DOCUMENT

FOR

PUBLIC HEARING

OF

MINI BLAST FURNACE PROJECT

M/S JIWANLAL JAIN

AT VILLAGE- NATHIYA NAWAGAON

DISTT. : KANKAR

STATE : CHHATTISGARH

PROPONENT

JIWANLAL JAIN

LODHA NIWAS

BASTAR ROAD DHAMTARI 493 773

STATE CHHATTISGARH

FEBRUARY 2008

C O N T E N T S

Sr.

No.

Particulars Page No.

1. Executive summary of Environmental for

Public hearing in English

2. Executive summary of Environmental for

Public hearing in Hindi

3. Annexures of above documents

4. Consent application under Air Act 1981,

Water Act 1974 & hazardous waste (M &

H) Rules 1989 As amended in 2003

EXECUTIVE SUMMARY

Introduction :

Shri Jiwanlal Jain, proprietor, is presently operating. Iron ore mines /

transportation / civil construction works etc.

To meet the enlarged demand of pig iron M/s Jiwanlal Jain has decided to

establish a mini blast furnace plant of 42,000 tons per annum capacity.

Indian steel making capacity comprises of output from both integrated and

mini steel plants. However, in the recent years, mini blast furnace is

commonly known as pig iron playing leading role in India being substitute

of melting scrap for electric/induction furnace. The mini blast furnace

technology based on coke make it viable alternative for processing a wide

range of iron ores with coke. In respect of high-grade iron ore deposits these

are well spread over the country.

The problems facing the mini steel industry are mainly scrap availability,

high cost power, escalating cost of the inputs etc. Under various

circumstances, it is natural to think of captive blast furnace units to cater to

the individual mini steel plant.

It is easy to exploit a production unit of this nature to its full potential. It is

also easy to incorporate energy saving techniques in stages without much

financial outlay. Particular emphasis has been laid on the technical and

technological aspects and profitability of operation of this unit.

.. 1 ..

BLAST FURNACE PROJECT – AT A GLANCE

Product PIG IRON

End-user Steel Industry

Capacity 42,000 tons per annum

Process Type BLAST FURNACE

Location VILL NATHIYA NAWAGOAN DIST

KANKER– (C.G.)

Implementation period 08 months

Total Plant Area 3.04 ha land

Raw Material Through

Rail/ Transport

Iron Ore from Kanker / NMDC Bailadila,

imported coke /own iron ore mine at

Barbaspur.

Consumption of Raw Material

(P.A)

(TPA)

1. IRON ORE 67200

2. COKE 29400

3. QUARTIZITE 1470

4. MANGANESE 19800

5. LIMESTONE 6300

6. DOLOMITE 6300

Manpower Requirement 60

Power Requirement 1250 KW Installed

Capital Cost Rs. 2000.00 lakhs

Debt – Equity Ratio 2 : 1

Term Loan from Commercial Bank Rs. 1400 lakhs

Equity Rs. 600 lakhs

Average Sales Rs. 6893 lakhs per annum

Net Profit before tax Rs. 603 lakhs per annum

.. 2 ..

Selection of site

Selection of suitable site for the proposed Blast furnace Plant is governed by

following factors:

• Proximity to raw materials

• Proximity to consuming centers

• Availability of infrastructure facilities like land, power, water,

communication etc.

M/s Jiwanlal Jain propose to use iron ores from Kanker region, imported and

Indian coke, limestone, dolomite and manganese from the local market. All

the raw materials viz., iron ore and coke, limestone, dolomite, manganese

etc. are available in reasonable proximity distance and the place of the site is

well connected by road and rail to the raw material sources. Kanker district

is one of the industrially backward in Chattisgarh. Various Govt incentives

are ailable for industry coming up in industrially backward state like

Chattisgarh. The Proposed unit will be first in its kind in Chattisgarh and in

Kanker district. Keeping above in view the proposed site would be an ideal

location for setting of proposed blast furnace plant. Location is shown in

Figure 1.

.. 3 ..

FIGURE 1

LOCATION OF THE PLANT

.. 4 ..

PROJECT SITE

Manufacturing Process

The proposed plant will produce pig iron in a conventional blast furnace as being

employed in all the integrated steel plants like Bhilai, Bokaro, Rourkela, Kalinga iron

etc. Granulated slag is a by-product from this plant, which is gainfully sold to cement

plant for cement making.

In the blast furnace iron making process, weighed quantities of lump iron ore, coke,

limestone, dolomite, manganese ore and quartzite are charged from the top at

predetermined rate. Hot air blast at 10000C (preheated in stoves) is blown into the

furnace from the bottom through Bnos nozzles (tuyeres) equally spaced around the

furnace. The hot coke reaching at this level from the top reacts with O2 of hot air and

generates heat and carbon mono-oxide. The gas thus generated rises upwards and

reacts with iron oxide of iron ore and form iron which melts in the lower zone and

collects in the lowest part called hearth. The SiO2 and Al2O3 of iron ore and coke ash

combine with CaO and MgO of limestone and dolomite to form slag which becomes

molten at lower part and floats on the top of metal bath. Mn ore is added to control

sulphur in metal. Quartzite is added to maintain requisite composition of Al2O3 in the

slag. Molten metal and slag are tapped out periodically. Molten metal is casted in pig

casting machine to form solid pig iron which is sold. Water is sprayed on the machine

for cooling. Return water is collected and after make-up, it is re-circulated for cooling

by two pumps (1W + 1R) of 65 m3/hr employed for Pre Casting Machine (PCM)

cooling.

.. 5 ..

Slag granulation unit is located adjoining the furnace. High-pressure water is sprayed

across the flow of liquid slag thus solidifying and granulating the slag. The slag-water

mix falls in a tank from where the slag settles and water flows to the adjoining tank

containing clarified water. Requisite make up water is added in this tank and water is

pumped back for granulation. Two pumps of 210 m3/hr (55KW), one working and

one reserve are employed for the system. The granulated slag is scooped by grab

from the 1st tank and loaded in the trucks for dispatch.

Blast furnace is cooled by water spray. Spray water is supplied by 350 m3/hr pump

(1W + 1R) of 55 KW each located in a pump house. Water after cooling collects in

the channel led to a underground tanks. Overflow of this tank is collected in the

adjoining tank which has the suction of the pumps. Make up water is added in the

suction tanks and re-circulated in the system.

The blast furnace charging system, with two bells operating in sequence ensure gas

fight-ness and does not allow any leakage of gas from furnace to the atmosphere.

The gases from the furnace are fed to a dust catcher where coarser particle of dust get

separated. The dust from dust catcher is withdrawn periodically through a dust valve

and disposed off (later to be used in sinter making). The semi-cleaned gas from dust

catcher is led to a gas cleaning plant constituting a two stage venturi scrubber and a

moister separator. Two pumps (1W+1R) of 90 m3/hr each (10 KW) are provided for

supply of water to the above gas cleaning plant. The clean water overflows the

clarifier and after adding make up water is pumped back in the system.

.. 6 ..

The thick sludge from the bottom of the clarifier is pumped to a concrete bed 10 m x

20 m. The bed is in two parts i.e. 5 m x 20 m each and is provided with a slope. At

any time, one bed is in use and the other is in reclamation of sludge. At the end of bed

is provided a gravel screen which allows clear water to be collected in the basin

below. The soldiered sludge is reclaimed and dumped in a specified location within

the premises for later use in sintering.

The cleaned gas from cleaning plant is used in stoves where the gas is burnt and the

heat is utilized for pre heating of air to 10000C.The product of combustion after pre

heating the air passes to atmosphere through a 30 m high chimney. Any surplus gas is

burnt in a surplus gas burner at 30 m high support structure using LPG for flame

stabilization.

All above systems are convectional and will be adopted in the proposed mini blast

furnace. Process flow chart is shown in Figure 2 and plan layout is given in

Figure 3.

.. 7 ..

FIGURE 2

PROCESS FLOWCHART

.. 8 ..

FIGURE 3

PLAN LAYOUT

.. 9 ..

Baseline environmental quality

Baseline environmental quality in core and buffer zones was verified in order to

facilitate assessment of degree of alterations / impacts due to proposed Mini Blast

Furnace and has been described in this chapter. Environmental quality is normally

described in terms of (i) ambient air quality in core and buffer zones, (ii) water

environment, (iii) present land use, (iv) fauna and flora in the region and (v) social &

economic status of the area.

Ambient air quality monitoring

Air quality prevailing in core and buffer zones is dependent on (a) micrometeorology

particularly the wind direction and speed, (b) types and emissions from mobile and

fugitive sources. A survey of the area has shown that there are no stationary sources.

Mobile sources are the trucks/tippers carrying iron ore from adjoining mining areas.

Fugitive sources are roads on which vehicles move. Air quality monitoring stations

were selected as per the prevailing wind directions. Ambient air quality at these

stations was monitored during Nov 2007 to January 2008 as per CPCB norms.

Ambient air quality data is given Annexure 1.

Air sampling stations are described below :

SAMPLING

CODE

SAMPLING STATIONS DIRECTION DISTANCE

(km)

A1 Proposed Site -- --

A2 Village Nathiya Nawagaon N 3.0

A3 Village Bagodar ENE 3.5

A4 Village Makri Singari SE 3.0

A5 Village Makrikhuna S 2.0

A6 Village Matwada SSW 3.5

A7 Village Maladobari WSW 3.5

A8 Village Pandarwahi WNW 2.5

.. 10 ..

Wind pattern at the site during monitoring period is depicted as a 16-point wind rose

in Figure 5.

FIGURE 5

.. 11 ..

WIND ROSE AS RECORDED DURING MONITORING PERIOD

OF AAQ

Air emissions

Emissions will be as under

a) Gas volume 19,000 Nm3 / d

b) Pressure 20 – 50 K pa

c) Temperature 100 – 250 0C, max. 400

0C

Control

a) Gravity dust catcher

b) Bag type gas cleaning plant (GCP)

Noise levels:

There is no precise source of noise at the proposed site. The only source of noise is

the vehicular movement on the nearest NH 43. During the operation of the proposed

mini blast furnace the noise levels will not exceed 90 dBA and workers will be

protected by using ear plug. Also control and recreation room will be provided in

front of BF with sound proof doors & windows.

Water Quality:

Eight ground and surface water samples were collected for physic-chemical analysis.

Samples collected for metal content were acidified (1ml HNO3). Sample for

bacteriological analysis were collected in sterilized glass bottles. Parameters analyzed

at the site are pH, temperature, odour, turbidity and dissolved oxygen. Physico-

chemical and bacteriological parameters in respect of the surface water and

groundwater are given Annexure 2.

.. 12 ..

Water requirement:

m3/day

� Blast furnace cooling 8400

� Pig casting machine 1560

� Granulation unit 5040

� Gas scrubbing 2160

� Make up water 10,000

� Losses 7,160

Wastewater generation will be occasional and it will be used for plantation.

Domestic water consumption 1.5

Discharge to septic tank followed by soak pit 1.2

.. 13 ..

Soil Characteristics

Soil samples were collected from the proposed site and its characteristics are given

below :

Proposed site soil sample Sr.

No.

Parameters Unit

0-30

cm

30-60

cm

60-90

cm

I PHYSICAL PROPERTIES

Particle Size Distribution

Gravel % 92 93 93

Sand % 58 54 51

Silt % 26 33 37

1.

Clay % 16 13 12

2. Texture Sandy

loam

Sandy

loam

Sandy

loam

3. Bulk density g/cm3 1.4 1.5 1.5

4. Permeability mm/hr 36.5 34.8 30.5

5. Available water retention

capacity

i. 1/3 bar

ii. 15 bar

%

%

30.2

14.7

32.7

15.8

33.8

16.2

II CHEMICAL PROPERTIES

1. pH 6.8 6.4 6.1

2. Elect. Conductivity mS/cm 0.23 0.20 0.18

3. CEC meq/100g 25.3 27.8 28.6

4. Exchangeable (Ca+Mg) meq/100g 15.7 17.9 17.4

5. Exchangeable (K) meq/100g 1.56 1.64 1.8

6. Organic Carbon % 1.29 1.26 1.25

7. Available Nitrogen kg/ha 155 146 140

8. Available Phosphorus kg/ha 3.1 3.9 4.2

9. Available Potassium kg/ha 338 400 442

.. 14 ..

Land use:

Total project area is 3.04 ha. Out of which only 0.8 ha area is required for the mini

blast furnace. The detailed land use pattern is given in following table:

Utilities Area (ha)

Plant area 0.8

Raw material yard 0.5

Finish goods 0.4

Internal roads 0.3

Green Belt 1.04

Total 3.04

Socio-economics:

Total population in the core and buffer zone is 34652 souls. The schematic

representation of population is given below:

..15 ..

Employment will be given to 60 local persons to be engaged in productive activity.

Environmental Impact and management

Sr.

No.

Emissions Quantity Control/ Disposal

1. Air Gas volume 19000 Nm3/day

(PM will be ≤ 10 mg/Nm3,

SO2 ≤ 5 mg/Nm3)

(Cleaned gas is reused for

heating)

• Dust catcher

• Bag type GCP (gas cleaning

plant)

• Venturi scrubber

• Cyclonic moisture separator.

2. Liquid

waste

Occasional since zero

discharge has been provided • Use for plantation

3. Solid

waste

Nil since all material from

scrubbers and blast furnace

will be sold.

• For sinter and cement.

4. Noise Will not exceed 90 dBA in

furnace house . Noise levels

will not be more than 75 dBA

beyond the plant limit.

• Personal protection equipment

will be provided.

• Control and worker recreation

room in front of BF will be

equipped with sound proof

doors & windows.

5. Socio-

economic

aspects

Employment to 60 local

persons to be engaged in

production activity.

• Gradual industrialization at

small scale will improve QOL

(quality of life)

.. 16 ..

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FIGURE 1111

LOCATION OF THE PLANT

21

PROJECT SITE

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22

FIGURE 2 2 2 2

PROCESS FLOWCHART, 23

FIGURE 3 3 3 3

PLAN LAYOUT

24

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Control A Gravity Dust Catcher B Bag Type Gas cleaning Plant /ofu i;kZoj.k 1- v/;;u {ks= esa 8 ijos”kh /ofu dh tkap dh xbZ A 2- jgoklh {ks=ksa rFkk laosnu”khy {ks=ksa esa /ofu dk Lrj 36-51 vkSj 37-45Msflcy ds chp jgkA

25

tyh; i;kZoj.k 1-ikuh ds xq.koRrk ds vkadyu gsrq ikuh ds uewus 8 LFkuksa ls yh xbZ ftlesa 2 uewus lrgh ty vkSj 6 gSaM iaiksa rFkk dqvksa ls yh xbZ A ikuh ds bu uewuksa dk fQftdks dsfedy] cSDVhfj;ksykftdy vkSj ck;ksykftdy xq.koRrk dh tkWap dh xbZ a 2- lrgh vkSj Hkwry ty ds fQftdks dsfedy ewY; lHkh uewuksa ds ewY; ekud Lrj ls de ik;s x;s gS A ikuh dh mi;ksfxrk & 1- CykLV Qjusl dwfyax & 8400 cum/d 2- fix dkfLVax e”khu & 1560 cum/d 3- xzsuqys”ku ;wfuV & 5040 cum/d 4- xsl Ldzfcax & 2160 cum/d 5- esdi okVj & 10000 cum/d 6- yklsl & 7160 cum/d 7- ?kjsyw mi;ksx & 1-5 cum/d 8- lsfIVd VSad esa fMLpktZ & 1-2 cum/d Hkwfe dk i;kZoj.k &

1- v/;;u {ks= ls uewus fy,s x;s ,oa mudk fo”ys’k.k HkkSfrd & jlk;fud fLFkfr iqf’Vdj fLFkfr ]otuh /kkrq ,oa lw{e tSfod fLFkfr gsrq fd;k x;k A

2- feV~Vh dh lajpuk nqeV ls fpduh nqeV]cYd ?kuRo 1-4&1-5 g/m3 fNfnzyrk

30-5&36-5 izfr”kr ikuh Fkkeus dh {kerk 14-7 ,oa 33-8 izfr”kr A

3- lkekU; feV~Vh & lkekU; {kkj ls gYdk vEyh; feV~Vh (pH 6.1-6.8)28.6 meg/100g.

4- iqf’Vdj fLFkfr % la?kfVr dkcZu & e/;e fo”ks’krk (1.25-1.29%)laiw.kZ

ukbVªkstu (140-155kg/ha)QkLQksjl (3.1-4.2kg/ha),oa iksVsf”k;e (338-442kg/ha)

26

lkekftd ,oa vkfFkZd i;kZoj.k v/;;u {ks= dk tu lkaf[;dh <kapk tula[;k & 34253 Male16985-49.39 % Female 17264 50. 41% vuwlwfpr tkfr & 5.25% - vuwlwfpr tutkfr 51.37% izkstsDV {ks= ,oa mlds vklikl esa jgus okys vkfnokfl;ks dh tula[;k jk’Vªh; vkSlr ls vf/kd gS A vkfFkZd fo”ks”krk % df̀’k eq[; O;olk;] ou mRiknksa dk laxzg.k ,oa ou mRikn ij fuHkZj A LokLFk fLFkfr & dqiks’k.k ]vuqi;qDr LoPNrk A lkaLd`frd ,oa lkSna;Zcks/kh fo”ks”k’krk% vkfnoklh fof/k& fo/kku ,oa R;ksgkj lkekftd ,oa vkfFkZd losZ T;knkrj yksxksa dks bl izkstsDV ds ckjs esa tkudkjh ugah gS A dkadsj esa gh ydM+h ]feV~Vh rsy ,oa ,y-ih-th- xSl miyC/k gS A Hkwfe mi;ksfxrk % ifj;kstuk esa dqy Hkwfe dk mi;ksx 3-04 gsDVs;j gS foLrr̀ Hkwfe mi;ksx tkudkjh uhps n”kkZbZ xbZ gS A mi;ksx {ks=Qy ¼gsDVs-½ la;a= 0-8 dPpkeky j[kko 0-5 rS;kj eky 0-4 okfudh 1-04 jkLrk ¼?kjsyw½ 0-3 dqy 3-04

27

Ik;kZoj.k izHkko ,oa vkadyu ,oa izca/ku dzekad izHkko vkadyu Izkac/ku 1- gok 19000 Nm3/d

(pm<10mg/nm3) (so2 <5mg/nm3) lkQ gok dks okil mi;ksx esa fy;k tk;sxk

MLV dspj cSx Vkbi xSl Dyhfuax IykaV osupqjh Ldzcj

2- ikuh thjks fMLpktZ okfudh dk;Z esa mi;ksx fd;k tk;sxk

3- lksfyM osLV

lEiw.kZ eky dh fczdh dh tkrh gS lhesaV m|ksx dks

4- /ofu 90 dBA ls de IykaV ds vanj ,oa 75 dBA A ls de IykaV ds ckgj

dkexkjksa dks ilZuy izksVsD”ku bDohieasV¼bZ;j Iyx ½ fn;k tk;sxk

5- lkekftd ,oa vkfFkZd

60 yksxksa dks jkstxkj dk volj vkS|ksfxd dj.k ls jkstxkj feyus ij /khjs&/khjs thou Lrj esa lq/kkj

28

A

N

N

E

X

U

R

E

S

ANNEXURE 1

AMBIENT AIR QUALITY DATA

A1 – Proposed site

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

01-11-07 95.3 57.4 6.3 7.5 W1

05-11-07 122.1 67.2 6.4 8.0

08-11-07 118.3 69.9 5.8 7.6 W2

12-11-07 92.7 57.7 6.7 7.3

15-11-07 88.9 57.5 6.1 7.5 W3

19-11-07 119.7 72.8 6.0 7.8

22-11-07 116.3 82.2 5.9 8.4 W4

26-11-07 90.7 66.5 4.8 6.8

29-11-07 95.3 59.5 6.2 7.2 W5

03-12-07 81.0 62.6 6.4 7.5

06-12-07 99.5 56.6 6.7 6.9 W6

10-12-07 89.2 62.6 6.2 7.6

13-12-07 101.5 59.6 5.8 8.1 W7

17-12-07 117.1 58.5 6.0 7.8

20-12-07 104.2 61.3 5.9 7.2 W8

24-12-07 89.0 68.6 6.3 8.1

27-12-07 121.8 62.1 5.3 7.5 W9

31-12-07 95.6 58.3 6.1 7.3

03-01-08 103.1 78.5 4.8 7.6 W10

07-01-08 125.5 63.3 5.3 8.2

10-01-08 116.7 60.3 5.8 7.8 W11

14-01-08 91.2 75.3 6.4 6.7

17-01-08 119.5 77.5 6.2 7.4 W12

21-01-08 95.6 59.0 4.9 8.2

24-01-08 96.2 75.5 5.5 7.6 W13

28-01-08 108.8 59.3 6.2 7.9

Minimum 81.0 56.6 4.8 6.7

Maximum

125.5 82.2 6.7 8.4

Average 102.8 65.0 5.9 7.6

98 Percentile 123.8 80.4 6.7 8.3

.. 30..

ANNEX. 1 : CONTD

A2 – Nathiya Nawagaon

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

01-11-07 91.5 61.3 5.8 6.8 W1

05-11-07 107.1 68.6 6.0 7.2

08-11-07 94.2 62.1 5.9 7.5 W2

12-11-07 79.0 58.3 6.3 6.9

15-11-07 111.8 78.5 5.3 7.6 W3

19-11-07 85.6 63.3 6.1 8.1

22-11-07 93.1 60.3 4.8 7.8 W4

26-11-07 115.5 75.3 5.3 7.2

29-11-07 112.1 77.5 5.8 8.1 W5

03-12-07 108.3 59.0 6.4 7.5

06-12-07 82.7 75.5 6.2 7.3 W6

10-12-07 78.9 59.3 4.9 7.6

13-12-07 109.7 74.6 5.5 6.8 W7

17-12-07 106.3 58.4 6.2 7.2

20-12-07 114.3 64.2 6.0 7.2 W8

24-12-07 108.4 71.9 5.4 8.6

27-12-07 118.6 81.2 7.2 8.3 W9

31-12-07 121.1 87.8 6.9 7.4

03-01-08 101.5 76.4 5.9 6.2 W10

07-01-08 105.7 71.1 5.7 6.4

10-01-08 121.2 68.8 6.3 7.1 W11

14-01-08 124.6 79.2 7.1 7.8

17-01-08 117.7 67.3 6.5 6.9 W12

21-01-08 116.4 65.2 6.7 7.4

24-01-08 105.6 68.0 5.8 6.4 W13

28-01-08 118.7 74.6 6.2 6.8

Minimum 78.9 58.3 4.8 6.2

Maximum

124.6 87.8 7.2 8.6

Average 105.8 69.5 6.0 7.3

98 Percentile 122.9 84.5 7.2 8.5

.. 31 ..

ANNEX. 1 : CONTD

A3 – Bagodar

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

01-11-07 80.4 66.5 6.0 7.5 W1

05-11-07 97.7 59.5 5.9 7.8

08-11-07 96.5 62.6 4.8 8.4 W2

12-11-07 103.7 56.6 6.2 6.8

15-11-07 86.5 62.6 6.4 7.2 W3

19-11-07 102.1 59.6 6.3 7.5

22-11-07 89.2 58.5 6.4 6.9 W4

26-11-07 74.0 61.3 5.8 7.6

29-11-07 116.8 68.6 6.7 8.1 W5

03-12-07 80.6 62.1 6.1 7.8

06-12-07 88.1 58.3 6.0 7.2 W6

10-12-07 110.5 78.5 5.9 8.1

13-12-07 103.3 63.3 4.8 7.5 W7

17-12-07 77.7 60.3 6.2 7.3

20-12-07 73.9 75.3 6.4 7.6 W8

24-12-07 104.7 65.4 6.7 8.2

27-12-07 101.3 58.7 6.2 6.8 W9

31-12-07 75.7 68.4 5.8 7.2

03-01-08 107.4 71.3 6.4 7.5 W10

07-01-08 114.6 59.4 6.0 6.9

10-01-08 109.3 53.4 6.2 7.5 W11

14-01-08 103.4 76.4 5.9 6.8

17-01-08 106.9 73.8 7.1 7.6 W12

21-01-08 99.3 77.6 6.8 6.7

24-01-08 93.9 69.0 6.4 6.4 W13

28-01-08 100.6 74.6 5.6 7.1

Minimum 73.1 53.4 4.8 6.4

Maximum

114.6 78.5 7.1 8.4

Average 95.3 65.4 6.1 7.4

98 Percentile 112.6 78.1 7.0 8.3

.. 32 ..

ANNEX. 1 : CONTD

A4 – Makri Singari

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

02-11-07 113.6 62.6 4.8 7.8 W1

06-11-07 116.1 56.6 5.3 7.2

09-11-07 96.5 62.6 5.8 8.1 W2

13-11-07 100.7 59.6 6.4 7.5

16-11-07 116.2 58.5 6.2 7.3 W3

20-11-07 119.6 61.3 4.9 7.6

23-11-07 112.7 68.6 5.8 6.8 W4

27-11-07 111.4 62.1 6.0 7.2

30-11-07 100.6 62.1 5.1 7.2 W5

04-12-07 113.7 58.3 6.3 8.6

07-12-07 100.6 78.5 5.6 8.3 W6

11-12-07 87.8 63.3 5.9 7.4

14-12-07 98.8 60.3 6.3 6.2 W7

18-12-07 90.3 75.3 5.3 6.4

21-12-07 97.8 77.5 6.1 7.1 W8

25-12-07 93.6 59.0 4.8 7.8

28-12-07 95.6 75.5 5.3 7.2 W9

01-01-07 100.7 59.3 5.8 6.8

04-01-08 106.1 74.6 6.4 6.9 W10

08-01-08 92.6 58.4 6.2 7.2

11-01-08 93.2 68.7 4.9 7.6 W11

15-01-08 90.2 66.9 5.5 6.8

18-01-08 109.6 68.3 6.2 6.7 W12

22-01-08 107.6 67.8 6.0 7.5

25-01-08 90.7 59.8 5.4 8.1 W13

29-01-08 104.1 72.4 7.2 7.9

Minimum 87.7 56.6 4.8 6.2

Maximum

119.6 78.5 7.2 8.6

Average 101.8 65.3 5.8 7.4

98 Percentile 117.9 78.0 6.8 8.5

.. 33 ..

ANNEX. 1 : CONTD

A5 – Makrikhuna

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

02-11-07 111.8 68.6 6.7 6.8 W1

06-11-07 85.6 62.1 6.1 7.2

09-11-07 93.1 58.3 6.0 7.5 W2

13-11-07 115.5 78.5 5.9 6.9

16-11-07 108.3 63.3 4.8 7.5 W3

20-11-07 82.7 60.3 6.2 6.8

23-11-07 78.9 75.3 6.4 7.6 W4

27-11-07 109.7 68.3 5.8 6.7

30-11-07 106.3 67.8 6.3 6.4 W5

04-12-07 114.3 59.8 6.7 7.1

07-12-07 108.4 72.4 4.8 7.8 W6

11-12-07 118.6 58.3 5.3 7.2

14-12-07 121.1 78.5 5.8 8.1 W7

18-12-07 101.5 63.3 6.4 7.5

21-12-07 105.7 60.3 6.2 7.3 W8

25-12-07 121.2 75.3 4.9 7.6

28-12-07 124.6 77.5 5.8 6.8 W9

01-01-07 117.7 59.0 6.0 7.2

04-01-08 116.4 64.2 5.1 7.2 W10

08-01-08 105.6 68.3 6.1 7.2

11-01-08 118.7 72.1 6.0 7.5 W11

15-01-08 122.5 76.3 5.9 6.9

18-01-08 107.7 57.4 4.8 7.5 W12

22-01-08 100.8 59.1 6.2 6.8

25-01-08 103.4 68.2 6.3 6.7 W13

29-01-08 118.8 61.3 6.1 7.4

Minimum 78.9 57.4 4.8 6.4

Maximum

124.6 78.5 6.7 8.1

Average 107.3 66.7 5.9 7.2

98 Percentile 123.6 78.5 6.7 8.0

.. 34 ..

ANNEX. 1 : CONTD

A6 – Matwada

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

02-11-07 110.6 68.4 4.8 7.8 W1

06-11-07 104.6 72.3 5.3 7.2

09-11-07 113.4 76.4 5.8 8.1 W2

13-11-07 120.6 81.0 6.4 7.5

16-11-07 113.6 75.4 6.2 7.3 W3

20-11-07 116.1 73.8 4.9 7.6

23-11-07 96.5 68.2 5.8 6.8 W4

27-11-07 100.7 67.9 6.0 7.2

30-11-07 116.2 76.3 5.1 7.2 W5

04-12-07 119.6 80.2 6.1 7.2

07-12-07 112.7 79.1 4.8 8.1 W6

11-12-07 111.4 74.6 5.3 7.5

14-12-07 100.6 69.8 5.8 7.3 W7

18-12-07 113.7 65.7 6.4 7.6

21-12-07 100.6 62.1 6.2 6.8 W8

25-12-07 113.7 58.3 4.9 7.2

28-12-07 100.6 78.5 5.5 7.2 W9

01-01-07 87.8 63.3 6.2 8.6

04-01-08 98.8 60.3 6.0 8.3 W10

08-01-08 90.3 75.3 5.4 7.4

11-01-08 97.8 77.5 7.2 6.2 W11

15-01-08 93.6 59.0 7.4 6.4

18-01-08 113.6 68.4 6.9 7.1 W12

22-01-08 116.4 65.3 6.7 7.8

25-01-08 103.4 73.6 6.5 7.2 W13

29-01-08 116.2 64.8 7.1 8.4

Minimum 87.8 58.3 4.8 6.2

Maximum

120.6 81.0 7.4 8.6

Average 106.3 70.6 6.0 7.4

98 Percentile 120.1 80.6 7.3 8.5

.. 35 ..

ANNEX.12 : CONTD

A7 – Maladobari

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

03-11-07 108.6 59.6 6.4 7.2 W1

07-11-07 111.9 58.5 6.2 7.5

10-11-07 106.8 61.3 4.9 6.8 W2

14-11-07 92.5 68.6 5.8 7.8

17-11-07 98.8 62.1 6.0 7.2 W3

21-11-07 96.7 62.1 5.1 8.1

24-11-07 104.8 58.3 6.3 7.5 W4

28-11-07 89.3 78.5 5.6 7.3

01-12-07 101.1 74.6 6.4 6.9 W5

05-12-07 87.6 58.4 6.2 7.2

08-12-07 88.2 68.7 4.9 7.6 W6

12-12-07 85.2 66.9 5.5 6.8

15-12-07 104.6 68.3 6.2 6.7 W7

19-12-07 102.6 67.8 6.0 7.5

22-12-07 85.7 59.8 5.4 8.1 W8

26-12-07 99.1 72.4 7.2 7.9

29-12-07 95.6 62.1 5.8 6.4 W9

02-01-07 108.7 58.3 6.4 7.1

05-01-08 95.6 78.5 5.9 7.8 W10

09-01-08 82.8 63.3 4.8 7.8

12-01-08 93.8 60.3 5.3 7.2 W11

16-01-08 85.3 75.3 5.8 8.1

19-01-08 92.8 77.5 6.4 7.5 W12

23-01-08 88.6 59.0 6.2 7.3

26-01-08 116.4 68.4 4.9 7.6 W13

30-01-08 108.6 70.2 5.8 6.8

Minimum 82.8 58.3 4.8 6.4

Maximum

116.4 78.5 7.2 8.1

Average 97.4 66.1 5.8 7.4

98 Percentile 114.2 78.5 6.8 8.1

.. 36 ..

ANNEX. 1 : CONTD

A8 – Pandarwahi

SPM RPM SO2 NOx Week Date

µg/m3 µg/m

3 µg/m

3 µg/m

3

03-11-07 106.1 74.6 6.4 6.9 W1

07-11-07 92.6 58.4 6.2 7.2

10-11-07 93.2 68.7 4.9 7.6 W2

14-11-07 90.2 66.9 5.5 6.8

17-11-07 109.6 68.3 6.2 6.7 W3

21-11-07 107.6 67.8 6.0 7.5

24-11-07 90.7 59.8 5.4 8.1 W4

28-11-07 104.1 72.4 7.2 7.9

01-12-07 113.7 58.3 5.9 7.8 W5

05-12-07 100.6 78.5 6.3 7.2

08-12-07 87.8 63.3 5.3 8.1 W6

12-12-07 98.8 60.3 6.1 7.5

15-12-07 90.3 75.3 4.8 7.3 W7

19-12-07 97.8 77.5 5.3 6.9

22-12-07 93.6 59.0 5.8 7.2 W8

26-12-07 95.6 75.5 6.4 7.6

29-12-07 100.7 59.3 6.2 6.8 W9

02-01-07 106.1 74.6 4.9 7.3

05-01-08 116.3 72.7 5.5 7.6 W10

09-01-08 114.3 68.2 6.2 6.8

12-01-08 103.4 71.6 6.0 7.2 W11

16-01-08 112.4 61.3 5.4 7.2

19-01-08 104.7 75.2 7.2 7.2 W12

23-01-08 103.4 77.6 6.8 8.2

26-01-08 113.3 72.5 7.5 7.8 W13

30-01-08 99.4 70.5 6.7 6.8

Minimum 87.8 58.3 4.8 6.7

Maximum

116.3 78.5 7.5 8.2

Average 101.8 68.8 6.0 7.4

98 Percentile 115.3 78.1 7.4 8.2

.. 37 ..

ANNEXURE 2

WATER QUALITY

Source of sample : W1 : Chhinar river at village Makrikhuna

W2 : Sendur river at village Gaurgaon

W3 : Bore-well water at proposed site

W4 : Handpump water at village Pandarwahi

Sr.

No.

Parameters Unit W1 W2 W3 W4

1. Temperature 0C 27.5 27.2 28.0 28.0

2. Colour Hazen Clear Clear Clear Clear

3. Odour UO UO UO UO UO

4. Taste AG AG AG AG AG

5. DO mg/L 5.6 5.7 1.3 1.2

6. pH 8.1 7.9 7.3 7.2

7. Conductivity µS 120 130 295 272

8. Turbidity NTU 5.0 4.5 < 1 < 1

9. Total dissolved solids mg/L 84 91 177 158

10. Total suspended solids mg/L 4 5 5 3

11. Total Alkalinity as CaCO3 mg/L 83 89 144 138

12. Total Hardness as CaCO3 mg/L 70 75 130 119

13. Ca Hardness as CaCO3 mg/L 52 56 85 72

14. Mg Hardness as CaCO3 mg/L 18 19 45 47

15. Chlorides as Cl mg/L 15 20 6.0 10

16. Sulphates as SO4 mg/L 10 12 2.5 4

17. Fluoride as F mg/L 0.4 0.5 0.7 0.6

18. Iron as Fe mg/L 0.4 0.3 2.5 2.8

19. Copper as Cu mg/L BDL BDL BDL BDL

20. Zinc as Zn mg/L Traces Traces BDL BDL

21. Manganese as Mn mg/L BDL BDL BDL BDL

22. Total Coliforms MPN/100ml 150 240 0 0

23. Cadmium as Cd mg/L BDL BDL BDL BDL

24. Lead as Pb mg/L BDL BDL BDL BDL

25. Chromium as Cr mg/L BDL BDL BDL BDL

26. Arsenic as As mg/L BDL BDL BDL BDL

27. Pestisides mg/L Absent Absent Absent Absent

.. 38 ..

ANNEX. 2 : CONTD

WATER QUALITY

Source of sample : W5 : Handpump water at village Nathiyanawagaon

W6 : Handpump water at village Matwada

W7 : Handpump water at village Makri Singari

W8 : Handpump water at village Bagodar

Sr.

No.

Parameters Unit W5 W6 W7 W8

1. Temperature 0C 27.5 27.2 28.0 28.0

2. Colour Hazen Clear Clear Clear Clear

3. Odour UO UO UO UO UO

4. Taste AG AG AG AG AG

5. DO mg/L 1.4 1.2 1.3 1.4

6. pH 7.6 7.4 7.3 7.6

7. Conductivity µS 276 291 285 264

8. Turbidity NTU < 1 < 1 < 1 < 1

9. Total dissolved solids mg/L 186 112 170 160

10. Total suspended solids mg/L 2 4 4 3

11. Total Alkalinity as CaCO3 mg/L 144 160 131 149

12. Total Hardness as CaCO3 mg/L 112 128 122 126

13. Ca Hardness as CaCO3 mg/L 76 88 79 79

14. Mg Hardness as CaCO3 mg/L 36 40 43 47

15. Chlorides as Cl mg/L 1 5 7 12

16. Sulphates as SO4 mg/L 2 5 3 3

17. Fluoride as F mg/L 0.5 0.6 0.4 0.6

18. Iron as Fe mg/L 1.3 0.8 2.4 2.1

19. Copper as Cu mg/L BDL BDL BDL BDL

20. Zinc as Zn mg/L BDL BDL BDL BDL

21. Manganese as Mn mg/L BDL BDL BDL BDL

22. Total Coliforms MPN/100ml 0 0 0 0

23. Cadmium as Cd mg/L BDL BDL BDL BDL

24. Lead as Pb mg/L BDL BDL BDL BDL

25. Chromium as Cr mg/L BDL BDL BDL BDL

26. Arsenic as As mg/L BDL BDL BDL BDL

27. Pestisides mg/L Absent Absent Absent Absent

.. 39 ..

ANNEXURE 3