executive summary of eia report (english) · effluent from each individual unit would be collected...

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EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) of M/S. GUJARAT HYDROCARBONS AND POWER SEZ LIMITED GIDC – VILAYAT (VAGRA) INDUSTRIAL ESTATE, VILAYAT, TAL : VAGRA, DIST : BHARUCH, GUJARAT

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Page 1: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

EXECUTIVE SUMMARY OF EIA REPORT

(ENGLISH)

of

M/S. GUJARAT HYDROCARBONS AND POWER SEZ LIMITED

GIDC – VILAYAT (VAGRA) INDUSTRIAL ESTATE,

VILAYAT, TAL : VAGRA, DIST : BHARUCH, GUJARAT

Page 2: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

EXECUTIVE SUMMARY OF EIA

INTRODUCTION

• The SEZ going to be developed by Gujarat Hydrocarbons and Power SEZ Limited (GHPSL) is amongst the first dedicated Hydrocarbon SEZ in India.

• GHPSL proposes to develop the sector specific SEZ project with both foreign and domestic investors as financial or technical collaborators to the project. However, these investors will be introduced into the project on a need basis, depending upon requirements of the project.

• GHPSL, 100% subsidiary of Assam Company, is setting up India’s first integrated Hydrocarbon in the most investor friendly state Gujarat in India. GHPSL is conceived as One stop “world class” integrated sector specific SEZ for providing products and related services addressing the entire range of Hydrocarbons value and supply chain. GHPSL is designed to exploit the massive unfolding opportunities in this fastest growing sector of the Indian economy addressing the mismatch between the demand and supply. The project intends to attract investors in this unique Special Economic Zone project which will entitle them to several fiscal incentives. Infrastructure availability including power, water, natural gas, effluent treatment, etc. will provide the required impetus.

• GHPSL has acquired land and received formal approval for SEZ, Petroleum hydrocarbon. The operations are expected to commence in 2012, aiding a quantum jump in India’s Hydrocarbon infrastructure.

• SEZ is situated in Bharuch near Dahej which is the hub of Oil & Gas and Chemicals. The SEZ also falls within the boundary of PCPIR (Petroleum, Chemical & Petro‐chemicals Investment Region), are well connected with Road (National Highway), Railway (Delhi‐Mumbai Rail Line), Airport (National Airport at Vadodara 80 Km and International Airport at Ahmedabad, 180 Km), nearest All‐weather port‐ Dahej. These SEZ also falls onto the link of Dedicated Freight Corridors (DFC) a mega project started by Govt. of India, with collaboration from JICA (Japanese International Collaboration Agency) for augmenting to Dedicated High Speed Rail Link between Delhi and Mumbai.

• Any Petroleum hydrocarbon industry service that will support industry in the SEZ for manufacturing, stocking, trading including logistics and utilities with local linkages, and for which site is available as per the approved detailed Master Plan, will be eligible for being set up in the PCPIR.

• GHPSL has also signed MOUs with Gujarat Maritime Board and Gujarat Industrial Development Corporation for setting up Fabrication yard and Shipyard. GHPSL plans to facilitate export activities of the SEZ by adding their own captive jetty.

• The Company is actively scouting for right partners who wish to leverage the state‐of‐art infrastructure and facilities.

DETAILS OF PROJECT SITE

Page 3: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

The SEZ going to be developed by Gujarat Hydrocarbons and Power SEZ Limited (GHPSL) is amongst the

first dedicated Hydrocarbon SEZ in India GHPSL proposes to develop the sector specific SEZ project with

both foreign and domestic investors as financial or technical collaborators to the project. However,

these investors will be introduced into the project on a need basis, depending upon requirements of the

project. It will be set up on Plot No. of Ind. Estate of Vilayat, Dist: Bharuch (Guj).

Sr. No. Location Survey No.

1

Village:Vilayat, Taluka: Vagra,

District: Bharuch

459

2 460

3 461

4 462

5 463/P

6 464/P

7 465

8 466/P

9 467

10 468

11 469

12 470

13 471/P

14 472/P

15 473/P

16 474

17 475

18 476

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19 477/P

20 478/P

21 479/P

22 Cart‐Tract.

23 480

24 481

25 482/P

26 483/P

27 484/P

28 485/P

29 486/P

30 487/P

31 488

32 489

33 490

34 491

35 492

36 493

37 494

38 495/P

39 497/P

40 498/P

41 499/P

42 500/P

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43 501

44 502

45 503

46 504

47

Village:Vilayat, Taluka: Vagra,

District: Bharuch

505

48 506

49 507

50 508

51 509

52 510

53 511

54 512

55 513

56 514/P

57 515

58 516/P

59 517/P

60 518/P

61 519

62 520

63 521/P

64 522/P

65 523/P

66 524/P

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67 525/P

68 526/P

69 527/P

70 528/P

71 529/P

72 530

73 531

74 532

75 533/P

76 534/P

77 535/P

78 536/P

79 537/P

80 538

81 539

82 540

83 541/P

84 542/P

85 543/P

86 544/P

87 545

88 546

89 547/P

90 548/P

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91 549/P

92 550/P

93

Village:Vilayat, Taluka: Vagra,

District: Bharuch

553

94 554

95 555

96 Cart‐Tract.

97 556/P

98 557

99 558

100 559

101 560

102 561

103 562

104 563

105 564

106 565

107 566

108 567

109 568

110 569

111 570

112 571

113 572

114 573

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115 574

116 575

117 576

118 577

119 578

120 579

121 580

122 594

123 595

124 596

125 597

126 598

127 599

128 600

129 601

130 Cart‐Tract.

131 602

132 603

133 604

134 605

135 606

136 607

137 608

138 609

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139

Village:Vilayat, Taluka: Vagra,

District: Bharuch

610

140 611

141 612

142 613

143 614

144 615

145 616

146 624

147 625

148 626

149 628

150 629

Locational Advantage

• Bharuch is located in the southern part of Gujarat, near the Gulf of Khambhat in Arabian Sea. • Dahej Port, operated by Gujarat Maritime Board (GMB), has made significant contribution to

facilitate industrial growth in the district. • Excellent port connectivity with the presence of Dahej port makes it an investment destination

in port & shipbuilding activities. • Centrally located within the industrial belt, Dahej is an ideal location in Asia to serve north, west

and central India and international destinations such as, Middle East, Africa, Europe and North America.

• The district has a large number of industrial estates and Special Economic Zones (SEZs).

Area falling within the zone of proposed PCPIR (Petroleum, Chemical & Petro Chemical

Investment Region.

Page 10: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

PLANNED ACTIVITIES

• Total Area of SEZ is 140 Hectares.

• To be developed over phases

• Propose to set up Sector Specific Special Economic Zone for Petroleum Hydrocarbon in Vilayat

Industrial Estate, Taluka: Vagra, Dist: Bharuch, Gujarat.

Break‐up of the Industries:

Total Petroleum Hydrocarbon Plant: 10

Fabrication Unit: 1

CETP: 1 & STP: 1

Incinerator: 1

Page 11: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

DISTRIBUTION OF SEZ

Zone Total Area (Ha) %

Hydrocarbons SEZ

Non‐Processing (Logistic Park, Parking facility, Colony, Restaurant,

Pumping Station, Weight Bridge, Custom Office, road and

Infrastructure Corridor, etc.)

24 17.00

Green Belt 46 33.00

Carbon Black Units 2 1.43

PTA Units 18 12.86

Dual Feed Petrochemical complex, Ethylene Oxide derivatives – MEG etc,

Polyethylene derivatives, n‐Butanol, Propylene derivatives, Polypropylene,

Para Xylene & Ortho Xylene, PET, Styrene,

Specialty Chemicals/Refinery Catalysts/Synthetic,

Lubricant/products, R & D/ Laboratory Testing Service

47 33.56

CETP, Common Incinerator 3 2.15

Total 140 100

PROJECT COST FOR DEVELOPMENT OF SEZ

Total estimated cost of the project will be Rs. 975 Cr. (Proposed).

• Cost of Development Rs.94 Crores

• Cost for ready built infrastructure – Rs.800 Crores

Page 12: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

• Cost of project management, water treatment plant, Sewage/ Effluent Collection,

Transportation, Incinerator, Treatment & Reuse, Storm Water Harvesting system & Fire

fighting system – Rs.68 Crores

• The annual budget for the EMP ( operational phase ) – Rs. 13 Crores

Page 13: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

Effluent Management System

• There will be facility for common effluent treatment plant (CETP).

• Effluent collection and disposal system of 1.2 Million liters per day (MLD), Primary, secondary

treatments to be done by individual units.

• Developer will be provided the guard pond to check the characteristic of treated effluent after

primary and secondary treatment by individual Industries at least once in day. There will be

available online monitoring facility (pH meter, Flow meter & TOC meter) to check the characteristic

of effluent.

• The effluent after secondary treatment at individual units will be transferred to the common

effluent treatment plant through tankers; this will help in maintaining check on the quality as well as

quantity of effluent intake to CETP. Each industry would be required to have collection tanks

separately to store high TDS effluents and another to store low TDS effluent and same for High COD

stream. The process effluents having high COD & TDS (0.060 MLD) will be sent to own common

incinerator.

• The final treated effluent will be discharged into already installed GIDC effluent disposal pipeline for

deep sea disposal near Dahej. So that there will be no risk of contamination of soil or ground water.

• A CETP is proposed inside the SEZ. The treatment of the effluent will be on segregation basis.

Effluent from each individual unit would be collected and transported to CETP. The effluent would

be divided in three categories:

• The treatment of the effluent will be on segregation basis. The effluent will be divided in three

categories:

1. Process Effluent Primary & Secondary Treatment given by Individual Industries CETP GIDC

Drainage pipeline.

2. The non‐biodegradable process effluent (high COD & TDS) own Common Incinerator.

3. Domestic waste water Common STP Reused for green belt development and Flushing and any

surplus quantity will be discharged into GIDC Drain.

• The utilities effluent having low COD after secondary treatment will be disposed into the sea

through effluent disposal line, after meeting GPCB norms. All other effluents after secondary

treatment at respective industries will be collected through tankers to the CETP. The bio‐degradable

process effluents will be subjected to aerobic treatment and after meeting the disposal standards

Page 14: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

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Page 15: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

The domestic & sewage effluent will be collected through pipeline and treated in common STP and

Treated Domestic waste water (600 KL/Day) shall be reused for green belt development and Flushing

after treatment and any surplus quantity will be discharged in GIDC sewage drain. During raining season,

after treatment of domestic waste water shall be discharged into GIDC sewage drain line.

Flow Diagram of Common STP:

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Diagram of Common Incinerator:

Solid & Hazardous Waste Management System

• Wastewater (domestic & commercial) to be treated in STP & CETP to be setup. Thereafter, the

same will be pumped to GIDC Effluent Pipeline.

• Hazardous wastes generated by units will be required to be treated and disposed as per MoEF/

GPCB/ HWM guidelines. Individual member units shall dispose the waste by themselves.

• Hazardous waste (ETP Suldge, Spent Carbon, etc.) will be disposed at nearest TSDF site at M/s.

BEIL, Ankleshwar or M/s. NECL, Nandesari or proposed TSDF site at M/s. BEIL, Dahej.

• Hazardous waste (Organics Residues, Process Waste, Spent Catalyst, etc.) will be disposed at

Common Incinerator Site in Proposed SEZ.

During the operation phase of the proposed SEZ solid wastes, having non hazardous as well as

hazardous nature would be generated from the various industrial units of SEZ.

Hazardous Wastes:

Organic residues from process.

Process wastes, spent carbon,

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ETP sludge from individual unit & CETP

Used oil

Non‐Hazardous Wastes:

Fly ash from boilers (including bottom ash)

Domestic waste from canteen & greenery wastes

Recyclable waste ‐ paper, card boards, scrap, etc.

DETAILS OF HAZARDOUS WASTE GENERATION & DISPOSAL

Sr.No. Type of waste Category Quantity

Disposal

1. ETP Sludge 34.4 80 MT/Day Disposal to TSDF site at M/s.

BEIL, Ankleshwar/Dahej or M/s.

NECL, Nandesari.

2. Ash ‐‐ 20 MT/Day Selling to Bricks Manufacturing

Unit.

3. Used Oil 5.1 4 Liters/Day Selling to GPCB registered

reprocessor.

4 Discarded

Containers/Bags

33.3 500 Nos./Day Sold to authorize Vendor after

decontamination.

ENERGY & FUEL REQUIREMENT

• Primary source of Energy will be Electricity from Gujarat State Electricity Corporation Limited

(GSECL)/ Gujarat Electricity Board (GEB) supplied through transmission lines of Gujarat Energy

Transmission Corporation Limited (GETCO).

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Power will be available from GETCO sub‐station (220/66 KVA) and transmission lines located near

site.

Power will be available from GHPSL‐Power Plant.

Requirement of fuel during development stage would be minimal for running of

construction machineries (Mixer, Crusher, etc), if required.

BASELINE ENVIRONMENTAL STATUS

1. AIR ENVIRONMENT

The dispersion of pollutants in the atmosphere is a function of several meteorological parameters viz.

temperature, wind speed and direction, mixing depths, inversion level, etc. The ambient air samples

were collected and analyzed for Suspended Particulate Matter (SPM), Respirable Suspended Particulate

Matter (RSPM), Sulphur Dioxide (SO2), Oxides of Nitrogen (NOx), Hydrocarbons(HC), Carbon Monoxide

(CO) and VOC for identification, prediction, evaluation and assessment of potential impact on ambient

air environment. A number of models have been developed for the prediction of pollutant

concentration at any point from an emitting source.

AMBIENT AIR QUALITY MONITORING AND POLLUTION CONTROL MEASURES

The ambient air quality monitoring was carried out in accordance with guidelines of Central

Pollution Control Board (CPCB) and National Ambient Air Quality Standards (NAAQS) of CPCB.

Ambient Air Quality Monitoring (AAQM) was carried out at eight locations during post monsoon

season from October 1, 2009 to December 31, 2009.

The arithmetic mean and 98th percentile values of 24 hourly SPM at all the locations ranged

between 74 – 94 µg/m3 and 79.6 – 97.6 µg/m3 respectively. Similarly, the arithmetic mean and

98th percentile values of RSPM varied in the range of 38 – 55 µg/m3 and 44.6 – 58.7 µg/m3,

respectively. The SPM and RSPM concentrations at all the AAQM locations were primarily

caused by local phenomena including vehicular activities and natural dust getting air borne due

to man made activities and blowing wind. SPM and RSPM concentrations were observed below

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stipulated standards of CPCB for industrial and residential area at all air quality monitoring

locations during the winter season.

The arithmetic mean and 98th percentile values of NOx at all the locations ranged between 18

– 30 µg/m3 and 23.3 – 34.4 µg/m3 respectively. The arithmetic mean and 98th percentile

values of SO2 at all the locations were observed to be in the range of 10 – 21 µg/m3 and 13.6 –

25 µg/m3 respectively. At all the ambient air quality monitoring locations, the 98th percentile

values of SO2 and NOx were observed to be within limits. Air Quality Status of CO, HC & VOC at

all the locations were observed BDL.

2. WATER ENVIRONMENT

The baseline water quality status in the region is established by analyzing surface water and ground

water. Water requirement at site would be met through GIDC water supply (surface water). Ground

water resources are predominantly exploited in most of nearby villages only for domestic and

agricultural purposes.

BASELINE GROUND WATER QUALITY

pH of ground water samples varied from 7.80 to 8.38. Turbidity was found to be 0.3 to 0.9 NTU, Total

Dissolved Solids varied in the range of 774 to 1850 mg/L respectively. Nitrate and Total Phosphate was

found in the range of 0.8 to 1.6 mg/L and 0.14 to 0.63 mg/L respectively. DO and COD was found in

range of 7.0 to 7.4 mg/L and 13.6 to < 6 mg/L respectively. BOD3 was found in range of 0.0 to 0.5 mg/L.

Total hardness (as CaCO3) varies from 260.2 to 75.90 mg/L. Calcium hardness (as CaCO3) varies from

63.4 to 190 .3mg/L. Total Alkalinity varied from 250 to 430 mg/L. Chloride and Sulfates was found in the

range of 138 to 985.5 mg/L and 26.38 to 68.9 mg/L. Magnesium Hardness was found in range of 193.1

to 562.7 mg/L. T‐Chromium & H‐ Chromium were found BDL. Sodium was found in the range of 134 to

570 mg/L and zinc was found in the range of BDL – 1.5 mg/L. Copper was found in the range of 25.9 to

76.3 mg/L, Cadmium was found ND. Fluorides were found BDL. Magnesium was found in range of 46.9

to 136.2 mg/L., Total Coliforms is present (range 17 – 34 MPN/ MPN/100 ml). Lead and Selenium were

found BDL.

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BASELINE SURFACE WATER QUALITY

pH of ground water samples varied from 7.91 to 8.14. Turbidity was found to be 5.0 to 5.7 NTU, Total

Dissolved Solids varied in the range of 210 to 360 mg/L respectively. Nitrate and Total Phosphate was

found in the range of 2.3 to 2.8 mg/L and 1.08 to 1.3 mg/L respectively. DO and COD was found in range

of 6.0 to 6.8 mg/L and 12.15 to 26.04 mg/L respectively. BOD3 was found in range of 0.5 to 0.6 mg/L.

Total hardness (as CaCO3) varies from 96.7 to 130 mg/L. Calcium hardness (as CaCO3) varies from 78.4 to

97mg/L. Total Alkalinity varied from 110 to 210 mg/L. Chloride and Sulfates was found in the range of

6.90 to 8.87 mg/L and 6.51 to 17.9 mg/L. Magnesium Hardness was found in range of 18.2 to 18.3 mg/L,.

T‐Chromium & H‐ Chromium was found BDL. Sodium was found in the range of 14 to 20 mg/L and zinc

was found in the range of 0.18– 0.26 mg/L. Copper was found in the range of 0.12 to 0.18 mg/L,

Cadmium was found ND. Fluorides were found BDL. Magnesium was found in the range of 4.4 to 5.4

mg/L., Total Coliforms is present (range 345 – 584 MPN/100 ml). Lead and Selenium were found BDL.

3. NOISE ENVIRONMENT

The objective of the noise pollution survey around the project site was to identify existing noise

sources and to measure background noise levels. The study was carried out in the following

steps:

• Reconnaissance

• Identification of noise sources and measurement of noise levels

• Measurement of noise levels due to transportation

• Community noise levels

BASELINE NOISE LEVEL

The noise level measured in study area at different locations is given in Table 3.8. The noise levels varied

in the study area during daytime [night time] in the range of 40‐42 [35‐37] dB(A) and 42‐48 [38‐45]

dB(A) in industrial and residential area respectively.

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4. LAND ENVIRONMENT

Soil samples were collected from eight different locations during study on Nov. 15, 2009 in the study

area (0‐20 cm depth).

BASELINE STATUS

pH varies from 7.75 to 8.05.WHC varies from 36.6% to 70.5 %. Organic Matter varies from 0.38

% to 1.76 %. Sulphate was found in the range 12 to 22 mg/kg. Chloride varied from 85.5 – 117

mg/kg. Magnesium was found in the range of 23 – 183 mg/kg. Total Organic Carbon varies from

0.30 % to 1.02 %. Total hardness varies from 563.9 to 1409.7 mg/kg, Total alkalinity varies from

800 to 1400 mg/kg, Calcium varies from 75 to 452 mg/kg, Sodium varies from 712 to 1632

mg/kg, Potassium varies from 1746 to 10463 mg/kg, T‐Cr, H‐Cr and Arsenic were found BDL,

Copper varies from 2.4 to 159 mg/kg, Zinc varies from 17.3 to 380 mg/kg, Lead varies from 18

to 380 mg/kg, Iron varies from 6 to 1967 mg/kg and Bulk density varies from 1.1 to 1.3 gm

/cm3.

ENVIRONMENTAL HAZARD

Raw material such as different chemicals, solvents, etc. are transported by road and stored in

the plant premises. On site emergency plan shall be prepared for storage and transfer of

hazardous chemicals and also been submitted to Government of Gujarat. This report shall be

prepared with the consideration of hazards associated with the chemicals and care taken for all

aspects of environmental hazards. The project proponent shall be considered all the safety

aspects in planning, designing and operation of the plant as per standard practices. Hence, no

adverse impact on this account is anticipated. Considering the pollution control measures taken

by the company environment management system adopted there is no significant adverse

impact on environment.

In general, from all the discussion undertaken above and the Environmental Impact Assessment study

carried out in the Post Monsoon season regarding the project, it can be concluded that there will not be

any significant negative impact on environment by M/s. GUJARAT HYDROCARBONS AND POWER SEZ

LIMITED. However, the same will be well within the statutory norms.

Page 22: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •
Page 23: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

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Page 24: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

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J.a[s.p).a[s.a[l. s[kTr Ap[s)f)k s[zni> (vkisn) yi[jni siY[> p\i[j[kT miT[ niNi>k)y tYi T[kn)kl shyi[g) tr)k[ b>n[ Birt)y tYi (vd[S) ri[kiNkiri[n) drKiAt kr[l C[ . ji[ k[, ai ri[kiNkiri[n[ j$(ryit p\miN[ diKl krvi d[vimi> aivS[.

J.a[s.p).a[s.a[l, aisim k>pn)n) 100% sbs)D)yr) C[, j[ Birtni[ si] p\Ym hieD^i[kib<n s[z g&jritmi> AYipvini> C[. g&jrit j[ Birtni[ si]Y) vw& eºv[ATr f[\ºDl) rijy C[. J.a[s.p).a[s.a[l. j[ (vÅvBrmi> si]Y) siri[ Ap[s)f)k s[z AYipvi je rh) C[ j[mi> smg\ hieD^i[kib<n s>b>(wt p\i[DkTs an[ t[n) siY[ ji[Diy[l s[viai[ aipvimi> aiv[ C[. J.a[s.p).a[s.a[l.n) (Dziena[ r)t[ krvimi> aivS[ k[ j[Y) Birtn) eki[ni[m)mi> zDp) (vkis Yiy j[Y) mi>g an[ s¼lieni[ tfivtn[ ¹yinmi> riK)n[ t[ni> s>b>(wt tki[ni[ (vkis krvimi> aivS[. J.a[s.p).a[s.a[l. eµC[ C[ k[ ri[kiNkiri[ ai a[kmi#i s[zmi> aik(P<t Yiy an[ t[mn[ (v(vw niNik)y p\[rNi> p\i¼t Yiy. eºf\iAT^crn) j$(ryit j[v) k[ v)jL), piN), n[crl g[s, p\d*(Pt piN)n) p\(k\yi an[ (nkil (vg[r[ ai p\(k\yin[ aigL vFirvimi> mdd krS[.

J.a[s.p).a[s.a[l.a[ p[T^i[(lym hieD^i[kib<n s[z miT[ jm)n Kr)d[l C[ an[ m>j*r) miT[ je rhy&> C[ ai ai[pr[Sn 2012mi> S$ Yvin) ap[xi C[ j[Y) Birt hieD^i[kib<n x[#in) p\(tAYimi> vwiri[ YS[.

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s[z B$cmi> dh[j nJk aiv[l C[ j[ ai[el an[ g[s t[mj k[(mkln&> m&²y k[ºd^ C[. s[z a[ p)s)p)aieairn) hdmi> aiv[l C[ j[ riÖ^)y wi[r)mig< (d9h)-m&b>eY) 17 k).m)., r[9v[lien-B$cY) 17 k).m)., vDi[dri hviemYkY) 80 k).m). an[ ai>trriÖ^)y hviemYkY) 180 k).m). d*r aiv[l C[. ai s[z Birt srkir an[ jipin)z eºTrn[Snl ki[libi[r[Sn a[jºs) oiri S$ krvimi> aiv[l m[gi p\i[j[kT (d9h) an[ m&>be n[ ji[Dti> D[D)k[T[D f[\Y ki[r)Di[rmi> aivr) l[vimi> aiv[ C[.

s[zmi> aiv[l eºDAT^)z p[T^i[(lym hieD^i[kib<nn&> uRpidn an[ T^[D)>g krt) eºDAT^)z miT[ aiFir$p C[ an[ j[ni miT[ m>j*r Yy[l (vgtvir miATr ¼linmi> sieT upl¾F C[, j[ p)s)p)aieairmi> s&yi[Jt miT[[ pi#i YS[.

J.a[s.p).a[s.a[l.a[ f[b\)k[Sn yiD< an[ S)pyiD<n) AYipni> miT[ g&jrit m[r)Tiem bi[D< an[ g&jrit eºDAT^)yl D[vli[pm[ºT ki[pi[<r[Sn siY[ MOUs sien kr[l C[. J.a[s.p).a[s.a[l. s[zn) (nkis p\vZ(t miT[ pi[tin) k[¼T)v j[Í)n) AYipni krvin) yi[jni kr) rh) C[.

k>pn) rijyn) aiT< eºfi\AT^cr an[ s&(vFini[ liB uqiv) Sk[ t[vi> siri> Big)dirn) tpis kr) rh) C[.

2. p\i[j[kT AYLn) mi(ht): g&jrit hieD^i[kib<ns an[ pivr s[z (l. oiri (vksivimi> aivnir s[z Birtni[ p\Ym hieD^i[kib<n s[z C[. J.a[s.p).a[s.a[l. s[kTr Ap[s)f)k s[zni> (vkisn) yi[jni siY[> p\i[j[kT miT[ niNi>k)y tYi T[kn)kl shyi[g) tr)k[ b>n[ Birt)y tYi (vd[S) ri[kiNkiri[n) drKiAt kr[l C[ . ji[ k[, ai ri[kiNkiri[n[ j$(ryit p\miN[ diKl krvi d[vimi> aivS[. s[zn&. AYL J.aie.D).s)> (vliyt eºDAT^)yl a[AT[T, til&ki: vigri, J9li[: B$c {g&jrit}

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Sr. No. Location Survey No.

1

gim:(vliyt, ti: vigri,

D): B@c

459

2 460

3 461

4 462

5 463/p)

6 464/p)

7 465

8 466/p)

9 467

10 468

11 469

12 470

13 471/p)

14 472/p)

15 473/p)

16 474

17 475

18 476

19 477/p)

20 478/p)

21 479/p)

Page 27: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

22 Cart‐Tract.

23 480

24 481

25 482/p)

26 483/p)

27 484/p)

28 485/p)

29 486/p)

30 487/p)

31 488

32 489

33 490

34 491

35 492

36 493

37 494

38 495/p)

39 497/p)

40 498/p)

41 499/p)

42 500/p)

43 501

Page 28: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

44 502

45 503

46 504

47

gim:(vliyt, ti: vigri,

D): B@c

505

48 506

49 507

50 508

51 509

52 510

53 511

54 512

55 513

56 514/p)

57 515

58 516/p)

59 517/p)

60 518/p)

61 519

62 520

63 521/p)

64 522/p)

65 523/p)

Page 29: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

66 524/p)

67 525/p)

68 526/p)

69 527/p)

70 528/p)

71 529/p)

72 530

73 531

74 532

75 533/p)

76 534/p)

77 535/p)

78 536/p)

79 537/p)

80 538

81 539

82 540

83 541/p)

84 542/p)

85 543/p)

86 544/p)

87 545

Page 30: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

88 546

89 547/p)

90 548/p)

91 549/p)

92 550/p)

93

gim:(vliyt, ti: vigri,

D): B@c

553

94 554

95 555

96 Cart‐Tract.

97 556/p)

98 557

99 558

100 559

101 560

102 561

103 562

104 563

105 564

106 565

107 566

108 567

109 568

Page 31: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

110 569

111 570

112 571

113 572

114 573

115 574

116 575

117 576

118 577

119 578

120 579

121 580

122 594

123 595

124 596

125 597

126 598

127 599

128 600

129 601

130 Cart‐Tract.

131 602

Page 32: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

132 603

133 604

134 605

135 606

136 607

137 608

138 609

139

gim:(vliyt, ti: vigri,

D): B@c

610

140 611

141 612

142 613

143 614

144 615

145 616

146 624

147 625

148 626

149 628

150 629

3. AYLni> fiydi:

• B$c g&jritni> d(xN Big mi> aiv[l C[, j[ arb) sm&omi> aiv[l g9f ai[f K>Bitn) nJk C[.

Page 33: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

• g&jrit m[r)Tiem bi[D< oiri s>ci(lt dh[j pi[T<ni[, J9lini> ai]wi[(gk (vkismi> ni[>Fpi#i fiLi[ ai¼yi[ C[.

• â[Oq pi[T< kn[kT)v)T) siY[ dh[j pi[T<n) hijr)a[, pi[T< an[ S)p(b9D)>g p\vZ(tmiT[ ri[kin&> AYL bniv[ C[.

• ai]wi[(gk b[9T siY[ m¹ymi> aiv[l C[, dh[j a[(Syin) u_ir an[ Birtn) p(Vm an[ m¹ymi> aiv[l a[k aidS< AYL C[. j[m k[ m¹y-p*v< ai(f\ki, y&ri[p an[ u_ir am[(rki.

• J9limi> an[k ai[wi[(gk a[AT[T an[ s[z aiv[li C[.

ai (vAtir s&(ct p)s)p)aieair{p[T^i[(lym, k[(mkl an[ p[T^i[k[(mkl ri[kiN (vAtir }n) hdmi> aiv[l C[.

4. aiyi[Jt p\vZ(tai[:

• s[zni[ k&l (vAtir 140 h[kTr C[. • crN p\miN[ (vkis krvimi> aivS[.

• J.aie.D).s). (vliyt eºDAT^)yl a[AT[T, til&ki: vigri, J9li[: B$c {g&jrit}mi> p[T^i[(lym hieD^i[kib<n miT[ s[kTr Ap[s)f)k s[z AYipvin) drKiAt kr[l C[.

5. eºD^AT)zn&> (vwTn: k&l p[T^i[(lym hieD^i[kib<n y&(nT: 10

f\[b)k[Sn y&(nT: 1

s)>eT)p) -1 an[ a[sT)p) -1

eºs)nr[Tr – 1

Page 34: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

6. s[zni[ jm)n (vAtir: zi[n k&l (vAtir %

hieD^i[kib<n s[z

ni[n p\i[s[s)>g {li[JAT)k pik<, pik)<>g, ki[li[n), r[ATi[rºT, pÀp)>g AT[Sn, v[eT b\)j

kATm ai[(fs an[ eºfi|ATcr ki[r)Di[r} 24 17.00

g\)n b[9T 46 33.00

kib<n ¾l[k y&(nT 2 1.43

p)T)a[ y&(nT 18 12.86

Dual Feed Petrochemical complex, Ethylene Oxide derivatives – MEG etc,

Polyethylene derivatives, n‐Butanol, Propylene derivatives, Polypropylene,

Para Xylene & Ortho Xylene, PET, Styrene,

Specialty Chemicals/Refinery Catalysts/Synthetic,

Lubricant/products, R & D/ Laboratory Testing Service

47 33.56

s)>eT)p) an[ a[sT)p)

eºs)nr[Tr 3 2.15

k&l 140 100

7. s[zni (vkis miT[ p\i[j[kT Kc<:

p\i[j[kT miT[ k&l a>diJt Kc< $. 975 kri[D C[.

• (vkis Kc< $. 94 kri[D

• eºfi|ATcr bnivvini[ Kc< $. 800 kri[D

Page 35: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

• p\i[j[kT s>ciln, piN) S&(okrN, s[v[z S&(okrN, vihnÄyvhir, eºs)nr[Tr, S&(okrN an[

p&n: upyi[g, vi[Tr hirv[AT)>g an[ fiyr fieT)>g - $. 68 kri[D

• pyi<vrN miT[ vi(P<k Kc< $. 13 kri[D

a[f9y&aºT m[n[jm[ºT s)ATm

• ki[mn a[f9y&aºT T^)Tm[ºT ¼liºT miT[n) s&(vFi C[. • 1.2 a[m.a[l.D). a[f9y&aºT a[kQ&> an[ (nkil s)ATm C[, y&(nT oiri p\iY(mk an[ s[kºDr)

T^)Tm[ºT aipvimi> aivS[. • y&(nT oiri p\iY(mk an[ s[kºDr) T^)Tm[ºT ai¼yi pC) D[vli[pr oiri bnivvimi> aiv[l giD<

pi[ºDmi> T^k oiri mi[klvimi> aivS[ jyi> (dvsmi> a[kvir c[k krvimi> aivS[. Ryi> ai[nlien mi[n)>Tr)>g s&(vFi riKvimi> aivS[.

• y&(nT oiri a[f9y&aºTn[ s[kºDr) T^)Tm[ºT ai¼yi pC) T^k oiri s)>eT)p)mi> mi[klvimi> aivS[

jyi> a[f9y&aºTn) g&Nv_ii an[ mi#ii ckisvimi>> aivS[. dr[k y&(nT hie T)D)a[s an[ li[

T)D)a[s a[f9y&aºT miT[ alg kl[kSn T[ºk riKvimi> aivS[ t[mj hie s)ai[D) AT^)m miT[ alg

kl[kSn T[ºk riKvimi> aivS[. hie T)D)a[s an[ hie s)ai[D) {0.06 a[ma[lD)} AT^)mn[

eºs)nr[Trmi> mi[klvimi> aivS[.

• T^)T[D a[f9y&aºT ni[ (nkil J.aie.D).s). a[f9y&aºT D)Api[zl pieplienmi> krvimi> aivS[ j[

dh[j nJk C[. j[Y) jm)n an[ piN) pr ki[e asr krS[ n(h.

• s)>eT)p) s[zmi> s&(ct krvimi> aivS[. a[f9y&aºTn) alg alg AT^)m miT[ alg S&(okrN

p\(k\yi n)c[ m&jb C[.

1. p\i[s[s a[f9y&aºT y&(nT oiri p\iY(mk an[ s[kºDr) T^)Tm[ºT s)>eT)p)

J.aie.D).s). a[f9y&aºT D)Api[zl pieplien

2. hie s)ai[D) an[ hie T)D)a[s eºs)nr[Tr

3. Grg¸Y&> g>d&piN) g\)n b[9Tni> (vkis miT[ an[ fls)>g miT[ t[mj tdupri>t mi#ii

J.aie.D).s). a[f9y&aºT D)Api[zl pieplien

Page 36: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

s)eT)p)

Diyig\im

Page 37: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

a[sT)p)

Grg¸Y&> g>d&piN) pieplien oiri a[kq&> krvimi> aivS[ an[ t[n&> S&(okrN a[sT)p)mi> krvimi> aivS[ an[ S&o piN)ni[ upyi[g g\)n b[9Tni> (vkis miT[ an[ fls)>g miT[ t[mj tdupri>t bik) rh[l piN)ni[ (nkil J.aie.D).s). a[f9y&aºT D)Api[zl pieplienmi> krvimi> aivS[. ci[mis&> dr(myin, S&(okrN bid piN)ni[ (nkil J.aie.D).s). a[f9y&aºT D)Api[zl pieplienmi> krvimi> aivS[.

Page 38: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

eºs)nr[Tr

8. Gn an[ ji[Km) kcri[ni> s>ciln s)ATm: • g>d&piN) {p\i[s[s an[ Grg¸Y&>} n&> S&(okrN s)eT)p) an[ a[sT)p)mi> krvimi> aivS[. • y&(nT oiri uRpºn Yti[ ji[Km) kcrin&> S&(okrN an[ (nkil MoEF/ GPCB/ HWM ni>

FiriFi[rN/mig<dS<n p\miN[ krvimi> aivS[. • ji[Km) kcri[ {eT)p) Alz\ an[ Ap[ºT kib<n, (vg[r[}ni[ (nkil T)a[sD)a[f sieT { M/s. BEIL

aYvi M/s. NECL } pr krvimi> aivS[. • ji[Km) kcri[ {D)AT)l[Sn r[s)Dy&, p\i[s[s v[AT, an[ Ap[ºT kib<n, Ap[ºT k[Til)AT(vg[r[} ni[

(nkil s[z ni> ki[mn eºs)nr[Trmi> krvimi> aivS[.

ji[Km) kcri[

• p\i[s[smi>Y) kib<(nk r[s)Dy& • p\i[s[s v[AT, Ap[ºT kib<n • eT)p) Alz • y&zD\ ai[el

Page 39: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

aji[Km) kcri[

• fliy a[S • Grg¸Y&> kcri[ • p&n: upyi[g kr) Skiy t[vi[ kcri[

ji[Km) kcrin) uRp(Rt an[ (nkil

k\mi>k kcrini[ p\kir k[T[gr) mi#ii

(nkil

1. eT)p) Alz

34.4 80 Tn/(dvs eT)p) Alz\ ni[ (nkil T)a[sD)a[f sieT { M/s. BEIL aYvi M/s. NECL } pr krvimi> aivS[.

2. fliy a[S

-- 20 Tn/(dvs e>T bnivti> y&(nTn[ v[cvimi> aivS[

3. y&zD\ ai[el

5.1 4 l)Tr/(dvs GPCB p\mi(Nt r)siyklrn[

v[cvimi> aivS[.

4 D)AkiD[D kºT[ns</b[g 33.3 500 n>/(dvs D) kºTim)n[Sn pC) p\mi(Nt

v[ºDrn[v[cvimi> aivS[.

9. pivr an[ bL_iNn) j$(ryit

• pivrni[ p\iY(mk A#ii[t g&jrit Uji< T^iºs(mSn ki[pi[<r[Sn l)m)T[D mirft[ g&jrit rijy v)j ki[pi[<r[Sn l)m)T[D/g&jrit v)j bi[D< oiri p*r) piDvimi> aivS[.

Page 40: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

• pivr g&jrit Uji< T^iºs(mSn ki[pi[<r[Sn l)m)T[Dni> sb AT[Sn {220/66 k[v)a[} an[ T^iºs(mSn lien nJkmi> upl¾F C[.

• pivr Ja[cp)a[sa[l pivr ¼liºT pr pN upl¾F C[. • (vkis dr(myin bL_iNni[ upyi[g ai[Ci[ kr)S&>

10. b[zliEn a[ºviyrm[ºTl AT[T`s :

hvin&> p\d&PN:

vitivrNmi> p\d&Pki[n&> (vKrivv&> {p\srv&>}, hvimin s>b>F) (v(Bºn GTki[ j[vi k[ uONtipmin, hvin)

g(t, (dSi, u>DiNY) (m~N Yv&> (Mixing Depths), uÃT) spiT) (Inversion Level) (vg[r[n) kimg)r) pr aiFir riK[ C[. vitivrN)y hvini pyi<vrN pr Ynir s&S&¼t asrn) ai[LK, aigih) an[ m&Ãyi>kn miT[ vitivrN)y hvini nm&ni B[gi> kr) SPM, RSPM,SO2, NOX, HC, CO an[ VOC miT[ pZ¸YkrN krvimi> aiv[l C[. ki[EpN bhir n)kLvin) j³yia[Y) p\d&Pki[ni j¸Yin) aigih) miT[ an[k mi[D[l (vks)t krvimi> aiv[l C[.

vitivrN)y hvin) g&Nv_ii ckisN) an[ p\d&PN (ny>#iN pgli>

vitivrN)y hvin) g&Nv_ii ckisN), j&d)j&d) j³yin) a[k$pti {s&m[r} ni miT[ s).p).s).b).ni mig<dS<n an[ s).p).s).b).ni vitivrN)y hvin) g&Nv_ii ckisN) (NAAQS) ni FiriFi[rN m&jb (AAQS) ni> j&di> j&di> 8 AYLi[ prY) ai[kTi[br 2009 Y) D)s[‚br 2009 (SyiLiät& dr(myin nm&niai[ le pZ¸YkrN krvimi> aiv[l&> C[.

bFij AYLi[ prY) SPM n) mi#ii ar[Ym[T)k m)n an[ 98 TkiviL) 24 klikni an&k|m[ 74 Y) 94 miek|i[g\im/m)3 an[ 79.6 Y) 97.6 miek|i[ g\im/m)3 n) myi<dimi> aiv[ C[. a[ j r)t[ ar[Ym[T)k m)n an[ 98 TkiviL) RSPM n) mi#ii t[ (vAtirni> bFi> j AYLi[ prY) an&k|m[ 38 Y) 55 miek|i[g\im/m)3 an[ 44.6 Y) 58.7 miek|i[g\im/m)3 n) myi<dimi> aiv[ C[. SPM an[ RSPM n) a[kig\tin&> p\iY(mk kirN AYi(nk p\vZ(tai[ j[v) k[ vihni[n) p\vZ(t {hln cln}, miNsi[n) p\vZ(tn[ kirN[ k&drt) F&L {DAT} uDv&> t[m jNiy C[. SPM an[ RSPM n) a[kig\ti s).p).s).b).ni> rh[Ni>k an[ giÀy (vAtirni> FiriFi[rN m&jbn) g&Nv_ii dr[k vitivrN)y hvin) g&Nv_ii ckisN) (AAQM) AYLi[a[ milm pD[l C[.

dr[k AYLi[a[ SO2 n) mi#ii ar[Ym[T)k m)n an[ 98 TkiviL) an&k|m[ 10 Y) 21 miek|i[g\im/m)3 an[ 13.6 Y) 25 miek|i[g\im/m)3 milm pD[ C[. dr[k AYLi[a[ NOx n) mi#ii ar[Ym[T)k m)n an[ 98 TkiviL) an&k|m[ 18 Y) 30 miek|i[g\im/m)3 an[ 23.3 Y) 34.4 miek|i[g\im/m)3 milm pD[ C[. dr[k

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a[Àb)aºT a[r kvi[l)T) mi[n)Tr)>g (AAQM) AYLi[ pr 98 TkiviL) SO2 an[ NOx ni> p(rNimi[ hvin) g&Nv_iini> Fi[rNn) a>dr Ô[vi mL[ C[.

dr[k AYL pr hvi g&Nv_iin&> AT[T`s {(nr)xN} CO, HC an[ VOC n) AYi(nk a[kig\ti an&k|m[ BDL

milm pD[ C[.

piN)n&> pyi<vrN :

B&-Atr)y piN)n) m&LB&t g&Nv_ii :

B&-Atr)y piN)ni nm&niai[n) pH 7.80 Y) 8.38 n) myi<dimi> mil&m pD[ C[.Tb)<D)T) 0.3 Y) 0.9 NTU, mil&m pD[ C[, Ti[Tl (Dzi[lv[D si[l)D an&k|m[ 774 Y) 1850 m).l).g\im/ (lTrn) myi<dimi> milm pD[ C[.nieT^[T an[ Ti[Tl fi[Af[T n) mi#ii an&k|m[ 0.8 Y) 1.6 m).l).g\im/ (lTrn) myi<dimi> an[

0.14 Y) 0.63 n) myi<dimi> Ô[vi mL[l C[. DO, COD an[ BOD n) mi#ii an&k|m[ 7.0 Y) 7.4 m).l).g\im/ (lTr, 0.6 Y) 13.6 m).l).g\im/ (lTr an[ 0.0 Y) 0.5 m).l).g\im/ (lTrn) myi<dimi>

mil&m pD[ C[.Ti[Tl hiD<n[S {as CaCO3} n) mi#ii 75.9 Y) 260.2 m).l).g\im/ l)Trn) myi<dimi>

mil&m pD[ C[. k[(ÃSym hiD<n[S {as CaCO3} 63.4 Y) 190.3 m).l).g\im/(lTrn) myi<dimi> milm pD[ C[. Ti[Tl aiÃkin)T) 250 Y) 430 m).l).g\im/(lTrn) myi<dimi> milm pD[ C[. kli[rieD an[ sÃf[T an&k|m[ 138 Y) 985.5 m).l).g\im/(lTr an[ 26.38 Y) 68.9 m).l).g\im/ (lTrn) myi<dimi> Ô[vi mL[ C[.

jm)n prni piN)n) m&LB&t g&Nvti :

jm)n Atr prni piN)ni nm&nin&> pH 7.91 Y) 8.14 C[.Tb)<D)T) 5.0 Y) 5.7 NTU mil&m pD[ C[, Ti[Tl (Dzi[lv[D si[l)D an&k|m[ 210 Y) 360 m).l).g\im/ (lTrn) myi<dimi> milm pD[ C[.nieT^[T an[ Ti[Tl fi[Af[T n) mi#ii an&k|m[ 2.3 Y) 2.8 m).l).g\im/ (lTr an[ 1.08 Y) 1.3 m).l).g\im/ (lTrn) n)

myi<dimi> milm pD[ C[. DO, COD an[ BOD n) mi#ii an&k|m[ 6.0 Y) 6.8 m).l).g\im/ (lTr, 12.15 Y) 26.04 m).l).g\im/ (lTr an[ 0.5 Y) 0.6 m).l).g\im/ (lTrn) n) myi<dimi> mil&m pD[ C[.Ti[Tl

hiD<n[S {as CaCO3} n) mi#ii 96.7 Y) 130 m).l).g\im/ l)Trn) myi<dimi> mil&m pD[ C[. k[(ÃSym

hiD<n[S {as CaCO3} 78.4 Y) 97 m).l).g\im/(lTr n) myi<dimi> milm pD[ C[. Ti[Tl aiÃkin)T) 110 Y) 210 m).l).g\im/(lTrn) myi<dimi> milm pD[ C[. kli[rieD an[ sÃf[T an&k|m[ 6.9 Y) 8.87 m).l).g\im/(lTr an[ 6.51 Y) 17.9 m).l).g\im/ (lTrn) myi<dimi> Ô[vi mL[ C[.

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avijn&> pyi<vrN:

avijn&> p\d&PNni[ sv<[ p\i[j[kTn) aij&bij& krvini[ h[t& vt<min avijn&> ud`Bv AYin ÔNvi an[ p\iVt` avij Atr ÔNvi miT[ kr[l C[. aini[ a¿yis n)c[ ÔNv[l cir m&Ñi ai[ Úiri krvimi> aiv[ C[.

Kis p\kirn) kiy<vih) (Reconnaissance) avijni udBv AYinn) ÔNkir) m[Lvv) an[ avijn&> Atr mipv&>. vihn Äyvhir Yk) uÑBvti avijni Atrn) mipN) krv). vsihti[ Yk) avijni Atrn) mipN).

avijn&> m&LB&t Atr :

avijn) mi#ii a¿yisx[#in) j&d)-j&d) j³yia[Y) mip[l C[. a¿yis (vAtirni AYL[Y) avijn) mi#ii

(dvs smy[ {ri(#i smy} drÀyin an&k|m[ 40-42 {35-37} dBA an[ 42-48 {38-45} dBA ai]Fi[(gk an[ rh[Ni>k (vAtirmi> Ô[vi mL[l C[.

jm)nn) pyi<vrN :

jm)nn) miT)n) g&Nv_ii ÔNvi miT[ (SyiLiät& dr(myin 8 AYL prY) miT)ni nm&ni le pZ¸YkrN krvimi> aiÄy&> C[.

b[zlien AT^[Ts:

pH n) mi#ii 7.75 Y) 8.05. k[(ÃSymn) mi#ii 0.04 Y) 0.24 m).l).g\im/g\imn) (v(vFtimi> Ô[vi mL[ C[. sÃf[T an&k|m[ 0.012 Y) 0.026 m).l).g\im/g\im an[ ±li[rieD an&k|m[ 0.2 Y) 6.2 m).l).g\im/g\imn) myi<dimi> Ô[vi mL[ C[. m[³i[n[S)ym an&k|m[ 0.02 Y) 0.15 m).l).g\im/g\im an[ pi[T[(Sym an&k|m[ 0.020 Y) 0.056 m).l).g\im/g\imn) myi<dimi> Ô[vi mL[ C[. Ti[Tl ai[g[<(nk kib<n an&k|m[ 1.58% Y) 2.51% Ô[vi mL[l C[. Ti[Tl hiD<n[S an&k|m[ 0.4 Y) 1.0 m).l).g\im/g\imn) myi<dimi> Ô[vi mL[ C[. Ti[Tl aiÃkl)n)T) an&k|m[ 0.8 Y) 5.4 m).l).g\im/g\imn) myi<dimi> an[ bÃk

D[ns)T) 1.25 Y) 1.36 gm/cm3 n) myi<dimi> Ô[vi mL[ C[.

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pyi<vrN)y ji[Km :

kici[ mil {ri[-mT)r)yl} si[lvºT j&di> j&di> k[m)kl (vg[r[n[ rAtiai[ pr pr)vhn kr) an[ k>pn)ni k>piuºDmi> ATi[r krvimi> aiv[ C[. g&jrit srkirni bFi (nd[<Si[ an&sir Ô[Km) k[m)klni[ s>g\h an[ pr)vhn miT[ ai[n siET Emrjºs) ¼lin t]yir krvimi> aivS[. dr[k p\kirni k[m)kl siY[ Ô[Diy[l Ô[Km an[ pyi<vrN)y Ô[Kmn) kiLJ riK[ t[m ai r)pi[T< {ah[vil} bnivvimi> aivS[. ai yi[jnini p\AtZtkti< Úiri ¼liºTn) s&rxini dr[k ÑOT)ki[N r[Kikiy< an[ p\(k|yimi> u(ct kiy<r)(tn[ ´yinmi> l[v) k[ j[Y) ai gNtr)mi> ki[EpN p\(tk&L asr lxmi> l[vin) rh) n Ôy. s>AYini py<ivrN ÄyvAYipn t>#i Úiri l[vimi> aiv[l p\d&PN (nvirN pgli> dSi<v[ C[ k[ pyi<vrN pr ki[e ni[Fn)y p\(tk&L asr Yt) nY).

bF) j cci< (vcirNi an[ s&(ct (vAtrN yi[jni miT[ a[ºviyri[m[ºT eÀp[kT a[s[sm[ºT a¿yis (vAtirmi> t]yir krvimi> aiv[l C[. t[ni prY) si(bt Yiy C[ k[ m[ss< g&jrit hiED^i[kib<n an[ pivr a[s.e.z[D. (lm)T[D, Úiri pyi<vrN pr ki[epN ni[>Fpi#i miq) asr Yvini[ s>Bv nY). t[m Cti> pN ki[e ud`gmn) siYi[siY kiydi(ky (nymi[n&> piln krS[.

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EXECUTIVE SUMMARY OF PROJECT REPORT

(ENGLISH)

of

M/S. GUJARAT HYDROCARBONS AND POWER SEZ LIMITED

GIDC – VILAYAT (VAGRA) INDUSTRIAL ESTATE,

VILAYAT, TAL : VAGRA, DIST : BHARUCH, GUJARAT

Page 45: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

EXECUTIVE SUMMARY OF PROJECT

INTRODUCTION

• The SEZ going to be developed by Gujarat Hydrocarbons and Power SEZ Limited (GHPSL) is amongst the first dedicated Hydrocarbon SEZ in India.

• GHPSL proposes to develop the sector specific SEZ project with both foreign and domestic investors as financial or technical collaborators to the project. However, these investors will be introduced into the project on a need basis, depending upon requirements of the project.

• GHPSL, 100% subsidiary of Assam Company, is setting up India’s first integrated Hydrocarbon in the most investor friendly state Gujarat in India. GHPSL is conceived as One stop “world class” integrated sector specific SEZ for providing products and related services addressing the entire range of Hydrocarbons value and supply chain. GHPSL is designed to exploit the massive unfolding opportunities in this fastest growing sector of the Indian economy addressing the mismatch between the demand and supply. The project intends to attract investors in this unique Special Economic Zone project which will entitle them to several fiscal incentives. Infrastructure availability including power, water, natural gas, effluent treatment, etc. will provide the required impetus.

• GHPSL has acquired land and received formal approval for SEZ, Petroleum hydrocarbon. The operations are expected to commence in 2012, aiding a quantum jump in India’s Hydrocarbon infrastructure.

• SEZ is situated in Bharuch near Dahej which is the hub of Oil & Gas and Chemicals. The SEZ also falls within the boundary of PCPIR (Petroleum, Chemical & Petro‐chemicals Investment Region), are well connected with Road (National Highway), Railway (Delhi‐Mumbai Rail Line), Airport (National Airport at Vadodara 80 Km and International Airport at Ahmedabad, 180 Km), nearest All‐weather port‐ Dahej. These SEZ also falls onto the link of Dedicated Freight Corridors (DFC) a mega project started by Govt. of India, with collaboration from JICA (Japanese International Collaboration Agency) for augmenting to Dedicated High Speed Rail Link between Delhi and Mumbai.

• Any Petroleum hydrocarbon industry service that will support industry in the SEZ for manufacturing, stocking, trading including logistics and utilities with local linkages, and for which site is available as per the approved detailed Master Plan, will be eligible for being set up in the PCPIR.

• GHPSL has also signed MOUs with Gujarat Maritime Board and Gujarat Industrial Development Corporation for setting up Fabrication yard and Shipyard. GHPSL plans to facilitate export activities of the SEZ by adding their own captive jetty.

• The Company is actively scouting for right partners who wish to leverage the state‐of‐art infrastructure and facilities.

PLANNED ACTIVITIES

• Total Area of SEZ is 140 Hectares.

• To be developed over phases

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• Propose to set up Sector Specific Special Economic Zone for Petroleum Hydrocarbon in Vilayat

Industrial Estate, Taluka: Vagra, Dist: Bharuch, Gujarat.

Break‐up of the Industries:

Total Petroleum Hydrocarbon Plant: 10

Fabrication Unit: 1

CETP: 1 & STP: 1

Incinerator: 1

DISTRIBUTION OF SEZ

Zone Total Area (Ha) %

Hydrocarbons SEZ

Non‐Processing (Logistic Park, Parking facility, Colony, Restaurant,

Pumping Station, Weight Bridge, Custom Office, road and

Infrastructure Corridor, etc.)

24 17.00

Green Belt 46 33.00

Carbon Black Units 2 1.43

PTA Units 18 12.86

Dual Feed Petrochemical complex, Ethylene Oxide derivatives – MEG etc,

Polyethylene derivatives, n‐Butanol, Propylene derivatives, Polypropylene,

Para Xylene & Ortho Xylene, PET, Styrene,

Specialty Chemicals/Refinery Catalysts/Synthetic,

47 33.56

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Lubricant/products, R & D/ Laboratory Testing Service

CETP, Common Incinerator 3 2.15

Total 140 100

PROJECT COST FOR DEVELOPMENT OF SEZ

Total estimated cost of the project will be Rs. 975 Cr. (Proposed).

• Cost of Development Rs.94 Crores

• Cost for ready built infrastructure – Rs.800 Crores

• Cost of project management, water treatment plant, Sewage/ Effluent Collection,

Transportation, Incinerator, Treatment & Reuse, Storm Water Harvesting system & Fire

fighting system – Rs.68 Crores

• The annual budget for the EMP ( operational phase ) – Rs. 13 Crores

Page 48: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

p\i[j[kT ni[ vh)vT) siri>S

m[ss< g&jrit hieD^i[kib<ns an[ pivr s[z (l.,

J.aie.D).s). (vliyt eºDAT^)yl a[AT[T,

til&ki: vigri, J9li[: B$c {g&jrit}

Page 49: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

p\i[j[kT ni[ vh)vT) siri>S

1. p\Ativni:-

g&jrit hieD^i[kib<ns an[ pivr s[z (l. oiri (vksivimi> aivnir s[z Birtni[ p\Ym hieD^i[kib<n s[z C[.

J.a[s.p).a[s.a[l. s[kTr Ap[s)f)k s[zni> (vkisn) yi[jni siY[> p\i[j[kT miT[ niNi>k)y tYi T[kn)kl shyi[g) tr)k[ b>n[ Birt)y tYi (vd[S) ri[kiNkiri[n) drKiAt kr[l C[ . ji[ k[, ai ri[kiNkiri[n[ j$(ryit p\miN[ diKl krvi d[vimi> aivS[.

J.a[s.p).a[s.a[l, aisim k>pn)n) 100% sbs)D)yr) C[, j[ Birtni[ si] p\Ym hieD^i[kib<n s[z g&jritmi> AYipvini> C[. g&jrit j[ Birtni[ si]Y) vw& eºv[ATr f[\ºDl) rijy C[. J.a[s.p).a[s.a[l. j[ (vÅvBrmi> si]Y) siri[ Ap[s)f)k s[z AYipvi je rh) C[ j[mi> smg\ hieD^i[kib<n s>b>(wt p\i[DkTs an[ t[n) siY[ ji[Diy[l s[viai[ aipvimi> aiv[ C[. J.a[s.p).a[s.a[l.n) (Dziena[ r)t[ krvimi> aivS[ k[ j[Y) Birtn) eki[ni[m)mi> zDp) (vkis Yiy j[Y) mi>g an[ s¼lieni[ tfivtn[ ¹yinmi> riK)n[ t[ni> s>b>(wt tki[ni[ (vkis krvimi> aivS[. J.a[s.p).a[s.a[l. eµC[ C[ k[ ri[kiNkiri[ ai a[kmi#i s[zmi> aik(P<t Yiy an[ t[mn[ (v(vw niNik)y p\[rNi> p\i¼t Yiy. eºf\iAT^crn) j$(ryit j[v) k[ v)jL), piN), n[crl g[s, p\d*(Pt piN)n) p\(k\yi an[ (nkil (vg[r[ ai p\(k\yin[ aigL vFirvimi> mdd krS[.

J.a[s.p).a[s.a[l.a[ p[T^i[(lym hieD^i[kib<n s[z miT[ jm)n Kr)d[l C[ an[ m>j*r) miT[ je rhy&> C[ ai ai[pr[Sn 2012mi> S$ Yvin) ap[xi C[ j[Y) Birt hieD^i[kib<n x[#in) p\(tAYimi> vwiri[ YS[.

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s[z B$cmi> dh[j nJk aiv[l C[ j[ ai[el an[ g[s t[mj k[(mkln&> m&²y k[ºd^ C[. s[z a[ p)s)p)aieairn) hdmi> aiv[l C[ j[ riÖ^)y wi[r)mig< (d9h)-m&b>eY) 17 k).m)., r[9v[lien-B$cY) 17 k).m)., vDi[dri hviemYkY) 80 k).m). an[ ai>trriÖ^)y hviemYkY) 180 k).m). d*r aiv[l C[. ai s[z Birt srkir an[ jipin)z eºTrn[Snl ki[libi[r[Sn a[jºs) oiri S$ krvimi> aiv[l m[gi p\i[j[kT (d9h) an[ m&>be n[ ji[Dti> D[D)k[T[D f[\Y ki[r)Di[rmi> aivr) l[vimi> aiv[ C[.

s[zmi> aiv[l eºDAT^)z p[T^i[(lym hieD^i[kib<nn&> uRpidn an[ T^[D)>g krt) eºDAT^)z miT[ aiFir$p C[ an[ j[ni miT[ m>j*r Yy[l (vgtvir miATr ¼linmi> sieT upl¾F C[, j[ p)s)p)aieairmi> s&yi[Jt miT[[ pi#i YS[.

J.a[s.p).a[s.a[l.a[ f[b\)k[Sn yiD< an[ S)pyiD<n) AYipni> miT[ g&jrit m[r)Tiem bi[D< an[ g&jrit eºDAT^)yl D[vli[pm[ºT ki[pi[<r[Sn siY[ MOUs sien kr[l C[. J.a[s.p).a[s.a[l. s[zn) (nkis p\vZ(t miT[ pi[tin) k[¼T)v j[Í)n) AYipni krvin) yi[jni kr) rh) C[.

k>pn) rijyn) aiT< eºfi\AT^cr an[ s&(vFini[ liB uqiv) Sk[ t[vi> siri> Big)dirn) tpis kr) rh) C[.

2. aiyi[Jt p\vZ(tai[:

• s[zni[ k&l (vAtir 140 h[kTr C[. • crN p\miN[ (vkis krvimi> aivS[. • J.aie.D).s). (vliyt eºDAT^)yl a[AT[T, til&ki: vigri, J9li[: B$c {g&jrit}mi>

p[T^i[(lym hieD^i[kib<n miT[ s[kTr Ap[s)f)k s[z AYipvin) drKiAt kr[l C[.

Page 51: EXECUTIVE SUMMARY OF EIA REPORT (ENGLISH) · Effluent from each individual unit would be collected and transported to CETP. The effluent would be divided in three categories: •

3. eºD^AT)zn&> (vwTn:

k&l p[T^i[(lym hieD^i[kib<n y&(nT: 10

f\[b)k[Sn y&(nT: 1

s)>eT)p) -1 an[ a[sT)p) -1

eºs)nr[Tr – 1

4. s[zni[ jm)n (vAtir:

zi[n k&l (vAtir %

hieD^i[kib<n s[z

ni[n p\i[s[s)>g {li[JAT)k pik<, pik)<>g, ki[li[n), r[ATi[rºT, pÀp)>g AT[Sn, v[eT b\)j

kATm ai[(fs an[ eºfi|ATcr ki[r)Di[r} 24 17.00

g\)n b[9T 46 33.00

kib<n ¾l[k y&(nT 2 1.43

p)T)a[ y&(nT 18 12.86

Dual Feed Petrochemical complex, Ethylene Oxide derivatives – MEG etc,

Polyethylene derivatives, n‐Butanol, Propylene derivatives, Polypropylene,

Para Xylene & Ortho Xylene, PET, Styrene,

Specialty Chemicals/Refinery Catalysts/Synthetic,

Lubricant/products, R & D/ Laboratory Testing Service

47 33.56

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s)>eT)p) an[ a[sT)p)

eºs)nr[Tr 3 2.15

k&l 140 100

5. s[zni (vkis miT[ p\i[j[kT Kc<:

p\i[j[kT miT[ k&l a>diJt Kc< $. 975 kri[D C[.

• (vkis Kc< $. 94 kri[D

• eºfi|ATcr bnivvini[ Kc< $. 800 kri[D

• p\i[j[kT s>ciln, piN) S&(okrN, s[v[z S&(okrN, vihnÄyvhir, eºs)nr[Tr,

S&(okrN an[ p&n: upyi[g, vi[Tr hirv[AT)>g an[ fiyr fieT)>g - $. 68 kri[D

• pyi<vrN miT[ vi(P<k Kc< $. 13 kri[D