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PRE - FEASIBILITY REPORT

For

Proposed 90 KLPD Grain Based Distillery

along with 3.0 MW Co-Generation Power Plant

At

Village Ganora, Tehsil Ghatol,

District Banswara (Rajasthan)

Applicant

Express Digital Payment Services Private Limited

Registered office: A-47, Lower Ground Floor, Hauz Khas,

New Delhi – 110016

Email id – [email protected]

i

INDEX

S. NO. CONTENTS PAGE NO.

1. EXECUTIVE SUMMARY 1

I INTRODUCTION 1

1.1 Environment Management Plan 3

2. INTRODUCTION OF THE PROJECT/BACKGROUND INFORMATION 5

(i) Identification of Project & Project Proponent 5

(ii) Brief Description of Nature of The Project 5

(iii) Need for The Project & Its Importance to The Country and/ Or Region 5

(iv) Demand-Supply Gap 6

(v) Import vs. Indigenous production 6

(vi) Export Possibility 6

(vii) Domestic / Export Markets 6

(viii) Employment Generation (Direct And Indirect) Due To The Project 6

3. PROJECT DESCRIPTION 7

(i) Type of Project Including Interlinked and Independent Projects, If Any 7

(ii) Location (Map Showing General Location, Specific Location and Project Boundary & Project Site

Layout) with Coordinates

7

(iii) Key Plan 9

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

environmental considerations gone into should be highlighted.

10

(v) Size or Magnitude of Operation 10

(vi) Project Description with Process Details 10

(vii) Raw material required along with estimated quantity, likely source, marketing area of final

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

15

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

outlined.

16

(ix) Availability of water it’s source, energy /power requirement and source should be given. 16

(x) Quantity of waste to be generated (liquid and solid) and scheme for their management/disposal 19

4. SITE ANALYSIS 19

(i) Connectivity 19

(ii) Land form, land use and land ownership 19

(iii) Topography 20

(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

20

(v) Existing Infrastructure 21

(vi) Soil Classification 21

(vii) Climatic Data From Secondary Sources 21

(viii) Social Infrastructure Available 21

ii

5. PLANNING BRIEF 21

(i) Planning concept (type of industries, facilities, transportation etc.) Town and country planning/

development authority classification.

21

(ii) Population Projection 21

(iii) Assessment of infrastructure demand (physical & social) 21

(iv) Amenities/Facilities 22

6. PROPOSED INFRASTRUCTURE 22

(i) Industrial Area (Processing Area) 22

(ii) Residential Area (Non Processing Area) 22

(iii) Green Belt 22

(iv) Social Infrastructure 22

(v) Connectivity 22

(vi) Industrial Waste Management 22

(vii) Solid Waste Management 22

(viii) Power Requirement & Source 23

7. REHABILITATION AND RESETTLEMENT (R & R) PLAN 23

(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)

23

8. PROJECT SCHEDULE & COST ESTIMATES 23

(i) Likely date of start of construction and likely date of completion (time schedule for the project to

be given)

23

(ii) Estimated project cost along with analysis in term of economic viability of the project. 23

9. ANALYSIS OF PROPOSAL 23

(i) Financial and social benefits with special emphasis on the benefit to the local people including tribal population, if any, in the area.

23

iii

LIST OF TABLES

TABLE NO. CONTENTS PAGE NO.

1 Salient Features Of The Project 1

2 Manpower Requirement 6

3 Raw Material Requirement for Grain Based Distillery 15

4 Fuel Requirement 15

5 Total Water Input 16

6 Steam requirement 18

7 Boiler details 18

8 Details Regarding the D.G. Sets 18

9 Environmental Settings of the Area 20

LIST OF FIGURES

FIGURE NO. CONTENTS PAGE NO.

1 Location Map 8

2 Key Plan 9

3 Process Flow Chart for Grain Based Distillery 14

4 Water Balance for Grain Based Operation 17

Proposed 90 KLPD Grain Based Distillery along with 3.0 MW Co-Generation Power Plant

At Village Ganora, Tehsil Ghatol, District Banswara (Rajasthan).

Pre - feasibility Report

M/s. Express Digital Payment Services Private Limited 1

PRE - FEASIBILITY REPORT

1.0 EXECUTIVE SUMMARY

(I) Introduction

M/s. Express Digital Payment Services Private Limited is proposing 90 KLPD Grain based

Distillery along with 3.0 MW of Co-Generation Power Plant at Village Ganora, Tehsil Ghatol,

District Banswara (Rajasthan).

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.

As per EIA Notification dated 14th Sep., 2006 and as amended from time to time; the

project falls in Category ‘A’, Project or Activity - 5(g)(ii) [Non-molasses based distilleries

>60 KLD].

Table – 1

Salient Features of the Project

S.

NO.

PARTICULARS DETAILS

A. Nature & Size of the Project Proposed 90 KLPD Grain Based Distillery along with 3.0 MW

Co-Generation Power Plant

B. Category of the Project As per EIA Notification dated 14th Sep., 2006 as amended

from time to time; the project falls in Category ‘A’, Project or

Activity - 5(g)

C. Location Details

Village Ganora

Tehsil Ghatol

District Banswara

State Rajasthan

Latitude 23046’21.78’’ N to 23046’37.48’’ N

Longitude 74016’58.94’’ E to 74017’22.85’’ E

Topo sheet No. 46 I/1, 46I/2, 46I/5, 46I/6

D. Area Details

Total Plant Area 20.0 acres (8.10 ha)

Greenbelt / Plantation Area 6.6 acres, i.e. ~33% of the project area will be covered under

green belt/ plantation

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

1. Nearest Village Dukwara Village (0.7 km in SE direction)





2. Nearest Town & City • Nearest Town: Ghatol (~12.5 km in ESE direction)

• District Headquarters: Banswara (~30 km in SSE direction)

3. Nearest National Highway /

State Highway

• SH - 32 (~2.5 Km in WSW direction)

• NH - 113 (~10.5 Km in SE direction)

4. Nearest Railway station Dungarpur (~58 km in West direction)

5. Nearest Airport Maharana Pratap Airport, Udaipur (~ 100 km in NNW

direction)

6. National Parks, Wild Life

Sanctuaries, Biosphere

Reserves, Tiger/ Elephant

Reserves, Wildlife Corridors

etc. within 10 km radius

No National Parks, Wild Life Sanctuaries, Biosphere Reserves,

Tiger/ Elephant Reserves, Wildlife Corridors etc. falls within

10 km radius from the plant site.

7. Reserved Forests (RF) /

Protected Forests (PF) etc.

within 10 Km. radius

• Kundli Dudka Block PF (~3.5 km in ENE direction)

• Bhoyar Borda PF (~4.5 km in ESE direction)

• Loharia Block A PF (~7.0 km in WSW direction)

• Gargiyamarga Block PF (~7.5 km in ENE direction)

• Loharia Block B PF (~8.4 km in West direction)

• Suliya Venka Block PF (~8.5 km in North direction)

8. River / Water Body (within 10

km radius)

• Budanpura Minor (~2.5 km in South direction)

• Mahi River (~5.7 km in NW direction)

• Mahi Canal (~7.2 km in East direction)

• Shakliya Nadi (~8.5 km in ESE direction)

• Som River (~9.0 km in NW direction)

F. Cost Details

Total Cost of the Project Rs. 170.75 Crores

Cost for Environment

Management Plan

Capital Cost: Rs. 20 Crores

Recurring Cost : Rs. 1.5 Crores/annum

G. Basic Requirements for the project

Water Requirement 760 KLPD

Source – Groundwater

Power Requirement 2.1 MW

Source – Co Generation Power Plant of 3.0 MW

Man Power Requirement 100

(Source:- Unskilled / Semi-Skilled - Local Area; Skilled- Local &





Outside)

H. Product Mix ENA / RS / IMFL /Ethanol

I. Working Days 350 days/annum

1.1 ENVIRONMENT MANAGEMENT PLAN

Particulars DETAILS

Air Quality Management

Possible

Sources

Boilers, Transportation vehicles, D.G. Sets etc.

Emissions � ESP/Bag Filters will be installed with the proposed boiler.

� Adequate boiler stack height will be provided.

� CO2 produced during the fermentation process will be collected and utilized as

an industrial gas.

� DG Sets will also have adequate stack of height as per CPCB Guidelines.

� Adequate measures for Fugitive Dust Emissions will be taken.

� All the internal roads will be asphalted.

� Development of Green Belt all around the periphery & within the premises of

the plant will help in attenuating the pollutants emitted by the plant.

Monitoring � Online stack monitoring system will be installed.

� Ambient air quality will be regularly monitored.

Water Management

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

� Fresh water requirement of the project will be met by Ground Water & recycled

water.

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

separation of Suspended Solids separated as Wet Cake.

� Thin Slops from the Decanter Centrifuge are 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 will be passed through steam tube bundle drier

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





dry cakes (DDGS) will be obtained finally.

� The Process condensate 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.

� Rainwater will be collected and recharged into underground resource through

scientifically designed Rainwater Harvesting System.

Noise Management

Management � Proper maintenance, oiling and greasing of machines at regular intervals.

� PPEs like earplugs and earmuffs to the workers exposed to high noise level.

� Development of Green Belt for 33% of the total project area.

� D.G sets will be provided with acoustic enclosures to control the noise level

within the prescribed limit.

Monitoring Regular monitoring of noise levels will be carried out and corrective measures in

concerned machinery will be adapted accordingly to the possible extent.

Solid Waste Management

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 will be ideally used as cattle feed.

� Ash from the boiler will be supplied to brick manufacturers & cement plant.

� The Yeast sludge will be added to the Wet Cake.

� Used oil & grease generated from plant machinery/Gear boxes as hazardous

waste will be sold out to the CPCB authorized recycler.

Green belt Development/ Plantation

Management � Out of the total plant area ~ 33% of total project area will be developed under

green belt/plantation.

� Plantation will be done as per Central Pollution Control Board (CPCB) Norms.

� Greenbelt will be developed all along the plant boundary and plantation will be

done all along the roads which attenuates noise level, arrest dust and improves

the surrounding environment.

� Native species will be given priority for plantation in consultation with local

horticulturist.

� The plantation would start along with the start of the construction activities of

the proposed unit.

Odour Management





Management � Adequate greenbelt all around the periphery of the plant.

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

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

� Better housekeeping 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.

2.0 INTRODUCTION OF THE PROJECT/ BACKGROUND INFORMATION

(i) Identification of Project and Project Proponent

M/s Express Digital Payment Services Private Limited (EDPSPL) is a company promoted by

Mrs. Anita Gupta and family. The promoters of EDPSPL have diversified interests in liquor,

edible oils, real estate, financial services etc. The promoters have the financial and

managerial capability to set up and manage large industrial projects.

Now, EDPSPL is proposing Project comprising of Grain Based Distillery, IMFL & Country

Liquor Bottling, Brewery and Co-Generation Power Plant at Village Ganora, Tehsil Ghatol,

District Banswara (Rajasthan). It would be an eco-friendly project. We shall adopt zero

discharge concepts.

(ii) Brief description of nature of the project

M/s Express Digital Payment Services Private Limited is proposing to set up Extra Neutral

Alcohol/ Rectified Sprites / Ethanol/Industrial Alcohol/Total Alcohol etc. manufacturing

facility with an installed capacity of 90 KLD & 3 MW Co-generation Power Palnt along with

CO2 & Distillers Dried Grains & Solubles (DDGS) for Cattle/Poultry/Fish or Prawn feed as by-

products. For the purpose of setting up the unit, the site is located at Village Ganora,

Tehsil Ghatol, District Banswara (Rajasthan). The company will manufacture ENA through

grain based process. The proposed site is chosen because of its proximity to the

agriculture field surrounding the area & easy availability of food grains like Maize, Bajra,

Sorghum & broken rice to the distillery for producing alcohol.

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

With hundreds of kind of alcoholic beverages being made and consumed in India, the

industry can be categorised into four broad groups’ viz. Indian Made Foreign Liquor

(IMFL), Country Liquor (CL), illicit liquor & Beer.

IMFL products contain about 42.85% of alcohol. The consumption of CL is slowly on the





decreasing trend as some cheap IMFL is available. In spite of this, the CL industry is

growing at around 8%. However, government is taking necessary steps to restrict the illicit

liquor as it causes loss of revenue and spoils the health of the people, also bad quality may

lead to death of consumer. The major consumption of alcohol as of now is for alcoholic

beverages. Ethyl alcohol has the potential to become the fuel of the future relegating

gasoline to a secondary place.

The ethanol produced from the grains is superior in quality as compared with that from

molasses. It is estimated that IMFL market will require around 3000 million litres in the

year 2014 and expected to grow more than 50% in next 3 years. As Government declares

5% mandatory mixing of fuel ethanol in the gasoline thus there is great potential for new

distillery establishment.

(iv) Demand- Supply Gap

Not required in this Project. This depends on excise Department.

(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 ethanol 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

Export of Alcohol is currently governed by Govt. policy.

(vii) Domestic / Export Markets

Sales and Marketing division has always been a key focus area for our company. Over the years

we have reached a number of key customers through our initiatives. We have a thrust on

institutional Buyers which is a paradigm shift from the tradition of selling to wholesale market.

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

For smooth functioning of the plant, the company needs a team of 100 persons. These

persons are responsible towards their respective department such as Process Plant, Boiler

Operating Plant and administrative block. Here is the detail description of the manpower

requirement of the company.

Table 2

Manpower Requirement

S. No. Units Requirement

1. Process Plant 18

2. Raw material and Product handling 19

3. Boiler House Plant 8





4. Administrative Plant 15

5. Others 40

Total 100

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 project boundary &

project site layout) with coordinates





Figure - 1: Location Map





(ii) Key Plan

Figure - 2: Key Plan





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

particularly the environmental considerations gone into should be highlighted.

No alternative site has been taken into consideration as the proposed site has been

acquired by the company keeping in mind following mentioned factors:

� Grant of state excise permissions (LOI) for setting up distillery in the district/state.

� The proposed site falls in the safe groundwater zone.

� Raw material availability & markets for both products & by-products within the

state.

� Nearness to SH-32 (~ 2.5 km in WSW direction) & NH 113 (~10.5 Km in SE direction)

makes it easier to transport raw materials & final product to market.

(v) Size or magnitude of operation

The total proposed capacity of Grain Based Distillery is 90 KLPD & Co-generation Power

Plant is 3.0 MW.

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.

S. No. Units Capacity

1. Distillery (ENA / RS / IMFL /Ethanol) 90 KLPD

2. Co-Generation Power Plant 3.0 MW

(vi) Project Description with Process Details

Process Description of Grain Based Operation

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.





Fig. 3: Process flow chart For Grain Based Distillery





(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

List of raw materials & Chemical required, their source along with mode of transportation

are given below:

Table 3

Raw Material Requirement for Grain Based Distillery

S.

No.

Name of Raw Material Requirement Storage Source & Mode of

Transportation

1 Grains 208 TPD Silo & Godowns Through vendors / By

road

2 CHEMICALS

Sodium Hydroxide

(Caustic)

300 -350 Kgs Solid form packing in 50 kg

bags & Stored Godown

Nearby areas via road

Nutrients 200 Kgs Solid form packing in bags

& Stored Godown

Enzymes 200 Kgs Liquid form packed in cane

& Stored Godown

Antifoam Agent 100 Kgs Semi Solid form packing in

drum & Stored Godown

Yeast (Active Dry

Yeast/Distiller’s Yeast)

90 Kgs Solid form packing in bags

& Stored Godown

(b) Fuel Requirement

Rice husk or Indian coal or pet coke will be used for the proposed boiler of 30 TPH. Details

regarding fuel requirements are given below.

Table 4

Fuel Requirement

Name of Raw Material Quantity (MT per day) Source Of Materials

Rice Husk or 180 Through Local vendors / By road

Indian Coal 130 From Authorized Dealers By road

Pet coke 80 Nearby Refinery by road





(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.

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

given.

(a) Water Requirement and Source

Total water requirement for the proposed project will be 760 KLPD (746 KLPD for Plant

Process and 14 KLPD Domestic & Others).

Description Water consumption (KLPD)

Distillery Plant 746 KLPD (8.29 KL/KL)

Domestic use & others 14 KLPD

Total 760 KLPD

Source – Ground water

Water Requirement for Grain Based Operation

The total water requirement for the Grain based is estimated 746 KLPD, worked out as per

details given below:

Table - 5

Total Water Break-up

Water Type Total Water

first run Input

Total water

recycling

Total Fresh water

requirement after recycling

Process Water 562 440 122

Soft Water 702 348 354

DM Water 699 429 270

Total 1963 1217 746

KL/KL 8.29





Figure 4: Water balance for Grain based Operation





(b) Power Requirement and Source

The power requirement is 2.1 MW, which will be sourced from proposed 3.0 MW Co-

Generation Power Plant via a straight back pressure turbine.

(c) Steam Requirement

Steam consumption for the process and boiler de-aeration is 21.70 TPH, which will be

sourced from Boiler (30 TPH).

Table 6 Steam requirement

S. No. Purpose Steam Requirement TPH

1. Cooking & Liquefaction 3.17

2. Multi-pressure Distillation & Evaporation (Integrated) 10.66

3. DWGS Drier 5.91

4. Boiler De-aeration 1.96

Total 21.70

Boiler Details

A Boiler of 30 TPH capacity with ESP as APCE is sufficient to meet the requirements.

Others details regarding this are mentioned in the table given below:

Table – 7 Boiler details

S. No. Details

1. Type of Fuel Rice Husk/ Indian Coal/ Pet

coke

2. Capacity of Boiler 30 TPH

3. Stack Height Adequate stack height

4. Pollution Control Equipment Measures ESP/Bag Filter

Details regarding the D.G. Sets

2 Number of D.G. sets of 1000 KVA & 500 KVA will be installed for the power backup.

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

Table – 8 Details Regarding the D.G. Sets

S. No. Details

1. Type of Fuel HSD

2. Capacity 1000 KVA & 500 KVA

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

4. Pollution Control Equipment Measures Adequate stack height/ Acoustic





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

management/disposal

� The proposed project is based on “ZERO EFFLUENT DISCHARGE”.

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

of Suspended Solids separated as Wet Cake.

� Thin Slops from the Decanter Centrifuge 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).

� DWGS is taken to a dryer operating on steam and is dried to make it DDGS – Distillers

Dried Grain Solubles.

� The process condensate is cooled and collected into a neutralization tank with

sufficient residence time. After Neutralization, this process condensate will be

recycled into process and is used for green belt 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 sold to Brick manufacturers and Cement manufactures.

� Yeast sludge 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 & 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 project site is well connected to National Highway SH - 32 (~ 2.5 Km in WSW direction)

& NH-113 (~10.5 km in SE direction). The nearest railway station is Dungarpur Railway

Station (~ 58 km in West direction) and nearest airport is Maharana Pratap Airport,

Udaipur (~ 100 km in NNW 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

Total plant area is 20 acres (8.10 ha) and the same has been acquired by the company.





(iii) Topography

Topography of the core zone of the proposed project 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

Table 9

Environmental Settings of the Area

S. NO. PARTICULARS DETAILS

1. Nearest Village Dukwara Village (0.7 km in SE direction)

2. Nearest Town & City • Nearest Town: Ghatol (~12.5 km in ESE direction)

• District Headquarters: Banswara (~30 km in SSE

direction)

3. Nearest National Highway / State

Highway

• SH - 32 (~2.5 Km in WSW direction)

• NH - 113 (~10.5 Km in SE direction)

4. Nearest Railway station Dungarpur (~58 km in West direction)

5. Nearest Airport Maharana Pratap Airport, Udaipur (~ 100 km in NNW

direction)

6. National Parks, Wild Life

Sanctuaries, Biosphere Reserves,

Tiger/ Elephant Reserves, Wildlife

Corridors etc. within 10 km radius

No National Parks, Wild Life Sanctuaries, Biosphere

Reserves, Tiger/ Elephant Reserves, Wildlife Corridors

etc. falls within 10 km radius from the plant site.

7. Reserved Forests (RF) / Protected

Forests (PF) etc. within 10 Km.

radius

• Kundli Dudka Block PF (~3.5 km in ENE direction)

• Bhoyar Borda PF (~4.5 km in ESE direction)

• Loharia Block A PF (~7.0 km in WSW direction)

• Gargiyamarga Block PF (~7.5 km in ENE direction)

• Loharia Block B PF (~8.4 km in West direction)

• Suliya Venka Block PF (~8.5 km in North direction)

8. River / Water Body (within 10 km

radius)

• Budanpura Minor (~2.5 km in South direction)

• Mahi River (~5.7 km in NW direction)

• Mahi Canal (~7.2 km in East direction)

• Shakliya Nadi (~8.5 km in ESE direction)

• Som River (~9.0 km in NW direction)





9. Soil Type Black soil & Red soil

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

(v) Existing Infrastructure

Proposed project is new project. There are no existing infrastructures.

(vi) Soil classification

The soils of the district fall under the following broad categories

• Black soil

• Red soil

Black soil is found predominantly in the district mostly in northern, southern, central and

eastern parts. Red soil is mostly found in western portion of the district from north to

south.

(vii) Climatic data from secondary sources

Average annual rainfall of the district is 935.5 mm. However normal rainfall for the period

1901 to 1970 is 870 mm. The annual rainfall gradually decreases from southern part to

northern part. The maximum average rainfall is 1118 mm at Dhanpur and minimum average

rainfall is 790 mm at Loharia.

The climate of the district is dry except S-W monsoon season. The cold season is from

December to February and is followed by summer from March to June. From mid of

September to end of November constitutes post monsoon season. The district

experiences either mild or normal drought once in two years. Severe type of drought has

been recorded very rarely. Most severe type of drought has never occurred in the district.

(viii) Social Infrastructure available

There are primary schools, dispensaries, small hospitals, 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 proposed project is an distillery unit. Facilities required for the proposed 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

proposed project area.

(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) Assessment of infrastructure demand (Physical & Social)

The Company will assess the demand of infrastructure (Physical & Social) in nearby area of

the proposed site and will be developed in under corporate social responsibilities

programs

(iv) Amenities/Facilities

The Company will be developed the Amenities/Facilities in nearby area of the proposed

project 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)

Approx. 20 acre area will be required for proposed Distillery unit.

(ii) Residential area (Non Processing area)

Residential colony is not proposed for proposed project. The local labor will be preferred

to provide employment opportunities.

(iii) Green Belt

Greenbelt will be developed in 33% of the total area of the proposed project.

(iv) Social Infrastructure

Proposed project will result 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 proposed project is well connected with Road.

(vi) Industrial Waste management

The proposed Grain based distillery would be based on “ZERO DISCHARGE”.

(vii) Solid Waste Management

� 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 or

Prawn Feed.

� Ash from the Boiler will be sold to Cement and Brick manufacturers.

� Yeast sludge will be sent to the Sludge Drying Beds or may be added to the Wet

Cake.





(viii) Power requirement and source

The total power requirement for the proposed project will be 2.1 MW, which will be

sourced from Co generation power plant of 3.0 MW & D.G Sets (1000 KVA & 500 KVA) (for

emergency).

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).

Any rehabilitation and resettlement plan is not applicable in this case since there is no

habitation on the proposed site location.

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 within 2 to 3 years of commencement.

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

project.

� Total cost of the Project: Rs. 170.75 Crores

� Cost for Environment Protection Measures:

� Capital Cost: Rs. 20 Crores

� Recurring Cost/annum: Rs. 1.5 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.

The proposed project is expected to bring significant socio-economic and environmental

benefits both at local level as listed below:

SOCIAL INFRASTRUCTURE:

Social awareness programmes will be improved by the local authority such as sanitation

and hygiene, HIV Prevention Program.

Adult education and female education programme is planned to the illiterate adults and

backward females of the villages in the project surrounding area.

EMPLOYMENT POTENTIAL:





The project is going to create some employment. Due to this project activity, some

persons in the project area will be recruited as skilled and semi skilled workers by the

company as per its policy. Therefore, some employment and income are likely to be

generated for the local people. So, the project will contribute in a positive manner

towards direct employment in the project area. Some employment potential benefits are

given below:

� Long term employment of up to 60 people in the operation phase.

� Plus indirect employment shall be generated substantially.

BENEFITS TO THE REGION

The company will supply its product to the domestic market which is likely to improve the

regional economy.

PERIPHERAL DEVELOPMENTS:

The Company intends to take up developmental work in the periphery area. The activities

that have been considered include the following:

� Supporting existing schools for development of education in the area.

� Help in imparting vocational training to local eligible youth.

� Provide health facilities by way of medical check up, by holding medical camps etc.

in the neighbourhood.

Thus, the proposed project shall usher in the social and economic up-liftment of the

persons living in the vicinity of the Project i.e. of society at large.

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