revised form – 1environmentclearance.nic.in/writereaddata/... · form 1 for expansion of kamanda...

REVISED FORM – 1 FOR

EXPANSION OF INTEGRATED STEEL PLANT

(AMENDMENT TO TOR VIDE MOEF&CC LETTER NO. J-11011/434/2009.IA.II(I) dated 03.08.2016)

VILLAGE KAMANDA

DISTRICT SUNDERGARH, ODISHA (0.60 MTPA to 0.75 MTPA STEEL)

November, 2016 (Issue 01, Rev. 0)

Submitted by:

RUNGTA MINES LIMTED RUNGTA HOUSE, CHAIBASA

JHARKHAND - 833201

Form 1 for Expansion of Kamanda Steel Plant of M/s Rungta Mines Ltd. 1

APPENDIX I (See Paragraph- 6)

FORM 1 (Issue 02, Rev 1, November 2016)

(I) Basic Information 1 Name of the Project/s Expansion of 0.60 MTPA to 0.75 MTPA

integrated steel plant at village Kamanda, Sundergarh, Odisha by M/s Rungta Mines Limited (This application is for an amendment to TOR)

2 S. No. in the Schedule 1(d), 2 (a), 2(b), 4 (b) and 3(a) 3 Proposed capacity/ area/ length/

tonnage to be handled/ command area/ lease area/ number of wells to be drilled

Area : 381.74 acres Steel production from 0.6 to 0.75 MTPA (against TOR granted for 0.7 MTPA on 03.08.2016) Refer enclosure I for proposed capacity & tonnage

4 New/ Expansion/ Modernization Expansion 5 Existing capacity/ area, etc. Area: 154.489 Ha (381.740 acres).

First environmental clearance was granted by MOEF letter no. J-11011/304/2007-IA.II.(I)dated 12.12.2008 for a steel making capacity of 0.20 MTPA

Second EC for expansion of steel making capacity from 0.20 MTPA to 0.60 MTPA was granted by MOEF&CC vide letter no. J-11011/434/2009-IA.II (I) dated 02.02.2015 (Copies of both above EC letters is enclosed as Enclosure II).

MOEF & CC granted TOR to expand existing facilities from 0.60 MTPA to 0.70 MTPA steel. TOR is issued by MOEF &CC vide letter No. J-11011/434/2009-IA.II(I) dated 03.08.2016 (copy of TOR letter is enclosed as Enclosure III)

However, configuration of sub-units within the plant have been modified for better integration and the total resultant capacity will become 0.75 MTPA, for which this application for modification is being made.

6 Category of Project i.e. ‘A’ or ‘B’ “A”


7 Does it attract general condition? If

yes, please specify No, because 1) Nearest WL sanctuary / Reserve eco

sensitive area Simpli Pal National Park = 97 km E

2) Simlipal Sanctuary = 130 km E 3) Inter-state boundary Jharkhand = 10.6 km

N 4) International Boundary Bangladesh = 393

km ENE 8 Does it attract specific condition? If

yes, please specify No as it is not located in any industrial complex/estate etc.

9 Location Refer Enclosure IV for location plan Plot/ Survey/ Khasra no. Land schedule is enclosed as Enclosure V Village Kamanda Tehsil Koida District Sundergarh State Odisha 10 Nearest railway station/ airport

along with distance in kms Railway Station : Barasuan 15 km Airport : Bhubaneshwar 210 km, Ranchi 210 km

11 Nearest town, city, district head

quarters along with distance in kms Nearest town : Koida 3 km District Head quarter : Sundergarh 124 km

12 Village Panchayats, Zilla Parishad,

Municipal Corporation, Local Body (complete postal addresses with telephone nos. to be given)

Vill. Panchayat : Kalta District : Sundergarh State : Odisha

13 Name of the applicant Rungta Mines Ltd. 14 Registered Address Rungta Mines Limited

8A, Express Tower 42 A, Shakespeare Sarani, Kolkata -700017

15 Address for correspondence : Name P. Deo Designation (Owner/ Partner/ CEO) General Manager (Commercial) Address Rungta Mines Limited

Sponge Iron Division, Main Road Barbil, Keonjhar Odisha

Pin Code 758035


E mail [email protected] [email protected]

Telephone no. (06767) 277391, 276081 Fax (06767) 276891 16 Details if Alternative sites examined,

if any. Location of these sites should be shown in a toposheet

No alternative sites under consideration because this application is for an amendment to TOR.

17 Interlinked Projects No 18 Whether separate application of

interlinked project has been submitted?

No

19 If yes, date of submission Not applicable 20 If no, reason Not applicable 21 Whether the proposal involves

approval/ clearance under : if yes, details of the same and their status to be gives:

Not applicable

(a) The Forest (Conservation) Act, 1980?

Not applicable since no forest land within project area.

(b) The Wildlife (Protection) Act, 1972?

Not applicable as not within 10 km of a notified area

(c) The CRZ Notification, 1991? Not applicable as it is not near sea shore. 22 Whether there is any Government

Order/ Policy relevant/ relating to the site?

No

23 Forest land involved (hectares) Nil 24 Whether there is any litigation

pending against the project and/or land in which the project is proposed to be set up?

No

(a) Name of Court Not applicable (b) Case No. Not applicable (c) Orders/ directions of the Court,

if any and its relevance with the proposed project

Not applicable

* Capacity corresponding to sectoral activity (such as production capacity for manufacturing, mining lease area and production capacity for mineral production, area for mineral exploration, length for linear transport infrastructure, generation capacity for power generation.


(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.)

Sl. 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)

Yes Total plant area of 154.489 ha (381.740 Acres). Company has purchased directly 111.08 acres private land, which is already under industrial usage. 186.340 acres private land and 61.52 acres Government land has been acquired through IDCO and balance 22.80 acres government land under process. The topography shall change where the proposed units shall be constructed.

1.2 Clearance of existing land, vegetation and buildings?

Yes The existing plant area has buildings, sheds, roads, storage etc constructed on it which shall remain as it is. The proposed expansion area has grasses, shrubs and a few trees, which will be cleared as per requirement. The construction will avoid cutting of any trees, but if any tree is to be cut, due permission shall be taken. One third of the plant area shall be planted with trees. No hutments or houses or buildings are there. Hence, clearance of existing buildings shall not be there.

1.3 Creation of new land uses? Yes Infrastructure facilities, offices, plantation etc. already created in the existing plant area which shall remain the same. The proposed plant area was either Govt. wasteland or private agricultural land prior to acquisition. The land use will change to industrial after installation of the plant.

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

No Exploration for estimation of load bearing capacity of soil has been carried out. It has not affected the topography or land form.

1.5 Construction works? Yes Within existing plant, augmentation will take place while there will be construction of additional


Sl. No.


Yes/No


with source of information data manufacturing facilities only.

1.6 Demolition works? No There is no structure in the area which will require any demolition.

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

Yes Mostly local workers will be employed. Some sheds will be there which will be temporary for some workers, technicians, engineers.

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

Yes The buildings will be above ground and storm water drainage system shall be designed around them to ensure efficient drainage of rainwater.

1.9 Underground works including mining or tunneling?

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

processes? Yes Process description and flow sheet are

given in PFR as Enclosure IX. 1.14 Facilities for storage of goods or

materials? Yes Facilities for storage of coal in coal

stack yard, iron in iron stack yard, etc will be provided. Storage facility for steel ingots/ billets and sponge iron.

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

Yes The various waste materials arising out of the technological processes shall be reutilised to the extent possible. Slag from blast furnace will be granulated and sold as bi-product. Other waste materials which cannot be reused are planned to be dumped in environmental friendly manner in a separate area. Zero Effluent Discharge will be practiced. Industrial effluent from plant will be treated in ETP and the domestic effluent will be separately treated in the STP. The treated water will be re- circulated in the plant for various uses.

1.16 Facilities for long term housing of operational workers?

Yes Local skilled/ unskilled workers shall be employed to the extent possible. However, for outstation employees, colony has been provided for long term housing


Sl. No.


Yes/No


with source of information data 1.17 New road, rail or sea traffic

during construction or operation?

Yes During additional manufacturing facilities construction there will be increase in the truck traffic bringing in the construction material and equipment, bus/ light motor vehicular traffic as well as 2 wheelers and cycles to bring in manpower. During operation, increase in road traffic due to transportation of raw materials, finished product, movement of man and material to and from the plant will necessitate widening of the existing road.

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

Yes Existing road will be strengthened and widened to cater for the traffic. No sea, rail or air transportation infrastructure will be built.

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

No

1.20 New or diverted transmission lines or pipelines?

No

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

Yes Three first & second order seasonal streams are respectively originating & passing through the project area and joining Karo Nala, which are likely to be disturbed. To ensure the uninterrupted evacuation of rain water runoff, the plant shall have well laid storm water drainage network leading to the Karo Nala near the eastern boundary

1.22 Stream crossings? No 1.23 Abstraction or transfers of water

from ground or surface waters? Yes The total water consumption shall

increase from 1943 m3/hr (for 0.7 MTPA) to 2385 cum/hr (for 0.75 MTPA) after implementation of entire expansion proposal

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

Yes There is no change in water bodies but the land surface will be changed due to construction of buildings and storage areas. Storm water drainage system is being provided to ensure systematic


Sl. No.


Yes/No


with source of information data rain water evacuation to the natural drains.

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

Yes Transportation of manpower, raw material, finished product will take place.

1.26 Long-term dismantling or decommissioning or restoration works?

No None

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

No None

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

Yes The existing manpower is 500 (for 0.2 MTPA) and proposed manpower for the expansion project will increase from 1252 (for 0.7 MTPA) to 1635 (for 0.75 MTPA) which will lead to influx of people in the area. Local inhabitants will be given preference in employment according to their capability and qualification. Outstation employees are and will be housed in the colony of the Company.

1.29 Introduction of alien species? No 1.30 Loss of native species or genetic

diversity? No

1.31 Any other actions? No

2. Use of Natural resources for construction or operation of the Project (such as land, water, materials or energy, especially any resources which are non-renewable or in short supply):

Sl. No.

Information/checklist confirmation

Yes/ No


with source of information data

2.1 Land especially undeveloped or agricultural land (ha)

Yes The acquired area is under industrial usage for the existing plant. The additional areas will also change from earlier govt wasteland, private agricultural, etc to industrial use.

2.2 Water (expected source & competing users) unit: KLD

Yes Total water requirement is 2385 m3/hr (for 0.75 MTPA) from Karo river to meet the plant requirement.


Sl. No.

Information/checklist confirmation

Yes/ No


with source of information data 2.3 Minerals (MT) Yes The raw material required for the steel plant

and its various sub units are Iron ore lumps, Washed Coal, Coke, ROM Coal, limestone/ dolomite, Quartzite, Scrap, etc. and the details have been given in the enclosed pre-feasibility report as Enclosure IX

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

Yes Civil construction work requires aggregate, steel, bricks, cement, etc which will be sourced from nearby area

2.5 Forests and timber (source – MT)

Yes Will be bought from vendors for construction of a few doors and windows.

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

Yes The power requirement of the plant is being met by own generation. The proposed requirement shall be increase from 143 MW (for 0.7 MTPA) to 177 MW (for 0.75 MTPA).

2.7 Any other natural resources (use appropriate standard units)

No

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.

Sl. No.


Yes/ No

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

with source of information data 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 No Hazardous material will be used as raw material. The hazardous waste material handled within the plant is used oil & lubricant and DM resin. The oil & lubricant will be sold and the DM resin shall be disposed as per CPCB norms.

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

No No water borne diseases anticipated since there is no disposal of waste water without treatment. All water is proposed for reuse and recycling.

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

Yes Direct employment will increase from 1252 persons (for 0.7 MTPA) to 1635 persons (for 0.75 MTPA)besides indirect employment to more will change the living


Sl. No.


Yes/ No


with source of information data condition of the locality / society.

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

No Since all practicable precautionary measure will be taken to control air, water and noise pollution, the project is expected not to affect the vulnerable group.

3.5 Any other causes No

4. Production of solid wastes during construction or operation or decommissioning (MT/month)

Sl. No.


Yes/ No


with source of information data 4.1 Spoil, overburden or mine

wastes No Not applicable

4.2 Municipal waste (domestic and or commercial wastes)

Yes Municipal waste is being generated from the canteen and offices of the plant. The waste generation is approximately at the rate of 100 gm/capita/day. About 50 kg waste is being generated currently for 0.2 MTPA steel plant. 164 kg/day is anticipated in future at full capacity (for 0.75 MTPA).

4.3 Hazardous wastes (as per Hazardous Waste Management Rules)

Yes Used oil, waste containing oil, oily sludge, spent resin and discarded oil and grease containers will be anticipated additionally.

4.4 Other industrial process wastes

Yes Char, ESP & Bag filter dust, Kiln accretion & misc. Dust, MBF Slag, MBF Flue dust, GCP Sludge, IF & LRF Slag, FES dust, CPP Fly ash, and CPP bottom.

4.5 Surplus product No 4.6 Sewage sludge or other

sludge from effluent treatment

Yes Sewage sludge is being and will be digested and used as compost / manure.

4.7 Construction or demolition wastes

No Not applicable

4.8 Redundant machinery or equipment

Yes Some parts shall be replaced which can be sold to recycling vendors, especially metal.

4.9 Contaminated soils or other materials

No

4.10 Agricultural wastes No 4.11 Other solid wastes No


5. Release of pollutants or any hazardous, toxic or noxious substances to air

(Kg/hr) Sl. No.


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 Emissions due to consumption of coal and coke shall be there from DRI kiln, AFBC, MBF, etc. The emissions due to burning of fossil fuel is being controlled by use of electrostatic precipitators, dust extractors etc. The details of the emissions had been enumerated in EIA/EMP submitted to MOEF at time of EC and same is and will be followed

5.2 Emissions from production processes

Yes Same as above

5.3 Emissions from materials handling including storage or transport

Yes Fugitive dust emissions are and shall be there which are and shall be controlled through sprinkling, dust extraction system, etc, as applicable.

5.4 Emissions from construction activities including plant and equipment

Yes Some dust generation shall take place during construction, which can be countered by regular water spraying and is for short duration.

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

No

5.6 Emissions from incineration of waste

No

5.7 Emissions from burning of waste in open air (e.g. slash materials, construction debris)

No

5.8 Emissions from any other sources

No

6. Generation of Noise and Vibration, and Emissions of Light and Heat:

Sl. No.


Yes/ No

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

of information data. 6.1 From operation of

equipment e.g. engines, Yes The noise generation due to machinery will

be in the range of 80-100 dB(A).


Sl. No.


Yes/ No

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

of information data. ventilation plant, crushers

6.2 From industrial or similar processes

Yes The noise levels near the sources such as plant machinery, induction furnace and diesel generator set will be slightly higher during operation in their vicinity. However, they shall be within the stipulated regulatory limits.

6.3 From construction or demolition

Yes Noise generation shall be there during construction phase, which will be temporary and reversible after completion of construction.

6.4 From blasting or piling No Not applicable 6.5 From construction or

operational traffic Yes By proper maintenance of the vehicles,

noise pollution during operational traffic will be controlled.

6.6 From lighting or cooling systems

Yes Heat generated in the vicinity of DRI kilns, light bulbs, furnace etc and from higher temperature emissions from stacks

6.7 From any other sources No

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

Sl. No.


Yes/ No


source of information data 7.1 From handling, storage, use

or spillage of hazardous materials

No Used oil, waste containing oil, oily sludge, spent resin and discarded oil and grease containers will be generated and will be stored and disposed to CPCB authorized recycling vendors as per norms

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

No Septic tank-soak pit system along with clarifiers has been used and there is no discharge into any water body or onto land. Industrial effluent from plant will be treated in ETP and the domestic effluent will be separately treated in the STP. The treated water will be re- circulated in the plant for various uses.

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

Yes Air pollutants will be controlled by water sprinkling on the roads, stack yards, etc. and by using ESP, dust extractors in the


Sl. No.


Yes/ No


source of information data plant. Hence, deposition will be minimal and washed off during rains

7.4 From any other sources No 7.5 Is there a risk of long term

build up of pollutants in the environment from these sources?

No

8. Risk of accidents during construction or operation of the Project, which

could affect human health or the environment Sl. No.


Yes/ No


with source of information data 8.1 From explosions, spillages,

fires etc from storage, handling, use or production of hazardous substances

Yes Fuels such as LDO/ HSD will be stored which are potential fire hazards. There can be explosion or fire in plant equipment. It is incorporated in the onsite emergency preparedness plan

8.2 From any other causes No 8.3 Could the project be affected

by natural disasters causing environmental damage (e.g. floods, earthquakes, landslides, cloudburst etc)?

No The Plant area falls in seismic Zone – II, which is not an active seismic zone. The project is not likely to be affected by floods, landslides, cloudburst etc.

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

Sl. 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 e.g.:

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

Yes Present road leading to the project site from the main road will be widened. Other roads will also be made.

Housing development Yes The nearby villages can see some


Sl. No.


Yes/ No


with source of information data development of residential and commercial properties to offer accommodation and services to the people coming to work in the plant

Extractive industries No No Supply industries Yes Some kiosks for supply of the daily

requirement of the employees and drivers can come up on the road and in the vicinity of the plant

Other No 9.2 Lead to after-use of the site,

which could have an impact on the environment

No

9.3 Set a precedent for later developments

No

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

Yes There are approximately 40 mines in the 25 km radius of the project. The nature and range of the pollutants from mines is mostly related to localized air pollution, pollution due to transportation and impact on surface & ground water besides ecology and land.

(III) Environmental Sensitivity (Refer Enclosure VI for 15 km study area map)

Sl. 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

Forests are listed in point 2 below

-

Torha RF 1.8 km NW Karo RF 1.0 km N Uliburu RF 6.3 km NNE Mendhamaruni RF 3.2 km E Kathamala RF 0.5 km E RF near Bhabani 3.6 km SSE Sarkanda RF 5.5 km S Siddhamath RF 11.4 km NE Rakshi RF 12.7 km NW

2. Areas which are important or sensitive for ecological reasons - Wetlands, watercourses or other water bodies, coastal zone, biospheres, mountains, forests

Khajurdihi RF 9.2 km SSE


Sl. No.



Rivers & Streams : Bacha nala 7.5 NW Boream nala 8.1 SE Erua nala 4.8 WNW Gera nala 5.4 W Geria nala 7.6 W Jakanal nala 8.6 SE Karo river 0.2 NE / E Khajurdihi nala 8.8 SE Khuntachira nala 7.3 SE Kukarha 0.5 E Lekerapani nala 1.9 E Samij nala 2.4 NW Karo nala 0.01 E Sirki nala 9.3 WSW Suna nadi 8.6 E

Teherai nala 6.5 SE 3. Areas used by protected, important

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

Forests as listed above

4. Inland, coastal, marine or underground waters

Water bodies are listed in point no 2

5. State, National boundaries Nil - 6. Routes or facilities used by the

public for access to recreation or other tourist, pilgrim areas

NH-215 0.6 km

7. Defense installations Nil 8. Densely populated or built-up area Koida 3.0 km, SE 9. Areas occupied by sensitive man-

made land uses (hospitals, schools, places of worship, community facilities)

Hospitals, Schools, Community facilities are present within 10 km of the study area. List of amenities in Villages in 10 km is given in Enclosure VII.

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

Nil, Forests and water bodies are listed in point 2 above

-

11. Areas already subjected to pollution Nil -


Sl. No.



or environmental damage. (those where existing legal environmental standards are exceeded)

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)

The Plant area falls in seismic Zone – II, which is not an active seismic zone. The project is not likely to be affected by floods, landslides, cloudburst etc.

IV) Proposed Terms of Reference for EIA studies: This application is for an

amendment to TOR. Copy of TOR earlier issued by MOEF&CC is enclosed as Enclosure III. As the TOR was issued in monsoon season, the baseline environmental monitoring was commenced on completion of monsoon season i.e. 15.09.2016, which is post monsoon season. The monitoring is ongoing and will continue till 31.12.2016 (totalling to 3+ months).

I hereby give undertaking that the data and information given in the

application and enclosures 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 given, if any to the project will be revoked at our risk and cost.

Date: 14.11.2016 Place: Barbil

(Project Proponent / Authorized Signatory )

Name P. Deo Designation General Manager (Commercial) Address Rungta Mines Limited

Sponge Iron Division, Main Road Barbil, Keonjhar Odisha-758035

Submit document supporting claim of authorized signatory for the specific project. (Refer Enclosure VIII)


LIST OF ENCLOSURES

Enclosure No. Description

I Proposed capacity and tonnage

II EC letter No. J-11011/304/2007-IA.II (I) dated 12.12.2008 for 0.2 MTPA steel production EC letter No. J-11011/434/2009-IA.II (I) dated 02.02.2015 for increase from 0.2 to 0.6 MTPA steel production

III TOR issued by MOEF&CC vide letter no. J-11011/434/2009-IA.II (I) dated 03.08.2016

IV Location plan

V Land schedule

VI Map showing 15 km radius around project site

VII List of amenities within 10 km radius

VIII Authorization to signatory

IX Pre-feasibility report

ENCLOSURES

ENCLOSURE: I

PROPOSED CAPACITY/ AREA/ LENGTH/ TONNAGE TO BE HANDLED/ COMMAND AREA/ LEASE AREA/ NUMBER OF WELLS TO BE DRILLED

(Question I.3 of form I) Sl. No.

Facility Present capacity as per EC dated

02.02.2015 (TPA)

TOR obtained for additional capacity(TPA)

dated 03.08.2016

TOR Amendment request

Additional Capacity

(TPA)

Total Capacity Additional capacity (TPA)

Total capacity after proposed

expansion (TPA)

(a) (b) (c) (d) (e) = (c)+(d) (f)= replaces (d), except 10

(g) = (c)+(f); replaces (e),

except 10 1 Beneficiation

Plant 1,100,000 1,00,000 1,200,000 No change 1,200,000

Pellet Plant-1 600,000 0 600,000 No change 600,000 Pellet plant-2 Nil Nil Nil 2X1,200,000+

10% upgradation (240,000)

2,640,000 2

Sub Total 600,000 0 600,000 2,640,000 3,240,000 3 Coal

Washery 924,000 0 924,000 No change 924,000

DRI Plant 6X100 TPD 180,000 77,400 257,400 No change 257,400 1X300 TPD 90,000 38,700 128,700 No change 128,700 3X350 TPD 315,000 100,800 415,800 No change 415,800 2X500TPD 330,000 66,000 396,000 No change 396,000

4

Sub total 915,000 282,900 1,197,900 1,197,900 5 Sinter Plant 240,000

(24 sq.m.) 175,800 18 sqm

415,800 (42 sq.m.)

Capacity enhanced of

existing 1X24 sq.m. by 26,112

+ Additional 1 X24

sq.m. of 266,112

532,224 2x24 sqm

Mini Blast Furnace

2X262 CUM 382,520 49,780 432,300 75,980 458,500 1X260 CUM 227,500 0 227,500 No change 227,500

6

Sub-total 610,020 49,780 659,800 686,000 7 Coke Oven (2

batteries of 140,000 0 140,000 No change 140,000

ENCLOSURE: I Contd..

Sl. No.


02.02.2015 (TPA)


dated 03.08.2016


Additional Capacity

(TPA)



expansion (TPA)



except 10 70,000 TPA) SMS 4X15T IF 2x15T LRF

200,000 17,800 217,800 31,000 231,000

9 X15T IF 5x15T LRF

430,000 60,050 490,050 89,750 519,750

8

Sub total 630,000 77,850 707,850 120,750 750,750 Billet/ Slab/ Bloom Caster

0.20 MTPA 200,000 15,000 215,000 26,380 226,380 0.42 MTPA 420,000 63,000 483,000 replacing 0, as

replaced 0.20 MTPA Nil Nil Nil 226,380 226,380 0.22 MTPA Nil Nil Nil 282,975 282,975

9

Sub total 620,000 78,000 698,000 735,735 Flat/ Round/ Wire Rod/ Structural Mill/ others

410,000 0 410,000

Mill -1 4,10,000 4,10,000 217,325 217,325 Mill-2 (no split 0 (no split 217,325 217,325 Mill -3 Specified) Specified) 271,656 271,656

10

Sub total 4,10,000 0 4,10,000 706,306 706,306 11 Ferro Alloy

Plant (1x9 MVA+1x18 MVA)

0

Ferro Manganese OR

- 9 MVA= 18,000 18 MVA=36,000

9 MVA= 18,000 18 MVA=36,000

No change 54,000

Silico Manganese OR

- 9 MVA= 14,400 18 MVA=28,800

9 MVA= 14,400 18 MVA=28,800

No change 43,200

ENCLOSURE: I Contd..

Sl. No.


02.02.2015 (TPA)


dated 03.08.2016


Additional Capacity

(TPA)



expansion (TPA)



except 10 Ferro Chrome OR

- 9 MVA= 14,400 18 MVA=28,800

9 MVA= 14,400 18 MVA=28,800

No change 43,200

Ferro Silicon - 9 MVA= 6,400 18 MVA=12,800

9 MVA= 6,400 18 MVA=12,800

No change 19,200

Briquette Plant for ferro chrome

- 88,320 88,320 No change 88,320

Briquette Plant for ferro manganese

- 111,360 111,360 No change 111,360

Captive Power Plant

142 MW 14 MW 156 MW 56 MW 198 MW

WHRB 66 MW 14 80 MW 21 MW 87 MW

12

AFBC / CFBC 76 MW 0 76 MW 35 MW 111 MW

ENCLOSURE : II

ENCLOSURE : II Contd..

ENCLOSURE : III

ENCLOSURE : III Contd..

ENCLOSURE : V

SL.NO. MOUZA KHATA NO. PLOT NO. KISSAM AREA IN ACRES

1 KAMANDA 137/85 792 FACTORY 3.820

793/1416 FACTORY 4.000

795 FACTORY 3.620

842 FACTORY 0.320

845 FACTORY 0.180

846 FACTORY 5.800

851 FACTORY 0.100

852 FACTORY 0.100

858 FACTORY 0.390

859 FACTORY 0.270

860 FACTORY 0.250

861 FACTORY 0.700

865 FACTORY 0.430

873 FACTORY 0.220

876 FACTORY 0.100

877 FACTORY 0.320

878 FACTORY 0.040

881 FACTORY 2.400

888 FACTORY 0.350

890 FACTORY 0.250

900 FACTORY 0.240

901 FACTORY 0.350

904 FACTORY 0.250

906 FACTORY 0.180

907 FACTORY 0.160

910 FACTORY 0.580

911 FACTORY 0.700

913 FACTORY 0.960

915 FACTORY 0.110

917 FACTORY 0.070

918 FACTORY 0.070

923 FACTORY 0.570

925 FACTORY 0.500

927 FACTORY 0.600

933 FACTORY 0.160

934 FACTORY 0.160

937 FACTORY 0.220

938 FACTORY 1.630

939 FACTORY 0.240

943 FACTORY 0.130

944 FACTORY 0.120

945 FACTORY 0.130

946 FACTORY 0.120

949 FACTORY 0.180

950 FACTORY 0.230

951 FACTORY 0.100

LAND DETAILS OF

M/S. RUNGTA MINES LIMITED

(KAMANDA STEEL PLANT)

AT- KAMANDA, PO- KOIRA

DIST- SUNDARGARH (ODISHA)

Page 1 of 12

ENCLOSURE : V


952 FACTORY 0.130

958 FACTORY 0.300

959 FACTORY 0.280

960 FACTORY 0.350

966 FACTORY 0.240

965 FACTORY 3.240

967 FACTORY 0.130

968 FACTORY 0.850

849 FACTORY 1.490


847 FACTORY 0.070

848 FACTORY 0.510

969 FACTORY 0.460

783 FACTORY 1.220

784 FACTORY 0.420

784/1324 FACTORY 0.200

869/1260 FACTORY 0.210

793 FACTORY 2.000

865 FACTORY 0.040

891 FACTORY 0.580

965 FACTORY 0.710

797 FACTORY 1.180

1323 FACTORY 0.540

832 FACTORY 3.500

833 FACTORY 0.150

843 FACTORY 0.140

853 FACTORY 0.100

857 FACTORY 0.290

862 FACTORY 0.340

866 FACTORY 0.740

875 FACTORY 0.160

872 FACTORY 0.500

892 FACTORY 0.360

893 FACTORY 0.120

897 FACTORY 0.200

902 FACTORY 0.300

840 FACTORY 0.290

922 FACTORY 0.450

926 FACTORY 0.510

932 FACTORY 0.400

940 FACTORY 0.110

941 FACTORY 0.070

953 FACTORY 0.150

954 FACTORY 0.110

961 FACTORY 1.870

962 FACTORY 0.240

963 FACTORY 0.200

971 FACTORY 1.460

972 FACTORY 0.640

791 FACTORY 2.460

835 FACTORY 4.000

839 FACTORY 0.350

Page 2 of 12

ENCLOSURE : V


844 FACTORY 0.160

854 FACTORY 0.350

864 FACTORY 1.060

874 FACTORY 0.180

883 FACTORY 0.260

884 FACTORY 0.280

885 FACTORY 0.180

914 FACTORY 0.070

916 FACTORY 0.090

931 FACTORY 0.400

942 FACTORY 0.140

886 FACTORY 0.100

889 FACTORY 0.170

894 FACTORY 0.200

896 FACTORY 0.440

899 FACTORY 0.100

903 FACTORY 0.490

909 FACTORY 0.550

912 FACTORY 0.510

947 FACTORY 0.080

948 FACTORY 0.100

955 FACTORY 0.180

956 FACTORY 0.170

964 FACTORY 2.240

855 FACTORY 0.330

784/1325 FACTORY 0.250

834/1 FACTORY 0.650

881/1295 FACTORY 1.490

871 FACTORY 0.280

869 FACTORY 1.590

781 FACTORY 0.460

782 FACTORY 0.420

1011 FACTORY 0.650

1022 FACTORY 1.180

800 FACTORY 0.750

803 FACTORY 0.090

804 FACTORY 0.800

801/1283 FACTORY 0.150

801 FACTORY 1.250

802 FACTORY 0.560

805 FACTORY 0.620

881/1357 FACTORY 1.030

881 FACTORY 1.370


928 FACTORY 7.400

930 FACTORY 1.500

973 FACTORY 0.800

786 FACTORY 1.840

790 FACTORY 1.060

880 FACTORY 1.850

882 FACTORY 7.360

935 FACTORY 0.540

Page 3 of 12

ENCLOSURE : V


936 FACTORY 2.350

4 KAMANDA ORDER NO. 3251/ 794 RASTA 0.360

25.10.2004 850 RASTA 0.320

856 RASTA 0.190

957 RASTA 0.620

976 RASTA 1.300

5 KULA 44/19 266 FACTORY 0.350

149 FACTORY 1.480

263 FACTORY 0.510

263/1 FACTORY 0.510

207 FACTORY 0.760

205 FACTORY 0.110

147 FACTORY 2.620

151 FACTORY 0.870

196 FACTORY 1.040

204 FACTORY 0.320

260 FACTORY 0.560

265 FACTORY 0.380

148 FACTORY 1.620

150 FACTORY 0.800

195 FACTORY 1.020

38 FACTORY 2.200

495/1 FACTORY 1.920

37 FACTORY 0.600

495/771 FACTORY 0.700

6 KUSUMDIHI 34/49 210/491 GHARBARI 1.820

TOTAL 149.370

7 KAMANDA 1 552 MA. SA. 0.090

602/1318 MA. SA. 0.140

558 BE. SA. 0.040

1035 BE. SA. 0.120

1024/1329 BE. SA. 0.100

1227/1335 BA. SA. 0.130

1227/1336 BA. SA. 0.150

0.770

2 1081 BE. SA. 0.200

3 1061 BE. SA. 0.370

4 1105 Goda-II 1.220

6 1132 Goda-II 1.900

1133 Goda-II 3.250

1134 Goda-II 1.340

1133/1272 Goda-II 0.300

6.790

7 977 BE. SA 0.140

1073 BE. SA 0.220

1071 MA. SA 0.870

1072 MA. SA 1.850

3.080

8 1065 BE. SA 0.440

Page 4 of 12

ENCLOSURE : V


1185 BE. SA 1.020

1.460

9 605 MA.SA 0.140

606 MA.SA 0.170

1109 Goda-II 2.520

1110 Goda-II 0.680

3.510

10 1142 Goda-II 2.270

13 929 Patita 1.590

1003 Patita 0.260

1112 Patita 0.200

2.050

17 1062 BE. SA 0.460

18 597 MA. SA. 0.300

620 MA. SA. 0.500

621 Goda-II 0.120

0.920

21 1027 BE. SA 0.360

23 603 MA.SA 0.260

610 MA.SA 0.780

618 MA.SA 0.030

1177 MA.SA 0.440

1177/1332 MA.SA 0.220

1151 BE. SA 0.540

2.270

24 1085 BA. SA 0.030

1194 BE. SA 1.200

1182 MA. SA 0.820

1086 Goda-II 0.100

2.150

25 1044 MA. SA. 0.210

26 1144 MA. SA. 0.780

27 1058 BE. SA 0.360

1078 BE. SA 0.330

0.690

29 1059 BE. SA 0.250

30 1089 MA. SA. 0.420

1166 MA. SA. 0.840

1169 MA. SA. 0.360

1171 MA. SA. 0.040

1090 Goda-II 3.710

1106 Goda-II 2.350

1156 Goda-II 1.270

1168 BA. SA 1.300

1190 BE. SA 1.200

1193 BE. SA 0.520

1199 BE. SA 0.180

12.190

32 974 BA. SA 0.240

928/1289 Goda-II 2.340

Page 5 of 12

ENCLOSURE : V


2.580

34 1084 MA. SA 0.480

1060 BE. SA 1.960

1207 BE. SA 0.800

1208 BE. SA 0.600

3.840

35 1087 BA. SA 0.740

1217 BA. SA 0.260

1091 Goda-II 0.750

1092 Goda-II 0.580

1107 Goda-II 3.420

1093 MA. SA 0.430

1167 MA. SA 0.860

1210 BE. SA 0.660

1218 BE. SA 0.300

8.000

37 1033 BE. SA 1.000

39 928/1290 Patita 1.900

40 554 MA. SA. 0.510

1082 BE. SA 0.840

1.350

41 1040 Goda-II 1.400

1161 Goda-II 1.580

1162 Goda-II 0.090

1163 Goda-II 0.120

1164 Goda-II 0.560

3.750

42 555 MA. SA. 0.090

601 MA. SA. 0.420

1023/1305 MA. SA. 0.170

552/1317 MA. SA. 0.100

552/1315 MA. SA. 0.110

602/1320 MA. SA. 0.100

756 Goda-II 0.400

834 Goda-II 1.200

553 Goda-II 0.080

557 BE. SA 0.100

1024 BE. SA 0.150

1037 BE. SA 0.020

1035/1330 BE. SA 0.140

1034 BA. SA 0.300

1036 BA. SA 0.120

1038 BA. SA 0.240

1227/1334 BA. SA 0.200

3.940

43 1178 BE. SA 0.150

1197 BE. SA 1.200

1.350

44 979 BE. SA 0.400

993 MA. SA 0.780

998 MA. SA 0.620

999 BA. SA 0.680

Page 6 of 12

ENCLOSURE : V


1001 BA. SA 0.670

1002 BA. SA 0.130

3.280

47 565 BE. SA 0.350

50 545 MA. SA 0.180

1051 MA. SA 0.140

0.320

51 754 Goda-II 0.840

52 1219 BE. SA 0.170

1220 BA. SA 0.220

0.390

54 542 MA. SA 0.520

1170 MA. SA 0.480

1231 MA. SA 1.200

1103 Goda-II 0.580

2.780

55 1063 BE. SA 0.400

57 1138/1307 Goda-I 0.120

1138 Goda-I 1.000

1198 BE. SA 1.180

1088 Goda-II 2.400

4.700

60 599 MA. SA 0.180

1236 BE. SA 1.480

1.660

63 980 BE. SA 0.040

1000 BE. SA 0.680

1214 BA. SA 0.300

1215 BA. SA 0.120

990 MA. SA 0.080

992 MA. SA 0.120

988 Goda-II 0.050

991 Goda-II 0.600

1.990

64 560 BE. SA 0.350

561 BE. SA 0.150

564 BE. SA 0.040

978 BE. SA 1.290

1213 BE. SA 0.160

1226 BE. SA 0.090

2.080

65 1005 Patita 0.100

1006 Patita 0.100

1007 Patita 0.090

1008 Patita 0.100

1009 Goda-II 0.860

1108 Goda-II 1.280

1068 BE. SA 0.300

2.830

67 549 MA. SA 0.220

550 MA. SA 0.140

Page 7 of 12

ENCLOSURE : V


753 Goda-I 0.520

0.880

68 1043 MA. SA 0.600

1067 BE. SA 1.140

1.740

71 1115 Goda-II 2.880

1121 Goda-II 1.260

1123 Goda-II 0.450

1174 Goda-II 0.530

1175 MA. SA 0.630

1118 BE. SA 1.760

1122 Gharbari 0.040

7.550

72 1080 BE. SA 0.230

1155 BE. SA 0.040

1154 Goda-II 0.400

1172 MA. SA 0.050

0.720

74 1013 Goda-II 1.170

1228 BE. SA 0.090

1230 MA. SA 0.760

2.020

77 543 MA. SA 0.380

544 MA. SA 0.220

1229 BE. SA 0.660

1.260

79 600 MA. SA 0.200

80 1101 Goda-II 1.100

607 MA. SA 0.220

611 MA. SA 0.380

1187 BE. SA 0.750

1216 BE. SA 0.110

2.560

82 608 MA. SA 0.220

83 1141 Goda-II 3.690

86 1212 BE. SA 0.260

88 1054 BE. SA 0.350

1056 BE. SA 0.380

1180 BE. SA 0.060

0.790

89 1048 MA. SA 0.110

92 1015 Goda-II 0.140

602 MA. SA 0.140

552/1316 MA. SA 0.150

1024/1328 BE. SA 0.250

1227/1333 BA. SA 0.580

1.260

93 598 MA. SA 0.300

617 MA. SA 0.450

1064 BE. SA 0.650

1202 BE. SA 0.330

1203 BE. SA 0.100

Page 8 of 12

ENCLOSURE : V


1221 BE. SA 0.850

2.680

94 1233 Goda-II 0.100

551 MA. SA 0.450

1232 MA. SA 0.950

1235 MA. SA 0.600

2.100

96 1042 BE. SA 0.220

1070 BE. SA 0.180

0.400

97 1104 Goda-II 1.840

1157 Goda-II 0.200

1158 Goda-II 0.440

1159 Goda-II 1.800

1179 BE. SA 0.200

1192 BE. SA 0.540

1200 BE. SA 0.530

1201 BE. SA 0.950

6.500

101 1012 Goda-II 0.490

1094 MA. SA 0.620

1095 Goda-II 0.220

1096 Goda-II 0.700

1097 MA. SA 0.440

1098 Goda-II 0.240

1150 BE. SA 1.300

879/1261 Goda-II 0.210

4.220

102 879 Goda-II 0.790

1127 Goda-II 2.120

1128 Goda-II 0.760

3.670

104 1049 MA. SA 0.200

1052 BE. SA 0.200

1079 BE. SA 0.200

1186 BE. SA 0.770

1.370

105 787 Goda-II 1.000

552/1314 MA. SA 0.100

562 MA. SA 0.160

602/1319 MA. SA 0.100

563 MA. SA 0.220

1023 MA. SA 0.680

559 BE. SA 0.100

1188 BE. SA 0.900

1024/1327 BE. SA 0.150

1227 BA. SA 0.280

3.690

107 755 Goda-II 1.220

788 Goda-II 0.270

1.490

108 1183 Goda-II 0.580

Page 9 of 12

ENCLOSURE : V


1173 MA. SA 0.560

1.140

109 1191 BE. SA 0.980

111 995 MA. SA 0.080

997 MA. SA 0.100

982 BE. SA 0.120

986 BE. SA 0.600

1026 BE. SA 0.530

1030 BE. SA 0.450

1074 BE. SA 0.200

1076 BE. SA 0.200

1224 BE. SA 0.260

2.540

110 1222 BE. SA 0.200

112 1204 MA. SA 0.150

113 628 MA. SA 1.080

1205 MA. SA 0.120

1204/1273 MA. SA 0.960

1209 BE. SA 0.720

1211 BE. SA 0.500

1206 BA. SA 0.400

3.780

114 975 BE. SA 0.210

115 1018 Goda-II 0.370

984 Goda-II 0.110

996 MA. SA 0.160

1021 MA. SA 0.560

976 BE. SA 0.200

983 BE. SA 0.060

985 BE. SA 0.520

987 BE. SA 0.440

1025 BE. SA 0.520

1031 BE. SA 0.480

1223 BE. SA 0.230

1225 BE. SA 0.110

1075 BE. SA 0.010

3.770

117 1165 Goda-II 3.160

118 1139 Goda-II 0.700

120 1050 BE. SA 0.210

1055 BE. SA 0.350

0.560

121 596 MA. SA 0.680

124 919 Goda-II 0.100

920 Goda-II 0.030

921 Goda-II 0.040

1234 MA. SA 0.070

0.240

127 547 MA. SA 0.040

131 1234/1301 MA. SA 0.060

132 546 MA. SA 0.050

136 981 MA. SA 0.090

Page 10 of 12

ENCLOSURE : V


137 994 MA. SA 0.040

137/1 1069 BE. SA 0.390

137/4 1032 BE. SA 0.270

137/5 1057 BE. SA 0.320

137/12 930/1293 Goda-II 1.900

137/13 1077 BE. SA 0.150

137/14 1083 BE. SA 0.360

1087/1381 BA. SA 0.300

0.660

137/15 838 Goda-II 0.150

863 Goda-II 0.600

870 Goda-II 0.100

887 Goda-II 0.280

1.130

137/17 895 Goda-II 1.750

137/18 841 Goda-II 0.250

849 Goda-II 1.510

1.760

137/19 796 Goda-II 1.430

965/1356 Goda-II 0.300

1.730

137/21 1016 Goda-II 0.200

1017 Goda-II 0.410

1019 Goda-II 0.040

1020 MA. SA 0.220

1039 BE. SA 0.210

1.080

137/22 1176 BE. SA 0.550

137/23 1149 BE. SA 0.650

137/24 1041 BE. SA 0.220

137/46 1071/1380 MA. SA 0.350

137/47 1153 Goda-II 0.450

1152 BE. SA 0.180

0.630

137/49 1148 MA. SA 1.700

1144/1384 MA. SA 1.220

2.920

137/53 1100 Goda-II 2.540

137/58 1040 BE. SA 0.250

977/1392 BE. SA 0.180

0.430

137/73 1010 Goda-II 0.350

1028 BE. SA 0.460

1029 BE. SA 0.090

0.900

137/77 1111 Goda-II 0.440

1113 Goda-II 0.860

1114 Gharbari 0.120

1.420

137/78 1207/1407 BE. SA 0.120

1208/1408 BE. SA 0.620

0.740

Page 11 of 12

ENCLOSURE : V


137/79 1207/1409 BE. SA 0.520

128 924 Goda-II 0.030

59 612 MA. SA 0.650

1066 BE. SA 0.430

1181 BE. SA 0.700

1143 Goda-II 2.420

4.200

TOTAL 186.340

8 KAMANDA 140 548 Patit 0.020

556 Patit 0.010

575 Patit 0.040

604 Patit 0.020

609 Patit 0.010

635 Patit 0.160

719 Patit 0.030

752 Patit 0.530

908 Patit 0.060

1004 Patit 1.100

1045 Patit 0.450

1047 Patit 0.060

1053 Patit 0.200

1117 Goda-II 3.920

1119 Goda-II 1.030

1120 Ga.Ba. 0.050

1126 Goda-II 2.410

1129 Goda-II 0.800

1130 Goda-II 4.920

1131 Goda-II 1.830

1136 Goda-II 2.300

928/1288 Goda-II 3.280

TOTAL 23.230

9 KAMANDA 138 711 Patit 0.040

1099 S.S.J. 6.720

1124 U.J.Jogya 4.000

1125 S.S.J. 2.820

989 Nalla 0.320

1046 Nalla 0.850

139 744 Rasta 0.120

747 Rasta 0.430

785 Rasta 0.360

789 Rasta 0.470

140 705 Patit 0.950

TOTAL 17.080

10 KUSUMDIHI 37 240 Patit 5.720

TOTAL 5.720

381.740GRAND TOTAL

Page 12 of 12

ENCLOSURE : VIIAMENITIES AVAILABLE IN VILLAGES WITHIN THE STUDY AREA (CENSUS 2011)

EXPANSION OF INTEGRATED STEEL PLANT AT KAMANDA OF M/S RML

Town/ Town/village EDUCATION FACILITIES

village name PPS PS MS SS SSS DCAS EC MC MI P VTS/ITI NFTC SFD EO

code Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt. Govt. Pvt.

District : Sundargarh

Sub distt.: Koida

384748 Tada N.A. - 1 - 1 - (<5 km) - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. - N.A. - N.A. -

384749 Jhirpani (10+ km) - 1 1 1 - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384750 Kalta (10+ km) - 3 - 1 - 1 - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384751 Nadikasira (10+ km) - 1 - 1 - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384752 Rengalbeda (10+ km) - 1 - 1 - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384753 Kasira (10+ km) - 1 - (<5 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384754 Kusumdihi (10+ km) - 1 - 1 - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384755 Kamanda N.A. - 1 - 1 - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. - N.A. - N.A. - N.A. - N.A. -

384756 Kula (10+ km) - 1 - 1 - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384757 Harischandrapur N.A. - 1 - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384758 Bhanjapali (5-10 km) - 1 - 1 - 1 - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384759 Segasahi (5-10 km) - 1 1 (5-10 km) - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384760 Badindipur (5-10 km) - 1 - 1 - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384761 Sanindipur (<5 km) - 1 - (5-10 km) - (<5 km) - (<5 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384762 Ghodabudani (5-10 km) - 1 - 1 - (5-10 km) - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384763 Adaghat (5-10 km) - 1 - (<5 km) - (5-10 km) - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384777 Ranisal (10+ km) - 1 - (<5 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384778 Sargigarh (10+ km) - 1 - (<5 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384780 Teherei (10+ km) - 1 - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384781 Kadodiha (10+ km) - 1 - (<5 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384782 Nuagaon (10+ km) - 1 - (<5 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384783 Rengua (10+ km) - 1 - (5-10 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384784 Bandal (10+ km) - 1 - (5-10 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384785 Tantra (10+ km) - 1 - (5-10 km) - (5-10 km) - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384786 Raikela (10+ km) - 1 - 1 - (5-10 km) - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384787 Dengula (10+ km) - 1 - 1 - 1 - (5-10 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384788 Tentulidihi (<5 km) - 1 - (<5 km) - (<5 km) - (<5 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384789 Sidimba (<5 km) - 1 - 1 - (<5 km) - (<5 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384791 Tantigram N.A. - 1 - (<5 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. - (10+ km) - N.A. - N.A. - N.A. -

384792 Kalmanga (10+ km) - 1 - 1 - 1 - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384793 Baldihi (10+ km) - 1 - 1 - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384794 Khajuridihi (5-10 km) - 1 - (<5 km) - (5-10 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

384802 Kiriakudar (5-10 km) - 1 - (5-10 km) - (<5 km) - (5-10 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

Sub distt.: Lahunipara

384903 Jaldihi N.A. - (10+ km) - (5-10 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. - (10+ km) - N.A. -

384944 Bahamda (10+ km) - 1 - (<5 km) - (<5 km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - (10+ km) - N.A. -

[1/3]

Town/ Town/village

village name

code


Sub distt.: Koida

384748 Tada

384749 Jhirpani

384750 Kalta

384751 Nadikasira

384752 Rengalbeda

384753 Kasira

384754 Kusumdihi

384755 Kamanda

384756 Kula

384757 Harischandrapur

384758 Bhanjapali

384759 Segasahi

384760 Badindipur

384761 Sanindipur

384762 Ghodabudani

384763 Adaghat

384777 Ranisal

384778 Sargigarh

384780 Teherei

384781 Kadodiha

384782 Nuagaon

384783 Rengua

384784 Bandal

384785 Tantra

384786 Raikela

384787 Dengula

384788 Tentulidihi

384789 Sidimba

384791 Tantigram

384792 Kalmanga

384793 Baldihi

384794 Khajuridihi

384802 Kiriakudar


384903 Jaldihi

384944 Bahamda

ENCLOSURE : VII Contd..AMENITIES AVAILABLE IN VILLAGES WITHIN THE STUDY AREA (CENSUS 2011)


MEDICAL FACILITIES

CHC PHC PHSC MCWC TBC HA HAM D VH MHC FWC NGMF-

OP

NGMF-

IOP

NGMF-

C

NGMF-

MBBS

NGMF-

OD

NGMF-

ND

NGMF-

TPFH

NGMF-

MS

NGMF-

O

(10+ km) (5-10 km) 1 (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) (10+ km) (5-10 km) (10+ km) - - - - 1 1 - 3 - (5-10 km) (5-10 km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) 1 (5-10 km) (5-10 km) (10+ km) 1 1 1 2 2 2 3 1 - (5-10 km) (5-10 km) 1 (5-10 km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) - - - 1 1 - 1 1 - (5-10 km) (5-10 km) (<5 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (<5 km) (5-10 km) (<5 km) (10+ km) - - - - - 1 1 - -

(<5 km) (5-10 km) 1 (<5 km) (10+ km) (<5 km) (<5 km) (5-10 km) (<5 km) (5-10 km) (5-10 km) - - - - 1 1 1 3 - (5-10 km) (5-10 km) 1 (5-10 km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) - - - 1 1 - - 1 - (5-10 km) (5-10 km) (<5 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) - - - 1 1 - - 1 - (5-10 km) (5-10 km) 1 (<5 km) (10+ km) (5-10 km) (5-10 km) (<5 km) (5-10 km) (<5 km) (10+ km) - - - - 1 1 - 3 -

(<5 km) (5-10 km) (5-10 km) (<5 km) (10+ km) (<5 km) (<5 km) (<5 km) (<5 km) (<5 km) (10+ km) - - - 1 - 1 - - -

(<5 km) (10+ km) (5-10 km) (<5 km) (10+ km) (<5 km) (<5 km) (5-10 km) (<5 km) (5-10 km) (10+ km) - - - - - 1 1 - - (5-10 km) (5-10 km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) - - - 1 1 - - 1 - (5-10 km) (5-10 km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) - - - 1 - 1 1 - - (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (10+ km) (5-10 km) - - - 1 1 1 1 1 -

(10+ km) (5-10 km) (5-10 km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) - - - - 1 1 - - -

(10+ km) (<5 km) (<5 km) (10+ km) (10+ km) (10+ km) (10+ km) (<5 km) (10+ km) (5-10 km) (10+ km) - - - - 1 1 - - - (5-10 km) (10+ km) (5-10 km) (<5 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (<5 km) (10+ km) (5-10 km) - - - 1 - 1 1 1 - (5-10 km) (10+ km) (<5 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) - - - 1 1 1 - - - (5-10 km) (10+ km) (<5 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (<5 km) (5-10 km) (<5 km) (5-10 km) - - - 1 1 1 2 1 -

(<5 km) (5-10 km) 1 (<5 km) (10+ km) (<5 km) (<5 km) (5-10 km) (<5 km) (5-10 km) (5-10 km) - - - 1 1 - - 1 - (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (10+ km) (5-10 km) - - - - - - - - -

(10+ km) (10+ km) (5-10 km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) - - - - 1 1 - - -

(10+ km) (10+ km) (5-10 km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) - - - - 1 1 - - -

(10+ km) (10+ km) (5-10 km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) - - - 1 1 - - - -

(10+ km) (10+ km) (5-10 km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) (10+ km) (5-10 km) (10+ km) - - - - 1 1 - 1 - (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (10+ km) - - - - 1 1 - - - (5-10 km) (10+ km) 1 (5-10 km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) - - - - - - - 3 - (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (5-10 km) (10+ km) (<5 km) - - - - 1 1 - - -

(10+ km) (10+ km) (5-10 km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) - - - - - 1 1 - -

(10+ km) (10+ km) (<5 km) (10+ km) (10+ km) (10+ km) (10+ km) (<5 km) (10+ km) (5-10 km) (5-10 km) - - - - 1 1 - - - (5-10 km) (10+ km) (10+ km) (<5 km) (10+ km) (5-10 km) (5-10 km) (<5 km) (<5 km) (5-10 km) (10+ km) - - - 1 1 - - - - (5-10 km) (10+ km) (10+ km) (5-10 km) (10+ km) (5-10 km) (5-10 km) (10+ km) (<5 km) (10+ km) (10+ km) - - - 1 1 - - - -

(10+ km) (10+ km) (5-10 km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) (10+ km) (5-10 km) (10+ km) - - - 1 1 - - - - (5-10 km) (10+ km) (<5 km) (10+ km) (10+ km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (5-10 km) (10+ km) - - - - - - - - -

(10+ km) (<5 km) (<5 km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) - - - - - - - - -

(10+ km) (10+ km) 1 (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (10+ km) (5-10 km) - - - - 1 1 - 3 -

[2/3]

Town/ Town/village

village name

code


Sub distt.: Koida

384748 Tada

384749 Jhirpani

384750 Kalta

384751 Nadikasira

384752 Rengalbeda

384753 Kasira

384754 Kusumdihi

384755 Kamanda

384756 Kula

384757 Harischandrapur

384758 Bhanjapali

384759 Segasahi

384760 Badindipur

384761 Sanindipur

384762 Ghodabudani

384763 Adaghat

384777 Ranisal

384778 Sargigarh

384780 Teherei

384781 Kadodiha

384782 Nuagaon

384783 Rengua

384784 Bandal

384785 Tantra

384786 Raikela

384787 Dengula

384788 Tentulidihi

384789 Sidimba

384791 Tantigram

384792 Kalmanga

384793 Baldihi

384794 Khajuridihi

384802 Kiriakudar


384903 Jaldihi

384944 Bahamda

ENCLOSURE : VII Contd..AMENITIES AVAILABLE IN VILLAGES WITHIN THE STUDY AREA (CENSUS 2011)


DRINKING WATER FACILITY COMMUNICATION SYSTEM

TWT TWUT CW UW HP TW/

BW

S R/C T/P WO PO SPO P&T PIN T PCO MPC IC/CSC PCF

N N N Y Y N N N Y N (10+ km) 1 (10+ km) 770052 1 N.A. 1 (10+ km) 1

N N N Y Y N N N Y N 1 (10+ km) (10+ km) 770052 1 1 1 (5-10 km) (5-10 km)

N Y N Y Y N N Y Y N 1 (5-10 km) (10+ km) 770052 1 N.A. 1 (5-10 km) 1

N N N Y Y N N N Y N (10+ km) (5-10 km) (10+ km) 770048 (10+ km) (10+ km) 1 (5-10 km) (5-10 km)

N N N Y Y N N N Y N (10+ km) (<5 km) (10+ km) 770048 1 N.A. 1 (<5 km) (<5 km)

N Y N Y Y N N Y Y N (10+ km) (5-10 km) (10+ km) 770048 1 1 1 (5-10 km) (5-10 km)

N Y N Y Y N N N Y N (10+ km) (5-10 km) (10+ km) 770048 (10+ km) (10+ km) 1 (5-10 km) (5-10 km)

N N N Y Y N N N Y N (10+ km) (5-10 km) (10+ km) 770048 (10+ km) (10+ km) 1 (5-10 km) (5-10 km)

N N N Y Y N N N Y N (10+ km) (<5 km) (10+ km) 770048 (<5 km) (<5 km) 1 (<5 km) (<5 km)

N N N Y Y N N N Y N (10+ km) (<5 km) (10+ km) 770048 1 1 1 (<5 km) (<5 km)

N N N Y Y N N N Y N (10+ km) (5-10 km) (10+ km) 770048 (10+ km) (10+ km) 1 (10+ km) (10+ km)

N N N Y Y N N N Y N (10+ km) (5-10 km) (10+ km) 770048 (5-10 km) (5-10 km) (10+ km) (5-10 km) (5-10 km)

N N N Y Y N N N Y N (10+ km) (5-10 km) (5-10 km) 770048 1 N.A. 1 (5-10 km) (5-10 km)

N N N Y Y N N N Y N (10+ km) (10+ km) (10+ km) 770048 (10+ km) (10+ km) 1 (10+ km) (10+ km)


N N N Y Y N N N Y N (10+ km) (5-10 km) (10+ km) 770048 (5-10 km) (5-10 km) 1 (5-10 km) (5-10 km)

N N N Y Y N N N Y N (10+ km) (5-10 km) (10+ km) 770048 1 N.A. 1 (5-10 km) (5-10 km)

N N N Y Y N N N Y N (5-10 km) (5-10 km) (10+ km) 770048 (5-10 km) (5-10 km) 1 (5-10 km) (5-10 km)

N N N Y Y N N N Y N (10+ km) (<5 km) (10+ km) 770048 1 N.A. 1 (<5 km) (<5 km)

N N N Y Y N N N Y N (10+ km) (5-10 km) (5-10 km) 770048 1 N.A. 1 (5-10 km) (5-10 km)



N Y N Y Y N N N Y N (10+ km) (<5 km) (10+ km) 770048 1 N.A. 1 (10+ km) (10+ km)

N N N Y Y N N N Y N (10+ km) (10+ km) (10+ km) 770042 1 N.A. 1 (10+ km) (10+ km)


N N N Y Y N N Y Y N 1 (5-10 km) (5-10 km) 770048 1 N.A. 1 (5-10 km) (5-10 km)



N N N Y Y N N N Y N (10+ km) (10+ km) (10+ km) 770048 (10+ km) (10+ km) (10+ km) (10+ km) (10+ km)

N N N Y Y N N N Y N (10+ km) (5-10 km) (5-10 km) 770048 (10+ km) (10+ km) (10+ km) (5-10 km) (5-10 km)

N N N Y Y N N Y Y N (10+ km) (5-10 km) (5-10 km) 770048 (5-10 km) (5-10 km) 1 (5-10 km) (5-10 km)


N N N N Y N N Y Y N 1 (5-10 km) (5-10 km) 770048 (10+ km) (10+ km) (10+ km) (5-10 km) (5-10 km)

N N N N Y N N N Y N (<5 km) (10+ km) (10+ km) 770044 (10+ km) (10+ km) 1 (10+ km) (10+ km)

N N N Y Y N N N Y N (5-10 km) (5-10 km) (10+ km) 770042 (10+ km) (10+ km) 1 (10+ km) (10+ km)

[3/3]

ENCLOSURE : VII

SUMMARY OF AMENITIES AVAILABLE (CENSUS 2011) IN VILLAGES WITHIN THE STUDY AREA OF EXPANSION OF INTEGRATED STEEL PLANT AT KAMANDA OF M/S RML

AMENITIES NOS. AMENITIES NOS. AMENITIES NOS.

EDUCATION FACILITIES DRINKING WATER FACILITY APPROACH TO VILLAGE

PPS (Pre-Primary School) 0 TWT (Tap Water-Treated) 0 NH (National Highway) 7

PS (Primary school) 38 TWUT (Tap Water Untreated) 4 SH (State Highway) 6

MS (Middle school) 16 CW (Covered Well) 0 MDR (Major District Road) 6

SS (Secondary school) 4 UW (Uncovered Well) 33 ODR (Other District Road) 6

SSS (Sr. Sec. School) 0 HP (Hand Pump) 35 BTPR (Black Topped (pucca) Road) 22

DCAS (Deg. College Arts & Science only) 0 TW/ BW (Tube Wells/Borehole) 0 GCR (Gravel (kuchha) Roads) 35

EC ( Engg. College) 0 S (Spring) 0 WBM (Water Bounded Macadam) 33

MC (Medicine College) 0 R/C (River/Canal) 5 AWR (All Weather Road) 35

MI (Management Institute) 0 T/P (Tank/Pond/Lake) 35 NWR/C (Navigable Waterways (River/Canal)) 18

P (Polytechnic) 0 WO (Others) 0 FP (Foot Path) 35

VTS/ITI (Vocational Trg School/ITI) 0

NFTC (Non Formal Training Centre) 0 COMMUNICATION SYSTEM BANKS AND COMMERCIAL SOCIETIES

SFD (School For Disabled) 0 PO (Post Office) 4 ATM (ATM) 0

EO (Others) 0 SPO (Sub Post Office) 1 CB (Commercial bank) 0

P&T (Post & Telegraph office) 0 COB (Co-operative bank) 0

MEDICAL FACILITIES PIN (Village PIN code) 35 ACS (Agricultural Crredit Societies) 0

CHC (Community Health Centres ) 0 T (Telephone (landline)) 15 SHG (Self-Help Group (SHG)) 31

PHC (Primary Health Centre) 0 PCO (Public Call Office/ Mobile PCO) 3 PDS (Public Distribution System (PDS)) 5

PHSC (Primary Health Sub-Centre) 8 MPC (Mobile phone coverage) 31 M/RM (Mandis/Regular Market) 0

MCWC (Maternity And Child Welfare Centre) 0 IC/CSC (Internet Cafes/Common Service Centre) 0 WH (Weekly Haat) 2

TBC (TB Clinic) 0 PCF (Private Courier Facility) 2 AMS (Agricultural Marketing Society) 1

HA (Hospital Allopathic) 0 NCICDS (Nutritional Centres-ICDS) 2

HAM (Hospiltal Alternative Medicine) 0 TRANSPORT SYSTEM NCAC (Nutritional Centres-Anganwadi Centre) 32

D (Dispensary) 1 PBS (Public Bus Service) 7 NCO (Nutritional Centres-Others) 1

VH (Veterinary Hospital) 0 PvtBS (Private Bus Service) 15 ASHA (ASHA) 35

MHC (Mobile Health Clinic) 0 RS (Railway station) 0 CC-TV (Community Centre with/without TV) 11

FWC (Family Welfare Centre) 0 MA (Auto/Modified Autos) 2

NGMF-OP (Non Govt. Med. facilities Out Patient) 1 Taxi (Taxi) 1 SPORTS AND ENTERTAINMENT

NGMF-IOP (Non Govt. Med. facilities In And Out Patient) 1 Van (Vans) 0 SF (Sports Field) 8

NGMF-C (Non Govt. Med. facilities Charitable) 1 T (Tractors) 5 SC/RC (Sports Club/Recreation Centre) 7

17 CPR-Man (Cycle-pulled Rickshaws (manual driven)) 35 C/VH (Cinema/Video Hall) 0

CPR-Mec (Cycle-pulled Rickshaws (machine driven)) 0 PL (Public Library) 0

26 CDA (Carts Drivens by Animals) 34 PRR (Public Reading Room) 0

S/R/FS (Sea/River/Ferry Service) 1 DNS (Daily Newspaper Supply) 35

23 APS (Assembly Polling Station) 30

POWER SUPPLY BDRO (Birth and Death Registration Office) 0

13 PSDU (Power Supply For Domestic Use) 32

PSIAU (Power Supply ForAgriculture Use) 30

NGMF-MS (Non Govt. Med. facilities Medicine Shop ) 25 PSCU (Power Supply For Commercial Use) 0

NGMF-O (Non Govt. Med. facilities Others) 0 PSALL (Power Supply For All Users) 29

NGMF-MBBS (Non Govt. Med. facilities Medical Prctitioner

with MBBS Degree )

NGMF-OD (Non Govt. Med. facilities Medical Prctitioner

with other Degree )

NGMF-ND (Non Govt. Med. facilities Medical Practitioner

with no Degree )

NGMF-TPFH (Non Govt. Med. facilities Traditional

Practitioner and Faith Healer )

ENCLOSURE : VII Contd..

SUMMARY OF AMENITIES AVAILABLE (CENSUS 2011) IN TOWNS WITHIN THE STUDY AREA OF EXPANSION OF INTEGRATED STEEL PLANT AT KAMANDA OF M/S RML

AMENITIES NOS. AMENITIES NOS. AMENITIES NOS.

EDUCATION Private-MS Office (Nos.) 0 WATER SUPPLY AND SANITATION

Govt. Primary School (Nos.) 3 Govt.-Desk Top Publishing (Nos.)) 0 Latrines-Pit (Nos.) 6

Private Primary School (Nos.) 0 Private-Desk Top Publishing (Nos.) 0 Latrines-Flush/Pour Flush (Nos.) 758

Govt. Middle School (Nos.) 1 Govt.-Vocational(Others) (Nos.)) 0 Latrines-Service (Nos.) 0

Private Middle School (Nos.) 0 Private-Vocational(Others) (Nos.) 0 Latrines-Others (Nos.) 8

Govt. Secondary School (Nos.) 1 Govt.-Non Formal Education (Nos.)) 0 Protected Water Supply Source-1 0

Private Secondary School (Nos.) 0 Private-Non Formal Education (Nos.) 0 Capacity Source-1 (KL) 0

Govt. Senior Secondary School (Nos.) 1 Govt.-Special School for Disabled (Nos.)) 0 Protected Water Supply Source-2 0

Private Senior Secondary School (Nos.) 0 Private-Special School for Disabled (Nos.) 0 Capacity Source-2 (KL) 0

Govt. Degree College-Art Only (Nos.) 0 Govt.-Others(Specify) (Nos.)) 0 Protected Water Supply Source-3 0

Private Degree College-Art Only (Nos.) 0 Private-Others(Specify) (Nos.) 0 Capacity Source-3 (KL) 0

Govt. Degree College-Science Only (Nos.) 0 MEDICAL Protected Water Supply Source-4 0

Private Degree College-Science Only (Nos.) 0 Hospital Allopathic (Nos.) 1 Capacity Source-4 (KL) 0

Govt. Degree College-Commerce Only (Nos.)) 0 Hospital Alternative Medicine (Nos.) 0 Protected Water Supply Source-5 0

Private Degree College-Commerce Only (Nos.) 0 Dispensary/Health Centre (Nos.) 0 Capacity Source-5 (KL) 0

Govt. Degree College-Art and Science Only (Nos.)) 0 Family Welfare Centre (Nos.) 0 TRANSPORT

Private Degree College-Art and Science Only (Nos.) 0 Maternity and Child Welfare Centre (Nos.) 0 Bus Route Road Distance (in kms.) 0

Govt. Degree College-Art and Commerce Only (Nos.)) 0 Maternity Home (Nos.) 0 Pucca Road Length (in kms.) 8.5

Private Degree College-Art and Commerce Only (Nos.) 0 Maternity Home Nearest facility Distance (in kms.) 35 Kutcha Road Length (in kms.) 8

Govt. Degree College-Art,Science and Commerce (Nos.)) 0 T.B. Hospital/ Clinic (Nos.) 1 ENTERTAINMENT AND COMMODITY

Private Degree College-Art,Science and Commerce (Nos.) 0 Nursing Home (Nos.) 0 Govt.-Stadium (Nos.)) 0

Govt. Degree College-Law (Nos.)) 0 Veterinary Hospital (Nos.) 1 Private-Stadium (Nos.) 0

Private Degree College-Law (Nos.) 0 Mobile Health Clinic (Nos.) 1 Govt.-Cinema Theatre (Nos.)) 0

Govt. Degree College-University (Nos.)) 0 Others (Nos.) 0 Private-Cinema Theatre (Nos.) 0

Private Degree College-University (Nos.) 0 Non-Government Out-Patient (Nos.) 0 Govt.-Auditorium/Community Hall (Nos.)) 0

Govt. Degree College-Others (Nos.)) 0 Non-Government In and Out Patient (Nos.) 0 Private-Auditorium/Community Hall (Nos.) 0

Private Degree College-Others (Nos.) 0 Non-Government Charitable-Hospital/Nursing Home (Nos.)0 Govt.-Public Library (Nos.)) 0

Govt.-Medical College (Nos.)) 0 Non-Government Medicine Shop (Nos.) 2 Private-Public Library (Nos.) 0

Private-Medical College (Nos.) 0 ELECTRICITY Govt.-Public Reading Room (Nos.)) 0

Govt.-Engineering College (Nos.)) 0 Electricity-Domestic Connection (Nos.) 1215 Private-Public Reading Room (Nos.) 0

Private-Engineering College (Nos.) 0 Electricity-Industrial Connection (Nos.) 0 Manufactured Commodity (First) 0

Govt.-Management Institute (Nos.)) 0 Electricity-Commercial Connection (Nos.) 25 Manufactured Commodity (Second) 0

Private-Management Institute (Nos.) 0 Electricity-Road Lighting Connection (Nos.) 2 Manufactured Commodity (Third) 0

Govt.-Polytechnic (Nos.)) 0 Electricity-Others Connection (Nos.) 0 HELP HOMES

Private-Polytechnic (Nos.) 0 FINANCIAL Govt.-Orphanage Home (Nos.)) 0

Govt.-Shorthand (Nos.)) 0 Nationalised Bank (Nos.) 2 Private-Orphanage Home (Nos.) 0

Private-Shorthand (Nos.) 0 Private Commercial Bank (Nos.) 0 Govt.-Working Women's Hostel (Nos.)) 0

Govt.-Typewriting (Nos.)) 0 Co-operative Bank (Nos.) 1 Private-Working Women's Hostel (Nos.) 0

Private-Typewriting (Nos.) 0 Agricultural Credit Society (Nos.) 1 Govt.-Old Age Home (Nos.)) 0

Govt.-Shorthand and Typewriting (Nos.)) 0 Non-Agricultural Credit Society (Nos.) 0 Private-Old Age Home (Nos.) 0

Private-Shorthand and Typewriting (Nos.) 0 FIRE FIGHTING

Govt.-MS Office (Nos.)) 0 Fire Fighting Service (Status A(1)/NA(2)) 2

ENCLOSURE : VIII

REVISED

PRE-FEASIBILITY REPORT

FFOORR

EEXXPPAANNSSIIOONN OOFF IINNTTEEGGRRAATTEEDD SSTTEEEELL PPLLAANNTT (AMENDMENT TO TOR VIDE MOEF&CC LETTER NO J-

11011/434/2009.IA.II(I) DATED 03.08.2016)

AATT

VVIILLLLAAGGEE KKAAMMAANNDDAA DDIISSTTRRIICCTT SSUUNNDDEERRGGAARRHH,, OODDIISSHHAA (0.60 MTPA to 0.75 MTPA STEEL)

NOVEMBER, 2016

(Issue 01, Rev. 0)

Submitted by:

RUNGTA MINES LIMTED RUNGTA HOUSE, CHAIBASA

JHARKHAND - 833201

ENCLOSURE : IX

ENCLOSURE : IX Contd..

Pre-feasibility Report – Expansion of Kamanda Steel Plant of M/s Rungta Mines Ltd. i

CONTENTS Sl. No. Description Page No. 1.0 Executive summary 1 2.0 Introduction 1

2.1 Identification of project and project proponent 1 2.2 Brief description of nature of the project 2 2.3 Need for the project and its importance to the country and or

region 2

2.4 Demand-supply gap 2 2.5 Imports vs. indigenous production 3 2.6 Export possibility 3 2.7 Domestic / export markets 3 2.8 Employment generation (direct and indirect) 3

3.0 Project description 3

3.1 Type of project including interlinked and interdependent projects

3

3.2 Location with coordinates 4 3.3 Details of alternate sites & environmental considerations 4 3.4 Size or magnitude of operation 5 3.5 Project description with process details 9 3.6 Raw material required along with estimated quantity, likely

source, marketing area of final product’s mode of transport of raw material and finished product

41

3.7 Resource optimization/recycling and reuse envisaged in the project

43

3.8 Availability of water its source, energy/ power requirement and source

44

3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their management /disposal

44

3.10 Schematic representations of the feasibility drawing which give information of EIA purpose

46

4.0 Site analysis 46

4.1 Connectivity 46 4.2 Land form, land use and land ownership 46


Pre-feasibility Report – Expansion of Kamanda Steel Plant of M/s Rungta Mines Ltd. ii

Sl. No. Description Page No.

4.3 Topography 46 4.4 Existing land use pattern 47 4.5 Existing infrastructure 47 4.6 Soil classification 47 4.7 Climatic data from secondary sources 47 4.8 Social infrastructure available 48

5.0 Planning brief 48

5.1 Planning concept 48 5.2 Population projection 49 5.3 Land use planning (break up along with green belt etc.) 49 5.4 Assessment of infrastructure demand (physical & social) 49 5.5 Amenities / facilities 50

6.0 Proposed infrastructure 50

6.1 Industrial area (processing area) 50 6.2 Residential area (non processing area) 50 6.3 Green belt 50 6.4 Social infrastructure 51 6.5 Connectivity 51 6.6 Drinking water management (source & supply of water) 51 6.7 Sewarage system & Industrial waste management 51 6.8 Solid waste management 51 6.9 Power requirement & supply / source 52

7.0 Rehabilitation and resettlement plan 52 8.0 Project schedule & cost estimates 53

8.1 Project schedule 53 8.2 Cost of the project 53

9.0 Analysis of proposal (final recommendations) 53


Pre-feasibility Report – Expansion of Kamanda Steel Plant of M/s Rungta Mines Ltd. iii

LIST OF TABLES

Table No. Description Page No.

1 Power supply position 2

2 Distance and direction (within 15 km) of water bodies, forests & mountains from project boundary

4

3 Comparison between wet & dry grinding 11

4 Specification of coke 28

5 Annual raw material requirement, and their sources for 0.75 MTPA steel plant

41

6 Final product for captive use out side sale 42

7 Solid waste generation (TPA) after expansion 44

8 Monthly average relative humidity at Keonjhar (1993-2004) 48

9 Break up of total plot area 49

10 Need evaluation for villages in and around mine area 50

11 CSR activities taken up by M/s Rungta Mines Limited 51


Pre-feasibility Report – Expansion of Kamanda Steel Plant of M/s Rungta Mines Ltd. iv

LIST OF FIGURES

Fig. No. Description Page No.

1 Process flow chart for sponge iron plant 54

2 Process flow sheet of power plant 55

3 Flow sheet of steel melting shop 56

4 Material & energy flow sheet for entire steel plant and ferro alloys plant

57


Pre-feasibility Report – Expansion of Kamanda Steel Plant of M/s Rungta Mines Ltd. 1

1.0 EXECUTIVE SUMMARY

Project name Expansion of Integrated Steel Plant (0.60 MTPA to 0.75 MTPA) at Kamanda, Sundergarh, Odisha by M/s Rungta Mines Limited.(seeking amendment to TOR)

Location Kamanda Total Area 154.489 ha (381.74 acres) Present Land status

Sl. No.

Details Area in Acres

Area in ha

1. Private Land purchased 111.08 44.954 2. Private land acquired

through IDCO 186.34 75.411

3. Govt. Land Acquired through IDCO

61.52 24.897

4. Balance Govt land under acquisition

22.80 9.227

Total 381.74 154.489

Product DRI, Pig Iron, Power Steel and Ferro alloys Rated capacity 1.2 MTPA DRI, 0.69 MTPA Pig iron, 198 MW Power and

0.75 MTPA Steel and 0.054 MTPA Ferro alloys. Working days 350 days Manpower 1635 Implementation Schedule

60 Months from date of environmental clearance

cost of the project Rs.2825.68 cores Topography Flat Water requirement 2385 cum/hr Source of water Karo River Power description Total power generation = 198 MW

Station Load + auxiliary = 21 MW Power for utilisation = 177 MW

Power source Captive Power Plant 2.0 INTRODUCTION 2.1 Identification of project and project proponent Rungta Mines Limited is operating 0.27 MTPA DRI, 0.20 MTPA Steel and

40 MW Power Plant at Kamanda, Sundergarh, Odisha by M/s Rungta Mines Limited. Environmental clearance for above existing plant is granted by MOEF vide letter No. EC letter no. J-11011/304/2007-IA.II (I) dated 12.12.2008

The company's vision & mission is to utilise its core values & strengths,

complemented with the vast experience gained, to help it keep pace with the changing times and respond to domestic & international market forces



by maintaining consistent quality & despatch schedules, making RML synonymous with reliability.

2.2 Brief description of nature of the project The nature of the project is ferrous metallurgical industries and fall under

the category of 1(d), 2 (a), 2 (b) and 3(a) under the category “A” of the schedule of EIA Notification, 2006.

2.3 Need for the project and its importance to the country and/or region Steel: India’s economic growth is contingent upon the growth of the Indian

Steel Industry. Consumption of steel is taken to be an indicator of economic development. While steel continues to have a strong hold in traditional sectors such as construction, housing and ground transportation, special steels are increasingly used in engineering industries such as power generation, petrochemicals and fertilizers.

Power: The DRI kiln operation produces substantial quantity of hot gases,

which can be utilised to power generation, further large quantity of waste produce char. So company will also install 87 MW WHRB + 111 MW AFBC based power plant. The generated power will meet the power requirement of Beneficiation, Pelletisation plant, Coal washery, DRI, Sinter plant, Blast Furnace, Coke oven plant, SMS, Billets/ slab / Bloom caster, Flat Round/ Wire rod/ Structural mill/ others, coal washery and Ferro Alloys Plant. Thus, power demand from the state grid will be not be there and will improve the power scenario locally as well as at state level.

2.4 Demand-supply gap Steel: The Indian Steel industry has entered into new development stage

from 2005-2006 riding high on the resurgent economy and rising demand of Steel. Rapid rise in production has resulted in India to become 5th largest producer of steel. It is estimated that, India’s Steel consumption will continue to grow at nearly 16% rate annually, fuelled by the demand of construction project. The National Steel Policy envisaged steel production to reach 110 million tonnes by 2020. So considering the huge demand of steel, this project is important for partially fulfilling of demand.

Power: Over the year electricity industry has made significant progress. It

may be seen that average gap between generation and demand in India is -1.9 %. Power supply positions are given Table 1.

TABLE 1

POWER SUPPLY POSITION Peak demand Peak met Deficit % Region

Jan 15 Jan 16 Jan 15 Jan 16 Dec 14 Dec 15 All Northern 42387 44124 40774 42019 -3.8 -4.6 Western 42247 45236 41553 45173 -1.6 -0.1



Peak demand Peak met Deficit % Region Jan 15 Jan 16 Jan 15 Jan 16 Dec 14 Dec 15

Southern 37004 37301 35446 36745 -4.2 -1.5 Eastern 15575 17343 15373 17198 -1.3 -0.8 North eastern

2455 2367 2202 2332 -1.03 -1.5

All India 139662 140782 135348 138075 -3.1 -1.9 Source: CEA

2.5 Imports vs. indigenous production Imports vs. indigenous production Steel: Imports from china had adversely affected the Indian Steel Market

and the policy change by Govt of India is now leading to recovery of the sector. There is no proposal for import of steel.

Power: There is no possibility of import and will be produced at plant site.

2.6 Export possibility Steel: First priority to meet domestic demand, should also take into account

the large export possibilities. Power: There is no possibility of export of power. 2.7 Domestic / Export markets 40 MW power plant (WHRB+AFBC) is under operation. Sponge Iron will be

used as raw material from within house for producing steel. The steel shall be sold in domestic market. Total power generated from the 198 MW captive power plant & 177 MW Power will be utilized in the Beneficiation, Pelletisation plant, Coal washery, DRI, Sinter plant, Blast Furnace, Coke oven plant, SMS, Billets/ slab / Bloom caster, Flat Round/ Wire rod/ Structural mill, and Ferro Alloys Plant etc.

2.8 Employment generation (Direct and Indirect) Total manpower currently is 500 and additional approximately 1635 will be

required during expansion. An equal number are expected to be in indirect employment. The estimate, however, does not cover the personnel for township, medical facilities, etc.

3.0 PROJECT DESCRIPTION 3.1 Type of project including interlinked and interdependent projects Nil.



3.2 Location with Coordinates District & State : Sundergarh, Odisha Village : Kamanda Latitude : 21°55’33’’ and 21°55’58’’ N Longitude : 85°13’16” and 85°13’52” E Location map showing general location, specific location and project

boundary enclosed as Enclosure II. 3.3 Details of Alternate Sites & Environmental Considerations No alternatives under consideration. The expansion project will be

incorporated within the existing plot (154.489 ha) of land to the existing plot. Environmental considerations: There are no National parks, Wildlife

Sanctuary, Biospheres reserves within 15 km radius. The nearest National Park is Simlipal at a distance of 97 km in E direction. The nearest Simlipal sanctuary at a distance of 130 km in E direction. There are several water bodies and forest present within the study area of the project. The distance to various water bodies, forest, etc are given in Table 2.

TABLE 2

DISTANCE AND DIRECTION (WITHIN 15 KM) OF WATER BODIES, FORESTS & MOUNTAINS FROM PROJECT BOUNDARY

Name Distance Direction Forests: Torha RF 1.8 km NW Karo RF 1.0 km N Uliburu RF 6.3 km NNE Mendhamaruni RF 3.2 km E Kathamala RF 0.5 km E RF near Bhabani 3.6 km SSE Sarkanda RF 5.5 km S Siddhamath RF 11.4 km NE Rakshi RF 12.7 km NW Khajurdihi RF 9.2 km SSE Rivers & Streams : Bacha nala 7.5 NW Boream nala 8.1 SE Erua nala 4.8 WNW Gera nala 5.4 W Geria nala 7.6 W Jakanal nala 8.6 SE Karo river 0.2 NE / E Khajurdihi nala 8.8 SE



Name Distance Direction Khuntachira nala 7.3 SE Kukarha 0.5 E Lekerapani nala 1.9 E Samij nala 2.4 NW Karo nala 0.01 E Sirki nala 9.3 WSW Suna nadi 8.6 E Teherai nala 6.5 SE

3.4 Size/Magnitude of operation Plant area: 154.489 ha Manufacturing facilities for which EC granted by MOEF&CC Government of

India vide letter no. J-11011/434/2009-IA.II (I) dated 02.02.2015 are:

Plant/ facility Phase-1 Phase-II Total DRI plant 0.585 MTPA 0.33 MTPA 0.915 MTPA Mini blast furnace 0.383 MTPA

2 X 262 m3 0.23 MTPA 1 X 260 m3

0.613 MTPA

Steel melting shop, Induction Furnace Ladle Furnace

0.20 MTPA 15T x 4 15T x 2

0.43 MTPA 15 T X 9 15 T X 5

0.63 MTPA

Billets/ slab/ bloom caster 0.20 MTPA 0.42 MTPA 0.62 MTPA WHR based CPP 42 MW 24 MW 66 MW Coal based CPP 25 MW 51 MW 76 MW Beneficiation Plant - 1.1 MTPA 1.1 MTPA Pelletisation Plant - 0.60 MTPA 0.60 MTPA Coal Washery - 0.92 MTPA 0.92 MTPA Sinter plant (24 Sq.m) - 0.24 MTPA 0.24 MTPA Coke Oven Plant - 0.14 MTPA

70,000 TPA each battery

0.14 MTPA

Flats/Round/Structural mill - 0.41 MTPA 0.41 MTPA Manufacturing facilities commissioned and under operation are:

Sl. No.

Facilities Product Capacity

1. DRI Plant (6X100 TPD+ 1X300 TPD) Sponge Iron 2,70, 000 TPA 2. Steel Melting Shop comprising: Induction Furnace (4X15 T) Billet caster (2x 2 Strand)

Steel billets 2,00,000 TPA

3. WHR based CPP and AFBC based CPP

Electricity 40 MW



Manufacturing facilities for which TOR letter for the ‘Expansion of Integrated Steel Plant from 0.60 MTPA to 0.70 MTPA was issued by MOEF&CC vide letter no J-11011/434/2009.IA.II(I) dated 03.08.2016 are given below :

Sl. No.

Facilities Present capacity as per

EC (TPA)

Additional proposed Capacity

(TPA)

Total capacity

(TPA) 1 Beneficiation Plant 1,100,000 1,00,000 1,200,000 2 Pellet Plant 600,000 0 600,000 3 Coal Washery 924,000 0 924,000

DRI Plant 6X100 TPD 180,000 77,400 257,400 1X300 TPD 90,000 38,700 128,700 3X350 TPD 315,000 100,800 415,800

4

2X500TPD 330,000 66,000 396,000 Sub total 915,000 282,900 1,197,900 5 Sinter Plant 240,000

(24 sq.m.) 175,800 415,800

(42 sq.m.) Mini Blast Furnace 2X262 CUM 382,520 49,780 432,300

6

1X260 CUM 227,500 0 227,500 Sub-total 610,020 49,780 659,800 7 Coke Oven (2 batteries

of 70,000 TPA) 140,000 0 140,000

SMS 4X15 Ton IF 2x15 Ton LRF

200,000 17,800 217,800 8

9 X15 Ton IF 5x15 T LRF

430,000 60,050 490,050

Sub total 630,000 77,850 707,850 9 Billet/Slab /Bloom

Caster

0.20 MTPA 200,000 15,000 215,000 0.42 MTPA 420,000 63,000 483,000 Sub total 620,000 78,000 698,000

10 Flat/Round/Wire Rod/ Structural Mill

410,000 0 410,000

Ferro Alloy Plant (9 MVA+18 MVA

0

Ferro Manganese Plant (9 MVA+18 MVA ) OR

- 9 MVA= 18,000 TPA 18 MVA=36,000 TPA

54,000

Silico Manganese Plant (9 MVA+18 MVA OR

- 9 MVA= 14,400 TPA 18 MVA=28,800TPA

43,200

Ferro Chrome Plant (9 MVA+18 MVA )OR

- 9 MVA= 14,400 TPA 18 MVA=28,800 TPA

43,200

Ferro Silicon Plant (9 MVA+18 MVA)

- 9 MVA= 6,400 TPA 18 MVA=12,800 TPA

19,200

11


- 88,320 88,320



Sl. No.

Facilities Present capacity as per

EC (TPA)

Additional proposed Capacity

(TPA)

Total capacity

(TPA) Briquette Plant for ferro manganese

- 111,360 111,360

Captive Power Plant 142 MW 14 MW 156 MW WHRB 66 MW 0 66 MW AFBC 76 MW 0 76 MW

12

WHRB from BF - 14 MW 14 MW This PFR is for the amended steel making capacity of 0.75 MTPA to modify

the above mentioned TOR granted by MOEF&CC on 03.08.2016. The modification in sub units and capacities vis-a-vis the TOR dt. 03.08.2016 is given in table below, in which changes are highlighted:

REVISED EXPANSION OF INTEGRATED STEEL PLANT FROM

0.60 MTPA TO 0.75 MTPA Sl. No.


02.02.2015 (TPA)


dated 03.08.2016


Additional Capacity

(TPA)

Total Capacity Additional capacity

(TPA)


expansion (TPA)



except 10 1 Beneficiation

Plant 1,100,000 1,00,000 1,200,000 No change 1,200,000

Pellet Plant-1 600,000 0 600,000 No change 600,000 Pellet plant-2 Nil Nil Nil 2X1,200,000+

10% up-gradation (240,000)

2,640,000 2

Sub Total 600,000 0 600,000 2,640,000 3,240,000 3 Coal

Washery 924,000 0 924,000 No change 924,000

DRI Plant 6X100 TPD 180,000 77,400 257,400 No change 257,400 1X300 TPD 90,000 38,700 128,700 No change 128,700 3X350 TPD 315,000 100,800 415,800 No change 415,800 2X500TPD 330,000 66,000 396,000 No change 396,000

4

Sub total 915,000 282,900 1,197,900 1,197,900 5 Sinter Plant 240,000

(24 sq.m.) 175,800 18 sqm

415,800 (42 sq.m.)

Capacity enhanced of

532,224 2x24 sqm



Sl. No.


02.02.2015 (TPA)


dated 03.08.2016


Additional Capacity

(TPA)


(TPA)


expansion (TPA)



except 10 existing 1X24

sq.m. by 26,112 +

Additional 1 X24 sq.m. of

266,112 Mini Blast Furnace

2X262 CUM 382,520 49,780 432,300 75,980 458,500 1X260 CUM 227,500 0 227,500 No change 227,500

6

Sub-total 610,020 49,780 659,800 686,000 7 Coke Oven (2

batteries of 70,000 TPA)

140,000 0 140,000 No change 140,000

SMS 4X15T IF 2x15T LRF

200,000 17,800 217,800 31,000 231,000

9 X15T IF 5x15T LRF

430,000 60,050 490,050 89,750 519,750

8

Sub total 630,000 77,850 707,850 120,750 750,750 Billet/ Slab/ Bloom Caster

0.20 MTPA 200,000 15,000 215,000 26,380 226,380 0.42 MTPA 420,000 63,000 483,000 replacing 0, as

replaced 0.20 MTPA Nil Nil Nil 226,380 226,380 0.22 MTPA Nil Nil Nil 282,975 282,975

9

Sub total 620,000 78,000 698,000 735,735 Flat/ Round/ Wire Rod/ Structural Mill/ others

410,000 0 410,000 10

Mill -1 4,10,000 4,10,000 217,325 217,325



Sl. No.


02.02.2015 (TPA)


dated 03.08.2016


Additional Capacity

(TPA)


(TPA)


expansion (TPA)



except 10 Mill-2 (no split 0 (no split 217,325 217,325 Mill -3 Specified) Specified) 271,656 271,656 Sub total 4,10,000 0 4,10,000 706,306 706,306

11 Ferro Alloy Plant (1x9 MVA+1x18 MVA)

0

Ferro Manganese OR

- 9 MVA= 18,000 18 MVA=36,000

9 MVA= 18,000 18 MVA=36,000

No change 54,000

Silico Manganese OR

- 9 MVA= 14,400 18 MVA=28,800

9 MVA= 14,400 18 MVA=28,800

No change 43,200

Ferro Chrome OR

- 9 MVA= 14,400 18 MVA=28,800

9 MVA= 14,400 18 MVA=28,800

No change 43,200

Ferro Silicon - 9 MVA= 6,400 18 MVA=12,800

9 MVA= 6,400 18 MVA=12,800

No change 19,200


- 88,320 88,320 No change 88,320


- 111,360 111,360 No change 111,360

Captive Power Plant

142 MW 14 MW 156 MW 56 MW 198 MW

WHRB 66 MW 14 80 MW 21 MW 87 MW

12

AFBC / CFBC 76 MW 0 76 MW 35 MW 111 MW 3.5 Project description with process details 3.5.1 Beneficiation Plant:

Present capacity as per EC Dated 02.02.2015 (TPA)

Additional capacity (TPA)

Total capacity after proposed expansion (TPA)

1,100,000 1,00,000 1,200,000



Product :

Product Description Unit Quantity Remarks Production/Generation TPA 720,000

Captive Consumption TPA 720,000 Used in Pellet Plant

Beneficiated Ore

Sale TPA NIL 3.5.1.1 Operating regime The plant will operate for 330 working days/year, three 8 hrs shift per day. 3.5.1.2 Process Beneficiation Plant mainly involves grinding of iron-ore fines and separation

of gangue to the extent possible within the required operational limits. Grinding of ore can be done in two alternatives:-

1) Wet Grinding & 2) Dry Grinding.

Later one is more expensive than the wet grinding system in terms of

processing & environmental measures. It is generally preferred in areas where there is a scarcity of water. In view of the requirement to transport beneficiated fines in the form of slurry, wet grinding system has been considered.

Beneficiation process mainly consists of

Primary Grinding Hydro cycloning Two stage spiral classification Single stage high gradient magnetic separation Regrinding & Thickening of concentrate received from both spirals &

magnetic separators. The thickened concentrate at approximately 65-66% solids by weight will be

pumped into the pellet plant by single stage pumping. Tailings from the beneficiation plant will be transported through pipeline & discharged into a tailing pond.

Primary grinding The main thrust in a beneficiation plant is given on adequate grinding which

is necessary to produce green balls with the required strength. Characteristic of ore fines govern the degree of fineness and it has been



observed that a Blaine index of 1850 to 2000 is necessary for production of competent green pellets.

Grinding of raw material is generally done by the following processes:-

a) Dry Grinding Process.

b) Wet Grinding Process.

a) Dry grinding process In case of dry grinding, the iron ore fines are dried in a separate dryer to

reduce moisture content to less than 1 %. The dried fines are fed to grinding mill. It is desirable to add flux materials and/or bentonite with the iron ore fines in case of dry grinding, which has an additional advantage of elimination of missing stage. Extensive dust separation and pollution control measures are to be adopted for dry grinding. Dry grinding can be carried out either in open circuit or in close circuit.

b) Wet grinding process

The iron ore fines are ground in wet grinding mill. The ground product in the

form of slurry is pumped to the slurry storage tank fitted with agitation mechanism. Water and finely ground raw materials are separated by pressure filters to obtain filter cakes. The moisture content of the filter cake is very important and depends on the size of the fine materials, nature of the ore, etc. wet grinding can also be done either in open circuit or in close circuit.

When wet grinding process is adopted, the preparation of flux materials and

binders (if bentonite is used) is done in dry state as elaborated earlier. Wet grinding process calls for thorough mixing of raw materials including fluxes and binders, and separate grinding equipment is to be installed. The advantage and disadvantages of wet grinding and dry grinding have been indicated in the comparison Table.

In the present context, for production of DR grade pellets, further up-

gradation or higher degree of beneficiation of lower grade ore fines is necessary. The wet beneficiation process is more efficient. Wet grinding is necessary when iron ore fines are transported to pellet plant site in the form of slurry. The comparison between wet & dry grinding is given in Table 3.

TABLE 3

COMPARISON BETWEEN WET & DRY GRINDING Wet grinding Dry grinding

Lower capital costs Lower wear on mill balls Advantages

Lower energy requirement

No need for thickening & filtering



Wet grinding Dry grinding

Less Pollution Wider selection of materials for processing

Low water requirement

Low binder requirement

Difficult to filter materials are excluded

More Pollution

High wear on mill balls High cost of drying

Disadvantages

Moisture level control is necessary

Considerable noise level

Technological Facilities Iron-ore fines from the mine will be transported by trucks. The fines will be

stockpiled in the raw material yard from where it can be reclaimed by pay loaders & tippers. Iron-ore fines will be reclaimed through pay-loaders, tippers & transported to silos. The silos shall be filled with the help of a shuttle conveyor. Vibrating feeders are provided below each of the silo. The output from the vibro feeder will feed the grinding mill feed conveyors.

The mill feed conveyors will feed primary ball mill. The primary ball mill’s

discharge is collected in pump sump for pumping to hydro Cyclone clusters. The overflow from the cyclone is sent to slime thickener. The cyclone under flow is fed to a bank of rougher spirals. The concentrate from the rougher spirals will be processed in cleaner spirals. The tailings from the rougher & cleaner spirals are fed to intermediate slime thickener. The concentrate from cleaner spiral are pumped to secondary hydro cyclone. The under flow from cyclone are fed to regrinding mills for further grinding to required product size whereas, the overflow from the cyclone is fed to concentrate thickener. The under flow from the concentrate thickener is pumped to slurry storage tanks and from there it is pumped into the pellet plant. The under flow from intermediate slime thickener is pumped to a linear screen. The over size from the screen is pumped to cone splitter preceding the primary grinding mill. The under flow of cone splitter is fed to grinding mill and overflow is directly sent to pump sump of primary grinding mill.

The under size from the screens is fed to High Gradient Magnetic Separator

(HGMS) for recovery of concentrate from slimes. The concentrate form HGMS is further ground in the same regrinding mill, which is close circulated with secondary hydro cyclone. The concentrate over flow from hydro cyclone is thickened in concentrate thickener before pumping to slurry storage tanks provided with agitators. The tailing from HGMS is fed to a tailing thickener. The tailing thickener underflow is pumped to a tailing dam in the beneficiation plant site. The overflow from the tailing thickener is sent to process water tank for re-circulation in the process. The major quantity of water of tailing dam shall be lost in evaporation and seepage.



One E.O.T. crane has been envisaged in grinding bay. Another E.O.T. crane of 12 T capacity has been envisaged in HGMS bay.

Major units/facilities provided within the battery limits of the beneficiation

plant are as under:

Iron ore bin building and iron ore grinding building with structural and aluminum sheeting

Beneficiation Unit – The complete unit involves major process equipment like Ball Mills, Hydro cyclones, Spiral Banks and HGMS

For the decantation of the slurry – Concentrate Thickener intermediate Slimes Thickener and Tailing Thickener, pumps and pump house etc.

E.O.T. cranes and hoists

Flocculent preparation and dosing system

The plant piping involves rubber lining.

Tailing discharge after the complete Beneficiation Process through 8” Dia rubber lined pipeline to a tailing pond

Instrumentation works for piping and in Beneficiation units. Distributed Control System (DCS) for automated control over the process parameters

Compressed air facilities.

Power supply and distribution, illumination, water storage and distribution, telecommunication, fire detection and protection, drainage, boundary wall and other utilities.

Ore fines receipt & storage of required capacity

Fines sampling system 3.5.2 Pelletisation Plant


02.02.2015 (TPA)


Total capacity after proposed expansion

(TPA) Pellet Plant-1 600,000 No change 600,000 Pellet plant-2 Nil 2X1,200,000+

10% upgradation (240,000)

2,640,000

Sub Total 600,000 2,640,000 3,240,000



3.5.2.1 Process design The proposed pellet plant is designed to produce 600,000 TPA (100 TPH) +

1.2 X 2 + 10 % upgradation = 2.64 MTPA pellets suitable for use in direct reduction process using beneficiated Iron-ore concentrate as feed material. The various steps involved in the pelletisation process are:-

Feed Preparation Green Ball Formation Pellet Induration Product Despatch

There are two established process for pelletisation of iron-ore such as:-

i. Straight Grate Process- Developed by M/s Lurgi (now Outokumpu) of Germany. In this process, drying, preheating, induration & cooling of pellets take place on the same strand.

ii. Grate Kiln Process- Developed by M/s Allis Chalmers (now Metso

Minerals) of USA. In this process pellets are dried & preheated on a grate, indurated in a rotary kiln and cooled in a circular cooler.

However, based on the techno-economic analysis and operating experience

of existing pellet plants, Straight Grate Kiln process has been selected for the proposed plant by M/s Rungta Mines Ltd.

Quality of Raw Material:

Parameter Iron-ore Concentrate

Coke Breeze

Bentonite Limestone

Fe (t) 63-64%

Fe2O3 92.14 %

SiO2 2.5 % 38 % 4 %

Al2O3 2.5 % 38 % 1.2 %

CaO 6.7 % 48 %

MgO 0.8 % 2.5 %

LOI 2 % 7.5 % 44 %

Others 0.86 % 9 % 0.3 %

Fixed Carbon 78.7%

Ash 20.2%

Sulpur 1.07%

Phosphorous 0.03%



Quality of Product: a. Chemical Properties:

Parameter - Specification Fe (t) - 66.50 % min SiO2 + Al2 O3 - 3.10 % max Na2O - 0.05 % max K2O - 0.05 % max TiO2 - 0.10 % max Mn - 0.10 % max P - 0.04 % max S - 0.02 % max Basicity Cao/SiO2 - 0.5 Moisture (Free moisture Loss at 105 degree centigrade)

- 4 % max (fair season), 6 % max (monsoon)

b. Physical Properties:

Screen Analysis - Specification + 19 mm - 5 % max - 16 mm, + 9mm - 85 % min - 9 mm, + 5 mm - 5 % min - 5 mm - 3 % max Tumbler test (ASTM) - Tumbler index (+6.36 mm) 94 % min

c. Metallurgical Properties:

Parameter - Specification Swelling (JIS) - 20% max. Compression strength - 250 Kg/pellet min Porosity - 18 25% min Reducibility (JIS) - 70% min

d. Various Process / Systems selected for Pelletisation are:-

i. Filtration of Slurry - Pressure Filters ii. Balling - Disc Pelletisers iii. Induration - Grate Kiln iv. Additive Grinding System - Ball Mill for Coke Breeze

& Limestone; Vertical Roller Mill for Bentonite.



3.5.2.2 Main plant facilities have been described below

Raw material receipt and handling, The ore fines storage and handling system is housed inside the RMHS.

Railways wagons / trucks carrying the ore fines are tippled in the wagon tipplers and stockpiled in the bed by means of slewing boom stacker. The stock pile would have capacity to store 20 days requirement of the pellet plant. The ore from the stockpile is reclaimed through a reclaimer and transported to the ore silos at the grinding unit. Additives like limestone and bentonite received into the plant through road transport, stocked on ground, unloaded in the underground hoppers and conveyed to storage bins of the additive grinding unit. Coal also received by road is conveyed to separate silos near the ore grinding unit. Coal is ground along with ore in the ball mills.

Wet grinding of iron ore fines in Ball Mills

Weigh feeders under ore silos will collect feed to the ball mills. The grinding

circuit will be installed in a close circuit with Cyclones. Facility exists to operate the mills in open circuit. Each feeder will be equipped with a scale. Coal is drawn from the coal silos through weigh feeder at a rate proportional to the ore. For adjusting the slurry density, radio-active density gauges are installed in each slurry line controlling the water addition to the feed pipes of each slurry pump. The mills will have a mixed charge of 40 and 80 mm dia grinding balls at a nominal 35% volumetric loading. The mills will be operated to produce a nominal 325 mesh grinding suitable for pelletisation.

Thickening & Filtration The product from grinding mills at nominal solid percentage of 28 to 32 will

be fed into a Gravity thickener. The thickener slurry with minimum 65% solids is pumped to slurry storage tanks. Slurry is pumped from these tanks to distributors arranged above the filters. Excess slurry from the distributors flows to thickener.

On the disc filters the slurry is dewatered to a moisture content of approx. 9

to 9.5%. For producing the necessary vacuum, each filter is equipped with a vacuum pump, sucking a mixture of air and filtrate water from the filters via a double stage vacuum receiver system, where air and filtrate water are separated. The filter cake from the disc filters is blown off by compressed air is collected on a belt conveyor and fed into an intermediate bin.

Additive Grinding

In this section two bins for ground Limestone and the other for bentonite are

also provided. Proportioning of Limestone and Bentonite to the required quantity of filter cake according to a pre-selected value is performed by weigh feeders which are installed underneath the bins for filter cake, Limestone and Bentonite.



The grinding plant for Limestone and Bentonite consists of roller mill. It is equipped with a hot gas generator for the simultaneous drying of the ground product, bag filter and fan. Ground products are stored in silos and transported pneumatically to Mixing and Balling building. Filter cake, Limestone and Bentonite are mixed in Lodge mixer enabling and intensive mixing of above materials.

Balling

The ground iron ore fines/ concentrates along with additives and binder are

converted to green pellets after through mixing. The degree of fineness of input materials, critical amount of water, amount of binder in the mix, etc. are most important for production of green pellets with adequate compression strength and size. The strength of green pellets result predominantly from capillary forces caused by wetting with water and mechanical consolidation, effected by rolling action. The critical amount of water varies from 8 to 13% depending upon the nature of feed material.

The types of equipment used in commercial plants for production of green

pellets are drum, disc and cone pelletisers. Recently, granulation of feed materials by using vibration granulation equipment and high agitating mixer are being reported to be developed and commercially used. However, majority of the pellet plants world wide uses either drum pelletiser or disc pelletisers. Brief descriptions of these two types of pelletisers are given below and selection of the most suitable pelletiser based on advantages, disadvantages, extent of commercial use, etc. has been done as follows:

a) Drum Pelletiser Drum pelletisers are the oldest equipment for production of green pellets. All

pelletizing plants operated on an industrial scale in USA and in Sweden were exclusively equipped with drums upto about 1956. Owing to the fact that their component parts have been known and proved for many years, as well as to their easy operational control under relevant operating conditions, they are now a days also used frequently in pelletising plants. The drum consists of a slightly inclined cylinder open at both ends, occasionally with a low retention ring or cone at the feed end in order to prevent backward flow of pellet feed. For the improvement of the adhesive strength and roughness, the metallic smooth inner wall is coated with a layer of moist fines and its thickness is controlled and limited by scrapers. These scrapers are stationary or rotating and arranged in parallel to the drum axis. In modern plant, so called rotating spiral scrapers are used which not only limit the bed depth but also impart a higher frictional resistance to the inner face. Due to the mode of operation, the drum has practically no sorting effect. The drum discharge has to be screened and the green pellets of desired size are separated. The product oversize after crushing combined with under size and fresh feed material and are jointly charged to the drum. The small pellets contained in the under size serve, during their repeated passage through the drum, as seeds for the formation of properly sized pellets.



b) Disc Pelletiser Disc pelletisers were already used for balling in cement raw mill and in the

fertilizer industry even before its application for iron ore pelletisation was investigated during 1949-50.

The disc pelletiser consists of a concentrically rotating inclined disc

composed by a circular plain bottom area with peripheral skirt. To ensure sufficient frictional resistance and a good lifting effect for the pellet feed, a moist ore bed of about 3-10 cm thickness is layered on the bottom and is controlled by scrapers. Different designs have been developed such as stationary and oscillating scrapers or rotating spirals. Attempts have been made to utilize a maximum part of the disc area for green ball formation has been achieved after extensive research and development. Since during ball formation a classification occurs unto the discharge of pellet of desired size, the quantity of necessary pellet feed corresponds to the amount of pellets discharged. If nevertheless, small amount of undersize develop, which mostly occurs during transportation, these are separated by roller screen and recycled. The size of the ball in a disc pelletiser is easily controlled by adjusting the moisture content of raw feed, angle of inclination of disc, rotational speed of disc, etc.

However, based on the techno-economic analysis and operating experience

of existing pellet plants, Straight Grate Kiln process has been selected for the proposed plant by M/s Rungta Mines Ltd.

3.5.3 Coal Washery:

Present capacity as per EC Dated 02.02.2015 (TPA)


Total capacity (TPA)

924,000 No change 924,000 Coal is one of the most important raw materials for a coal based DRI plant.

It acts as a reductant for reducing iron ore to produce sponge iron and also to preheat the charge mix to the reaction temperature of 1000°C. The ROM coal needs crushing and washing to reduce the ash content. The coal washery will consist of a coal crushing and screening station and a coal washery.

It is therefore proposed to install a suitable Three-Product Coal Washery (Dense Media Cyclone)

The capacity of Coal Washery has been derived on the basis of

requirement. ROM coal assuming 50 % washery yield = 924,000 TPA Washery operating hrs per annum, = 924,000/150 = 6160 hours Assuming 320 days availability, washery operating hours / day = 19.25

hours The usable ROM coal will be 924,000 T containing: -



a. Clean Coal (50 %) – 462,000 T with 27% ash

b. Middlings (42.5%) – 392,700 TPA with 56% ash (For Power Plant)

c. Rejects (7.5 %) – 69,300 TPA with 80% ash 3.5.3.1 Process Description The coal washery has been designed to wash the coal in heavy media

circuit to produce clean coal with 25% ash and middling. The process consists of crushing of the ROM coal in a combination of rotary breaker and 2 stages roll crushers. The crushed coal is then washed in the heavy media cyclone to produce clean coal and middling. The heavy media preparation / regeneration unit for maintaining the required density in the heavy media circuit is also included in the plant design. The effluent from various points in the circuit is collected and treated in the thickener. The thickened tailing is envisaged to be dewatered in a belt press while the clarified water is recycled back in the process circuit. The coal washery can be divided in the following sections:

Primary Coal Preparation Circuit A rotary breaker, which has a top size capacity of 800 mm, is used to

deshale the ROM coal. This rotary breaker is provided with 250-mm openings, which gives a positive control on the top size of feed to the plant. Following this, the coal size is reduced to 20 mm in 2 stage crushing. A primary screen is first used to remove the –20 mm material already present in the coal following which is fed to a roll crusher. The product from the roll crusher is then fed to a secondary screen separating –20 mm material. Oversize from the secondary screen feeds the secondary crusher, which operates in closed circuit with the secondary screen. –20 mm from the screens is stored in a stockpile and feeders below the stockpile are used to feed to the washery building.

Main Washery Building The main washery building houses the coal beneficiation circuit and is

comprised of the following modules. One stream of washery having a nominal capacity of 200 tph.

Desliming Module The ROM coal, crushed to –20mm size is drawn from the feed stockpile

through conveyor. The reclaimed material is transferred through to discharge the material on the desliming screen. The feed shall be deslimed at 1 mm (alternatively 0.5 mm). Water shall be sprayed on the desliming screen to enhance the desliming by removing the attached fines on the bigger particles. The coal feed is treated in circuit of (1 X 175) TPH capacity. The screen overflow shall be collected in a fine coal sump and pumped to fine coal thickener for recovery of the coal fines.



The deslimed coal shall be collected in Heavy Media sump for further treatment in the H.M. Washing circuit.

H.M. Washing Module The oversize of the desliming screen is collected in the Heavy Media Sump

where Heavy Media (finely ground magnetite) is mixed so as to maintain the desired pulp density based on the desired product quality. The coal-media slurry is then pumped to the Heavy Media Cyclones. The clean coal, being lighter shall report as the cyclone overflow. While the heavier fraction shall report to the cyclone underflow as rejects. The clean coal and the rejects shall be dewatered and rinsed with water on the separate D & R screens.

The D & R screens for clean coal are provided with 2 decks to separate at 5

mm. This enables in segregation of the clean coal into –20+5 mm product and –5mm product.

The products from D & R screens still contains about 20-25% moisture,

which is further dewatered in the vibrating screen centrifuges (1no.on each size fraction of clean coal & 2 nos. for rejects line). The final products from the centrifuges are then transferred to rejects stockpile and clean coal storage bins. The clean coal and rejects shall be reclaimed from the storage through the sector gate and transported to desired destination through loaders / trucks.

Fine Coal Module The fine coal –1mm (alternatively 0.5 mm) fraction from the desliming

screen, rejects D & R screen, clean coal D & R screen and Centrifuges (clean coal and rejects) shall be collected in the fine coal sump. Then it is pumped to the fine coal thickener for thickening before further dewatering, as the solid concentration in the slurry is very low. The thickened slurry shall be reclaimed from the conical bottom of the thickener and pumped to a Belt press for further dewatering. The dry coal from the Belt Press shall be discharged on the fines conveyor. The clarified water from the thickener shall be collected in the thickener of sump and pumped back into the circuit for reuse in the process.

Media Preparation & Regeneration Module The finely powdered magnetite feed (90% passing 45 microns), shall be

stored in Magnetic Media feed bin. The media shall be reclaimed by weigh feeder via Rake & pinion gate and mixed with water in the feeding launders and added to the over-dense media sump as a make-up to maintaining the density.

The dilute media from the D & R screens from the washing is collected in

the dilute media sump. The dilute media contains finely ground magnetite and coal fine, which comes from rinsing the clean coal/rejects and a good quality of wash water. The dilute media is first pumped to a densifying



cyclone. The thickened u/f from the cyclone is sent to the over dense media tank while the dilute overflow is sent to the magnetic separators for reclamation of magnetite. The magnetic fraction is collected in the over dense media sump while the non-magnetic fraction is used for rinsing in the D & R screens.

Density Control System The objective of the control system for a heavy media cyclone is to

maximise the clean coal yield subject to a specific ash constraint and to reduce product ash variation to a minimum. Full advantage of the dense media cyclone’s inherently sharp separation can be obtained only if some means is provided for maintaining the specific gravity of the medium at a point in the circuit the over-dense media (discharge line) feed to heavy media sump.

The application of a nuclear density gauge is to monitor the density of the

over dense media tank. Any deviation from the desired specific gravity causes an error signal to be sent to the indicator / controller. If the medium specific gravity is too low, the controller sends a signal to the fresh magnetic feed, causing more medium to be directed to the over-dense media sump. If the medium specific gravity increases, the controller either activates a water valve that, in turn, simply adds water to the over-dense media discharge line.

3.5.4 Sponge Iron Plant:

Facility Present capacity as per EC Dated

02.02.2015 (TPA)



(TPA) DRI Plant 6X100 TPD 180,000 77,400 257,400 1X300 TPD 90,000 38,700 128,700 3X350 TPD 315,000 100,800 415,800 2X500TPD 330,000 66,000 396,000

Sub total 915,000 282,900 1,197,900 3.5.4.1 Process Iron Ore (Pellets) is reduced by heating with solid carbonaceous material,

such as coal, in a Rotary Kiln to temperature of about 1000°C. If low volatile coal is used as the reductant, the kiln is fired by gas or oil. The use of high volatile coal, however, eliminates the need for this additional source of heat. After reduction, products are cooled in a drum type rotary cooler and then separated into Sponge Iron and Char by magnetic separation. High degree of reduction and thermal efficiency can be obtained by controlling process parameters such as reduction temperature, rate of feed, size of feed, grade of feed, etc. The superior quality of coal is used, which reduced the



consumption of coal i.e. reduced from 1.5 T/T of DRI to 0.85 T/T of DRI. When the coal consumption reduced, we feed more Iron Ore in the Kiln for reduction & producing more DRI. Which results, the Kiln of 100 & 300 TPD will have 30 % increased production; kiln of 350 & 500 TPD kiln will have 20 & generation. In this practice the char generation also decreased from 25% to 18%.

The basic reactions in this process are as given below:

C + O2 = CO2 CO2 + C = 2CO Fe2O3 + CO = Fe3O4 + CO2 Fe3O4 + CO = FeO + CO2 FeO + CO = Fe + CO2

The reduced iron is discharged into coolers where it is cooled by spraying

water and conveyed through conveyors for magnetic separation and subsequent storage/ consumption.

3.5.4.2 Raw Material Handling System Main Raw Materials Iron Ore, Coal & Dolomite are being/will fed to the

ground hoppers with the help of Pay loaders and Tippers and carried by belt conveyors to the Crusher House. Screened and Crushed Material will be carried out by belt Conveyers to the stock house, having 5 days bins. The main raw material handling system consists of iron ore crusher, vibrating screen and conveyor belts for preparation of raw material as mentioned above.

3.5.4.3 Raw Material Feed System The stored Raw Material are calibrated by Weigh Feeders separately for

Iron Ore, Feed coal, Lump Coal, Injection Coal and Dolomite and fed to the Kiln through a Rotary Airlock Feeder. The feed mix will be fed through feed tube, which is being sealed for leakage of gases with a sealing air fan, which creates a positive pressure to avoid the gas escape. The Injection Coal system injects coal at the discharge end of rotary kiln to avoid Coal starvation with 1 bar pressure at which leakages are not possible. There is a burner system, which is being used for initial heating of the Kiln up to 400C. The calibrated quantity of combustion air is also fed through the same opening.

3.5.4.4 Main Processing System - Kiln The main reduction process occurs in a Rotary Kiln of 80 m length and 4.80

m diameter made by boiler quality plate. The drive unit consists of 2 nos. main drive gearbox and 1 no. aux gearbox. The kiln is supported by four nos. tyres and 08 nos. support rollers, one girth gear and two pinions. Calibrated quantity of air is fed to the kiln by shell air fans mounted on the



kiln shell. The iron ore is reduced by the carbon monoxide generated by burning coal.

The product of kiln is taken to a sealed rotary cooler where the product is

cooled by indirect water spray, which is discharged to a conveyor at about 90C.

The cooler discharge is also sealed with a collecting hopper. There are 4

nos. slip seals at Kiln Inlet, Kiln Outlet, Cooler Inlet & Cooler Outlet being made up of Ni hard steel. The seals are also being lubricated to avoid false air entry into the kiln and gas leakage from the kiln. At inlet side of the Kiln a back flow chute is made which is sealed with a Double Pendulum Flap Gate Valve.

3.5.4.5 Cooling System The material is discharged in the Rotary Cooler at a temperature of about

700ºC, which is cooled up to 90o C. The Drive Unit consists of one Main gearbox and one Auxiliary gearbox. The cooler is supported by Two Tyres and four support rollers. This is being cooled by indirect circulating cooling water system, the hot water being collected and passed through the cooling tower. The evaporation loss is made up with makeup water.

3.5.4.6 Product Separation System The Cooler Discharge material consists of Sponge Iron lumps, fines and

ash of coal (char), and is taken to a vibratory screen and two nos. magnetic separators by belt conveyor. The Magnetic and Non Magnetic material are separated here and stored in fully closed hoppers. The Product House consists of silo for sponge iron lumps, sponge iron fines and char. The char shall be used as fuel in the proposed Power Plant.

3.5.4.7 Flue Gas Cleaning and Pollution Control The flue gas coming out from the Rotary Kiln is passed through a Dust

Settling Chamber, in which the heavier dust is settled down. The bottom of the dust settling chamber is immersed in the wet scrapper water which is working as the sealing to avoid the gas leakage and false air entry. The gas next passes through the After Burning Chamber (A.B.C.) in which the carbon monoxide and un-burnt carbon are burnt completely.

The flue gas is taken to the Waste Heat Recovery Boiler (WHRB), where

the recoverable heat is utilized for generation of high pressure steam. The flue gas is next passed through an electro static precipitator (ESP), where the gas is cleaned up to maximum level. The clean gas passes to the atmosphere through the Chimney with the emission level of less than 100 mg/Nm3.

The boiler bottom hoppers and E.S.P. hoppers are provided with a dense

phase ash handling system. The dust collected from these hoppers is sent



to an ash silo by pneumatic conveying system. Finally the stored dust in the ash silo is taken to the solid waste disposal site for storage and final disposal to brick manufacturing plants/cement plants.

3.5.4.8 Requirement of Raw Materials The main raw materials for sponge iron production are iron ore, coal, and

dolomite. 3.5.5 Sinter Plant:

Present capacity as per EC dated 02.02.2015

(TPA)



(TPA) 240,000

(24 sq.m.) Capacity enhanced of existing 1X24 sq.m. by

26,112 + Additional 1 X24 sq.m. of 266,112

532,224 2x24 sqm

Two sinter plants will be installed to produce 0.532 MTPA sinter, which will

be adequate for 70% Sinter feed in Blast Furnace. In order to increase the productivity of Blast Furnace, Rungta Mines Ltd proposes to charge 70 % Sinter in the Charge Mix, Balance being Lump Ore. The productivity of Blast Furnace will increase from 2 to 2.5 T/CUM per day. Comparison of sectioned TOR and proposed amendment unit are given below:

Description Units Values Up-gradation

Unit Capacity SQM 42 Split into two of 24 SQM

Unit Quantity Nos. 1 2 No. of working Days/ Year

Days 330 330

No. of working Hours / Day

Hours 24 24

Production per SQM Ton /SQM 1.25 1.4 Total Capacity (Based on Output)

TPA 415,800 532,224

Say MTPA 0.415 0.532 Sintering is an agglomeration process through incipient fusion at 1050

degree C brought in to the hearth bed carrying Iron Ore Fines / Blue Dust, Coke Breeze (available surplus from Coke Breeze and Fluxes). It is possible to make any grade of Sinter namely basic Super fluxed Sinter etc.depending upon the quality requirement of raw materials charged into Blast Furnace.



3.5.6 Mini Blast Furnace Mini Blast Furnace of capacity 2x262 CUM (with upgradation of 13%

production) + 1x260 CUM will be installed. The Blast furnace charge mix will comprise of 70% Sinter & 30% Blast Furnace Grade Iron-Ore in the charge mix. The productivity of Blast Furnace will increase from 2.0 to 2.5 T/M3 per day. The Hot Metal produced in MBF will be cast to Pig

Facility Present capacity as

per EC dated 02.02.2015 (TPA)



(TPA) 2X262 CUM 382,520 75,980 458,500 1X260 CUM 227,500 No change 227,500

Sub-total 610,020 75,980 686,000

The purpose of a blast furnace is to chemically reduce and physically convert iron oxides into liquid iron called "hot metal". The blast furnace is a huge, steel stack lined with refractory brick, where iron ore, coke and limestone are dumped into the top, and preheated air is blown into the bottom. The raw materials require 6 to 8 hours to descend to the bottom of the furnace where they become the final product of liquid slag and liquid iron. These liquid products are drained from the furnace at regular intervals. The hot air that was blown into the bottom of the furnace ascends to the top in 6 to 8 seconds after going through numerous chemical reactions. The air is blown through tuyers in the bottom portion and liquid iron is tapped from the tap hole. The blast furnace complex will consist of two blast furnaces and two pig casting machines along with the requisite support facilities, namely the stock house, coal injection system, cast house, gas cleaning plant, de-dusting facilities, slag granulation facilities, etc.

The blast furnace flue gas is passed through Gas Cleaning Plant. A part of

the clean gas is utilized for stove of blast furnace and balance clean gas is used as a fuel in the boiler.

3.5.7 Coke Oven Plant (2 X batteries of 70,000 TPA)

Present capacity as per EC dated 02.02.2015 (TPA)


Total capacity after proposed expansion (TPA)

140,000 No change 140,000 3.5.7.1 Non-recovery type coke ovens The proposed non-recovery coke ovens have been specially developed

based on the imported coking coal with a volatile matter content in the range of 20%-24%. The coke yield will be slightly lower than the yield from the coal of Jharia coal field due to higher loss of volatile matter. Moisture control of coal is important as it has direct bearing on the carbonization rate & bulk density of coal.



Non-recovery coke ovens are capable of producing coke of large size, strong, dense & abrasion resistant. The coarse mosaic micro-structure, low porosity during carbonization and development of minor crack result in low reactivity, strength in high temperature, stability and superior post reaction strength. The ovens are unique in that, no external heat source is required. All the energy in carbonization is supplied by burning the gaseous volatile products released from the coal charge during carbonization. The required air is drained into each oven through various inlets provided at various stage located in both above the arch and sole levels.

The heat, generated by the combustion of the volatile matter produces high

temperature zone in the free space above the coal charge. This heat radiates back into the coal charge and comes downward for carbonization of the coal mass. The products of combustion are drawn through the various points in the oven arch and subsequently passes through side wall off takes flues into a series of sole flues located below the oven floor.

As the hot products of combustion passes through the sole flues, they

liberate some of their heat upwards which has resulted in continuous process of carbonization of the coal mass in the oven. The gas enters into the sole flues through connecting ducts and passes along the common waste gas tunnel to the discharge stack.

Hence carbonization takes place by the application of heat from above

sides and below the charge. Temperature at the point where burning gases are drawn into the side off take ports are of the order of 1200oC to 1250oC. Temperature at the base of the sole flues is around 850oC to 900oC. The available temperature at the entry of the main stack has been observed as 750oC to 800oC.

Advantages of non-recovery type coke oven

- Low capital cost.

- Low revenue cost in regard to operating & maintenance of oven.

- Low cost per tonne of coke / conversion.

- High coke yield.

- Any oven in a battery may be isolated and cooled down for repair any time during running condition without any considerable effect on oven life.

- No effluent, only emission being fully burnt clean flue gas resulting to minimal environmental impact.

- Ovens of non-recovery type are being operated under suction to avoid any explosion during operation to prevent pollution.

- Extensive flue system ensures complete combustion of all hydrocarbons leaving a clean Stack gas within permissible limit.



Manufacturing process Raw coal is crushed in a crusher into powdered form and charged in the

oven for the purpose of carbonization. In the process the volatile matter in the raw coal get released in the form of gas and is burnt in the oven as well as in the flues and after the completion of the carbonization process, within the duration of 36 to 38 hours, the raw coal get converted in the from of coke. The cake of coke is being pushed out from the oven and quenched it by water. Thus coke is ready for dispatch.

The duration of coking depends upon the quality & quantity of raw coal fed

into the oven, charge height and thermal condition of the oven. A proper thermal regime will therefore have to be maintained for optimum result and consistency in the charging cycle time. Coking coal is stacked, either manually or by the pay loader as required in to a ground bunker and is reclaimed daily from the bottom of the bunker by a belt conveyor for feeding the crusher. The provision of a electromagnet has been proposed to remove tramp iron from the raw coal. Crushed coal from crusher is fed into a belt conveyor to carry coal up to the overhead bunker which acts as overhead storage to feed charging car as & when required.

Charging car carries the crushed coal over the oven to be changed and coal

is discharged into the oven through the charging hole. After charging, charged coal is leveled & then oven lids are closed. The carbonization starts in the oven at the temperature of 1200oC. Leveling is required as the cycle time for carbonization depends upon the charge height of coal mass to the great extent. During the cycle time, ovens are checked time to time to determine the completion of the generation of gas. Thus coke mass is ready for withdrawal from the oven the quenching.

The doors of the ready oven are then lifted and hot coke mass is pushed

out by the pusher car and water is sprayed on the hot coke for quenching. Quenched coke is then stacked and dispatched.

The hot quenching water is continuously collected into a settling tank & the

coke particles are also being carried out upto the settling tank with water. These particles are allowed to be settled below the settling tank and then the water almost free from suspended is allowed to be again used for the purpose of quenching of hot coke mass. Time to time the settled particles are reclaimed and these have the large demand in mini cement plants, briquetting plants etc.

3.5.7.2 Raw Material The required quantity of coking coal will be met through import from

countries like South Africa or equivalent from elsewhere. Company also will make afforts to procure from the domestic market to the maximum extent possible. The specification of coke is Table 4:



TABLE 4 SPECIFICATION OF COKE

Sl. No. Properties Contents (In Percentage) 1 Moisture 0.9 % 2 Ash 12.3 % 3 V. M. 1.4 % 4 Sulphur 0.49 % 5 Phosphorous 0.014 % 6 M10 5.4 7 M40 89 8 CRI 20.4 9 CSR 73.6

For flexibility in operation, blending provisions in the plant may be

incorporated at a later stage to operate the plant with Indian coal or more of Indian medium coking coal and prime coking coal from suitable sources, in admixture with imported low ash coking coal. The plant can also run with 100 % prime coking coal of India.

3.5.8 Steel Melting Shop 3.5.8.1 Induction furnace & ladle refining furnace :


02.02.2015 (TPA)

Additional capacity

(TPA)


expansion (TPA)

SMS 4X15T IF 2x15T LRF

200,000 31,000 231,000

9 X15T IF 5x15T LRF

430,000 89,750 519,750

Sub total 630,000 120,750 750,750 A brief description of the manufacturing process is as follows: Induction furnace works on the principle of Induction melting of scrap/

sponge iron with the help of electric power. An alternating electromagnetic field induces eddy current in the metal so that the electrical energy converts into heat, whose quantity depends on the resistively of the charge. Induction furnaces operate on current of commercial frequencies (50Hz) or on current of higher frequencies from 500 to 2000 Hz. These furnaces are beneficial in steel making for low melting loss.

An induction furnace constitutes a single larger primary coil made of water-

cooled copper tube. The working voltage is impressed across the terminals of the coil. The furnace has a rammed lining. The ramming material silica mass contains more than 96% silica and minimum of Al2O3 & Fe2O3. Before



ramming the material, a steel template is kept inside the furnace and the material is rammed between the template and the insulated coil of the induction heater. To minimize the consumption of electric power and cut down the melting period, the crucible wall is as thin as possible. The inside of crucible lining is in contact with liquid metal while it’s outside surface contacts the water-cooled induction

3.5.8.2 Charging In order to control the air pollution in the induction furnace, dust extraction

system is installed. It consists of suction hood, cyclone, wet scrubber etc. Suction hood mounts on the head of furnace; the flue gases will be sucked through the hood. The blower sucks the flue gases through hood along with pipe, which is connected to the cyclone and wet scrubber. The wet scrubber cools the hot gases of furnace through water spray. The nozzles spray water uniformly and perform the fog. The cyclone and scrubber separates the solid particles, dust and its fall down in the bottom of the water tank. The cool and fresh air is exhausting through the Air Vent, in which the dust concentration will be less than 100 mg/Nm3.

3.5.9 Ladle refining furnace The LF installation will be single station system with provision for arc

heating, inert gas stirring, and addition of ferroalloys and additives. The LF will be complete with the transformer, ladle stirring system aluminum wire feeder, carbon injecting device, additives storage and addition system, sampling and temperature measuring device. A fume extraction and cleaning system consisting of bag filters, ID fan and chimney with the related ductwork will be provided.

3.5.10 Billet/Slab /Bloom Caster


02.02.2015 (TPA)

Additional capacity

(TPA)


(TPA)

0.20 MTPA 200,000 26,380 226,380 0.42 MTPA 420,000 replacing 0, as replaced 0.20 MTPA Nil 226,380 226,380 0.22 MTPA Nil 282,975 282,975 Sub total 620,000 735,735

3.5.11 Flat/Round/ WireRod /Structural Mill /others Three streams of rolling mill will be installed for finished steel to be rolled

from the captively available from caster.




02.02.2015 (TPA)

Additional capacity

(TPA)


expansion (TPA)

Flat/ Round/ Wire Rod/ Structural Mill/ others

410,000

Mill -1 4,10,000 217,325 217,325 Mill-2 (no split 217,325 217,325 Mill -3 Specified) 271,656 271,656 Sub total 4,10,000 706,306 706,306

3.5.12 Ferro Alloys Plant (9 MVA+18 MVA)

Facility Capacity (TPA)

Total capacity

Ferro Alloy Plant (1x9 MVA+1x18 MVA)

Ferro Manganese OR 9 MVA= 18,000 18 MVA=36,000

54,000

Silico Manganese OR 9 MVA= 14,400 18 MVA=28,800

43,200

Ferro Chrome OR 9 MVA= 14,400 18 MVA=28,800

43,200

Ferro Silicon 9 MVA= 6,400 18 MVA=12,800

19,200


88,320 88,320


111,360 111,360

Submerged Arc Furnaces produce a wide range of metal products by

smelting various minerals to metal products. In some processes a valuable slag or vapor product arise as well as metal. This tech-commentary covers the principal submerged arc processes in use today, but is in no way an exhaustive review of all submerged arc processes.

In the submerged arc furnace electric power heats the raw materials and

provides the energy to reduce the ore to a metallic state. Generally carbon serves as the reducing agent and fluxes are often added to facilitate the process. The common practice is to mix the ore materials, the reducing agent, and any fluxes outside of the furnace and then to periodically change this mixture (often called charge mix) into the furnace. Although the charge mix is added periodically, the reduction reactions and metal production proceed continuously. The metal is usually allowed to accumulate until



tapping occurs at appropriate intervals; however continuous tapping is not uncommon.

The term “Submerged Arc” is used because the electrodes are usually

buried deep in the furnace burden and the reduction reaction takes place near the tip of the electrodes. At the top of the burden little current flows between the electrodes because of the high resistivity of the un-melted charge. As the burden descends in the furnace the non-carbon portion of the charge begins to malt. As the carbon heats, its resistance decreases providing a conductivity path between the electrodes.

This current flow creates the intense heat needed for the high temperature

and energy required for the reduction reactions. Due to the relatively low resistivity of most smelting process charge mixture, submerged arc furnaces generally operate at lower secondary voltages and higher currents than steelmaking furnaces. Depending on the size of the furnace and the resistivity of the charge mix, the secondary voltage will typically range between 160 to 280 volts in modern furnaces. The current can reach 200,000 amperes in the largest Furnaces. Since changes in the resistance are very slow in Submerged Arc Furnaces and the process are continuous, electric control is much simpler, and any disturbance to the electrical distribution network is much less severe than is the case with typical Electric Arc Furnace Steel production.

The term “Submerged Arc Furnace” does not rally describe all Electric

Smelting processes because in some cases, arcing is to be avoided. Although each Smelting Process is unique, most processes fall into one of three operating modes:-

1) Slag less Processes- with an arc between the electrode and the metal

bath.

2) Slag Processes- Frequently with a coke bed formed under the electrode. The coke bed floats on the slag layer and the current passes through the coke bed and the slag before reaching the molten metal. In these slag processes arcing is usually minimized.

3) Slag Resistance Processes- where the heat is generated by the current passing through a slag layer. There is no coke bed and no arcing should occur.

Most Submerged Arc Furnaces use Three-Phase AC Power with Three

Electrodes Arranged in a conventional Delta configuration in a Round Furnace, however, there are some Six-Electrodes Systems used to produce Pig Iron, Copper- Nickel Matte, Ferro-Nickel, and for Slag Cleaning.

Self- Baking Electrodes Most submerged arc furnaces that produce ferro alloys use a self-baking

electrode system invented nearly eighty years ago by a team led by C.W.



Soderberg. This system takes advantage of the electric power used for the process to bake the electrode in place.

A series of cylindrical steel casing welded on top of each other forms the

electrodes column. Operators periodically add solid green carbon “paste” blocks to the top of

the column. The paste blocks melt to from the unbaked electrodes shape. Vertical fins, which are attached to the casing carry the power in to the carbon paste so that the paste bakes to a solid carbon electrode in the casing. As the process consumes the braked electrode, more electrodes is “slipped” in to the furnace.

The self-baking electrodes system reduces electrodes cost by at least 50%

over the purchase of prebaked amorphous carbon electrodes. It also allows the furnace to be larger since prebaked electrodes are limited to 55 inches in diameter, whereas self-baking electrodes can be as large as 72 inches in diameter.

Slagless Processes: The Silicon Alloys- Ferrosilicon and Silicon Metal

The most widespread use of Submerged Arc Furnaces in the United States

today is in the production of Silicon Alloys in these Slags-Less process an arc is made between the Electrodes and the Metal bath within a cavity under the charge mix.

Ferro-Silicon is widely used as a deoxidizer and alloying element in the Iron

and steel industry. Most grades of Ferro-Silicon contain either 50% or 75% silicon by weight, commonly referred to as 50% Fe si and 75% Fesi. Silicon metal (usually > 99% Si purity) is primarily used as an alloying element in aluminium products and as a feedstock for the production of silicones.

A mixture of silica (usually quartz or quartzite), coke or coal, and wood chips

makeup the charge mix. The coal or coke acts as the reducing agent and the wood chips improve charge porosity and resistivity. Iron usually in the form of light steel scrap, is added for ferrosilicon production. The raw materials are thoroughly mixed, transferred to overhead mix bins, and then gravity fed through chutes into the furnace. Silicon metal and 75% Fe-SI are typically made in an open furnace where a stocking machine spreads the charge mix after it drops from the chutes. The stocking machine adds raw material as needed to correct the charge composition and stokes the burden to prevent sintering and to help release any gaseous pressure build up in the burden. The reaction to produce silicon metal can be summarized as follows: SIO2+2C Si+2CO however, there are complex side reaction that generate SIO gas and which burn to SIO and CO as they escape the burden. Successful operations keep the electrodes deeply buried so that the evolving SIO fume which is aerosol in nature exits the furnace through a hooding system and collects in bag house filters. The collected fume is very



light (9 to 12 lbs/ft3). If the fume is pure enough and handled correctly, it can be resold as an additive to cement, ceramic, and refractory products.

Depicts an open furnace used to produce silicon metal. Note the prebaked

amorphous carbon electrodes are used in this case. The steel casing used for a self-baking electrode would contaminate the silicon metal product with iron as the casing is consumed by the process; therefore self-baking electrodes are not used when producing silicon metal.

Silicon metal furnaces typically range from 10 MW to 25 MW in electric

power rating and ferro silicon furnace range from 10 to 40 MW in the United States.

TYPICAL OPERATING DATA FOR FERRO-SILICON

(9 MVA+18 MVA) 19,200TPA Sl. No.

Description Unit Furnace-1

Furnace-2

Total Specific Consumption

I Ferro-Silicon Plant A Ferro-Silicon Smelting Unit 1 Furnace Capacity MVA 9 18 9+18 2 Power Factor 0.90 0.90 0.90 3 Total Power MW 8.10 16.20 24.30 4 Working Hours in a Day Hours 24 24 24 5 Working day in a Year Days 320 320 320 6 Total Power in a Day MW 194.40 388.80 583.20 7 Unit Required for 1T

Production KWH/T 8500 8500 8500

8 Furnace Efficiency 87.5% 87.5% 87.5% 9 Day Production TPD 20.01 40.02 60.04

10 Annual Production TPA 6,403.76 12,807.53 19,211.29 11 Say TPA 6,400 19,800 19,211 B Ferro-Silicon Smelting Raw

Material

1 Quartz (94%-95%) TPA 12,480 24,960 37,440 1.950 2 Charcoal / Coke TPA 8,320 16,640 24,960 1.300 3 Iron Ore/ Mill Scale TPA 1,600 3,200 4,800 0.250 4 Electrode Paste TPA 448 896 1,344 0.070 5 Dolomite TPA 448 896 1,344 0.070 C Product & By-Products 1 Ferro-Silicon TPA 6,400 12,800 19,200 27.47%

Slag processes Manganese Alloys-Ferromanganese and Silicon-Manganese Steelmaker use manganese as a deoxidizer and to counteract the

deleterious effects of sulfur. Manganese is also used in the production of abrasion-resistant steel products, such as “Head field” type steels.



Submerged arc furnace produce high-carbon or “standard” ferro manganese (typically 79% Mn and 7%C) and a silicon-manganese-Iron alloy commonly referred to as Silico-manganese. Silico-manganese typically contains 68 to 72% Mn, 15 to 23% Si, and 1 to 2% C. High-carbon ferro manganese can be refined to medium-carbon or low carbon ferro manganese in post tapping processes.

Manganese ores, which usually contain iron oxide, are mixed with coal or

coke reductant and usually a small quantity of fluxes from the charge mix. Silico-manganese is produce by reprocessing high carbon ferromanganese by-product slag and smelting cheaper high silicon-manganese ores.

Modern Ferromanganese Furnace has a closed roof designed to prevent

ambient air from mixing with the processes off- gas. The off-gas contains 65 to 70% CO and can be used as fuel for other plant processes such as raw material drying.

The raw material are premixed and then transported to overhead mix bins.

From the overhead mix bin the mix drop through chutes which distribute the mix around the electrodes. The CO gas produce in the reaction zone pre-reduces the higher manganese oxide forms to MnO; however, gas reduction of MnO is impossible. The electric current passes through the coke bed and the slag layer and a reaction between the solid carbon reductant and the MnO occurs in the slag the coke layer minimizes arcing between the electrodes and the slag bath.

In order to reduce manganese vitalization, ferromanganese producer

operate at as low a temperature as possible while still keeping the slag fluid. The lower temperature limits the amount of Mno reduction; therefore the slag may contain up to 45% MnO and can be used as a raw material for the production of silico- manganese, manganese chemicals or electrolytic manganese.

The electric resistance of the ferromanganese mix is lower than it is for

silicon alloys; therefore ferromanganese furnace operate at lower voltage and higher currents. Table gives typical operating data for Manganese Alloys Furnaces.

TYPICAL OPERATING DATA FOR SILICON-MANGANESE

(9 MVA+18 MVA =43,200TPA) Sl. No.

Description Unit Furnace-1 Furnace-2 Total Specific Consumption

I Silico-Manganese Plant A Silico-Manganese

Smelting Unit

1 Furnace Capacity (1X18 MVA+ 1X 9 MVA)

MVA 9 18 9 + 18

2 Power Factor 0.90 0.90 0.90 3 Total Power MW 8.10 16.20 24.30



Sl. No.


4 Working Hours in a Day Hours 24 24 24 5 Working Day in a Year Days 320 320 320 6 Total Power in a Day MW 194.40 388.80 583.20 7 Unit Required for 1T

Production KWH/

T 3,950 3,950 3,950


10 Annual Production TPA 14,410 28,820 43,230 11 Say TPA 14,400 28,800 43,200 B Silico-Manganese

Smelting Raw Material

1 Quartz (94%-95%) TPA 2,160 4,320 6,480 0.150 2 Charcoal/ Coke TPA 6,912 13,824 20,736 0.480 3 Iron Ore / Mill Scale TPA 180 360 540 0.013 4 Electrode Paste TPA 360 720 1,080 0.025 5 Manganese Ore (38%-40%) TPA 10,368 20,736 31,104 0.720 6 Low-Grade High Silicon

Moil Ore TPA 12,456 24,912 37,368 0.865

7 Fe-Mn Slag TPA 10,368 20,736 31,104 0.720 8 Dolomite TPA 1,441 2,882 4,323 0.100 9 Coal TPA 3,312 6,624 9,936 0.230 C Product & By-Products 1 Silico-Manganese TPA 14,400 28,800 43,200 30.28%

TYPICAL OPERATING DATA FOR FERRO-MANGANESE-

(9 + 18 MVA= 27MVA) =54,000 TPA Sl. No.


I Ferro-Manganese Plant

A Ferro-Manganese Smelting Unit

1 Furnace Capacity MVA 9 18 9 + 18 2 Power Factor 0.90 0.90 0.90 3 Total Power MW 8.10 16.20 24.30 4 Working Hours in a

Day Hours 24 24 24

5 Working Day in a Year

Days 320 320 320

6 Total Power in a day MW 194 388 583 7 Unit Required for 1T

Production KWH/T 3,100 3,100 3,100

8 Furnace Efficiency 89.70% 89.70% 89.70%



Sl. No.


9 Day Production TPD 56.25 112.50 168.75 10 Annual Production TPA 18,000 36,000 54,000 11 Say TPA 18,000 36,000 54,000 12 Briquette Required

for 1T Production T/T 2 2 2

13 Briquette required per Day

TPD 112.50 225.00 337.50

14 Capacity of Briquette Plant

TPH 4.69 9.38 14.06

15 Briquette Plant to be installed

TPH 5.00 9.50 14.50

B Ferro-Manganese Smelting Raw Material

1 Briquettes TPA 37,120 74,240 111,360 2.062 2 Manganese Ore

Lump TPA 3,600 7,200 10,800 0.200

3 Coke TPA 1,000 2,000 3,000 0.056 4 Quartz TPA 1,098 2,196 3,294 0.061 5 Electrode Paste TPA 396 792 1,188 0.022 C Product & By-

Products

1 Ferro-Manganese (High Carbon Ferro-Manganese at 75 to 80% Mn)

TPA 18,000 36,000 54,000 41.65%

2 Slag TPA 21,607 43,214 64,821 50.00% 3 Fines 3,606 7,213 10,819 8.35% II Briquetting Plant A Ferro-Manganese

Briquette Plant

1 Capacity Of Briquette Plant

TPA 111,360

2 Unit Required for 1T Production

KWH/T 22.00

3 Total Power MW 0.31 B Briquette Plant

Raw Material

1 Manganese Ore Concentrate

TPA 100,224 90.00%



Sl. No.


2 Lime TPA 4,454 4.00% 3 Molasses TPA 6,681 6.00% C Product & By-

Products

1 Briquette TPA 94,656 85% 2 Reused Briquette

Fines TPA 16,704 15%

TYPICAL OPERATING DATA FOR FERRO-CHROME-

(9 +18 MVA= 27MVA) =43,200 TPA Sl. No.


I Ferro-Chrome Plant A Ferro-Chrome

Smelting Unit

1 Furnace Capacity MVA 9 18 9 + 18 2 Power Factor 0.90 0.90 0.90 3 Total Power MW 8.10 16.20 24.30 4 Working Hours in a

Day Hours 24 24 24

5 Working Day in a Year

Days 320 320 320

6 Total Power in a day MW 194.4 388.8 583.20 7 Unit required for 1T

Production KWH/T 3,950 3,950 3,950


10 Annual Production TPA 14,410 28,820 43,230 11 say TPA 14,400 28,800 43,200 12 Briquette required for

1T Production T/T 2.00 2.00 2.00

13 Briquette required per day

TPD 90 180 270

14 Capacity of Briquette Plant

TPH 3.75 7.51 11.26

15 Briquette plant to be installed

TPH 4 7.50 11.50

B Ferro-Chrome smelting raw material

1 Briquettes TPA 29,440 58,880 88,320 2.043 2 Chrome Ore Lump TPA 2,882.04 5,764.08 8,646.12 0.200 3 Coke (400kg/fc) TPA 800.57 1,601.13 2,401.70 0.056 4 Quartz TPA 879.02 1,758.05 2,637.07 0.061



Sl. No.


5 Electrode Paste TPA 317.02 634.05 951.07 0.022 6 Refractories TPA - - - 0.000 C Product & By-

Products

1 Ferro-Chome TPA 14,410.21 28,820.42 43,230.62 41.99% 2 Slag TPA 17,159.33 34,318.66 51,477.98 50.00% 3 Fines 2,749.12 5,498.24 8,247.36 8.01% II Briquetting Plant A Ferro-Chrome

Briquette Plant

1 Capacity Of Briquette Plant

TPA 88,320.00

2 Unit Required For 1T Production

KWH/T 22.00

3 Total Power MW 0.25 B Briquette Plant Raw

Material

1 Chome-ore concentrate

TPA 79,488.00 90.00%

2 Lime TPA 3,532.80 4.00% 3 Molasses TPA 5,299.20 6.00% C Product & By-

Products

1 Briquette TPA 75,072 85% 2 Reused Briquette

Fines TPA 13,248 15%

Slag Resistance Furnaces Matte Smelting The treatment of copper and nickel sulfides to produce copper nickel matte

or copper matte is often done in an electric furnace. In the matte smelting operation, the sulfide minerals are separately concentrated and readied for separation into matte (a molten solution of copper, nickel, iron, and sulfur) and slag.

The smelting processes is carried out using electric resistance heating of

the slag. Arcing is to be avoided. Thus, the term slag resistance furnace is applied to this type of process. The solid concentrate charge floats on the slag and gradually melts into the slag. The slag is in constant motion due to the passage of the electric current. In addition to provided resistance heating, the slag serves as means for discarding some of the iron and gangue. The matte particles sink to the bottom of the furnace to form a liquid metal pool. This type of smelting is usually carried out in a rectangular furnace with six electrodes.



Slag Cleaning Furnaces Slag cleaning furnaces are used in conjunction with the flash smelting of

copper and nickel concentrates. In the most widely used flash smelting process a mixture of concentrate and flux is suspended in a stream of preheated air and then fired down a shaft. Droplets of molten matte and slag collect at the bottom of the shaft. Due to the rapidity of the matte formation the slag still contains magnetite (Fe O4 ) and an excess of copper and nickel, some in an oxidized from. Depending on the grade of the matte, the copper and nickel contents can be as high as 1.5% which may be as high as their values in the original ore.

The molten slag from the flash smelter is transferred to a slag cleaning

furnace where it undergoes a secondary smelting operation. Coke breeze is added to reduce the Fe3O4 to FeO and allow separation from the copper and nickel. During the settling time in the furnace the matte precipitates from the slag into the matte bath under the slag. By using this procedure 75 to 80% of the copper and nickel contained in the slag can be recovered in the form of matte. The slag cleaning furnace also processes solid revert and converter slags which can contain up to 5 to 6% Cu and Ni. For this furnace, the coke addition is about 2% of the liquid slag treated, and the energy consumed is 90 to 135 kwh/ton of liquid slag.

3.5.13 Captive Power Plant 3.5.13.1 WHRB Power Generation Unit Sponge Iron is produced by heating Iron with coal and other additives under

controlled conditions in Rotary Kiln. The outlet gases are mixed with air and burnt to convert CO into CO2. As the flue gases contain substantial sensible heat, it is proposed to utilize the heat for power generation through waste heat recovery boilers.

The waste heat recovery boilers consist of radiation chambers with water

walls just like conventional boiler with a drum to evaporate steam at 88 kg/cm2 pressure. The steam is carried to super heater system where the temperature is maintained at 515°C. The boiler has an economizer, which utilises the heat of outgoing gases to raise the temperature of feed water from 100 to 200 °C. The steam is used to rotate the turbine and to generate power. The condensed steam is collected and recycled to the boilers as boiler feed water. A DM water plant is provided for preparation of de-mineralized water for make-up to the steam-condensate cycle. The output of the boilers will be used to generate electricity through Steam Turbo Generator Sets of capacities as mentioned above. The flue gases leave the economizer zone at about 150°C. The gases are passed through ESPs, where the dust concentration is brought down to below 100 mg/m3. Three ESPs and stacks of appropriate heights are provided, one for each boiler.

Total WHRB based power generation will be 87 MW. Details are given

below :



Facilities Capacity as per EC dated 02.02.2015 in

(MW)

Additional capacity in

(MW)

Total capacity after proposed expansion in

(MW) WHRB 6X100 TPD from DRI Kilns

12 0 12

WHRB 1NoX300 TPD from DRI Kilns

6 2 8

WHRB 3Nosx350 TPD from DRI Kilns

24 0 24

WHRB 2NosX500 TPD from DRI Kilns

24 0 24

WHRB from MBF 0 14 14 WHRB from Coke oven 0 5 5 Total 66 21 87

3.5.13.2 AFBC / CFBC based Power Plant Total AFBC based power generation will be 111 MW. Details are given

below :

Facilities Capacity as per EC dated

02.02.2015

additional capacity

(TPA)

Total Power Generation

(MW) AFBC/CFBC 25 - 25 AFBC/CFBC 51 - 51 AFBC/CFBC 35 35 35 111

20 MW AFBC based power plant has been commissioned and is under

operation. The boiler is/will be of natural circulation, balanced draft, single drum type and is/will be equipped with fluidized bed firing system. The boiler generates steam at 88 kg/cm2 pressure and temperature 515 5oC. The boiler is/will be provided with Electrostatic Precipitator. Overall efficiency of ESP is around 99.50% to maintain particulate concentration in flue gas at chimney outlet below 100 mg/Nm3.

TG set to be installed

Facilities No of Units

Generation Capacity (In MW)

Generation Voltage (In KV)

Total Power

(In MW) TG Sets (2X20 MW) 2 Nos. 20.00 11KV 40.00 TG Sets (New) 4 Nos. 30.00 11KV 120.00 TG Sets (New) 2 Nos. 20.00 11KV 40.00 Total Production 200.00



3.6 Raw material required along with estimated quantity, likely source, marketing area of final product’s Mode of transport of raw material and Finished product

The detail of raw material and their sources is given below in Table 5 &

finished products is given in Table 6.

TABLE 5 ANNUAL RAW MATERIAL REQUIREMENT, AND THEIR SOURCES FOR 0.75 MTPA STEEL PLANT

S.N. Facilities Raw Material Specific Consumption

Unit Required Own Source

From outside Purchased

Unit Quantity I Iron Ore

Beneficiation Plant

Iron Ore T/T 1.66 TPA 1,200,000 1,200,000 NIL

Iron Ore Fines T/T 1.097 TPA 3,554,280 3,554,280 NIL Dolomite T/T 0.014 TPA 45,360 45,360 Bentonite T/T 0.015 TPA 48,600 48,600 Coke Breeze T/T 0.017 TPA 55,080 55,080 Coal T/T 0.048 TPA 155,520 155,520

II Pellet Plant

Heavy Furnace Oil

KL/T 0.00935 KLPA 30,294 30,294

III Coal Washery

ROM Coal (Linkage/Auction)

T/T 2 TPA 924,000 - 924,000

Iron Ore Pellets T/T 1.5 TPA 1,796,850 1,796,850 NIL Coal

T/T 0.85 TPA 1,018,215 1,018,215 556,215 IV Sponge Iron

Plant

Dolomite T/T 0.04 TPA 47,916 47,916 Iron Ore Fines T/T 0.95 TPA 505,613 505,613 NIL Coke Fines T/T 0.065 TPA 34,594 - 34,594 Lime Stone T/T 0.15 TPA 79,834 - 79,834

V Sinter Plant

Dolomite T/T 0.05 TPA 26,611 - 26,611 BF Grade T/T 1.5 TPA 308,700 308,700 NIL Sinter T/T 1.5 TPA 720,300 532,224 188,076 Coke T/T 0.61 TPA 418,460 140,000 278,460 Coal Fines T/T 0.05 TPA 34,300 34,300 Dolomite T/T 0.14 TPA 13,446 13,446

VI MBF

Quartz T/T 0.052 TPA 35,672 35,672 VII Coke Oven Coking Coal T/T 1.51 TPA 210,000 210,000

DRI T/T 1.176 TPA 706,588 706,588 NIL Pig Iron T/T 1.087 TPA 81,603 81,603 NIL

VII Steel Melt Shop (I.F.) Scrap T/T 1.087 TPA 81,603 81,603

VIII Billet/Slab/Bl

oom Caster Hot METAL T/T 1.02 TPA 750,750 750,750



S.N. Facilities Raw Material Specific Consumption

Unit Required Own Source

From outside Purchased

Unit Quantity Rolling Mill (TMT/ Round / Wire Rod / Structural/ Flat/ Others)

Casted T/T 1.0416 TPA 735,735 735,735 NIL

IX

Furnace Oil L/T 45 KL/A 33,108 33,108 X Ferro Alloy

Plant

X.1 Ferro-Chrome Chome Ore Concentrate

TPA 93,744 93,744

X.2 Ferro-Manganese

Manganese Ores

TPA 122,472 122,472 NIL

X.3 Ferro-Silicon Chome Ore Concentrate

TPA 41,664 41,664

X.4 Silico-Manganese

Manganese Ores

TPA 74,304 74,304 NIL

Char T/KWH 1.325 TPA 215,622 215,622 NIL Coal Fines T/KWH 0.883 TPA 122,186 122,186 NIL Middlings T/KWH 1.204 TPA 392,700 392,700 NIL

XI Power Plant

Coal T/KWH 0.48 TPA 123,237 123,237

TABLE 6 FINAL PRODUCT FOR CAPTIVE USE OUT SIDE SALE

S.N. Product Unit Production Captive Use Outside Sale

1 Beneficiated Ore TPA 720,000 720,000 NIL

2 Pellets TPA 3,240,000 1,796,850 1,443,150

3 Clean Coal TPA 462,000 462,000 NIL

4 Middlings TPA 392,700 392,700 NIL

5 Rejects TPA 69,300

6 DRI TPA 1,197,900 706,588 491,312

7 Char TPA 215,622 215,622 NIL

8 Coal Fines TPA 122,185 122,185 NIL

9 Sinter TPA 532,224 532,224 NIL

10 Pig Iron TPA 686,000 81,603 604,397

11 Coke TPA 140,000 140,000 NIL

12 Hot Metal TPA 750,750 750,750 NIL

13 Billet/Slab/Bloom TPA 735,735 735,735 NIL

14 (TMT/ Round / TPA 706,306 - 706,306



S.N. Product Unit Production Captive Use Outside Sale Wire Rod / Structural/ Flat/ others)

15 Ferro-Chrome or TPA 43,200 - 43,200

16 Ferro-Manganese or TPA 54,000 - 54,000

17 Ferro-Silicon or TPA 19,200 - 19,200

18 Silico-Manganese TPA 43,200 - 43,200 3.6.1 Mode of transport of Raw material Raw material will be transport through Rail/ Road. Presently raw material is

being transport by Rail/ Road. 3.7 Resource optimization/ recycling and reuse envisaged in the project Recirculating cooling water system shall be provided in the plant. The

recirculating cooling water pumps to the various consumers in the plant will pump cold water from the cooling tower basin. The hot water return from the consumers will return to the cooling tower for cooling and recirculation.

To meet the requirement of demineralization water as make-up water for

boiler, de-mineralization plant of suitable capacity will be provided. Water quality shall meet the Turbine and Boiler Manufacturers’ recommendation.

Entire waste water from the SMS and CPP complex shall be treated and

reused for afforestation, green belt watering, sprinkling and dust suppression. There shall be no liquid waste discharge from the plant premises except during monsoon when the sprinkling and watering demand will be almost negligible.

The main solid waste generated would be bottom and fly ash in 20:80 ratio. Bed ash will be collected in bottom ash hopper which will have effective 8 hours storage capacity. The bed ash collected in bottom ash hopper will be removed in 60 minutes once in every shift of 8 hours through jet pumps in the form of ash slurry. The ash slurry will be collected in slurry pump from where it will be pumped to ash dyke area through slurry pumps.

Fly ash from economizer, air pre-heater and ESP hoppers will be

automatically extracted one after another in sequence. A steel silo will be constructed for fly ash collection via which ash will be discharged from the bottom of silo into trucks for utilizing it for various applications such as brick making, road embankments, etc. Other solid wastes such as dust particles collected in the hoppers (below ESP) will be conveyed pneumatically and will be stored in Silos. This will be further disposed by trucks. Wastes like slag, runners & raiser from IF and scales and return scrap etc from billets caster will be recycled and reused in the process.



Domestic waste shall be generated from the plant office, organic component of which shall be composted/ vermi composted. The sewage from the Plant shall be led to Sewage Treatment Plant. It will be provided with biological treatment facility to control BOD and suspended solids. The treated effluent conforming to prescribed standards will continue to be used for watering plantation. Wastes such as used oils/ spent oil shall be generated periodically, which shall be sold to authorized recycling vendors in drums.

3.8 Availability of water its source, energy / power requirement and source The water required for the plant shall be sourced from Karo River. The total

water consumption shall become to 2385 cum/hr after implementation of entire expansion proposal.

The plant will generate 198 MW energy in form of electricity from its captive

power plant and will utilize 177 MW power generated in its Steel plant. 3.9 Quantity of wastes likely to be generated (liquid and solid) and

scheme for their management /disposal The main solid waste generated is and would be bottom and fly ash

generated from power plant. Bed ash is collected in bottom ash hopper and is removed in the form of ash slurry. The ash slurry is collected in slurry pump from where it will be pumped to ash dyke area through slurry pumps. Fly ash from economizer, air pre-heater and ESP hoppers is automatically extracted one after another in sequence. A Silo is constructed for fly ash collection via which ash is discharged from the bottom of silo into trucks for utilizing it for various applications such as brick making, road embankments, etc.

Electrostatic Precipitator and Bag Filters Systems is/ will proposed to be

installed for pollution control of air emissions. Dust particles collected in the hoppers (below ESP) are conveyed pneumatically and stored in Silos. This is further disposed by trucks. Wastes like slag, runners & raiser from IF and scales and return scrap etc from billets are recycled and reused in the process. Domestic waste is generated from the plant office, organic component of which shall be composted/ vermi composted. Quantity of waste generation is estimated and given in Table 7.

TABLE 7

SOLID WASTE GENERATION (TPA) AFTER EXPANSION Sl. No.

Source Total (TPY) Reuse/ Sale

(TPY)

Remarks Balance for Disposal

(TPY)*

1 Waste Oil & Lubricant

150 KL 150 KL Shall be sold 0

2 DM plant resin 15 KL 15 KL Shall be disposed in properly constructed pit

0



Sl. No.

Source Total (TPY) Reuse/ Sale

(TPY)

Remarks Balance for Disposal

(TPY)* as per CPCB norms

3 Refractory waste 5 - Into disposal site 5 DRI Plant

4 Char 215622 215622 AFBC boiler 0 5 Coal fines 122185 122185 AFBC boiler 0 6 ESP & In plant

Dust 22500 0 Into disposal site 22500

7 Kiln Accretion 5000 0 - 5000 Blast Furnace

8 MBF Slag 91675 91675 To cement plants 0 9 MBF Flue Dust 8980 8980 To cement plants 0

SMS 10 IF & LRF Slag 50000 5000 Village road

construction & low land filling, disposal

00

Power Plant 11 Fly Ash 254000 254000 To cement plant/bricks

manufacturing units 0

Coal Washery 12 Middlings 535500 AFBC boiler 0 13 Reject 94500 AFBC boiler after re-

beneficiation 0

Beneficiation Plant 14 Tailings waste 72000 Will be disposed in

tailing 72000

Ferro Alloys Plant 15 Slag 65442.10 Will be used in Ferro

silicon plant

16 Fines 1441.54 Into disposal site Sinter plant 17 solids 2660 2660 Will be reused in sinter 0

Coke oven plant 18 Coke breeze 45000 10200 Will be used in pellet

and sinter making within plant

0



3.10 Schematic Representations of the Feasibility drawing which give information of EIA purpose

Process Flow sheet is given in Fig 1 for sponge iron plant, Fig 2 for power

plant Fig 3 for steel melting shop, and entire plant materila & energy flow sheet is given Fig 4. All the above are annexed to the end of project feasibility report.

4.0 SITE ANALYSIS 4.1 Connectivity The existing plant is located in village Kamanda,Tehsil Koira, District

Sundergarh, Odisha. The location of plant and study area can be seen in Survey of India Topo sheet No. 73G/1 & 5. The coordinates of this plant are:

Latitude - 21°55’33’’ and 21°55’58’’ N Longitude - 85°13’16” and 85°13’52” E

Road link The plant is accessible by all weather road from the Tehsil headquarter

Koira, district headquarter Sundergarh and town Raurkela, which are located at distances of 31 km, 124 km and 52 km respectively. The site is located close to NH-215, which connects Barakot in the south to Rourkela in the north.

Rail link The nearest railway station is Barasuan at a distance of 15 km from the

plant. Air link The nearest air port is at Ranchi, which is approximately 250 km from the

plant. 4.2 Land form, land use and land ownership Company has purchased directly 111.08 acres private land, which is

already under industrial usage. 186.340 acres private land and 61.52 acres Government land has been acquired through IDCO, and balance 22.80 acres government land is under process.

4.3 Topography The core zone represents nearly flat land (about 560 m AMSL) devoid of

any significant drainage or topographical features. The general slope is due northeast with a local depression in the eastern part and over a small area in north.



The study area, a part of South Koel River basin, falls in Sundergarh district

of Odisha. It lies on the bank of Karo Nala a tributary to the river South Koel and forms the major drainage system of the study area. The river South Koel flows westerly and Karo Nadi northeasterly in the North part of the study area and both join each other at Goilkera outside study area in Odisha. The general land slope is towards north and northwest.

4.4 Existing land use pattern The existing and proposed plant establishment land use is given below:

Land ownership

Private Land

Land use Factory Goda-II Patit Goda-I MA.SA. BE.SA BA.SA. Gharbari Total Total 96.310 85.280 4.340 1.640 35.460 52.070 7.390 14.930 297.420

Land

ownership Govt. Land

Land use Factory Patit S.S.J. U.J.JOGYA GODA-II Rasta Gharbari Nala Total Total 35.500 10.180 9.540 4.000 19.710 4.170 0.050 1.170 84.320

Total Acres (Pvt. + Govt.) = 381.740

4.5 Existing infrastructure New supporting infrastructure like office building, canteen, strengthening of

roads, waste or waste water treatment is proposed. Temporary sheds for workers will be established at the site. Kamanda & Kula village have a primary school and power supply for domestic use.

4.6 Soil classification The soil of the study area is less fertile. The area is occupied by mixed red

and black soil, red sandy soil, gravelly and lateritic soil. The mixed red and black soil contain a large quantity of calcium and magnesium carbonate but is generally deficient in nitrogen and phosphorous. The red sandy soil, gravelly and lateritic soils are generally deficient in potash, phosphoric acid and lime. Soil is in general open in texture and well drained. Plenty of iron concentration is present in the soil.

4.7 Climatic data from secondary sources Temperature As per the nearest IMD station, Keonjhar. The monthly mean of minimum

temperature ranges from 10.82°C in December to 23.84°C in May. The monthly mean of maximum temperature ranges from 25.81°C in December to 36.64°C in May.



Rainfall Rainfall shows wide and erratic variations. The average annual rainfall at

IMD station Keonjhar was recorded as 1369.50 mm from 1996 to 2001. The monsoon season is spread over the months from June to September.

Relative Humidity The average daily relative humidity data, obtained from IMD station

Keonjhar is given Table 8.

TABLE 8 MONTHLY AVERAGE RELATIVE HUMIDITY AT KEONJHAR (1993-2004)

Months Relative humidity (%) At 0830 hrs At 1730 hrs January 62.0 40.1 February 59.8 33.2 March 49.3 26.5 April 49.7 26.7 May 55.4 34.4 June 73.8 63.9 July 80.8 75.5 August 84.2 72.8 September 76.3 72.9 October 76.8 62.0 November 68.7 47.6 December 62.6 37.3 Average 66.6 49.4

4.8 Social infrastructure available Hospitals, school, community facilities are present in the villages in buffer

zone within 10 Km of study area. Social infrastructures existing as per Census 2011 is given in as Enclosure V to the Form 1.

5.0 PLANNING BRIEF 5.1 Planning concept Presently the company is operating 900 TPD DRI plant 2,00,000 TPA steel,

40 MW power plant at village Kamanda in Sundergarh District of Odisha environmental clearance for the existing plant was granted by MOEF vide letter no. J-11011/304/2007-IA.II (I) dated 12.12.2008

Further we had applied for expansion of steel plant from 0.20 MTPA to 0.60

MTPA for which Environmental Clearance was granted by MOEF&CC vide letter no. J-11011/434/2009-IA.II(I) dated 02.02.2015



We had applied online application vide proposal no. IA/OR/IND/53279/2016 dated 29.04.2016 to expand existing as well as proposed facilities from 0.60 MTPA to 0.70 MTPA steel. TOR was issued by MOEF &CC vide letter No. J-11011/434/2009-IA.II(I) dated 03.08.2016.

In the mean time, for better integration of various sub-units, company now

proposes to enhance capacity of pelletisation plant, Sinter, SMS, Billets Bloom/ slab caster, Flat / round/wire rod/ structural/ others and power plant.

5.2 Population projection Total manpower currently is 500 and additional approximately 1635 will be

required during expansion. An equal number are expected to be in indirect employment. The estimate, however, does not cover the personnel for township, medical facilities, etc. Many more persons will also get employment in the ancillary & other services connected with this project. Unskilled and semi skilled (after training) will be hired from in and around the Plant while skilled, engineers, managerial staff and technical experts will have to be hired from outside.

5.3 Land use planning (break up along with green belt etc.) The Steel Plant will be set up in the existing plant premises. Total plant

premises will be 381.58 acres (154.489 ha). Break up of total land use are given Table 9.

TABLE 9

BREAK UP OF TOTAL PLOT AREA As per EC 02.02.105 Proposed Sl.

No. Description

Area (Ac) Percent Area (ac) Percent 1. Plants & facilities 140.39 36.78 150.39 39.40 2. Stock yards 23.03 6.04 23.03 6.0 3. Area for solid waste

treatment and disposal 61.8 16.18 51.8 13.60

4. Green belt & plantation 125.97 33.0 125.97 33.0 5. Administration building 1.98 0.52 1.98 0.52 6. Water reservoir 9.4 2.46 9.4 2.46 7. Roads 19.17 5.02 19.17 5.02 Total 381.74 100 381.74 99.98

30.78 acres land is additional available adjacent to the proposed plant

boundary which can be utilized for fly ash and other solid waste disposal near plant.

5.4 Assessment of infrastructure demand (physical & social) An assessment of the facilities available in the villages in and adjacent to

the plant site is education, Hospitals, drinking water, communication and approach road. An assessment of the facilities available in the villages in the study area based on Census 2011 has been done and given in Table 10.



TABLE 10 NEED EVALUATION FOR VILLAGES IN AND AROUND MINE AREA

Sl. No.

Parameter Present Status in Senegara village

Scope for improvement

1. Education Primary Schools-38 Middle school - 16 Secondary school – 4

Provision of middle school, secondary etc.

2. Hospitals PHSC-8 There are no medical facilities in Kamanda village

Provision of medical facilities such as 4 bed primary health centre, has been constructed

3. Drinking water For drinking purpose the village has well and tank water as source.

Provision of potable drinking water supply through hand pumps, tankers etc already provided.

4. Power supply The village has power supply for domestic purpose

Power for agriculture and other purposes could be provided.

5. Communication No bus stop or railway station.

Transportation facility to hospital and nearest town could be maintained and strengthened.

6. Approach to village Concrete road Approach road to the village already strengthened.

7. Post and Telegraph Post office is present and telephone facility is available in the village.

Communication facilities could be improved.

8. Banks/ credit societies Commercial Bank -1 5.5 Amenities / facilities Education, Hospitals, drinking water, power supply, post and telegraph,

banks, communication and approach roads are present in the villages in buffer zone within 10 Km of study area.

6.0 PROPOSED INFRASTRUCTURE 6.1 Industrial area (processing area) The steel plant will be established in the existing plant premises. 6.2 Residential area (non processing area) Residential colony is under construction near plant. 6.3 Green belt The green belt equivalent to 33% of the plot area will be developed.



6.4 Social infrastructure The social infrastructure in the surrounding villages will be improved as a

part of the CSR activities of the company. Approximate expenditure for CSR Initiatives activities already taken up by the Company for the year 2006 -2015 is given Table 11.

TABLE 11

CSR ACTIVITIES TAKEN UP BY M/S RUNGTA MINES LIMITED Sl. No. Activities Amount (Rs)

1. Improvement of health & Hygine 8,17,082

2. Drinking water 29,70,794

3. Educational support 25,96,338

4. Improvement of Social Welfare Activities 15,27,849

5. Infrastructure Development 1,77,04,532

Total 2,56,16,595 6.5 Connectivity Refer section 4.1 6.6 Drinking water management (source & supply of water) Refer section 3.8 6.7 Sewerage system & industrial waste management Domestic waste shall be generated from the plant office, organic component

of which shall be composted/ vermi composted. The sewage from the Plant shall be led to Sewage Treatment Plant. It will be provided with biological treatment facility to control BOD and suspended solids. The treated effluent conforming to prescribed standards will continued to be used for watering plantation and in monsoons, discharged to the nearest nala. The plant will be based on zero discharge principle. All the domestic and industrial effluents will be properly treated and completely recycled in the system. Thus there is no discharge of effluents envisaged from the plant.

6.8 Solid waste management The main solid waste generated would be bottom and fly ash in 20:80 ratio.

Bed ash will be collected in bottom ash hopper which will have effective 8 hours storage capacity. The bed ash collected in bottom ash hopper will be removed in 60 minutes once in every shift of 8 hours through jet pumps in the form of ash slurry. The ash slurry will be collected in slurry pump from where it will be pumped to ash dyke area through slurry pumps.



Fly ash from economizer, air preheater and ESP hoppers will be

automatically extracted one after another in sequence. A steel silo will be constructed for fly ash collection via which ash will be discharged from the bottom of silo into trucks for utilizing it for various applications such as brick making, road embankments, filling the low line area etc. Other solid wastes such as dust particles collected in the hoppers (below ESP) will be conveyed pneumatically and will be stored in Silos. This will be further disposed by trucks. Wastes like slag, runners & raiser from IF and scales and return scrap etc from Bar and Rod Mill will be recycled and reused in the process.

The municipal solid waste generated from the plant will be segregated and

separated as combustible and non-combustibles wastes. The combustible wastes will be used as fuel in the kiln. This will solve the problem of solid waste disposal and will also reduce the fuel requirement for the kiln.

The kiln will act as an incinerator in this case. The non-combustible wastes

will be land filled for composting and other (non-compostable) waste will be sold to the authorised recycling vendors.

The hazardous waste like transformer oil, spent oil etc will be utilized in kiln

as a source of high calorific fuel which will also reduce the fuel consumption and solve the problem of hazardous waste disposal. The solid waste which will be used for landfill is basically ground dust which has no toxic elements as constituents. Hence the question of soil contamination, by the way of disposal of solid waste, does not arise.

6.9 Power requirement & supply / source Refer section 3.8 7.0 REHABILITATION AND RESETTLEMENT PLAN No rehabilitation and resettlement plan has been made as no displacement

of population. Company has purchased directly 111.08 acres private land, which is already under industrial usage. 186.340 acres private land acquired through IDCO and 61.52 acres Government land acquired through IDCO Odisha and balance 22.80 acres government land under Process.

The plant and allied activities will provide job opportunities for eligible

persons and many will find employment in ancillary & other services connected with this project.

The proposed long term activity will open up market and opportunities

growth for self employed and cultivators. To this extent, the impact will be significantly beneficial since un-employment and under employment is the main socio-economic problem faced by the people in this area.



8.0 PROJECT SCHEDULE & COST ESTIMATES 8.1 Project Schedule The completion schedule of the proposed plant will be 60 month after

receipt of Environmental Clearance. 8.2 Cost of the Project The total cost of the proposed project expansion to 0.75 MTPA will be Rs.

2825.68 crores 9.0 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS) The persons will be provided with either direct employment or indirect

employment. They would be mostly recruited in unskilled, semi skilled office assistant categories etc. This will improve the economic condition of the local people. The employment of local people in primary and secondary sectors of project will upgrade the prosperity of the region.

With the advancement in technology and the stringency in permissible limits

of emission along with regular monitoring, it is possible to operate small plants of this type by having minimal impact on the environment.


FIG 1 : PROCESS FLOW CHART FOR SPONGE IRON PLANT

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FIG 2 : PROCESS FLOW SHEET OF POWER PLANT

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FIG 3 : FLOW SHEET OF STEEL MELTING SHOP

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FIG 4 : MATERIAL & ENERGY FLOW SHEET FOR ENTIRE STEELPLANT


FIG 4 : MATERIAL & ENERGY FLOW SHEET FOR FERRO ALLOYS PLANT

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revised form – 1environmentclearance.nic.in/writereaddata/... · form 1 for expansion of kamanda...

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