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COSMIC FERRO ALLOYS LIMITED
PRE-FEASIBILITY REPORT
1
PRE FEASIBILITY REPORT
Proposed Expansion of Ferro Alloys Capacity by
Installation of 1x9MVA Submerged Electric Arc Furnace in
Phase-I and 6x9MVA Submerged Electric Arc Furnaces in
Phase-II
at
village Ghutgoria, P.O. Barjora,
Dist. Bankura, West Bengal
Project Proponent:
M/s Cosmic Ferro Alloys Limited Kolkata, West Bengal
Environment Consultant:
Recognised by MoEF (GOI) Notifn. No. D.L.33004/99 Dt.24.10.2007 NABL (DST GOI) Cert. No. T-1550 Dt. 16/05/2011 NABL (DST GOI) Cert. No.T-1826 dt. 04/10/2010
QCI-NABET Scheme for Accreditation of EIA Consultant ISO 9001:2008 vide Registration No. 44 100 094152-E3 Head Office: 60, Bajiprabhu Nagar, Nagpur-440 033, MS
Lab. : FP-34, 35, Food Park, MIDC, Butibori, Nagpur � 441122 Ph. : (0712) 2242077, 9373287475 Fax: (0712) 2242077 Email: [email protected], [email protected]
website: www.anaconlaboratories.com, www.anacongarway.com
September 2012
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INDEX
Sr. No.
Description Page no.
1.0 EXECUTIVE SUMMARY
2.0 INTRODUCTION OF THE EXPANSION PROJECT
2.1 Project Proponent
2.2 Need for Project
2.3 Employment Generation
3.0 PROJECT DESCRIPTION
3.1 Product and Raw Material
3.2 Manufacturing Process
3.3 Resource � Utilize & Recycling
3.4 Waste Water Generation
3.5 Air Emission
3.6 Solid Waste Generation
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Sr. No.
Description Page no.
3.7 Purpose of EIA Study
4.0 SITE ANALYSIS
4.1 Connectivity
4.2 Land Use / Topography
4.3 Infrastructure
5.0 PLANNING BRIEF
6.0 PROPOSED INFRASTRUCTURE
7.0 REHABILITATION & RESETTLEMENT (R&R) PLAN
8.0 PROJECT SCHEDULE & COST ESTIMATES
9.0 ANALYSIS OF PROPOSAL
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1.0 EXECUTIVE SUMMARY OF THE PROJECT
PLANT EXPANSION SUMMARY
Sr. No.
Description Details
01 Proposed project Proposed Expansion of Ferro Alloys Capacity by Installation of 1x9MVA Submerged Electric Arc Furnace in Phase-I and 6x9MVA Submerged Electric Arc Furnaces in Phase-II
02 S. No. of the schedule
Activity 3(a)
03 Location:
M/s Cosmic Ferro Alloys Limited has
proposed setting up of 6th furnace for
Phase-I and 6x9 MVA furnace for
Phase-II manufacturing of Silico
Manganese and high carbon Ferro
Manganese within the existing premises
near village Ghutgoria, P.O. Barjora,
dist Bankura in West Bengal. The index map and location is presented in Annexure-I
04 Plot/Survey/ Khasra No.
The land details are given in Annexure-I
05 Village/Town Ghutgoria village 06 Tehsil Barjora 07 District Bankura 08 State West Bengal 09 Land Requirement 25 acres of total 46.62 acres
10 Landuse Industrial area
11 Water Requirement 72 m3/d
12 Source of Water Tube well in project site
13 Power Requirement 25MW
14 Source of Power Damodar Valley Corporation
15 Employment 365
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2.0 INTRODUCTION
M/s Cosmic Ferro Alloys Limited has proposed setting up of 6th furnace in Phase-I and
6x9 MVA Furnaces for Phase-II for manufacturing of Silico Manganese and high carbon
Ferro Manganese respectively, within the existing premises near village Ghutgoria, P.O.
Barjora, dist Bankura in West Bengal. The company has identified an area of 25 acres
(10.11ha approx) for the expansion.
The 5th furnace of Phase-I on commissioning will produce 13,540 MTPA and 18,000
MTPA of Ferro Manganese. Thus with the expansion taken place up to 6th furnace the
total production capacity of the Phase-I plant will be 72,540 (14,400 + 14,400 + 14,400 +
13,540 + 15,800) Silico-Manganese MTPA and 1,03,3000 (21,600 + 21,600 + 21,600 +
18,000 + 21,000) Ferro-Manganese MTPA for Phase-I. The capacity utilization of the
proposed unit has been estimated at 86% graduating to 94% at optimum level.
2.1 Project Proponent
M/s Cosmic Ferro Alloys Limited is an ISO-9001:2000 Certified Company and accorded
the status of One Star Export House in accordance with the provisions of Foreign Trade
Policy, 2004-09 by the Office of the Joint Director General of Foreign Trade, Govt. of
India.
Cosmic Ferro Alloys Limited has installed production capacity of 75,000 tones of Ferro
Alloys annually. The Company has installed four 9 MVA Submerged Arc Furnace
equipped with pan casting facilities for slag and tramp free tapping, ensuring cleaner
product. The adequate Port facilities at Haldia & Kolkata helps distribution of its
products across the globe smoothly.
Quality Control is not a sporadic initiative at Cosmic Ferro Alloys Limited. It is a 24 x 7
obsession within the Organisation, reinforced by competent team which checks across
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PRE-FEASIBILITY REPORT
6
critical parameters for quality consistency, right from receipt of raw materials to
finished products. Sophisticated equipments has been installed for the purpose.
Superior raw materials are procurred and utmost care taken at Cosmic Ferro Alloys
Limited's state-of-art manufacturing facilities. The supplier includes MOIL, OMC and
more. Well connectivity of works with road and rail ensures uninterrupted supply of
inputs.
As a responsible corporate Cosmic Ferro Alloys Limited fundamentally believes in
environmental protection and thus installed all most modernized and sophisticated
Pollution Control Equipments strictly conforming the prescribed norms.
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2.2 Demand � Supply Gap
There is huge demand of ferro alloys by various integrated and mini steel plants. Apart
from this, ferro alloys has a big export potential.
Asia is the fastest growing region in the world.
India is the 2nd fastest growing economy in Asia.
Per capita income of India is USD 705 against USD 42,000 in USA. This presents
huge potential of growth.
Steel consumption in India is 40 Kg/Capita (1 kg for Stainless Steel) against
world average of 185 Kg (15 kg for Stainless Steel). This again presents
enormous potential for growth in India.
For Stainless Steel capacity increase forecast for India is �
o 2006-07 _ 2.52 Million Tons (Long Product : 650 Th)
o 2015-16 _ 5.67 Million Tons (Long Product : 2.1 Mi.T)
o New investment of USD 3 Billion by 2015.
Industrial Growth of India & China in excess of 9/10%.
Production Bases are shifting to Asia and more particularly to China & India.
So are exports increasing.
India is bestowed with adequate resources of all raw materials to produce alloy
& stainless steel.
Based on the demand and availability of Manganese Alloys, the resultant gaps/
surpluses on all India basis has been worked out as furnished in Table 1.2.
TABLE-1.2
RESULTANT GAPS/ SURPLUSES OF MANGANESE ALLOYS
ON ALL INDIA BASIS
(�000 tonnes) Year Demand Availability Resultant gap (-)/ Surplus (+)
Domestic With export
Without export With export
2011-12 915 1098 700 (+) 215 (-) 398 2019-20 1675 2010 700 (-) 975 (-) 1310
Source : Indian Ferro Alloys Producers Association.
It is observed that existing all India capacity is likely to face shortage of manganese
alloys in 2011-12 by 215,000 tones. This will increase to 975,000 tons in the year 2019-20.
Considering the export demand, country is likely to face shortage of 398,000 tons in
2011-12 and 1,310,000 tons in 2019-20.
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8
2.3 Need for Capacity Expansion
Alloy Steel Industry
The presence of one or more Ferro Alloys Manganese, Silicon and Vanadium, among
others, enhances strength and durability. The use of alloy steel has increased
substantially across the industrial, consumer durables and automobile industries, the
demand for which is expected to grow at a CAGR of 5% across 2013-14.
Stainless Steel Industry
This value-added product enjoys corrosion resistance due to a minimum 10.5%
chromium presence. Ferro Chrome is used as deoxidizer in the production of stainless
steel. Stainless steel�s resistance to corrosion and staining, low maintenance and luster
make it an ideal base material for a host of commercial applications like utensils,
infrastructure, automobile, builders� hardware and railways.
There is no substitute for chromium in stainless steel production, and is widely
practiced as the substitute for nickel to some proportion.
The growth of Ferro Alloys Industry is directly linked with the growth of Iron and Steel
Industry which in turn depend upon its user industry i.e. infrastructures and housing,
automobiles, consumer durables etc. About 90% of world Ferro Alloy production is
consumed by the Iron and Steel Industry with balance 10% being consumed by
engineering sector.
Ferro Alloys Sector
The robust 7.5% growth in global steel production strengthened the upstream demand
for ferro alloys by 7% in 2007-08 and China recorded the highest demand for ferro
alloys, followed by India and Russia.
India, with a 5-7% share of the global ferro alloys industry, is among the 10 largest
producers of the material in the world. In India, majority of the ferro alloys furnances
are largely located in Orissa, Andhra Pradesh, West Bengal, Chattisgarh and Goa due to
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PRE-FEASIBILITY REPORT
9
proximity to mines. Most ferro alloy companies manufacture manganese or chrome
alloys.
Indian bulk ferro alloys supply constitutes of Ferro Chrome about 32%, Ferro
Manganese and Silicon Manganese about 62% and rest others.
India enjoys a natural advantage as it has the fifth-largest in chrome ore with a 100
million tones estimated reserve and the sixth-largest in manganese ore with an
estimated 176 million tones reserve.
2.4 Employment Generation
Industrialization uplift the socio-economic standard of local people surrounding the
plant site due to proposed capacity increase. During the construction phase work will
be generated for skilled, semiskilled and unskilled labors. Technical persons will be
recruited during the operation phase. It is estimated to employ direct / indirect
employment of 365-400 people of various skills.
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3.0 PROJECT DESCRIPTION
The project envisages setting up of a sub merged electrical arc furnaces with 9 MVA
capacity. The capacity has been estimated to be utilized equally to manufacture Silico
Manganese and Ferro Manganese.
The production process using electrolytic process involves five main steps namely
a) Raw material preparation
b) Stock house
c) Blending of inputs as per receipts
d) Electric arc melting & production
e) Sizing of the Alloys
Plant layout with proposed capacity expansion details is attached as Figure � 1.
Environmental settings and infrastructures available surrounding the unit is as under,
Env. Settings
&
Infrastructure
Name & Aerial Distance
Town/City Durgapur 11 km, NE
Forest Beliator Protected Forest (0.8 Km) S
River Damodar River (7 km) NE
Village Ghutgoria
Railway
station
Durgapur 11 km, NE
National
Highway
Durgapur Expressway NH-2, 17 km, NE
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The Existing production capacity are shown below:
Furnace No.
Capacity Silico-
Mangane
se TPA
Ferro-
Manganese
TPA 1 9 MVA 10800 16200 2 9 MVA 10800 16200
3 9 MVA 10800 16200
4 9 MVA 10800 16200
5 9 MVA 13540 18000
Total 56740 82800
Grand total
139540
Proposed addition �
The proposed addition to production capacity are shown below:
Furnace
No.
Capacity Silico-
Manganese
TPA
Ferro-
Manganese
TPA
Phase-I
6 9 MVA 15800 21000
Phase-II
1 9 MVA 10800 16200 2 9 MVA 10800 16200
3 9 MVA 10800 16200
4 9 MVA 10800 16200
5 9 MVA 10800 16200
6 9 MVA 10800 16200
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3.1 Product and Raw Material
The raw material requirement of existing Capacity of Phase-I alongwith proposed 1x9
MVA are mentioned below.
Material Quantity, TPM Storage capacity (tones)
Phase-I (Existing 5 x9 MVA and
proposed 1x9 MVA)
Manganese ore 16283 Existing High MnO2 ore 2600 Existing Dolomite 2575 Existing Bauxite/Magnesite Nil Existing
Coal 667 Existing Iron ore Nil Existing Coke 5334 Existing
The raw material requirement of capacity after proposed expansion (Phase-II of 6x9
MVA) are mentioned below,
Material Quantity, TPM Storage capacity (tones)
Phase-II (6 x9 MVA)
Manganese ore 16283 Existing
High MnO2 ore 2600 Existing Dolomite 2575 Existing Bauxite/Magnesite Nil Existing
Coal 667 Existing
Iron ore Nil Existing Coke 5334 Existing
The quality of raw materials is key factor for effective plant operation. The raw materials
sources and composition required for proposed project are given Table 2.5. The principal raw
materials to be used are manganese ore and manganese bearing slag, dolomite, coke, silicon
electrodes, quartzite. Raw materials are available locally within a radius of 100 kms.
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This will procured from organized markets. The raw materials are abundantly available and
will be procured mainly from Manganese Ore India Limited, Tata Group, Graphite India
Limited and Damodar Valley Corporation. The Company is also proceeding to import raw
materials from the world known ore dealers like Eramet (Central Africa), BHP (Australia), CML
(Australia) to enhance the quality of its products to sustain in this competitive market. The
seasonal factors will not affect the working result of the unit and the company has in any way
drawn out sufficient stock of the required raw materials. The site is strategically located as
rich mining belt of West Bengal, Jharkhand and Orissa, which are in close vicinity. The
company also proposes to enter into long term arrangement with mine owners for supplying
of raw materials on a regular basis.
TABLE 2.5
SOURCES AND COMPOSITION OF RAW MATERIALS
Ore Sources Mn% Fe% SiO2% Phos% Mn/Fe
IMP Ore Australia 47.00 4.75 9.00 0.120 9.89
Pak Ore Pakisthan 21.24 18.43 28.05 0.108 1.15
Balaghat Nahpur 50.00 4.50 8.00 0.07 11.15
D.B.(C) Nagpur 44.93 9.50 11.04 0.27 4.73
MLR 40/42 Orissa 35.50 16.00 6.50 0.07 2.22
OMC
32/34
Orissa 28.00 22.00 11.52 0.08 1.27
OMC
28/30
Orissa 22.97 24.05 16.90 0.07 2.22
OMC LGHS Orissa 21.75 21.78 20.44 0.07 1.00
MANSER Nagpur 36.00 5.50 28.00 0.24 6.55
MOIL35/37 Nagpur 33.71 6.25 34.40 0.36 5.39
BG (C) Nagpur 45.39 4.25 154.22 0.097 10.68
BG (D) Nagpur 36.21 5.75 28.52 0.97 6.30
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FIGURE 2.3
MATERIAL BALANCE
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3.2 Manufacturing Process
The project envisages setting up of a sub merged electrical arc furnaces with 9
MVA capacity. The capacity has been estimated to be utilized equally to
manufacture Silico Manganese and Ferro Manganese.
The production process using electrolytic process involves five main steps
namely
a) Raw material preparation
b) Stock house
c) Blending of inputs as per receipts
d) Electric arc melting & production
e) Sizing of the Alloys
The Raw Material preparation plant consists of crushers and screen through
with the sizing ore required for process is prepared. The details of the
manufacturing process is given in the Figure 3
FIGURE 3
BRIEF PROCESS OF MANUFACTURING
Raw Material Bunker house
Feeding raw material to charging choot
Charging raw material to furnace
Charging power through electrode to furnace
Meting raw material with power
Taking hot metal every 2.5 hours
Taking hot metal in cast iron bay
WP holding period is 5-6 hours
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The stack house comprises of four charging bins one each for Manganese ore
coke breeze quartzite dolomite. The raw materials are lifted to the charging
platform of the furnace with the help of electric hoist. As per pre-determined
charge mix, materials are fed into the furnace.
The lower ends of the electrodes are maintained at about 0.9 to 1.5 meters (3
to 5 feet) below the charge surface. Three phase electric current arcs from
electrode to electrode, passing through the charge material. The charge
material melts and reacts to form the desired product as the electric energy is
converted into heat. The carbonaceous material in the furnace charge reacts
with oxygen in the metal oxides of the charge and reduces them to base
metals. The reactions produce large quantities of carbon monoxide (CO) that
passes upward through the furnace charge. The molten metal and slag are
removed (tapped) through 1 or more tap holes extending through the furnace
shell at the hearth level. Feed materials may be charged continuously or
intermittently. Power is applied continuously. Tapping can be intermittent or
continuous based on production rate of the furnace.
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3.3 Resource � Utilized & Recycling
Water
The water system required for the Plant may be broadly classified into two categories as
follows:
Sl.
No.
Consuming
Terminal
Requirement
1. Industrial Required for cooling of various parts of the
Furnace.
2. Drinking
and
sanitary
Required for drinking and sanitary purposes for
the Water.
Plant�s personnel and for the Plant�s cleaning
and washing purposes.
Consumption of Water
Requirement of water at various consuming point including industrial, drinking, sanitary and
miscellaneous uses are furnished in Table2.3.
TABLE-2.3
WATER CONSUMPTION DATA/FURNACE
Sl.
No.
Consuming
Terminal
Quality Quality
in circulation
M³ / day
Terminal
Pressure
Kg/ cm²
Looses
Circulation
M³ / day
1. Submerged
Electricity
Arc Furnace
Clear /
Soften.
150
4.5 5.00
2. Drinking
Sanitary &
Laboratory
use
Raw Water 1.00
Total
quantity of
make up
water
required.
6.00 M³ / day
The Table gives the quality of water required in circulation, and the total quantum to be fed in
the system as make up.
It is apparent from the above Table that the total quantity of makeup water required for the
proposed Plant is about 72.00 M³ /day. Out of the above quantity 65.00 M³ /day water are
not required to be filtered and the 7.0 M³ /day. may be filtered and chlorinated for drinking
and sanitary purposes. Make up water required in the closed circuit cooling handling D.M.
Water is only nominal. Schematic diagram water flow for SAF is shown in Figure 2.2
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Sources
The make up water required for the proposed Ferro Plant will be made available from sub soil. The
permission letter from Government of West Bengal is enclosed as Annexure-III.
Storage of Water
Under Ground Storage Tank having capacity of 500 KL for Soft Water / Raw Water have been
provided in the system.
FIGURE 2.2
SCHEMATIC DIAGRAM WATER FLOW FOR SAF
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Power / Energy
The power requirement of the company will be met from Damodar Valley Corporation
(DVC) to the tune of 8000 KVA (9 MVA). The Power Supply is intended from Damodar
Valley Corporation at a 33 KV feeder to the G.O.D.
Emergency Power
One 100 KVA diesel generating set is provided for supplying LT power to various
critical areas like cooling water pump, crane and lighting to take care of process work
during main power supply failure. Diesel @ 20 liters per hour will be required during
operation of DG.
3.4 Waste Water Generation
As the water requirement is only for cooling purpose and there would minimal
discharge to the outside area. Hence at present there appears no requirement
for any Effluent treatment plant. Domestic discharge from canteens and toilets
must be channeled through proper sewage channels and soak pits. Should any
situation arise for discharge for liquid effluents, necessary treatment facility
will be incorporated.
3.5 Air Emission
Activities of the material handling, machine operations, Debagging, Crushing and Sweeping
are the important aspects of air pollution. Cutting and welding operation, loading-unloading,
operation are mainly responsible for the release of heavy concentrations of SPM, RSPM, SO2,
Nox etc. However the overall impact may be rated as direct short-term, adverse and their
magnitude is from low to high. Water spraying is considerable as an important measure to
reduce the intensity of such pollution.
The details of stack emission (with APC) Table 4.2, the details of proposed
stack connected with fume extractor is given in Table 4.3
TABLE 4.2
DETAILS OF STACK EMISSION (WITH APC)
Stack Connected to Re-
heating Furnace Existing unit Proposed unit
Height from GL 30 M 30 M
Duct Diameter 1.5 m 1.5 m
Exit Temp. 100 - 120 oC 100 - 120
oC
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Exit Velocity 8 - 9 m/s 8 - 9 m/s
Gas Flow Rate (Nm3/hr) 91281 10000
PM (mg/Nm3) 19 22
SO2 (mg/Nm3) 10 13
TABLE 4.3
DETAILS OF PROPOSED STACK CONNECTED WITH FUME EXTRACTOR
Stack Connected To Suction Hood/Fugitive Emission
Stack from GL 30 m
Diameter of Stack 1.5 M
Diameter of Duct 0.9 Sq m.
Gas Temperature Normal Temp.
Dust Collection Quantity 0.12 mt + 0.17mt =0.29 mt/day
The following measures for minimizing adverse impact on the environment
have been incorporated
(i) Fume extraction system with appropriate Air pollution control System to
control the emissions from the process and fugitive emissions at furnace
will be installed. Particulate matter emission from de-dusting units will be
maintained below 100 mg/NM3.
(ii) All de-dusting units will be connected to a stack of height 30 m. The stack
height calculated for proper dispersion of SO2 (with the formula of H=
14Q0.3
. Where Q= emission of SO2 in kg/h, comes to 17.24 m and 19.46
m for the two stacks.
(iii) The fugitive emissions of suspended particulate matter (SPM) will be
maintained below the standards at a distance of 10 m (approx.) from the
source.
(iv) Appropriate disposal of solid waste.
(v) Possibility for utilization of waste heat will be explored for pre-heating and
/ or drying of raw materials and for utilization in adjacent plants.
The on site & off-site emergency plan will be an integral part of any major
hazard control system. It will be based on those accidents identified by the
works management, which could affect people and the environment outside
the works. The responsibility for the off-site plan will be likely to rest either
with the works management or with the local authority.
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Fugitive Emission Control
Apart from the Stack attached to the SA Furnace, there would be dust
generation at the product tapping hole and in the raw material handling
section. To curb the spreading of the dust into the other areas of the plant the
management shall install Bag filter System at tapping hole and raw material
handling system to keep the atmosphere inside the plant clean and ambient
air quality within norms.
Fugitive emissions can also be kept low by making pucca haul roads within the
premises and making arrangements for water spraying at all the dusty places
in the premises and during loading, unloading process.
1. Control of Stack Emissions and Fugitive Emissions will have a direct impact
on the ambient conditions.
2. Water Sprinkling System at dusty areas and loading / unloading zone.
3. Storage of raw materials in covered space.
4. Development of planned green belt in the industry will also control ambient
conditions. The objective for providing plantations are as under:
a) To act as wind shelter and prevent air pollution in surrounding area.
b) To act as a natural sink to absorb dust and sequester carbon.
c) To act as a medium to absorb noise energy and reduce noise.
d) Plantations absorb air borne dust.
e) Plantations provide shed.
3.6 Solid Waste Generation
There will be no hazardous wastes from the plant process. Solid waste
generated will be:
TABLE � 2.7
SOLID WASTE GENERATION (PER FURNACE)
Unit Quantity Disposal
From SA Furnace 20.88 TPD Used for low land filling &
road making
From APC System 3.5 TPD Reuse after cakes making
Fume extractor system
for molten metal taping
section
0.5 TPD Reuse after cakes making
The Solid waste is the Slag for the manufacturing process of FeMn and SiMn.
The 100% Slag of FeMn is being used to produce SiMn. The slag of SiMn is
being reused for further extraction in the manufacturing process of SiMn when
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the slag of SiMn is no more value for production of SiMn, the slag is
dispatched of to fill up the low land inside the plant boundary.
Precontionary measures have taken to store the left over stock of Slag
materials in a safe place for 100% consumption on the followed days.
The slag is being stored at the slag yard which has been constructed with a
non-permeable lining having 1.5 mm high density polyethylene geomembrane
and over lying 90 cm soil clay lining followed by 125 mm RCC flooring. It is
not required to store the slag for a long time. We consumed the slag within 3-
5 days of its production
1. 2.3 MT of Mn is used for Producing FeMn/MT
2. Total Qty of mixing material is 19.5/MT per heat.
3. Total Qty of FeMn production and Qty of Slag per heat is 7.5 M.Ton (metric
ton) of FeMn and 6.5 M.Ton of slag.
4. Time duration each heat and total nos of heat per day 3 hours and 8 heats
per day.
5. Total Qty. Slag generated for FeMn per heat is 6.5 M.Ton.
6. This slag is being used to manufacture SiMn.
For SiMn are as follows
I) Mn 1.53 MT for SiMn/MT.
II) 22 MT of mixing material per heat.
III) 8.75 MT of SiMn and 8.75 MT of slag per heat.
IV) 3 hours and 8 heats per day.
V) 8.75 MT slag generated per heat.
This slag is being reused for further extraction to produce SiMn.
3.7 Purpose of EIA Study
Considering the products & project location of the expansion project it is noticed that
the proposed project falls under Category 3 (a) �A� of the Schedule-I of EIA Notification
2006 and amendments thereof.
The required construction of new projects or activities or the expansion or
modernization of existing projects or activities listed in the Schedule to this notification
entailing capacity addition with change in process and or technology shall be
undertaken in any part of India only after the prior environmental clearance from the
Central Government or as the case may be, by the State Level Environment Impact
Assessment Authority
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SITE ANALYSIS
Connectivity
Cosmic Ferro Alloys location is well connected with road, rail and air route. Details
about the connectivity with proposed project site is shown in below table.
Sr. No.
Description of Connectivity
Distance in Kms.
1 National Highway (Durgapur Expressway NH � 2)
17 km, NE
2 Railway station, Durgapur 9.6 km, NE
3 Domestic Air port
(Kolkata)
155
3.8 Land Use / Topography
------------------------
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3.9 Infrastructure
Key infrastructures are available at or near by the running unit is described below.
Sr. No.
Description Available within 10 km around the project
1 Marine Sanctuary No
2 Stream / Rivers Yes (Damodar
River)
3 Airports Yes (Kolkata� 155
Km)
4 Railway station Yes (Durgapur�
9.6 Km, NE)
5 Bus Station Yes
6 National Highways Yes (NH � 2) (17
kms)
7 Bank Yes
9 Social Infrastructure
Primary School Yes
Religious Place Yes
4 PLANNING BRIEF
Proposed expansion activities will be started after getting statutory clearance form
related authorities. The project will be completed in 2013.
Further proposed expansion activities will take care of all the rules and regulation of
statutory authority and provide the control measure and devices to achieve the
standard norms.
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5 PROPOSED INFRASTRUCTURE
Sr. No.
Infrastructure Description
1 Total area 46.62 acre
2 Processing area (Plant
area)
As mentioned in Layout plan.
3 Non-processing area
(Residential area)
No plan to expand.
4 Green belt As per statutory requirement.
5 Social Infrastructure As mention in para 4.3
6 Connectivity As mention in para 4.1
7 Drinking water
management
Water supply from tube wells through
treatment plant
8 Effluent Treatment
plant
Nil
9 Industrial waste
management
Proper EMP shall be in place in EIA
report.
9 Solid waste
management
Proper EMP is in place in EIA report.
10 Power requirement &
Supply source
9 MVA
Source : Damodar Valley Corporation
6 REHABILITATION & RESETTLEMENT (R&R)
PLAN
Rehabilitation & Resettlement (R&R) plan is not applicable to this expansion project as
it is already a running unit.
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7 PROJECT SCHEDULE & COST ESTIMATES
Proposed expansion activities will be started after getting statutory clearance form
related authorities. The project will be completed in the year 2013.
7.2 Project Cost Estimates
SL
No Particulars
Rupees in Lakhs
1 Land & Site Development Existing
2 Buildings 359.10
3 Furnace Plant & Machinery -
indigenous 702.15
4 Pollution control equipment 150.60
5 Electrical equipment 213.35
6 Misc. Fixed Assets 204.56
7 Contingencies 40.74
8 Pre-operative expenses 87.00
9 Margin money for working
Capital 486.13
Total Project cost 2243.63
8 ANALYSIS OF PROPOSAL
We have analyzed our proposal and found following financial & social benefits to the
local people in the project area.
1. Employment to approx. 365 local people as direct and 100 people as indirect
employment is envisaged and they all will be employed from local.
2. Farmers will get adequate fertilizers which is in short supply now.
3. Govt. will get additional revenue.
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