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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 – 495335

(Chattisgarh)

Proposed By :-

AEGIS BEVERAGES PVT. LTD. Regd. Office :

23, Sarat Bose Road, Annapurna Building, 3rd Floor, Flat 3A, Kolkata, WB – 700020, India

INDEX

Contents Page Nos.

1. Executive Summary 01

2. Introduction of the Project / Background Information 01

3. Project Description 04

4. Site Analysis 10

5. Planning Brief 13

6. Proposed Infrastructure 16

7. Rehabilitation and Resettlement (R & R) Plan 17

8. Project Schedule & Cost Estimates 17

9. Analysis of Proposal 18

Pre Feasibility Report for Proposed Grain based Distillery Project of Aegis Beverages Pvt. Ltd.

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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 grains @ 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 m3/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.


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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 26th

July.’1996 having CIN No. U51109WB1996PTC080627 and Registration No. is 080627.

Project Proponent ; Mr. H S Ahuja President Aegis Beverages Pvt. Ltd. 709 711, 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.


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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 2014-15.

Projection for the year 2015-16 is 50.50 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:


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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 Co-

generation 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.


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AEGIS BEVERAGES PROJECT LOCATION MAP

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.

Howrah Delhi Main Line


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(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 ;

Yeast Enzyme Invertase C12H22O11 + H2O 2C6H12O6 ………………(1) (Sucrose) (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 CO2 according to the

following exothermic reaction :-

Yeast C6H12O6 2 C2H5OH + 2 CO2 + 26 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 400-700µ) 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 6.0-6.2 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


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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 90- 950 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 co-

product. 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


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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.


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Low boiling impurities are separated in the purifier column & bottom is sent to Rectifier-

cum-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 ;


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MANUFACTURING PROCESS FLOW SHEET OF AEGIS BEVERAGES PVT. LTD..

ENA


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(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) 30 Kg / Day From Kolkata & Bilaspur

By trucks

Urea 150 Kg / day

Antifoam Agent 15 Kg / Day

Enzymes

Liquefying Enzyme 22 Kg. / day From Suppliers Kolkata & Bilaspur

By Trucks Saccharifying Enzyme 38 Kg / Day Yeast 15 Kg / Day

(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 M3 / day 2. Process Water in Fermentation 46.0 M3 / day 3. DM Water for RS Dilution & Vaccum Pump 30.0 M3 / day


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4. Moisture in Grains 8 M3 / day 5. Total Steam Input to Process Plant 122.0 M3 / day 6. Soft Water as Cooling Tower Make up 300.0 M3 / day 7. Water for Domestic Use 8.0 M3 / day 8. Green Belt Water Requirement 10.0 M3 / day

GRAND TOTAL 525.0 M3 / day

(B) Total Water Output

Water Requirement Quantities

Spent lees PR 30.0 M3 / day

Spent lees rectifer 27.0 M3 / day

Steam condensate recycle 113.0 M3 / day

Water in product 1.0 M3 / day

Water in DDGS (by-product) 2.0 M3 / day

Spent lees recovery column 3.0 M3 / day

Moisture vented through dryer 30.0 M3 / day

Moisture vented with co2 0.6 M3 / day

Cooling tower drift losses 300.4 M3 / day

Domestic losses (consumption) 1.5 M3 / day

Domestic effluent 6.5 M3 / day

Green Belt 10.0 M3 / day


(C) Total Recycle Water


Spent lees recycle 46 M3 / day

Steam condensate recycle for boiler 113 M3 / day

Cooling water makeup 8 M3 / day

Process condensate recycle 109 M3 / day

Green belt irrigation 10.0 M3 / day


(D) Total Fresh Water Requirement


1. Process Water in Liquefaction 1.0 M3 / day

2. DM Water for RS Dilution & Vacuum Pump 30.0 M3 / day


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3. Steam Input 9.0 M3 / day

4. Water for Fermentation 46.0 M3 / day

5. Misc. Process Requirements 145.0 M3 / day

6. Domestic 8.0 M3 / 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 wash @ 180 m3/day would be generated during

the production of alcohol @ 30 KL/day. The spent wash would be sent to the decanter

where wet cake @ 25 MT/day would be separated. The remaining liquid i.e. thin slops @

145 m3/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 lees @ 67 m3/day would be generated and MEE condensate @ 446

m3/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 effluent @ 5

m3/day, cooling towers blow down @ 19 m3/day, domestic effluent @ 6.5 m3/day, D.M.

plant reject @ 12 m3/day, and boiler blowdown @ 10 m3/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,


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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 30 TPD It will be collected in Ash silos and send to brick manufacturing units

DDGS (Distillers Dried Grain Soluble) from Dryer

25 TPD

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

Yeast Sludge / ETP Sludge

0.25 – 0.5 TPD

Mix with DDGS

4. Site Analysis:

(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 - 130 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.


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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.


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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.


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10 KM. RADIUS TOPOSHEET OF AEGIS BEVERAGES PROJECT SITE


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vii) Climatic Data ;

The project area receives rainfall mainly from the southwest monsoon. It sets in 3rd / 4th

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 (1992-2011). 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 ;

Year Rainfall in mm.

(Source IMD Data)

2010 973.9

2011 1290.1

2012 1350.1

2013 1449.5

2014 1348.2

Average Rainfall 1282.36 mm. viii) Social Infrastructure available ;

All the social infrastructure, as mentioned below, are available within 10 - 20 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


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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).



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.


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AEGIS BEVERAGES GRAIN BASED DISTILLERY SITE LAYOUT PLAN


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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.


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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 30 TPD It will be collected in Ash silos and send to brick manufacturing units

DDGS (Distillers Dried Grain Soluble) from Dryer

25 TPD

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

Yeast Sludge / ETP Sludge

0.25 – 0.5 TPD

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.


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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.

.

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