proposed 150 klpd molasses/grain based distillery along with … · esp/bag filter with stack of...

Proposed 150 KLPD Molasses/Grain based Distillery along with 7.0 MW Co-generation power plant & 10 KLPD Malt Spirit Plant

within existing non-operational Distillery Plant

At Village Satrod Khas, Tehsil & District Hisar, Haryana

Pre - Feasibility Report

Associated Distilleries (A Unit of Globus Spirits Limited) 1

PRE - FEASIBILITY REPORT

1.0 EXECUTIVE SUMMARY:

(I) Introduction

Associated Distilleries (A Unit of Globus Spirits Limited) installed 25 KLPD distillery and IMFL/CL

Bottling Plant at Village Satrod Khas, Tehsil & District Hisar, Haryana.

Presently, the distillery unit is non- operational and only IMFL/CL bottling is being carried out in

the plant. 25 KLPD distillery plant was commercially non- viable so the company suspended its

operation. But now because of the increasing demand of ethanol in Indian market, the company

intends to restart the plant operations and is thus proposing 150 KLPD grain/ molasses based

distillery along with 7 MW Co-generation power plant & 10 KLPD Malt Spirit Plant within existing

plant premises. The old redundant machinery will be replaced with the new one.

In view of above, the company is proposing 150 KLPD Molasses/Grain based Distillery along with

7.0 MW Co-generation power plant & 10 KLPD Malt Spirit Plant within existing non-operational

Distillery Plant at Village Satrod Khas, Tehsil & District Hisar, Haryana.

As per EIA Notification dated 14th

September, 2006 and subsequent amendments, the project falls

under Category “A”, Project or Activity 5(g).

TABLE – 1

Salient Features of the Project

S. NO. PARTICULARS DETAILS

A Nature & Size of the Project Proposed 150 KLPD Molasses/Grain based Distillery along with 7.0

MW Co-generation power plant & 10 KLPD Malt Spirit Plant within

existing non-operational Distillery Plant

B Category of the Project As per EIA Notification dated 14th

Sep., 2006 and subsequent

amendments; the project falls in Category ‘A’, Project or Activity - 5(g)

Distilleries.

C Location Details

Village Satrod Khas

Tehsil Hisar

District Hisar

State Haryana

Latitude 29008’08.79’’ N to 29

008’17.71’’ N

Longitude 75047’41.78’’ E to 75

048’00.27’’ E

Toposheet H43P16 and H43P12

D Area Details






Total Plant Area o Existing plant area: 8.0 hectares (19.77 Acres)

o No additional land is required for the project, as the same will be

done within the existing non-operational Distillery Plant.

Greenbelt / Plantation Area 2.64 hectares i.e. 33% of the total plant area has already been

developed as greenbelt & plantation

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

1. Nearest Village Satrod Khas (1 km in SW direction)

2. Nearest City Hisar (4.5 km in West direction)

3. Nearest National Highway /

State Highway

• NH 10 (Adjacent in SW direction)

• NH 65 (7.2 km in West direction)

4. Nearest Railway station Hisar (7 km in West direction)

5. Nearest Airport New Delhi (142 km in SE direction)

6. Reserved Forest (RF)/ Protected

Forest (PF)

Bir Hisar PF (5.0 km in NW direction)

7. National Parks, Reserved Forests

(RF)/ Protected Forests (PF),

Wildlife Sanctuaries, Biosphere

Reserves, Tiger/ Elephant

Reserves, Wildlife Corridors etc.

within 10 km radius

No National Parks, Wildlife Sanctuaries, Biosphere Reserves, Tiger/

Elephant Reserves, Wildlife Corridors etc. lies within 10 km radius of

the plant site.

8. Water Body (within 10 km

radius)

• Balsamand Sub Branch (Bhakra Canal) (Adjacent in East direction)

• Hisar Major Distributary (Western Yamuna Canal) (Adjacent in North direction)

• Dewa Distributary (~ 1.5 km in South direction)

• Petwar Distributary (~ 4.0 km in South direction)

Few minor agricultural canals are also present in 10 km radius area

F Cost Details

Total cost of the project Rs. 125 Crores

Cost for Environment

Management Plan

Capital Cost: Rs. 40 Crores

Recurring Cost: Rs. 4.0 Crores/annum

G Basic Requirements for the project 150 KLPD Distillery Plant

Water Requirement (KLD) 1450 KLPD (1350 KLPD Distillery + 80 KLPD Malt Spirit Plant + 15

KLPD Bottling Plant + Domestic 5 KLPD)

Source: Surface water (Canal water) /ground water






Power Requirement (MW) 4.5 MW

Source: 7 MW Co-generation power plant

Man Power Requirement Regular Basis - 100 & Contract Basis - 200

Source: Unskilled/Semi-Skilled - local area; Skilled–Local & outside

areas

H Product Mix Ethanol / Extra Neutral Alcohol (ENA) / Rectified Spirit (RS) & Power

I By-products During Molasses based operation - CO2

During Grain based operation - DDGS and CO2

J Working Days 365 days/annum

1.1 ENVIRONMENT MANAGEMENT PLAN

Air Management:

� ESP/Bag Filter with stack of adequate height will be installed with the boiler to control the

particulate and gaseous emissions due to combustion of fuel.

� CO2 generated during the fermentation process will be collected by utilizing CO2 scrubbers

and sold to authorized vendors

� Roads within the plant will be concreted to control the fugitive emissions.

� Greenbelt around the periphery and within premises will be maintained.

� Online Stack Monitoring system will be installed.

� Ambient air quality will be regularly monitored to ensure that ambient air quality standards

and suggested limits are maintained.

Water Management:

� The distillery will be based on “Zero Effluent Discharge”.

� During Molasses Based Operation: The spent wash will be concentrated in MEE and the

concentrated spent wash will be mixed with auxiliary fuel and burnt in the incinerator boiler.

Process Condensate will be neutralized and treated in state of art Condensate Polishing

Unit (CPU) and recycled in Fermentation process and for Cooling Tower makeup.

� During Grain Based Operation: Grain Slops (Spent Wash) will be passed through centrifuge

decanters for separation of suspended solids separated as Wet Cake (also known as DWG –

Distillers Wet Grains). Thin Slops from the Decanter Centrifuge will be partly recycled back

to process (20% to 35%) and the balance will be fed to Thin Slop Evaporation Plant for

concentration of remaining solids to form Syrup (35% TS). DWGS Drier: The Wet Cake and

Syrup mixture (DWGS) will be dried in Steam Tube Bundle Dryer for producing DDGS with

8-10% moisture (max.). The DDGS will be utilized as Cattle, poultry and fish feed

ingredients. The process condensate will be treated in condensate treatment plant. The






treated water will be recycled back in cooling tower makeup.

� Domestic waste water generated from the plant will be treated in STP.

� Rain Water harvesting will be done within the plant premises.

Noise Management:

� Personal Protective Equipment like earplugs and earmuffs will be provided to the workers

exposed to high noise level.

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

� Proper maintenance, oiling and greasing of machines at regular intervals will be done to

reduce generation of noise.

� Greenbelt of appropriate width inside the plant premises and at the plant boundary will be

developed.

� Regular monitoring of noise level will be carried out and corrective measures in concerned

machinery are also being done.

Solid Waste Management

� During Molasses based operation: The concentrated spent wash from molasses based

distillery will be burnt in incinerator boiler along with Biomass as fuel (15% coal will also be

used as auxiliary fuel).

� During Grain based operation: Solid waste from the grain based operations generally

comprises of fibres and proteins in the form of DDGS, which will be ideally used as Cattle

Feed. Yeast sludge will be sent to the sludge drying beds or may be added to the wet cake.

� Ash from the boiler will be given to brick or cement manufacturing unit.

� ETP sludge will be dewatered using filter press and will be used as manure.

� Used oil & grease generated from plant machinery/gear boxes as hazardous waste will be

sold out to the CPCB authorized recyclers.

Odour Management

� Adequate greenbelt all around the periphery of the plant.

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

� DWGS dryer will be installed for complete drying of solids.

� Better housekeeping, hygienic conditions will be maintained inside as well as surrounding

areas of the plant.

� Regular use of disinfectants in the drains to avoid generation of putrefying micro-

organisms.

Greenbelt Development / Plantation:

� 2.64 hectares, i.e. ~33% of the plant area is already covered under greenbelt & plantation.

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

� Greenbelt 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:

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.

The company has 5 distillery industries which are situated in the states of Haryana, Rajasthan,

Bihar and West Bengal. Headquarter of the Globus Spirits Limited is situated 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.

Given the new Bio-fuels policy of the government of India, there’s a huge surge in demand for

ETHANOL/ Alcohol in the country. The current capacity is not sufficient to meet this growing

demand in order to meet the ETHANOL targets for blending in petrol as per this policy. Hence we

decided to expand our capacity in order to meet this growing demand. This in turn will help

towards meeting the ETHANOL targets as set by the GOI & will also help provide in increased

employment & investment in the state of Haryana. Please provide us Company details

(ii) Brief description of Nature of the Project:

Associated Distilleries (A Unit of Globus Spirits Limited) has installed 25 KLPD distillery and

IMFL/CL Bottling Plant at Village Satrod Khas, Tehsil & District Hisar, Haryana.

Presently, the distillery unit is non- operational and only IMFL/CL bottling is being carried out in

the plant. 25 KLPD distillery plant was commercially non- viable so the company suspended its

operation. But now because of the increasing demand of Ethanol in Indian market, the company

intends to restart the plant operations and is thus proposing 150 KLPD grain/ molasses based

distillery along with 7 MW Co-generation power plant within existing plant premises. The old

redundant machinery will be replaced with the new one.

In view of above, the company is proposing 150 KLPD Molasses/Grain based Distillery along with

7.0 MW Co-generation power plant & 10 KLPD Malt Spirit Plant within existing non-operational

Distillery Plant at Village Satrod Khas, Tehsil & District Hisar, Haryana

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).

(ii) Need for the Project and its Importance to the Country and/ or Region:

Govt. of India has mandated 10% blending of Ethanol in Petrol by 2022 so as to reduce

dependence on imported Crude Oil and to provide a cleaner fuel. The project will help fulfilling

the demand for ETHANOL. In addition it will provide for employment & investment in the state of

UP.






(iii) Demand- Supply Gap:

The total demand for alcohol in India is as follows

Current in bulk liters (BL) 2022 projected in bulk liters (BL)

Ethanol 330 cr 450 cr

Beverage alcohol 200 cr 250 cr

Industrial alcohol 70 cr 90 cr

TOTAL 600 cr 790 cr

The total demand for alcohol in India is expected to grow from 600 crore bulk liters currently to

790 crore bulk liters by 2022. The current installed capacity is 600 cr liter. Therefore capacity of

another 190 crore bulk liters is required to be set up in the next 3-4 years to meet the rapidly

increasing demand.

(iv) Import vs. Indigenous Production:

India is one of the largest importers of crude oil. The indigenous production of ethanol for

blending in petrol will substitute this imported crude oil.

(v) Export Possibility:

Currently India exports 7.5 Cr Bulk liters of ENA to various countries. As this project can also make

good export quality ENA the same can too be exported to countries in east and west Africa such

as Nigeria, Ghana, Angola, Camaroon, Congo, Kenya, Uganda, Zambia, Sierra Leone, Rwanda,

Tanzania, Togo and Liberia. Also export possibilities of ENA exist to Middle Eastern countries such

as Lebanon, Jordon and Turkey.

(vi) Employment Generation (Direct and Indirect) due to the project:

Direct and indirect employment will be generated due to the project. The total manpower

requirement for the project will be 100 persons on regular basis and 200 persons on contract

basis. Unskilled / semi-skilled manpower will be sourced from the local area and skilled

manpower will be sourced from outside / local.

3.0 PROJECT DESCRIPTION:

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

There are no interlinked projects related to this proposed project.

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

plant site layout) with coordinates






Figure - 1: Location Map

Proposed 150 KLPD Molasses/Grain based Distillery along with 7.0 MW Co-generation power plant & 10 KLPD Malt Spirit Plant within existing non-operational Distillery Plant




(iii) Key Plan

Figure - 2: Key Plan




Pre - feasibility Report


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

site, particularly the environmental considerations gone into should be

highlighted.

The company is proposing 150 KLPD Molasses/Grain based Distillery along with 7.0 MW

Co-generation power plant within existing non-operational Distillery Plant; therefore, no

alternative site has been considered.

(v) Size or magnitude of operation

Proposed 150 KLPD Molasses/Grain based Distillery along with 7.0 MW Co-generation

power plant within existing non-operational Distillery Plant at Village Satrod Khas, Tehsil

& District Hisar, Haryana

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.

Units Plant

Capacity

Product By product

Molasses/Grain

based Distillery

Plant

150 KLPD Ethanol / Extra

Neutral Alcohol (ENA)

/ Rectified Spirit (RS)

During Molasses based operation - CO2

During Grain based operation - DDGS

and CO2

Co-Generation

Power Plant

7.0 MW Power

Malt Spirit Plant 10 KLPD Malt Spirits DDGS

(vi) Project Description with Process Details

A) Proposed 150 KLPD Molasses Based Distillery

� Molasses Unloading and Storage

Molasses from tankers/pipe line will be unloaded at unloading point and transferred in to

molasses storage tank.

� Yeast propagation and fermentation:

Yeast activation:

Yeast seed material will be prepared in water-cooled Yeast Activation vessel by

inoculating sterilized mash with active dry yeast. Optimum temperature will be

maintained by cooling water. The contents of the yeast activation vessel will be then

transferred to fermenter.

Fermentation:

The Molasses from storage tank to be pumped to dilutor installed in fermentation section

and diluted with water. The diluted molasses called Wort will be fed into culture vessels






and Pre-fermenter for activation of yeast. The activated yeast from the yeast activation

vessel transferred into pre fermenter.

Once the yeast activated in pre-fermenters, it will be transferred in to fermenters and

diluted molasses to be added. The process of fermentation is to convert the fermentable

substrate into alcohol. The pH of the wort is adjusted by the addition of acid. Yeast will be

available in sufficient quantity to initiate fermentation rapidly and complete it within the

cycle time.

At the start of the cycle, the fermenter will be charged with wort and contents of the yeast

activation vessel. Significant heat release takes place during fermentation. This is removed

by passing cooling water through the fermenter PHE’s to maintain an optimum

temperature. The recirculating pumps also serve to empty the fermenters into beer well.

After the fermenters will be emptied, they will be cleaned with water and caustic solutions

and sterilized for the next batch. The carbon dioxide evolved during the process will be

vented to atmosphere (to be processed and stored for industrial use) after recovery of

alcohol in a scrubber.

� Distillation: (Multi Pressure Distillation with Integrated Evaporation)

Fermented wash from wash holding tank will be pumped by wash feed pump to the top

of degassing column after preheating the same in beer heater and spent wash heat

exchanger. The vapours along with non-condensable gases from the top of degassing

column will be rectified in Heads column, to expel the high volatiles, technically known as

heads. Bottom liquid from the degasser flows into analyzer column where alcohol is

stripped from the liquid. The liquid from bottom of analyzer column will be completely

stripped of alcohol and will be pumped out by thick slop discharge pump through heat

exchanger where it preheats the fermented wash before it enters degassing column. The

slop from the analyzer column will be fed in to decanter. The dilute alcohol vapors from

near the top of analyzer column will be condensed first in beer heater while exchanging

heat with wash feed and then in analyzer condenser. Degasser and analyzer operate

under vacuum. The condensate will be collected in rectifier feed tank. The vapors for

stripping alcohol will be generated from analyzer column bottom liquid in the analyzer

column re-boiler by using the rectified column top vapors, as discussed subsequently.

Vapors from the top of heads column are condensed in heads column condenser and

then in head column vent condenser. Part of the condensate is returned to column as

reflux while a small portion is taken out as an impure spirit cut. Liquid from bottom is also

taken into rectified feed tank.

Dilute alcohol water mixture from rectifier feed tank will be pumped by rectifier feed

pump through rectifier feed pre-heater in to rectifying column. Rectifier and its associated

equipment work under pressure so that these vapors can supply the necessary heat for

generating the vapors.






The condensate is then pumped as reflux to rectifying column. Rich alcohol vapors at a

concentration of 95.5% v/v from top of rectifying column are condensed first in analyzer

and then in reflux vent condenser. The liquid form will be collected in rectifier reflux tank.

Part of the liquid may be drawn off as impure spirit. The impure spirit cut will be

maintained as little as possible to maintain aldehyde levels to meet the required limits in

RS/ ENA. From rectifier column the draw will be taken to produce RS and for ENA draw

will be sent to ED column, rectifier column and finally to polishing column to maintain

quality of ENA and final draw from polishing column will be sent to receivers.

Liquid from the reflux tank is pumped by product pump partly as product and partly as

reflux to the top of the rectifying column. The necessary rectifying vapors are generated

by boiling the bottom liquid in Rectifier Column Re-boiler using medium pressure steam.

Some side streams are drawn from rectifier column as light and heavy fractions of higher

alcohols called fusel oils and cooled in fusel oil coolers and are mixed with water and

allowed to separate out in fusel oil separator. All vents will be connected to Vent Gas

Absorber where the vent gases are scrubbed with water to recover entrained alcohol. The

scrubber water is used for washing the fusel oils in fusel oil separator to recover alcohol

from the fusel oil fractions. The absorber vent is connected to vacuum pump which is

used to create vacuum in the analyzer and degasser.

Absolute alcohol is manufactured by dehydration of Rectified Spirit. The process adopted

here is based on Pressure Swing Adsorption (PSA) system using Molecular Sieves.

Rectified spirit, after preheating by waste hot streams, is vaporized and superheated by

using medium pressure steam at 6 Kg/cm2g pressure. Hot vapors at 6 kg/cm² g pressure

and 130° C temperature pass through PSA column, where the water vapors are retained

while water free alcohol is released as vapors. The vapors are condensed and collected as

absolute alcohol. When the molecular sieve bed is saturated with water the alcohol

vapors are shifted to the other tower and the first tower is taken for regeneration.

Regeneration is done first by pressure releasing and creating vacuum and then by

elutriating with dehydrated alcohol vapors from the tower in dehydration operation. The

vapors are condensed and the vent vapors are recovered through scrubber. Vacuum can

be created. Product will be cooled and transferred to absolute alcohol receiving tank and

then on to storage tank.

� Alcohol bulk storage:

Alcohol will be first taken to daily receiver storage tanks, which will be based on the State

Excise laws, storage for three days considering the weekly holidays of two days.

Thereafter, the alcohol will be transferred to bulk storage tanks after taking the daily

receiver Dip. This is transferred using flameproof pumps. Final dispatch of alcohol will be

metered and again will be carried out using special flameproof pumps. The Bulk spirit

storage is proposed to be set up for 30 days.






� Effluent handling section in the process

a) Evaporation section:

• The spent wash coming from distillation section will be fed in to first calendria of

the evaporator section. There will be five calendria installed as per design to

concentrate the dissolved solids. Suggested treatment scheme is a four FF +

finisher evaporation plant for spent wash evaporation. The following points will

elucidate the basic working principle:

• After Integrated evaporator spent wash will be fed to stand alone evaporators

four effects ( 3+1) Forced circulation to concentrate it up to 60 brix to burn in

incineration boiler

• Shell & tube type evaporators with highly efficient liquid distributor working on

the principle of falling film evaporation will be used, with Plate type Preheaters

for preheating of FEED stream which serves the purpose of energy conservation.

• Analyzer vapor will be fed to the first effect evaporator shell side at the given

pressure and temperature as the heating medium.

• The feed from the feed balance tank will be taken to make the best heat recovery.

• The feed after getting heated to the predetermined temperature in pre-heater

will be fed from the first effect evaporator which is falling film evaporator -1

• Vapors generated in 1steffect VLS (Vapor Liquid Separator) will be used as heat

source in the 2nd

effect and from 2nd

to third and so on.

• The product at the desired concentration of TS will be obtained at the outlet from

the final effect.

• A Shell & tube type multi-pass surface condenser will be employed for

condensing the shell side vapors.

• The pure and the process condensate are collected in receiving vessels.

• Highly efficient operating pumps will be provided for pumping the required fluid.

• The operation of the plant will be under vacuum. Vacuum is created with the help

of a water ring vacuum pump.

• The plant will have high level of automation to get consistent output at required

concentration.

• The system will operate under vacuum. Water-ring vacuum pumps will be used to

maintain a desired vacuum.

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

condensing the vapors.

b) Incineration boiler along with the turbine generator:

The concentrated effluent will be mixed with bagasse/biomass/coal and fired into

specially designed incineration boiler to generate steam and power.






Figure 3:- Process flow diagram of 150 KLPD Molasses based Distillery






Distillery Effluent Treatment Scheme - RO based Process condensate Treatment

Plant

The process condensate treatment plant will be based on the process of Reverse Osmosis

technology. The system will comprise of following unit process & equipment.

• Equalization tank

• Neutralization tank

• Filtration section

• Pressure sand filter

• Dual media filter

• Feed RO system

• Permeate RO system

• Reject RO system

• RO CIP system

Neutralization process: The stored process condensate will be transferred to the

downstream neutralization tank. Process condensate will be neutralized in this tank with

dosing of alkali solution. The neutralization process will be automated &will be controlled

through the controller. Neutralized condensate will be then collected in filter feed tank

for further processing through the filtration system.

Filtration Process: Neutralized condensate from the filter feed tank will be passed

through two stage media filters. First condensate will be filtered by pressure sand filter in

order to remove suspended matters & turbidity present in it. The primary sand filter

outlet will be filtered in Dual media filter to remove the fine suspended solids.

Feed RO system: The neutralized & filtered water will be treated through Feed RO

system. The feed water will be dosed with anti-scalant& SMBS solutions to condition the

feed water prior to passing it through Feed RO system. The feed RO skid will be two stage

systems comprising of two pressure vessels containing six elements each configured in

series. As the feed water flows through the first pressure membrane from feed to reject

end, the pure water permeates through membrane and will be collected in the permeate

header. The concentrated water will be collected in Reject header& then passed through

the second pressure vessel. The permeate generated from the Feed RO system will be

collected in the permeate RO feed tank & Reject generated will be collected in the Reject

RO feed tank.

Permeate RO system: The permeate generated from the feed RO skid will be passed

through the permeate RO system for further removal of dissolve solid. The system

comprises of two pressure vessels containing four elements each configured in series. As

the feed water flows through the first membrane from feed to reject end the pure water

permeates through the membranes &will be collected in the permeate header. The

concentrated water will be collected in Reject header & then passes through the second






pressure vessel. The permeate generated from the system will be collected on the

permeate RO product tank & Reject generated will be collected in reject RO feed tank.

Reject RO system: The reject generated from the feed RO skid & permeate skid will be

passed through the Reject RO system for further recovery of low TDS water. The system

will comprise of two pressure vessels containing four elements each configured in series.

As the feed water flows through the first membranes from feed to reject end the pure

water permeates through the membranes & will be collected in the permeate header. The

concentrated water will be collected in Reject header & then passed through the second

pressure vessel. The permeate generated from the Reject RO system will be collected in

the reject RO product tank & reject generated will be collected in the final reject

collection tank. The permeate from Permeate RO system & permeate from Reject RO

system will be used in cooling towers & fermentation for makeup water & molasses

dilution. The final reject will be fed to evaporation again.

Table - 2

Characteristics of Untreated and treated effluent

S.

No.

Parameters Untreated Effluent Treated effluent Evaporation process

condensate Cooling tower

blow down

1. TDS 200 mg/l 2000 mg/l <10 mg/l

2. pH 3.5 7.2 6.5-7.5

3. BOD 2500 mg/l 60 mg/l <10 mg/l

4. COD 3500 mg/l 200 mg/l <100 mg/l

B) Process Description of 150 KLPD Grain based operation

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

1) 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.






2) 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.

3) 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.

4) 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 Re boiler. 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.

5) 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).

6) 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.

7) 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.

8) 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.

Proposed 150 KLPD Molasses/Grain based Distillery along with 7.0 MW Co-generation power plant & 10 KLPD Malt Spirit Plant within existing non-operational Distillery Plant




Figure - 4: Process flow chart For Grain Based Distillery

Proposed 150 KLPD Molasses/Grain based Distillery along with 7.0 MW Co-generation power plant & 10 KLPD Malt Spirit Plant within





C) Manufacturing process of Malt Spirit Plant (10 KLPD)

Malt Spirit Production process is given below:

� Malt handling- Malt is usually stored in silos before being milled and mashed. It has a low

moisture content of between 3 and 5%. The main processes in malt handling are Intake,

storage, conveying, removing unwanted materials & stones, weighing.

� Milling - The objective of milling is to reduce the malt to particles sizes, which will yield the

most economic extract (wort) and will operate satisfactorily under brewhouse conditions

and throughout the brewing process. The more extensive the malt is milled, the greater the

extract production.

� Mashing- Mashing is the process of combining a mix of milled grain (typically malted barley

with supplementary grains such as corn, sorghum, rye or wheat), known as the "grain bill",

and water, known as "liquor", and heating this mixture. Mashing allows the enzymes in the

malt to break down the starch in the grain into sugars, typically maltose to create malty

liquid called wort.

� Fermentation- Fermentation is an essential stage in the brewing process. It involves adding

yeasts to the cooled malt. These yeasts are fed by the amino acids in the brew and produce

alcohol from the sugar that is present. These natural reactions also produce carbon dioxide.

� Pot Distillation- Malt Whisky is distilled twice - although a few distilleries may undertake a

third distillation - in Pot Stills which resemble huge copper kettles. The spirit is driven off

from the fermented liquid as a vapour and is then condensed back to a liquid. In the first

distillation the fermented liquid, or wash, is put into the Wash Still which is heated either

directly by fire or by steam-heated coils. At this stage the wash contains yeast, crude

alcohol, some un-fermentable matter and the by-products of fermentation. During the

process of boiling the wash, changes take place in its constituents which are vital to the

flavour and character of the whisky. As the wash boils, vapours pass up the neck of the still

and then pass through a water-cooled condenser or a worm, a coiled copper pipe of

decreasing diameter enclosed in a water jacket through which cold water circulates. This

condenses the vapours and the resulting distillate, known as low wines, is collected for re-

distilling. The liquor remaining in the Wash Still is known as pot ale or burnt ale and is

usually treated and converted into distillers' solubles for animal feed.

� Decantation- The decantation section comprises of a Centrifuge Decanter for separation of

suspended solids from Spent Wash coming out of distillation Plant.

Wet cake/DWGS- Spent grains also known as DWGS, has a commercial value and can be sold as

by-products for livestock feed or Wet cake / DWGS will be passed through steam tube bundle

drier for drying into cake with 10 - 12% moisture (max.) to give higher shelf life.






Figure 5: Process flow diagram of Malt Spirit production

D) Power Co-Generation (7.0 MW)

The unit proposes to set-up boiler (56 TPH) and power turbine (7 MW). Boiler will operate mainly

to feed steam to distillery and 7.0 MW power generations from Turbine. During Molasses based

operation boiler fuel will used concentrated Spent Wash and Coal or Biomass and during Grain

based operation boiler fuel will used biomass/Rice Husk/ Bagasse/ Paddy & Wheat Straw or Coal.

Proposed 7 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 Bag Filter where the dust particles are collected. The dust is collected from here.

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 boiler auxiliaries etc. Surplus power can be

exported to Grid.

Figure 6: 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 Ethanol & ENA/RS will be Molasses and Grain.

Molasses will also be used as a raw material in molasses based operation which is available from

nearby sugar mills. Grains such as damaged grain feed stock, broken rice, maize, bajra & sorghum

will be used as raw material which is easily available from the local market.

The raw material for the boiler fuel will be various biomasses such as Rice Husk/ paddy straw/ cow

dung/ poultry waste etc. and concentrated spent wash for incineration when the distillery is

operated on molasses.

TABLE - 3 Raw Material Requirement

S.

No.

Particular Total

Requirement

Source & Mode of

Transportation

1 Molasses 660 to 700 TPD From nearby sugar mill & suppliers by

tankers (road)

Or

Grain - Broken Rice, Sorghum, Baira,

Maize etc.

335 to 360 TPD Through Grain suppliers By road

2. Barley Malt & adj Flour for Malt Plant 22 TPD Through suppliers By road

3. Process Chemicals Near-by Markets by road

Sodium Hydroxide (Caustic) 1200 Kg/day

Enzyme 9 Kg/day






Antifoam Agent 225 Kg/day

Others Chemicals 300 Kg/day

Yeast (Active Dry Yeast/Distiller’s

Yeast)

Own Propagation

(B) Fuel Requirement for Boilers:

During Molasses based operation - Concentrated Spent Wash and Coal or Bagasse / Rice husk /

Indian coal will be used for the proposed boiler of 56 TPH.

During Grain based operation Coal or Biomass will be used for the proposed boiler of 56 TPH.

Details regarding fuel requirements are given below.

TABLE – 3

Fuel Requirement

Operation Mode

Name of Raw Material

Total Requirement Source & Mode of Transportation

Molasses based operation

Concentrated Spent Wash and Coal or Biomass

Concentrated Spent Wash - 560 TPD and

Biomass 190TPD / Coal 140 TPD

Spent wash - Own plant through pipelines

Coal / biomass - From authorized dealers by road

or

Grain based operation

Coal or Biomass Coal 240 TPD or Biomass 375 TPD

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

be briefly outlined.

Water as a resource will be recycled at each possible step of the process and latest technology

and methodology will be adopted to conserve and reuse the resources.

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

given.

(a) Water Requirement and Source

Total fresh water requirement for the project will be 1450 KLPD (1350 KLPD Distillery + 80 KLPD

Malt Spirit Plant + 15 KLPD Bottling Plant + Domestic 5 KLPD) which will be sourced from

Surface water (Canal) or Ground Water

Water Requirement for Proposed 150 KLPD Molasses based Distillery based on Incarnation

Boiler

The water requirement for the first run for project would be 2789 KLPD, which will be further

reduced through recycling to 1439 KLPD. Hence, fresh water requirement is 1350 KLD. Details

given below:






Figure 7: Mass & water balance of proposed 150 KLPD Molasses based Distillery based on Incarnation Boiler






(b) Power Requirement and Source

The total power requirement will be 4.5 MW, which will be sourced from 7.0 MW Co-Generation

Power Plant. Surplus power can be exported to Grid.

(c) Steam Requirement

Total Steam requirement will be met by 56 TPH boiler. The steam requirement for different

purposes is given below:

TABLE – 4

Steam Requirement

S.

No.

Purpose Total Steam Requirement for 150 KLPD Molasses based

distillery (Incineration Route)

1. Multi-pressure Distillation 10.5

2. Multi Effect Evaporator 14.25

3. Boiler De - Aeration 3.75

Total 28.5

Source Proposed 56 TPH Incinerator Boiler

Steam for Malt Spirit 4 TPH

Boiler Details:

Details regarding boilers are mentioned in the table given below:

TABLE – 5

Boiler Details

S. No. Item Boiler details

1. Boiler Capacity 56 TPH

2 Type of Fuel During Molasses based operation - Concentrated Spent Wash and Coal or Biomass

During Grain based operation - Coal or Biomass

3. Stack Height 82 Metres

4. Pollution Control Equipment Measures

Electrostatic Precipitator (ESP)

Details regarding the D.G. Sets

2 nos. of D. G. Sets of capacity 1500 KVA each will be installed with the plant for emergency back-

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

TABLE – 6

Details Regarding the D.G. Sets

S. No. Details

1. Type of Fuel HSD

2. Capacity 2 x 1500 KVA

3. Stack Height (above roof level) As per CPCB/SPCB norms

4. Pollution Control Equipment Measures Adequate stack height/ Acoustic Enclosure






(x) Quantity of Waste to be generated (liquid and solid) and Scheme for their

Management/Disposal:

Waste Water Generation and management:

� The project will be based on “ZERO EFFLUENT DISCHARGE”.

� Fresh water requirement of the project will be met by ground water. Efforts will be made to

conserve as much water as possible by recycling and reusing waste water.

� Molasses slops (spent wash) shall be concentrated in evaporators and incinerated in boiler.

� Grain Slops (Spent Wash) will be taken through Decanters Centrifuge for separation of

Suspended Solids separated as Wet Cake. Thin Slops from the Decanter Centrifuge will be

partly (20%) recycled back to Liquefaction Process), partly (20%) used in Analyser Column

Reboiler for flash steam generation under vacuum and the balance (60%) taken to Multi

Effect Evaporation Plant for concentration of thin slop to form a Syrup. This Syrup as

Condensed Distillery Solubles (CDS) is mixed with the Wet Cake coming out of Decanter

Centrifuge and the mixture is known as Distillers Wet Grain with Solubles (DWGS). DWGS

will be fed to Dryers operating on steam and is dried to make it DDGS – Distillers Dried

Grain with Solubles.

� Process condensate is cooled and collected into an equalization tank with sufficient

residence time. After equalization, this process condensate will be fed for Ecophotox and

after treatment it will be used for greenbelt development within the complex.

� Solid waste from the grain based operations generally comprises of fibres and proteins in

the form of DDGS, which will be ideally used as cattle feed.

� Ash from the boiler will be given to brick manufacturing unit.

� Used oil & grease generated from plant machinery / gear boxes & D.G. Set will be partly

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

to the CPCB authorized recycler.

4.0 SITE ANALYSIS:

(i) Connectivity

The plant site is well connected to Highway NH 10 (Adjacent in SW direction) and NH 65 (~ 7.2

km in West direction). The nearest railway station is Hisar (~ 7 km in West direction) and nearest

airport is New Delhi (~ 142 km in SE direction). The site is suitably located with respect to

availability of raw material, water, road network, skilled/ semi-skilled/unskilled and professional

manpower etc. All communication facilities such as telephone, telefax & internet are available in

the vicinity of the project site.

(ii) Land from Land use and Land ownership

The existing plant area is 8.0 hectares (19.77 Acres). No additional land is required for the

proposed project as the same will be done within the existing old non - operational 25 KLPD

Distillery plant premises. The project is being proposed in existing old non- operational distillery

plant premises and land has already been converted for industrial use.






(iii) Topography

Topography of the core zone of the project is 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 Satrod Khas (1 km in SW direction)

2. Nearest City Hisar (4.5 km in West direction)

3. Nearest National Highway / State

Highway

• NH 10 (Adjacent in SW direction)

• NH 65 (7.2 km in West direction)

4. Nearest Railway station Hisar (7 km in West direction)

5. Nearest Airport New Delhi (142 km in SE direction)

6. Reserved Forest(RF)/Protected Forest (PF) Bir Hisar PF (5.0 km in NW direction)

7. National Parks, Reserved Forests (RF)/

Protected Forests (PF), Wildlife

Sanctuaries, Biosphere Reserves, Tiger/

Elephant Reserves, Wildlife Corridors etc.

within 10 km radius

No National Parks, Wildlife Sanctuaries, Biosphere

Reserves, Tiger/ Elephant Reserves, Wildlife Corridors etc.

lies within 10 km radius of the plant site.

8. Water Body (within 10 km radius) • Balsamand Sub Branch (Bhakra Canal) (Adjacent in East direction)

• Hisar Major Distributary (Western Yamuna Canal) (Adjacent in North direction)

• Dewa Distributary (~ 1.5 km in South direction)

• Petwar Distributary (~ 4.0 km in South direction)

Few minor agricultural canals are also present in 10 km

radius area

9. Seismic Zone Zone II: Low Damage Risk Zone (MSK VI or less)

(v) Existing Infrastructure


proposed project as the same will be done within the existing old non-operational distillery plant

premises. Existing infrastructure includes 25 KLPD distillery & CL/IMFL Bottling Plant and utilities






like boilers, water treatment plant, steam, power, ETP, storage facilities etc.

(vi) Soil classification

The soils of the district are of three types i.e. Arid brown solonized (in north eastern parts

covering north eastern part of Narnaund and Uklana Mandi blocks.), Sierozem (in major parts

covering Barwala, Hansi-I, Bass (Hansi-II), Hisar-I & Agroha blocks and parts of Uklana, Narnaund,

Adampur & Hisar-II blocks) and desert soils (in southern western parts covering part of Adampur

and Hisar-II blocks).

(vii) Climatic data from secondary sources

The climate of Hisar owes to its continental location on the outer margins of the south-west (SW)

monsoon region. It has tropical monsoonal climate and is characterized as arid type of climate.

The district has characteristically four seasons during the year viz., summer (March to May), SW

Monsoon (June to September), Post-Monsoon (October to November) and winter (December to

February) season. SW monsoon also known as summer monsoon brings rain during last week of

June to mid-September. The period from October onward until next June remains almost dry

except, few light showers received due to westerly depressions/western disturbances (WDs). The

summers are generally quite hot and winters are fairly cool. The main characteristics of climate of

in the district are its dryness, extremes of temperature and scanty rainfall.

Rainfall: The normal annual rainfall of the district is 330 mm which is unevenly distributed over

the area 22 days .Around 75 to 80 per cent of the annual rainfall is received during South West

Monsoon season (June to September) with 50 per cent coefficient of variation (CV). The average

annual rainfall is around 450 mm, of which the average monthly rainfall received during July and

August months is 133.4 and 116.2 mm, respectively. The average monthly rainfall during

September is 54.5 mm and June 49.8 mm. The average rainfall received during normal monsoon

season is 283 mm. Generally rainfall in the district increases from southwest to northeast.

(viii) Social Infrastructure available

There are primary schools, dispensaries, small hospital, places of worship in nearby area of the

plant site.

5.0 PLANNING BRIEF

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

Planning/ Development authority classification.

Proposed industry is a Molasses / grain based distillery. Facilities required for the project will be

provided as per requirement. Transportation of raw material and final product will be done via

existing road network and cement concrete road will be developed within the plant premises.

(ii) Population Projection

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

outsiders. A projection may be made by a governmental organization, or by those unaffiliated

with a government.

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






The company already have infrastructure (Physical & Social) in nearby area of the plant site under

corporate social responsibilities programs.

(iv) Amenities/Facilities

The company has already developed the amenities/facilities in nearby areas of the existing

plant/project site as per requirement of local people under Corporate Social Responsibilities

Programs.

6.0 EXISTING INFRASTRUCTURE:

(i) Industrial Area (Processing Area)


proposed project as the same will be done within the existing old 25 KLPD Distillery plant

premises. The project is being proposed in existing old non - operational distillery plant premises

and land has already been converted for industrial use.

(ii) Residential area (Non Processing area)

Residential colony is not existing and also not proposed for the plant. The local labour was/ will

be preferred to provide employment opportunities. All operation managers and operation staff

are stayed nearby towns.

(iii) Greenbelt

2.64 hectares, i.e. ~33% of the plant area has already been covered under greenbelt & plantation.

(iv) Social Infrastructure

Project results in growth of the surrounding areas by increased direct and indirect employment

opportunities in the region including ancillary development and supporting infrastructure.

(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

5 m3/ day water will be required for drinking purpose after installation which will be sourced from

Ground Water.

(vii) Sewage Treatment System

Domestic waste water generated from the plant will be treated in STP.

(viii) Industrial Waste management

The distillery will be based on “ZERO EFFLUENT DISCHARGE”. Waste water generated from

plant premises will be treated in ETP.

(ix) Solid Waste Management

• Molasses slops (spent wash) shall be concentrated in evaporators and incinerated in boiler.

• Solid waste from the grain based operations generally comprises of fibres and proteins in

the form of DDGS, which will be ideally used as cattle/poultry/fish feed.

• Ash from the boiler will be given to brick manufacturers.






• ETP sludge will be dewatered in filter press and used as manure.

(x) Power Requirement and Source

The total power requirement for the project will be 4.5 MW which will be sourced from the 7 MW

Cogeneration Plant.

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).

Rehabilitation & Resettlement is not applicable because the proposed project will be done within

the existing old 25 KLPD non - operational Distillery plant premises. The complete land is already

under the company’s possession.

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 all other required

clearance and will complete the molasses part within 3 to 4 years.

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

project.

� Total cost of the Project: Rs. 125 Crores

� Cost for Environment Protection Measures:

� Capital Cost: Rs. 40 Crores

� Recurring Cost/annum: Rs. 4.0 Crores

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.

The 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.

Haryana state will get revenues in terms of taxes. Business opportunities for local community will

be available like transport of raw material/product to market, fly ash transport to brick

manufactures, maintenance & house-keeping contract work etc.

proposed 150 klpd molasses/grain based distillery along with … · esp/bag filter with stack of...

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