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PRE-FEASIBILITY REPORT By CHANDU CATTLE FEEDS 10 KLPD GRAIN BASED ETHANOL UNIT & 50 TPD CATTLE FEED UNIT at Plot no. 31 & 30 B of Sy. No. 432/2 Part, APIIC Industrial park, Kakuturu village, Venkatachalam mandal, SPSR Nellore, Andhra Pradesh

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Page 1: PRE-FEASIBILITY REPORT - environmentclearance.nic.inenvironmentclearance.nic.in/writereaddata/FormB/TOR/PFR/15_Nov... · PRE-FEASIBILITY REPORT By CHANDU CATTLE FEEDS ... This hot

PRE-FEASIBILITY REPORT

By

CHANDU CATTLE FEEDS 10 KLPD GRAIN BASED ETHANOL UNIT

& 50 TPD CATTLE FEED UNIT

at

Plot no. 31 & 30 B of Sy. No. 432/2 Part, APIIC Industrial park, Kakuturu

village, Venkatachalam mandal, SPSR Nellore, Andhra Pradesh

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Pre-feasibility Report

10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

TABLE OF CONTENTS

Chapter –1: EXECUTIVE SUMMARY ..................................................................................................................1

1.0 ABOUT THE PROPOSED PROJECT ......................................................................................................1

Chapter – 2 : INTRODUCTION OF THE PROJECT / BACKGROUND INFORMATION ..............................................2

2.1 IDENTIFICATION OF PROJECT AND PROJECT PROPONENT ................................................................2

2.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT ............................................................................2

2.3 DEMAND – SUPPLY GAP ..................................................................................................................2

2.4 EMPLOYMENT GENERATION DUE TO THE PROJECT .........................................................................3

Chapter – 3 : PROJECT DESCRIPTION ................................................................................................................4

3.1 TYPE OF PROJECT.............................................................................................................................4

3.2 LOCATION OF PROJECT ....................................................................................................................4

3.3 SIZE AND MAGNITUDE OF OPERATION ............................................................................................6

3.5 MANUFACTURING PROCESS .......................................................................................................6

3.5.1 RECTIFIED SPIRIT / ETHANOL.....................................................................................................6

3.5.2 CATTLE FEED .............................................................................................................................8

3.6 RAW MATERIAL REQUIREMENT FOR PROPOSED DISTILLERY .......................................................... 10

3.7 WATER REQUIREMENT AND ITS SOURCE ........................................................................................ 10

3.8 WASTE WATER GENERATED AND IT’S MANAGEMENT .................................................................... 10

3.9 SOLID WASTE GENERATED AND IT’S MANAGEMENT....................................................................... 10

Chapter – 4 : SITE ANALYSIS ........................................................................................................................... 11

4.1 CONNECTIVITY ............................................................................................................................... 11

4.2 LAND USE AND LAND OWNERSHIP ................................................................................................ 11

4.3 TOPOGRAPHY ................................................................................................................................ 11

4.4 EXISTING LAND USE PATTERN ........................................................................................................ 11

4.5 EXISTING INFRASTRUCTURE ........................................................................................................... 11

4.6 CLIMATIC DATA FROM SECONDARY SOURCES ............................................................................... 11

Chapter – 5 : PLANNING BRIEF ....................................................................................................................... 12

5.1 PLANNING CONCEPT ..................................................................................................................... 12

5.2 POPULATION PROJECTION ............................................................................................................. 12

5.3 LAND USE PLANNING ..................................................................................................................... 12

5.4 AMENITIES / FACILITIES ................................................................................................................. 12

Chapter – 6 : PROPOSED INFRASTRUCTURE ................................................................................................... 13

6.1 INDUSTRIAL AREA (PROCESSING AREA).......................................................................................... 13

6.2 RESIDENTIAL AREA (NON PROCESSING AREA) ................................................................................ 13

6.3 GREENBELT .................................................................................................................................... 13

6.4 SOCIAL INFRASTRUCTURE .............................................................................................................. 13

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Pre-feasibility Report

10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

6.5 CONNECTIVITY ............................................................................................................................... 14

6.6 DRINKING WATER MANAGEMENT ................................................................................................. 14

6.7 ENVIRONMENT MANAGEMENT PLAN ............................................................................................ 14

6.7.1 AIR EMISSION AND ITS MANAGEMENT ................................................................................... 15

6.7.3 WASTEWATER GENERATION AND ITS MANAGEMENT ............................................................. 15

6.8 POWER REQUIREMENT AND SUPPLY........................................................................................ 15

Chapter – 7: REHABILITATION & RESETTLEMENT (R & R) PLAN ....................................................................... 16

Chapter – 8 : PROJECT SCHEDULE & COST ESTIMATES .................................................................................... 17

8.1 PROJECT SCHEDULE ....................................................................................................................... 17

8.2 PROJECT COST ................................................................................................................................ 17

Chapter – 9 : ANALYSIS OF PROPOSAL ............................................................................................................ 18

9.1 TECHNO COMMERCIAL VIABILITY .................................................................................................. 18

9.2 FINANCIAL AND SOCIAL BENEFITS .................................................................................................. 18

9.3 SOCIO-ECONOMIC DEVELOPMENTAL ACTIVITIES ........................................................................... 18

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Pre-feasibility Report

10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

1

Chapter –1: EXECUTIVE SUMMARY

1.0 ABOUT THE PROPOSED PROJECT

Chandu cattle feeds is an existing unit located Plot no. 31 & 30 B of Sy. No. 432/2 P, APIIC

Industrial park, Kakuturu village, Venkatachalam mandal, SPSR Nellore, Andhra Pradesh.

At present unit is producing cattle feed using Spent wash as raw material.

Now it is proposed to put up 10 KLPD grains (maize, broken rice, bajra, jowar and other

starch containing raw materials) based ethanol unit in the existing site premises. After the

installation of the proposed project the spent wash generated from the Ethanol unit will be

used as raw material for producing cattle feed.

Project Details

Name of the company Chandu Cattle feeds

Registered address Plot no. 31 & 30 B of Sy. No. 432/2 Part, APIIC

Industrial park, Kakuturu village, Venkatachalam

mandal, SPSR Nellore, Andhra Pradesh

Corporate office D.no. 26-13-492, back side of Mother Teresa

home, B.V Nagar, SPS Nellore

Factory Plot no. 31 & 30 B of Sy. No. 432/2 Part, APIIC

Industrial park, Kakuturu village, Venkatachalam

mandal, SPSR Nellore, Andhra Pradesh

Constitution Proprietary

Promoters of the project Puli Niveditha

Proprietrix

Line of Activity Manufacture of

Rectified Spirit / ENA / Ethanol / Industrial

Alcohols / Potable Alcohol / Grain Impure Spirit

with Denatured Spirit

Cattle feed

Calcium hydroxide

Source of Plant &Machinery

Supplies

Indigenous Technology.

Proposed Capacity Rectified Spirit / ENA / Ethanol / Industrial Alcohols

/ Potable Alcohol / Grain Impure Spirit with

Denatured Spirit – 10 KLPD

Cattle feed – 50 TPD

Calcium hydroxide – 2 TPD

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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Chapter – 2 : INTRODUCTION OF THE PROJECT / BACKGROUND INFORMATION

2.1 IDENTIFICATION OF PROJECT AND PROJECT PROPONENT

Chandu cattle feeds is an existing unit located Plot no. 31 & 30 B of Sy. No. 432/2 P, APIIC

Industrial park, Kakuturu village, Venkatachalam mandal, SPSR Nellore, Andhra Pradesh.

At present unit is producing cattle feed using Spent wash as raw material.

Now it is proposed to put up 10 KLPD grains (maize, broken rice, bajra, jowar and other

starch containing raw materials) based ethanol unit in the existing site premises. After the

installation of the proposed project the spent wash generated from the Ethanol unit will be

used as raw material for producing cattle feed.

Promoters

The proposed project of the Ethanol Plant would be undertaken & implemented by the

management of Chandu Cattle feeds. The promoters have made a thorough study of entire

project, planning as well as implementation schedule.

The names and designations of the Promoters are as under:

S.No Name Designations

1. Puli Niveditha w/o Puli Sudhakar Proprietrix

2.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT

At present unit is producing cattle feed using Spent wash as raw material.

Now it is proposed to put up 10 KLPD grains (maize, broken rice, bajra, jowar and other

starch containing raw materials) based ethanol unit in the existing site premises. After the

installation of the proposed project the spent wash generated from the Ethanol unit will be

used as raw material for producing cattle feed.

2.3 DEMAND – SUPPLY GAP

The Center’s ‘Gasohol Program’ of blending 5% ethanol in petrol has given an assured scope

for ethanol industry in the country. The Center’s Kisan-friendly imitative has definitely been

a boost to the venture. Following statistics could show how there is definite market

potential for such industry.

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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PETROL CONSUMPTION

10000000 KILO Liters

500000 KILO Liters - 5% ALCOHOL required

500000000 Ltrs.

Demand all over Country 5000 Lac liters

Existing Production 1840 Lac liters

Total demand 2460 Lac liters

In view of the above, we proposed to go for Ethanol unit in the existing unit premises.

2.4 EMPLOYMENT GENERATION DUE TO THE PROJECT

The plant will be continuous and automatic in operation, with necessary control

instrumentation.

The personnel required for all operations are listed below with their grades. The man power

required for the industry is 20 Nos. which is inclusive of permanent basis and temporary or

contract basis.

Skilled : 5 no.s

Semiskilled : 10 no.s

Unskilled : 5 no.s

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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Chapter – 3 : PROJECT DESCRIPTION

3.1 TYPE OF PROJECT

Proposed project is an Ethanol unit along cattle feed unit for production of Rectified Spirit /

Ethanol & cattle feed at Plot no. 31 & 30 B of Sy. No. 432/2 Part, APIIC Industrial park,

Kakuturu village, Venkatachalam mandal, SPSR Nellore, Andhra Pradesh.

Following is plant configuration and production capacity (Products / By products):

S.No. Product / By Products Quantity

Products

1. Rectified Spirit / ENA / Ethanol / Industrial Alcohols / Potable

Alcohol / Grain Impure Spirit with Denatured Spirit

10 KLPD

2. Cattle feed 50 TPD

By-products

3. Calcium Hydroxide 2 TPD

3.2 LOCATION OF PROJECT

Chandu cattle feeds is an existing unit located Plot no. 31 & 30 B of Sy. No. 432/2 Part,

APIIC Industrial park, Kakuturu village, Venkatachalam mandal, SPSR Nellore, Andhra

Pradesh.

At present unit is producing cattle feed using Spent wash as raw material.

Now it is proposed to put up 10 KLPD grains (maize, broken rice, bajra, jowar and other

starch containing raw materials) based ethanol unit in the existing site premises. After

the installation of the proposed project the spent wash generated from the Ethanol unit

will be used as raw material for producing cattle feed.

Total land taken on lease is 1.6 acres (6,454 Sq.m)

The Coordinates of the proposed site is 14°20'42.9", 079°55'32.5"

Nellore town is at a distance of 6 Kms. (aerial) from the Plant site.

Kanupuru kaluva is flowing at distance of 50 mts (aerial) from the plant site.

NH # 5 is passing at distance of 0.5 Kms. (aerial) from the plant site.

Kanupuru west RF, Kakuturu RF, Kantepalli RF, Kanupuru East RF, Chemudugunta RF,

Dontali RF, Amancharla RF, Ambapuram RF, Nellore RF, Kondlapudi RF, Mopuru RF,

Toderu RF, Biradavolu RF, Kasumuru RF, Marupuru RF exist within study area.

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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3.3 SIZE AND MAGNITUDE OF OPERATION

Chandu Cattle feeds is an existing unit producing cattle feed using Spent wash as raw

material.

Now it is proposed to put up 10 KLPD grains (maize, broken rice, bajra, jowar and other

starch containing raw materials) based ethanol unit in the existing site premises. After the

installation of the proposed project the spent wash generated from the Ethanol unit will be

used as raw material for producing cattle feed.

S.No. Product / By Products Quantity

Products

4. Rectified Spirit / ENA / Ethanol / Industrial Alcohols / Potable

Alcohol / Grain Impure Spirit with Denatured Spirit

10 KLPD

5. Cattle feed 50 TPD

By-products

6. Calcium Hydroxide 2 TPD

Proposed Distillery plant will be operational for 330 days in a year.

3.5 MANUFACTURING PROCESS

3.5.1 RECTIFIED SPIRIT / ETHANOL

The processes of manufacturing of cattle feed is relatively simple and consist of

reduction of size of grains,

heating,

Fermentation,

Condensation,

Separation of spirit from spent wash

Distillation

The selected Grains will be passed through a bulk chain conveyer and dropped into the

grinder to reduce the size of the particles to the required mesh size. The different powdered

raw material will be taken to the liquefaction tank with the help of grinder blower. This

liquefaction tank will be half filled with normal water from water storage tank No 1. The

agitator of the liquefaction tank will mix grain powder with water uniformly inside of the

tank. Alfa amylase enzyme will be added at time of mixing. After mixing uniformly, this liquid

will be sent to jet cooker with the help of pump motor. The cooker will be half filled with

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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normal water and heated up to 100°C temperature at water boiling point. The liquid from

the liquefaction tank will be slowly fed into the cooker with hot water with the help of pump.

The agitator of the cooker will enable thorough mixing of fermentable mash and hot water in

the cooker. The fermentable mash in cooker will be subjected to 4 hours of continuous

heating process till temperature reaches up to 90°C. This heating will be with help of

industrial burners using furnace oil as fuel.

When the temperature of the liquid is between 87°C- 90°C, the solution becomes as Maize

soup. This hot Maize soup will be transferred in to the fermenters with the help of Gear

motor pump. After Complete transfer to the fermenters, (the fermenters have their own

cooling coils inside and jackets outside ) the soup will be cooled with the help of cooling coils

with continuous water pumping from water tank and recycle the same water. The same

water will flow up to 3 hour continuously through cooling coils. The temperature of the

maize soup will be decreased up to 30°C. The temperature of the maize soup will be

maintained in between temperature levels 32°C- 36°C at the time of fermentation with help

of jackets and cooling coils.

At the time of fermentation the Maize soup will be the stirred with the help of agitator which

are fixed in fermentation chambers. At this stage, 4 Kg of Yeast powder will be added to each

and every fermenter to ferment Maize soup. After adding Yeast powder, 1 Litre of liquor

Ammonia as well as another Enzyme Gluco amalyze will be added. The liquor ammonia helps

to maintain pH and nutrient food for yeast cells to grow very rapidly thus resulting in

completion of fermentation in short time. Glucose amylase Enzyme added will convert starch

into sugar. Every day temperature levels of the fermenter will increase or decrease due to

whether condition.

To raise the temperature of the Fermenters Thermic fluid will be injected (This thermic fluid

oil will be heated with industrial burners using furnace oil at thermic fluid oil tank furnace) to

the jacket. To decrease the temperature levels of the fermenters, cool water from water

storage tank will be passed through fermenter cooling coils and same water will be recycled

further. This process will continues up to 24 hours for each and every fermenter.

We will be having 2 nos of water storage tank with fixed cooling towers on top of each water

tanks. First one is for cooling hot soup at fermenters and second one is for cooling S.S

condenser jackets and S.S cooling coils.

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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After complete fermentation, spent wash will be generated. Sample of Spent wash will be

collected and sent to the lab for testing purpose. After confirming the quality of spent wash,

the same will be transferred to reactor (This reactor has their own jacket to circulate heated

thermic fluid oil). Spent wash will be subjected to heating continuously for 3 hours to reach

the desired temperature of 78°C temperature. At this constant temperature between 78°C to

80°C, the vapors from reactor will be passed through the separate stainless steel cooling coils

and sent to the Stainless steel Condenser. The liquid formed will be sent to the receiver tank

with the help of sucking vacuum pump.

The rectified spirit will be transferred to the Tray Filter from receiver tank with help of flame

proof centrifugal pump to absorb H2O from spirit by using of Quick Lime Powder (CaO). The

rectified spirit slowly dropped in to the trays and passed through Quick Lime Powder at trays.

The Quick Lime Powder will absorb only H2O and release 99.9% pure spirit (Ethanol). This

Ethanol will be sent to storage tank. The Calcium Hydroxide generated through tray filter

process, will be sent to cement brick manufacturing Industries and remaining Bio syrup

(Spent Wash) will be sent to the Bio syrup storage tank for the further process to

manufacture cattle feed.

3.5.2 CATTLE FEED

The manufacturing of cattle feed involves the following

Blending of various grain husk and dry grass

Thorough mixing of spent wash with husk & dry grass

Drying

The selected grain husks or dry grass chips are passed through bulk chain conveyer dropped

into a screw conveyer. The spent wash will be uniformly mixed with with blended grain husk

and dry grass in screw conveyer.

The material extruded from screw conveyor will be in wet cake form. This wet cake is called

as DWGS (Distillery wet grains with soluble).

This wet cake will be taken to the dryer to dry. After drying this wet cake becomes dry grade

(Mash) form. This dry mash is called as DDGS (Dried Distillery Grains with soluble). This

Product is then packed in plastic bags (PP Bags) and will be transported to dairy farms.

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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PROCESS FLOW DIAGRAM

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3.6 RAW MATERIAL REQUIREMENT FOR PROPOSED DISTILLERY

Following are the raw material requirement:

S.NO. RAW MATERIAL SOURCE QUANTITY (TPD)

METHOD OF TRANSPORT

1 Grains (Maize, Corn, Sorghum Grain, Broken rice and Starch based grains, etc.)

Local area 24 By Road (Covered trucks)

Dry grass / grain husk Local area 26 By Road (Covered trucks)

2 FUEL : Industrial burners

Furnace oil Local areas / HPCL

2 KLPD Tankers

3. Calcium Oxide (CaO) Piduguralla 1 By Road (Covered trucks)

3.7 WATER REQUIREMENT AND ITS SOURCE

Water required for the proposed project will be sourced from Ground Water sources / from

River Penna.

Water required for the proposed project will be 60 KLPD

3.8 WASTE WATER GENERATED AND IT’S MANAGEMENT

Spent wash generated will be mixed with dry husk and grain husk and will be sold as cattle

feed in wet cake form or dried form after drying. No spent wash will be discharged to the

outside premises.

Only source of waste water generation will be cooling tower blowdown and sanitary waste

water.

3.9 SOLID WASTE GENERATED AND IT’S MANAGEMENT

Following will be solid waste generation and its management from the proposed project:

S.No Solid waste Total Quantity (TPD) Disposal

1. Calcium Hydroxide

2 Will be given to cement industries

2. Waste lube oil 300 lit/annum Will be given to the SPCB approved vendors

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Chapter – 4 : SITE ANALYSIS

4.1 CONNECTIVITY

The project site can be approached by NH # 5. The project site is at a distance of 6 Kms. from

Nellore. The nearest Airport is at Renigunta at a distance of 90 Kms.

4.2 LAND USE AND LAND OWNERSHIP

Total envisaged for the proposed project is 1.6 acres (6454 Sq.m) and same is taken on lease.

4.3 TOPOGRAPHY

The topography of the land is flat without undulations.

4.4 EXISTING LAND USE PATTERN

1.6 acres (6454 sq.m) acres of land is envisaged for the proposed project. The land is taken

on lease.

There are no ecologically sensitive places like national park, sanctuary, biosphere

reserve, etc. around 10 Kms. radius of the site. Few Reserve forest exists within the study

area. There is no route of migratory animals within the project site.

4.5 EXISTING INFRASTRUCTURE

As Nellore is very near to the site, well laid roads are available for transportation,

educational facilities are available.

4.6 CLIMATIC DATA FROM SECONDARY SOURCES

The climatic conditions of the district consist of extremely hot summers and moderately hot

winters and may be classified as tropical. The period starting from April to June is the

hottest. The annual rainfall in the region is about 1028 mm and is contributed to by the

Southwest monsoon. Three types of soils viz., Black Cotton (57.6%), Sand clay loams (22.3%)

and Red loams (19.4%).

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10 KLPD Grain based Ethanol unit along with 50 TPD Cattle feed unit

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Chapter – 5 : PLANNING BRIEF

5.1 PLANNING CONCEPT

The proposed project is fermentation type industry in which starch containing raw materials

will be fermented for manufacturing Rectified Spirit / Ethanol and cattle feed will be

manufactured using Spent wash as raw material

5.2 POPULATION PROJECTION

The project will be providing employment to nearly 20 workers. The local persons will be

given preference in employment as per the qualification and technical competencies. The

above manpower covers the top management, middle and junior level executives and

other supporting staff including workforce.

5.3 LAND USE PLANNING

Total land envisaged for the proposed project is 1.6 acres (6454 sq.m) and same in

possession of management. Following is breakup of land use:

S.No. Particular Extent of Land (In Sq.m)

1. Built up area including storage 1421.26

2. Greenbelt 2491.00

3. Open area including open roads 2541.74

Total 6454.00

5.3 ASSESSMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL)

The road facility is already available which shall be used and maintained. Infrastructure

facilities like road transport, Post & Telegraph, Telephone, Banks etc. are basics for each and

every area.

5.4 AMENITIES / FACILITIES

A well planned office will be provided having sufficient space to accommodate executives

and staff. It will be equipped with telephones and Internet facilities.

Facilities like canteen, rest room and indoor games facilities will be provided in the proposed

plant as basic facilities to workers.

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Chapter – 6 : PROPOSED INFRASTRUCTURE

6.1 INDUSTRIAL AREA (PROCESSING AREA)

The following plant and machinery will be installed in the Industrial processing area

1. Tanks for liquefaction

2. Tanks for fermentation

3. Distillation

4. Bulk conveyor

5. Screw conveyor

6.2 RESIDENTIAL AREA (NON PROCESSING AREA)

No colonization is proposed in the proposed project.

6.3 GREENBELT

More than 1/3rd of total land availability is reserved for plantation i.e. greenery.

Greenbelt development plan

Local DFO will be consulted in developing the green belt.

Greenbelt of 33% of the area will be developed in the plant premises as per CPCB

guidelines.

The tree species to be selected for the plantation are pollutant tolerant, fast growing,

wind firm, deep rooted. A three tier plantation is proposed comprising of an outer

most belt of taller trees which will act as barrier, middle core acting as air cleaner and

the innermost core which may be termed as absorptive layer consisting of trees

which are known to be particularly tolerant to pollutants.

6.4 SOCIAL INFRASTRUCTURE

With the start of Construction phase, various employment opportunities will be generated.

Several persons will be benefited with contract works, employment through contractor,

running of jeep and buses, canteens, different kind of shops and transport related business

avenues. Peoples will be provided with either direct employment or indirect employment

such as contract work, development work like road etc.

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6.5 CONNECTIVITY

The project site can be approached by NH # 5. The project site is at a distance of 6 Kms. from

Nellore. The nearest Airport is at Renigunta at a distance of 90 Kms.

6.6 DRINKING WATER MANAGEMENT

Drinking water for the proposed project will be sourced ground water sources. It is estimated

about 2 KLD will be required for domestic and drinking purpose during operation of the

proposed plant.

6.7 ENVIRONMENT MANAGEMENT PLAN

The major objective and benefit of utilizing Environmental Management Plan in project

planning stage itself, is to prevent avoidable losses of environmental resources and values as

a result of Environmental Management Plan. Environmental Management Plan includes

protection/mitigation/enhancement measures as well as suggesting post project monitoring

programme. It may often suggest additional project operations that have to be incorporated

in the conventional operation.

The industrial development in the study area needs to be with judicious utilization of non-

renewable resources of the study area and within the limits of permissible assimilative

capacity. The assimilative capacity of the study area is the maximum amount of pollution

load that can be discharged in the environment without affecting the designated use and is

governed by dilution, dispersion, and removal due to Physic-chemical and biological

processes. The EMP is required to ensure sustainable development in the study area of the

proposed plant site, hence it needs to be all encompasses plan for which the proposed

industry. Government, regulating agencies like pollution control board working in the region

and more importantly the affected population of the study area need to extend their

cooperation and contribution.

It has been evaluated that the study area has not been affected adversely as there are no

major polluting industries in the study area and likely to get economical fillip. The affected

environmental attributes in the region are air quality, water quality, soil, land use, ecology

and public health. The management action plan aims at controlling pollution at the source

level to the possible extent with the available and affordable technology followed by

treatment measures before they are discharged. Environmental management plan aims at

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the preservation of ecosystem by considering the pollution abatement facilities at the plant

inception.

6.7.1 AIR EMISSION AND ITS MANAGEMENT

The air pollution will be due to industrial burners and emissions from the same discharged

through a combined stack of 30 m height. The particulate emissions from the burners will be

below 50 mg/Nm3

DG sets: The industrial unit is planning to have one DG set of 2 x 125 kVA as backup to state

power supply. As per the applicable norms, the DG sets will be housed in an acoustic

chamber. The combustion emission outlet, of the DG set, will be provided with a muffler

along with a minimum stack height of 7.5 m above the height of nearest building.

6.7.2 SOLID WASTES GENERATION & ITS MANAGEMENT

Following is solid waste generated and its management from the proposed project:

S.No Solid waste Total Quantity (TPD) Disposal

1. Calcium Hydroxide 2 Will be given to cement industries

2. Waste lube oil 300 lit/annum Will be given to the SPCB approved vendors

Hazardous Waste Generation

The plant facility will result in generation of spent oils (lubricants and transformer oil), which

will be stored on site and sold to SPCB authorised recyclers.

6.7.3 WASTEWATER GENERATION AND ITS MANAGEMENT

Spent wash generated will be mixed with dry husk and grain husk and will be sold as cattle

feed in wet cake form or dried form after drying. No spent wash will be discharged to the

outside premises.

Only source of waste water generation will be cooling tower blowdown and sanitary waste

water.

6.8 POWER REQUIREMENT AND SUPPLY

Power required for the proposed plant will be taken from APSPDCL.

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Chapter – 7: REHABILITATION & RESETTLEMENT (R & R) PLAN

No rehabilitation and resettlement is required as there are no habitations in the in the

Project site.

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Chapter – 8 : PROJECT SCHEDULE & COST ESTIMATES

8.1 PROJECT SCHEDULE

The plant will be implemented in 6 months from the date of receipt of Environmental

Clearance from the Hon’ble MoEF & NOC from SPCB.

8.2 PROJECT COST

S.No. Particulars

AMOUNT

(Rs. In lacs)

1. Land Development & Civil Works : 137 Lakhs

2. Plant & Machinery : 305 Lakhs

3. Interest During Construction : 53 Lakhs

4. Preliminary & Pre-Operative Expenses : 2 Lakhs

5.

Margin Money for Working Capital &

Contingency : 65 Lakhs

Total : 562 Lakhs

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Chapter – 9 : ANALYSIS OF PROPOSAL

9.1 TECHNO COMMERCIAL VIABILITY

The techno –commercial viability of the proposed ethanol unit is proved as the following

factors significantly favour setting up the unit.

Assured supply of grains in abundance around the factory.

Establishment of Plant & Machinery to handle broken rice to manufacture all or any

of the two finished products RS/Ethanol

Viability of the project is established beyond doubt with broken rice as input raw

materials.

The proposed process and plant and machinery makes the project environmental

friendly.

The proposed manufacture of fuel ethanol makes the country that much less

dependent on imports of petroleum product (fuel).

To the extent of its installed capacity, production of fuel ethanol improves energy

security & self-sufficiency and saving of foreign exchange for the country.

9.2 FINANCIAL AND SOCIAL BENEFITS

With the implementation of the proposed project, the socio-economic status of the local

people will improve substantially. The land rates in the area will improve in the nearby areas

due to the proposed activity. This will help in upliftment of the social status of the people in

the area.

9.3 SOCIO-ECONOMIC DEVELOPMENTAL ACTIVITIES

The management is committed to uplift the standards of living of the villagers by

undertaking following activities / responsibilities as the part of Corporate Social

Responsibility.

Education for poor

Lighting

Providing books to all poor children.