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Proposed Expansion of Existing Grain Based Distillery (120 to 240 KLPD) & Co-Generation Power Plant (3.5 to 8.0 MW) by installation of Unit II – 120 KLPD Grain Based & 4.5 MW Co-Generation Power Plant within Existing Plant Premises At Panagarh Industrial Park, Panagarh, District Burdwan, West Bengal

Pre - feasibility Report

M/s. Globus Spirits Limited 1

PRE - FEASIBILITY REPORT

1.0 EXECUTIVE SUMMARY

(I) Introduction

Globus Spirits Ltd is one of the leading players in the Alcohol industry in North India.

Established in 1992, Globus Sprits Limited is engaged in manufacturing, marketing and

sale of Indian Made Indian Liquor (IMIL), Indian Made Foreign Liquor (IMFL), Bulk Alcohol

and contract bottling for established IMFL brands. The Company has a well-established

presence in the IMIL segment and is making its mark in the IMFL segment apart from

taking up contract bottling to cater to renowned Indian players. GSL currently operates

three modern and fully integrated distilleries at Behror, Rajasthan and Samalkha and

Hisar, Haryana. It is one of the largest and most efficient grain based distilleries in India

with highest alcohol recovery per unit of grain.

Globus Spirits Limited is having an existing 120 KLPD Grain based Distillery along with 3.5

MW Co-Gen Power Plant at Industrial Park, Panagarh, District Burdwan, West Bengal.

Environmental Clearance for the same has been obtained from MoEFCC, New Delhi vide

Letter No. J-11011/337/2013- 1A II (I) dated 15th May, 2015.

The company is now proposing Expansion of Existing Grain Based Distillery (120 to 240

KLPD) & Co-Generation Power Plant (3.5 to 8.0 MW) by installation of Unit II – 120 KLPD

Grain Based & 4.5 MW Co-Generation Power Plant within their existing plant premises at

Industrial Park, Panagarh, District Burdwan, West Bengal.

As per EIA Notification dated 14th September, 2006 and as amended from time to time,

the project falls under Category “A”, Project or Activity 5(g) (i) [Non-Molasses based

Distilleries ≥ 60 KLPD].

Salient Features of the Project

S. NO.

PARTICULARS DETAILS

A. Nature & Size of the Project

Units Existing Capacity

Proposed Unit II

Total Capacity after Proposed expansion

Grain Based Distillery

120 KLPD 120 KLPD 240 KLPD

and

Co-generation Power Plant (MW)

3.5 MW 4.5 MW 8.0 MW

B. Category of the Project

As per EIA Notification dated 14th Sept., 2006 & as amended from time to time; this project falls under Category “A”, Project or Activity - 5(g) (i) [Non-Molasses based Distilleries ≥ 60 KLPD]

C. Location Details




Village Plot No B7, Panagarh Industrial Park (West Bengal Industrial Development Corporation Limited)

District Burdwan

State West Bengal

Latitude 23026’06.93’’ N to 23026’20.22’’ N

Longitude 87030’47.09’’ E to 87030’56.50’’ E

D. Area Details

Total Plant Area o Existing plant area: 18.81 Acres (7.61 ha)

o No additional land is required for the proposed expansion, as the same will be done within the existing plant premises.

Greenbelt / Plantation Area (ha)

6.2 acre (2.51ha) i.e. 33% of the project area

E. Environmental Setting Details (with approximate aerial distance & direction from plant site)

1. Nearest Village Kotachandipur (~0.5 km , West direction)

2. Nearest City Panagarh (~ 5.5 km , West direction)

3. National Highway/State Highway

NH-2 (~1.8 km, SSW direction)

4. Nearest Railway Station Panagarh (~ 5.5 km , West direction)

5. Nearest Airport Kolkata Airport (~130 km, SE direction)

6. National Parks/ Wild Life Sanctuaries / Biosphere Reserves within 10 km radius

No National Park/ Wild Life Sanctuary/ Biosphere Reserve lies within 10 km radius of the proposed project site.

7. Reserved / Protected Forest within 10 km radius (Boundary to boundary distance)

o Khandari PF (~0.5 km, NNE direction)

o Baradoba PF(~3.5 km , North direction)

o Bilaspur PF (~4.0 km , NNW direction)

o Radhaballabpur PF (~4.0 km , ENE direction)

o Premganj PF (~5.0 km , NNE direction)

o Amarargarh PF (~6.0 km , East direction)

o Kuldiha PF (~6.2 km , NE direction)

o Lakshminarayanpur PF (~6.5 km, ENE direction)

o Pratappur PF (~6.5 km , ENE direction)

o Durgapur PF (~7.5 km , NNW direction)

o Babuisol PF (~7.5 km , NE direction)

o Dombandhi PF (~8.0 km , ENE direction)

o Ramharipur PF (~8.5 km , NE direction)

o Suta PF (~8.5 km , East direction)

o Bhalki PF (~9.0 km , ENE direction)

8. Defense installations o Defense Research & Development Organization (DRDO) (~2.5 km, South to SE Direction)

o Panagarh Air Force Base (~ 9.0 km, WNW Direction)

9. Nearest Water Bodies o Panagarh Branch Canal (~0.2 km, North direction)

o Left Bank Main Canal (~4.8 km, SW direction)




o Damodar River (~7.5 km , SW direction)

o Kunur Nadi (~ 9.0 km , North direction)

10. Seismic Zone Seismic Zone-III as per IS: 1893 (Part-I) : 2002

F. Cost Details

Total Cost of the Proposed Expansion Project

Rs. 120 Crores

Cost for Environment Management Plan

o Capital Cost - Rs. 20.0 Crores

o Recurring Cost - Rs. 2.0 Crores / annum.

G. Basic Requirements for the project

Existing Additional for proposed Capacity

Expansion

Total after proposed Capacity Expansion

Water Requirement (KLD)

1205 1205 2410

Source: Ground Water

Power Requirement (MW)

3.0 4.0 7.0

Source: Co-Generation Power Plant & D.G set - 2x1250 KVA & 2X 750 KVA D. G. Sets will be used after the proposed expansion for the power back up.

Man Power Requirement

100 100 200

Source: Unskilled / Semi-Skilled - Local Area; Skilled - Outside West Bengal

H. Product Rectified Spirit, Extra Neutral Alcohol & IMFL/CL Bottling

I. By-product DDGS & CO2

J. Working Days 350 Days per Annum

1.1 ENVIRONMENTAL MANAGEMENT PLAN

Particulars DETAILS

Air Quality Management

� Stacks of 52 m height equipped with ESP have been installed with the boiler to control the particulate and gaseous emissions due to combustion of fuel.

� ESP will be installed with the proposed Boiler to keep the emissions below permissible level after proposed expansion & installation.

� CO2 generated during the fermentation process is being/will be collected by utilizing CO2 Scrubbers and sold to authorized vendor.

� All the roads are concreted to control the fugitive dust emissions.

� Online Stack Monitoring system is already in place and operational.

� Greenbelt is being/will be developed all around the plant boundary and the same will be maintained.

Water Management

� The Grain based distillery is being/will be based on “Zero Effluent Discharge”.

� Grain Slops (Spent Wash) is being/will be taken through Centrifuge Decanters for separation of Suspended Solids separated as Wet Cake and which goes as cattle feed as it contains high protein. (Also known as DWG – Distillers Wet Grains)




� Thin Slops from the Decanter Centrifuge is being/will be partly recycled back to process (30-35%) and partly taken to Thins Slops Evaporation Plant for concentration of remaining solids to form a Syrup. This Syrup is also mixed into the Wet Cake coming out of Centrifuge and forms part of Cattle Feed. (Also known as Soluble - Collectively known as DWGS).

� DWGS Drier - Wet cake / DWGS is being passed through steam tube bundle drier for drying into cake with 10 - 12% moisture (max.) to give higher shelf life. Solid dry cakes are being obtained finally.

� The Process condensate is being / will be cooled and collected into a neutralization tank with sufficient residence time. After Neutralization and filtration (UF+RO) this process condensate will be recycled into process use.

� Domestic waste water generated from the plant is being/will be disposed off in soak pits via septic tanks.

� Rain Water harvesting is being/will be done within the existing plant premises.

Noise Management

� Personal Protective Equipment like earplugs and earmuffs is being / will be provided to the workers exposed to high noise level.

� D.G sets are being /will be provided with acoustic to control the noise level within the prescribed limit.

� Proper maintenance, oiling and greasing of machines at regular intervals is being / will be done to reduce generation of noise.

� Green Belt of appropriate width inside the plant premises and at the plant boundary has been developed.

� Regular monitoring of noise level is being / will be carried out and corrective measures in concerned machinery are being/will be adapted accordingly to the possible extent.

Solid Waste Management

� Solid waste generated would be wet cake, yeast sludge and ash from the boiler.

� Solid waste from the Grain based operations generally comprises of Fibres and proteins in the form of DDGS, which are being / will be ideally used as Cattle Feed.

� Ash from the Boiler is being / will be sold to Brick/Cement manufacturers.

� Yeast sludge is being / will be sent to the Sludge Drying Beds or may be added to the Wet Cake.

� Used oil & grease generated from plant machinery/Gear boxes as hazardous waste are being / will be sold out to the CPCB authorized recycle.

Odour Management

� Adequate greenbelt all around the periphery of the plant.

� Efficient CO2 scrubbing to avoid carry over of alcohol vapours & other fumes.

� DWGS Dryer is being/will be installed for complete drying of solids.

� Better housekeeping is being/will maintain good hygiene condition by regular steaming of all fermentation equipment.

� Longer storages of any product/by-products will be avoided & use of efficient biocides to control bacterial contamination.

� Regular use of bleaching powder/formalin in the drains to avoid generation of putrefying micro-organisms.

Green belt Development/ Plantation

� Green belt development in and around the plant site helps to attenuate the pollution level.

� Out of the total plant area approx. 33% land is being / will be developed as green belt/plantation.




� Green belt has been developed as per Central Pollution Control Board (CPCB) guidelines.

� Native species have been planted in consultation with the local DFO.

2.0 INTRODUCTION OF THE PROJECT/ BACKGROUND INFORMATION

(i) Identification of Project and Project Proponent

Applicant : M/s Globus Spirits Limited.

Registered Address : F-0, Ground Floor, The Mira Corporate Suites, Plot

No. 1 & 2, Ishwar Nagar, Mathura Road, New Delhi.

Globus Spirits Limited has enjoyed a good track record in the business of manufacture,

marketing and sale of Indian Made Foreign Liquor (IMFL), Industrial Alcohol comprising

Rectified Spirit & Extra –Neutral Alcohol and Country Liquor.

With headquarter in Delhi, the company markets its own IMFL brands in North Indian

states of Rajasthan, Haryana and Uttar Pradesh and also in union territory of Chandigarh.

Company also proposes to launch IMFL brands in three more states in North India. In

South India it is already selling in Kerala, Andhra Pradesh and Karnataka. The company

also has an extensive brand portfolio of its own brands in the country liquor segment.

Globus Spirits Limited is having an existing 120 KLPD Grain based Distillery along with 3.5

MW Co-Gen Power Plant at Industrial Park, Panagarh, District Burdwan, West Bengal.

Environmental Clearance for the same has been obtained from MoEFCC, New Delhi vide

Letter No. J-11011/337/2013- 1A II (I) dated 15th May, 2015.

(ii) Brief description of nature of the project

The company is now proposing Expansion of Existing Grain Based Distillery (120 to 240

KLPD) & Co-Generation Power Plant (3.5 to 8.0 MW) by installation of Unit II – 120 KLPD

Grain Based & 4.5 MW Co-Generation Power Plant within their existing plant premises at

Industrial Park, Panagarh, District Burdwan, West Bengal.

The Proposed expansion capacity of 120 KLPD will be Grain based alcohol using Grain as

raw materials which are abundantly available in the state. The Project is based on zero

effluent discharge. The distillery has put up the most modern technology for treatment of

distillery spent wash which ensures Zero discharge of distillery effluents. The distillery

unit will generate its own electricity by proposed Co-Generation power plant of 8.0 MW.

As per EIA Notification dated 14th September, 2006 and as amended from time to time,

the project falls under Category “A”, Project or Activity 5(g) (i) [Non-Molasses based

Distilleries ≥ 60 KLPD].

(iii) Need for the project and its importance to the country and or region

Advancement in science and technology has created so many products that have

enhanced the quality of human life in every passing year. The human race is largely




dependent on industrialization for up gradation in quality of life. Progress of the nation is

judged through its economic growth which is largely dependent on industrial

productivity. In Indian economy (which is agro based) many industries are dependent

over agricultural produce for production of luxury and need based commodities. Alcohol

has assumed a very important place in the Country’s economy. It is a vital raw material for

a number of chemicals. It has been a source of revenue by way of excise duty levied by

the State Government on alcohol liquors. It has a potential as fuel in the form of power

alcohol for blending with petrol in the ratio of 20:80. The use of alcohol for the purpose

of potable liquor is as high as its use for industrial purposes. The Country Liquor is mainly

used by the common masses.

According to analysts, the Indian alcoholic beverages industry is expected to witness

accelerating growth in coming years with the consumer base likely to expand amidst

rising disposable income. The domestic alcoholic drinks market is estimated around $13

billion and has been growing at a compounded annual growth rate in excess of 10% in the

past few years. The growth rate is higher than other major Asian markets like China and

South Korea, etc.

In the path of company’s growth and development this project will serve as yet another

milestone.

(iv) Demand- Supply Gap

The total production of ENA from molasses and grain is 148 crores litres per annum. The

total requirement of ENA for IMFL in India is 120 crores litres (35% ENA from grain & 65 %

from molasses). Next five year projection ENA from grain 60 % & from molasses 40 %

Alcohol produced from molasses also used by oil companies 30.50 crores in the year of

2014-15. Projection for the year 2015-16 – 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. Thus the huge demand of ENA made out of grain will arise.

(v) Import vs. Indigenous Production

Indian market could not meet present alcohol demand. So they import alcohol 5-7% of

total demand. As far as ENA production is concerned, Indian market play a vital role at

both domestic & international level. So they require produce the more alcohol to meet

the demand.

(vi) Export Possibility

There will be possibility of export of alcohol to African, European & Asian countries.

(vii) Domestic / Export Markets




Market depends on excise Department.

(viii) Employment Generation (Direct and Indirect) due to the project

The total manpower requirement after the proposed expansion & installation project will

be 200.

3.0 PROJECT DESCRIPTION

(i) Type of Project including interlinked and independent projects, if any.

There are no interlinked projects related to this expansion project.

(ii) Location (map showing general location, specific location, and project boundary &

project site layout) with coordinates




Figure - 1: Location Map




(iii) Key Plan

Figure 2: Environmental Settings of 10 km radius area




(iv) Details of alternative sites consideration and basis of selecting the proposed site,

particularly the environmental considerations gone into should be highlighted.

Since the proposed expansion will be done within the existing plant premises and no

additional land will be required; therefore, no alternative site has been considered.

(v) Size or magnitude of operation

Proposed Expansion of Existing Grain Based Distillery (120 to 240 KLPD) & Co-Generation

Power Plant (3.5 to 8.0 MW) by installation of Unit II – 120 KLPD Grain Based & 4.5 MW

Co-Generation Power Plant within their existing plant premises at Panagarh Industrial

Park, Panagarh, District Burdwan, West Bengal. The process includes basic raw material

requirement, sizing of equipment, utilities & services, infrastructure facilities & sources of

waste generation, their quantity, treatment & safe disposal of the waste.

(vi) Project Description with Process Details

Project Description

S. No.

Units Existing Capacity

Additional Capacity for Expansion

Total Capacity after proposed Expansion

1. Grain based Distillery

120 KLPD 120 KLPD 240 KLPD

2. Co-Generation Power Plant

3.5 MW 4.5 MW 8.0 MW

Process Description

Distillery Unit - Production from Grain:

• Grain storage

• Grain cleaning, milling and flour handling

• Slurry preparation & liquefaction

• Multi pressure distillation

• Alcohol (ENA & IA) daily receivers & bulk storage

• MEE & Dryer

A) Grain Storage Silos, Cleaning, Handling and Milling Section:

Grain is received from various sources and is pre-cleaned off stones, husk, etc. and then

stored in specially designed storage silos. Grains are continuously lifted from the bottom

of the silos and screened followed by removal of stones in de-stoner and iron matters in

magnetic separators. Cleaned Grains are then milled using dry milling process in Hammer

Mills. The flour is fed through the bucket elevator and conveyed to the Batch Tipping

Machine through a Screw Conveyor.

B) Liquefaction Section

Grain flour mixed with recycle streams and water in Pre-masher and slurry has been fed to

Liquefaction tank. Required temperature has been maintained by applying steam through




steam sparger in liquefaction tank. The cooking process, accomplished in the above

manner, converts the slurry into a hydrated, sterilized suspension (as starch molecule is

solubilized) and is therefore susceptible to enzyme attack for liquefaction. The liquefied

mash is cooled in slurry cooler and transferred to Fermentation section.

C) Fermentation Section

The purpose of fermentation is to convert the fermentable substrate into alcohol. To

prepare the mash for fermentation, it is diluted with water. Yeast is added in sufficient

quantity to complete fermentation to produce alcohol.

At the start of the cycle, the Fermenter is charged with mash and contents of the Yeast

Activation Vessel (Pre-fermenter). Significant heat release takes place during

fermentation. This is removed by passing the mash through heat exchangers to maintain

an optimum temperature. The recirculation pumps also serve to empty the Fermenters

into Beer Well. CO2 evolved during fermentation carries along with it some entrained

alcohol. This CO2 is taken to a CO2 scrubber where it is washed with water to remove the

entrained alcohol. The scrubbed CO2 can then be taken to CO2 plant or vented out. After

emptying of Fermenter, it is cleaned with CIP using cleaning nozzles. After CIP Fermenter

is ready for next batch to be filled.

D) MPR Distillation Wash to ENA:

Multi-Pressure Distillation system has eight Distillation columns operating at various

pressure conditions. Heat energy from columns operating under high pressure is utilized

for columns operating under low pressure to optimize the operation for energy

consumption. Following Columns will be under operation

• Analyser Column

• Degasifying Column

• Pre-Rectifier Column cum

• Exhaust Column

• Extractive Distillation Column

• Rectifier cum Exhaust Column

• Recovery Column

• Simmering Column

Pre-heated fermented wash is fed at the top of the Degasifying column. Analyser Column

is provided with Reboiler. Top vapors of Analyser column containing all the alcohol in the

wash are sent to Pre-Rectifier column. Rest of the fermented wash flows down the

Analyser column and is taken out as thick slops from Analyser 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 column. Dilution water

is fed to this column. The Extractive Column operates on the principle of inversion of

relative volatility. Low boiling impurities are separated in the Extractive Distillation

Column & bottom is sent to Rectifier cum Exhaust column. The Rectifier/Exhaust column

concentrates the alcohol to 96% v/v. The spirit is drawn from the upper trays of the

Rectification Column. Fusel oil build up is avoided in the Rectifier cum exhaust column by

withdrawing side streams (fusel oils). ED condensates, fusel oil draw from R/E 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 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 drawn from the

Simmering Column is taken to the receiver after cooling in ENA cooler.

E) Decantation Section Excluding Decanter Centrifuges

Decantation section comprises of a Centrifuge Decanters (Client scope) for separation of

suspended solids from Thick slop coming out of Grain Distillation Plant. Wet cake is

removed from bottom of Decanter. Thin slops coming out of Decanter are collected in a

tank and partly recycled into the process & Evaporation for further concentration. The

concentrated thin slops called as Syrup is mixed with Wet cake and sold in wet form as

cattle feed (DWGS) or the entire mixture can be dried in a DWGS Dryer and then sold in

dry form as Cattle feed (DDGS).

F) Integrated Evaporation

The suggested treatment scheme is a Multi Effect Evaporation Plant for Thin Slop

Evaporation. Shell & Tube type Evaporators with highly efficient liquid distributor working

on the principle of Falling Film and Forced circulation Evaporation has been used.

The product at the desired concentration of 40%w/w Total Solid is obtained at the outlet

of the final effect. Each effect is provided with recirculation cum transfer pumps. The

condensate from surface condensers is collected in a common condensate pot. The

condensate is transferred for further treatment / drain by using centrifugal pump. The

system operates under vacuum. Water-ring vacuum pumps are used to maintain a desired

vacuum. Cooling water from cooling tower is used in the surface condensers for

condensing the vapours.




G) DWGS Dryer Section

Wet distiller’s grains shall be fed into the dryer housing at controlled rate through a

suitable feeding system. The Rotary Bundle is enclosed in an insulated dryer housing and

on its outer flights are fixed. Dry, saturated steam is to be supplied to the bundle through

rotary joint at one end & the condensate is discharged through rotary joint mounted of

another end. During the course of rotation, these flights pick up the material and shower

them on to the tube bundles. The heat transfer is primarily by conduction. The water

vapors are exhausted through an Exhaust Blower & passed through a cyclone separator

for separating fines. Dry product partially recycled back to feed conditioner for feed

conditioning through Product Screw & Recycle Conveyor. Entire operation of the Dryer is

controlled through Local Indication cum Control panel.

G) Process Condensate Treatment Section

The process condensate from the evaporation section is treated in this unit and this

treated condensate is then recycled back to process thus reducing the fresh water

consumption.




Figure - 3: Process flow chart For Grain Based Distillery




B) Power Co-Generation (3.5 MW + 4.5 MW = 8.0 MW)

OPERATIONS

Proposed 4.5 MW co-generation plant consists of a high pressure water tube steam boiler

extraction cum condensing steam turbine. Fuel in the steam boiler will be burnt with the

help of air in the boiler furnace. Water will be circulated in the boiler drum and tubes thus

getting heated by the flame burning in the boiler furnace. Water comes out of the boiler

drum located at the top of the boiler as steam. Flue gases rise in the boiler furnace and

come in contact with the steam coming out of boiler drum. Steam after coming in contact

with flue gases gets heated up further thus getting superheated. Super heated steam

leaves the boiler in a pipe. Flue gases after super heating the steam pass through

economizer where they pre-heat the boiler feed water before it enters the boiler drum.

After economizer, flue gases pass through air pre-heaters where they heat the air which is

fed to the boiler furnace for burning the fuel. After air pre heaters flue gases pass

through an ESP where the dust particles are collected on charged electrodes. The dust is

collected from the bottom of the ESP.

High pressure superheated steam from boiler is passed through a steam turbine, which is

used for distillery process operations. While passing through the turbine, the high

pressure and temperature steam rotates the turbine rotor and an electric alternator

mounted on the same shaft. Electric power is generated by the alternator. This electric

power generated is consumed in house i.e. for running the distillery and utilities like

boilers auxiliaries etc.

Figure 4: Process flow chart for Proposed Co-generation Power Plant




vii) Raw material required along with estimated quantity, likely source, marketing

area of final products, mode of transport of raw material and finished product.

(a) Raw Material Requirement

The basic raw material for the manufacturing of ENA/RS/Ethanol will be Grain. In the

present scenario, grains with different starch content are used like broken Rice, sorghum,

baira, maize etc. The process requires the above grains to be milled into specific flour

size. Small quantity of sulphuric acid is sometimes required. The raw material for the

boiler fuel will be Coal/Rice Husk.

S. No.

Particular Requirement Source & Mode of Transportation Existing

Additional for proposed expansion

Total after proposed expansion

1 Grain - Broken Rice, Sorghum, Baira, Maize

etc. (MT/day)

295 295 590 Through Grain suppliers By

road/Rail

2. Chemicals (kg/day) Near-by Markets /by road Sodium Hydroxide

(kg/day) 1000 1000 2000

Liquefying Enzyme (kg/day)

129 129 258

Saccharifying Enzyme (kg/day)

144 144 288

NH2-CO- NH2 (kg/day)

330 330 660

Antifoam Agent (kg/day)

65 65 130

Yeast (Active Dry Yeast/Distiller’s Yeast

(kg/day)

200 200 400

(b) Fuel Requirement

Name of Raw

Material

Requirement Source & Mode of Transportation Existing (TPD) Additional for

Proposed Expansion (TPD)

Total Quantity after Proposed Expansion

(TPD)

Coal (Use 100%)

160 175 335 From Authorized Dealer by Truck

or

Rice Husk (Use 100%)

205 260 465




(viii) Resources optimization/ recycling and reuse envisaged in the project, if any,

should be briefly outlined.

The waste water generated from the industry is being /will be properly treated through

most modern technology i.e. Decantation followed by Evaporation with the Dryer; and

the condensate water is being / will be recycled back in the process & also, reused for

greenbelt development, which is being / will be results in ‘’Zero- Discharge’’.

(ix) Availability of water it’s source, energy /power requirement and source should be

given.

(a) Water Requirement and Source

Existing water requirement for 120 KLPD Grain Based Distillery is 1205 KLPD.

Existing Water requirement

Additional water requirement for Expansion

Total water requirement after expansion

1205 KLPD 1205 KLPD 2410 KLPS

Source of Water: Ground Water.

(b) Power Requirement and Source

Existing power requirement is 3.0 MW and additional 3.0 MW of power will be required

for proposed Expansion. Thus, the total power requirement after proposed expansion &

installation project will be 6.0 MW.

Source: 8.0 MW Co-generation Power Plant & D.G Sets (for back-up).

(c) Steam Requirement

Existing steam requirement is 32 TPH which is being met by boiler of capacity (35 TPH)

and after proposed expansion & installation will be 64 TPH of steam will be required

which will be met by existing 35 TPH boiler & proposed 40 TPH boiler.

(d) Boiler Details

Existing and proposed boiler details are mentioned in the table given below:

S. No. Boiler Details Existing Proposed

1. Boiler Capacity 35 TPH 40 TPH

2. Type of Fuel Coal or Rice Husk Coal or Rice Husk

3. Stack Height 52 metres 52 meter

4. Pollution Control Equipment Measures ESP ESP

(e) Details regarding the D.G. Sets

Two D.G. sets of 1250 KVA & 750 KVA have already been installed for the power backup

and after proposed expansion additional 2 D.G sets of 1250 KVA & 750 KVA will be

installed. Details regarding the D.G. Sets are mentioned in the table given below:




DETAILS REGARDING THE D.G.SETS

S. No. Details Existing Proposed

1. Type of Fuel Diesel Diesel

2. Capacity 1 x 1250 KVA & 1 x 750 KVA 1 x 1250 KVA & 1 x 750 KVA

3. Stack Height (above roof level) As per CPCB guidelines As per CPCB guidelines

(x) Quantity of waste to be generated (liquid and solid) and scheme for their

management/disposal

o The proposed expansion & installation project is being/will be based on “ZERO

EFFLUENT DISCHARGE”.

o Grain Slops (Spent Wash) is being/will be taken through Centrifuge Decanters for

separation of Suspended Solids separated as Wet Cake.

o Thin Slops from the Decanter Centrifuge are being/will be partly recycled back to

process (30-35%) and partly taken to Thins Slops Evaporation Plant for

concentration of remaining solids to form a Syrup. This Syrup is mixed with the Wet

Cake coming out of Decanter Centrifuge and forms part of Cattle Feed. (Also

known as Distillers Wet Grain Solubles - Collectively known as DWGS)

o DWGS is being/will be taken to a dryer operating on steam and is dried to make it

DDGS – Distillers Dried Grain Solubles.

o The process condensate is being/will be cooled and collected into a neutralization

tank with sufficient residence time. After Neutralization, this process condensate is

being/will be recycled into process and is used for green belt development within

the complex.

o Solid waste from the Grain based operations generally comprises of Fibres and

proteins in the form of DDGS, which are being / will be ideally used as Cattle Feed.

o Fly Ash from the Boiler is being / will be sold to Brick/Cement manufacturers.

o Used oil & grease generated from plant machinery / Gear boxes & D.G. Set is being /

will be partly used in oiling & greasing as lubrication of external parts of machinery

& partly is being / will be sold to the CPCB authorized recycler.

4.0 SITE ANALYSIS

(i) Connectivity

The project site is located at Panagarh Industrial Park, Panagarh, District Burdwan, West

Bengal and is well connected with NH-2 (~ 1.8 Km in SSW direction) from the project site.

Nearest Railway Station is Panagarh, which is about 5.5 km in West direction from the

project site. Nearest Airport is at Kolkata which is approx. 130 km in SE direction. It has an




easy access to raw material availability and other infrastructural facilities e.g. land, power,

water, transport and communication, approach through road & access distances from the

nearest highway, railway station etc.

(ii) Land from Land use and Land ownership

Total plant area is 18.81 Acres (7.61 ha). Since, the proposed expansion & installation will

be done within the existing plant premises, thus, no additional land is required for the

same.

(iii) Topography

The topography of the area is almost flat.

(iv) Existing land use pattern (agriculture, non-agriculture, forest, water bodies

(including area under CRZ)), shortest distances from the periphery of the project

to periphery of the forests, national park, wild life sanctuary, eco sensitive areas,

water bodies (distance from the HFL of the river), CRZ. In case of notified

industrial area, a copy of the Gazette notification should be given

Environmental Settings of the Area

S. NO. PARTICULARS DETAILS

1. Nearest Village Kotachandipur (~0.5 km , West direction)

2. Nearest City Panagarh (~ 5.5 km , West direction)

3. National /State Highway NH-2 (~1.8 km, SSW direction)

4. Nearest Railway Station Panagarh (~ 5.5 km , West direction)

5. Nearest Airport Kolkata Airport (~130 km, SE direction)

6. National Parks/ Wild Life Sanctuaries / Biosphere Reserves within 10 km radius

No National Park/ Wild Life Sanctuary/ Biosphere Reserve lies within 10 km radius of the proposed project site.

7. Reserved / Protected Forest within 10 km radius (Boundary to boundary distance)

o Khandari PF (~0.5 km, NNE direction)

o Baradoba PF(~3.5 km , North direction)

o Bilaspur PF (~4.0 km , NNW direction)

o Radhaballabpur PF (~4.0 km , ENE direction)

o Premganj PF (~5.0 km , NNE direction)

o Amarargarh PF (~6.0 km , East direction)

o Kuldiha PF (~6.2 km , NE direction)

o Lakshminarayanpur PF (~6.5 km, ENE direction)

o Pratappur PF (~6.5 km , ENE direction)

o Durgapur PF (~7.5 km , NNW direction)

o Babuisol PF (~7.5 km , NE direction)

o Dombandhi PF (~8.0 km , ENE direction)

o Ramharipur PF (~8.5 km , NE direction)

o Suta PF (~8.5 km , East direction)




o Bhalki PF (~9.0 km , ENE direction)

8. Defense installations o Defense Research & Development Organization (DRDO) (~2.5 km, South to SE Direction)

o Panagarh Air Force Base (~ 9.0 km, WNW Direction)

9. Nearest Water Bodies o Panagarh Branch Canal (~0.2 km, North direction)

o Left Bank Main Canal (~4.8 km, SW direction)

o Damodar River (~7.5 km , SW direction)

o Kunur Nadi (~ 9.0 km , North direction)

10. Seismic Zone Seismic Zone-III as per IS: 1893 (Part-I) : 2002

(v) Existing Infrastructure

Total plant area is about 18.81 Acres (7.61 ha). Proposed expansion & installation will be

done within the existing plant premises. Existing infrastructure comprises of Grain based

Distillation & Fermentation unit and basic utilities such as water, power, etc.

(vi) Soil classification

Different types of soil are encountered in different topographical biological and

hydrological as well as geological condition within the Burdwan district. In the west

coarse gritty soil blended with rock fragments is formed from the weathering of

pegmatites, quartz veins and conglomeratic sandstones, whereas sandy soil characteristic

of granitic rocks and sandstones. This soil is of reddish colour, medium to course in

texture, acidic in reaction, low in nitrogen, calcium, phosphate and other plant nutrients.

Water holding capacity of this soil increases with depth as well as with the increase of clay

portions.

Towards the east alluvial soil attains an enormous thickness in the low level plains to the

east. This alluvial soil is formed of alluvium brought down by the Ajay, Damodar,

Bhagirathi and numerous other rivers. These soils are sandy, well drained and slightly

acidic in nature.

(vii) Climatic data from secondary sources

The winter season starts from about middle of November and continues till the end of

February. March to May is dry summer; July to September is monsoon while October to

November is autum. The normal rainfall is 1442 mm and the average rainfall is 1173 mm.

Maximum rainfall in a day is 150 mm while bulk of rainfall occurs in the months of July-

September.

(viii) Social Infrastructure available

There are schools, College, dispensaries, hospitals, Post offices, Banks, Market and

places of worship in nearby area of the project site.




5.0 PLANNING BRIEF

(i) Planning Concept (type of industries, facilities, transportation etc.) Town and

country Planning/Development authority classification.

The existing unit is Distillery industry and proposed expansion & installation will be done

within the existing plant premises. Facilities required for the proposed expansion &

installation project will be provided as per requirement. Transportation of raw material

and final product is being / will be done by road.

(ii) Population Projection

Temporary influx of people will be there as the managerial and supervisory staff will

generally be outsider. A projection may be made by a governmental organization, or by

those unaffiliated with a government.

(iii) Land use planning (breakup along with green belt etc)

Total Plant area is 18.81 Acres (7.61 ha). Proposed expansion & installation project will be

set up in the existing plant premises. No additional land will be required. About 33 % of

the total plant area is being/will be covered under green belt & plantation in order to

reduce dust & noise pollution levels & to increase aesthetic beauty of the area.

(iv) Assessment of infrastructure demand (Physical & Social)

Globus Spirits Ltd. has assessed the demand of infrastructure (Physical & Social) in

nearby area of the plant site and development activities are being undertaken under

corporate social responsibilities program for rural development initiatives for the

upliftment of the nearby communities from time to time.

(v) Amenities/Facilities

Globus Spirits Ltd. has developed and will further develop the Amenities/Facilities in

nearby area of the Plant site as per requirement of local people of the nearby area under

corporate social responsibilities programs.

6.0 PROPOSED INFRASTRUCTURE

(i) Industrial Area (Processing Area)

For the proposed expansion of Grain based Distillery from 120 to 240 KLPD & Co-

generation Power Plant from 3.5 MW to 8.0 MW, additional infrastructure will be built

which includes grain storage, starch conversion, fermentation, distillation, boiler, turbine,

evaporator & dryer for Unit II – 120 KLPD Grain Based & 4.5 MW Co-Generation Power

Plant.

(ii) Residential area (Non Processing area)

No residential area is envisaged.




(iii) Green Belt

About 33 % of the total plant area is being/will be covered under green belt & plantation in

order to reduce dust & noise pollution levels & to increase aesthetic beauty of the area.

(iv) Social Infrastructure

Proposed expansion & installation project will result in growth of the surrounding areas

by ancillary development and supporting infrastructure in the region.

(v) Connectivity

The site is well connected with communication facilities like telephone, fax, and wireless

as such no constraints are envisaged in this aspect.

(vi) Drinking Water

7 m3/ day water will be required for drinking purpose after proposed expansion &

installation project which will be sourced from Ground Water.

(vii) Sewage Treatment System

The waste water generated from the sanitary blocks is being/will be disposed off in soak

pit via septic tank.

(viii) Industrial Waste management

The grain based distillery project is being / will be based on “ZERO DISCHARGE”.

(ix) Solid Waste Management

o Solid waste from the Grain based operations generally comprises of Fibres and

proteins in the form of DDGS, which are being / will be ideally used as Cattle Feed.

o Ash from the Boiler is being / will be sold to Cement & Brick manufacturers.

(x) Power requirement and source

Existing power requirement is 3.0 MW and additional 4.0 MW. Thus, the total power

requirement after proposed expansion project will be 7.0 MW.

Source: Co-generation Power Plant & D.G Sets (for Power Back-Up).

7.0 REHABILITATION AND RESETTLEMENT (R & R) PLAN

(i) Policy to be adopted (Central/State) in respect of the project affected persons

including home oustees, land oustees and landless labourers (a brief outline to be

given).

Proposed expansion & installation will be done within the existing plant premises. No

additional land is required for the same and hence, Rehabilitation & Resettlement is not

applicable.




8.0 PROJECT SCHEDULE AND COST ESTIMATES

(i) Likely date of start of construction and likely date of completion (time schedule

for the project to be given).

The project will start only after obtaining Environmental Clearance and other statutory

permissions. Project will be completed in 14 months after getting all the regulatory

approvals.

(ii) Estimated project cost along with analysis in term of economic viability of the

project.

� Total cost of the Project: Rs. 120 Crores

� Cost for Environment Protection Measues:

� Capital Cost: Rs. 20.0 Crores

� Recurring Cost/annum: Rs. 2.0 Crores / annum.

9.0 ANALYSIS OF PROPOSAL

(i) Financial and social benefits with special emphasis on the benefit to the local

people including tribal population, if any, in the area.

Proposed expansion & installation project will result in growth of the surrounding areas

by increasing ancillary development and supporting infrastructure. Special emphasis on

Financial and Social benefits will be given to the local people including tribal population, if

any, in the area.

Development of social amenities will be in the form of medical facilities, education to

underprivileged and creation of self help groups.

West Bengal state will get revenues in terms of taxes. Business opportunities for local

community will be available like transport of alcohol to market, fly ash transport to Brick

manufactures, maintenance & house-keeping contract work etc.

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