domestic losses (consumption) Domestic effluent Green Belt GRAND TOTAL Quantities 30.0 M 3 / day 27.0 M 3 / day M 3 / day 1.0 M 3 / day 2.0 M 3 / day 3.0 M 3 / day 30.0 M 3 / day 0.6 M 3 / day M 3 / day 1.5 M 3 / day 6.5 M 3 / day 10.0 M 3 / day M 3 / day (C) Total Recycle Water Water Requirement Spent lees recycle Steam condensate recycle for boiler Cooling water makeup Process condensate recycle Green belt irrigation GRAND TOTAL Quantities 46 M 3 / day 113 M 3 / day 8 M 3 / day 109 M 3 / day 10.0 M 3 / day M 3 / day (D) Total Fresh Water Requirement Water Requirement Quantities 1. Process Water in Liquefaction 1.0 M 3 / day 2. DM Water for RS Dilution & Vacuum Pump 30.0 M 3 / day 12 P a g e

15 Water Requirement Quantities 3. Steam Input 9.0 M 3 / day 4. Water for Fermentation 46.0 M 3 / day 5. Misc. Process Requirements M 3 / day 6. Domestic 8.0 M 3 / day GRAND TOTAL M 3 / day (ix) Quantity of waste to be generated (Liquid and solid) and scheme for their management. WASTE WATER GENERATION & TREATMENT ; In the proposed grain based distillery project following types of effluent will be generated; Spent Wash from Distillation Process : The project would result in generation of spent wash from the distillation process. Spent 180 m 3 /day would be generated during the production of 30 KL/day. The spent wash would be sent to the decanter where wet 25 MT/day would be separated. The remaining liquid i.e. thin 145 m 3 /day would be treated in multi-effect evaporation system. Condensates from Process and MEE : The project would result in generation of process condensates (spent lees) from the distillation process and multiple effect evaporation condensates. Spent 67 m 3 /day would be generated and MEE 446 m 3 /day would be generated. Whole of the condensates after treatment would be used for makeup water of cooling towers. Effluent from other processes : Besides the above mentioned streams, effluent would be generated from misc. other streams such as floor/fermentor washing 5 m 3 /day, cooling towers blow 19 m 3 /day, domestic 6.5 m 3 /day, D.M. plant 12 m 3 /day, and boiler 10 m 3 /day. This effluent would be moderately polluted and after treatment would be used on land for irrigation purposes. Air Pollution: The air pollution control system will comprise of; a) Ducting arrangement to transport emissions to the APCD, 13 P a g e

16 b) An APCD electro-static precipitator / Bag filters / Wet Scrubber c) An ID fan, and d) A stack to discharge the cleaned flue gas at adequate height. The emissions, from the boilers, will be conveyed into the APCD, the electro-static precipitator (ESP) / Bag Filters / Wet Scrubbers, where it will get cleaned (PM removal) before being discharged into the atmosphere, through a stack of adequate height. If efficiently operated, the PM removal efficiency for the system is expected to be more than 99.8%. Solid Waste Management: All solid waste generated during the process will be managed as under ; Nature of Solid Waste Quantity Management Boiler Ash DDGS (Distillers Dried Grain Soluble) from Dryer Yeast Sludge / ETP Sludge 4. Site Analysis: 30 TPD 25 TPD TPD It will be collected in Ash silos and send to brick manufacturing units This is in form of dry powder containing moisture less than 10%. This will be bagged in 50 Kg bag and will be stored in warehouse and will be sold to Cattle feed manufacturers Mix with DDGS (i) Connectivity: Proposed grain based distillery project of M/s Aegis Beverages Pvt. Ltd., (ABPL) is coming up near Vill. Kirna, Block Mungeli, Dist. Bilaspur, Chattisgarh. Project site of ABPL is accessible through NH from Bilaspur. Nearest railway station is at Bhatapara on Howarh Mumbai Section. ii) Land Form, Land use & Land ownership: Land Form :- Land Use :- Land use of the project area and surrounding is agriculture in nature. Land Ownership :- Project land of 10 Acres was acquired by Aegis Beverages Pvt. Ltd. & is purchased from local villagers on prevailing market price. 14 P a g e

17 iii) Topography (along with map): The terrain is almost hilly at Project site. Physiographically the Bilaspur district can be divided into two parts. The first part consists high plateau area covering north and central part of the district (covering Lormi, Kota, Gaurela, Pendra and Marwahi blocks) separated by the intermittent narrow valleys and steeply slopping plains. The second part is the gently slopping plain land covering southern parts of the district (Takhatpur, Mungeli, Pathariya, Belha and Masturi blocks). The high topographic area on the northern part of the district forms water divide between the rivers Ganges and Mahanadi. The hill ranges on the northwestern part is the water divide between Mahanadi and Narmada Rivers. Major part of the Chhattisgarh basin is drained by Mahanadi River. The topography varies between 250 m amsl in the southern plains and 1120 m amsl in the northern hills. The hill ranges on the northwestern boundary of the district forms part of the Amarkantak ranges. The Deccan traps along the western boundary forms high peaks. Basically the hill ranges on northern part are due to structural activities and the area on southern part (Chhattisgarh plain) can be categorised as pediplain. (Refer Toposheet on next page) iv) Existing land use pattern (Agriculture, non agriculture, forest, water bodies including CRZ), shortest distance from the periphery of the project forest, national park, wild life sanctuary, eco- sensitivity area, water bodies Distance from HFL line, CRZ notification for notified industrial area. There is no reserved forest, national park, wild life sanctuary, eco sensitive zones in surrounding 10 Km of the plant boundary. CRZ is not applicable to the project. v) Existing Infrastructure ; All the required infrastructures are available at Mungeli Tehsil. vi) Soil Classification: The vertisol are mostly found in south and southeastern parts of the district. They range from grey/red to deep black colour and are almost impermeable when saturated. They are sticky in wet season and are very hard in dry season. 15 P a g e

18 The ultisol types of soil are found in east and northern parts of the district and is red to yellow in colour. This colour is attained mainly due to accumulation of iron oxide, which is highly insoluble in water. Inceptisol soils occupy mostly hill slopes and are found along the western boundary of the district. Alfisol soils are fertile leached soils found in humid areas where annually dropping leaves form a thick humus layer. These soils cover maximum area in the northern and central parts of the district. In general it can be said that the district is covered by red gravely soils, red sandy soils, lateritic soils, red and yellow soils and black soils. 16 P a g e

19 10 KM. RADIUS TOPOSHEET OF AEGIS BEVERAGES PROJECT SITE 17 P a g e

20 vii) Climatic Data ; The project area receives rainfall mainly from the southwest monsoon. It sets in 3 rd / 4 th week of June and continues till mid August/ September with heaviest showers in the months of July and August. The average annual rainfall for the Bilaspur district is around 1082 mm ( ). The months of July and August are the heaviest rainfall months and nearly 95% of the annual rainfall is received during June to September months. The rainfall is unevenly distributed in different tehsils and also the amount of rainfall varies from year to year. The area experiences a hot and semi-humid climate. The annual temperature varies from 10 C to 45 C. The hottest months are May and June and the minimum temperature is observed in the months of December and January. Rainfall Status ; Rainfall in mm. Year (Source IMD Data) Average Rainfall mm. viii) Social Infrastructure available ; All the social infrastructure, as mentioned below, are available within Km. of proposed distillery Project Site. Schools (Primary as well as secondary) Colleges (Science, commerce, Arts, engineering, medical, pharmacy, education) Health centers, dispensaries, hospitals Electricity Drinking water supply Banks (Cooperative as well as nationalized) and credit societies 18 P a g e

21 5. Planning Brief: i) Planning concept (type of Industries, facilities, transportation etc) Town and country planning/development authority classification. Type of Industry : As per EIA Notification 2006 and amendments thereof, the proposed distillery project is B category project and listed in Schedule of EIA Notification 2006 at Sl. No. 5(g). The proposed distillery project of Aegis Beverages Pvt. Ltd., is for setting up of manufacturing facilities to produce Extra Neutral Alcohol (ENA). It is based on primarily agricultural products (grain based). The will be equipped with fully diversified processing facilities and will have a capacity of producing 30 KL of ENA per Day. ii) Population Projection: There will be population influx anticipated due to the proposed distillery project in the region either on temporary or permanent basis.. iii) Land Use Planning Site Layout Plan showing along with green belt area is shown herewith on next page. 19 P a g e

22 AEGIS BEVERAGES GRAIN BASED DISTILLERY SITE LAYOUT PLAN 20 P a g e

23 iv) Assessment of Infrastructure demand (physical & social) : The basic infrastructure such as roads, electricity, transportation, drinking water supply, health centers and hospitals, school, colleges, sanitation facilities are available in the vicinity. The proposed project is not going to exert any unbearable load on any of these resources. v) Amenities/Facilities: Canteen, Laboratory, rest room, medical facilities, drinking water, etc. will be made available within proposed distillery project premises. 6. Proposed Infrastructure: All new infrastructure, i.e. new buildings and sheds will be constructed for the proposed grain based distillery project. i) Residential Area (Non-Processing Area): No residential area is envisaged in the proposed project. ii) Green Belt Area : 33% of total project area i.e. 3.3 Acres of land will be utilized as green belt are and will be developed and maintained. iii) Social Infrastructure: All infrastructure facilities are existing in the vicinity of the project area within 10 km. radius. iv) Connectivity Proposed grain based distillery project of M/s Aegis Beverages Pvt. Ltd., (ABPL) is coming up at Vill. Kirna, Block Mungeli, Dist. Bilaspur. Project site of ABPL is accessible through NH 130 from Bilaspur. Nearest railway station is at Bhatpara on Howarh Mumbai Section. 21 P a g e

24 v) Drinking Water Management : Borewell will be used as drinking water source for the proposed distillery project. vi) Sewerage System: All the industrial waste water to be generated from the proposed distillery project will be recycle & reuse within premises after treatment. No industrial waste water will be discharged outside project premises. vii) Industrial Waste Management: Waste Water Generation & Treatment ; All the generated water water will be treated inside the distillery premises by MEE & ETP and will be recycle & reuse within the premises. Air Pollution: For proposed distillery project air pollution control system will be installed at all strategic locations. viii) Solid Waste Management: Nature of Solid Waste Quantity Management Boiler Ash DDGS (Distillers Dried Grain Soluble) from Dryer Yeast Sludge / ETP Sludge 30 TPD 25 TPD TPD It will be collected in Ash silos and send to brick manufacturing units This is in form of dry powder containing moisture less than 10%. This will be bagged in 50 Kg bag and will be stored in warehouse and will be sold to Cattle feed manufacturers Mix with DDGS ix) Power Requirement & Supply/Source: 2.5 MW of power will be utilized for operation of proposed distillery project. Power will be sourced through company s own co-generation plant which will be located adjacent to the distillery project. 22 P a g e

25 7) Rehabilitation & Resettlement (R & R) Plan: All the land for the proposed distillery project of Aegis Beverages Pvt. Ltd. is purchased from local villagers on prevailing market price, so there is no need of any new Rehabilitation and Resettlement (R&R) Plan. 8) Project Schedule & Cost Estimates: i) Likely date of start of construction & likely date of completion. Project activities will be started immediately after obtaining Environmental Clearance from MoEF & CC, Govt. of India. Construction activities will be completed within 8-12 months time after start. ii) Estimated Project cost along with analysis in terms of economic validity: Total Estimated Cost of proposed distillery project is Rs. 44 Crores. 9) Analysis of Proposal (Final Recommendation): (Financial & Social benefits with special emphasis on the benefit to the local people including tribal population, if any, in the area.) After establishment of proposed distillery project in the region direct and indirect employment avenues will be created in the nearby areas. Approx. 50 nos. of manpower including officers, management personnel and workers etc. will be employed after the establishment of the distillery project. Moreover, State Govt. will get additional revenue in the form of taxes due to proposed distillery project and surplus power of approx 2.5 MW will be outsourced to Govt. Grids for public distribution.. * * * * * 23 P a g e