FORM – I

TERMS OF REFERENCE

&

PRE-FEASIBILITY REPORT

For

5,00,000 (2 X2,50,000 TPA in two phases)

CALCINED PETROLEUM COKE PLANT

At Kalagarh Village,Mahakalpada Tehsil,

Kendrapara District, Odisha.

By

INDIA CARBON LIMITED

PREPARED BY

B.S. ENVI-TECH (P) LTD Secunderabad - 500 017

NABET Accreditation No: NABET/EIA/1316/RA002

1

CONTENTS

CHAPTERS

1. Executive Summary

2. Introduction of the Project / Background information

3. Project Description

4. Site Analysis

5. Planning Brief

6. Proposed infrastructure

7. Rehabilitation and resettlement (R & R) Plan

8. Project schedule & Cost Estimates

9. Analysis of proposal (Final Recommendations)

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CHAPTER - I

1.0 EXECUTIVE SUMMARY

M/s. INDIA CARBON LIMITED (ICL), India’s leading producer of

Calcined Petroleum Coke, provides the right blend of people &

products to serve the needs of the Aluminum, Steel, & other Carbon

consuming industries.

Calcined Petroleum Coke (CPC) is used extensively as Anode in

Alumina Smelters, as Soderberg's Electrode for Ferroalloy Industries,

and in the manufacturing of Graphite/ Graphite Electrodes, and

Thermal Paste for Ferro Alloys & allied industries in Submerged Arc

Furnaces.

CPC is also used in various Steel Industries for - Melting of Steel,

Recurburisation and for making Special Steels & Alloys.

The Company, established in 1961 was founded by Mr. B.

Himatsingka and is a pioneer of the Calcining industry having set up

Asia's first Calcination Plant at Guwahati in 1962. ICL since

inception, has also been in Technical & Financial Collaboration with

Oxbow Calcining LLC (formerly Great Lakes Carbon LLC) USA -World

Leaders in the Calcined Petroleum Coke field. The Company then went

ahead and established its second calcination plant in 1969 at Budge

Budge, West Bengal.

India Carbon's primary business is the manufacture and supply of

high quality Calcined Petroleum Coke (CPC) which is the purest form

of Carbon, containing over 99.5% of it. Along with the Calcined Coke

the Company also specializes in the production of Electrode Carbon

Paste (ECP) and Tamping Paste used widely in the Ferro Alloys and

Allied industries and also in the production of Carbide. Both the

Electrode Carbon Paste as well as the Tamping Paste are produced

from a mixture of different carbonaceous material (CPC, Calcined

Anthracite Coal, etc.) and Soft Pitch which is used as a binder.

The primary raw material used by ICL for its operations is Raw

Petroleum Coke, frequently referred to as RPC which is purchased

from Oil refineries all over the world. RPC itself is produced from the

3

thermal cracking of crude.

Some of the primary customers for ICL in the aluminium industry are

National Aluminium Company Limited (NALCO), HINDALCO

Industries Limited (HINDALCO), Bharat Aluminium Company Limited

(BALCO) and Madras Aluminium Company Limited (MALCO), Vedanta

etc.. Some of the major consumers in the steel industry are Steel

Authority of India Limited (SAIL), Tata Iron and Steel Company

Limited (TISCO) and Essar Steel, whereas Graphite India Limited and

Hindustan Electro Graphite Limited are some of our customers from

the Graphite industry.

The Company is constantly undertaking activities with a view on

Research & Development, thus enabling itself to maintain its position

on the leading edge of technology.

A unique combination of experience, technology & teamwork goes into

every ton of Calcined petroleum coke that ICL ship's to meet the most

demanding requirements. An unerring focus on consistency, and

working continuously towards maximum value creation for both it's

customers as well as it's shareholders are principles ingrained in the

Company. ICL's ability to maintain Leadership is based on it's

commitment to Quality, Long Term Relationships & Reliability of

supply.

Apart from the production of an industrial raw material such as CPC,

in 1991 ICL's dynamic management team also led the Company into

the field of floriculture through the establishment of orchid farms in

Guwahati, Assam. The orchid flowers are currently being sold

primarily in the cities of Bangalore, Mumbai, New Delhi and Kolkata,

but the Company is looking ahead to new export possibilities.

ICL is also one of the few Companies to go beyond the required norms

for the betterment of the environment. Conservation of energy and

water resources has forever been a key objective for the Company.

Moreover, the installation of high end Gas Cleaning Systems has

ensured that industrial pollution is kept to a minimum and is causing

no damage to the environment. Few things would prove the

Company's care for flora and fauna better than the fact that they are

growing some of the worlds most beautiful and delicate flowers on the

very premises in which their factory operates.

4

ICL proposes to set up a Greenfield Coke Calciner Project for

manufacturing of 5,00,000 TPA (2,50,000 TPA in each phase) of

Calcined Petroleum Coke (CPC) in an area of 8.52 Ha (21.05 acres) at

Kalagarh Village, Kendrapara District, Odisha .

Raw Petroleum Coke shall be imported. Raw pet coke will be imported

and also purchased from indian refineries .

Water requirement of the plant is 1200 m3/day for both phases and

the same will be met from Ground water / public supply

No solid waste generation from the plant.

Wastewater generation is only from domestic use and the same is

treated in Sewage Treatment Plant.

There are no wild life sanctuaries, national parks, elephant/tiger

reserves within 10km radius of the study area.

Plant site has been selected in the vicinity of Paradip Port. Paradip has

adequate infrastructural facilities like highways, broad gauge rail

lines, water source. Paradip Port is one of the major ports of India and

is the main outlet and inlet of the sea-borne trade of the eastern part

of India.

Greenbelt will be developed in about 2.81 Ha.

The total power requirement for the plant is estimated to be about

2500 kW which will be met from the Captive Power Plant and from

CESCO/OSEB.

1x1000 kVA DG sets will be installed as standby power supply units.

These DG sets will be operated only when there is a power supply

failure.

Plant expected to be commissioned by March 2021 (2 years after

MOEF & CC Clearance)

Total capital Investment Cost is Rs. 315 Crores. and Rs. 60 crores

will be spent for Environmental Management Plan. Includes

incinerator, Gas cleaning plant &FGD

5

2.0 INTRODUCTION OF THE PROJECT / BACKGROUND

INFORMATION

i. IDENTIFICATION OF PROJECT AND PROJECT PROPONENT. IN

CASE OF MINING PROJECT, A COPY OF MINING LEASE / LETTER

OF INTENT SHOULD BE GIVEN.

M/s. India Carbon Limited (ICL) proposes to set up a Greenfield

Coke Calciner Project for manufacturing of 5,00,000 TPA of Calcined

Petroleum Coke (CPC)(2x2,50,000 TPA) in an extent of 8.52 ha. (21.05

acres) at Kalagarh Village, Mahakalpada Tehsil, Kendrapara District,

Odisha .

ii) Brief description of nature of the project

The basic raw material, Green Petroleum Coke (GPC), is calcined into

the end product called Calcined Petroleum Coke (CPC). Rotary

Calcination Technology is being adopted for the Plant as this process

shall produce good quality of CPC.

The calcined coke industry is considered part of the pyro-processing

industry. Its profitability is usually controlled by the aluminium

industry’s performance, blending quality, cost of feed stocks and

transportation costs.

The plant operations are continuous in nature, except during planned

maintenance periods / break-downs. The GPC consumption per

annum will be 3,37500 TPA (on dry basis for each phase. The

expected yield is above 85 % .

II. Need for the project and its importance to the country and or

region.

There are several reasons for setting up this Petroleum Coke Calcining

unit in India. First, the local Indian Aluminum Industry currently is in

a rapid expansion mode. Second, the competing Indian CPC producers

are comparatively smaller in production capacities. Lastly, a new CPC

Plant can benefit from a valuable income stream by co-generating

electricity by recovering heat from the process flue gases evolved

during calcination of GPC.

6

Benefits of the New Project are:

Substantially improved quality of CPC produced.

Meet the increase in demand in the region.

Increased availability factor due to the Process technology

adopted.

III. Demand– supply Gap

Demand is increasing and supply is inadequate as some are

importing.

IV. Imports Vs. Indigenous production.

The indigenous product will be more economical when compared to

the imported.

V. Export possibility

The Project is basically conceived to cater to the Indian Market.

However, being located close to the Port facilities, export

opportunities can be explored down the line to earn valuable foreign

exchange for the country.

VI. Domestic / export markets

The demand in domestic front is continuously improving and

the project is considered to meet the same. Export may be considered

VII. Employment generation (direct and indirect) due to the

project

The establishment of the Plant would aid in the overall social and

economic development of the region. The plant will give direct

employment to about 30 people. In addition, there will be indirect

employment to many more people in the form of business

opportunities, service facilities etc. This will enhance their economic

status and lead to better social environment.

7

3. PROJECT DESCRIPTION

I. Type of project including interlinked and interdependent

projects, if any.

This is a green field project. And there is no interlinked or

interdependent projects envisaged.

II. Location (map showing general location, specific location, and

project boundary & project site layout) with coordinates.

The proposed plant will be located in Kalagarh Village, Kendrapara

District of Odisha. Fig - 1 shows the location map of the Plant.

This plant site is a part of the Survey of India Toposheet No. 73/L/11.

The average altitude of 3 m above MSL. The latitude and longitudes of

the plant site are given below:

S. NO LATITUDE LONGITUDE

1. 20°22'27.80"N 86°31'10.00"E

2. 20°22'27.30"N 86°31'10.60"E

3. 20°22'27.10"N 86°31'10.80"E

4. 20°22'26.50"N 86°31'11.00"E

5. 20°22'22.90"N 86°31'9.90"E

6. 20°22'18.90"N 86°31'6.60"E

7. 20°22'18.50"N 86°31'4.60"E

8. 20°22'18.30"N 86°31'2.70"E

9. 20°22'19.30"N 86°31'0.80"E

10. 20°22'18.90"N 86°31'0.20"E

11. 20°22'17.90"N 86°30'58.20"E

12. 20°22'21.00"N 86°30'59.10"E

13. 20°22'21.00"N 86°30'59.20"E

14. 20°22'23.40"N 86°30'59.50"E

15. 20°22'28.40"N 86°30'59.60"E

Fig – 2 shows the Key Map of the ICL.

Fig. – 3 show the 10 km radius topographical map and the salient

feature around the plant is given in Table -1.

Fig – 4 shows the plant layout of the project site.

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9

10

11

12

TABLE - 1

SALIENT FEATURES OF THE PROJECT SITE

Feature Details

Altitude 3 m above msl

Longitude & Latitude 20°22'17.90"N - 20°22'28.40"N,

86°30'58.20"E - 86°31'11.00"E,

Village, Tehsil, District,

State

Kalagarh Village, Kendrapara District of

Odisha, India

Area 8.52 Ha

Annual rainfall 1475 mm

Nearest water bodies Nuna Nadi – 2.2 km – N Gobari Nadi – 8.2 km – NE Kula Nadi – 0.8 km – SE

Nearest Highway National Highway (NH-5A) Cuttack –Paradip -

0.07 km - N

Nearest Railway station Paradip RS – 14.2 km - SE

Bird sanctuaries/National

Parks

None within 10 km radius

Nearest Industries None within 10 km radius

Nearest Villages Kalagarh – 0.3km – N

Jadupur – 1.0 km – ESE

Nearest Town Cuttack – 67.0 km - WNW

Nearest Port Area Paradip Port – 20.0 km – SE

Inter State Boundary Odisha – West Bengal – 174.0 km – NNE

Nearest Air port Bhubaneshwar – 110 km – WSW

Nearest Forest None within 10 km radius

Historical places None within 10 km radius

* All distances mentioned in the above table are aerial distances.

III. Details of alternate sites considered and the basis of selecting the

proposed site, particularly the environmental considerations gone

into should be highlighted.

The Project site at Kalagarh Village, Kendrapara District of Odisha.

Plant site has been selected in the vicinity of Paradip Port. Paradip has

adequate infrastructural facilities like highways, broad gauge rail

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lines, water source. Paradip Port is one of the major ports of India and

is the main outlet and inlet of the sea-borne trade of the eastern part

of India.

IV. Size or magnitude of operation.

It is proposed to set up a Greenfield Coke Calciner Project consisting

of two streams, amounting to a total manufacturing capacity of

5,00,000 ( 2x 2,50,000) TPA of Calcined Petroleum Coke (CPC) in

the first phase with corresponding Process Heat recovery based Power

generation totalling to a capacity of 3MW.

V. Project description with process details (a schematic

diagram/ flow chart showing the project layout ,

components of the project etc. should be given)

Pet coke calcination is a high temperature pyrolysis treatment of green

coke with the major objective being to produce a coke having

properties suitable for a particular end use. It is a process whereby

green or raw petroleum coke is thermally upgraded to remove

associated moisture and volatile combustible matter (VCM) and to

otherwise improve critical physical properties, e.g. electrical

conductivity, real density and oxidation characteristics. The calcining

process is essentially a time- temperature function. The most

important variables to control are heating rate, VCM to air ratio and

final temperature. To obtain the calcined coke properties necessary for

its end use by the amorphous carbon or graphite industries, the coke

must be heat treated to temperatures of 1200-1500 °C to refine its

crystalline structure.

The eventual quality of the calcined coke is directly related to the

particular characteristics/quality of the green coke fed to the calciner.

While calcination cannot improve upon certain quality limits inherent

in the green coke, potential quality can be lost by improper calcining,

e.g., by using incorrect heating rates and/or atmospheric conditions.

The calcination of petroleum coke in a rotary kiln involves several

steps. As the wet coke is fed to {the rotary kiln, the residual moisture

in the coke is first driven off. As the coke feed advances down the

kiln, the volatiles commence to leave the particles. The particles, now

14

devoid of moisture and volatiles begin to heat rapidly and they

experience and expansion phase followed by a contraction phase in the

hottest, firing end of the kiln and just prior to being discharged from the

kiln. The final density of the material is a critical measurement of the

quality of the product, which is largely affected by adjusting the heat

intensity within the kiln in the section following the devolatilizing

The hot calcined coke leaves the kiln at a temperature in the range of

1200-1500°C and discharges into a rotary cooler where it is cooled to

100°C by both a water spray and with air flowing co-current to the flow of

the hot coke. The exhaust gases leaving the cooler are vented into an

incinerator . The gases are pure air, except moisture practically pure air

(with the exception of the moisture from the water spray) and provide the

preheated oxygen necessary for combustion in the incinerator.

In the calcining kiln, the volatiles that are driven from the petcoke are

partially burnt . In order to minimize the amount of coke burned, and

consequently lost as product, the burning process in the kiln is done

under reducing conditions by closely regulating the amount of

combustion air to the kiln. Not only is the amount of air controlled, but

the points of entry into the kiln are also closely managed. This is done by

mounting the combustion air fans onto the kiln shell and having a

multitude of air inlet points along a specified length and section of the

kiln. The process heat furnished to the rotary kiln for calcination is from

two sources. The initial source of the process heat is the amount of oil

fired through kiln burner. . Main source of process heat is the burning of

the certain percentage of the evolved volatile matter in the kiln.

The evolved volatile matter which is not burnt in the kiln together with the

products of combustion and particulates are carried out of the kiln and

into the incinerator where combustion is completed.

The incinerator exhaust gases are high in heat content, and in this

application they are passed on to waste heat recovery boiler then

scrubbing system, which passes through ID fan and stack.

Process flow diagram is shown in Fig – 5.

VI. Raw material required along with estimated quantity, likely

source, marketing area of final product/s, mode of

transport of raw material and finished product.

15

The Raw Material required for the Project is GPC on dry basis. The

Annual requirement is shown below:

RAW MATERIAL REQUIREMENT

Raw Material Required Quantity (TPA) on

Dry basis

Green Petroleum coke 3,37,500

SOURCE

GPC has to be procured from refineries producing Anode grade Green

Coke. Accordingly, most of the GPC will be sourced from various

refineries in North America, South America, Middle East and Asia.

TRANSPORTATION

Paradip Port, a natural harbor, exists at a distance of approx. 20.0

km. The raw material / finished product will be handled through port,

as required.

GPC will be brought to the plant site in covered trucks. The raw

material will be unloaded from trucks and will be conveyed to the

covered storage area. .

The same way the finished product will be bagged as needed and

despatched thro.. inthrough trucks. In case of export, the same port

facilities shall be utilized.

16

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17

VII. Resource optimization / recycling and reuse envisaged in

the project, if any, should be briefly outlined.

No Industrial waste water will be generated. Only domestic sewage will

be generated, which is treated in septic tanks followed by soak pit.

Sewage water of 16m3/day will be generated.

.

VIII. Availability of water its source, energy / power requirement

WATER

The water requirement of the plant is about 1200 m3/ day for each

phase and the same will be sourced from the Ground/Public Supply.

WATER BALANCE (m3/day)

REQUIREMENT CONSUMPTION/ EVAPORATION

WASTEWATER

CALCINATION

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FLOOR WASH 20 10 10

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19

POWER

The Proposed Power generation from the plant is 3MW from WHRB.

IX. Quantity of wastes to be generated (liquid and solid) and

scheme for their management / disposal.

The total fresh water requirement of the plant is 1200 m3/day.

Of the total water consumption of about 1200 m3/day in the plant,

wastewater generation is estimated to be about 126 m3 / day.

.

The domestic waste water of 16 m3 / day will be going to septic tank

followed by the soak pit.

LAND ENVIRONMENT AND CONTROL MEASURES

The Project will be located in an area of 21.05 Acres (8.52 Hectares).

There is no solid waste generation from the plant.

ICL will keep open areas to an extent of 2.81 ha. and take up green

belt development wherever possible in these areas.

X. Schematic representations of the feasibility drawing which

give information of EIA purpose.

Fig. – 5 shows the process flow diagram which represent the EIA

purpose.

20

CHAPTER – IV

4.1 SITE ANALYSIS

I. Connectivity

Nearest railway line connecting Cuttack – Paradip of South Eastern

Railway line is located at a distance of 10.2 km to SSW direction from

the site. The nearest railway station is Paradip RS at 14.2 km in SE

direction.

The National Highway (NH-5A) connecting Cuttack – Paradip is located

at a distance of about 0.07 km in N direction. Bhubaneshwar airport is

at 75.0 km in WSW. The Harbour is located at Paradip which is 20.0

km in SE direction.

II. Land form, land use and land ownership

A barren land of 21.05 acres (8.52 Hectares),acquired by ICL, is

available for setting up the Project.

III. Topography (along with map)

Topography of the proposed site appears almost flat. Foundation for

building, main structures shall be based on geotechnical report. The

geo technical investigations will be conducted at site.

About 21.05 acres of land has been identified to implement the

proposed project. The proposed site comprises mostly of barren land.

The proposed site reveals that the terrain is almost flat. No major

cutting and filling is required during construction stage. No major HT

lines / Power cables are passing through the proposed site. No major

streams are passing through the site area.

The site is located at an average elevation of 3 m above Mean Sea

Level (MSL). There are no sensitive areas surrounding the plant area.

Fig. – 3 show the 10 km radius topographical map and the salient

feature around the plant is given in Table -1.

21

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.

The Project will be located in an area of 21.05 acres in plant site.

LAND BREAKUP

S.No. Area Name Area in acres

1 Process Area 9.0

2 Storage Area 3.0

3 Utilities & Roads 2.05

4 Green Belt 7.00

Total Area 21.05

V. Existing infrastructure

There is no existing infrastructure available inside the Project Site.

VI. Soil classification

Soil in this area showed Sandy loam in texture.

VII. Climatic data from secondary sources

Regional Meteorology

The climate of this area is characterized by high humidity nearly all

the year round, and oppressive summer season and good seasonal

rainfall. Summer starts from mid of February and continues up to

first week of June, when the monsoon breaks. The monsoon continues

till the end of September. Winter is between November and middle of

February. The peak of summer is in May. The maximum temperature

is about 45.70C. During the cold months of December the temperature

falls to 7.8 .0C. The average rainfall of the district is 1457 mm.

22

WIND

Mean wind speed generally vary between 8-10 kmph. With maximum

being in July during the SW monsoon and in December during the NE

monsoon. The wind direction is generally between south and west

quadrant during the months of March to September, while it is from

the North to East quadrant during October to December. January and

February are transition months in which the wind direction is

variable.

VIII. Social infrastructure available

The area experiences humid climate and most of the area in the study

zone is well developed under the industries. All the infrastructure is

available in the region with good rail,road and surface water facilities.

No improvement of any infrastructural facilities are required for the

new project.

CHAPTER – 5

5. PLANNING BRIEF

I. Planning concept (type of industries, facilities, transportation

etc) town and country planning / development authority

classification.

The plant is based on Advanced Rotary Calciner Technology which is

more environment friendly and highly efficient with the following

advantages.

Part requirement of external fuel.

Improved quality of CPC

More Energy Efficient.

Better availability of equipment

The Project envisages utilisation of a low end by product of refineries -

Green Petroleum Coke (GPC) and converting it to a carbon enriched

product - Calcined Petroleum Coke (CPC). Valuable power is also

generated by recovering the heat from the Flue gases evolved in the

Process.

23

The finished product, CPC is an important input material for the

Aluminium Industry. It is also used in Steel and Titanium di-oxide

industries.

II. Population projection

ICL will employ about 100 persons directly for operation of the plant

III. Land use planning ( breakup along with greenbelt etc.,)

A land of 21.05 acres (8.52 Hectares) has been developed for the

project. The land breakup / land-use pattern is presented below,

LAND BREAKUP

S.No. Area Name Area in acres

1 Process Area 9.0

2 Storage Area 3.0

3 Utilities & Roads 2.05

4 Green Belt 7.00

Total Area 21.05

IV. Assessment of infrastructure demand (physical & social )

At present there are no major infrastructure facilities available inside

the plant area.

V. Amenities / Facilities

The amenities and facilities have to be developed for the project.

24

CHAPTER – 6

6.1. PROPOSED INFRASTRUCTURE

I. Industrial area (processing area)

The proposed plant will be located in Kalagarh Village, Kendrapara

District of Odisha. The land is well developed and all the infra

facilities are available. .

II. Residential area ( non-processing area)

Residential area is not proposed in the present project. Instead the

industry will help the surroundings in the development activities.

III. Green belt.

ICL will take up green belt development in the Open areas of 7.00

acres with plantation of trees.

IV. Social infrastructure.

Implementation of the plant will result in the following benefits:

a. Employment will be provided to the eligible persons both during

construction and operational phase

b. Temporary employment for people from the neighboring villages

during construction phase.

c. Community development activities such as :

Conducting Health camps for surrounding villages.

Providing infrastructure to schools including uniforms, black

board, course material, text books etc

Sponsoring rural sports and adult education.

V. Connectivity (traffic and transportation road/ rail/ metro/

water ways etc.,)

Nearest railway line connecting Cuttack – Paradip of South Eastern

Railway line is located at a distance of 10.2 km to SSW direction from

the site. The nearest railway station is Paradip RS at 14.2 km in SE

direction.

25

The National Highway (NH-5A) connecting Cuttack – Paradip is located

at a distance of about 0.07 km in N direction. Bhubaneshwar airport is

at 75.0 km in WSW. The Harbour is located at Paradip which is 20.0

km in SE direction.

VI. Drinking water management (source & supply of water)

The Drinking water requirement of the plant is about 20 m3/ day. The

water requirement will be sourced from the utilities.

VII. Sewerage system

The domestic waste water estimated is around 16 m3/day. For that

the septic tank followed by the soak pit is envisaged.

VIII. Industrial waste management

Total of 110m3 per day will be generated out of which 85 m3 will be

used for Greenbelt Development and 25m3 is recirculated in the

process .

WASTEWATER GENERATION TREATMENT AND DISPOSAL

No wastewater generation is envisaged from the process. The

wastewater generation from the plant is estimated to be about

16 m3/day.

WASTEWATER GENERATION, M3/DAY

WASTEWATER

Calcination plant 70

Power Plant 40

Domestic wastewater 16

Total 126

Domestic waste is about 16 m3/day will be generated.

IX. Solid waste management.

There is no solid waste generation from the plant.

26

X. Power requirement & supply / source.

The estimated overall plant power requirement is 3MW and the same

will be sourced from captive cogen. Plant / Odisha Transco Grid.

CHAPTER – 7

7. REHABILITATION AND RESETTLEMENT (R & R) PLAN

Policy to be adopted (central / state) in respect of the project

affected persons including home oustees, land oustees and

landless labourers (a brief out line to be given).

No rehabilitation is required in the plant site area.

CHAPTER – 8

8. PROJECT SCHEDULE & COST ESTIMATES

I. Likely date of start of construction and likely date of

completion (time schedule for the project to be given).

The Site activities will be commenced duly after receipt of

Environmental Clearance. It is expected that commercial operations

would be started by Jan 2021

II. Estimated project cost along with analysis in terms of

economic viability of the project.

The estimated project cost is around Rs 315 Crores and Rs 60

crores will be spent for Environmental Management Plan.

Since the Product CPC is expected to be in short supply in India by

the time the Project commences Commercial Operations, (Owing to

additions to Aluminium Production capacity), the project is expected

to be economically viable and generate good profits.

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CHAPTER - 9

9. ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS)

Financial and social benefits with special emphasis on the benefit

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

The establishment of the Plant would aid in the overall social and

economic development of the region. The plant will give direct

employment to about 100 people. In addition, there will be indirect

employment to many more people in the form of business

opportunities, service facilities etc. This will enhance their economic

status.