suryadev alloys & power pvt. ltd....expansion of steel plant suryadev alloys & power pvt....

Executive Summary

0

SUMMARY ON

ENVIRONMENTAL IMPACT ASSESSMENT

REPORT

OF

Expansion of Steel Plant

at

Sirupuzhalpet & New Gummidipoondi Village,

Gummidipoondi Tehsil

Tiruvollur District, Tamil Nadu

Suryadev Alloys & Power Pvt. Ltd.

Submitted to

TAMIL NADU POLLUTION CONTROL BOARD

Suryadev Alloys & Power Pvt. Ltd. Expansion of Steel Plant

Executive Summary

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1.0 PROJECT DESCRIPTION

M/s. Suryadev Alloys & Power Pvt. Ltd. is operating steel plant Sirupuzhalpet & New

Gummidipoondi Village, Gummidipoondi Taluk, Tiruvollur District, Tamil Nadu. Now it is

proposed to expand existing steel plant by installing DRI Kiln with WHRB power plant,

Sinter plant, Pig Iron plant, Induction Furnace unit, Power plant (PCF based) and Oxygen

plant unit, partly in the existing plant premises and remaining in the adjoining land. Total

land envisaged for the entire project is 164.01 acres [i.e. 119.01 acres (existing land) + 45

acres (adjoining land)]. Entire land is in possession of management. Total land is private

land. There are no water bodies & settlement in the land envisaged for the proposed

expansion project.

As per the Ministry of Environment & Forests, New Delhi notification, dated 14th

September, 2006 and its subsequent amendments, all Primary metallurgical processing

industries are classified under Category ‘A’. The Ministry of Environment, Forest & Climate

Change, New Delhi has accorded Terms of Reference (TOR) for the proposed project vide

letter no. J-11011/595/2011- IA II (I) dated 24th June 2015. The EIA Report has been

prepared by incorporating the TOR stipulated by the Hon’ble EAC.

Pioneer Enviro Laboratories & Consultants Private Limited, Hyderabad, which is accredited

by NABET, Quality Council of India for conducting EIA studies for Metallurgical Unit, have

prepared Draft Environmental Impact Assessment (EIA) report for the proposed expansion

project of Mini Integrated Steel plant by incorporating the TOR approved by Ministry of

Environment & Forests, New Delhi. The report contains detailed description of the

following:

Characterization of status of environment with in an area of 10 km radius from the

plant for major environmental components including air, water, noise, soil, flora,

fauna and socio-economic environment.

Assessment of air emissions, liquid waste and solid waste from the proposed project

along with the noise level assessment.

Environmental Management Plan comprising of emission control measures proposed

to be adopted in the proposed project, solid waste management, Greenbelt

development.

Post Project Environmental Monitoring & Budget for Environmental Protection

Measures.


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1.0 Plant Configuration and Production Capacity

The proposed Mini Integrated Steel Plant envisages manufacturing of the following products

S.No. Products / Units EC obtained in 2011 Units implemented Present proposal Total after expansion

1. Sponge Iron through DRI Kilns 2,31,000 TPA (4 x 175 TPD)

[This unit is yet to be implemented. Now it is

proposed to be dropped]

--- 3,30,000 TPA (2 x 500 TPD)

[Instead of 4 x 175 TPD, 2 x 500 TPD is proposed]

3,30,000 TPA

2. Sinter through Sinter plant --- --- 10,08,000 TPA (1 x 2880 TPD)

10,08,000 TPA

3. Pig Iron through Blast Furnace --- --- 7,56,000 TPA (1 x 2160 TPD)

7,56,000 TPA

4. Billets through Induction Furnace and Arc Furnace

12,50,000 TPA 3,20,000 TPA Billets through IF/ Converter (BOF) / Arc Furnace

12,50,000 TPA

5. Rolled Products (Wire Rods & Bars)

12,00,000 TPA 5,00,000 TPA --- 12,00,000 TPA

6. Power Plant (WHRB) 1 x 15 MW (Dropped)

--- 2 x 15 MW 30 MW

7. Power Plant (utilising Blast furnace gases)

--- --- 1 x 30 MW 30 MW

8. Power Plant 2 x 80 MW (CFBC based)

2 x 80 MW (CFBC based)

1x 330 MW (PCF based)

490 MW

9. Ferro Manganese 12000 TPA --- ---- 12,000 TPA

10. Silico Manganese 24000 TPA --- ---- 24,000 TPA

11. Oxygen plant --- --- 1 x 400 TPD 400 TPD


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1.2 Raw Materials

The following will be the raw material requirement for the proposed expansion project:

Raw Material Quantity

(TPA) Sources Mode of Transport

For manufacturing of Sponge Iron

Iron Ore (for 2 x 500 TPD DRI Kilns) 5,30,000 Karnataka / Odisha

By rail & road (through covered trucks)

Coal (2 x 500 TPD DRI Kilns)

Indian 5,75,000 SECL / MCL By rail /sea/ road (through covered trucks)

Imported 3,54,000 Indonesia / South Africa /

Australia

Through sea route / by road

Dolomite 16,600 Local area By road (through covered trucks)

For manufacturing of Sinter

Iron ore fines 1008000 Karnataka / Odisha


Limestone fines 10080 CG / MP By rail & road (through covered trucks)

Flux 20160 Bhilai (CG) By rail & road (through covered trucks)

Coke breeze 90720 SECL Korba By rail & road (through covered trucks)

BF fines 100800 In house gen. through covered conveyors

Flue dust 27216 In house gen. through covered conveyors

Return fines 403200 In house gen. through covered conveyors

For manufacturing of Pig Iron

Iron ore lump 454500 Karnataka / Odisha


BF coke 453600 In house gen. through covered conveyors

Quartzite 18900 CG / MP region By rail & road (through covered trucks)

Sinter 756000 In house gen. through covered conveyors

Manganese ore 11340 MOIL, Maharashtra


For Generation of Power through Pulverized Coal Fired boiler [330 MW]

Coal Indian 17,74,600 SECL / MCL By rail /sea/ road


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Raw Material Quantity

(TPA) Sources Mode of Transport

(through covered trucks)

Imported 10,87,000 Indonesia / South Africa /

Australia

Through sea route / by road

For Oxygen plant

Air 400 MT ---- ----

1.3 Manufacturing Process

1.3.1 Sponge Iron (DRI)

Refractory lined rotary kilns will be used for reduction of iron ore in solid state. A central

Burner located at the discharge end will be used for initial heating of the kiln.

Iron ore will be continuously fed into the kiln along with coal which has dual role of fuel as

well as reductant. Dolomite will be added to scavenge the sulphur from the coal. A

number of air tubes will be provided along the length of the kiln. The desired temperature

profile will be maintained by controlling the volume of the combustion air through these

tubes. The Carbon monoxide generated due to the combustion of coal, reduces the iron

ore and converts it into sponge iron. The rotary kiln is primarily divided into two zones viz.

the pre heating zone and the reduction zone. The preheating zone extends over 30 to 50

% of the length of the kiln and in this the moisture in the charge will be driven off and the

volatile matter in the coal will be burnt with the combustion air supplied through the air

tubes. Heat from the combustion raises the temperature of the lining and the bed surface.

As the kiln rotates, the lining transfers the heat to the charge. Charge material, pre-heated

to about 10000C enters the reduction zone. Temperature of the order of 10500C will be

maintained in the reduction zone, which is the appropriate temperature for solid state

reduction of iron oxide to metallic iron.

This hot material will be transferred to Heat exchanger. In Heat exchanger the material

will be cooled to 1600C. The cooler discharge material consists of sponge iron lumps,

sponge iron fines and char. Magnetic and non-magnetic material will be separated through

magnetic separators and stored in separate bins. The hot flue gases will be taken to a

Waste Heat Recovery Boilers and after heat recovery they will be treated in high efficiency


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ESP and discharged into the atmosphere through stack whose height will be in accordance

with CPCB norms.

1.3.2 Sinter Plant

The proposed sinter plant complex will consist of one sinter Machine of suitable grate area

along with associated services facilities. The sinter plant is rated for a total production of

10,08,000 TPA of BF Sinter.

1.3.3 Blast Furnace

The blast furnace shop will comprise of furnace of capacity 1 x 2160 TPD. The blast furnace

is envisaged to operate with sized lump Pellets, coke, fluxes and additives. The hot metal

produced will be cast at pig casting machines to produce cold pigs. The liquid slag will be

granulated at cast house granulation unit. The BF top gas will be cleaned in dust catcher

and gas cleaning system and distributed to the stoves, burners for runner drying, boilers

for process and process steam supply. The surplus gas will be utilized for power

generation. 30 MW power will be generated with BF gas.

1.3.4 Power Generation

1.3.4.1 Through WHRB Boiler

The hot flue gases from DRI kilns will pass through waste heat recovery Boilers to recover

the heat and to generate 2 x 15 MW electricity. The gases after heat recovery will pass

through ESPs and then discharged through chimneys into the atmosphere for effective

dispersion of emissions into the atmosphere.

1.3.4.2 Through PCF Boiler

The concept of burning coal that has been pulverized into a fine powder stems from the

belief that if the coal is made fine enough, it will burn almost as easily and efficiently as a

gas. The feeding rate of coal according to the boiler demand and the amount of air

available for drying and transporting the pulverized coal fuel is controlled by DSC / PLC.

Pieces of coal will be crushed between balls or cylindrical rollers that move between two

tracks or "races." The raw coal will then be fed into the pulverizer along with air heated to

about 343oC from the boiler. As the coal gets crushed by the rolling action, the hot air dries

it and blows the usable fine coal powder out to be used as fuel. The powdered coal from

the pulverizer is directly blown to a burner in the boiler. The burner mixes the powdered


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coal in the air suspension with additional pre-heated combustion air and forces it out of a

nozzle similar in action to fuel being atomized by a fuel injector in modern cars. Under

operating conditions, there is enough heat in the combustion zone to ignite all the

incoming fuel. 330 MW of power will be generated.

1.3.4.3 Through Blast furnace

The blast furnace gas coming-out from the furnace will be used as fuel for stoves, Ladle.

Any excess gas will be let to Sinter Plant as fuel. A total of 30 MW will be generated by

utilizing flue gases from blast furnace.

1.4 Water Requirement

The water requirement for expansion project will be 2090 m3/day. This includes Make-up

water for DRI, Sinter Plant, Blast Furnace, PCF based Power Plant, Oxygen plant and

Domestic water.

A reservoir is envisaged in the proposed expansion project. Water required for the

expansion project will sourced from this reservoir. It is also envisaged to draw the water

from Ground water source. Air cooled condenser are proposed instead of water cooled

condenser to reduce water consumption significantly. The following is the break-up of the

water requirement for proposed project.

WATER REQUIREMENT (For Expansion)

S.No. Units Water requirement (m3/day)

1. Sponge iron 50

2. Blast furnace + Sinter plant 1510

3. Power Plant (WHRB) 70

4. Power Plant (Pulverized Coal Fire boiler)

330

5. Oxygen plant 120

6. Domestic 10

Total 2090

Total water requirement after the expansion will be 767 m3/day + 2090 m3/day =

2857m3/day


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1.4 Waste Water Generation

There will be no effluent generation in the DRI plant, Sinter plant & Oxygen plant as closed

circuit cooling system will be adopted. Effluent from Gas cleaning plant of Blast Furnace

will be treated in a settling tank and after treatment it will be recycled. Effluent from

power plant will be treated and after ensuring compliance with TNPCB norms, it will be

reused in the Blast furnace, dust suppression in CHP, ash conditioning, slag granulation and

for greenbelt development. Sanitary waste water will be treated in septic tank followed by

sub-surface dispersion trench.

The following will be the total wastewater & it’s break-up.

WASTE WATER GENERATION (Expansion)

S.No. Source Generation (m3/day)

1. GCP effluent from Blast Furnace 160 (to be recycled)

2. Power Plant

a) Boiler blowdown 11

b) Cooling tower blowdown Nil (No cooling tower)

c) D.M. plant regeneration water 8

3. Sanitary Wastewater 8

Total 187

Total wastewater generation after expansion project will be 878 m3/day + 187 m3/day =

1065 m3/day.

1.5 Wastewater Characteristics

Characteristics of Sanitary Waste Water (Untreated)

PARAMETER CONCENTRATION

pH 7.0 – 8.5

BOD 200 – 250 mg/l

COD 300 – 400 mg/l

TDS 800 – 900 mg/l

CHARACTERISTICS OF BOILER BLOWDOWN


pH 9.5 – 10.5

TDS 1000 mg/l

CHARACTERISTICS OF DM PLANT REGENERATION



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pH 5 – 10

TDS 5000 – 6000 mg/l

CHARACTERISTICS OF GCP BLOWDOWN (Untreated)


pH 7.5 – 8.0

SS 350 mg/L

TDS 600

2.0 DESCRIPTION OF ENVIRONMENT

Base line data has been collected on ambient air quality, water quality, noise levels, flora

and fauna and socio economic details of people within 10 km radius of the plant.

2.1 Ambient air quality

Ambient air quality was monitored for PM2.5, PM10, SO2, NOx & CO at 9 stations including

project site during December 2013 to February 2014 and subsequently during 7th May

2015 to 6th June 2015 also as per TOR letter issued by MoEF. The following are the

concentrations of various parameters at the monitoring stations:

Baseline data Period - December 2013 to February 2014

Parameter Concentration

PM2.5 : 22.8 to 51.8 g/m3

PM10 * : 38.2 to 86.5 g/m3

SO2 : 9.8 to 23.9 g/m3

NOX : 10.6 to 31.7 g/m3

CO : 550 to 1130 g/m3

* PAH in PM10 were analyzed and their concentrations at all monitoring Stations are Below

Detectable Level.

Baseline data Period - 7th May 2015 to 6th June 2015

Parameter Concentration

PM2.5 : 25.5 to 52.9 g/m3

PM10 * : 39.6 to 88.2 g/m3

SO2 : 10.8 to 25.6 g/m3

NOX : 12.5 to 32.8 g/m3

CO : 630 to 1250 g/m3

* PAH in PM10 were analyzed and their concentrations at all monitoring Stations are Below

Detectable Level.


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2.2 Water Quality

2.2.1 Surface Water Quality

Arani River is flowing at distance of 3.4 Kms. from the plant site. Two nos. of Surface water

samples have been collected, one from upstream & other on downstream of Arani River

w.r.t the project site to assess surface water quality during February 2014 and

subsequently in May 2015. The analysis of samples shows that all the parameters are in

accordance with BIS-2296 specifications.

2.2.2 Ground Water Quality

8 No. of ground water samples from open wells / bore wells were collected from the

nearby villages to assess ground water quality impacts during February 2014 and

subsequently in May 2015 and analyzed for various Physico-Chemical parameters. The

analysis of samples shows that all the parameters are in accordance with BIS: 10500

specifications.

2.3 Noise Levels

Noise levels were measured at 5 locations during day time & Night time. The noise levels at

the monitoring stations are ranging from 46.9 dBA to 67.5 dBA during December 2013 to

February 2014 and 46.8 dBA to 68.9 dBA during 7th May 2015 to 6th June 2015.

3.0 ANTICIPATED ENVIRONMENTAL IMPACTS AND MITIGATION MEASURES

3.1 Prediction of impacts on air quality

The likely emissions from the proposed project are PM10, SO2, NOx & CO. The predictions

of Ground level concentrations have been carried out using Industrial Source Complex (ISC-

3) model. Meteorological data such as wind direction, wind speed, max. and min.

temperatures collected at the site have been used as input data to run the model.

The predicted max. Incremental rise in PM concentration (24 hourly) will be 1.4 g/m3 at a

distance of 1700 m from the origin stack in the down wind direction over the baseline

concentrations due to the proposed expansion project.


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The predicted max. Incremental rise in SO2 concentration (24 hourly) will be 17.9 g/m3 at

a distance of 1700 m from the origin stack in the down wind direction over the baseline

concentrations.

The predicted max. Incremental rise in NOx concentration (24 hourly) will be 6.9 g/m3 at a

distance of 1700 m from the origin stack in the down wind direction over the baseline

concentrations.

Net Resultant maximum concentrations due to the Proposed Project

Item PM

(g/m3)

SO2

(g/m3)

NOX

(g/m3)

Maximum average baseline conc. in the study area

(collected during 7th May 2015 to 6th June 2015) 78.2 25.6 32.8

Maximum predicted incremental rise in concentration

due to the proposed expansion project 1.4 17.9 6.9

Maximum predicted incremental rise in concentration

due to the other Industries in the study area. 0.7 4.2 1.8

Net resultant concentrations during operation of the

plant 80.3 47.7 40.5

National Ambient Air Quality Standards 100 80 80

The predicted results show that the net resultant concentration (max. baseline conc. +

max. incremental rise in conc.) of PM10, SO2, and NOx will be well within the National

Ambient Air Quality Standards after commissioning of proposed expansion project. Hence

there will not be any adverse impact on air environment due to the proposed expansion

project.

3.2 Prediction of impacts on noise quality

The major sources of noise generation in the proposed project will be STG, boilers,

compressors, DG set, etc. Acoustic enclosures will be provided to the STG. The ambient

noise levels will be within the standards prescribed by MoEF vide notification dated 14-02-

2000 under the Noise Pollution (Regulation & Control), Rules 2000 i.e. the noise levels will

be less than 75 dBA during day time and less than 70 dBA during night time. 54.0 acres

(inclusive of existing) of extensive greenbelt will be developed to further attenuate the


Executive Summary

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noise levels. Hence there will not be any adverse impact due to noise on population in

surrounding areas due to the proposed project.

3.3 Prediction of impacts on Water Environment


circuit cooling system will be adopted.

Effluent from Gas cleaning plant of Blast Furnace will be treated in a settling tank and after

treatment it will be recycled. Effluent from power plant will be treated and after ensuring

compliance with TNPCB norms, it will be reused in the Blast furnace, dust suppression in

CHP, ash conditioning, slag granulation. Sanitary waste water will be treated in septic tank

followed by sub-surface dispersion trench.

A reservoir will be built in the low lying area. Water required for the expansion project will

sourced from this reservoir. It is also envisaged to draw the water from Ground water

source and Arani river.

Hence there will not be any adverse impact on environment due to the proposed project.

3.4 Prediction of Impacts on Land Environment

The effluent will be treated to achieve TNPCB standards. Zero effluent discharge will be

adopted. All the required air pollution control systems will be provided to comply with

CPCB / TNPCB norms. All solid wastes will be disposed / utilized as per CPCB / TNPCB

norms. 54.0 Acres (inclusive of existing) of greenbelt will be developed as per guidelines.

Hence there will not be any adverse impact on land environment due to the proposed

project.

3.5 Socio - Economic Environment

There will be lot of opportunities in employment to local people during construction as

well as in operation phase. There will be further upliftment in Socio Economic status of the

people in the area. Hence there will be further development of the area due to the

proposed expansion project.


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4.0 ENVIRONMENTAL MONITORING PROGRAMME

Post project monitoring will be conducted as per the guidelines of TNPCB and MoEF are

tabulated below:

MONITORING SCHEDULE FOR ENVIRONMENTAL PARAMETERS

S.No. Particulars Frequency of Monitoring

Duration of sampling

Parameters required to be monitored

1. Water quality

Water quality in the area

Once in a month except for heavy metals which

will be monitored on quarterly basis.

Composite sampling (24 hourly)

As per IS: 10500

2. Air Quality

A. Stack Monitoring Online monitors (WHRB, PCF boiler

stacks) Once in a month

--- PM

PM, SO2 & NOx

B. Ambient Air quality Twice a week 24 hours continuously

PM2.5, PM10, SO2 & NOx

C. Fugitive emissions Once in a Month 8 hours PM

3. Meteorological Data

Meteorological data to be monitored at the plant.

Daily Continuous monitoring

Temperature, Relative Humidity, rainfall,

wind direction & wind speed.

4. Noise level monitoring

Ambient Noise levels Twice in a year Continuous for 24 hours with 1-hour

interval

Noise levels

5.0 ADDITIONAL STUDIES

No Rehabilitation and Resettlement is involved in the proposed project. Hence no R & R

study has been carried out.

6.0 PROJECT BENEFITS

With the establishment of the proposed project employment potential will increase. Land

prices in the area will increase. The economic status of the people in the area will improve

due to the proposed project. Periodic medical checkups will be carried out. Top priority will

be given to locals in employment.


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7.0 ENVIRONMENT MANAGEMENT PLAN

7.1 Air Environment

The following are air emission control systems proposed in the proposed project:

S.No. Source Control Equipment Guaranteed Outlet

Dust Emission

1. Sinter Plant Electro Static Precipitators (ESP) < 50 mg / Nm3

2. Blast Furnace Dust catcher followed by

venturi scrubber < 10 mg/Nm3

3. PCF boiler based Power Plant Electro Static Precipitators (ESP) < 50 mg / Nm3

4. DRI with WHRB Electro Static Precipitators (ESP) < 50 mg / Nm3

The following air pollution control systems/ measures are proposed in the Plant:

All conveyors will be completely covered with G.I. sheets to control fugitive dust.

All bins will be totally packed and covered so that there will not be any chance for dust

leakage.

All the dust prone points material handling systems will be connected with de-dusting

system with bag filters.

All discharge points and feed points, wherever the possibility of dust generation is there a

de-dusting suction point will be provided to collect the dust.

The emissions from sinter plant will be treated in a High efficiency ESP to bring down the

particulate matter in the exhaust gas to less than 50 mg/Nm3 & then discharged into the

atmosphere through a stack of 40 m height.

The flue gases from MBF will be treated in a dust catcher followed by venturi scrubber and

the treated gases will be discharged into the atmosphere through stack of 50 m height.

The hot waste flue gases from the DRI kilns will pass through Waste Heat Recovery Boilers

and after heat recovery the gases will be treated in High efficiency ESPs to bring down the

particulate emission in the exhaust gases to below 50 mg/Nm3 and then discharged into

the atmosphere through a Combined stack of 92 m height for 2 x 500 TPD DRI Kilns.

The flue gases from the PCF boiler will be treated in a high efficiency Electrostatic

Precipitator to bring down the particulate emission to less than 50 mg/Nm3 and will be


Executive Summary

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discharged through a stack of 146 m height for effective dispersion of emissions into the

atmosphere.

7.2 Water Environment


circuit cooling system will be adopted.

Effluent from Gas cleaning plant of Blast Furnace will be treated in a settling tank and after

treatment it will be recycled. Effluent from power plant will be treated and after ensuring

compliance with TNPCB norms, it will be utilized for dust suppression, ash conditioning and

for greenbelt development.

Effluent Treatment Plant:

pH of the boiler blowdown will be between 9.5 to 10.5. Hence a neutralization tank will be

constructed for neutralizing the boiler blow down. DM plant regeneration water will be

neutralized in a neutralization tank. After neutralization these two effluent streams will be

mixed with Cooling Tower blowdown in a Central Monitoring Basin (CMB). The treated

effluent will be utilized for dust suppression, ash conditioning and for Green belt

development. No effluent will be let out of the plant premises. Hence Zero discharge

concept will be implemented. Sanitary waste water will be treated in septic tank followed

by sub-surface dispersion trench.

7.3 Noise Environment

The major sources of noise generation in the proposed project will be STG, boilers,

compressors, DG set, etc. Acoustic enclosure will be provided. All the machinery will be

manufactured in accordance with MoEF norms on Noise levels. The employees working

near the noise generating sources will be provided with earplugs. The extensive greenbelt

development proposed within the plant premises will help in attenuating the noise levels

further. Noise barriers in the form of trees are recommended to be grown around

administrative block and other utility units.


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7.4 Land Environment

The waste water generated from the proposed expansion project will be treated in the

Effluent Treatment Plant to comply with the TNPCB standards and will be used for dust

suppression, ash conditioning and for greenbelt development. All the required Air emission

control systems will be installed and operated to comply with TNPCB norms. Solid wastes

will be disposed off as per norms. Extensive greenbelt will be developed in the plant

premises. Desirable beautification and landscaping practices will be followed. Hence there

will not be any impact due to the proposed expansion project.

Solid waste generation and disposal

S.No Waste Quantity (TPD)

Method of disposal

1. Ash from DRI 407 Is being given (for existing) to Cement Plants & Brick manufacturers. The same practice will be continued after expansion.

2. DoloChar 330 Will be used in FBC boiler as fuel

3. MBF, FES, ESP & Bag filter dust (inclusive of existing)

20 ESP, Bag filter dust will be partly used in sinter plant and the remaining will be given to brick manufacturers in the nearby area.

4. Kiln Accretion Slag 1.1 Will be used in road construction

5. Granulated slag 150 Will be given to cement manufacturer

6. GCP Sludge 0.2 Will be used in sinter plant

7. Ash from Power Plant (with Indian coal)

2662 Will be given to Cement Plants & Brick manufacturers.

8. Ash from Power Plant (with Imported coal)

362 Will be given to Cement Plants & Brick manufacturers.

7.5 Greenbelt Development

Greenbelt of 54.0 acres (inclusive of existing) will be developed in the proposed project.

Capital cost for environment protection for the total project is Rs. 19.0 Crores.

7.6 Implementation of CREP Recommendations

All the CREP recommendations will be strictly followed.

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suryadev alloys & power pvt. ltd....expansion of steel plant suryadev alloys & power pvt....

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