28 Outputs

FORM-I FOR

CAPACITY ADDITION OF INTEGRATED STEEL PLANT FROM 5.0 MTPA TO 10.0 MTPA AND

CAPTIVE POWER PLANT FROM 300 MW TO 600 MW AT JSW ISPAT STEEL LIMITED,

NEAR GEETAPURAM, DOLVI VILLAGE, PEN TALUKA, RAIGAD DISTRICT, MAHARASHTRA

Submitted to:

Ministry of Environment and Forests New Delhi

ISPAT STEEL LIMITED

DOLVI WORKS

Submitted by:

JSW ISPAT STEEL LTD., DOLVI WORKS DOLVI VILLAGE, PEN TALUK, RAIGAD DISTRICT

MAHARASHTRA

1

APPLICATION FOR PRIOR ENVIRONMENTAL CLEARANCE (FORM-1)

(I) BASIC INFORMATION Name of the Project/s Capacity Addition of Integrated Steel Plant from

5.0 Mtpa To 10.0 Mtpa and Captive Power Plant from 300 MW To 600 MW at JSW ISPAT Steel Ltd., Dolvi Works, Dolvi Village, Raigad District, Maharashtra.

S. No. in the schedule 3 (a) Proposed capacity / area / length / tonnage to be handled / command area / lease area / number of wells to be drilled

Capacity Addition of Integrated Steel Plant from 5.0 Mtpa To 10.0 Mtpa and Captive Power Plant from 300 MW To 600 MW.

New / Expansion / Modernization

Expansion

Existing Capacity / Area etc.

Expansion of 3.0 MTPA Steel Plant to 5.0 MTPA and 300 MW Captive Power Plant under implementation.

Category of Project i.e. ‘A’ or ‘ B’

Category ‘A’

Does it attract the general condition? If yes, please specify.

No

Does it attract the specific condition? If yes, please specify.

No

Location

The proposed plant facility is located in existing plant premises at Geetapuram, Dolvi Village, Pen Taluka, Raigad District, Maharashtra State. The site falls between - Longitude - 73°00’00” - 73°05’00” E Latitude - 18°39’00” - 18°45’00” N The location of the site and study area map are given in Figure-1 & Figure-2, respectively.

Plot/Survey /Khasra No.

Land comprises Dolvi, Jui Bapuji & khar Karavi Villages.

Village

Dolvi

Tehsil

Pen

District

Raigad

State

Maharashtra

Nearest railway station /airport along with distance in kms.

Pen is the nearest railway station at about 8 km (aerial distance) on the Konkan Railway line connecting Mumbai-Mangalore along the west

2

coast of India. The nearest airport is Mumbai (national and international) located about 80 km in the north direction from the proposed project site.

Nearest Town, City, District Headquarters along with distance in kms.

Alibag 20 Km

Village Panchayat, Zilla Parishad Municipal Corporation, Local body (complete postal address with telephone nos.

Grampanchayat, Dolvi.

Name of the applicant

JSW ISPAT Steel Ltd., Dolvi Works

Registered Address

JSW ISPAT Steel Limited, Dolvi Works Jindal Mansion, 5A, Dr. G. Deshmukh Marg, Mumbai – 400 026

Address for correspondence

JSW ISPAT Steel Limited, Dolvi Works Geetapuram, Village – Dolvi, Taluka – Pen, District – Raigad. Maharashtra - 402107.

Name Shri. Murali B. Shenoy

Designation (Owner / Partner /CEO) Head-Utility & Services

Address JSW ISPAT Steel Limited, Dolvi Works Geetapuram, Village – Dolvi, Taluka – Pen, District – Raigad. Maharashtra.

Pin Code 402 107

E-mail [email protected]

Telephone No. Phone no: 02143 277501 – 15

Fax No. Fax No. : 02143 – 277542

Details of Alternative Sites examined, if any. Location of these sites should be shown on a topo sheet.

Not Applicable

Interlinked Project

No

Whether separate application of interlinked project has been submitted?

Not Applicable

If yes, date of submission

Not Applicable

If no, reason

Not Applicable

3

Whether the proposal involves approval / clearance under: if Yes, details of the same and their status to be given. (a) Name of the Court (b) Case No. (c) Order/ directions of the Court, if any and its relevance with the proposal project.

Not Applicable

(II) ACTIVITY

1. Construction, operation or decommissioning of the Project involving actions, which will cause physical changes in the locality (topography, land use, changes in water bodies, etc.)

Sr. No.

Information/Checklist Confirmation

Yes/ No

Details thereof (with approximate quantities/ rates, wherever possible) with source of information data

1.1 Permanent or temporary change in land use, land cover or topography including increase in intensity of land use (with respect to local land use plan)

No The company has already a total of about 1200 acres of land in its possession for its existing operating integrated steel plant complex of 5.0 MTPA capacity. Some of the proposed additional capacities are proposed to be setup within the existing plant and some need relocated by acquiring additional 600 acres land.

1.2 Clearance of existing land, vegetation and building?

No There will be clearance of existing land, vegetation wherever required. The proposed area is generally plain area with slight undulation.

1.3 Creation of new land uses No Some of the proposed facilities will be constructed within the existing industrial area and some require land to be acquired adjacent to the existing plant boundary.

1.4 Pre-construction investigations e.g. bore houses, soil testing?

Yes Detailed land survey, topographical surveys and soil testing / investigation studies have been carried out earlier for existing plant while the land which is to be acquired has neither been surveyed, nor topographical surveys or soil testing /investigation have been done.

1.5 Construction works? Yes 5.0 MTPA Integrated Steel Plant and 300 MW Captive Power Plant and support infrastructure such as township, raw water reservoir and railway sidings

4

Sr. No.


Yes/ No

Details thereof (with approximate quantities/ rates, wherever possible) with source of information data will be expanded / constructed. The proposed facilities are furnished at Para 1.0 of Annexure-I.

1.6 Demolition Works? No There will not be any demolition works during the construction of the plant.

1.7 Temporary sites used for construction works or housing of construction workers?

Yes Temporary construction offices will be set up during the construction stage, which will be removed later.

1.8 Above ground buildings, structures or earthworks including linear structures, cut and fill or excavations

Yes Excavation works will be carried out for constructing the civil structures of the facilities. The project requires filling, leveling and piling works.

1.9 Underground works including mining or tunnelling?

No Not applicable

1.10 Reclamation works? No Not applicable

1.11 Dredging? No Not applicable 1.12 Offshore structures? No Not applicable 1.13 Production and

manufacturing Process? Yes The description of manufacturing process

and process flow of plant is presented in Annexure-I.

1.14 Facilities for storage of goods or materials?

Yes Storage facilities are planned for raw material and finished goods.

1.15 Facilities for treatment or disposal of solid waste or liquid effluents?

Yes The wastewater generated from the indirect cooling circuit would be routed through the cooling tower and pressure filter for recycling purpose. The wastewater generated from the coke ovens will be treated in a bio-oxidation plant to reduce the level of phenolic compounds, oil & grease and cyanide. The treated wastewater will be reused in the system. The wastewater of gas cleaning plants of blast furnace and steel melt shop containing suspended solids will be clarified in the wastewater treatment plant. The clarified water will be recycled to the waste gas cleaning units. Similarly, the wastewater coming out from the continuous casting machine will be treated to remove scale and oil and the treated water will be recycled after cooling.

5

Sr. No.


Yes/ No

Details thereof (with approximate quantities/ rates, wherever possible) with source of information data The plant sanitary waste water will be treated in sewage treatment plant and the treated water will be used for dust suppression and maintenance of plant green belt.

1.16 Facilities for long term housing of operational workers?

No It is proposed to create housing complex for employees / construction workers.

1.17 New road, rail or sea traffic during construction or operation?

Yes Augmentation of port, road and rail facilities for receipt of additional raw materials and dispatch of additional products.

1.18 New road, rail, air water or other transport infrastructure including new or altered routes and stations, ports, airports etc?

Yes Augmentation of port, road and rail facilities for receipt of additional raw materials and dispatch of additional products.

1.19 Closure or diversion of existing transport routes or infrastructure leading to changes in traffic movements?

No Not envisaged

1.20 New or diverted transmission lines or pipelines?

Yes It is proposed to relocate the existing MSDS to a new location.

1.21 Impoundment, damming, culverting, realignment or other changes to the hydrology of watercourses or aquifers?

No

The plant drainage network will be planned and designed in line with the existing topography and systems.

1.22 Stream crossings? No Not envisaged 1.23 Abstraction or transfers of

water from ground or surface waters?

No The total water requirement for the 10.0 MTPA steel plant, 600 MW power plant and township will be about 116 MLD. At present JSW ISPAT Steel Ltd., Dolvi Works has been allocated about 56.0 MLD water from Amba river, Nagothane, K.T.Bandhara and consent for 30 MLD has been obtained. Application is in progress for the balance amount.

1.24 Changes in water bodies or the land surface affecting drainage or run-off

No The plant drainage net work will be designed such that there are no significant alterations in the existing drainage network.

1.25 Transport of personnel or materials for construction, operation or decommissioning?

Yes Construction materials, mechanical and electrical materials will be sourced from different parts of the state and as well as various part of country through road, rail and sea network.

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Sr. No.


Yes/ No


1.26 Long-term dismantling or decommissioning or restoration works?

No Not envisaged.

1.27 Ongoing activity during decommissioning which could have an impact on the environment?

No Not envisaged

1.28 Influx of people to an area in either temporarily or permanently?

Yes The requirement of total manpower for proposed expansion project will be about 5,000. However, the proposed Integrated steel plant will additionally generate more than 15,000 indirect secondary and tertiary employment.

1.29 Introduction of alien species? No Not envisaged

1.30 Loss of native species or genetic diversity?

No Not envisaged

1.31 Any other actions? No -

2. Use of Natural resources for construction or operation of Project

(such as land, water, materials or energy, especially any resources which are non-renewable or in short supply).

Sr. No.


Yes/No


2.1 Land specially undeveloped or agricultural land (ha)

Yes Additional 600 acres land is required for the proposed project.

2.2 Water (expected source and competing users)

Yes The total water requirement for the 10.0 MTPA steel plant, 600 MW power plant and township will be about 116 MLD. At present JSW ISPAT Steel Ltd., Dolvi Works has been allocated about 56.0 MLD water from Amba river, Nagothane, K.T.Bandhara and consent for 30 MLD has been obtained. Application is in progress for the balance amount.

2.3 Minerals (MT) Yes The additional raw material requirement for the proposed capacity expansion is given below:

Iron Ore Fines/Conc. (For Pellet Plant) 4,200,000

Iron ore fines (for sinter plant) 6,880,000

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3. Use, storage, transport, handling or production of substances or

materials, which could be harmful to human health or the environment or raise concerns about actual or perceived risks to human health

Sr. No.


Yes/ No


3.1 Use of substances or materials, which are hazardous (as per MSIHC rules) to human health or the environment (flora, fauna, and water supplies)

Yes In-built safety features of the plant and machinery would be made adequate in order to avoid hazardous events causing damage to the life and property.

Iron Ore Lumps 380,000

Coking Coal (for coke oven) 3,500,000

Non-coking coal for PCI 675,000

Limestone (for sinter plant) 491,000

Limestone (for pellet plant) 80,000

Dolomite (for sinter plant) 503,000

Quartzite 60,000

Limestone (for SMS) 860,000

Dolomite (for SMS) 388,000

Ferro-Alloy (for SMS) 103,600

Bentonite (For pellet plant) 28,000

Clinkers (For Grinding unit) 5,000,000

2.4 Construction material – stone, aggregates, and/ soil (expected source-MT)

Yes Cement – 0.85 million tonnes Coarse aggregates – 1.25 million cu.m. Fine aggregates – 0.85 million cu.m Reinforcement steel – 0.125 million

tonnes Structural Steel – 0.35 million tonnes

2.5 Forests and timber (source-MT)

No No timber use is envisaged in the proposed expansion project.

2.6 Energy including electricity and fuels (source, competing users) Unit: fuel (MT), energy (MW)

Yes The total power requirement is proposed to be supplied from the captive power plant of 600 MW capacity. Some power would also be available from the top pressure recovery turbine generators of the blast furnace & CDQ. Any additional power requirement will be met from the local grid.

2.7 Any other natural resources (use appropriate standard units)

No Not envisaged

8

Sr. No.


Yes/ No


3.2 Changes in occurrence of disease or affect disease vectors (e.g. insect or water borne diseases)

No Not envisaged

3.3 Affect the welfare of people e.g. by changing living conditions?

Yes Standard of living of the population surrounding the proposed project area is likely to be further improved.

3.4 Vulnerable groups of people who could be affected by the project e.g. hospital patients, children, the elderly etc

No Not envisaged

3.5 Any other causes

No -

4. Production of solid wastes during construction or operation or

decommissioning (MT/month)

Sr. No.


Yes/No


4.1 Spoil, overburden or mine wastes

Yes No major spoil or overburden will be generated at the project site during land development. However, the spoil or earthwork generated during construction will be reused for construction.

4.2 Municipal waste (domestic and or commercial wastes)

Yes All municipal solid waste generated from the sewage treatment plant will be used within the plant site for plantation as manure.

4.3 Hazardous wastes (as per hazardous waste management rule-s)

Yes The oil sludge from the oil storage area and oil & grease removed from the wastewater treatment plant will be sold to authorized users/recyclers approved by state pollution control board.

4.4 Other industrial process wastes

Yes Major solid waste generated from the industrial processes would include BF slag, gas cleaning plant sludge, ESP/bag filter dust, refractory debris, etc. All the solid waste described above would be recycled/used in a proper manner / sinter plant and the rejects would be dumped in a designated area.

4.5 Surplus product No Not envisaged

4.6 Sewage sludge or other sludge from effluent treatment

Yes Process sludge generated from the plant will be used as raw material in sinter plant. The sewage sludge from the STP will be

9

Sr. No.


Yes/No

Details thereof (with approximate quantities/ rates, wherever possible) with source of information data used within the plant premises as organic manure.

4.7 Construction or demolition wastes

Yes Small quantity of metallic scrap waste expected and the same will be used as melting scrap in steel making. Construction material will be used internally for filling and leveling of the sites within the plant site area.

4.8 Redundant machinery or equipment

No Not envisaged

4.9 Contaminated soils or other materials

No Not envisaged

4.10 Agricultural wastes No Not envisaged

4.11 Other solid wastes No Not envisaged

5. Release of pollutants or any hazardous, toxic or noxious

substances to air (kg/hr)

Sr. No

Information/ Checklist Confirmation

Yes/No

Details thereof (with approximate quantities/ rates, wherever possible)

with source of information data 5.1 Emissions from combustion of

fossil fuels from stationary or mobile sources

Yes The captive power plant is proposed to use Multi fuel gases having relatively low sulphur content. A stack of adequate height will be provided which may be single or two nos. depending upon the design and detailed engineering. The steam generators would be provided with low NOx burners and hence the emissions of the Oxides of Nitrogen from the steam generator would be minimum. The associated traffic with respect to the steel plant complex would generate carbon monoxide and Oxides of Nitrogen.

5.2 Emission from production processes

Yes From Pellet Plant, Sinter Plant, Coke Oven Plant, Blast Furnace, Direct Reduction Plant, Calcining Plant, Slab Caster Shop, BOF caster, LF & RH-Degasser Shop and Rolling Mills, SO2, NOx, dust, TSP, CO2, PAH, VOCs, heat and dust will be generated. The principal air pollution control system for pellet plant, sinter plant, DR Plant would be dedusting and waste gas cleaning systems separately.

10

Sr. No


Yes/No


with source of information data The coke oven gas generated in the coke ovens after by-product recovery would be utilized as supplementary fuel for proposed steel plant complex. The top gas coming from the blast furnace would be cleaned by taking the gas through BF gas cleaning device for separation of particulate before the clean gas is recovered for meeting in-plant energy demand. The stock house and cast house areas would be provided with proper DE/FE systems complete with ESPs and stacks. The LD gas generated in the SMS shop would be subjected to cleaning before it is used as plant supplementary fuel. There would be proper FE systems to capture any secondary fumes generated during hot metal and liquid steel transfer points. Dust emissions from calcining plant would be controlled by bag filters. The re-heating furnaces would generate particulates, SO2, NOx and CO. The combustion system would incorporate low NOx burner system and controlled combustion.

5.3 Emissions from materials handling including storage or transport

Yes Fugitive dust will be generated from the material handling activities.

Dust suppression or dust extraction systems with bag filters along with water sprinklers will be provided to prevent the fugitive dust emissions. Further, the development of Greenbelt would prevent the fugitive dust emissions.

5.4 Emissions from construction activities including plant and equipment

Yes Fugitive Dust.

5.5 Dust or odours from handling of materials including construction materials, sewage and waste

Yes Dust emissions from raw material handling and construction materials are envisaged. Suitable dust suppression and dust extraction methods will be followed. There is no possibility of any odour generation as there are no organic solvents / processes involved. There is a possibility of odour from sewage; however, this can be reduced by maintaining good ventilation conditions.

5.6 Emissions from incineration of waste

No Not envisaged

11

Sr. No


Yes/No


with source of information data 5.7 Emissions from burning of

waste in open air (e.g. slash materials, construction debris)

No Not envisaged

5.8 Emissions from any other sources

No Not envisaged

6. Generation of Noise and vibration, and emissions of Light and heat

Sr. No.


Yes/No


6.1 From operation of equipment e.g. engines, ventilation plant, crushers

Yes Noise will be generated from Sinter plant, Blast furnace, Rolling mills, continuous caster and Oxygen plant which will not be allowed to exceed 85 dB (A).

6.2 From industrial or similar processes

Yes Blast furnace, pellet plant, sinter plant, DR Plant, Rolling mills, continuous casting machines and Oxygen plant are likely to generate noise The expected noise level will not be allowed to exceed 85 dBA or proper noise protection systems will be used whenever required. There will be no adverse effect on the ambient Noise. Waste heat recovery unit is proposed for the proposed Sinter Plant and CDQ & Waste heat boiler is proposed for the Coke Oven Plant, so that no heat shall be wasted.

6.3 From construction or demolition

Yes Yes. This will be in the range of about 65-80 dB(A). Regular maintenance of the equipment will help in reducing these noise levels.

6.4 From blasting or piling Yes Some noise <85 dB (A) will be generated. 6.5 From construction or

operational traffic Yes The noise levels are expected to be in the

range of about 70-75 dB(A). 6.6 From lighting or cooling

systems

No Not envisaged

6.7 From any other sources No Not envisaged

12

7. Risks of contamination of land or water from releases of pollutants into the ground or into sewers, surface waters, groundwater, coastal wasters or the sea

Sr. No.


Yes/No


with source of information data

7.1 From handling, storage, use or spillage of hazardous materials

No Not envisaged.

7.2 From discharge of sewage or other effluents to water or the land (expected mode and place of discharge)

No The sewage water will be treated and used for greenbelt development within the premises. Out side discharge is not envisaged. The wastewater from the plant units will be treated at the individual source of generation and re-used or re-cycled into the processes. There will not be any external discharge of wastewater.

7.3 By deposition of pollutants emitted to air into the land or into water

No There is no discharge of wastewater outside the plant.

7.4 From any other sources No Not envisaged

7.5 Is there a risk of long term build up of pollutants in the environment from these sources?

No Not envisaged

8. Risk of accidents during construction or operation of the project,

which could affect human health or the environment

Sr. No.


Yes/ No


8.1 From explosions, spillages, fires etc and from storage, handling, use or production of hazardous substances

Yes There is a possibility of oil spillages and fires from the storages. However, suitable risk assessment will be carried out and disaster management plan will be in place.

8.2 From any other causes No Not envisaged

8.3 Could the project be affected by natural disasters causing environmental damage (e.g. floods, earthquakes, slides, could burst etc)

No The area is generally flat land. There is no record of occurrence of floods, land slides, cloud bursts etc. The proposed project site falls in Zone-IV as per IS-1893 (Part-I):2002.

13

9. Factors which should be considered (such as consequential development) which could lead to environmental effects or the potential for cumulative impacts with other existing or planned activities in the locality

Sr. No.


Yes/ No


with source of information data 9.1 Lead to development of

supporting, facilities, ancillary development or development stimulated by the project which could have impact on the environment

Yes

Existing and ancillary facilities will improve.

Supporting infrastructure (roads, power supply, waste or waste water treatment, etc)

Yes Existing infrastructure facilities will be expanded / extended to take care of the project.

Housing development Yes

New facilities about 10 km North of plant, away from pre-dominant wind direction.

Extractive industries No

The proposed facilities are captive to JSW ISPAT Steel Ltd., Dolvi Works.

Supply industries Yes Existing supply chain will improve

Other --- 9.2 Lead to after use of the site,

which could have an impact on the environment

Yes The proposed project will have impact on environment. However, these impacts will be contained by adopting suitable mitigation measures.

9.3 Set a precedent for later developments

Yes Ancillary industries will be developed as a consequence.

9.4 Have cumulative effects due to proximity to other existing or planned projects with similar effects

Yes The industry is not located in a critical zone. There are not many major industries operating in this region. Hence, no major effects are envisaged.

(III) Environmental Sensitivity

Sr. No.

Areas Name /

Identity

Aerial distance (within 15 km) Proposed project location boundary

1 Areas protected under international conventions, national or local legislation for their ecological, landscape, cultural or other related value

No There are no ecological, landscapes, cultural or other related sensitive areas in 15 –km radius.

14

Sr. No.

Areas Name /

Identity


2 Areas which are important or sensitive of ecological reasons – wetlands, water courses or other water bodies, coastal zone, biospheres, mountains, forests

Yes There are no national parks, sanctuaries in 15-km radius from proposed project site. Two rivers are within 15km radius from proposed project site. 1. Amba river 0.8 – km, W 2. Bhogeswar river 7.8-km, N

3 Areas used by protected,

important or sensitive species of flora or fauna for breeding, nesting, foraging, resting, over wintering, migration

Yes Four reserve forests exist in 15 Km radius area as listed below: • RF near Kharkhara village (1- km, E) • RF near Katkariwadi village (5.3-

km, NE) • RF near Turmal village (4.6-km, E) • RF near Katvira village(5.1- km, SW) • RF near Dhavte village(8.5-km NE) Detailed floral and fauna studies will be conducted and details will be incorporated in EIA report.

4 Inland, coastal, marine or underground waters

Yes Amba river 0.8 – km, W Bhogeswar river 7.8-km, N

5 State, national boundaries No Nil

6 Routes or facilities used by the public for access to recreation or other tourist, pilgrim areas

No Not applicable

7 Defence installations No Nil within 10-km radius

8 Densely populated or built-up area

Yes Pen Taluka is 6.9-km from the plant site.

9 Areas occupied by sensitive man made land uses (hospitals, schools, places of worship, community facilities)

Yes Pen Taluka has all the facilities such as primary schools, middle schools, high schools, hospitals health centers, public health sub centers, dispensaries and places of worship.

10 Areas containing important, high quality or scarce resources (ground water resource, surface resources, forestry, agriculture, fisheries, tourism, minerals)

No No scarce resources are present in 15-km radius

11 Areas already subjected to pollution or environmental damage. (those where existing legal environmental standards are exceeded)

No This is not a listed or critically polluted area.

15

Sr. No.

Areas Name /

Identity


12 Areas susceptible to natural

hazard which could cause the project to present environmental problems (earthquakes, subsidence, landslides, erosion, flooding or extreme or adverse climatic conditions)

No The proposed project site falls in zone-IV as per IS-1893 (Part-I): 2002. No land slides / flooding is envisaged in project area.

(IV) Proposed Terms of Reference for EIA Studies – Annexure – II.

I hereby given undertaking that the data and information given in the application and enclosure are true to the best of my knowledge and belief and I am aware that if any part of the data and information submitted is found to be false or misleading at any stage, the project will be rejected and Clearance give, if any to be the project will be revoked at our risk and cost.

Date: 03rd December 2012 Place: Dolvi Murali B. Shenoy Head – Utility & Services JSW ISPAT Steel Limited Geetapuram, Village – Dolvi, Taluka – Pen, District – Raigad Maharashtra 402107.

16

FIGURE -1 LOCATION MAP

Plant Site

17

FIGURE -2 STUDY AREA MAP

Bhalpada

Mothe vadhav

Vashi

Vadhav

Dolvi

Medhekhar

Pitkari

RatalpadaKusambale

Kachali

ShirgaonKatkorwadi

Vadvali

Vagholi

Ambeghar

KurkundiChari

Sutarpada

Ghasvadkhar

Talanikar

Kamalpada

Shahabaj

ValvadeDadaji

Kalve

Sonkhar

Kalesri

KanebachapadaTukaramwadi

Kaproli

KaneBorze

Tambatshet

Sapoli

Poinad

Tadvagle

Kathodipada

Kharoshi Kolghar

Thakurwadi

Talashet

Shahapur

Ruishet Bhomoli

Chaura

Ruishet Bidwagale

Ananwadi

Dattawadipada

KurdusNavakar

Bidbav

Vadkhal

Kandepada

RodeKashmire

Kandale

Borgaon

MalegharVashinaka

Umbarde

Dhondapada

Patnoli

Kharkaravi

RESERVED FOREST

Gadab

DhombiTakachiwadi

Mounepale

Kherpale

RESERVED FOREST

Pimpalpada

Ramwadi

Vadgaon

KhapachiwadiTadmalwadi

Jirne

RESERVED FOREST

Indranagar

Navegaon

Katkariwadi

Ambeghar

BenavleNarvel

Div

BoriShinganvat

Kolve

Masad BudrukShirkiBorve

Turmal

Patharmal

RESERVED FOREST

Chaphegani

Bangalwadi

BakegharShekatmal

Ramraj

Antora

TarankhopAntoraNavgharwadi

Shinole

Hamrapur

Varedi

Masad Khurd

ViraniRESERVED FOREST

Dhavte

R F

Chinchghar

Masad Khurd

Kharjul

RESERVED FOREST

Dhakta Shahapur

KOPAR

Dharamtar

Wave

Uchede

Pipalpada

Johe

LebhiKhidki

Sutwadi

Aveti

Sambri

Pandapur

KasuBurdi

KaranjatepBrahmanwadi

Khadakwadi

Kalad

Pedkyawadi

KatvaripadaVaghvira

Hemnagar

Sukatrie

Navenagar

DivlangPezari

Nagjhari

Ambepur BhakhwadiDehankoni

Chikhali

Katvira

Khar Sapoli

DevaliAnandnagar

Dherankhar

BandhanwadiPLANT

18°45'

73° 0'

18°40'

Bhanghar

PEN

Amba R.

Bhogeshwar R.

27.8km

Mahabalewsaram133.7km

Khalapur

98kmMumbai

73° 5'

73° 0' 73° 5'

18°45'

18°40'

LEGEND

Road

Railway Line

Settlements

Nadi/Nala/Water Body

Forest Boundary

N

Plant Site

18

ANNEXURE-I

INTEGRATED STEEL PLANT PROCESS DESCRIPTION

1.0 Introduction

The project envisages capacity addition of Integrated Steel Plant from 5.0 MTPA to 10.0 MTPA and Captive Power Plant from 300 MW to 600 MW at Dolvi. The plant will be equipped with coke oven complex, pellet plant, sinter plant, blast furnace, Direct Reduction Plant, BOF converter, ladle furnace, RH-Degasser, continuous casting facility, hot rolling mill, cold rolling mill, lime & dolo calcinations plant, oxygen plant, grinding unit & township for the production of value added products. Supporting facilities up to production of finished products will also be set up in the plant based on the state-of-the-art technology. All technological facilities required at each processing step to achieve good quantity rolled products are given below:

S. No.

Facilities Unit Total capacity at 5 MTPA (EC Received)

Additional units from 5 MTPA to 10 MTPA

Total capacity at 10 MTPA

1 DRI (Gas based Mega Module)

MTPA 2.0 (by augmenting)

2.0 4.0

2 Pellet Plant MTPA 4.0 4.0 8.0 3 Coke oven with By- Product

Plant & CDQ MTPA 2.0 2.5 4.5

4 Sinter Plant MTPA 2.8 + 3.2 8.0 14.0 5 Blast Furnace with Pig

/Granshot Casting & TRT MTPA 2.0 + 1.6 4.5 8.1

6 SMS (CONARC) MTPA 5.2 (By Augmenting the existing facilities)

- 5.2

7 SMS – BOF MTPA - 6.0 6.0 8 Ladle Furnace 2x200 T + 1x205 T 2 X 280/300 T 2x200 T + 1x205 T

+ 2x280/300 T 9 VD/VOD/RH-Degasser 1x200 T + 1x205 T 2 X 280/300 T 1x200 T + 1x205T

+ 2x280/300 T 10 CSP (HRC Coil) Thin Caster-

cum- Hot Strip Finishing Train


- 3.5

11 Conventional Slab Caster MTPA 2 x 1 strand 2 x 2 strand Total 6 strands 12 Plate Mill MTPA 1.5 - 1.5 13 Galvanizing Line (Cold Rolled

Steel Strips, Hot Dip Zinc Coated Full Hard)

MTPA 0.6 - 0.6

14 Electrical Steel CRGO Line MTPA 0.4 - 0.4 15 Tin Plate Line MTPA 0.4 - 0.4 16 Color Coating Plant MTPA 0.5 - 0.5 17 Lime & Dolo Plant TPD 1800 1800 3600

19

18 Oxygen Plant TPD 4100 3500 7600 19 Captive Power Plant (Gas

Based) MW 300 300 600

20 Hot Rolling Mill with Shearing & Slitting line

MTPA - 6.0 6.0

21 Slag & Clinker Grinding Unit MTPA - 10.0 10.0 22 CRM (Hot Rolled Skin Pass +

Cold Rolled Full Hard Coil + Hot Rolled Pickled & Oiled Coil)

MTPA 1.0 1.5 2.5

23 Township - - √ √

Facilities required outside the plant boundary like sourcing of iron ore, coking and non-coking coal will also be taken up along with township etc.

2.0 Coke Oven Batteries Coke is one of the prime requirements for production of hot metal through blast furnace route. The coke supplies heat to the blast furnace for smelting purpose and also acts as reducing agent inside the furnace for reduction of iron oxides to metallic iron. Both active hot carbon of coke as well as reducing gas, generated in the furnace, by burning of coke, take part in reduction reaction. A number of technologies have been developed for reduction of coke requirement in blast furnaces resulting in cost effectiveness viz injection of auxiliary fuels like non-coking coal/tar/natural gas through tuyeres, etc. Considering the level of technological development in the coke making area and total requirement of blast furnace coke in the blast furnace, installation of recovery type coke oven batteries have been envisaged. The gross coke generated in the coke ovens will be screened. BF coke and nut coke will be sent to the blast furnace and coke fines/ coke breeze generated in the plant will be utilized in the sinter plant. The coke making technology would include pre-carbonization and post carbonization technologies like selective crushing of coal, stamp charging and high capacity ovens. 4 x 65 nos. batteries of 5.5 m tall Coke Oven having capacity of 2.5 MTPA has been envisaged for the capacity addition from 5.0 to 10.0 Mtpa.

3.0 Sinter Plant The sinter plant will be equipped with the following major facilities:

Base blending for input materials Flux and fuel crushing facilities Lime dozing facility Mixing and nodulising unit Sintering machine equipped with sinter strand, ignition furnace, wind

boxes, suction fan, dust cleaning unit, etc. Sinter coolers Sinter screening and transportation facilities

Capacity of the sinter plant has been estimated based on use of about 80-85% sinter in the burden of blast furnaces, which shall be obtained from the twin (2) modules of sintering machine of 4.0 MTPA capacity each.

20

4.0 Pellet Plant

The Pelletization process involves reduction of moisture in the iron ore to less than 1%, grinding to 45 micron size, feed preparation by adding binders and moisture, green pelletization and induration (heat hardening). It is proposed to install a Pellet Plant capable of producing upto 4.0 Mtpa of pellets. This Pellet Plant will produce DRI grade pellets to be used in the sponge iron plant and balance pellets will be used in the BF.

5.0 Blast Furnace Hot metal production using blast furnace process has been envisaged for the proposed project, as the process is most established and competitive iron making technology till date. A number of technological improvements have taken place in blast furnace which have resulted in higher production, less coke consumption, most energy efficient, long campaign life, etc. State-of-the-art blast furnace equipped with the following major facilities has been envisaged for the proposed plant:

Covered stock house with automatic conveyor charging facilities Bell less top charging equipment High top pressure operation (2.5 kg/cm2 top pressure) and matching gas-

cleaning plant. Stoves for generation of high hot blast temperature (1250°C blast

temperature). Coal dust injection facilities (150 kg/thm) Oxygen enrichment of blast. Cast house slag granulation plant. (The slag would be grinded in slag

grinding unit) Top gas recovery Turbine Level- III automation and control system, etc.

Hot metal produced from the blast furnace will be transported to the steel melting shop using torpedo ladles/open top ladles. Considering the daily requirement of hot metal in the steel melting shop for production of liquid steel, which is sufficient to produce about 4.5 Mtpa hot metal, 1 (one) blast furnace of 4.5 Mtpa capacity have been envisaged for the proposed project. Slag generated from the blast furnaces will be granulated in the cast house slag granulation plant. The granulated slag will be processed in the grinding units.

6.0 Pig Casting Machine The mismatched / off grade hot metal is proposed to be handled in a pig casting machine or a energy efficient hot metal noduliser unit. The PCM will consist of the following units / facilities. - PCM proper - Lime preparation unit - Settling tank and pump house - Pouring end and discharge end sprocket - Centralised grease lubrication system - PCM control room and sub-station. - Pig storage yard with magnet crane. These will be of adequate capacity for production of pig iron/nodulised iron.

21

7.0 Direct Reduction Plant

One Mega Module Direct Reduction (DR) Plant based on the natural gas/coke oven gas/LD gas/Mixed gas with average gross production capacity of 2.0 Mt/yr has been envisaged.

8.0 Steel making and Secondary Refining

8.1 Hot Metal Desulphurisation Two (2) twin hot metal desulphurisation stations of 280/300 t ladle capacity have been envisaged to bring down the sulphur content in hot metal received from blast furnaces. Desulphurisation of hot metal will be carried out in the hot metal charging ladles of steelmelting shop prior to charging into BOFs. Hot metal from blast furnace to steelmelting shop will be received by torpedo ladles/open ladles. Hot metal will be pretreated in desulphurisation stations before being used for steelmaking. The desulphurisation facilities will be based on lance injection process. Desulphurisation facilities are planned in hot metal receipt-cum-charging bay. Calcium carbide and magnesium based reagents will be used for desulphurisation of hot metal. Nitrogen will be used as the carrier gas during injection.

8.2 Steel Making Basic oxygen furnace technology for production of liquid steel has been envisaged for the proposed project. This process till date dominates the steel production scenario of high capacity integrated steel plant worldwide mainly due to its energy efficiency. As such, external energy in terms of either electrical power or solid/liquid/gaseous fuel is not required for process. However, requirement of electricity and gaseous fuel are mainly for driving of electrical equipment, ladle heating, etc. Most of the other steel making process like electric arc furnace/Induction furnace process consumes high amount of electrical energy. However, oxygen with high purity is required for conversion of hot metal to liquid steel and scrap/iron ore/DRI is required as coolant in BOF process. A significant amount of medium calorific value (2000 kCal/Nm3) gas is generated during carbon refining reaction period of steel making which will be separated in the gas cleaning plant using suppressed combustion system. Hot metal will be pre-treated before charging into the converter. For capacity addition from 5.0 to 10.0 Mtpa capacity, a new converter shop has been envisaged which has been designed to handle about 6.0 Mtpa hot metal, 4.5 Mtpa hot metal from proposed new Blast Furnace-2 and 1.5 Mtpa hot metal from existing Blast Furnace-1. Considering the requirement of liquid steel for subsequent process requirements, chemical composition of input materials, quality of liquid steel to be produced, sequence of casting of liquid steel into slabs, oxygen blowing rate etc., two (2) number of converters of capacity 280/300 t each have been envisaged for the proposed project.

8.3 Ladle Furnace (LF) With a view to achieve improved homogeneity and productivity of the primary unit and serving as a buffer between the Converter and the caster, ladle

22

furnace is the ideal secondary refining unit. The correction and homogenization of steel composition and temperature, desulphurisation and recarburisation, etc. can be efficiently carried out in a LF. Two (2) nos. LF of adequate size has been envisaged for the proposed project. The LF will also be equipped with argon purging facilities.

8.4 RH-Degasser In order to produce value-added products subject to market requirements, RH are essential as secondary refining units. The processes assure liquid steel of high purity, low level of inclusions and good homogeneity with respect to temperature and chemistry. These processes help attainment of very low levels of gases and inclusions and provide controlled alloying and mixing to produce a great variety of alloys. These processes also allow improvement in plant productivity (through sharing of refining load) and yield, in addition to ensuring good quality. Two (2) RH-Degasser units of matching size 280/300 t have been envisaged for production of value-added steels. The RH-TOP unit will be used for production of various steel grades and for special applications.

9.0 Slab Caster

To produce hot rolled plates, slab casters have been proposed. The technology of continuous casting of steel into slabs has been fully mastered today for any grade of steel. This technology has become well established through extensive mechanisation and control of various operating parameters. The continuous casting process has gained worldwide acceptance, mainly because of high yield, good product quality and good economics of operation. In order to cast 6.0 MTPA liquid steel into Flat products, slab casters have been envisaged for the proposed project. Considering market requirements, two double strand casters capable of producing slabs of 950-2150 mm width and 220/250 mm thickness have been envisaged. However this could be revised to cater to the future market requirements.

10.0 Finishing Mill 10.1 Hot Rolling Mill

The continuous cast slabs from the slab caster are fed to a reheating furnace. The first part of the furnace serves as a heating zone while the second part as holding zone for the continuous cast slabs. The slabs are heated to achieve homogenous temperature over their enter length. The slabs are then passed through a descaler where high-pressure water is sprayed simultaneously on top and bottom surfaces to remove the scale. The cleaned slab is then rolled in the rolling mill comprising of roughing mill and continuous finishing mill train to the desired thickness. The rolled strip is then cooled to the desired coiling temperature by the laminar cooling water spray system on the runout roller table. The hot rolled strip is then coiled on the downcoiler. The hot rolled coil is transported by a coil conveyor system to the coil storage yard. The hot rolled coils are delivered by the coil conveyor system to the coil

23

yards where they are stored for further despatch. Based on the product-mix, one hot rolling mill of 6.0 Mtpa capacity has been proposed for the project.

10.2 Cold Rolling Mill

Hot strips produced in the Hot rolling mill will be processed in the Cold rolling Mill. EC had been obtained at 5 Mtpa stage for CRM of 1.0 Mtpa capacity. It is now proposed to apply for amending the capacity to 2.5 Mtpa. This large size would be more energy efficient.

11.0 Captive Power Plant

To meet the requirement of power for the proposed plant, a captive power plant of capacity 1 x 300 MW has been envisaged based on the excess fuel gases.

12.0 Lime & Dolo Plant

The limestone and raw dolomite from storage bunkers will be fed to the screen by belt conveyor and undersize lime stone and dolomite will be screened out and stored in another bunker which is meant to store the undersize material. The undersize limestone and raw dolomite will be stored for onward disposal to other consuming units. Screened materials of Oversize will be fed to shaft kilns. Limestone and raw dolomite will be calcined at temperature of 950-1150°C. The lime and calcined dolomite from the kilns will be discharged to two different conveyors which are placed below the kilns. The lime and calcined dolomite will then be fed to single deck screen to separate out undersize material. The undersize lime and dolomite material will be stored in two separate bunkers. The sized lime and calcined dolomite of Oversize will be stored in bunkers. Lime and calcined dolomite of Oversize will be conveyed to SMS through belt conveyor and undersize lime will be transported through trucks/cement tanker to other consuming units. 3 Nos. x 600 TPD capacity Lime and Dolo Calcination Plant have been envisaged for the proposed.

13.0 Oxygen Plant

Oxygen, nitrogen and argon will be produced by air separation process based on low pressure cryogenic cycle and double column rectification system. The unit will be able to produce gaseous as well as liquid products. Gaseous products from the oxygen plant will be distributed through pipeline network system consisting of pressure regulating and metering station to various consumers. Oxygen will be required for oxygen enrichment in the blast furnace, secondary refining in VD, cutting of slabs in continuous casting plant, and for general purpose use in various units of the steel plant. Nitrogen will be mainly required as carrier gas in coal dust injection system, bell less top equipment for blast furnace, purging in GCP of BF and also for occasional purging of fuel gas pipelines and equipment.

24

Argon will be required for shrouding in the tundish, mould in the continuous casting plant and stirring in ladle. Argon will also be required for laboratory purpose. Oxygen Plant of capacity 3500 tpd has been envisaged for the proposed project. Flow sheet of the production process is shown in Figure-3.

14.0 Township

The township is to serve a large steel plant of 10 Mtpa capacity and CPP of 600 MW capacity and may have up to 7065 dwellings of various categories in about 150 Acres of land. The new township shall be constructed to take care of the accommodation facilities of the employees. Area for the township has been identified near Pen but the specific details are yet to be finalized.

Township details are given below:

DOLVI TOWNSHIP AREA CALCULATION

Type BHK Nos.

Area (sq. Ft)/

house

Total Area

(sq. Ft) No. of

storeys

No. of houses

per floor

Total houses

per bldg

No. of blds.

Required Area Req (sq. ft)

1 5 15 4000 60000 1 1 1 15 60000 2 4 50 2500 125000 1 1 1 50 125000 3 3 500 1700 850000 3 2 6 83 283333 4 2 1500 1200 1800000 7 4 28 54 257143 5 1 3000 600 1800000 7 4 28 107 257143 6 1 2000 350 700000 7 4 28 71 100000

Total 7065 5335000 1082619

7 Area of roads/parking area in between houses, etc - 3 times more area than blgs. Area 3247857

Total 4330476

8 Area for GH / schools / gardens / play grounds/ water pond / temple / parkings / shopping centres/hospital etc 2178930

Total 6509406 sq. ft

604743 sq. m

TOTAL 149 acres say 150 acres

Raw water shall be treated in the plant and pumped to the township for their water requirement. Sanitary faecal sewage will be collected from the ablution blocks through pipeline and the same will be connected to a sewage treatment plant. The effluent from sewage treatment plant will be utilized for the development and maintenance of greenery. Details of the Sewage Treatment Plant are given below:

Sewage treatment Plant provide only preliminary and primary treatment, and tertiary treatment is rare.

25

1. Preliminary treatment: This is the mechanical removal of coarse and fine solid material. The sewage passes through screens, which trap pieces of wood, rags, wire, etc.

2. Primary treatment: The sewage then flows slowly through grit tanks,

where particles of sand or grit settle out. Fine particles still remain suspended in the sewage, so it is passed to large primary sedimentation tanks where most of the remaining particles settle out to form a sludge. Primary treatment removes about 60–70% of suspended solids. The liquid leaving the primary sedimentation tanks still contains very fine solids and dissolved matter, so secondary treatment is usually required.

3. Secondary treatment: This is a biological process, involving the

oxidation of dissolved organic material by micro-organisms to decompose the organic compounds, a process similar to that taking place in rivers, the soil, or filter beds in water treatment works. The process is speeded up by increasing the amount of oxygen available, which can be done by two possible methods: • Filter beds:, • Activated sludge:.

Secondary treatment in addition to primary treatment removes about 70–90% of the BOD in the sewage, so the effluent is usually sufficiently purified.

4. Tertiary treatment: Primary and secondary treatment remove only 20–40% of the phosphorus and nitrogen, and about half of the toxic compounds. If it is necessary to reduce plant nutrients or toxic compounds beyond these levels tertiary treatment is required, but this is very expensive and not commonly used. Various types of tertiary treatment exists, e.g. nutrient stripping, disinfection by UV light or filter membranes.

26

FIGURE -3

PROCESS-CUM-MATERIAL FLOW SHEET

27

ANNEXURE-II

PROPOSED TERMS OF REFERENCE

Project Implementation: A detailed description of all the additional elements of the project from 5.0 to 10.0 Mtpa stage during the pre-construction, construction and operational phases will be prepared. The elements analyzed will include the infrastructures of the project including: drainage features, roads, waste collection, disposal and management and utility requirements.

Analysis and assessment of designs to ensure environmental soundness, sustainability and regulatory compliance of the designs will be studied and incorporated in the draft and final EIA Report.

Field Assessments:

Field assessments of the physical, ecological, and socioeconomic aspects of the site and associated environs will be conducted during winter season. These assessments will be used to determine the potential impacts, if any, of the proposed project. A photographic survey of the proposed site and the nearby environs has been conducted. The survey included a photo-inventory of the physical and biological features of the site and environs, and the areas are viewed with respect to the suitability of the proposed facility. The assessments included:

Physical:

Meteorology, air quality, geology, topography, soils, groundwater/surface water hydrology quality, hazard vulnerability, noise levels, land use, water use and solid waste management.

Ecological:

Terrestrial and aquatic communities; presence of rare, threatened and endangered species.

Socioeconomic:

Demography, regional setting, location assessment, and land uses.

The technical scope of work for carrying out the baseline monitoring would be as given below. The baseline monitoring will be carried out in 10-km radius study area around the proposed project site for three months representing the winter season.

Sr. No.

Attributes Scope of Work

1 Ambient Air Quality 4 Locations - 2 days/week for 13 weeks (3 months) PM-2.5, SPM, RPM, SO2, NOx, and CO will be monitored as per CPCB guidelines. Design of ambient air quality sampling network with regard to topography, population, sensitive locations, emission sources, background

28

Sr. No.


concentrations and possible impact zones, through application of screening air quality models for assessing the maximum GLC zones prior to start of baseline study.

2 Meteorological data 1 Location - 90 days Wind speed, direction, temperature, humidity, cloud cover and rainfall will be monitored. This is further supported by the meteorological data for the area of interest from the nearest meteorological observatory and Trend analysis of micrometeorological data generated at the site.

3 Water Quality 9 Locations- (Surface and Ground water samples) – Once during the EIA study Parameters as per IS-10500, IS:2296 and EPA Act as applicable . The survey also include estimation of water balance and assessment of impacts on regional water demand and availability of fresh water due to drawl of water for plant, recommendations on water conservation and rain water harvesting measures based on past experience on similar projects; and identification of suitable location and methodology for disposal of waste water form all sources.

4 Soil Quality 6 Locations once during EIA study. Parameters related to afforestation, nutrients, pollutants etc. will be carried out.

5 Noise Levels 8 Locations (Residential, Commercial and Sensitive areas) once during EIA study. Readings will be taken for 24-hr duration at each location

6 Land use Land use as per the district census handbooks as well as with the help of satellite imagery will be presented in 10-km radius study area.

7 Solid waste Characterization of all the solid wastes generated from the plant operations and its disposal including impacts due to disposal.

8 Socio-Economic and Demography

Socio-economic and health aspects are covered for 10-km radius study area based on the Census documents and NIC database.

9 Ecological studies (Terrestrial and Aquatic)

Flora and fauna will be studied in 10-km radius study area. These studies will be based on primary as well as secondary sources. The survey also includes assessment of the species diversity, density, abundance etc. in the study area and formulation of ecological indexes, assessment of likely changes on flora and fauna due to the project related activities, suggestions

29

Sr. No.


for conservation and protection of flora and fauna in the study area and suggestions for development of new conservation areas locally.

10 Traffic Study Traffic at important points on the approach roads will be surveyed for the existing total daily traffic, peak hour traffic and traffic composition. Assessment of the change in traffic composition and volumes and suggestions for improvement of traffic flow around the project site and around will be studied

11 Aesthetic/Cultural Aspects

Identification of all historical/ archeological sites/monuments in the study area.

Detailed qualitative assessments of the physical, ecological, and socioeconomic conditions associated with the site in the Draft and Final Report.

Legislation and Regulatory Considerations

Government policies, legislation and regulations relevant to the proposal will be identified. Local plans and policies will also be evaluated. Project characteristics will be analyzed to ensure compliance with these policies, legislation and regulations. Appropriate recommendations will be provided to ensure regulatory compliance.

The legislation relevant to the project will be summarized and presented in the EIA Reports.

Environmental Impact Assessment The guidelines suggested and international practices will be reviewed to

determine the adverse impacts and critical areas. There are various qualitative as well as quantitative methods of conducting

EIA studies, each having its own merits and demerits. We intend to use the best logical tool to assess the impact of the project.

The baseline data generated from above studies will be analyzed and

compared with applicable standards for each environmental attribute, so that the critical environmental areas and also attributes of concern will be identified. The short term and long-term impacts particularly on sensitive targets such as endangered species, plants and historically important monuments will be identified.

The Environmental Impact Assessment of proposed project will be done on

above basis to determine the environmental acceptability of this proposed project in absence of control measures and after implementation of the mitigation measures, including worst impact.

A qualitative and quantitative assessment of pollution aspects of proposed

project (air and dust, wastewater, noise pollution, wastewater discharges etc.) will also be done to identify the adequacy of the proposed control measures as well as the likely impact on existing critical areas. Mitigation measures to reduce adverse impacts will be suggested.

30

Air Impacts:

Emission Inventory will be carried out in an area of 10-km around the project site. A computer based internationally recognized mathematical air quality model (ISC-ST3) will be used to predict the concentration of SO2, NOx and SPM due to the operation of the proposed project. The model would also take into account other sources of pollution and topographical features of the area. The emission of relevant pollutant (SO2, NOx and SPM) from nearby sources shall be used in the model for more accurate estimate of air quality. The results will be presented for short term (24 hourly) concentrations over a radius of 10-km around the plant site. The dispersion model results will be included in the report using isopleths or other graphical methods, over laying a land use map of the surrounding area. The predicted air quality will be compared with existing regulations and mitigative measures, if any, will be identified. The long term and short term impact at all the monitoring locations shall also be estimated.

Noise Impacts:

Sources of noise and its impact on the environment would be clearly brought out. The noise level at varying distances for multi-sources will be predicted using suitable model. A comparison of measured noise (Leq) at monitoring locations to that of predicted noise levels (Leq) would be made and mitigatory measures required, if any, will be recommended to conform to regulatory ambient air noise standards.

We propose to estimate increase in noise levels over the baseline conditions

in different zones like industrial, residential and sensitive areas like hospitals, wild life habitation etc. The potential noise level exposure will be determined and evaluated for acceptable limits of exposure.

Environment Management Plan

For each potential negative impact identified, recommendations will be presented for avoidance, minimization or mitigation of impacts along with costs associated with potential mitigation.

An EIA/EMP, based on three months baseline study, will be prepared for the

project. The EMP will address the following:

• Identify and summarize all anticipated significant adverse environmental impacts;

• Identify and summarize all mitigation measures, including the type of impact to which it relates and the conditions under which it is required;

• Define a set of policies and objectives for environmental performance and continual enhancement of performance;

• Recommend monitoring measures including the parameters to monitored, methods to be used, sampling locations, frequency of measurements, detection limits and definition of thresholds that will signal the need for corrective actions;

• Recommend monitoring and reporting procedures; • Recommend capacity development and training requirements for

implementation of EMP;

31

• Recommend organizational structure for effective implementation of the EMP; and

• Draw up an implementation and cost schedule for EMP.

Environmental Monitoring

An environmental monitoring and management plan will be developed for the sensitive elements of the environment that may require monitoring during construction and operations of the facility. Recommendations will be made on the institutional arrangements that will be necessary to ensure effective monitoring and management.

A detailed management and monitoring program will be developed to reduce the effects of potential negative environmental impacts.

Risk Assessment and Disaster Management Plan

Risk Assessment studies comprising sub-activities such as hazard identification, assessment and quantification of risk for suggesting risk mitigation measures based on Maximum Credible Accident (MCA) Analysis to be carried out for the proposed project. Preparation of the Risk Assessment Report will be followed by Disaster Management Plan (DMP) and Emergency Preparedness Plan (EPP) based on the quantitative Risk Assessment of the proposed activity and associated infrastructure for the project.

Occupational Health and Safety

We will review the existing system of safety management and occupational health surveillance system in the plant and recommend for further appropriate measures in view of the proposed expansion facilities.

LF & VDLCP-3

A M

B A

R

I V

E R

MAIN GATE

FIN

FA

N C

OO

LER

S

FIN FANCOOLERS

H. R. JHONSON PLANT AREA

TW TW TW

GOA GATE

BOU

NDARY WALL

BO

UN

DA

RY

B L

A S

T

F U

R N

A C

E

S P

O N

G E

I R

O N

P

L A

N T

R M H S A R E A

H O

T

S T

R I

P

M I

L L

SINTER PLANT - 1

HELIPAD AREA PRO

POSE

D RA

ILW

AY S

IDIN

G

POWER PLANT1x53.5 MW

B T3

SINTERPLANT-3

LIMEPLANT

OXYGENPLANT

HOTSTRIPMILL

SMS

BASEMIX

FLUX

IRON

ORE

COKING

COAL

CEMENTPLANT

POWERPLANT HARSCO

COKE OVEN PLANT-3

SINTER

PLANT-2

COLDROLLING

MILLS

MSDS

DRPLANT-2

BLASTFURNACE

PELLETPLANT-2

PLATEMILL

ISPAT STEEL LTD.

Capacity Addition of Integrated Steel Plant from 5.0 MTPA to 10.0 MTPA and

Captive Power Plant from 300 MW to 600 MW

Dolvi, Maharashtra

Project Report

Techno Projects Management Ltd. Mumbai

December 2012

JSW ISPAT Steel Limited

Maharashtra Capacity Addition of ISP from 5.0 MTPA to 10.0 MTPA and CPP from 300 MW to 600 MW

Project Report

CONTENTS

Chapter No. Title Page Nos.

From To

01 Introduction 1-1 1-4

02 Market Analysis & Product Mix 2-1 2-6

03 Major Technological Facilities 3-1 3-10

04 Raw Materials Requirements 4-1 4-4

05 Proposed Site 5-1 5-6

06 Services, Utilities & Manpower Requirement 6-1 6-4

07 Environmental Management 7-1 7-4

08 Project Implementation 8-1 8-1

09 Block Capital Cost 9-1 9-1

LIST OF DRAWINGS

Sl. No. Description Drawing No.

1. Location Map JSW/DW/PR/001

2. Regional Map JSW/DW/PR/002

3. Road Linkage JSW/DW/PR/003

4. Process-cum-Material Flow Sheet JSW/DW/PR/004

5. General Layout JSW/DW/PR/005

6. Implementation Schedule JSW/DW/PR/006



Project Report

1-1

01 INTRODUCTION

01.01 Preamble

Steel being a basic commodity for all industrial activities, quantum

of its consumption is considered as an index of industrial

prosperity. Since independence, there has been a substantial

growth in the steel sector in India from 1.5 Mtpa in 1950-51 to

about 71.3 Mtpa finished steel at present.

The per capita steel consumption continues to remain at a level of

about 59 kg only, compared to about >250 kg in the developed

countries and about 50 – 250 kg in some of the developing

countries. Further with nearly 20% of the world population,

India’s consumption is only of the order of 4% of the world steel

production.

The National Steel Policy 2005 had envisaged steel production to

reach 110 million tonnes by 2019-20. However, based on the

assessment of the current ongoing projects, both in greenfield

and brownfield, the Working Group on Steel for the 12th Plan has

projected that the crude steel capacity in the country is likely to

be 140 Mt by 2016-17 and has the potential to reach 149 Mt if all

requirements are adequately met.

India is world's fourth largest crude steel producer in 2011-12

with 71.3 million tonnes (Mt) in 2011-12 and is expected to

become the second largest producer of crude steel in the world by

2015-16.

JSW ISPAT Steel Ltd. is a 3.0 Mtpa Steel plant at Dolvi,

Maharashtra based on BF-DR-CONARC-CSP process route. It also

has cold rolling, galvanizing, colour coating plant, galvalume and



Project Report

1-2

pipe & tube plant at Kalmeshwar, Nagpur in the state of

Maharashtra.

JSW ISPAT Steel Ltd., Dolvi Works has applied for and received

the Environmental clearance for expansion of the integrated steel

plant from 3.0 to 5.0 Mtpa and 300 MW captive power plant.

JSW ISPAT Steel Ltd., Dolvi Works is again proposing to add some

more units to take the capacity of the plant to 10.0 Mtpa at Dolvi.

The proposed capacity enhancement has been envisaged keeping

in view the projected demand of steel in domestic market. The

total capital investment in the proposed project will be around Rs.

17,000 crores. The additional capacity can be produced with

minor additions of land, water, power etc. by using large

equipment and state of the art technology. The proposed

investment will further boost the socio-economic profile of the

region and will open up additional employment opportunities for

the local people in the region.

This Project Report is based on proven production technology,

market demand, site suitability with respect to environmental

norms, available infrastructure and economic viability of the

project.

01.02 Existing & Additional expansion Facilities

JSW ISPAT Steel Ltd., Dolvi Works has the existing capacity of 3.0

Mtpa and has Environmental clearance for 3.0 to 5.0 Mtpa

expansion. It is proposed to further addition of some plant units

which take the final plant capacity to 10.0 Mtpa.



Project Report

1-3

Details of facilities envisaged at 5 and 10 Mtpa Stages

Details of facilities at 5.0 Mtpa stage and the proposed expansion

from 5.0 to 10.0 Mtpa to attain 10.0 Mtpa are shown in Table –

01.01.

Table - 01.01

Facilities at 5.0 Mtpa stage and the proposed expansion from 5.0 to 10.0 Mtpa

S. No.






2.0 4.0


Plant & CDQ MTPA

2.0 2.5 4.5




- 5.2

7 SMS – BOF MTPA - 6.0 6.0 8 Ladle Furnace 2x200 T + 1x205 T 2 X 280/300 T 2x200 T + 1x205 T

+ 2x280/300 T 9 VD/VOD/RH-Degasser 1x200 T + 1x205 T 2 X 280/300 T 1x200 T + 1x205T

+ 2x280/300 T 10 CSP (HRC Coil) Thin Caster-

cum- Hot Strip Finishing Train


- 3.5

11 Conventional Slab Caster MTPA

2 x 1 strand 2 x 2 strand Total 6 strands

12 Plate Mill MTPA 1.5 - 1.5 13 Galvanizing Line (Cold

Rolled Steel Strips, Hot Dip Zinc Coated Full Hard)

MTPA

0.6 - 0.6

14 Electrical Steel CRGO Line MTPA 0.4 - 0.4 15 Tin Plate Line MTPA 0.4 - 0.4 16 Color Coating Plant MTPA

0.5 - 0.5



Project Report

1-4

17 Lime & Dolo Plant TPD 1800 1800 3600 18 Oxygen Plant TPD 4100 3500 7600 19 Captive Power Plant (Gas

Based) MW 300 300 600


MTPA

- 6.0 6.0

21 Slag & Clinker Grinding Unit MTPA - 10.0 10.0 22 CRM (Hot Rolled Skin Pass

+ Cold Rolled Full Hard Coil + Hot Rolled Pickled & Oiled Coil)

MTPA 1.0 1.5 2.5




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02 MARKET ANALYSIS AND PRODUCT MIX 02.01 General

JSW ISPAT Steel Ltd., Dolvi Works, envisages capacity addition of

integrated steel plant to reach final capacity of 10.0 Mtpa. In

order to arrive at a reasonable product-mix for the plant, a quick

desk study based on the secondary data has been carried out and

derived in the following paragraphs.

02.02 Global Steel Scenario

World steel industry experienced growth during the previous years

followed by a period of downturn. The fall in demand is attributed

to the global downturn.

All the major steel-producing countries and regions showed

growth in 2011. The America, Asia & Oceania had higher growth

rates while Europe and the CIS recorded relatively lower growth.

However, Africa & Middle East showed negative growth in 2011.

World crude steel production during 2011 was reported as 1,518

Million tonnes (Mt), 6.23% increase on the annual 2010 total of

1,429 Million tonnes. Annual production for Asia was 974.9 Mt of

crude steel in 2011, an increase of 8.57% compared to 2010.

World trade in finished steel, expressed as a percentage of world

steel consumption is generally about 40 percent. Accordingly, it

may be expected that total trade in finished steel will be of the

order of 450 Million tonnes annually, of which flat products may

constitute upto 60 percent i.e. about 270 Million tonnes and long

products may constitute about 180 Million tonnes.



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02.03 Indian Steel Scenario

02.03.01 Production

The finished steel production in India has grown from a mere 1 Mt

in 1951 to 13.2 Mt in 1990-91 and further increased to 74 Mt in

2011-12. During the first two decades of the planned economic

development, i.e. 1950 to 1960-61 and 1960-61 to 1970-71, the

average annual growth rate of steel production has been about

8%. However, this growth rate could not be maintained in the

following two decades. During 1970-71 to 1980-81, the average

annual growth rate in finished steel production came down to

5.2% and picked up marginally to 5.6% during 1980-81 to 1990-

91. However, average annual growth during 1990-91 to 2000-01

has been encouraging to the level of 8%. The production of

finished steel grew by 16.52 percent, from 44.54 Mt in 2005-06 to

49.39 Mt in 2006-07. The finished steel production for the 2008-

09 registered a growth of 0.6% over 2007-08. Based on the

assessment of the current ongoing projects, both in greenfield

and brownfield, the Working Group on Steel for the 12th Plan has

projected that the crude steel capacity in the country is likely to

be 120 Mt by 2020.

02.03.02 Demand

Domestic Demand

Generally, a developing economy undertakes large number of

infrastructure projects, which are necessary for building of the

nation and ensuring economic growth. China is a leading example

of the economic growth through phenomenal development of

infrastructure.



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The Indian economy grew at 6.5% in 2011-12, down from 8.4%

in 2010-11. The GDP growth in 2011-12 was the lowest in the

past nine years.

Global crisis, geopolitical disturbances and weather extremities

contributed to the domestic economic slowdown. The industrial

sector growth slowed to 3.4% in 2011-12 against 7.2% in 2010-

11 and was primarily responsible for the slowdown of India’s

economic progression. Present low per capita consumption in

India is expected to drive demand for steel, which is likely to grow

@ 7.5% per annum as per Ministry of Steel, Government of India

projections, as detailed in the National Steel Policy 2005.

Export demand

Though India started steel production in 1911, steel exports from

India began only in 1964. Exports in the first five years were

mainly due to recession in the domestic Iron and Steel market.

Once domestic demand revived, exports declined. India again

started exporting steel only in 1975 touching a figure of 1 Mt of

pig iron and 1.4 Mt of steel in 1976-77. Thereafter, exports again

declined to pick up only in 1991-92 to 0.39 Mt. In 1995-96,

exports of semi-finished and finished steel products were 1.77 Mt

while in 2003-04 exports reached 5.2 Mt. During 2004-05, exports

of these products have declined to 4.4 Mt. The exports have

increased by 8.9 per cent in 2006-07 over 2005-06 to touch 4.9

Mt. Exports have declined in the year 2007-08 by 6.1 per cent to

4.6 Mt from 8.9 per cent in 2006-07.

Imports of semi finished and finished steel products mainly HR

plates, HR coils/sheets and CR coils/sheets by India have been in

the range of 1.1 Mt and 2 Mt, during the last ten years.



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In view of the above and anticipated higher emphasis on export of

steel products in future as per National Steel Policy-2005 (26 Mt

exports of steel products by 2020), export demand in the range of

10% to 15% of apparent consumption of various products and

150% for GP/GC sheets has been considered.

Iron and steel industry’s growth in India has been exceptional

though there have been occasional downturns. National steel

policy 2005 estimated domestic steel production to grow by 7.3%

annually and consumption to grow by 6.9% and projected steel

production of 110 million tonnes by the year 2019-20. However, in

2006-07 domestic steel production grew at the rate of 10.9% and

consumption at 11.6%, accordingly, the estimates for production

of steel was revised in 2008 and was projected at 180 million

tonnes as target to be achieved by 2019-20.

02.03.03 Resultant GAPS/Surpluses

Based on the demand and availability, future gaps and surpluses

have been projected in Table-02.01:

Table-02.01

Demand, Availability and Resultant Gaps/Surpluses

Sl.No. Products In (‘000 t)

2006-07 2011-12 2016-17

Steel Products

I Non Flat Products

1 Wire Rods

Demand 6040 8840 12970

Availability 4940 4940 4940



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- Gaps/Surpluses* - 1100 - 3900 - 8030

2 Light Merchant Products

Demand 9790 14060 20220


- Gaps/Surpluses* (+) 360 (-) 2160 (-) 8320

3 Medium Merchant Products

Demand 2440 3465 4910


- Gaps/Surpluses* (-) 325 (-) 1350 (-) 2795

4 Heavy Sections

Demand 560 750 1000


- Gaps/Surpluses* (+) 160 (+) 70 (-) 180

II Flat Products

5 HR Plates

Demand 3680 5175 6900


- Gaps/Surpluses* (-) 2330 (-) 2475 (-) 4200

6 HR Coils /Sheets

Demand 14400 23160 42525


- Gaps/Surpluses* (-) 2360 (-) 6980 (-) 26345*Note: Demand and Gaps/Surpluses are including ‘Export’. From the above, the following conclusions can be drawn:



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• There is enough scope for creation of additional steel

making capacity in the country to meet the growing

domestic demand.

• There is enough opportunity for Indian Steel Producers

to enter the growing world trade in steel.

02.04 Keeping in view the steel market trends, it is proposed to enhance

the capacity to attain 10.0 Mtpa integrated steel plant at Dolvi.

02.05 The tentative product ranges would be :

Flat products



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03 MAJOR TECHNOLOGICAL FACILITIES 03.01 General

The project envisages capacity addition to attain the final capacity

of integrated steel plant to 10.0 Mtpa at Dolvi.

The plant will be equipped with coke oven complex, pellet plant,

sinter plant, blast furnace, sponge iron plant, BOF, ladle furnace,

RH-Degasser, continuous casting facility, hot rolled mill, cold

rolling mill, captive power plant, lime & dolo plant, oxygen plant,

grinding unit, raw material handling system, township and jetty

expansion for the production of flat products. The General Layout

is shown in the Drg. No. JSW/DW/PR/005. Supporting facilities up

to production of finished products will also be set up in the plant

based on the state-of-the-art technology. In this chapter, all major

technological facilities required at each processing step of the

plant are given (Table – 03.01) below with brief description in

subsequent paragraphs.

Table – 03.01

Processing Steps and Technological Facilities

Sl. No. Processing step Technological facility

1. Coke making Recovery Coke Ovens

2. Pelletization Pellet plant

3. Sintering Sinter Plant

4. Iron making Blast Furnace Direct Reduction Plant

5. Steel making BOF

6. Secondary refining

Ladle Furnace

RH-Degasser

7. Continuous casting Slab Caster

8.

Finished Steel Hot Rolled Mill

Cold Rolled Mill



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9. Power generation Captive Power Plant

10. Calcining Lime & Dolo Calcination Plant

11. Oxygen making Oxygen Plant

12. Slag & Clinker Grinding

Slag & Clinker Grinding Unit

13. Township Dwelling units Facilities required outside the plant boundary like expansion of

JSW ISPAT Dolvi jetty and RMHS facilities, sourcing of iron ore,

coking and non-coking coal will also be taken up along with

township etc. The process-cum-material flow sheet has been

shown in the drawing no. JSW/DW/PR/004.

03.02 Coke Oven Batteries

Coke is one of the prime requirements for production of hot metal

through blast furnace route.

Considering the level of technological development in the coke

making area and total requirement of blast furnace coke in the

blast furnace, installation of recovery type coke oven batteries

have been envisaged. The complex is proposed to be equipped

with four (4), stamp charged 5.5m tall coke oven batteries of 65

ovens each. The gross coke generated in the coke ovens will be

screened. BF coke & nut coke will be sent to the blast furnace and

coke fines/ coke breeze generated in the plant will be utilized in

the sinter plant.

The coke making technology would include pre-carbonization and

post carbonization technologies like selective crushing of coal,

stamp charging and high capacity ovens.

Introduction of these technologies are required to reduce the hard

coking coal requirement by blending with soft coking coal in coal



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blend to improve coke quality, to facilitate automation and

pollution control and to maximize the use of semi-soft coking coal.

03.03 Pellet Plant

The Pelletization process involves reduction of moisture in the iron

ore to less than 1%, grinding to 45 micron size, feed preparation

by adding binders and moisture, green pelletization and induration

(heat hardening).

It is proposed to install a Pellet Plant capable of producing upto

4.0 Mtpa of pellets. This Pellet Plant will produce DRI grade pellets

to be used in the sponge iron plant and rest pellets will be used in

the BF.

03.04 Sinter Plant

Sintering is an agglomeration process in which iron ore fines are

mixed with return materials, limestone, and finely sized fuel such

as coke breeze. The return materials consist of mill scale from hot

rolling operations and dust from steel melting shop and blast

furnaces. The raw materials are mixed before they are placed on

the traveling grate of the sinter machine. Near the head end of

the grate, the surface of the raw materials is ignited by a gas fired

ignition furnace located over the bed. As the mixture moves along

the grate, air is drawn through the mixture at the wind boxes to

enhance combustion and sinter (fuse) the fine particles. As the

bed burns, carbon dioxide, cyanides, sulfur compounds, chlorides,

fluorides and oil and grease are driven off with the gases.

The sinter drops off the grate at the discharge end and is cooled

(either by air or a water spray), crushed, and screened to

maintain uniformity in the size of the sinter fed to blast furnaces.



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Improperly sized sinter and fines from screening are returned for

reprocessing.

The advantages of agglomerated burden in the blast furnace is

well established and almost all the high capacity blast furnaces

world-wide are using agglomerated burden for most efficient

furnace operation. The major advantages for use of sinter in blast

furnace are as follows:

Control of physical, chemical and high temperature properties

of burden materials

Avoid use of raw flux charging directly in the blast furnace

Increase in productivity of the furnace

Decrease in coke/fuel rate

Longer life of furnace

Production of desired grade of hot metal, etc.

Apart from the above advantages, the iron ore fines generated in

the mines during production of iron ore lumps are used in the

sinter plant which avoids the problems related to disposal of fines

in the iron ore mines. Moreover, metallurgical waste materials

generated in different process steps shall be recycled in the sinter

plant, which minimizes the dust pollution inside the plant

boundary. The sinter plant is equipped with the following major

facilities:

Base blending for input materials

Flux and fuel crushing facilities

Lime dozing facility

Mixing and nodulising unit

Sintering machine equipped with sinter strand, ignition

furnace, wind boxes, suction fan, dust cleaning unit, etc.

Sinter Coolers



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Sinter screening and transportation facilities

Capacity of the sinter plant has been estimated based on use of

about 75-80% sinter in the burden of blast furnaces, which shall

be obtained from the sintering machine of 8.0 Mtpa capacity.

03.05 Blast Furnace

Hot metal production using blast furnace process has been

envisaged for the proposed project, as the process is most

established and competitive iron making technology till date. A

number of technological improvements have taken place in blast

furnace which has resulted in higher production, less coke

consumption, most energy efficient, long campaign life, etc.

State-of-the-art blast furnace equipped with the following major

facilities has been envisaged for the proposed plant:

Stock house with automatic conveyor charging facilities

Bell less top charging equipment

High top pressure operation (3.0 kg/cm2 top pressure) and

matching gas-cleaning plant

Stoves for generation of high hot blast temperature (1250oC

blast temperature)

Coal dust injection facilities (150 kg/t-hm)

Oxygen enrichment of blast

Cast house slag granulation plant

Top Gas Recovery Turbine

Cast house slag granulation plant. (The slag would be

grinded in slag grinding unit)

Level-III automation and control system, etc.

Hot metal produced from the blast furnace will be transported to

the steel melting shop using hot metal ladles.



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Considering the daily requirement of hot metal in the steel melting

shop for production of liquid steel, which is sufficient to produce

about 4.5 Mtpa hot metal, 1 (one) blast furnace of 4.5 Mtpa

capacity have been envisaged for the proposed project. Slag

generated from the blast furnaces will be granulated in the cast

house slag granulation plant. The granulated slag will be

processed in the grinding units.

03.06 Direct Reduction (DR) Plant

One Mega Module Direct Reduction (DR) Plant based on the

Natural Gas/coke oven gas/LD gas/Mixed gas with average gross

production capacity of 2.0 Mt/yr has been envisaged.

03.07 Steel making and Casting Facilities 03.07.01 Steel Making

Basic oxygen furnace technology for production of liquid steel has

been envisaged for the proposed project. This process till date

dominates the steel production scenario of high capacity

integrated steel plant worldwide mainly due to its energy

efficiency. As such, external energy in terms of either electrical

power or solid/liquid/gaseous fuel is not required for process.

However, requirement of electricity and gaseous fuel are mainly

for driving of electrical equipment, ladle heating, etc. Most of the

other furnaces like electric arc furnace/ induction furnace

consumes high amount of electrical energy. However, oxygen

with high purity is required for conversion of hot metal to liquid

steel and scrap/iron ore/DRI is required as coolant in BOF

process. A significant amount of medium calorific value (2000

kcal/Nm3) gas is generated during carbon refining which is



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separated in the gas cleaning plant. Hot metal will be pre-treated

before charging into the converter.

Considering the requirement of liquid steel for subsequent process

steps, chemical composition of input materials, quality of liquid

steel to be produced, sequence of casting of liquid steel into slabs,

oxygen blowing rate etc., two (2) number of converters of

capacity 280/300 t has been envisaged for the proposed project.

03.07.02 Ladle Furnace (L.F.)

With a view to achieve improved homogeneity of the primary unit,

ladle furnace is the ideal secondary refining unit. The correction

and homogenization of steel composition and temperature,

desulphurisation and recarburisation, etc. can be efficiently carried

out in a L.F. Two (2) L.F. of size 280/300 t has therefore been

envisaged for the proposed project. The LF will also be equipped

with argon purging facilities.

03.07.03 RH-Degasser

RH degasser are envisaged as secondary refining units. The

process assures liquid steel of high purity, low level of inclusions

and good homogeneity with respect to temperature and

chemistry. This process helps attainment of low levels of gases

and inclusions and provides controlled alloying and mixing to

produce variety of alloys. This process also allows improvement in

plant productivity (through sharing of refining load) and yield.

Two (2) RH-Degasser units of matching size 280/300 t has been

envisaged for production of value-added steels. The RH-Degasser

unit will be used for production of various steel grades and for

special applications.



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03.07.04 Slab Caster

The product-mix envisages processing of approximately 6.0 Mt of

liquid steel through conventional slab caster. Considering the

capacity of the plant, conventional slab casting machine has been

envisaged for the proposed plant. The slab caster will be equipped

with the state-of-the-art facilities like electro-magnetic stirring,

mould oscillation, shrouding of liquid metal with inert gas, online

width control, etc. Considering market requirements, two double

strand casters capable of producing slabs of 950-2150 mm width

and 220/250 mm thickness have been envisaged. However this

could be revised to cater to the future market requirements.

03.08 Finished Steel

03.08.01 Hot Rolling Mill

It is envisaged to process slabs through Hot Rolling Mill Finishing

Train for the production of hot rolled coils / strips. This will have

the ability to produce coils of thickness 1.6 to 8.0 mm and with

900 to 2000 mm width with a capacity of 6.0 Mtpa.

03.08.02 Cold Rolling Mill

Hot strips produced in the hot rolling mill will be processed in the

Cold rolling Mill. EC had been obtained at 5 Mtpa stage for CRM of

1.0 Mtpa capacity. It is now proposed to apply for amending the

capacity to 2.5 Mtpa. This large size would be more energy

efficient.



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03.09 Captive Power Plant

To meet the requirement of power for the proposed plant, a

captive power plant of capacity 1 x 300 MW has been envisaged

based on the multi fuel gases.

03.10 Lime & Dolo Calcination Plant

Calcined lime and dolo will be used in steelmaking shop of the

steel plant. In order to meet the requirement of proposed

expansion of integrated steel plant, 3 x 600 tpd lime & dolo

calcination plant have been envisaged.

03.11 Oxygen Plant

To meet the oxygen requirement of proposed expansion of

integrated steel plant, oxygen plant of capacity 3,500 TPD has

been envisaged. The oxygen plant will also meet the requirement

of nitrogen and argon of different technological facilities

envisaged in the proposed integrated steel plant.

Table-03.02 Major Additional Plant Facilities and Their Capacities

S. No.






2.0 4.0


Plant & CDQ MTPA

2.0 2.5 4.5




- 5.2

7 SMS – BOF MTPA - 6.0 6.0



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8 Ladle Furnace 2x200 T + 1x205 T 2 X 280/300 T 2x200 T + 1x205 T + 2x280/300 T

9 VD/VOD/RH-Degasser 1x200 T + 1x205 T 2 X 280/300 T 1x200 T + 1x205T + 2x280/300 T

10 CSP (HRC Coil) Thin Caster-cum- Hot Strip Finishing Train


- 3.5

11 Conventional Slab Caster MTPA

1 x 2 strand 2 x 2 strand Total 6 strands

12 Plate Mill MTPA 1.5 - 1.5 13 Galvanizing Line (Cold

Rolled Steel Strips, Hot Dip Zinc Coated Full Hard)

MTPA

0.6 - 0.6

14 Electrical Steel CRGO Line MTPA 0.4 - 0.4 15 Tin Plate Line MTPA 0.4 - 0.4 16 Color Coating Plant MTPA

0.5 - 0.5

17 Lime & Dolo Plant TPD 1800 1800 3600 18 Oxygen Plant TPD 4100 3500 7600 19 Captive Power Plant (Gas

Based) MW 300 300 600


MTPA

- 6.0 6.0

21 Slag & Clinker Grinding Unit MTPA - 10.0 10.0 22 CRM (Hot Rolled Skin Pass

+ Cold Rolled Full Hard Coil + Hot Rolled Pickled & Oiled Coil)

MTPA 1.0 1.5 2.5




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04 RAW MATERIALS REQUIREMENTS 04.01 General

Raw materials availability is becoming critical due to the heavy

demands made and the limited resources. Proper sourcing and

appropriate beneficiation combined with logistics planning has

become vital for the success of any plant operation. The other

important criterion, concerned to raw materials, is the cost of

transportation involved from mine site to plant site. Iron ore

lumps, Iron ore fines, non-coking coal, coking coal, limestone,

dolomite and quartzite are the major raw materials required for

the plant.

Keeping in view the plant location it is proposed to utilize the

waterways for major transportation. For this purpose it is

proposed to suitably extend the jetty.

04.02 Requirement of Raw Materials

The additional annual (net and dry) requirements of various raw

materials for capacity addition from 5.0 to 10.0 Mtpa are given in

table 04.01.

Table-04.01

Additional Annual Major Raw Material Requirement (net & dry basis):

Sl. No.

Raw material Quantity (tpa)

1. Iron Ore Fines/Conc. (For Pellet Plant) 4,200,000

2. Iron ore fines (for sinter plant) 6,880,000

3. Iron Ore Lumps 380,000

4. Coking Coal (for coke oven) 3,500,000



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5. Non-coking coal for PCI 675,000

6. Limestone (for sinter plant) 491,000

7. Limestone (for pellet plant) 80,000

8. Dolomite (for sinter plant) 503,000

9. Quartzite 60,000

10. Limestone (for SMS) 860,000

11. Dolomite (for SMS) 388,000

12. Ferro-Alloy (for SMS) 103,600

13. Bentonite (For pellet plant) 28,000

14. Clinkers (For Grinding unit) 5,000,000

Estimated requirement of all raw materials have been briefly

described in subsequent paragraphs.

04.02.01 Iron ore

The estimated requirement of total Iron ore fines is 11.08 Mtpa on

net and dry basis. Considering about 10% losses due to moisture,

and 5% losses due to handling, the iron ore requirement works

out to about 13.0 Mtpa.

Iron ore lumps requirement is estimated to around 0.38 Mtpa in

the Blast furnace. Considering about 10% losses due to moisture,

and 5% losses due to handling, the iron ore lumps requirement

works out to about 0.45 Mtpa in Blast Furnace.

04.02.02 Coal

Generally, for coke making, metallurgical coal of different grades

are used in blend. Availability of low ash coking coal of desired

quality in this country is limited. Hence, it has been envisaged that

requirement of metallurgical coal for the proposed steel plant will

be met through imports. The possible sources of supply of



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metallurgical coal are Australia and China, while Australia, Russia,

South Africa and Indonesia are the possible sources of coal used

for PCI coal for BF.

04.02.03 Coking coal

The requirement of coking coal is about 3.5 Mtpa on Net and Dry

basis. 100% Imported Coking Coal is proposed to be used in the

coke oven complex. Considering moisture loss of 10%, handling

loss of 5% the annual requirement is about 4.12 Mt.

04.02.04 Coal for PCI

The PCI Coal requirement for the blast furnace is about 675,000

tpa on Net and Dry basis for pulverized coal injection through the

tuyeres. Considering moisture loss of 10%, handling loss of 5%

the annual requirement is about 0.79 Mt.

The ash content of the injected coal is normally lower than that of

the coke for the most efficient coal dust injection operation. Since

very low ash content non-coking coal is not available in India, it

will be met through imports.

04.02.05 Limestone Limestone will be required as flux material both for iron making

and for steel making. In case of steel making, limestone will be

calcined in a captive calcination plant and the calcined product,

namely burnt lime, will be used in steel melt shop for production

of liquid steel.

The desirable chemical analysis of BF grade limestone is as

follows:



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SiO2 Al2O3 CaO MgO % % % %

3.61 0.60 50.74 1.91

For quality reasons, sustained supply and cost effectiveness, some

imported SMS grade limestone may also be used. High-grade low

silica limestone is produced and traded by several countries

namely Japan, Vietnam, Thailand, Middle-East etc. The typical

analysis of imported limestone is as follows:

SiO2 Al2O3 CaO MgO% % % %

0.43 0.20 54.54 0.91

Some of the Calcined Lime requirement will be fulfilled from the

existing lime calcination plant.

04.02.06 Dolomite

Dolomite will be required as flux material both for iron making and

for steel making. In case of steel making, Dolomite will be

calcined in a captive calcination plant and the calcined product,

namely burnt dolo, will be used in steel melt shop for production

of liquid steel.

For quality reasons, sustained supply and cost effectiveness, some

imported SMS grade limestone may also be used.

04.02.06 Quartzite

It has been proposed to use quartzite in the blast furnace. It has

been proposed to procure quartzite from local region.

A typical analysis of quartzite from this area is as follows:

SiO2 Al2O3 % %

96.5 0.60



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05 PROPOSED SITE

05.01 Site Location The capacity addition of integrated steel plant to take the final

capacity to 10.0 MTPA is proposed to be set up within the existing

steel plant of JSW ISPAT Steel Ltd., Dolvi Works. The existing

integrated steel plant is situated in Dolvi village of Raigad district

in the state of Maharashtra. The site is at a distance of 100 km

from Mumbai, and about 40 km from Panvel by Road. The

location map and the regional map of the proposed site have been

shown in the drawing no. JSW/DW/PR/001 and drawing no.

JSW/DW/PR/002 respectively.

The indicative coordinates of the proposed site are given below:

Longitude - 73°00’00” - 73°05’00” E

Latitude - 18°39’00” - 18°45’00” N

05.02 Area Requirement

The company has already a total of 1200 acres of land in its

possession for its existing integrated steel plant complex. The

layout of its existing plant was prepared keeping in mind the area

requirement for infrastructure, material handling facilities,

different shops / units as required and also area for steel plant

ancillaries and for future expansion within the acquired land.

Some of the proposed additional capacity is proposed to be setup

within the existing plant and some needs relocated by acquiring

additional 600 acres of land.

The area requirement for the proposed plant has been minimized

since the infrastructure and auxiliary facilities are already existing.



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Special attention has been made to provide connectivity to the

existing facilities viz. utilities, raw material corridors, hot metal

tracks, railway tracks, etc.

It is proposed to procure additional 600 acres of land at plant site

for the expansion from 5.0 to 10.0 Mtpa.

05.03 Logistics

The raw material sources are already connected by rail/

road/waterways which will require to be further upgraded. It is

proposed to built additional Jetty of suitable length and connect it

with closed conveyors to the plant.

05.03.01 Road

The National Highway NH-17 (Mumbai-Goa) passes on the east

side of the plant. State Highway also passes on the north side of

the plant. Mumbai city is located at about 100 km on the North-

West side of the plant.

The Road linkage of the proposed site is shown in Drg.No.

JSW/DW/PR/003.

05.03.02 Railways

The nearest railway station Pen is about 8 km from the plant site

and is located in the east on the Konkan Railway Mumbai -

Mangalore main line. Rail linkage from plant site has to be

strengthen to avoid the congestion if part of the finished products

could be sent through railways.

05.03.03 Port Connectivity

The Dolvi complex has a captive port located close to it on the

Amba River, which opens into the Arabian Sea. This port can



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handle barges and mini-bulk carriers up to 4000 dry weight

tonnage (DWT). Moreover, a jetty adjoining the complex is

capable of handling cargo of up to 10 million tonnes per annum.

Imported raw materials and finished products, to be exported,

could be handled through these ports. It is proposed to increase

the jetty length to handle the additional raw material that will

handle upto 50 million tones per annum.

05.03.04 Air Connectivity

The nearest Mumbai airport is 80 km away from site connected

through major road. The proposed Navi Mumbai International

airport is 40 km away from plant site.

05.04 Water

The total water requirement for the 10.0 MTPA steel plant, 600

MW power plant and township will be about 116 MLD. At present

JSW ISPAT Steel Ltd., Dolvi Works has been allocated about 56.0

MLD water from Amba river, Nagothane, K.T.Bandhara and

consent for 30 MLD has been obtained. Application is in progress

for the balance amount.

05.05 Power

The total power requirement for the proposed capacity addition is

proposed to be supplied from the captive power plant and the

State electricity grid. Some power would also be available from

the top pressure recovery turbine generators of the blast furnace

and the Coke Dry Quenching Plant. Waste heat recovery from

sinter cooler is also proposed.



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Power supply for the proposed plant shall be made available from

the 220 kV existing switchyard. It is proposed to relocate the

existing switchyard and suitably augment it.

05.06 Township

The new township shall be constructed to take care of the

accommodation facilities of the employees. Area for the township

has been identified near Pen/Plant but the specific details are yet

to be finalized.

The township is to serve a large steel plant of 10 Mtpa capacity

and CPP of 600 MW capacity and may have up to 7065 dwellings

of various categories in about 150 Acres of land. Township details

are given below:

DOLVI TOWNSHIP AREA CALCULATION

Type BHK Nos.

Area (sq. Ft)/

house

Total Area (sq.

Ft) No. of

storeys

No. of houses

per floor

Total houses

per bldg

No. of blds.

Required Area Req (sq. ft)

1 5 15 4000 60000 1 1 1 15 60000 2 4 50 2500 125000 1 1 1 50 125000 3 3 500 1700 850000 3 2 6 83 283333 4 2 1500 1200 1800000 7 4 28 54 257143 5 1 3000 600 1800000 7 4 28 107 257143 6 1 2000 350 700000 7 4 28 71 100000

Total 7065 5335000 1082619

7 Area of roads/parking area in between houses, etc - 3 times more area than blgs. Area 3247857

Total 4330476

8 Area for GH / schools / gardens / play grounds/ water pond / temple / parkings / shopping centres/hospital etc 2178930

Total 6509406 sq. ft

604743 sq. m

TOTAL 149 acres say 150 acres



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5-5

Raw water shall be treated in the plant and pumped to the

township for their water requirement. Sanitary faecal sewage will

be collected from the ablution blocks through pipeline and the

same will be connected to a sewage treatment plant. The effluent

from sewage treatment plant will be utilized for the development

and maintenance of greenery. Details of the Sewage Treatment

Plant are given below:

Sewage treatment Plant provides only preliminary and primary

treatment, and tertiary treatment is rare.

1. Preliminary treatment: This is the mechanical removal of

coarse and fine solid material. The sewage passes through

screens, which trap pieces of wood, rags, wire, etc.

2. Primary treatment: The sewage then flows slowly through grit

tanks, where particles of sand or grit settle out. Fine particles

still remain suspended in the sewage, so it is passed to large

primary sedimentation tanks where most of the remaining

particles settle out to form sludge. Primary treatment removes

about 60–70% of suspended solids. The liquid leaving the

primary sedimentation tanks still contains very fine solids and

dissolved matter, so secondary treatment is usually required.

3. Secondary treatment: This is a biological process, involving

the oxidation of dissolved organic material by micro-organisms

to decompose the organic compounds, a process similar to

that taking place in rivers, the soil, or filter beds in water

treatment works. The process is speeded up by increasing the

amount of oxygen available, which can be done by two

possible methods:

• Filter beds

• Activated sludge



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5-6

Secondary treatment in addition to primary treatment removes

about 70–90% of the BOD in the sewage, so the effluent is

usually sufficiently purified.

4. Tertiary treatment: Primary and secondary treatment remove

only 20–40% of the phosphorus and nitrogen, and about half

of the toxic compounds. If it is necessary to reduce plant

nutrients or toxic compounds beyond these levels tertiary

treatment is required, but this is very expensive and not

commonly used. Various types of tertiary treatment exists,

e.g. nutrient stripping, disinfection by UV light or filter

membranes.



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06 SERVICES, UTILITIES & MANPOWER REQUIREMENT 06.01 General

Besides raw materials, other major requirements of the plant are

water, power and fuel. Blast furnace, coke oven and LD gas

generated in the plant combined with Natural gas will meet the

demand of fuel of different consuming units. Multi fuel gases may

be utilized for generation of power. The power demand of the

plant will be met from the captive power plant and augmented

thru the existing main receiving substation.

06.02 Power System

The power requirement is proposed to be supplied from the

captive power plant and the state electricity grid. Some power

would also be available from the top pressure recovery turbine

generators of the blast furnace and the CDQ.

From the main receiving and step down station of the plant,

power will be stepped down to 33 kV to feed to the various plant

load centers. These load centers will have provision to step down

further to 11 kV/6.6 kV and 415 V for distribution of power at

required voltages.

Necessary power compensation equipment and harmonic filters

will be provided to take care of the fluctuating load of converter

shop and continuous casters.

For all 220 kV, 33 kV, 11 kV and 6.6 kV supplies, centralized

supervision, monitoring and emergency control system will be

adopted.



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6-2

06.03 Water System

The total water requirement for the 10.0 MTPA steel plant, 600

MW power plant and township will be about 116 MLD. At present

JSW ISPAT Steel Ltd., Dolvi Works has been allocated about 56.0

MLD water from Amba river, Nagothane, K.T.Bandhara and

consent for 30 MLD has been obtained. Application is in progress

for the balance amount.

Raw water treatment plant will be installed for pretreatment of

raw water and the clarified water will be pumped through MS

pipeline to the proposed units.

The different categories of water to be used in the recirculating

system are:

a) Demineralised (DM) water for closed recirculating cooling

systems.

b) Soft water for closed recirculating cooling systems.

c) Indirect cooling water (ICW) for secondary cooling of the

water-to-water heat exchangers of the closed cooling circuits.

d) Direct cooling water (DCW) for gas cleaning circuits, slag

granulation, open machinery cooling and scale flushing.

e) Make-up water & service water for captive power plant.

For conserving water, independent recirculating systems have

been proposed along with cooling towers, pump houses and

treatment units.

Make-up water for different process units will be made available

from main plant make-up water ring main and will be conveyed to



Project Report

6-3

respective cold wells of various recirculating systems and storage

reservoirs.

In order to combat industrial pollution and to comply with

guidelines laid down by the statutory authorities, suitable

treatment units and neutralization pits will be provided to control

water pollution in different water system units. Attempts will be

made to achieve zero discharge as far as practicable by making

use of bleed water from cooling tower and other effluent water for

dust suppression.

Waste water generated from different areas of plant will be

treated to the desired extent and recycled in the recirculating

system as far as possible, facilitating adequate reuse of water.

Backwash water generated from different pressure filters will be

treated in a treatment plant having sludge disposal facilities. The

treated water will be reused in the direct cooling circuit.

06.04 Manpower Requirement

The steel plant will not only require management and executive

manpower but also, skilled, semi-skilled, unskilled and clerical

manpower. However, a number of jobs like major repair and

maintenance, cleaning, transportation and loading/unloading of

bulk materials, etc. will be done by engaging out side agencies.

Considering a labour productivity of 1,100 tonnes of finished steel

per man-year, which is at par with international standard, the

requirement of total manpower is about 5,000 including power

plant.

The above number covers the top management, middle and junior

level executives and other supporting staff. The above manpower

excludes the manpower required for outsourcing of repair and



Project Report

6-4

maintenance jobs of the entire plant and also does not cover the

personnel for township, medical facilities, etc. The category wise

break-up of manpower is indicated in table – 06.01.

Table – 06.01

Category wise break-up of manpower

Sl. No. Category Requirement

1. Managerial 180

2. Executive 400

3. Skilled 1300

4. Semi-skilled 1600

5. Unskilled 1400

6. Clerical 120

Total 5,000



Project Report

7-1

07 ENVIRONMENTAL MANAGEMENT

The proposed units of steel plant would result in air, water and

land pollution of varying nature and degree. This chapter briefly

outlines the nature and sources of pollution and also suggests

broad environmental protection measures to be adopted for

limiting pollution within permissible levels.

07.01 Nature of Pollution

The additional capacity would comprise various production

facilities such as raw material yard, coke oven plant, sinter plant,

blast furnace, Steel making & secondary refining, captive power

plant, lime & dolo calcining plant, continuous casting, hot rolling

mill and cold rolling mill. The inputs to the above facilities will

comprise raw materials/in-process materials along with water, fuel

and power. These would therefore lead to release of emissions to

the air, generation of wastewater and solid wastes. The sources of

pollution from the proposed project and the types of

environmental pollution likely to occur are summarized in Table-

07.01.

Table-07.01

Sources and Nature of Pollution

Facility/Department Pollutants released Type of pollution

Raw material yard Fugitive dusts Air pollution

Sinter plant SO2, NOx, dust, heat, noise

Air pollution & Noise pollution

Heating in cooling water

Thermal pollution of water bodies at the outfall

Coke Oven TSP, CO2, NOx, SO2, PAH, heat

Air pollution



Project Report

7-2

TSP, VOC Work zone air pollution

Oil & grease, phenol, cyanide

Water pollution

Blast furnace Dust, SO2, NOx, heat, noise

Air pollution and Noise pollution

Sponge Iron Plant Dust, SO2, NOx, heat, noise


Calcining plant Heat, dust, SO2 & NOx Air pollution

Work zone air pollution

Steel Melt Shop Dust, NOx, heat Work zone air pollution

Continuous caster Heat, particulate dust, SO2, NOx, noise


Suspended scales, Traces of oil & grease

Water pollution

Rolling Mills (HSM & CRM)

Heat, particulate dust, SO2, NOx, noise


Suspended scales, Traces of oil & grease

Water pollution

Power Plant Heat, SO2 & NOx Air pollution

Water pollution

07.02 Pollution Prevention and Control Measures

In consideration of the above stated pollution potential of the

integrated steel plant, suitable mitigation schemes are envisaged

in order to control environmental pollution within the permissible

norms and keep the environment fairly clean.

07.03 Design Targets

The proposed pollution control measures would be designed on

the basis of the following criteria:



Project Report

7-3

Characteristics of treated waste water to be discharged to plant drain

a. Temperature shall not exceed 5oC above ambient TSS < 100 mg/l Oil & grease < 10 mg/l BOD < 30 mg/l at 20oC for 5 days COD < 250 mg/l.

b. Stack emissions TSP < 50 mg/N m3

c. Work zone dust level (8 hrs TWA)

< 5 mg/m3

d. Work zone noise (Leq) (Time weighted average of 8 hrs)

85 dB (A)

Routine environmental monitoring of stack emission, ambient air

quality, work zone air quality, noise level and waste water

receiving pond and surface water stream will have to be carried

out. The monitored data would be recorded and necessary

corrective measures implemented to ensure that design targets

are maintained and avoid any non-compliance of Statutory

Regulations.

07.04 Plant safety

Plant safety measures would form an integral part of the

environment protection plan of the proposed plant. Workers’

safety would be of highest degree of concern so as to avoid any

form of personal injury or untoward accident. In-build safety

features of the plant and machinery would be made adequate in

order to avoid hazardous events causing damage to the life and

property.



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7-4

07.05 Greenbelt and landscaping

Adequate space would be created for gardening and tree

plantations to dovetail with the existing greenbelts. This would

prevent the fugitive dust emissions. Unpaved areas, if any, within

the plant boundary would be provided with grass cover. This

would not only act as ‘lung space’ but would also improve the

plant aesthetics.



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08 PROJECT IMPLEMENTATION 08.01 General

Implementation of capacity enhancement of an Integrated Steel

Plant is a challenging task and calls for meticulous planning,

scheduling and monitoring to realize the project goals in budgeted

time frame. Dovetailing the new units with the existing ones is a

great challenge. JSW has an enviable track record for project

execution. A highly experienced team has been set up for the

purpose through specifically defined responsibilities.

08.02 Schedule

The implementation schedule for installation of the proposed

Integrated Steel Plant is indicated in the form of bar chart in the

drawing no. JSW/DW/PR/006. The overall schedule shows that

from the date of start of the project (Zero date), the complete

plant will be commissioned in 36 months. The schedule as

presented is based upon conventional project implementation

logics for Steel Plant, preliminary vendor information available and

in-house experience. The schedule of 36 months has been

conceived, considering the existing practices and delivery

schedule of similar plants & equipment at Dolvi.

08.03 Zero Date

The date of start of project activities has been assumed as “zero

date” for installation of the proposed capacity addition at Dolvi.



Project Report

9-1

09 BLOCK CAPITAL COST

The estimated block capital cost for the capacity addition to take

the integrated steel plant capacity from 5.0 to 10.0 Mtpa is

estimated as Rs. 17,000 crores.

LF & VDLCP-3

A M

B A

R

I V

E R

MAIN GATE

FIN

FA

N C

OO

LER

S

FIN FANCOOLERS

H. R. JHONSON PLANT AREA

TW TW TW

GOA GATE

BOU

NDARY WALL

BO

UN

DA

RY

B L

A S

T

F U

R N

A C

E

S P

O N

G E

I R

O N

P

L A

N T

R M H S A R E A

H O

T

S T

R I

P

M I

L L

SINTER PLANT - 1

HELIPAD AREA PRO

POSE

D RA

ILW

AY S

IDIN

G

POWER PLANT1x53.5 MW

B T3

SINTERPLANT-3

LIMEPLANT

OXYGENPLANT

HOTSTRIPMILL

SMS

BASEMIX

FLUX

IRON

ORE

COKING

COAL

CEMENTPLANT

POWERPLANT HARSCO

COKE OVEN PLANT-3

SINTER

PLANT-2

COLDROLLING

MILLS

MSDS

DRPLANT-2

BLASTFURNACE

PELLETPLANT-2

PLATEMILL

SL. ACTIVITIES DURATION OF NO. ACTIVITY

1 Project Approval 0 Month

2 Basic Engineering 6 Months

3 Detailed Engineering 29 Months

4 Tendering, Scrutiny and order placement 23 Months

5 Planning & construction of Infrastructure facilities 15 Months

6 Civil works 30 Months

7 Fabrication & Erection of Structures 24 Months

8 Delivery of Equipment 21 Months

9 Erection of Equipment 20 Months

10 Testing & Commissioning of Steel Plant 4 Months

11 Production to commence -

26 28242

DRG. NO. JSW/DW/PR/006

3210 12 14 16 3018 20 224 6 8

CAPACITY ADDITION OF ISP FROM 5.0 MTPA TO 10.0 MTPA AND CPP FROM 300 MW TO 600MW AT DOLVI, MAHARASHTRA

PROJECT IMPLEMENTATION SCHEDULE

D U R A T I O N I N M O N T H S34 36

28 Outputs

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