ANNEXURES - environmentclearance.nic.inenvironmentclearance.nic.in/.../online/EC/2911201693YUK3GLAnnexures.pdf · Gujarat Refinery AOR MATERIAL BALANCE OF PROCESS UNITS 2014-15 PAGE

ANNEXURES

FOR

M/s IOCL GUJARAT REFINERY “PROPOSED BS – IV & VI PROJECT”

AT

VILLAGE : KOYALI TALUK : VADODARA

DISTRICT : VADODARA STATE : GUJARAT

SUBMITTED BY

INDIAN OIL CORPORATION LIMITED, GUJARAT REFINERY (IOCL GUJARAT REFINERY)

[PROJECT TERMED UNDER SCHEDULE 4 (a) – CATEGORY ‘A’ AS PER

EIA NOTIFICATION 2006 AND ITS SUBSEQUENT AMENDMENTS]

REPORT PREPARED BY

HUBERT ENVIRO CARE SYSTEMS PVT. LTD., CHENNAI

NOVEMBER 2016

Page 1 of 244

LIST OF ANNEXURES

S.No. Description Annexure No. Page No. 1 Material Balance 7 3

2 Plant Layout and Site Plan 4 11

3 Raw Material Quantities 5 12

4 Fresh Water Agreement 6 13

5 Block Flow Diagram of CETP 8 25

6 Storm Water Layout 9 26

7 Stack Reports 10 27

8 Material Safety Data Sheet 12 68

9 Disaster Management Plan 13 72

10 EC Compliance 14 95

11 Fire Protection Facility 15 144

12 Hazardous Waste Disposal – Authorized Vendor

Certificate

16 153

13 Green Belt Layout 17 154

14 Raw data of AAQ for 12 weeks for 8 locations 18 155

15 Flaring System 19 161

16 Transport of Raw Material and Products 20 167

17 Details of rain water harvesting wells 21 176

18 Details of show cause notices received from GPCB 22 178

19 Terms of Reference (ToR) compliance statement 24 179

20 Risk Assessment Report (attached separately) 11 (attached

separately)

21 Environmental Clearances 1 193

22 Consents Obtained 2 212

23 Standard Terms of Reference (ToR) 3 240

24 Public Hearing Proceedings 23 (attached

separately)

Gujarat Refinery AORMATERIAL BALANCE OF PROCESS UNITS 2014-15

PAGE 51

Atmospheric Unit (1):Input MT % wt

South Gujarat 795,299 58.0North Gujarat 512,937 37.4Bombay High 40,675 3.0Imported-LS 22,653 1.7Total 1,371,563 100.0OutputGas 1,967 0.1LPG 23,044 1.7Naphtha 246,393 18.0ATF component 83,020 6.1SKO 148,824 10.9SR Gas Oil 235,224 17.2RCO 631,221 46.0Loss 1,870 0.1Total 1,371,563 100.0

Atmospheric Unit (2) :Input MT % wt

South Gujarat 72,289 4.2North Gujarat 651,678 38.3Bombay High 566,465 33.3Imported-LS 412,755 24.2Total 1,703,186 100.0OutputGas 2,739 0.2LPG 25,528 1.5Naphtha 226,046 13.3SR Kerosene 30,612 1.8ATF component 224,336 13.2SR Gas Oil 308,684 18.1RCO 882,961 51.8Loss 2,280 0.1Total 1,703,186 100.0

Atmospheric Unit (3) :Input MT % wt

North Gujarat 2,432,178 99.0Bombay High 0 0.0Imported-LS 0 0.0Imported-HS 0 0.0Total 2,432,178 99.0Slops 25,426 1.0

Total 2,457,604 100.0OutputGas 1,700 0.1LPG 10,578 0.4LT Naphtha 117,487 4.8HY Naphtha 14,859 0.6SR Kerosene 222,895 9.1SR Gas Oil 302,550 12.3RCO 1,785,359 72.6Loss 2,176 0.1Total 2,457,604 100.0

Page 3 of 244

Consultancy

Typewritten text

Annexure-7


PAGE 52

Atmospheric Unit (4): Input MT % wt

South Gujarat 5,750 0.1Bombay High 47,223 1.2Imported-LS 353,911 9.0Imported-HS 3,150,811 79.8Mangla 392,366 9.9Total 3,950,062 100.0OutputGas 7,912 0.2LPG 55,493 1.4D02 Naphtha 182,000 4.6C06 Naphtha 241,119 6.1HY Naphtha 151,657 3.8SR Kerosene 402,638 10.2Lt. Gas Oil 158,409 4.0Hy. Gas Oil 532,655 13.5RCO 2,215,508 56.1Loss 2,671 0.1Total 3,950,062 100.0

Atmospheric Unit (5):Input MT % wt

South Gujarat 0 0.0Bombay High 0 0.0Imported-LS 11,715 0.3Imported-HS 3,467,560 89.8Mangla 349,039 9.0Total 3,828,314 99.2Slop 32,647 0.8Total 3,860,961 100.0OutputGas 4,144 0.1LPG 52,425 1.4Lt. Naphtha 300,142 7.8Hy. Naphtha 145,900 3.8SR Kerosene 440,686 11.4SR Gas Oil 703,321 18.2RCO 2,211,442 57.3Loss 2,901 0.1Total 3,860,961 100.0

Atmospheric Unit (1,2,3,4,5):Input MT % wt

South Gujarat 873,338 6.5North Gujarat 3,596,793 27.0Bombay High 654,362 4.9Imported-LS 801,034 6.0Imported-HS 6,618,371 0.0Mangla 741,405 49.6Total 13,285,303 94.0Slops 58,073 0.4Total 13,343,376 94.4Output

Gas 18,462 0.1LPG 167,068 1.3Lt. Naphtha 1,313,187 9.8HY Naphtha 312,416 2.3SR Kerosene 1,245,655 9.3ATF component 307,356 2.3SR Gas Oil 2,240,843 16.8RCO 7,726,491 57.9Loss 11,899 0.1Total 13,343,377 100.0

Page 4 of 244


PAGE 53

Naptha Rerun Column I MT %

Naphtha Feed 1,009,140 100.0OutputK8 Top 187,086 18.5K9 Top 202,512 20.1K10 Bottom 256,736 25.4K9 Bottom 362,200 35.9Loss 606 0.1Total 1,009,140 100.0

AU -II K-7 ColumnMT %

Feed 135,357 100.0OutputK7 Top 14,679 10.8K7 Bottom 120,673 89.2Loss 5 0.0Total 135,357 100.0

Feed Preparation Unit-I:MT % wt

Feed 2,668,132 100.0OutputSlop Oil 13,614 0.5Hy. HSD 197,552 7.4LVGO 474,296 17.8HVGO 508,062 19.0VR 1,472,358 55.2Loss 2,250 0.1Total 2,668,132 100.0

Feed Preparation Unit -IIMT % wt

Feed 3,619,439 100.0OutputSlop Oil 25,391 0.7Hy HSD 449,416 12.4LVGO 780,747 21.6HVGO 809,413 22.4HHVGO 912 0.0Slop Distillate 216,343 6.0VR 1,334,861 36.9Loss 2,356 0.1Total 3,619,439 100.0

Vacuum Distillation Unit (VDU)MT % wt

Feed 1,174,510 100.0OutputSlop Oil 7,205 0.6Hy. HSD 84,526 7.2LVGO 202,669 17.3HVGO 220,986 18.8Slop Distillate 79,810 6.8VR 577,895 49.2Loss 1,419 0.1Total 1,174,510 100.0

Page 5 of 244


PAGE 54

Fluid Catalytic cracking Unit MT % wt

FeedIND VGO 0 0.0Mixed VGO 1,708,597 97.8IMP HS VGO 0 0.0VDU Hy HSD 0 0.0VB Naphtha 0 0.0HCU Bottom 38,684 2.2Total 1,747,281 100.0OutputGas 47,353 2.7Cracked LPG 260,770 14.9Gasoline 651,054 37.3Hy Naphtha 216,599 12.4LCO 308,867 17.7HCO 0 0.0CLO 186,018 10.6Coke 73,914 4.2Loss 2,706 0.2Total 1,747,281 100.0

HydrocrackerMT % wt

Feed 0.0IND VGO 1,604,890 98.1IMP VGO 0 0.0Sub total 1,604,890 98.1Hydrogen (H2) 31,595 1.9Total 1,636,485 100.0OutputGas 34,288 2.1LPG 57,592 3.5Lt.Naphtha 231,526 14.1Hy .Naphtha 154,964 9.5SKO/ATF component 566,870 34.6HSD component 542,521 33.2Bottom 46,650 2.9Loss 2,073 0.1Total 1,636,485 100.0

VGO- HydrotreaterMT % wt

Feed 2,372,984 98.7Hydrogen to VGOHDT 32,399 1.3Total 2,405,383 100.0OutputFuel gas 7,270 0.3LPG 1,635 0.1Lt.Naphtha 42,712 1.8Kerosene 78,648 3.3Gas Oil 358,330 14.9Sweet VGO 1,914,224 79.6Loss 2,564 0.1Total 2,405,383 100.0

Page 6 of 244


PAGE 55

Visbreaker UnitMT % wt

FeedFPU VR/VDU VR 23,900 100.0Slop 0 0.0RCO 0 0.0VGO 0 0.0Total 23,900 100.0OutputGas 526 2.2VB Naphtha 722 3.0VB gas oil 1,654 6.9VB FO 20,986 87.8Loss 12 0.1Total 23,900 100.0

Bitumen Blowing UnitMT % wt

FeedSub Total 346,044 100.0Direct VR 0 0.0Total 346,044 100.0OutputBitumen 345,650 99.9Loss 394 0.1Total 346,044 100.0

DCUMT % wt

Feed 3,487,654 100.0OutputGas 146,637 4.2LPG 93,507 2.7Naphtha 197,080 5.7LCGO 1,372,132 39.3HCGO 913,423 26.2COKE 760,860 21.8Loss 4,017 0.1Total 3,487,654 100.0

DHDSMT % wt

Feed 1,455,324 99.4Hydrogen 8,731 0.6Total 1,464,055 100.0OutputHSD 1,407,479 96.1Wild Naphtha 16,959 1.2H2S 38,571 2.6Loss 1,046 0.1Total 1,464,055 100.0

Page 7 of 244


PAGE 56

DHDTMT % wt

Feed 2,089,539 98.3Hydrogen to DHDT 35,531 1.7Total 2,125,070 100.0Output 0 0.0Off gas 8,667 0.4Naphtha 123,367 5.8DHDT diesel 1,991,636 93.7Loss 1,400 0.1Total 2,125,070 100.0

HYDROGEN UNIT -IMT % wt

Feed 79,008 100.0

Hydrogen 24,012 30.4Purge Gas 54,883 69.5Loss 114 0.1Total 79,009 100.0

HYDROGEN UNIT - IIMT % wt

Feed 5,791 100.0


HYDROGEN UNIT -IIIMT % wt

Feed 141,050 100.0


Catalyst Reforming UnitMT % wt

Feed 390,800 100.0

Gas 43,555 11.1LPG/Drag Stream 35,702 9.1Reformate 311,263 79.6Loss 280 0.1Total 390,800 100.0

Page 8 of 244


PAGE 57

MSQ MT % wt

Feed FCC Gaoline 0 0.0 SRN Naphtha 666,689 100.0Total 666,689 100.0OutputH2 16,892 2.5Gas 32,593 4.9LPG 207 0.0Merox R/D 0 0.0Lt Reformate 198,895 29.8Hy Reformate 417,502 62.6Loss 600 0.1Total 666,689 100.0

ISOMMT % wt

Feed 213,984 99.4H2 as feed 1,384 0.6Total 215,368 100.0Output 0 0.0Fuel gas 1,984 2.3LPG 8,805 1.9Isomerate 204,069 95.4Loss 510 0.4Total 215,368 100.0

Udex UnitMT % wt

Feed 113,300 100.0Output Benzene 18,183 16.0 Toluene 0 0.0 Raffinate 94,934 83.8 Loss 183 0.2Total 113,300 100.0

FGH UnitMT % wt

Feed 96,942 100.0OutputFGH +PGH FEED 7,333 7.6n-Pentane 0 0.0Balance -Naphtha 89,453 92.3Loss 156 0.2Total 96,942 100.0

Page 9 of 244


PAGE 58

LAB : UNIT

MT % wt Feed 527,336 92.5 Benzene 38,965 6.8H2 Gas 1,170 0.2n-Paraffin 2,467 0.4Total 569,938 100.0OutputOff Gas 5,908 1.0Wild Naphtha 9,991 1.8LAB Return Stream 440,435 77.3LAB 105,092 18.4n-Paraffins 808 0.1Hy Alkylates 6,489 1.1Loss 1,215 0.2Total 569,938 100.0

MTBEMT % wt

Feed 221,486 95.0MeOH 11,545 5.0Total 233,031 100.0OutputMTBE 33,240 14.3LPG 199,459 85.6Loss 332 0.1Total 233,031 100.0

Page 10 of 244

Page 11 of 244

Consultancy

Typewritten text

Annexure-4

Gujarat Refinery AOREXECUTIVE SUMMARY 2014-15

PAGE 46(figures are in MT)

UNIT T'PUT ON STREAM MT (DAYS)

UDEX 113,300 364.8FGH 96,942 364.4LAB 527,336 350.8MTBE 233,031 352.2H2U-I 79,008 354.0H2U-II 5,791 344.8H2U-III 141,050 119.2

4 UNITWISE / CRUDEWISE BREAKUP :UNIT S G N G B H IMP-LS IMP-HS+ M TOTAL

AU-1 795,299 512,937 40,675 22,653 0 1,371,563AU-2 72,289 651,678 566,465 412,755 0 1,703,186AU-3 0 2,432,178 0 0 0 2,432,178AU-4 5,750 0 47,223 353,911 3,543,177 3,950,062AU-5 0 0 0 11,715 3,816,599 3,828,314TOTAL 873,338 3,596,793 654,362 801,034 7,359,776 13,285,303

5 IMPORTED CRUDE BREAK UP :

IMPORTED HIGH SULPHUR CRUDE RECEIPT PROCESSED % ON IMP

KUWAIT 3,551,083 3,582,870 43.90BASARH LIGHT 2,362,895 2,356,814 28.88ARAB MIX 282,663 282,138 3.46IRAN MIX 18,933 18,962 0.23UPPER ZAKUM 864 2,400 0.03MARLIM 21,298 25,420 0.31DUBAI 24,337 24,980 0.31MAYA 190,571 192,944 2.36ALSHAHEEN 34,858 34,858 0.43QLCONDENSATE 20,651 20,651 0.25RONCADOR 66,020 66,020 0.81CASTILLA 12,615 10,314 0.13MANGLA 729,999 741,405 9.08SUB-TOTAL 7,316,787 7,359,776 90.18

IMPORTED LOW SULPHUR CRUDE ZAFIRO 16,268 16,178 0.20OKWUIBOME 34,885 34,885 0.43PENNINGTON 31,907 27,469 0.34ESCRAVOS 0 0 0.00FORCADOS 52,509 50,348 0.62BONNY LT 260,244 233,016 2.86QUAIBOE 59,229 61,723 0.76NEMBA 14,024 14,109 0.17CEIBA 0 0 0.00GIRASSOL 3,394 3,394 0.04KISSSANJE 0 294 0.00BONGA 34,969 45,686 0.56SERIA LIGHT 0 0 0.00AMENAM 20,342 22,570 0.28EA CRUDE 40,443 41,369 0.51ERHA 0 0 0.00MURBAN 183,192 177,706 2.18KIKEH 0 0 0.00HUNGO 0 0 0.00YOHO 1,225 4,934 0.06OKORO 11,847 11,673 0.14PAZFLOR 6,939 7,105 0.09AGBAMI 10,989 11,129 0.14CABINDA 0 22 0.00SATURNO 5,060 5,060 0.06OKORO 0 0 0.00AKPO 4,690 4,690 0.06DALIA 2,981 2,983 0.04CPC 24,691 24,691 0.30SUB-TOTAL 819,828 801,034 9.82TOTAL 8,136,615 8,160,811 100.00

6 MODEWISE DESPATCHES OF PRODUCTS :

MODE OF QUANTITY % ON TOTALDESPATCH MT DESPATCHES

PIPELINE 8,451,461 66.7RAIL 3,195,677 25.2ROAD 1,022,387 8.1TOTAL 12,669,524 100.0

Page 12 of 244

Consultancy

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Annexure-5

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AGREEMENT

village Vasad for their industrial usase purpose'

This agreement made on this tfl Day of M qI :2012 between

the ,,Gujarat Refinery, lndian oil corporation Limited, Vadodara,, a

publiclimitedcompanyregisteredunderthecompaniesact,1956-t "

*--X4. /( ksft- €- qrqer<-t. o. PARASHARChief Power & Utilities Manag,:rilnn"".T,i[", v"dss"*;r;x;ffii"".il":fi ,"bii-"'i"i-n'tin"tv' '""*-vADoDARA'

7 45 493

Vadodara.

Page 13 of 244

Consultancy

Typewritten text

Annexure-6

through its Chief Power & Utilities Manager (hereinafter in this

agreement called the "licensee" Which expression shall, unless

context otherwise requires and admits be deemed to include its

administratorS, executors, successorS and assign) having its

registered office at G-9 AIi Yavar Jung Marg, Bandra (East), Mumbai -400 05L ofthe one part and the governor ofthe state ofthe state of

Gujarat through Executive Engineer, Vadodara lrrigation Division,

Vadodara in office (herein after called as "the Government" which

expression shall, unless context otherwise requires and admits be

deemed to include his successors in office and assigns) of the other

part.

WHERE AS the licensee has applied to the Government for

permission to draw water from Mahi River, near, village Vasad for

the purpose of industrial complex and for drinking purpose to its

Township and also supply to GSFC, Vadodara under agreement with

them in respect of drawl of water from French wells in Mahi river

under joint ownership of Gujarat Refinery and GSFC.

AND WHEREAS The Government has under its sanction letter

WTR/1097/33/P date 26.02.1998..agreed to grant such permission

on the terms and condition herein after appearing and as mentioned

in the Government of Gujarat Narmada Water Resources, Water

Supply & Kalpsar Departement Resolution No.WTR/20O5/41lP dated

3.2.2007,,\t./*oy'

-+P:'*:Y(ff. €- qr?Ter<

G. D. PARASHARChief Power & Utilities Managerl.O. C.L., Gularat Refinery,

Vadodara.

Executive i'nlineerVadodara lrrigailon Divisio4

VADOOAR'/A'

-2-

Page 14 of 244

NOW THIS INDENTURE WITNESS and the parties here to

hereby agree as follows:

(1)The Government hereby grants the permission to the licensee

to draw water from Mahi River, near village Vasad on the terms

and conditions hereafter appearing. The license Shall construct

and maintain the head works for drawing water from Mahi

River, and other required structures at suitable places as

approved by the Government or its authorized officer at their

risk & cost and shall provide all ancillary arrangements that

may be required in connection with the drawing and conveying

the water required for the use of licensee. The intake

structures shall be open to inspection by the government and

the government shall exercise necessary control.

(2)The licensee shall install and maintain at its own cost, the

pipeline and other requirements required for conveying water

from the source of supply to the place of actual use. The

expenditure towards the drawl of water i.e. installation of

pumps, Pipelines, meters and all other requirements in

connection with the drawl of water, shall be borne by the

licensee.

(3)The licensee shall draw water directly from Mahi River, near

village Vasad to the extent of 56370 Cubic meters per day

throughout the year or less as may be required for the

Executive EngineerVadodrra lrrigation Division

VADODARA.

(ff- S- GrrqrerirG. D. PARASHAR

Chief Power & Utilities ManagerLO. C.L., Guiarat Refinery,

Vadodara.

-3-

Page 15 of 244

optimum plant capacity under operation from time to time' lt

would be permissible for the Licensee to increase the intake up

to 56370 Cubic meters per day for a period not exceeding one

month with the approval of the Narmada, water Resources,

water supply & Kalpsar Department to facilitate the filling of

the licensee reservoir'

(4)(1) The license agrees to bear the cost herein below detailed

that may be apportioned between the beneficiaries on prorate

basis of their demands, on account of remodeling that may

take place to meet the total requirements of the beneficiaries

in case supply of water to him is from Mahi River, near village

Vasad.

(4X2) Not APP|icable.

(S)The licensee shall pay a license fee at the rate of Rs'5011- per

year or at as such rates as may be fixed by the Government

from time to time in that behalf during the subsistence as the

agreement.

(6)The licensee shall pay for the quantity of water drawn, as

measured in the manner provided under clause-7 below, at the

rates and terms given below.

(i) The Licensee shall pay the water charges for the quantity of

\ff- S- ErrqrerqG. D. PARASHAR

Chief Power & Utilities Managerl.O. C. L., Guiarat Refinery,

Vadodara.

Executive EngineerVadodara lrrigation Divis'on

VADOOARA.

water actually drawn as per the rates mentiged in the

_=il& 4. g

Page 16 of 244

Government of Gujarat, Narmada, Water Resources, Water

Supply & Kalpsar Department Resolution No.WTR/20O5/41"1P

dtd: 03.02.2007, effective from 0L.01.2007 subject to

fulfillment of conditions laid down in above mentioned

resolution as well as conditions mentioned in sanction letter.

(ii)The interest rates, penalty and all other charges/conditions

mentioned in above mentioned Government of Gujarat,

Narmada, Water Resources, Water Supply & Kalpsar

Department, resolution No.WTR/TOj'/ At/P, dated : 03.O2.20O7

shall be applicable and the licensee shall have to fulfill it.

(iii) The above rates so fixed shall be subject to upward

revision that may be made by the government in Narmada,

Water Resources, Water Supply & Kalpsar Department from

time to time in connection with water reserved and used for

irrigation & non-irrigation purpose. The rates fixed by the

government shall be exclusive of cost of pumping, conveying

etc. of water from the resource.

(iv) The charges as mentioned in sub clause-(i), above, shall

be paid in advance by the Licensee before 10th day of each

month following the month to which water charges pertains

calculated as per the estimated requirement of water for the

month. The bills as per actual payment of charges shall be

prepared every month and served on the Licensee for payment

there of.a)

ab544S- S- qr<Ter<

G. D. PARASHARChief Power & Utrlitres ManagerI O.C.L, Gujarat Refineiy,

Vadodara.

Executive EngineerVadodara lrrigation Divisbn

VADODARA.

-5-

Page 17 of 244

L

L

(v)lf the arrears of water charges referred to above accumulate

for more than six months, the Government shall be at liberty to

ask the licensee to stop drawl of water from the source and it

shall be incumbent on the licensee to do so and in case of

default, Government may take action to stop entry into the

intake without any notice at the risk and cost of the licensee.

(vi) lf the measuring devices referred to in Clause-7 below,

ceases to function or goes out of order in any month, the

charges leviable in respect of that month shall be calculated on

the basis of the average quantity of water drawn in the

preceding three months or the quantity of water drawn in the

same month of preceding year whichever is higher, provided

that there has been no increase in the capacity of the

plant/plants and the corresponding water requirements

thereof during such year. lf the capacity of the Plant/Plants has

increased during such year, the water drawn shall be

correspondingly estimated on the prorata basis. For the

purpose of such estimate, the licensee shall furnish necessary

data to the Executive Engineer concerned whose decision in the

matter shall be final and binding to the licensee.

(7)A suitable scientific measuring device shall be installed by the

Licensee at suitable place in consultation with and with the

approval of the Executive Engineer, Vadodara lrrigation

-A<.) Executive EnEineerVadodara lrrigation Division

VADODARA.\ff_ €- rrT<TarqG. D. PARASHAR

Chief Power & Utilities Managerl. O. C. L., Guiarat Refineiy,

Vadodara.

-6

Page 18 of 244

Division, Vadodara or his successor in office for measuring the

quantity of water drawn by the Licensee.

The cost of measuring device, its installation and

of the quantity of water drawn shall be taken jointly by

representative of the Government and of the Licensee'

measuring device shall be open for inspection by the concerned

authorities.

(8)lf the measuring device referred to in the clause-7, ceases to

function or goes out of order, the Licensee shall, as and when

such occasion arises, get necessary repairs thereto carried out

and restore the same to its original position or replace the

same if so found necessary and as required by the Executive

Engineer concerned within one month of its going out of order.

(9)The water drawn by the Licensee from the Mahi River shall be

used only for the purpose for which permission to use the same

is granted to him and as such the use shall be confined to the

legitimate requirement of the Licensee.

The Licensee shall not draw water from the above mentioned

sources for sale or supply to any person, firm or Company other

body by whatever named called except GSFC Vadodara who is

the joint owner with Gujarat Refinery for 2 Nos. of wells A & B

on Mahi river. The water supplied to and used to GSFC from

these wells shall be treated from the reserve quantitgof GSFC.

-de&'rff- g- Err<Ter<

G. D. PARASHARChief Power & Utilities Managerl.O.C.L., Gularat Refinery,

Vadodara.

maintenance shall be borne by the Licensee. The measurement

Vadodara lrrigation D ivision

the

The

-7 -

YADOOXI/L

Page 19 of 244

(10x1) The grant of the permission to draw water'under this

agreement shall not mean any assurance to the Licensee

regarding availability of quantity of water as per the

requirements of the Licensee and regarding the quality of

water. The Licensee shall not be entitled to any compensation

for non availability of quantity of water on account of reasons

beyond the control of the Government / Department' lt shall

be incumbent on the licensee to make its own arrangement to

meet its requirement of water during the period when water is

not available in the river. No water shall be released from Mahi,

Kadana or Panam or sardar Sarovar Project in the river.

(10X2) lf the special measures for conserving the water and

reducing the losses of evaporation and seepage are found

necessary in scarcity years, the expenses on this account shall

be borne by the Licensee.

(11) The permission granted in this agreement shall not in any

manner prejudicially affect the existing water rights vested in

the riparian owners nor shall it any way prejudice the rights of

government to launch or implement any new scheme or

schemes in public interest in connection with the water of Mahi

river from which Licensee is permitted to draw water'

The drawl of water under this agreement by the licensee

shall be subject to -the provisions of the Bombay lrruation Act,

w 8 w4(f,f- S- qrqrgT< Execltive Engine.er

G' D' PARASHAR Vaa;ara krigation DivirbnChief Power & Utilities Manager VADOOARA'LO.C. L., Guiarat Refinery,

Vadodara.

(12)

Page 20 of 244

1,879 and rules made there under as amended from time to

time and orders that may be passed or issued in that behalf by

the Government/Department from time to time.

(13) The Licensee shall at all reasonable times allow the

officers of the government to inspect the work sites and

records regarding quantity of water drawn, utilized and

supplied to other parties, if any and to take copy of the records.

(I4) An amount equivalent to three months prevailing water

charges shall be initially deposited by the licensee with the

Executive Engineer, Vadodara lrrigation Division, Vadodara or

his successor in the office as security deposit for the due

performance of the terms of this agreement. The deposit shall

be in the form of fixed deposit in any scheduled bank and shall

be pledged by the licensee in favors of the Executive engineer,

Vadodara irrigation Division, Vadodara or his successor in

office. The enhancement in amount of security deposit due to

yearly increase in the rate of water charges also be deposited

by the Licensee.

(15) The Executive Engineer, Vadodara irrigation Division,

Vadodara shall dispose of all matters pertaining to this

agreement subject and falling within his purview subject to

decision that may be taken in appeal before the Superintending

Engineer, Vadodara lrrigation Circle, Vadodara in the matter

(ff- r+- qrqrer...G. D. PARA S t.{A R

Chief Power & Uti,itrt.,s ivtanagerl.O. C. L., Gujarar i{efineiy,

Vadodara.

Executive EngineerVadodara lrrigation Division

VADODAR.A.

Page 21 of 244

and the decision of the Superintending Engineer in the matter

shall be final.

(16) The licensee shall make its own arrangements for storing

its water requirement of about 1-5 days.

(17) The Licensee shall arrange at its own cost the discharge of

the trade waste and effluents after due treatment as may be

permitted from time to time by the State Water Pollution

Control Board safely in place ear-marked for the purpose in the

vicinity in consultation and with the approval of Public Health

Authority. ln case where the Collector, Vadodara District finds

that the arrangement of discharge is not suitable, it shall be the

duty of Licensee to make other suitable arrangement as may be

directed by him. lf the discharge of trade waste and effluent

proves to be a source of nuisance to the field and or the

population in the neighborhoods, the Licensee shall treat the

same further in such manner as may be directed by the

Government.

(18) This agreement shall remain in force for a period of 5

(Five) years from the date of 08.02.2012 unless terminated

earlier, by the Licensee by giving six calendar month's notice in

writing to the Government for the purpose. The licensee shall

not be eligible for any compensation on account of such

prematu re termination.

,.r"1;llifi ,i,?1,'?iiL""VADODARA.rift- €- qr<Ter<

G. D. PARASHARChief Power & Utilities Managerl.O.C.L , Gularat Refinery,

Vadodara.

-10-

Page 22 of 244

(19) The Government may allow the drawl of water according

to the terms stated in this agreement after the expiry of the

agreement on receipt of a request to that effect from the

Licensee at least six month before the expiry of the period of

this agreement.

(20) The Licensee shall bear all the legal charges, stamp duty,

registration fees and translation charges and all other charges

and expenses incurred in connection with this presents.

{21) The Government shall be entitled to terminate this

agreement upon serving the Licensee with a notice of six

months for breach of any of the terms and conditions of this

agreement or in the event the Licensee fails to pay any sum

due to the Government under this agreement. The Licensee

shall not be eligible to claim any compensation from the

Government on account of withdrawing the facility of drawl of

water aS a result of premature termination of the agreement or

even otherwise. Without prejudice to any right of the

Government to proceed in accordance with the relevant rule

No.6 (v) to recover such sums due from the Licensee, the

security deposit shall be forfeited. Any drawl of water from the

Mahi River, near village Vasad after the expiry of the period of

the notice shall be treated as unauthorized act and shall be

subject to such penal charges as may be determined by the

Government.

(22) Except as otherwise herein provided, all notices to be

given and other actions to be taken on behalf of the Licensee

shall be given or taken by the Chief Power & Utilities Manager,

Gujarat Refinery (IOCL), Vadodara or any other official

authorized by the Iicensee.

. Executive EngineerVedodara lrrigation Divigiorl

VADODARAEft. S- qrqTerirG. D. PARASHAR

Chief Power & Utilities Managerl.O. C. L., Gularat Refineiy,

Vadodara.

Lt-

Page 23 of 244

(23) All sums and amount due and payable under this

agreement shall be recoverable as arrears of land revenue

under the Bombay Land Revenue Code, 1879 without prejudice

to any other rights or remedies available to the Government

under any other case.

lN WITNESS WHERE OF Shri G.D.Parashar, Chief Power &

Utilities Manager, Gujarat Refinery, Vadodara duly authorized

by the Board of Director of the Licensee for and on behalf of

the licensee and Shri BS Chaudhary, Executive Engineer,

Vadodara lrrigation Division, Vadodara for and on behalf of the

Governor of Gujarat have signed there presents and herein set

their respective seals on the day and year first above written.

s}- €t- qr<rer<G. D. PARASHAR

, Erccutlve EnginccrSigned, Vadodera lrrigrtion Division

Sealed and del

Shri B.S. Chaudhary,

Executive Engineer,

Vadodara lrrigation Division,

Vadodara.

For and on behalf of the

Governor of Gujarat in

Presence of Witness

Witness (l) ft4*et'c r- P' P"+'\)

hief Po ManagerO.C.L

Signe v'v L efinery'

Sealed and delivered by

Shri G,D.Parashar

Chief Power & Utilities Manager

Gujarat Refi nery (IOCL)

Vadodara.

For and on behalf of the

Licensee in presence of

PfeSenCe 6f \A/i+nacc

Witness (l)c-d ftt'+t>-:::?,r rlR c6 " -' r t>LU)v (ry vlatox1ez | '

/4"'cr.D .u'fl 2L t'4)

1n"a,tct/-"(P3 u )

*-$rnWitness (ll)

t2

Witness (ll)S-r,

Page 24 of 244

TPI OIL

SEPARATOR

TPI

SUMP

EQU.

TANKSURGE

SUMP

SURGE

TANK

Polyelectrolyte

FLASH

MIXER

PAC H2SO4INFLUENT

FROM GR/

GRE SUMP

FLOCCULATION

TANK

Polyelectrolyte

INFLUENT

FROM GHC

& GRSPF

DAF

TANKFT SUMP

BIO

TOWER

AERATION

TANK

SLUDGE

LAGOON

SLOP

OIL

TANK

BOTTOM

SLUDGE

SKIMMED

OIL

CLARIFIER

A/B

GUARD

POND

OVERFLOW

PSF/ ACFTREATED

EFFLUENT

SLOP

OIL

SUMP

OILY

SLUDGE

PIT

CHEMICAL

SLUDGE

PIT

MELTING

PIT

UNDERFLOW

BIO

SLUDGE

SUMP

RECYCLE

WASTING

SLUDGE

THICKENER CENTRIFUGE

BIO SLUDGE

DRYING BED

Polyelectrolyte

SKIMMED

OIL

BLOCK FLOW DIAGRAM OF CETP AT GUJARAT REFINERY ANNEXURE - A

BACTERIAL

CULTURE

Polyelectrolyte

Polyelectrolyte

Abbreviations :

PAC - Poly aluminium chloride

PE - Polyelectrolyte

Note: Flow losses due to TPI oil skimming,

des ludging and DAF des ludging w i l l be

calculated as below:

a) TPI oil skimming and desludging:

b) DAF de sludging:

FI-04

FI-05

PumpPer day running

hrs (A), hrs

Pump capacity

(B), m3/hr

P-13A

P-13B

Flow (A*B/24),

m3/hr

P-13C

P-13D

P-08A

P-08B

Volume of sludge

collected in sump

(A), m3

Nos. of time

sump is filled in

a day (B)

Flow (A*B/24),

m3/hr

FI-08

TOWNSHIP

SEWAGESIPHON DRAIN TO

SURGE SUMPFILTER BACK WASH TO

AERATION TANK/ SURGE SUMP

OIL SKIMMING TO

SURGE SUMP

OIL SKIMMING TO

SURGE SUMP

DRAIN TO

SURGE SUMP

HRSCC

OVERFLOW

Cowdung &

jaggery

Page 25 of 244

Hecs

Typewritten text

Annexure-8

Page 26 of 244

Consultancy

Typewritten text

Annexure-9

UNIT STACK TEMP.C DIA OF GAS VEL. FLUE GAS FLUE GAS HYDRO CARBON

T STACK VOLUME VOLUME CARBON MONOXIDE

M M/SEC AT T.C AT 25 .C

M3/SEC M3/SEC mg/Nm3 kg/hr kg/day ppm mg/Nm3 kg/hr ppm mg/Nm3 kg/hr ppm ppm

SRU-II (New) ~ 1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

SRU-I (Old) ~ 1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

SRU-F03 166 1.7 9.36 21.23 14.41 ~ ~ ~ 42.2 110.5 5.7 38.6 72.47 3.76 ~ 1.2

STACK CALCULATION FOR THE PERIOD OF January-2015.

SULPHUR OXIDES

MATTER DIOXIDE OF

PARTICULATE

For Maxwell Engineers

SRU

Remarks: Under shutdown in SRU (New) & (Old) stack in date of 09/01/2015

NITROGEN

SRU

Page 27 of 244

Consultancy

Typewritten text

Annexure-10

UNIT STACK TEMP.C DIA OF GAS VEL. FLUE GAS FLUE GAS PARTICULATE HYDRO CARBON




AU-I

F-1 226 2.4 8.79 39.74 23.73 64.9 5.54 132.96 67.6 176.94 15.1 42.6 79.98 6.83 1 1.3

F-2 234 1 9.15 7.18 4.22 42.3 0.64 15.36 46.9 122.76 1.9 43.6 81.86 1.24 1.3 1.6

F-3 214 0.8 8.15 4.09 2.5 31.6 0.28 6.72 34.9 91.35 0.8 34.2 64.21 0.58 1.2 1.4F-4 226 0.8 8.95 4.5 2.69 42.6 0.41 9.84 47.6 124.59 1.2 42.9 80.55 0.78 0.9 1.2F-5 240 1.1 7.89 7.49 4.35 51.3 0.8 19.2 42.1 110.19 1.7 51.3 96.32 1.51 1.2 1.6

15.1 6.83

F-1 242 2.4 9.21 41.64 24.09 56.6 4.91 117.84 62.3 163.07 14.1 42.3 79.58 6.9 1.1 1.3

F-2 227 1 8.43 6.62 3.95 34.9 0.5 12 37.6 98.42 1.4 33.6 63.09 0.9 1.2 1.4

F-3 238 0.8 8.06 4.05 2.36 46.9 0.4 9.6 44.4 116.21 1.0 37.3 70.03 0.59 1 1.3

F-4 0.8 0 0 0 0 0 0.0 0 0

F-5 1.1 0 0 0 0 0 0.0 0 0

14.1 6.9

F-2 232 2.1 9.23 31.95 18.85 34.6 2.35 56.4 46.9 122.76 8.3 26.9 50.51 3.43 1.2 1.5

F-3 221 1.7 8.34 18.92 11.41 26.9 1.1 26.4 34.9 91.35 3.8 22.6 42.43 1.74 1.0 1.2

11.6 2.75

CRU 21-F-01 240 0.84 9.11 5.05 2.93 16.9 0.18 4.32 38.9 101.82 1.1 41.3 77.54 0.818 1 1.2

CRU 21-F-02 236 1.1 8.34 7.92 4.64 14.3 0.24 5.76 31.3 81.93 1.4 30.2 56.7 0.947 0.8 1

CRU 22-F-01 224 1.28 9.15 11.77 7.06 12.3 0.31 7.44 27.6 72.24 1.8 24.9 46.75 1.188 1 1.3

CRU F1 38 2.2 - - - - - - 15.9 41.62 21.3 39.99 1.2 1.5

4.3 2.135

UDEX Udex 172 1.88 ~ ~ ~ - ` ` 19.6 51.3 ~ 24.6 46.19 ~ 1.1 1.4

AU-V

AU-5 243 3.15 9.41 73.3 42.33 58.6 8.93 214.32 62 162.02 24.7 41.3 77.54 11.816 1.3 1.7

FCC

CO-BOILER 142 2.6 15.6 82.78 59.44 142 30.39 729.36 46.9 122.76 26 43.6 81.86 17.52 ~ 4.8

FCCU Charge Heater 234 1.9 8.16 23.12 13.59 10 0.49 11.76 22.3 58.37 2.9 35.9 67.4 3.3 1 1.2

FPU-1 8/2 F01 224 2.3 8.69 36.09 21.64 9.6 0.75 18 43.6 114.12 8.9 22.9 43 3.35 1.2 1.5

OF

NITROGEN

AU-II

STACK CALCULATION FOR THE PERIOD OF FEBRUARY-2015.

SULPHUR OXIDES

MATTER DIOXIDE

AU-III

CRU

Page 28 of 244

UNIT STACK TEMP. DIA OF GAS VEL. FLUE GAS FLUE GAS OXIDES HYDRO CARBON

T0C STACK VOLUME VOLUME CARBON MONOXIDE

M M/SEC AT T.C AT 25 .C NITROGEN


F-101 133 1.7 7.65 17.36 12.74 9 0.41 9.84 9.8 25.65 1.2 23.3 43.75 2.01 1.1 1.3

F-01 146 3.5 8.97 86.26 61.35 14.6 3.22 77.28 12.1 31.67 7.0 24.6 46.19 10.20 1.0 1.2

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 144 3 ~ ~ ~ ~ ~ ~ 72.3 188.87 ~ 26.9 50.51 ~ 1.1 1.5

GRE

AU-IV AU-IV712F01 213 1.9 7.88 22.33 13.69 54.2 2.67 64.1 67 175.89 8.7 46.6 87.49 4.31 1.0 1.3

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 234 2.4 9.12 41.24 24.24 33.2 2.9 69.6 108 282.68 24.7 33.6 63.09 5.51 1.2 1.4

CDU-E 232 1.9 8.02 22.73 13.41 24.6 1.19 28.56 52.6 137.68 6.7 37.6 70.6 3.4 1.3 1.5

CDU-W 213 1.9 8.26 23.41 14.35 32.6 1.68 40.32 64.9 169.87 8.8 42.3 79.42 4.1 1.0 1.3

BBU F-1 361 1.3 8.64 11.46 5.39 23.4 0.45 10.8 23.6 61.77 1.2 26.9 50.51 0.98 0.8 1.0

BBU F-2 392 1.3 9.11 12.09 5.42 26.1 0.51 12.24 18.6 48.68 1.0 27.6 51.82 1.01 1.0 1.2

48.77 17.33

CGP-I HRGS-1 126 3.5 8.12 78.08 58.32 7.0 1.47 35.28 6.4 16.75 3.5 18.9 35.49 7.451 1.1 1.3

HRGS-2 141 3.5 7.69 73.95 53.23 9.0 1.72 41.28 5.5 14.4 2.8 22.9 43 8.24 1 1.2

HRGS-3 133 3.5 8 76.93 56.47 7.5 1.52 36.48 7.1 18.58 3.8 31.9 59.89 12.175 0.8 1.0

CGP-II HRGS-4 141 3.5 8.78 84.43 60.77 8.4 1.84 44.16 6.8 17.8 3.9 26.4 49.57 10.845 1.1 1.3

HRGS-5 138 3.5 9.14 87.89 63.73 9.4 2.16 51.84 5.1 13.35 3.1 18.9 35.49 8.142 0.9 1.1

FPU-II

FPU -03FF001 227 2.67 9.07 50.76 30.25 51.6 5.62 134.88 129 337.65 36.8 37.6 70.6 7.688 1.2 1.4

32.5 9.88

HCU 1&2 234 2.1 8.26 28.59 16.8 42.3 2.56 61.44 137 358.59 21.7 34.6 64.96 3.93 1.2 1.6

HCU 3&4 247 2.1 8.79 30.43 17.44 32.9 2.07 49.68 124 324.56 20.4 40 75.1 4.72 1.3 1.7

MSQ 15 F01-04 141 2.9 9.21 60.8 43.76 8.0 1.26 30.24 7 18.32 2.9 33.6 63.1 10 0.9 1.2

14 F01 153 1.57 7.79 15.07 10.54 8.5 0.32 7.68 6.1 15.97 0.6 38.1 71.5 3 1.0 1.3

15 F05 137 1.45 8.12 13.4 9.74 7.4 0.26 6.24 5.9 15.44 0.5 42.3 79.4 3 1.2 1.6

15 F01 157 1.45 7.94 13.1 9.08 8.6 0.28 6.72 8.9 23.3 0.8 29.5 55.4 2 1.0 1.2

LAB Hot iol 2063F01 234 4.5 9.34 148.47 87.27 56.9 17.88 429.12 137.0 358.59 113 42.3 79.42 24.952 1.2 1.6

2061 F-001 207 0.7 8.16 3.14 1.95 29.5 0.21 5.04 49.6 129.83 0.9 21.6 40.56 0.285 1.3 1.6

114 25.24

PARTICULATE SULPHUR

DIOXIDE

HGU-III

MATTER OF


HCU

Page 29 of 244





DHDS DHDS 223 1.6 7.86 15.8 9.49 12.9 0.44 10.56 28.9 75.64 2.6 42.9 80.55 2.752 1.2 1.4

F-01-F-02 127 1.7 8.06 18.29 13.63 13.6 0.67 16.08 12.6 32.98 1.6 27.6 51.82 2.54 1.3 1.5

DHDT F- 01 142 1.75 8.69 20.89 15 19.6 1.06 25.44 16.6 43.45 2.4 34.6 64.96 3.51 0.8 1.0

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 154 1.7 8.98 20.37 14.22 0 0 83.6 218.82 11.2 38.6 72.47 3.71 1.2

DCU F-01 142 2 9.08 28.51 20.47 13.6 1 24 23.9 62.56 4.6 42.3 79.42 5.85 1 1.3

F- 02 153 2 8.64 27.13 18.98 20.6 1.41 33.84 18.6 48.68 3.3 23.9 44.87 3.07 1.2 1.4

VGO_HDT

F-01/F22 159 1.2 8.13 9.19 6.34 29.9 0.68 16.32 43.6 114.12 2.6 38.9 73.04 1.67 1.0 1.3

HU-I HU-I 219 2.1 7.96 27.56 16.69 14.6 0.88 21.12 12.6 32.98 2.0 38.6 72.47 4.354 1.1 1.3

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

PARTICULATE SULPHUR

MATTER DIOXIDE OF


ISOM

SRU

Page 30 of 244

UNIT STACK TEMP.C DIA OF GAS VEL. FLUE GAS FLUE GAS HYDRO CARBON




SRU-II (New) ~ 1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

SRU-I (Old) ~ 1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

SRU-F03 174 1.7 8.98 20.37 13.58 ~ ~ ~ 52.3 136.9 6.7 41.1 77.17 3.77 ~ 1

STACK CALCULATION FOR THE PERIOD OF March-2015.

SULPHUR OXIDES

MATTER DIOXIDE OF

PARTICULATE

For Maxwell Engineers

SRU

Remarks: Under shutdown in SRU (New) & (Old) stack in date of 17/03/2015

NITROGEN

SRU

Page 31 of 244





AU-I

F-1 255 2.4 8.88 40.15 22.66 88.6 7.23 173.52 82.2 215.15 17.6 42.3 79.42 6.48 1 1.3

F-2 238 1 9.22 7.24 4.22 55.6 0.84 20.16 62.6 163.85 2.5 29.6 55.58 0.84 1.1 1.5

F-3 244 0.8 8.02 4.03 2.32 42.6 0.36 8.64 34.9 91.35 0.8 35.6 66.84 0.56 0.8 1.0F-4 222 0.8 7.94 3.99 2.4 38.6 0.33 7.92 48.6 127.21 1.1 42.3 79.42 0.69 1 1.2F-5 248 1.1 8.11 7.7 4.4 33.3 0.53 12.72 51.2 134.01 2.1 27.6 51.82 0.82 1.2 1.5

17.6 6.48

F-1 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-2 ~ 1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-3 ~ 0.8 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-4 ~ 0.8 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-5 ~ 1.1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-2 245 2.1 8.26 28.59 16.45 33.6 1.99 47.76 42.3 110.72 6.6 24.6 46.19 2.74 1.1 1.4

F-3 228 1.7 9.02 20.46 12.17 24.9 1.09 26.16 31.3 81.93 3.6 18.6 34.92 1.53 1.0 1.2

11.6 2.75

CRU 21-F-01 258 0.84 8.26 4.58 2.57 26.6 0.25 6 33.3 87.16 0.8 26.6 49.94 0.462 1 1.2

CRU 21-F-02 242 1.1 9.05 8.6 4.98 13.6 0.24 5.76 22.9 59.94 1.1 30.3 56.89 1.02 0.9 1

CRU 22-F-01 231 1.28 8.22 10.57 6.25 16.9 0.38 9.12 28.6 74.86 1.7 24.9 46.75 1.052 1.2 1.4

CRU F1 41 2.2 - - - - - - 16.6 43.45 32.3 60.64 1.5 1.9

3.6 2.072

UDEX Udex 158 1.88 ~ ~ ~ - ` ` 14.6 38.21 ~ 31.3 58.77 ~ 1.1 1.6

AU-V

AU-5 252 3.15 8.88 69.17 39.26 58.6 8.28 198.72 99 258.08 36.5 62.5 117.35 16.586 1.3 1.6

FCC

CO-BOILER 140 2.6 13.8 73.23 52.84 127 24.16 579.84 58.6 153.38 29 18 33.8 6.43 ~ 4.6

FCCU Charge Heater 238 1.9 8.61 24.4 14.23 12.6 0.65 15.6 38.5 100.77 5.2 22.3 41.87 2.14 1.1 1.3

FPU-1 8/2 F01 248 2.3 9.09 37.75 21.59 16.6 1.29 30.96 62.6 163.85 12.7 58.6 110.02 8.55 1.3 1.6

AU-III

CRU

NITROGEN

AU-II

STACK CALCULATION FOR THE PERIOD OF AUGUST-2015.

SULPHUR OXIDES

MATTER DIOXIDE OF

Page 32 of 244





F-101 166 1.7 9.12 20.69 14.04 16.6 0.84 20.16 48.6 127.21 6.4 14.6 27.41 1.39 1.2 1.5

F-01 188 3.5 8.26 79.43 51.35 18.6 3.44 82.56 18.6 48.68 9.0 42.3 79.42 14.68 1.0 1.3

TPS B1 155 3 7.66 54.12 37.68 33.3 4.52 108.48 62.3 163.07 22.1 10.6 19.9 2.70 1.1 1.3

B2 164 3 8.14 57.51 39.22 28.6 4.04 96.96 74.6 195.26 27.6 51.6 96.88 13.68 1.2 1.5

B3 155 3 7.89 55.74 38.81 38.6 5.39 129.36 34.6 90.56 12.7 44.6 83.74 11.70 1.0 1.3

B4 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

GRE

AU-IV AU-IV712F01 233 1.9 8.09 22.93 13.5 54.6 2.65 63.6 72 189.24 9.2 33.3 62.52 3.04 1.3 1.6

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 248 2.4 9.08 41.06 23.49 44.6 3.77 90.48 122 319.33 27.0 48.6 91.25 7.72 1.2 1.4

CDU-E 252 1.9 8.29 23.49 13.33 28.9 1.39 33.36 88.9 232.69 11.2 53.6 100.64 4.8 1 1.2

CDU-W 237 1.9 7.88 22.33 13.05 37.6 1.77 42.48 66.9 175.11 8.2 42.6 79.98 3.76 1.3 1.5

BBU F-1 366 1.3 9.44 12.52 5.84 18.6 0.39 9.36 33.6 87.95 1.9 40.6 76.23 1.6 1.1 1.3

BBU F-2 329 1.3 8.69 11.53 5.71 26.6 0.55 13.2 22.9 59.94 1.2 34.9 65.53 1.35 1.0 1.3

55.60 19.35

CGP-I HRGS-1 144 3.5 8.22 79.05 56.49 10.6 2.16 51.84 1.2 3.14 0.6 33.3 62.52 12.714 1.2 1.5

HRGS-2 130 3.5 7.69 73.95 54.68 13.6 2.68 64.32 2.1 5.5 1.1 12.3 23.09 4.545 0.9 1.0

HRGS-3 149 3.5 8.12 78.08 55.14 9.8 1.95 46.8 3.3 8.64 1.7 9.9 18.59 3.69 1.1 1.3

CGP-II HRGS-4 155 3.5 8.48 81.55 56.78 12.3 2.51 60.24 55.6 145.53 29.8 30.3 56.89 11.629 1.2 1.5

HRGS-5 163 3.5 9.12 87.7 59.94 14.6 3.15 75.6 62.6 163.85 35.4 27.6 51.82 11.182 1 1.3

FPU-II

FPU -03FF001 242 2.67 8.77 49.08 28.4 42.8 4.38 105.12 125 327.18 33.5 37.6 70.6 7.218 1.1 1.3

32.5 9.88

HCU 1&2 234 2.1 8.64 29.91 17.58 51.3 3.25 78 112 293.15 18.6 40 75.1 4.75 1.0 1.2

HCU 3&4 246 2.1 9.32 32.26 18.52 37.6 2.51 60.24 127 332.42 22.2 53.3 100.07 6.67 1.1 1.4

MSQ 15 F01-04 166 2.9 9.11 60.14 40.82 12.6 1.85 44.4 4.6 12.04 1.8 33.6 63.1 9 0.8 1

14 F01 152 1.57 8.33 16.12 11.3 9.9 0.4 9.6 5 13.09 0.5 29.9 56.1 2 1.0 1.2

15 F05 144 1.45 7.48 12.35 8.83 14.6 0.46 11.04 7.6 19.89 0.6 30.3 56.9 2 0.9 1.2

15 F01 152 1.45 8.26 13.63 9.56 9 0.31 7.44 10 26.17 0.9 24.9 46.8 2 1.2 1.5

LAB Hot iol 2063F01 232 4.5 8.91 141.64 83.58 26.6 8 192 112.0 293.15 88 44.6 83.74 25.196 1.2 1.5

2061 F-001 222 0.7 8.29 3.19 1.92 42.3 0.29 6.96 38.6 101.03 0.7 23.6 44.31 0.306 1 1.2

89 25.50

OF


HCU

HGU-III

MATTER

PARTICULATE SULPHUR

DIOXIDE

Page 33 of 244





DHDS DHDS 223 1.6 8.45 16.98 10.2 18.6 0.68 16.32 26.6 69.62 2.6 41.3 77.54 2.847 1.2 1.4

F-01-F-02 144 1.7 7.55 17.13 12.24 18.6 0.82 19.68 22.2 58.11 2.6 33.3 62.52 2.76 1.4 1.7

DHDT F- 01 167 1.75 9.04 21.73 14.72 26.6 1.41 33.84 15.6 40.83 2.2 31.6 59.33 3.14 1 1.3

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 172 1.7 8.91 20.21 13.53 0 0 86.6 226.67 11.0 34.6 64.96 3.16 1.4

DCU F-01 166 2 8.39 26.34 17.88 21.3 1.37 32.88 11.3 29.58 1.9 14.6 27.41 1.76 1 1.4

F- 02 152 2 9 28.26 19.82 31.6 2.25 54 8.9 23.3 1.7 10.3 19.34 1.38 1.2 1.5

VGO_HDT

F-01/F22 157 1.2 7.67 8.67 6.01 32.6 0.71 17.04 21.6 56.54 1.2 16.6 31.17 0.67 1.2 1.5

HU-I HU-I 234 2.1 8.45 29.25 17.19 14.6 0.9 21.6 18.6 48.68 3.0 33.6 63.09 3.904 1.1 1.6

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Remark:- Under shudwon in stack TPS B-4,, VBU- 731F01, HGU-II, SRU (Old), & (New) for Month of August- 2015.

SRU

ISOM

PARTICULATE SULPHUR

MATTER DIOXIDE OF


Page 34 of 244





AU-I

F-1 241 2.4 7.94 35.9 20.81 72.6 5.44 130.56 66.5 174.06 13.0 38.6 72.47 5.43 1.1 1.4

F-2 222 1 9.04 7.1 4.27 43.9 0.67 16.08 59.6 156 2.4 41.6 78.11 1.2 0.9 1.1

F-3 252 0.8 8.69 4.37 2.48 37.6 0.34 8.16 46.9 122.76 1.1 30.6 57.45 0.51 1.0 1.2F-4 238 0.8 8.34 4.19 2.44 46.9 0.41 9.84 39.4 103.13 0.9 34.9 65.53 0.58 1.1 1.3F-5 255 1.1 7.81 7.42 4.19 36.4 0.55 13.2 42.7 111.77 1.7 33.5 62.9 0.95 1.2 1.6

13.0 5.43

F-1 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-2 ~ 1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-3 ~ 0.8 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-4 ~ 0.8 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-5 ~ 1.1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-2 253 2.1 8.14 28.18 15.97 38.6 2.22 53.28 46.6 121.97 7.0 22.1 41.49 2.39 1.0 1.2

F-3 247 1.7 9.20 20.87 11.96 27.7 1.19 28.56 28.6 74.86 3.2 19.6 36.8 1.58 1.2 1.5

11.6 2.75

CRU 21-F-01 248 0.84 8.75 4.85 2.77 31.3 0.31 7.44 38.6 101.03 1.0 22.2 41.68 0.416 0.8 1

CRU 21-F-02 256 1.1 9.12 8.66 4.88 15.6 0.27 6.48 27.6 72.24 1.3 25.6 48.07 0.844 0.9 1.1

CRU 22-F-01 243 1.28 7.92 10.19 5.88 13.6 0.29 6.96 22.6 59.15 1.3 31.3 58.77 1.244 1.1 1.3

CRU F1 42 2.2 - - - - - - 15.6 40.83 26.9 50.51 1.4 1.8

3.5 2.088

UDEX Udex 162 1.88 ~ ~ ~ - ` ` 8 20.94 ~ 14.6 27.41 ~ 1.0 1.3

AU-V

AU-5 247 3.15 9.16 71.35 40.89 48.6 7.15 171.6 76 197.88 29.1 43.6 81.86 12.05 1.2 1.5

FCC

CO-BOILER 146 2.6 11.9 63.15 44.91 134 21.66 519.84 44.6 116.74 19 16 30.04 4.86 ~ 4.8


FPU-1 8/2 F01 253 2.3 9.24 38.37 21.74 15 1.17 28.08 21.9 57.32 4.5 13.9 26.1 2.04 1.3 1.7

OF

NITROGEN

AU-II

STACK CALCULATION FOR THE PERIOD OF SEPTEMBER-2015.

SULPHUR OXIDES

MATTER DIOXIDE

AU-III

CRU

Page 35 of 244





F-101 156 1.7 7.92 17.97 12.48 15 0.67 16.08 27.6 72.24 3.3 12.6 23.66 1.06 1.0 1.3

F-01 172 3.5 9.14 87.89 58.86 17.5 3.71 89.04 16.9 44.23 9.4 8.6 16.15 3.42 1.2 1.5

TPS B1 160 3 8.65 61.11 42.06 38.6 5.84 140.16 52.1 136.37 20.7 12.6 23.66 3.58 1.0 1.3

B2 153 3 9.25 65.35 45.71 26.6 4.38 105.12 46.9 122.76 20.2 26.9 50.51 8.31 1.2 1.6

B3 157 3 7.94 56.1 38.88 27.6 3.86 92.64 26.9 70.41 9.9 21.9 41.12 5.76 1.0 1.2

B4 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

GRE

AU-IV AU-IV712F01 244 1.9 7.95 22.53 12.99 46.6 2.18 52.3 65 169.09 7.9 35.5 66.65 3.12 1.1 1.3

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 251 2.4 9.11 41.19 23.42 38.9 3.28 78.72 113 295.77 24.9 40.6 76.23 6.43 1 1.2

CDU-E 234 1.9 8.42 23.86 14.02 24.6 1.24 29.76 76.1 199.19 10.1 42.6 79.98 4.0 0.9 1.1

CDU-W 246 1.9 7.64 21.65 12.43 30.9 1.38 33.12 58.6 153.38 6.9 34.9 65.53 2.93 1.2 1.5

BBU F-1 375 1.3 8.49 11.26 5.18 15.6 0.29 6.96 28.9 75.64 1.4 26.9 50.51 0.94 1 1.3

BBU F-2 341 1.3 8.88 11.78 5.72 19.6 0.4 9.6 18.6 48.68 1.0 24.6 46.19 0.95 1.0 1.2

49.76 16.52

CGP-I HRGS-1 138 3.5 7.82 75.2 54.52 11.0 2.16 51.84 1 2.62 0.5 16.6 31.17 6.118 1 1.2

HRGS-2 127 3.5 8.42 80.97 60.32 12.6 2.74 65.76 1.6 4.19 0.9 8.6 16.15 3.507 0.9 1.1

HRGS-3 139 3.5 8.09 77.8 56.27 9.0 1.82 43.68 2.1 5.5 1.1 9 16.9 3.423 1.2 1.5

CGP-II HRGS-4 146 3.5 8.67 83.37 59.29 10.0 2.13 51.12 16.9 44.23 9.4 14.6 27.41 5.851 1.0 1.2

HRGS-5 157 3.5 9.09 87.41 60.58 13.5 2.94 70.56 24.6 64.39 14.0 12.9 24.22 5.282 1 1.2

FPU-II

FPU -03FF001 239 2.67 7.59 42.48 24.72 38.6 3.44 82.56 112 293.15 26.1 31.6 59.33 5.28 1.2 1.5

32.5 9.88

HCU 1&2 247 2.1 9.15 31.68 18.16 43.6 2.85 68.4 109 285.3 18.7 34.6 64.96 4.25 1.1 1.4

HCU 3&4 252 2.1 8.88 30.74 17.45 34.6 2.17 52.08 121 316.71 19.9 42.6 79.98 5.02 0.9 1.2

MSQ 15 F01-04 157 2.9 9.24 61 42.27 13.2 2.01 48.24 2.6 6.81 1.0 16.6 31.2 5 1 1.2

14 F01 146 1.57 7.86 15.21 10.82 11.3 0.44 10.56 3.1 8.11 0.3 12.6 23.7 1 0.9 1.1

15 F05 153 1.45 7.29 12.03 8.42 12.6 0.38 9.12 2.6 6.81 0.2 16.9 31.7 1 1.1 1.3

15 F01 142 1.45 8.06 13.3 9.55 10 0.34 8.16 3.7 9.68 0.3 12.1 22.7 1 1.0 1.3

LAB Hot iol 2063F01 4.5 0 0 0 0 0 0 0 0

2061 F-001 0.7 0 0 0 0 0 0.0 0 0

0 0.00

PARTICULATE SULPHUR

DIOXIDE

HGU-III

MATTER OF


HCU

Page 36 of 244





DHDS DHDS 234 1.6 7.81 15.69 9.22 14.6 0.48 11.52 14.6 38.21 1.3 17.6 33.04 1.097 1 1.2

F-01-F-02 153 1.7 8.08 18.33 12.82 15 0.69 16.56 16.4 42.93 2.0 12.2 22.91 1.06 1.2 1.5

DHDT F- 01 157 1.75 8.67 20.84 14.44 18.9 0.98 23.52 8.6 22.51 1.2 10.3 19.34 1.01 1 1.2

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 166 1.7 8.38 19.01 12.9 0 0 62.6 163.85 7.6 14.6 27.41 1.27 1.3

DCU F-01 153 2 8.67 27.22 19.04 16.6 1.14 27.36 6.9 18.06 1.2 7.2 13.52 0.93 1.1 1.2

F- 02 142 2 7.69 24.15 17.34 24.6 1.54 36.96 5.4 14.13 0.9 6.8 12.77 0.80 0.9 1.0

VGO_HDT

F-01/F22 162 1.2 7.92 8.95 6.13 27.6 0.61 14.64 17.6 46.07 1.0 12.3 23.09 0.51 1.1 1.3

HU-I HU-I 245 2.1 8.21 28.42 16.35 13.3 0.78 18.72 14.6 38.21 2.3 24.6 46.19 2.719 1 1.3

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

PARTICULATE SULPHUR

MATTER DIOXIDE OF


ISOM

Remark:- Under shudwon in stack AU-II, Lab, TPS B-4,, VBU- 731F01, HGU-II, SRU (Old), & (New) for Month of September- 2015.

SRU

Page 37 of 244





AU-I

F-1 234 2.4 7.26 32.83 19.3 62.6 4.35 104.4 60.6 158.62 11.0 32.6 61.21 4.25 1 1.2

F-2 242 1 8.87 6.96 4.03 34.9 0.51 12.24 52.6 137.68 2.0 42.0 78.86 1.14 0.8 1

F-3 228 0.8 8.21 4.12 2.45 42.6 0.38 9.12 38.9 101.82 0.9 34.6 64.96 0.57 1.1 1.3F-4 246 0.8 8.61 4.33 2.49 36.4 0.33 7.92 42.6 111.5 1.0 28.9 54.26 0.49 1.1 1.4F-5 258 1.1 7.92 7.52 4.22 33.8 0.51 12.24 46.6 121.97 1.9 34.6 64.96 0.99 1.2 1.5

11.0 4.25

F-1 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-2 ~ 1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-3 ~ 0.8 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-4 ~ 0.8 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-5 ~ 1.1 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

F-2 241 2.1 8.08 27.97 16.22 43.6 2.55 61.2 52.6 137.68 8.0 27.6 51.82 3.03 1.1 1.3

F-3 228 1.7 8.61 19.53 11.62 31.9 1.33 31.92 34.9 91.35 3.8 18.9 35.49 1.48 1.2 1.6

11.6 2.75

CRU 21-F-01 234 0.84 8.11 4.49 2.64 28.6 0.27 6.48 41.6 108.89 1.0 19.9 37.36 0.355 0.9 1.1

CRU 21-F-02 246 1.1 7.91 7.51 4.31 16.9 0.26 6.24 33.6 87.95 1.4 23.4 43.93 0.682 1 1.2

CRU 22-F-01 251 1.28 7.88 10.13 5.76 15.6 0.32 7.68 26.6 69.62 1.4 28.6 53.7 1.114 1.2 1.4

CRU F1 41 2.2 - - - - - - 11.3 29.58 23.4 43.93 1.4 1.7

3.8 1.796

UDEX Udex 157 1.88 ~ ~ ~ - ` ` 7.9 20.68 ~ 11.6 21.78 ~ 0.9 1.2

AU-V

AU-5 237 3.15 8.46 65.9 38.51 41.6 5.77 138.48 67 174.32 24.2 38.6 72.47 10.047 1.1 1.4

FCC

CO-BOILER 133 2.6 13.4 71.11 52.19 121 22.73 545.52 47.6 124.59 23 21.3 39.99 7.51 ~ 4.3


FPU-1 8/2 F01 241 2.3 8.09 33.59 19.47 21.6 1.51 36.24 29.6 77.48 5.4 16.9 31.73 2.22 1.2 1.5

AU-III

CRU

NITROGEN

AU-II

STACK CALCULATION FOR THE PERIOD OF OCTOBER-2015.

SULPHUR OXIDES

MATTER DIOXIDE OF

Page 38 of 244





F-101 153 1.7 7.64 17.33 12.12 18.6 0.81 19.44 22.6 59.15 2.6 10.6 19.9 0.87 1.0 1.4

F-01 164 3.5 8.42 80.97 55.22 21.6 4.29 102.96 16.2 42.4 8.4 7.5 14.08 2.80 1.1 1.5

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 163 3 ~ ~ ~ ~ ~ ~ 34.9 91.35 ~ 34.6 64.96 ~ 1.1 1.3

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 154 3 ~ ~ ~ ~ ~ ~ 23.6 61.77 ~ 24.9 46.75 ~ 1.3 1.5

GRE

AU-IV AU-IV712F01 234 1.9 7.72 21.88 12.86 44.4 2.06 49.4 73 190.03 8.8 41.6 78.11 3.62 1.2 1.5

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 243 2.4 8.24 37.26 21.52 46.9 3.63 87.12 123 321.95 24.9 31.6 59.33 4.6 1 1.3

CDU-E 231 1.9 8.08 22.9 13.54 37.6 1.83 43.92 64.6 169.09 8.2 28.9 54.26 2.6 1.2 1.4

CDU-W 237 1.9 7.88 22.33 13.05 32.6 1.53 36.72 52.6 137.68 6.5 23.9 44.87 2.11 1.0 1.4

BBU F-1 347 1.3 8.79 11.66 5.6 17.6 0.35 8.4 30.3 79.31 1.6 22.2 41.68 0.84 0.8 1.1

BBU F-2 311 1.3 9.05 12.01 6.13 20.6 0.45 10.8 17.9 46.85 1.0 18.9 35.49 0.78 1.0 1.3

48.45 12.97

CGP-I HRGS-1 142 3.5 8.11 77.99 56 14.6 2.94 70.56 1.3 3.4 0.7 8.9 16.71 3.369 0.9 1.1

HRGS-2 131 3.5 7.68 73.85 54.47 16.9 3.31 79.44 1.3 3.4 0.7 10.6 19.9 3.902 1.1 1.5

HRGS-3 127 3.5 7.45 71.64 53.37 12.6 2.42 58.08 2 5.23 1.0 12.6 23.66 4.546 1.2 1.6

CGP-II HRGS-4 141 3.5 8.06 77.51 55.79 17.6 3.53 84.72 11.6 30.36 6.1 15.9 29.85 5.995 0.9 1.3

HRGS-5 153 3.5 8.61 82.8 57.92 21.3 4.44 106.56 15.6 40.83 8.5 12.2 22.91 4.777 1 1.3

FPU-II

FPU -03FF001 239 2.67 7.59 42.48 24.72 38.6 3.44 82.56 112 293.15 26.1 31.6 59.33 5.28 1.2 1.5

32.5 9.88

HCU 1&2 237 2.1 8.61 29.81 17.42 37.6 2.36 56.64 120 314.09 19.7 28.6 53.7 3.37 1.0 1.3

HCU 3&4 227 2.1 7.81 27.04 16.12 42.6 2.47 59.28 105 274.83 16.0 36.9 69.28 4.02 1.2 1.4

MSQ 15 F01-04 142 2.9 8.26 54.53 39.16 15.6 2.2 52.8 3.1 8.11 1.1 12.6 23.7 3 1 1.2

14 F01 137 1.57 7.49 14.49 10.53 10.6 0.4 9.6 2.2 5.76 0.2 14.9 28.0 1 0.8 1

15 F05 141 1.45 7.81 12.89 9.28 14.6 0.49 11.76 2.8 7.33 0.2 15.5 29.1 1 0.9 1.2

15 F01 126 1.45 8 13.2 9.86 9.5 0.34 8.16 3 7.85 0.3 13.9 26.1 1 1.0 1.4

LAB Hot iol 2063F01 4.5 0 0 0 0 0 0 0 0

2061 F-001 0.7 0 0 0 0 0 0.0 0 0

0 0.00

OF


HCU

HGU-III

MATTER

PARTICULATE SULPHUR

DIOXIDE

Page 39 of 244





DHDS DHDS 227 1.6 7.69 15.45 9.21 15.6 0.52 12.48 16.6 43.45 1.4 15.6 29.29 0.971 1.1 1.3

F-01-F-02 162 1.7 8.12 18.42 12.62 18 0.82 19.68 15.6 40.83 1.9 10.6 19.9 0.90 1.1 1.4

DHDT F- 01 160 1.75 7.85 18.87 12.99 22.3 1.04 24.96 9.1 23.82 1.1 13.6 25.53 1.19 0.9 1.1

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 158 1.7 7.69 17.45 12.07 0 0 55.6 145.53 6.3 12.6 23.66 1.03 1.2

DCU F-01 146 2 7.69 24.15 17.18 21.6 1.34 32.16 7.6 19.89 1.2 8.4 15.77 0.98 1 1.3

F- 02 159 2 8.08 25.37 17.5 17.6 1.11 26.64 6.8 17.8 1.1 7.6 14.27 0.90 0.8 1.2

VGO_HDT

F-01/F22 166 1.2 8.05 9.1 6.18 18.9 0.42 10.08 15.6 40.83 0.9 11.1 20.84 0.46 1.0 1.2

HU-I HU-I 233 2.1 7.68 26.59 15.66 16.6 0.94 22.56 12.2 31.93 1.8 18.9 35.49 2.001 1.1 1.4

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Remark:- Under shudwon in stack AU-II, Lab, TPS B-1, B-3, VBU- 731F01, HGU-II, SRU (Old), & (New) for Month of October- 2015.

SRU

ISOM

PARTICULATE SULPHUR

MATTER DIOXIDE OF


Page 40 of 244





AU-I

F-1 253 2.4 7.68 34.73 19.68 82.4 5.84 140.16 61.6 161.23 11.4 31.6 59.33 4.2 1.2 1.3

F-2 238 1 8.69 6.82 3.98 48.6 0.7 16.8 48.6 127.21 1.8 36.6 68.72 0.98 0.8 1.1

F-3 248 0.8 8.84 4.44 2.54 34.6 0.32 7.68 41.6 108.89 1.0 33.3 62.52 0.57 1.0 1.3F-4 251 0.8 8.18 4.11 2.34 41.3 0.35 8.4 38.6 101.03 0.9 30.3 56.89 0.48 1 1.2F-5 240 1.1 7.48 7.1 4.12 38.6 0.57 13.68 49.6 129.83 1.9 38.6 72.47 1.07 1.1 1.6

11.4 4.2

F-1 242 2.4 8.81 39.84 23.05 66.6 5.53 132.72 62.6 163.85 13.6 42.3 79.58 6.6 1 1.2

F-2 223 1 7.91 6.21 3.73 42.3 0.57 13.68 38.6 101.03 1.4 32.6 61.21 0.82 1.1 1.3

F-3 242 0.8 8.26 4.15 2.4 34.6 0.3 7.2 42.6 111.5 1.0 29.6 55.58 0.48 1 1.3

F-4 239 0.8 8.12 4.08 2.37 38.6 0.33 7.92 34.6 90.56 0.8 34.6 64.96 0.55 0.9 1.2

F-5 252 1.1 7.69 7.3 4.14 46.9 0.7 16.8 38.1 99.72 1.5 41.6 78.11 1.16 1.1 1.4

F-2 248 2.1 7.69 26.62 15.23 42.3 2.32 55.68 41.3 108.1 5.9 19.6 36.8 2.02 0.8 1

F-3 236 1.7 8.19 18.58 10.88 29.1 FALSE 0 26.6 69.62 2.7 21.6 40.56 1.59 1.0 1.3

11.6 2.75

CRU 21-F-01 253 0.84 8.26 4.58 2.59 37.6 0.35 8.4 42.6 111.5 1.0 27.6 51.82 0.483 1 1.3

CRU 21-F-02 246 1.1 7.86 7.47 4.29 18.5 0.29 6.96 31.6 82.71 1.3 20.6 38.68 0.597 0.8 1.1

CRU 22-F-01 257 1.28 8.12 10.44 5.87 14.6 0.31 7.44 24.6 64.39 1.4 32.3 60.64 1.281 1.2 1.5

CRU F1 39 2.2 - - - - - - 10.6 27.74 12.3 23.09 1.2 1.6

3.7 1.878

UDEX Udex 158 1.88 ~ ~ ~ - ` ` 9.2 24.08 ~ 12.3 23.09 ~ 0.9 1.2

AU-V

AU-5 256 3.15 8.78 68.39 38.53 53.6 7.43 178.32 69 179.56 24.9 38.6 72.47 10.052 1.1 1.3

FCC

CO-BOILER 138 2.6 12.6 66.86 48.48 126 21.99 527.76 41.3 108.1 19 18.2 34.17 5.96 ~ 4.3


FPU-1 8/2 F01 248 2.3 8.26 34.3 19.62 12.6 0.89 21.36 18.6 48.68 3.4 15.3 28.73 2.03 1.2 1.5

AU-III

CRU

NITROGEN

AU-II

STACK CALCULATION FOR THE PERIOD OF NOVEMBER-2015.

SULPHUR OXIDES

MATTER DIOXIDE OF

Page 41 of 244





F-101 162 1.7 7.39 16.77 11.49 16.6 0.69 16.56 24.6 64.39 2.7 14.6 27.41 1.13 0.9 1.2

F-01 176 3.5 8.46 81.35 53.99 18.6 3.62 86.88 18.6 48.68 9.5 9.4 17.65 3.43 1.1 1.3

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 148 3 ~ ~ ~ ~ ~ ~ 51.6 135.06 ~ 18.6 34.92 ~ 1.0 1.2

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 154 3 ~ ~ ~ ~ ~ ~ 34.9 91.35 ~ 22.1 41.49 ~ 0.9 1.1

GRE

AU-IV AU-IV712F01 234 1.9 8.14 23.07 13.56 41.3 2.02 48.5 58 150.77 7.4 33.3 62.52 3.05 1.0 1.2

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 248 2.4 8.46 38.25 21.88 26.9 2.12 50.88 108 282.68 22.3 42.6 79.98 6.3 1.2 1.4

CDU-E 243 1.9 7.69 21.79 12.58 34.6 1.57 37.68 68.6 179.56 8.1 34.6 64.96 2.9 0.8 1

CDU-W 237 1.9 8.24 23.35 13.64 27.6 1.36 32.64 52.6 137.68 6.8 28.6 53.7 2.64 1.1 1.3

BBU F-1 366 1.3 7.49 9.94 4.64 14.6 0.24 5.76 24.6 64.39 1.1 21.6 40.56 0.68 1 1.4

BBU F-2 381 1.3 8.06 10.69 4.87 17.6 0.31 7.44 19.4 50.78 0.9 18.6 34.92 0.61 0.9 1.1

44.52 14.93

CGP-I HRGS-1 144 3.5 7.42 71.35 50.99 13.6 2.5 60 2.3 6.02 1.1 11.6 21.78 3.998 0.9 1.2

HRGS-2 132 3.5 8.21 78.95 58.09 17.6 3.68 88.32 3.4 8.9 1.9 9.1 17.09 3.574 0.8 1.1

HRGS-3 138 3.5 7.91 76.06 55.15 13.3 2.64 63.36 2 5.23 1.0 7.6 14.27 2.833 1 1.3

CGP-II HRGS-4 152 3.5 8.34 80.2 56.23 10.0 2.02 48.48 12.3 32.19 6.5 11.6 21.78 4.409 1.1 1.4

HRGS-5 162 3.5 7.69 73.95 50.66 15.6 2.85 68.4 17.6 46.07 8.4 13 24.41 4.452 0.9 1.1

FPU-II

FPU -03FF001 246 2.67 8.16 45.66 26.22 42.6 4.02 96.48 104 272.21 25.7 27.9 52.38 4.944 1.1 1.3

32.5 9.88

HCU 1&2 237 2.1 8.35 28.91 16.89 51.6 3.14 75.36 89.9 235.31 14.3 31.6 59.33 3.61 1.2 1.4

HCU 3&4 241 2.1 8.09 28.01 16.24 31.6 1.85 44.4 121 316.71 18.5 40 75.1 4.39 1.0 1.3

MSQ 15 F01-04 162 2.9 8.69 57.37 39.3 15.5 2.19 52.56 3.4 8.9 1.3 14.3 26.9 4 0.9 1.2

14 F01 143 1.57 8.36 16.18 11.59 14.6 0.61 14.64 4.1 10.73 0.5 10 18.8 1 1.0 1.3

15 F05 157 1.45 7.49 12.36 8.57 17.6 0.54 12.96 2.2 5.76 0.2 13.6 25.5 1 0.8 1

15 F01 150 1.45 8.21 13.55 9.55 16.4 0.56 13.44 3.1 8.11 0.3 10.3 19.3 1 1.1 1.3

LAB Hot iol 2063F01 237 4.5 8.11 128.92 75.33 42.3 11.47 275.28 115.0 301.01 82 28.6 53.7 14.563 1.2 1.4

2061 F-001 211 0.7 7.86 3.02 1.86 28.6 0.19 4.56 41.3 108.1 0.7 14.6 27.41 0.184 1 1.2

82 14.75

OF


HCU

HGU-III

MATTER

PARTICULATE SULPHUR

DIOXIDE

Page 42 of 244





DHDS DHDS 227 1.6 7.45 14.97 8.92 16.6 0.53 12.72 18.6 48.68 1.6 14.6 27.41 0.88 1.1 1.3

F-01-F-02 162 1.7 8.12 18.42 12.62 17 0.77 18.48 14.2 37.17 1.7 10 18.78 0.85 1.0 1.3

DHDT F- 01 148 1.75 7.75 18.63 13.19 21.3 1.01 24.24 8.1 21.2 1.0 12.3 23.09 1.10 1.1 1.3

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 157 1.7 7.69 17.45 12.09 0 0 44.6 116.74 5.1 18.6 34.92 1.52 1.2

DCU F-01 143 2 7.69 24.15 17.3 18.6 1.16 27.84 8.6 22.51 1.4 6.6 12.39 0.77 0.9 1.0

F- 02 157 2 8.14 25.56 17.71 22.2 1.42 34.08 6.8 17.8 1.1 8.1 15.21 0.97 1 1.3

VGO_HDT

F-01/F22 166 1.2 7.66 8.66 5.88 23.3 0.49 11.76 14.6 38.21 0.8 11.1 20.84 0.44 1.0 1.2

HU-I HU-I 231 2.1 8.06 27.9 16.5 14.6 0.87 20.88 11.3 29.58 1.8 18.6 34.92 2.074 0.9 1.1

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Remark:- Under shudwon in stack TPS B-1,B-3, VBU- 731F01, HGU-II, SRU (Old), & (New) for Month of November- 2015.

SRU

ISOM

PARTICULATE SULPHUR

MATTER DIOXIDE OF


Page 43 of 244





AU-I

F-1 242 2.4 7.49 33.87 19.6 51.6 3.64 87.36 56.4 147.62 10.4 26.9 50.51 3.56 1.1 1.5

F-2 231 1 8.09 6.35 3.75 29.6 0.4 9.6 44.6 116.74 1.6 40.6 76.23 1.03 0.9 1.1

F-3 219 0.8 7.86 3.95 2.39 34.6 0.3 7.2 41.6 108.89 0.9 33.3 62.52 0.54 1.1 1.4F-4 234 0.8 8.77 4.41 2.59 42.6 0.4 9.6 33.6 87.95 0.8 37.6 70.6 0.66 1 1.3F-5 240 1.1 8.12 7.71 4.48 37.6 0.61 14.64 36.5 95.54 1.5 24.6 46.19 0.74 1.2 1.4

10.4 3.56

F-1 231 2.4 8.08 36.53 21.6 61.6 4.79 114.96 51.9 135.85 10.6 40.9 76.95 5.98 1.1 1.4

F-2 229 1 7.69 6.04 3.59 33.6 0.43 10.32 34.6 90.56 1.2 24.9 46.75 0.6 1 1.2

F-3 218 0.8 7.84 3.94 2.39 43.9 0.38 9.12 48.9 127.99 1.1 34.6 64.96 0.56 0.9 1.2

F-4 242 0.8 7.16 3.6 2.08 34.9 0.26 6.24 31.6 82.71 0.6 26.9 50.51 0.38 1 1.3

F-5 234 1.1 7.83 7.44 4.37 41.9 0.66 15.84 29.8 78 1.2 36.4 68.34 1.08 1.2 1.5

F-2 236 2.1 8.14 28.18 16.5 38.6 2.29 54.96 48.9 127.99 7.6 26.9 50.51 3 0.9 1.2

F-3 242 1.7 7.66 17.38 10.06 28.6 1.04 24.96 33.6 87.95 3.2 21.9 41.12 1.49 1.1 1.4

11.6 2.75

CRU 21-F-01 243 0.84 8.26 4.58 2.65 18.9 0.18 4.32 34.9 91.35 0.9 19.9 37.36 0.356 0.9 1.1

CRU 21-F-02 247 1.1 7.65 7.27 4.17 22.6 0.34 8.16 28.4 74.34 1.1 23.4 43.93 0.659 1 1.2

CRU 22-F-01 253 1.28 7.39 9.5 5.38 18.9 0.37 8.88 22.9 59.94 1.2 28.6 53.7 1.04 1.2 1.4

CRU F1 36 2.2 - - - - - - 3.2 8.38 16.9 31.73 1.3 1.6

3.2 1.699

UDEX Udex 148 1.88 ~ ~ ~ - ` ` 6.8 17.8 ~ 10.6 19.9 ~ 1.0 1.3

AU-V

AU-5 243 3.15 8.13 63.33 36.57 36.4 4.79 114.96 59 153.38 20.2 33.4 62.71 8.256 1 1.3

FCC

CO-BOILER 124 2.6 12.7 67.39 50.58 114 20.76 498.24 44.6 116.74 21 32.6 61.21 11.15 ~ 4

FCCU Charge Heater 227 1.9 7.69 21.79 12.99 14.6 0.68 16.32 20.6 53.92 2.5 14.6 27.41 1.28 1 1.3

FPU-1 8/2 F01 240 2.3 8.02 33.3 19.34 18.6 1.3 31.2 23.9 62.56 4.4 16.9 31.73 2.21 1.1 1.4

AU-III

CRU

NITROGEN

AU-II

STACK CALCULATION FOR THE PERIOD OF DECEMBER-2015.

SULPHUR OXIDES

MATTER DIOXIDE OF

Page 44 of 244





F-101 166 1.7 8.07 18.31 12.43 14.9 0.67 16.08 16.5 43.19 1.9 8.4 15.77 0.71 1.1 1.3

F-01 151 3.5 7.59 72.99 51.3 18.6 3.44 82.56 13.8 36.12 6.7 7 13.14 2.43 1.0 1.3

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 144 3 ~ ~ ~ ~ ~ ~ 54.6 142.91 ~ 21.6 40.56 ~ 1.0 1.2

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 160 3 ~ ~ ~ ~ ~ ~ 33.3 87.16 ~ 18.6 34.92 ~ 1.1 1.4

GRE

AU-IV AU-IV712F01 222 1.9 7.56 21.42 12.9 38.6 1.79 43.0 68 176.94 8.2 23.9 44.87 2.08 1.0 1.3

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 233 2.4 7.89 35.68 21.01 40.6 3.07 73.68 108 282.68 21.4 24.6 46.19 3.49 1.2 1.5

CDU-E 223 1.9 7.69 21.79 13.09 33.9 1.6 38.4 72.9 190.81 9.0 22.9 43 2.0 1 1.3

CDU-W 244 1.9 8.11 22.98 13.25 26.9 1.28 30.72 62.9 164.64 7.9 30.9 58.02 2.77 1.3 1.5

BBU F-1 366 1.3 8.26 10.96 5.11 16.5 0.3 7.2 26.9 70.41 1.3 29.6 55.58 1.02 1 1.2

BBU F-2 341 1.3 8.95 11.87 5.76 18.8 0.39 9.36 16.9 44.23 0.9 19.7 36.99 0.77 0.8 1.2

46.44 10.37

CGP-I HRGS-1 ~ 3.5 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

HRGS-2 156 3.5 8.11 77.99 54.17 14.6 2.85 68.4 1.3 3.4 0.7 8.9 16.71 3.259 0.9 1.1

HRGS-3 145 3.5 7.66 73.66 52.51 17.6 3.33 79.92 3.6 9.42 1.8 8 15.02 2.839 1 1.3

CGP-II HRGS-4 159 3.5 8.15 78.37 54.06 16.9 3.29 78.96 10.9 28.53 5.6 13.6 25.53 4.969 1.0 1.4

HRGS-5 164 3.5 8.24 79.24 54.04 22.2 4.32 103.68 18.6 48.68 9.5 10.9 20.47 3.982 1.1 1.5

FPU-II

FPU -03FF001 242 2.67 7.34 41.08 23.77 33.9 2.9 69.6 107 280.07 24.0 16.9 31.73 2.715 1.1 1.4

32.5 9.88

HCU 1&2 233 2.1 7.69 26.62 15.68 33.9 1.91 45.84 126 329.8 18.6 22.2 41.68 2.35 1.1 1.4

HCU 3&4 217 2.1 8.06 27.9 16.97 29.4 1.8 43.2 114 298.39 18.2 19.9 37.36 2.28 1.3 1.6

MSQ 15 F01-04 139 2.9 7.69 50.77 36.72 18.9 2.5 60 2.9 7.59 1.0 9.9 18.6 2 0.8 1

14 F01 144 1.57 8.12 15.71 11.23 14.6 0.59 14.16 3.4 8.9 0.4 10.9 20.5 1 0.9 1.2

15 F05 153 1.45 7.66 12.64 8.84 19.9 0.63 15.12 4.2 10.99 0.4 8.6 16.2 1 1.0 1.3

15 F01 137 1.45 7.49 12.36 8.98 14.9 0.48 11.52 3.9 10.21 0.3 10.7 20.1 1 0.9 1.1

LAB Hot iol 2063F01 246 4.5 7.69 122.24 70.19 37.6 9.5 228 109.0 285.3 72 24.6 46.19 11.671 1 1.3

2061 F-001 229 0.7 7.49 2.88 1.71 22.9 0.14 3.36 37.6 98.42 0.6 12.9 24.22 0.149 1.2 1.5

73 11.82

OF


HCU

HGU-III

MATTER

PARTICULATE SULPHUR

DIOXIDE

Page 45 of 244





DHDS DHDS 233 1.6 7.44 14.95 8.8 14.5 0.46 11.04 18.6 48.68 1.5 11.6 21.78 0.69 1 1.3

F-01-F-02 159 1.7 7.89 17.9 12.35 16.7 0.74 17.76 21.6 56.54 2.5 13.9 26.1 1.16 1.2 1.5

DHDT F- 01 167 1.75 8.06 19.38 13.13 18.6 0.88 21.12 12.6 32.98 1.6 9.5 17.84 0.84 0.8 1.1

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 165 1.7 7.85 17.81 12.12 0 0 51.6 135.06 5.9 9.8 18.4 0.80 1.3

DCU F-01 133 2 7.49 23.52 17.26 17.6 1.09 26.16 12.9 33.77 2.1 7.9 14.83 0.92 1.1 1.4

F- 02 146 2 7.88 24.74 17.6 22.6 1.43 34.32 9.8 25.65 1.6 9.5 17.84 1.13 1.9 1.2

VGO_HDT

F-01/F22 171 1.2 7.79 8.81 5.91 26.4 0.56 13.44 17.6 46.07 1.0 7.6 14.27 0.30 1.1 1.4

HU-I HU-I 217 2.1 7.66 26.52 16.13 21.6 1.25 30 16.9 44.23 2.6 7.6 14.27 0.829 1 1.3

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Remark:- Under shudwon in stack TPS B-1, B-3, VBU- 731F01, HGU-II, SRU (Old), & (New) for Month of December- 2015.

SRU

ISOM

PARTICULATE SULPHUR

MATTER DIOXIDE OF


Page 46 of 244


UNIT STACK TEMP.C

DIA OF

GAS VEL.

FLUE GAS

FLUE GAS

PARTICULATE

SULPHUR OXIDES

HYDRO CARBON

T STAC

K

VOLUME

VOLUME MATTER DIOXIDE OF

CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N

m3 kg/hr kg/day ppm

mg/Nm3

kg/hr ppm mg/Nm3 kg/hr ppm ppm

AU-I

F-1 226 2.4 7.26 32.83 19.61 57.6 4.07 97.6

8 52.5 137.4

2 9.7 34.6 64.96 4.59 1 1.3

F-2 241 1 8.21 6.44 3.73 34.6 0.46 11.0

4 38.6 101.0

3 1.4 29.6 55.58 0.75 1.1 1.4

F-3 234 0.8 8.04 4.04 2.37 41.1

0.3

5 8.4

46.

1

120.6

6 1.0

34.

8 65.34 0.56 0.9 1.2

F-4 247 0.8 8.39 4.22 2.42 32.6

0.2

8 6.72

30.

8 80.62 0.7

28.

6 53.7 0.47 1 1.2

F-5 231 1.1 7.84 7.45 4.4 36.4

0.5

8

13.9

2

39.

7

103.9

1 1.7

22.

9 43 0.68 1.1 1.4

9.7

4.59

AU-II

F-1 237 2.4 7.48 33.82 19.76 56.6 4.03 96.7

2 56.4 147.6

2 10.5 36.9 69.42 4.94 1 1.3

F-2 241 1 7.89 6.19 3.59 44.6 0.58 13.9

2 42.9 112.2

9 1.5 26.9 50.51 0.65 1.9 1.2

F-3 222 0.8 8.46 4.25 2.56 38.6 0.36 8.64 37.6 98.42 0.9 24.9 46.75 0.43 1 1.2

F-4 216 0.8 8.27 4.15 2.53 40.6 0.37 8.88 42.4 110.9

8 1.0 34.7 65.15 0.59 1.2 1.5

F-5 235 1.1 7.93 7.53 4.42 34.8 0.55 13.2 31.9 83.5 1.3 33.3 62.52 0.99 1 1.3

AU-III

F-2 242 2.1 7.91 27.38 15.84 34.6 1.97 47.2 41.6 108.8 6.2 26.9 50.51 2.88 1.0 1.3

Page 47 of 244

8 9

F-3 227 1.7 8.15 18.49 11.02 26.9 1.07 25.6

8 30.6 80.09 3.2 23.9 44.87 1.78 0.9 1.2

11.6

2.75

CRU

CRU 21-F-01 238 0.84 8.1 4.49 2.62 21.3 0.2 4.8 30.6 80.09 0.8 17.6 33.04

0.312 1 1.2

CRU 21-F-02 242 1.1 7.85 7.46 4.32 17.6 0.27 6.48 24.6 64.39 1.0 20.9 39.24 0.61 1.1 1.3

CRU 22-F-01 237 1.28 7.64 9.83 5.74 19.4 0.4 9.6 26.9 70.41 1.5 22.7 42.62

0.881 1.2 1.5

CRU F1 38 2.2 - - - - - - 3.7 9.68

12.6 23.66

1.4 1.8

3.2

1.491

UDEX Udex 158 1.88 ~ ~ ~ - ` ` 7.1 18.58 ~ 9.6 18.02 ~ 0.9 1.2

AU-V

AU-5 237 3.15 8.09 63.01 36.82 28.9 3.83 91.9

2 49 127.2

1 16.9 28.6 53.7 7.118 1.2 1.4

FCC

CO-BOILER 137 2.6 13.8 73.23 53.23 124 23.7

6 570.24 41.6

108.89 21 29.6 55.58

10.65 ~ 4.6

FCCU Charge Heater 234 1.9 7.48 21.2 12.46 12.6 0.57

13.68 18.6 48.68 2.2 11.6 21.78 0.98 1.1 1.4

FPU-1 8/2 F01 243 2.3 8.17 33.93 19.6 16.8 1.19

28.56 20.4 53.4 3.8 14.4 27.04 1.91 1 1.3


UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS

FLUE GAS PARTICULATE SULPHUR

OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

Page 48 of 244

M3/SEC M3/SEC mg/N

m3 kg/hr kg/day ppm mg/Nm3


HGU-III

F-101 158 1.7 7.84 17.79 12.3 12.6 0.56 13.4

4 12.6 32.98 1.5 7.6 14.27 0.63 1.0 1.2

F-01 167 3.5 7.44 71.54 48.45 16.8 2.93 70.3

2 10.9 28.53 5.0 6.8 12.77 2.23 1.1 1.4

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 154 3 ~ ~ ~ ~ ~ ~ 44.6 116.7

4 ~ 17.6 33.04 ~ 0.9 1.2

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 163 3 ~ ~ ~ ~ ~ ~ 31.6 82.71 ~ 14.9 27.98 ~ 1.0 1.4

GRE

AU-IV

AU-IV712F01 234 1.9 7.89 22.36 13.14 42.9

2.03 48.7 58

150.5 7.1

31.6 59.33 2.81 0.9 1.2

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 241 2.4 7.68 34.73 20.14 34.9 2.53

60.72 116

303.62 22.0

22.8 42.81 3.1 0.8 1.1

CDU-E 218 1.9 8.15 23.1 14.02 29.6 1.49

35.76

82.6

216.2 10.9

18.6 34.92 1.8 1 1.2

CDU-W 229 1.9 7.65 21.68 12.87 23.8 1.1 26.4 56.8

148.67 6.9

28.6 53.7 2.49 1.2 1.5

BBU F-1 381 1.3 8.09 10.73 4.89 18.7 0.33 7.92

22.4

58.63 1.0

24.6 46.19 0.81 1 1.3

BBU F-2 367 1.3 8.29 11 5.12 22.6 0.42

10.08

27.9

73.03 1.4

18.6 34.92 0.64 0.9 1.1

46.93

10.16

CGP-I HRGS-1 164 3.5 8.26 79.43 54.17 16.7 3.26

78.24 2.1 5.5 1.1 7.6 14.27

2.783 1 1.1

HRGS-2 151 3.5 7.89 75.87 53.32 15.9 3.05 73.2 1.8 4.71 0.9 8 15.02 2.88

3 1.1 1.3

HRGS-3 157 3.5 8.41 80.87 56.04 18.4 3.71 89.0

4 2.6 6.81 1.4 7.4 13.89 2.80

2 0.9 1.2 CGP-II HRGS-4 168 3.5 8.09 77.8 52.57 15.9 3.01

72.24 6.9 18.06 3.4 10.9 20.47

3.874 1.1 1.4

Page 49 of 244

HRGS-5 153 3.5 7.93 76.26 53.35 19.7 3.78 90.7

2 8.9 23.3 4.5 12.9 24.22 4.65

2 1 1.3 FPU-II

FPU -03FF001 237 2.67 7.84 43.87 25.63 28.6 2.64

63.36 115

301.01 27.8 21.6 40.56

3.742 1 1.3

HCU

32.5

9.88

HCU 1&2 241 2.1 7.88 27.28 15.82 38.6 2.2 52.8 116 303.6

2 17.3 20.2 37.93 2.16 1.0 1.3

HCU 3&4 234 2.1 8.14 28.18 16.56 32.9 1.96 47.0

4 106 277.4

5 16.5 17.6 33.04 1.97 1.1 1.4

MSQ 15 F01-04 136 2.9 7.84 51.76 37.71 17.4 2.36 56.6

4 3.4 8.9 1.2 8.5 16.0 2 0.9 1.1

14 F01 148 1.57 8.02 15.52 10.99 16.9 0.67 16.0

8 2.7 7.07 0.3 10 18.8 1 1.1 1.5

15 F05 157 1.45 8.17 13.48 9.34 18.4 0.62 14.8

8 3.3 8.64 0.3 7.6 14.3 0 1.0 1.2

15 F01 147 1.45 7.59 12.53 8.89 15.5 0.5 12 3.6 9.42 0.3 9.6 18.0 1 1.1 1.3

LAB Hot iol 2063F01 234 4.5 7.49 119.06 69.98 26.9 6.78

162.72

101.0

264.36 67 22.2 41.68 10.5 0.9 1.3

2061 F-001 221 0.7 7.69 2.96 1.79 22.9 0.15 3.6 33.9 88.73 0.6 13.9 26.1 0.16

8 1.2 1.4

67 10.6

7


UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS


OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N



DHDS DHDS 244 1.6 7.82 15.72 9.06 15.6 0.51 12.2

4 21.6 56.54 1.8 10.9 20.47 0.66

8 0.9 1.2

Page 50 of 244

ISOM

F-01-F-02 164 1.7 8.11 18.4 12.55 15.3 0.69 16.5

6 16.9 44.23 2.0 8.8 16.52 0.75 1.0 1.3

DHDT F- 01 156 1.75 7.95 19.11 13.27 16.6 0.79 18.9

6 10.6 27.74 1.3 8.4 15.77 0.75 0.9 1.1

SRU

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 158 1.7 7.69 17.45 12.07

0 0 48.6 127.2

1 5.5 8.8 16.52 0.72

1.4

DCU F-01 142 2 7.29 22.89 16.44 15.6 0.92 22.0

8 11.1 29.05 1.7 8.4 15.77 0.93 1 1.3

F- 02 156 2 7.77 24.4 16.95 17.9 1.09 26.1

6 9.2 24.08 1.5 9.2 17.27 1.05 1.2 1.4

VGO_HDT

F-01/F22 167 1.2 7.86 8.88 6.01 23.6 0.51 12.2

4 16.4 42.93 0.9 7.4 13.89 0.30 1.0 1.2

HU-I HU-I 226 2.1 7.81 27.04 16.15 18.6 1.08 25.9

2 15.9 41.62 2.4 8.8 16.52 0.96 0.8 1.2

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Page 51 of 244

Remark:- Under shudwon in stack TPS B-1, B-3, VBU- 731F01, HGU-II, SRU (Old), & (New) for Month of February- 2016.

STACK CALCULATION FOR THE PERIOD OF MARCH-2016.

UNIT STACK TEMP.C

DIA OF

GAS VEL.

FLUE GAS

FLUE GAS

PARTICULATE

SULPHUR OXIDES

HYDRO CARBON

T STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N

m3 kg/hr kg/day ppm

mg/Nm3


AU-I

F-1 252 2.4 7.29 32.96 18.71 33.8 2.28 54.7

2 47.8 125.1

1 8.4 26.7 50.13 3.38 0.9 1.2

F-2 234 1 8.04 6.31 3.71 38.6 0.52 12.4

8 29.8 78 1.0 18.6 34.92 0.47 1 1.3

F-3 227 0.8 8.38 4.21 2.51 22.8

0.2

1 5.04

40.

5

106.0

1 1.0

33.

4 62.71 0.57 1.1 1.5

F-4 238 0.8 7.49 3.76 2.19 42.5

0.3

4 8.16

33.

4 87.42 0.7

24.

8 46.56 0.37 0.8 1.1

F-5 244 1.1 7.88 7.48 4.31 27.9

0.4

3

10.3

2

27.

8 72.77 1.1

28.

9 54.26 0.84 1.0 1.3

8.4

3.38

AU-II

F-1 234 2.4 8.08 36.53 21.47 42.6 3.29 78.9

6 37.6 98.42 7.6 28.6 53.81 4.16 1 1.3

F-2 247 1 7.86 6.17 3.54 33.7 0.43 10.3

2 22.8 59.68 0.8 18.9 35.49 0.45 1.2 1.5

F-3 241 0.8 8.15 4.09 2.37 27.6 0.24 5.76 26.9 70.41 0.6 24.9 46.75 0.4 0.9 1.2

Page 52 of 244

F-4 229 0.8 7.62 3.83 2.27 34.5 0.28 6.72 34.8 91.09 0.7 34.6 64.96 0.53 1 1.3

F-5 236 1.1 7.85 7.46 4.37 25.9 0.41 9.84 29.4 76.95 1.2 27.8 52.2 0.82 1.1 1.5

AU-III

F-2 233 2.1 7.64 26.45 15.58 27.8 1.56 37.4

4 32.8 85.85 4.8 28.6 53.7 3.01 0.9 1.2

F-3 247 1.7 8.01 18.17 10.41 36.8 1.38 33.1

2 26.4 69.1 2.6 20.8 39.05 1.46 1.1 1.4

11.6

2.75

CRU

CRU 21-F-01 248 0.84 8.79 4.87 2.79 19.6 0.2 4.8 27.6 72.24 0.7 22.6 42.43

0.426 0.9 1.2

CRU 21-F-02 241 1.1 7.94 7.54 4.37 16.8 0.26 6.24 19.6 51.3 0.8 19.6 36.8

0.579 1.1 1.5

CRU 22-F-01 232 1.28 8.11 10.43 6.15 21.6 0.48

11.52 22.6 59.15 1.3 24.6 46.19

1.023 0.8 1.1

CRU F1 42 2.2 - - - - - - 3 7.85

9 16.9

1.3 1.8

2.9

1.602

UDEX Udex 162 1.88 ~ ~ ~ - ` ` 8.6 22.51 ~ 6.9 12.96 ~ 1.0 1.2

AU-V

AU-5 247 3.15 8.26 64.34 36.87 38.6 5.12 122.88 33 87.16 11.6 22.8 42.81

5.682 1.2 1.6

FCC

CO-BOILER 143 2.6 13.7 72.7 52.08 116 21.7

5 522 33.6 87.95 16 34.6 64.96 12.18 ~ 4.4


20.88 14.6 38.21 2.0 14.6 27.41 1.4 1 1.3

FPU-1 8/2 F01 237 2.3 8.14 33.8 19.75 22.9 1.63

39.12 21.9 57.32 4.1 11.8 22.16 1.58 1.2 1.4

Page 53 of 244

STACK CALCULATION FOR THE PERIOD OF MARCH-2016

UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS


OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N



HGU-III

F-101 164 1.7 8.61 19.53 13.32 13.6 0.65 15.6 10.9 28.53 1.4 8.2 15.4 0.74 1.0 1.3

F-01 153 3.5 7.95 76.45 53.48 19.6 3.77 90.4

8 16.8 43.97 8.5 12.7 23.84 4.59 1.2 1.5

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 166 3 ~ ~ ~ ~ ~ ~ 33.8 88.47 ~ 13.6 25.53 ~ 1.0 1.2

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 161 3 ~ ~ ~ ~ ~ ~ 43.8 114.6

4 ~ 18.6 34.92 ~ 1.2 1.5

GRE

AU-IV

AU-IV712F01 247 1.9 7.69 21.79 12.49 53.4 2.4 57.6 43

111.5 5.0

26.6 49.94 2.25 1.0 1.2

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 229 2.4 7.77 35.13 20.85 42.6 3.2 76.8 106 277.45 20.8

21.6 40.56 3.04 1.2 1.5

CDU-E 249 1.9 8.16 23.12 13.2 23.8 1.13

27.12

59.6 156 7.4

18.6 34.92 1.7 0.9 1.2

CDU-W 232 1.9 7.89 22.36 13.19 37.6 1.79

42.96

79.6

208.35 9.9

17.7 33.23 1.58 1.2 1.5

BBU F-1 346 1.3 8.39 11.13 5.36 15.5 0.3 7.2 24.6

64.39 1.2

24.9 46.75 0.9 1 1.3

BBU F-2 386 1.3 8.04 10.67 4.82 19.6 0.34 8.16

15.9

41.62 0.7

19.9 37.36 0.65 0.8 1.2

43.14

8.53

Page 54 of 244

CGP-I HRGS-1 166 3.5 8.26 79.43 53.92 12.6 2.45 58.8 3.4 8.9 1.7 7.6 14.27 2.77 0.9 1.2

HRGS-2 158 3.5 7.69 73.95 51.13 16.8 3.09 74.1

6 2.1 5.5 1.0 6.6 12.39 2.28

1 1.1 1.4

HRGS-3 169 3.5 7.46 71.74 48.37 10.9 1.9 45.6 1.8 4.71 0.8 9.4 17.65 3.07

3 1 1.3 CGP-II HRGS-4 162 3.5 8.15 78.37 53.69 19.6 3.79

90.96 6.4 16.75 3.2 14.6 27.41

5.298 1.2 1.5

HRGS-5 176 3.5 7.86 75.58 50.16 22.9 4.14 99.3

6 8.6 22.51 4.1 9.4 17.65 3.18

7 1 1.3 FPU-II

FPU -03FF001 238 2.67 7.39 41.36 24.12 32.6 2.83

67.92 84.6

221.44 19.2 11.6 21.78

1.891 1.2 1.5

HCU

32.5

9.88

HCU 1&2 231 2.1 8.34 28.87 17.07 18.6 1.14 27.3

6 98.6 258.0

8 15.9 21.6 40.56 2.49 1.1 1.3

HCU 3&4 246 2.1 7.61 26.34 15.12 34.6 1.88 45.1

2 116 303.6

2 16.5 13.7 25.72 1.40 0.9 1.2

MSQ 15 F01-04 178 2.9 7.29 48.13 31.8 12.6 1.44 34.5

6 3.8 9.95 1.1 9.6 18.0 2 0.8 1

14 F01 159 1.57 8.09 15.65 10.8 9.9 0.38 9.12 4.6 12.04 0.5 7.21 13.5 1 1.0 1.2

15 F05 163 1.45 7.65 12.63 8.63 14.9 0.46 11.0

4 2.9 7.59 0.2 12.6 23.7 1 1.0 1.3

15 F01 154 1.45 8.06 13.3 9.28 12.9 0.43 10.3

2 4.9 12.83 0.4 8.8 16.5 1 1.2 1.5

LAB Hot iol 2063F01 248 4.5 7.26 115.41 66.01 34.9 8.29

198.96 84.6

221.44 53 16.8 31.54

7.495 1 1.2

2061 F-001 231 0.7 8.01 3.08 1.82 16.6 0.11 2.64 31.1 81.4 0.5 11.6 21.78 0.14

3 1.2 1.5

53 7.64

STACK CALCULATION FOR THE PERIOD OF MARCH-2016

UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS


OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE

Page 55 of 244


NITROGEN

M3/SEC M3/SEC mg/N



DHDS DHDS 231 1.6 8.21 16.5 9.76 24.6 0.86 20.6

4 18.6 48.68 1.7 10.2 19.15 0.67

3 1 1.2

ISOM

F-01-F-02 175 1.7 7.86 17.83 11.86 17.6 0.75 18 12.6 32.98 1.4 8.6 16.15 0.69 1.1 1.4

DHDT F- 01 161 1.75 8.12 19.52 13.4 16.9 0.82 19.6

8 12.1 31.67 1.5 8.1 15.21 0.73 0.8 1.0

SRU

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 156 1.7 7.66 17.38 12.07

0 0 36.4 95.28 4.1 16.9 31.73 1.38

1.1

DCU F-01 159 2 8.05 25.28 17.44 18.6 1.17 28.0

8 8.6 22.51 1.4 12.6 23.66 1.49 1.1 1.3

F- 02 169 2 7.98 25.06 16.9 11.1 0.68 16.3

2 12.6 32.98 2.0 7.9 14.83 0.90 1.2 1.5

VGO_HDT

F-01/F22 178 1.2 8.1 9.16 6.05 22.6 0.49 11.7

6 10.6 27.74 0.6 13.9 26.1 0.57 1.1 1.4

HU-I HU-I - 2.1 - - - - - - - - - - - - - -

Page 56 of 244

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Remark:- Under shudwon in stack TPS B-1, B-3, VBU- 731F01, HU-I, HGU-II, SRU (Old), & (New) for Month of March- 2016.

STACK CALCULATION FOR THE PERIOD OF APRIL-2016.

UNIT STACK TEMP.C

DIA OF

GAS VEL.

FLUE GAS

FLUE GAS

PARTICULATE

SULPHUR OXIDES

HYDRO CARBON

T STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N

m3 kg/hr kg/day ppm

mg/Nm3


AU-I

F-1 243 2.4 7.65 34.59 19.98 66.5 4.78 114.72 46.8 122.5 8.8 26.6 49.94 3.59 0.9 1.2

F-2 253 1 7.92 6.22 3.52 42.6 0.54 12.9

6 32.6 85.33 1.1 16.9 31.73 0.4 1 1.3

F-3 229 0.8 8.26 4.15 2.46 32.6

0.2

9 6.96

29.

6 77.48 0.7

34.

9 65.53 0.58 1.1 1.5

F-4 238 0.8 8.49 4.27 2.49 42.9

0.3

8 9.12

40.

6

106.2

7 1.0

22.

9 43 0.39 0.8 1.2

F-5 247 1.1 7.99 7.59 4.35 33.3

0.5

2

12.4

8

27.

6 72.24 1.1

27.

6 51.82 0.81 1.0 1.3

8.8

3.59

AU-II

Page 57 of 244

F-1 228 2.4 7.22 32.65 19.42 46.6 3.26 78.2

4 41.6 108.8

9 7.6 36.2 68.11 4.76 1.1 1.4

F-2 232 1 8.09 6.35 3.75 33.6 0.45 10.8 34.6 90.56 1.2 20.6 38.68 0.52 1 1.3

F-3 248 0.8 8.48 4.26 2.44 24.6 0.22 5.28 29.6 77.48 0.7 34.1 64.02 0.56 0.9 1.1

F-4 242 0.8 7.86 3.95 2.29 42.9 0.35 8.4 33.6 87.95 0.7 22.9 43 0.35 1 1.2

F-5 254 1.1 8.01 7.61 4.3 25.6 0.4 9.6 27.6 72.24 1.1 29.6 55.58 0.86 1 1.3

AU-III

F-2 247 2.1 7.82 27.07 15.51 24.4 1.36 32.6

4 33.8 88.47 4.9 20.5 38.49 2.15 1.1 1.4

F-3 237 1.7 8.23 18.67 10.91 18.6 0.73 17.5

2 26.4 69.1 2.7 27.6 51.82 2.04 0.8 1

11.6

2.75

CRU

CRU 21-F-01 320 0.84 7.89 4.37 2.2 18.6 0.15 3.6 26.6 69.62 0.6 14.4 27.04

0.214 1.1 1.3

CRU 21-F-02 295 1.1 8.14 7.73 4.06 16.4 0.24 5.76 16.9 44.23 0.7 22.6 42.43 0.62 1 1.2

CRU 22-F-01 248 1.28 7.38 9.49 5.43 21.3 0.42

10.08 22.6 59.15 1.2 17.6 33.04

0.646 0.9 1.2

CRU F1 40 2.2 - - - - - - 3.5 9.16

14.6 27.41

1.2 1.6

2.4

1.266

UDEX Udex 166 1.88 ~ ~ ~ - ` ` 12.6 32.98 ~ 11.3 21.22 ~ 1.0 1.2

AU-V

AU-5 248 3.15 7.95 61.92 35.42 33.6 4.28 102.72 43 111.5 14.2 26.9 50.51

6.441 1.1 1.3

FCC

CO-BOILER 144 2.6 14.6 77.48 55.37 135 26.9

1 645.84 44.6

116.74 23 23.6 44.31 8.83 ~ 4.9


20.64 15.6 40.83 2.1 10.6 19.9 1.03 1 1.2

FPU-1 8/2 F01 239 2.3 8.26 34.3 19.96 21.6 1.55 37.2 17.6 46.07 3.3 12.6 23.66 1.7 1.1 1.3

Page 58 of 244


UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS


OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N



HGU-III

F-101 161 1.7 8.26 18.74 12.87 18.6 0.86 20.6

4 18.6 48.68 2.3 9.5 17.84 0.83 1.2 1.4

F-01 152 3.5 7.69 73.95 51.85 14.6 2.73 65.5

2 12.6 32.98 6.2 13.6 25.53 4.77 1.0 1.2

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 166 3 ~ ~ ~ ~ ~ ~ 55.5 145.2

7 ~ 13.6 25.53 ~ 1.0 1.3

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 173 3 ~ ~ ~ ~ ~ ~ 22.6 59.15 ~ 19.6 36.8 ~ 0.9 1.2

GRE

AU-IV

AU-IV712F01 246 1.9 8.15 23.1 13.26 48.6

2.32 55.7 41

106.27 5.1

24.6 46.19 2.2 1.1 1.3

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 248 2.4 7.82 35.36 20.23 42.7 3.11

74.64 99

258.08 18.8

18.6 34.92 2.54 0.9 1.1

CDU-E 238 1.9 7.69 21.79 12.71 34.6 1.58

37.92 74

193.69 8.9

16.4 30.79 1.4 1.1 1.5

CDU-W 238 1.9 7.94 22.5 13.12 28.6 1.35 32.4

46.0

120.4 5.7

22.6 42.43 2 1.0 1.3

BBU F-1 374 1.3 9.21 12.22 5.63 26.9 0.55 13.2

16.7

43.71 0.9

29.6 55.58 1.13 0.8 1.1

Page 59 of 244

BBU F-2 389 1.3 8.64 11.46 5.16 18.6 0.35 8.4

22.9

59.94 1.1

17.7 33.23 0.62 1.0 1.2

38.42

8.15

CGP-I HRGS-1 159 3.5 7.86 75.58 52.14 14.6 2.74

65.76 3.4 8.9 1.7 6.9 12.96

2.433 1.1 1.3

HRGS-2

3.5

HRGS-3 167 3.5 8.29 79.72 53.99 14.6 2.84 68.1

6 2.5 6.54 1.3 8.2 15.4 2.99

3 0.9 1.1 CGP-II HRGS-4 174 3.5 7.69 73.95 49.3 12.6 2.24

53.76 4.6 12.04 2.1 7.4 13.89

2.465 1.0 1.3

HRGS-5 162 3.5 8.14 78.28 53.63 15.5 2.99 71.7

6 5.4 14.13 2.7 9.6 18.02 3.47

9 1.1 1.4 FPU-II

FPU -03FF001 249 2.67 8.26 46.22 26.39 36.6 3.48

83.52 101

264.36 25.1 34.6 64.96

6.171 1.1 1.4

HCU

32.5

9.88

HCU 1&2 237 2.1 7.64 26.45 15.46 43.6 2.43 58.3

2 92.6 242.3

8 13.5 23.6 44.31 2.47 0.8 1.1

HCU 3&4 249 2.1 8.16 28.25 16.13 28.6 1.66 39.8

4 88.2 230.8

6 13.4 18.8 35.3 2.05 1.0 1.2

MSQ 15 F01-04 149 2.9 7.26 47.93 33.85 16.6 2.02 48.4

8 4.2 10.99 1.3 7.6 14.3 2 1.1 1.3

14 F01 169 1.57 8.29 16.04 10.81 14.6 0.57 13.6

8 3.8 9.95 0.4 12.6 23.7 1 1.3 1.6

15 F05 176 1.45 7.96 13.14 8.72 22.2 0.7 16.8 6.6 17.28 0.5 8.5 16.0 1 1.1 1.3

15 F01 159 1.45 7.64 12.61 8.7 18.6 0.58 13.9

2 4.3 11.26 0.4 13.6 25.5 1 0.9 1.2

LAB Hot iol 2063F01 242 4.5 7.36 117 67.7 34.6 8.43

202.32

112.0

293.15 71 29.6 55.58

13.546 1.2 1.5

2061 F-001 239 0.7 8.02 3.08 1.79 27.6 0.18 4.32 42.6 111.5 0.7 18.6 34.92 0.22

5 1 1.2

72 13.7

7


Page 60 of 244

UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS


OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N



DHDS DHDS 236 1.6 7.69 15.45 9.05 22.6 0.74 17.7

6 34.6 90.56 3.0 8.6 16.15 0.52

6 1 1.3

ISOM

F-01-F-02 188 1.7 7.89 17.9 11.57 18.6 0.77 18.4

8 22.2 58.11 2.4 12.6 23.66 0.99 1.1 1.3

DHDT F- 01 168 1.75 8.14 19.57 13.22 23.6 1.12 26.8

8 14.6 38.21 1.8 11.6 21.78 1.04 1.8 1.0

SRU

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 171 1.7 7.26 16.47 11.05

0 0 38.5 100.7

7 4.0 12.6 23.66 0.94

1.3

DCU F-01 156 2 7.44 23.36 16.23 21.3 1.24 29.7

6 14.6 38.21 2.2 7.6 14.27 0.83 0.9 1.2

F- 02 168 2 7.63 23.96 16.19 16.6 0.97 23.2

8 10.8 28.27 1.7 13.6 25.53 1.49 1.1 1.4

VGO_HDT

F-01/F22 173 1.2 7.93 8.96 5.99 18.6 0.4 9.6 32.6 85.33 1.8 14.6 27.41 0.59 1.2 1.5

Page 61 of 244

HU-I HU-I 238 2.1 8.15 28.21 16.45 23.6 1.4 33.6 12.6 32.98 2.0 10.9 20.47 1.21

2 1 1.2

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Remark:- Under shutdown in stack TPS B-1, B-3, VBU- 731F01, HGU-II, SRU (Old) & (New), HRSG-II, for Month of April- 2016.

STACK CALCULATION FOR THE PERIOD OF MAY-2016.

UNIT STACK TEMP.C

DIA OF

GAS VEL.

FLUE GAS

FLUE GAS

PARTICULATE

SULPHUR OXIDES

HYDRO CARBON

T STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N

m3 kg/hr kg/day ppm

mg/Nm3


AU-I

F-1 241 2.4 7.65 34.59 20.05 44.3 3.2 76.8 37.6 98.42 7.1 23.6 44.31 3.2 1 1.3

F-2 246 1 8.21

6.44 3.7 36.5 0.49 11.7

6 22.6 59.15 0.8 27.6 51.82 0.69 0.9 1.2

F-3 238 0.8 7.95

3.99 2.33 36.8

0.3

1 7.44

33.

6 87.95 0.7

38.

4 72.1 0.6 1.1 1.4

F-4 247 0.8 8.24

4.14 2.37 38.6

0.3

3 7.92

26.

5 69.36 0.6

25.

7 48.25 0.41 0.9 1.3

F-5 238 1.1 7.59

7.21 4.2 29.8

0.4

5 10.8

34.

9 91.35 1.4

33.

9 63.65 0.96 1.1 1.5

Page 62 of 244

7.1

3.2

AU-II

F-1 252 2.4 7.48 33.82 19.2 49.5 3.42 82.0

8 33.8 88.47 6.1 24.6 46.28 3.2 1.1 1.4

F-2 240 1 7.95 6.24 3.62 29.5 0.38 9.12 23.4 61.25 0.8 26.9 50.51 0.66 1 1.2

F-3 234 0.8 8.34 4.19 2.46 34.9 0.31 7.44 29.4 76.95 0.7 18.9 35.49 0.31 1.2 1.6

F-4 248 0.8 8.16 4.1 2.35 26.8 0.23 5.52 22.9 59.94 0.5 27.6 51.82 0.44 0.9 1.2

F-5 233 1.1 7.95 7.55 4.45 34.7 0.56 13.4

4 34.9 91.35 1.5 33.9 63.65 1.02 1.1 1.4

AU-III

F-2 248 2.1 7.39 25.58 14.63 33.8 1.78 42.7

2 26.5 69.36 3.7 23.5 44.12 2.32 1.0 1.3

F-3 239 1.7 8.21 18.63 10.84 41.6 1.62 38.8

8 22.7 59.42 2.3 22.6 42.43 1.66 1.1 1.5

11.6

2.75

CRU

CRU 21-F-01 253 0.84 8.66 4.8 2.72 22.6 0.22 5.28 33.4 87.42 0.9 28.6 53.7

0.526 1 1.2

CRU 21-F-02 255 1.1 8.14 7.73 4.36 17.6 0.28 6.72 22.8 59.68 0.9 22.6 42.43

0.666 0.9 1.3

CRU 22-F-01 247 1.28 7.69 9.89 5.67 24.9 0.51

12.24 18.6 48.68 1.0 18.6 34.92

0.713 1.1 1.5

CRU F1 45 2.2 - - - - - - 4.3 11.26

12.2 22.91

1.4 1.9

2.8

1.379

UDEX Udex 168 1.88 ~ ~ ~ - ` ` 9.8 25.65 ~ 8.9 16.71 ~ 1.1 1.3

AU-V

AU-5 238 3.15 7.26 56.55 32.98 42.6 5.06 121.44 43

112.29 13.3 29.5 55.39

6.576 1.1 1.4

FCC

CO-BOILER 158 2.6 14.6 77.48 53.57 124 23.9

1 573.84 36.5 95.54 18 26.9 50.51 9.74 ~ 4.6


26.16 18.6 48.68 2.3 12.6 23.66 1.14 1.1 1.3

Page 63 of 244

FPU-1 8/2 F01 248 2.3 7.85 32.6 18.65 19.4 1.3 31.2 23.6 61.77 4.2 16.9 31.73 2.13 1.2 1.5

STACK CALCULATION FOR THE PERIOD OF MAY-2016

UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS


OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N



HGU-III

F-101 172 1.7 8.21 18.63 12.48 15.6 0.7 16.8 12.6 32.98 1.5 12.6 23.66 1.06 0.9 1.3

F-01 163 3.5 7.26 69.81 47.71 23.6 4.05 97.2 19.4 50.78 8.7 9.5 17.84 3.06 1.1 1.4

TPS B1 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B2 159 3 ~ ~ ~ ~ ~ ~ 42.6 111.5 ~ 16.6 31.17 ~ 1.1 1.3

B3 ~ 3 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

B4 167 3 ~ ~ ~ ~ ~ ~ 34.9 91.35 ~ 22.6 42.43 ~ 1.2 1.5

GRE AU-IV

AU-IV712F01 235 1.9 8.26 23.41 13.73 46.5 2.3 55.2 35

90.56 4.5

23.2 43.56 2.15 0.9 1.2

VDU VBU731F01 ~ 2.4 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

VDU721F01 238 2.4 7.36 33.28 19.41 36.5 2.55 61.2 97

252.58 17.7

18.6 34.92 2.44 1.1 1.4

CDU-E 242 1.9 7.89 22.36 12.94 24.9 1.16

27.84

46.9

122.76 5.7

26.4 49.57 2.3 1 1.3

CDU-W 229 1.9 8.06 22.84 13.56 34.6 1.69

40.56

83.6

218.82 10.7

18.4 34.55 1.69 1.2 1.6

Page 64 of 244

BBU F-1 336 1.3 8.42 11.17 5.47 19.5 0.38 9.12

16.9

44.23 0.9

16.5 30.98 0.61 0.9 1.2

BBU F-2 367 1.3 8.13 10.79 5.02 17.6 0.32 7.68

26.8

70.15 1.3

22.4 42.06 0.76 1.0 1.3

38.53

8.59

CGP-I HRGS-1 178 3.5 7.69 73.95 48.86 15.6 2.74

65.76 4.2 10.99 1.9 6.9 12.96 2.28 1 1.3

HRGS-2 164 3.5 8.21 78.95 53.84 21.6 4.19 100.56 3.6 9.42 1.8 8.2 15.4

2.985 0.9 1.2

HRGS-3 173 3.5 7.81 75.1 50.18 12.6 2.28 54.7

2 2.7 7.07 1.3 7.4 13.89 2.50

9 1 1.2 CGP-II HRGS-4 168 3.5 8.26 79.43 53.67 16.4 3.17

76.08 7.6 19.89 3.8 12.6 23.66

4.571 1.1 1.4

HRGS-5 172 3.5 7.69 73.95 49.52 20.8 3.71 89.0

4 9.4 24.6 4.4 16.9 31.73 5.65

7 1.2 1.5 FPU-II

FPU -03FF001 248 2.67 7.49 41.92 23.98 42.6 3.68

88.32 72.6

190.03 16.4 14.6 27.41

2.366 1.1 1.3

HCU

32.5

9.88

HCU 1&2 247 2.1 7.69 26.62 15.26 22.4 1.23 29.5

2 86.6 226.6

7 12.5 26.6 49.94 2.74 1.0 1.3

HCU 3&4 238 2.1 8.03 27.8 16.21 37.6 2.19 52.5

6 106 277.4

5 16.2 18.6 34.92 2.04 1.1 1.4

MSQ 15 F01-04 168 2.9 7.36 48.59 32.83 14.6 1.73 41.5

2 4.6 12.04 1.4 12.3 23.1 3 0.9 1.2

14 F01 176 1.57 8.12 15.71 10.43 10.2 0.38 9.12 6.8 17.8 0.7 8.9 16.7 1 1.1 1.3

15 F05 169 1.45 8.26 13.63 9.19 18.6 0.62 14.8

8 3.9 10.21 0.3 16.9 31.7 1 0.9 1.2

15 F01 174 1.45 7.69 12.69 8.46 16.4 0.5 12 7.4 19.37 0.6 9.9 18.6 1 1.1 1.4

LAB Hot iol 2063F01 233 4.5 7.36 117 68.91 39.6 9.82

235.68 78.4

205.21 51 22.4 42.06

10.434 0.9 1.2

2061 F-001 247 0.7 8.12 3.12 1.79 21.6 0.14 3.36 23.6 61.77 0.4 14.6 27.41 0.17

7 1 1.4

51 10.6

1

Page 65 of 244

STACK CALCULATION FOR THE PERIOD OF MAY-2016

UNIT STACK TEMP.

DIA OF

GAS VEL.

FLUE GAS


OXIDES

HYDRO CARBON

T 0C STAC

K

VOLUME


CARBON

MONOXIDE


NITROGEN

M3/SEC M3/SEC mg/N



DHDS DHDS 227 1.6 7.85 15.78 9.4 33.4 1.13 27.1

2 16.9 44.23 1.5 11.4 21.4 0.72

4 1.1 1.3

ISOM

F-01-F-02 169 1.7 8.24 18.69 12.6 19.6 0.89 21.3

6 14.4 37.69 1.7 16.4 30.79 1.40 0.9 1.3

DHDT F- 01 173 1.75 8.09 19.45 13 19.6 0.92 22.0

8 16.9 44.23 2.1 12.8 24.03 1.13 0.9 1.2

SRU

SRU-II (New) _ 1 - - - - - - - - - - - - - -

SRU-I (Old) - 1 - - - - - - - - - - - - - -

SRU SRU-F-04 169 1.7 7.81 17.72 11.95 0 0 33.8 88.47 3.8 18.6 34.92 1.50 1.2

DCU F-01 164 2 7.89 24.77 16.89 22.4 1.36 32.6

4 9.4 24.6 1.5 14.6 27.41 1.67 1 1.2

F- 02 177 2 8.14 25.56 16.93 14.6 0.89 21.3

6 14.6 38.21 2.3 8.9 16.71 1.02 1.3 1.6

Page 66 of 244

VGO_HDT

F-01/F22 183 1.2 7.95 8.99 5.88 26.9 0.57 13.6

8 13.6 35.6 0.8 10.6 19.9 0.42 1.0 1.2

HU-I HU-I - 2.1 - - - - - - - - - - - - - -

HGU-II

F-01 - 1.6 - - - - - - - - - - - - - -

Remark:- Under shudwon in stack TPS B-1, B-3, VBU- 731F01, HU-I, HGU-II, SRU (Old), & (New) for Month of May- 2016.

Page 67 of 244

Deepak Nitrite Limited

Effective Date : 05.03.2007 2-Ethyl Hexyl Nitrate Page 1 of 4

Material Safety Data Sheet 2-Ethyl Hexyl Nitrate

1 Product And Company Identification :

Product Name : 2-Ethyl Hexyl NitrateCAS No. : 27247-96-7Supplier : Deepak Nitrite Ltd.

National Games Road, Opposite Golf Course, Yerawada, Pune – 411 006. (India).

Telefax : +91 – 20 – 26685448E – mail : [email protected] Tel. No (US) : 800-424-9300 (CHEMTREC)Emergency Tel. Nos. (Outside US)

: +91-22-24452017Cell : +91-98200 29917

2 Composition / Information On Ingredients :

Hazardous components : 2-Ethyl Hexyl Nitrate Synonyms : Octyl nitrate, Nitric acid 2-ethylhexyl esterChemical formula : C8H17NO3

Molecular weight : 175CAS No. : 27247-96-7UN No. : 3082EINECS No. : 248-363-6Hazard symbols : Marine Pollutant Risk phrases : R 5/8/20/21/22/36/37/38Safety phrases : S 15/26/27/36/37/39

3 Hazards Identification :

Potential Health Effects:Harmful by inhalation, in contact with skin and if swallowed. May cause eye, respiratory system and skin irritation.

4 First Aid Measures :

Remove all contaminated clothing immediately. Following skin contact : Wash skin immediately with plenty of water and soap. If skin reactions occur, contact a physician. Following eye contact: Open the eyelids and rinse for an adequate length of time with water. Consult an eye specialist immediately. Upon inhalation : Remove victim to fresh air area. If there is difficulty in breathing, medical attention should be obtained. Upon swallowing : Rinse mouth several times. Ensure that patient drinks plenty of water. Seek medical advice.

Page 68 of 244

Consultancy

Typewritten text

Annexure-12



5 Fire Fighting Measures :

Fire Extinguishing Media : Dry chemical powder, foam. Do NOT use water jet. Thermally unstable above 100 oC. May undergo self-accelerating exothermic decomposition. Cool containers exposed to heat by flooding water. Beware of exploding containers. Keep safe distance while fighting fire. Beware of formation of toxic fumes of Nitrogen oxides, Carbon monoxide, Carbon dioxide. Wear respiratory protection equipment. Do not allow contaminated extinguishing water to enter soil, ground water or surface waters.

6 Accidental Release Measures :

Fill into labeled sealable containers. Use necessary personal protective equipment when handling.

7 Handling & Storage :

Store in a cool, dry, well ventilated area, away from heat, sparks and flames. Be careful while opening drums, which may be pressurised. Preferred material for storage is stainless steel as mild steel can be attacked by the nitric acid liberated by hydrolysis, with water traces. During processing, ensure sufficient exhaust ventilation in the working area. Vent waste air via suitable separators or scrubbers.

8 Exposure Control / Personal Protection :

Respiratory protection :Follow the OSHA respirator regulations found in 29CFR 1910.134 or European Standard EN 149. Always use a NIOSH or European Standard EN 149 approved respirator when necessary.Eye protection: GogglesWear butyl rubber gloves if contact with product is possible.Avoid contact with eyes or skin. Do not inhale vapours.

9 Physical And Chemical Properties :

Colour : Straw coloredOdour : Strong pungent pH : Not applicableBoiling Point/range : Decomposes above 100 0 C (212 0 F)Melting point : < 45 oCFlash Point : 79 °C (174 oF)Auto ignition temperature

: 130 oC

Explosion properties : Can explode if heated above 100 oC. LEL : 0.25% v/v in air

Density : 0.96 g / cm3

Solubility : 13 mg/l at 20 oC

Page 69 of 244



10 Stability And Reactivity :

Chemically stable. Incompatible with strong acids, strong bases. Nitrogen oxides, transition metal oxides and their chelates greatly accelerate decomposition rate. Formation of nitrogen oxides, carbon monoxide and carbon dioxide in the event of fire.

11 Toxicological Information :

Acute toxicity : LD50 (Oral rat) : > 5000 mg/kg.Irritation of the eyes : May produce temporary discomfort.Irritation of the skin : Harmful by skin contact.RTECS# : CAS No. 27247-96-7 unlisted.Carcinogenicity : None of the components present in this material at

concentrations equal to greater then 0.1% are listed by ACGIH, IARC, NIOSH, NTP or OSHA.

Special properties : Data not available.

12 Ecological Information :

Acute fish toxicity LC50 : above solubility limitThe product does not contain any organically bonded halogens, which can lead to AOX values in the waste water.Readily hydrolysed in water.

13 Disposal Considerations :

Examine possibilities for re-utilization. Package product wastes. Close and label waste containers. Dispose these at a suitable waste incineration plant in accordance with the official regulations. Where large quantities are concerned, consult the supplier. When uncleaned empty containers / packing material is passed on, the recipient must be warned of any possible hazard that may be caused by the residues.

14 Transport Information :

UN No. : 3082 Hazard Class : 9 Packing Group : IIIProper shipping name : Environmentally Hazardous Substance, Liquid, N.O.S. Declaration for land shipment : As aboveDeclaration for sea shipment : As aboveDeclaration for air shipment (IATA) : As above DOT Classification (USA) : NA 1993 – Combustible liquids, NOS. (2-ethyl hexyl nitrate)

Page 70 of 244



15 Regulatory Information :

Symbols : Harmful Xn Combustible

Contains 2-Ethyl Hexyl Nitrate R 5 : Heating may cause explosion. R8 : Contact with combustible material may cause fire. R20/21 : Harmful by inhalation, in contact with skin. R44 : Risk of explosion if heated under confinement. S15 : Keep away from heat. S26 : In case of contact with eyes, rinse immediately with plenty of water and seek medical advice. S27 : Take off immediately all contaminated clothing. S36/37 : Wear suitable protective clothing and gloves.

16 Other Information:

DISCLAIMER : Deepak Nitrite Ltd. provides the information contained herein in good faith but makes no representation as to comprehensiveness or accuracy. This document is only as a guide to a properly trained person, for the appropriate precautions and handling of the material. Individuals receiving the information must exercise their independent judgement in determining its appropriateness for a particular purpose. The data does not signify any warranty with regard to the product’s properties.

Page 71 of 244

Disaster Management planat Gujarat Refinery, District Vadodara, Gujarat

DISASTER MANAGEMENT PLAN

1. BASIS OF DMPThis DMP has been designed based on the range, scales and effects of"major generic hazards" described in the risk assessment report justmentioned and on their typical behaviours predicted therein. The DMPaddresses the range of thermal and mechanical impacts of these majorhazards so that potential harm to people on-site and off-site, plant andenvironment can be reduced to a practicable minimum. The scenarios ofloss of containment are credible worst cases to which this DMP is linked.

2. CAPABILITIES OF DMPThe emergency plan envisaged is designed to intercept full range ofhazards specific to plant such as fire, explosion, major spill etc. Inparticular the DMP is designed to mitigate those losses of containmentsituations which have potentials to escalate into major perils.

Another measure of the DMP's capability is to combat small and large firedue to ignition of flammable materials either from storage or from processstreams and evacuate people from the affected areas speedily to safelocations to prevent irreversible injury.

Emergency medical aids to those who might be affected by incident heatradiation flux and toxic exposure are inherent in the basic capabilities.

The most important capability of this DMP is the required speed ofresponse to intercept a developing emergency in good time so thatdamages can be minimised.

3. DISASTER CONTROL PHILOSOPHYThe emergency control philosophy of the plant is in line with its normaloperational controls. All emergency operations that may involve shut-down of the plant are controlled from the emergency control room bysending commands to initiate the shutdown procedure using "automaticshut-down system".

The principal strategy of DMP of the plant is "prevention" of identifiedmajor hazards. The "identification" of the hazards is conducted employingone or more of the techniques [e.g. hazard and operability study (HAZOP),accident consequence analysis etc.] based on "Manual on EmergencyPreparedness for Chemical Hazards" prepared by Hazardous SubstancesManagement Division of MOEF, New Delhi. And since these hazards canoccur only in the event of loss of containment one of the key objectives oftechnology selection, project engineering, construction, commissioningand operation is "total and consistent quality assurance". The ProjectAuthority is committed to this strategy right from the conceptual stage ofthe plant so that the objective of prevention can have ample opportunitiesto mature and can be realised in practice.

Page 72 of 244

Consultancy

Typewritten text

Annexure-13


The codes, standards and regulations (acts and rules) are followed to theextent applicable such as OISD norms, API standards, NFPA standards,Indian Explosives Act & Explosives Rules, The Petroleum Act, Standardsof BIS, Factories Act, Environment (Protection) Act and Rules,Manufacture, Storage & Import of Hazardous Chemicals Rules, etc.

The Disaster Management Plan (DMP) or Emergency Preparedness Plan(EPP) will consist of:

- On-site Emergency Plan- Off-site Emergency Plan

Preparation of Disaster Management Plan under the headlines of On-siteEmergency Plan and Off-site Emergency Plan is in consonance with theguidelines laid by the Ministry of Environment and Forests (MOEF), Govtof India.

As per the guidelines given by the Government, the "occupier" of thefacility is responsible for the development of the On-site Emergency Plan.The Off-site Emergency Plan should be developed by the Government(District Authorities).

Gujarat Refinery has already laid down an On-site Emergency Planprepared based on the risk analysis.

4. ORGANISATIONAL PLANThe occurrence of any emergency (viz.) Minor or Major Fires, Toxicrelease etc. will be informed by staff / officers of the concerned area tothe Fire and Safety Control Room and RSM initially by breaking the glassor by telephone.

RSM and/or Shift–in-charge of Fire Station C/Room will intimate thesame to CPNMs, CMF&S and DGM (PN). Meanwhile Fire and Safetyofficer along with his F&S crew, concerned persons of the affected areaand on duty RSM will handle the situation. After reaching the siteDMF&S/ MF&S/ CMF&S will assess the situation and give informationto DGM (PN). On the arrival of DGM (PN) and /or CPNMs, dependingapon the assessment of prevailing situation, decision will be taken toactivate the Onsite Emergency Plan. Once decided to declare an on-siteemergency, instructions will be passed on by DGM (PN) to Fire StationControl room to blow the siren according to type of emergency.

Upon declaration of emergency, Disaster Control Room (DCR) at FireStation will be activated, and all the functionarirs as per the followingtable will be assuming their specific roles & responsibilities. Intimation toall functionaries will be given through emergency siren and by phonefrom F&S control room.

Page 73 of 244


CONTACT TELEPHONE NUMBERS OF FUNCTIONARIES OF ONSITE EMERGENCY PLAN

AUTO TELEPHONE P&T TELEPHONE MOBILE NO.DISASTER MANAGEMENT CENTRE

AT REFINERYINCOMING

7300/7400 2233346 Nil

OUTGOING

7600/7700 2233347 Nil

OFFSITE INDUSTRIAL EMERGENCY CONTROLROOM (OCR) (AT-RIL):

Nil 2232327 &2230556

2232327 &2230556

DISTRICTCOLLECTOR’SOFFICE

VINOD RAO Collector &DM

Nil 2432093 (PA)2423100 &2433000

9978406224

RESPONSIBILTY OFFICER DESIG.AUTO P&T AUTO P&T MOBILE NO.

OFFICE RESIDENCE

CHIEF INCIDENTCONTROLLER (CIC)

Roy Gautam ED 7101 2233301 6101 2266101 8980933366

FIRST SUCCESSION Mandal PK GM(HSE) 7105 2233305 - 2266105 9726028282

SECONDSUCCESSION

Ray Sukumar GM(T) 7108 2233308 6108 2266108 9428820453

TECHNICALADVISER TO ED

Manvi R GM(TS) 7110 2233310 6110 2266110 8469921212

FIRST SUCCESSION Garg DK DGM(HSE)

7113 2233313 6113 2266113 9586025252

SECOND SUCCESSION Sahney AS CTSM 7303 2230196 6303 2265916 9979307571

CRISIS MGT. GROUP SKChakraborthy

DGM(TS) 7112 2233312 - 2334852 9426760058

FIRST SUCCESSION SarkarSubhajit

CTSM 7302 2233390 6302 2266096 9586022722

SECOND SUCCESSION Ranalkar VM CM(HSE) 7371 2233388 - 2353738 9426553368

(SIC) SITE INCIDENTCONTROLLER-PLANT/RUP

Ukey SM DGM(PN) 7116 2233316 6116 2265116 8238091544

FIRST SUCCESSION Bakre RD CPNM 7401 2233361 - 2662010 9099928127SECOND SUCCESSION Bose S SPNM 7410 6410 2265144 9376692300(SIC) SITE INCIDENTCONTROLLER-OFFSITE,CETP& OMS

Patel NU DGM(PN) 7120 2233362 - 2290156 9898177552

FIRST SUCCESSION Solanki PV CPNM 7402 2230590 - 2391073 9416563030

SECOND SUCCESION Patil Pankaj PNM 7437 - 6421 - 9537081295

(SIC) SITE INCIDENTCONTROLLER-TPS & CGP

Dasgupta TK GM(P&U) 7104 2233304 6104 2266104 8980144222

FIRST SUCCESSION Parashar GD CPUM-I 7701 2233454 6701 2266067 9426411825

SECOND SUCCESSION Hymarao GV CPUM-II 7702 2233375 6702 2265773 9726112826

Page 74 of 244


INCIDENTCO-ORDINATOR(RSM)

RSM RSM 7407 2233372 - 23931572390115

9426022327/9099502326

PLANTCO-ORDINATOR

Parmar MM CPNM 7404 2233359 - 2395944 9687053507

FIRST SUCCESSION Sen Bhaskar SPNM 7408 - 6408 - 8238091216SECOND SUCCESSION Roy AK PNM 7406 - 2773839 9426984608FIRE & SAFETY CO-ORDINATOR

Singh AK CM(F&S) 7441 2233345 6441 2265607 9825041923

FIRST SUCCESSION Panda BK SM(F&S) 7443 - 6443 - 9898376101

SECOND SUCCESSION Wanjari IK SM(F&S) 7445 - - 6452979 9427841459

MECH. MAINT.CO-ORDINATOR

ChakrabortySK

DGM(MN) 7122 2233322 6122 2265218 9586022622

FIRST SUCCESSION Das SK CMNM 7602 2233453 6602 2265892 8866001969

SECOND SUCCESSION Kanti Sunil CMNM 7603 2230593 6603 2265313 9724258130

TRANSPORT/RELIEF/WELFARECO-ORDINATOR

Solanki PT DGM(HR) 7106 2233306 - 2351227 9811921963

FIRST SUCCESSION Ms. PiyaliChakraborty

CHRM 7126 2233326 6126 2264166 9825106221

SECOND SUCCESSION Sarma MVV CM(A&W) 7127 2233696 6127 2265188 9879576578EVACUATIONCO-ORDINATOR

DasBhagwan

SM(A&W) 7131 - 6131 - 9408704949

FIRST SUCCESSION Surve CG M(ER) 7136 2230181 - 2390285 9925117010SECOND SUCCESSION K.Manivasag

anDMER 8132 2233355 6138 - 8238019633

COMMUNICATION &UTILITY CO-ORDINATOR

Sengupta D DGM(IT) 7119 2233319 - 2974707 8980233222

FIRST SUCCESSION AgarwalMukul

CMNMEL 7801 2230545 6801 2266931 9429536030

SECOND SUCCESSION Nanda Manoj CITM 7851 2233367 6851 2264083 9537033355

MEDICAL CO-ORDINATOR

Dr. VipinSagar

CMO 6501 2264039 - 6546259 9825708569

FIRST SUCCESSION Dr. DChakraborti

ACMO 6502 - 6515 - 9925269240

SECOND SUCCESSION Dr. DNNagpure

JCMO 6503 - 6513 - 9687695330

SECURITY/TRAFFICCO-ORDINATOR

Vashist BS COMDT(CISF)

6571 2265127 6581 2265054 9426411818

FIRST SUCCESSION Manasseh M Inspector 6573 - 6194 - 9426955628SECOND SUCCESSION Payasi PK Inspector 7993 - 6995 - 8000052944

MATERIALS CO-ORDINATOR

Mondal TK GM(M&C) 7111 2233311 6111 2266111 9426411803

FIRST SUCCESSION Makwana AC CMTM 7251 2233351 - 2327531 9998484963SECOND SUCCESSION Prasad UK CMTM 7252 2233364 6252 2266289 9537022277

Page 75 of 244


PROJECT CO-ORDINATOR

Atha HS DGM(PJ) 7118 2233318 6118 2265793 9428423868

FIRST SUCCESSION Mahendra C CPJM 7901 2230153 6901 2265315 9427056928SECOND SUCCESSION Bendbar BN SPJM(I/c) 7902 2233387 - 2391563 9825872064FINANCE CO-ORDINATOR

Murali G GM(F) 7103 2233303 6103 2266103 8980533366

FIRST SUCCESSION Jain VK DGM(F) 7117 2233317 6117 2265657 8238091380

SECOND SUCCESSION Banik S CFM 7201 2233342 6201 2265142 9408339622MEDIA CO-ORDINATOR

Ms. BhaveAnjali

SHRM 7197 2230916 - 2351692 9537868170

FIRST SUCCESSION Ms. PhilipCiny Mathew

DMER 7142 - - 2648751 8238091518

SECOND SUCCESSION Ms. PatadeDS

O (CC) 7198 - 6198 9909360700

MARKETINGCO-ORDINATOR

Shaikh MG GM(RC) 7051 2232910 - 2314261 9426416101

FIRST SUCCESSION Parate GM CM(RC) 7057 2232733 6064 2265357 9408705914SECOND SUCCESSION Saha Samir SM(RC) 7055 2232805 6061 2265130 9429899881PIPELINESCO-ORDINATOR

Lal Madan DGM 7081 2230107 6081 2264048 9427214487

FIRST SUCCESSION KargaonkarAN

COM 7091 2232396 6077 - 9426802791

SECOND SUCCESSION Pande SD CMNM 7096 2233214 6088 2265263 9879393471

Note:1) Shri Prasant Rout, CM (A&W) shall be present in DMC to assist Security and Traffic Co-ordinator.

2) All auto numbers can also be contacted through P&T by pre-fixing 223.

3) In absence of Main Co-ordinator, first successor will take over. In absence of first successor, secondsuccessor will take over.

OVERALL OBJECTIVES OF AN EMERGENCY CONTROL ORGANIZATIONSHALL BE:

(a) To promptly control problems as they develop at the scene.

(b) To prevent or limit the impact on other areas and off-site.

(c) To provide emergency personnel, selecting them for duties compatiblewith their normal work functions wherever feasible. The duties andfunctions assigned to various people shall include making full use ofexisting organizations and service groups such as fire, safety,occupational health, medical, transportation, personnel, maintenance,and security.

(d) Employees must assume additional responsibilities as per laid downprocedure of ERDMP whenever an emergency alarm sounds.

Page 76 of 244


In setting up the organization, the need for round-the-clock coverage shallbe essential. Shift personnel must be prepared to take charge of theemergency control functions or emergency shutdown of system, if need be,until responsible personnel arrive at the site of emergency. The organizationshould have an alternate arrangement for each function.

Organisation Chart

Medical Servicesand Ambulance

Fire BrigadeServices

PoliceServices

Off-Site IncidentCommander

(DistrictMagistrate)

CHIEF INCIDENT

CONTROLLER

Affected StakeHolders andGovernmentAuthorities

SITE INCIDENT

CONTROLLER

Mutual Aid

Municipal transportrescue and

rehabilitation team

Transport/Relief/Welfareand

CommunicationCoCoordinator

SupportServices *

Fire SafetyCoordinator

Operation Team,technical team, etc.

Page 77 of 244


5. ROLES & RESPONSIBILITY OF FUNCTIONARIES OF ONSITEEMERGENCY PLAN

During the emergency, Key functions & location of functionaries issummarized in table below. Detailed role for each functionary along withreporting organogram, contact telephones and residential address is alsogiven in subsequent pages.

FUNCTIONARY REPORTING & KEY FUNCTIONS LOCATION

Chief Incident Controller (CIC)

ED

GM (HSE)

GM (T)

Overall In charge

First Succession

Second Succession

DMC or Site.

In order to exercise overallcommand, control &communication of theprevailing disastrous situation,

ED/GM (HSE)/GM (T) maybe available at Site or atDisaster Management Centreor at ED's office depending onthe requirement, based onfeedback from Site IncidentController (SIC).

Technical Adviser to ED Reports to ED for Technical Assistance. DMC

Crisis Mgt. Group Reports to Technical Adviser for technical Assistance DMC

Site Incident Controller (SIC)

SIC- Plant & RUP

SIC-Offsite,OMS & CETP

SIC-TPS & CGP

Reports to ED & reaches at siteMain functions are: Declaration of emergency after assessing the situation

at site. Overall in-charge of the emergency situation at site

and positions himself at site Take commands & control of the situation at site. Establishes communication with DMC and emergency

site. Liaison with all the functional coordinators / sub-coordinators through DMC.

Emergency Site.

Note: Other two SIC has totake care of his respectiveunit.

Incident Co-ordinator(RSM)

Reports at emergency site & will take charge at site tillarea in charge or SIC arrives. He will return to RSMoffice after handing over the charge to SIC.

Initially at Site & then RSMoffice

Plant Co-ordinator Takes instruction from SIC or DMC and implementstheir decision.

RSM Office

Fire & Safety Co-ordinator Reports to SIC & will be in charge of fire fighting andrescue operations inside the refinery. He will maintainconstant link with Disaster Management Centre throughwireless.

Emergency Site

Mech.Maint. Co-ordinator Reports to DMC and will co-ordinate with SIC for anyrequirement at site.

DMC

Transport / relief/ welfare Co-ordinator

Reports to DMC and will arrange for transport, welfare,and co-ordination with district authority

DMC

Evacuation Co-ordinator Take instruction from SIC and arrange the transportationof people from Assembly points to exit gate of Refinery.

Time Office

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Comm. & utility Co-ordinator In-charge of Operation, Maint. Of Communication andGeneration / Distribution of Utilities.

DMC

Medical Co-ordinator Reports to ED / DMC on phone for providing medicalaid & casualty management.

GR Hospital

Security & Traffic Co-ordinator Reports to ED & will be in charge of the Security &Traffic control at gates & inside refinery. He willarrange CISF for providing help in fire fighting, search& rescue operation at emergency site.

DMC

Material Co-ordinator Emergency procurement of fire fighting materials. DMC

Project Co-coordinator Take stock of Refinery situation & at all project sites. DMC

Finance Co-ordinator Taking care of cash, insurance claim etc. DMC

Media Coordinator Reports to ED & takes care of press/ media personnel DMC

Marketing Coordinator/Pipeline Coordinator

Contacting Disaster Management Centre to obtain detailinformation about disaster

DMC

All the Functional Co-ordinatorother than mentioned above

All the main Coordinators report ED at DMC and theywill ensure deployment of Sub-Coordinators to report toSIC at emergency site and meets requirements as pertheir functional role

DMC

All Successors and other officersunder the control of the eachFunctionalCo-ordinator

They will report to their respective FunctionalCoordinator & follow their instructions

All Successors & otherofficers will remain in contactwith the Functional Co-ordinator and makethemselves available at theirdesignated office / telephoneto receive instructions as perthe situation.

6. GENERAL FUNCTIONS OF FUNCTIONAL CO-ORDINATORS1. All the Functional Coordinators will report immediately at their

designated locations as mentioned above on declaration of On-SiteEmergency and extend all possible help for mitigation of emergencysituation.

2. Keep list of officers / staff of their department ready.

3. Keep track of number of their department personnel deployed foremergency duty.

4. Head count of personnel of his department working in refinery at the timeof disaster occurrence and establish contact with them. Report names /employee numbers of the missing to Welfare/Transport Coordinator.

5. Prepare list of persons who are required for handling the on-site disastersituation and communicate to HR for necessary arrangement.

6. To inform the number of personnel engaged in emergency jobs toTransport, Relief & Welfare Coordinator for drinking water, food etc.

7. Give periodic feed back to Disaster Management Centre, ED, and SiteIncident Controller.

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7. FUNCTIONS OF CO-ORDINATOR7.1 Function of Chief Incident Controller (CIC)

CHIEF INCIDENT CONTROLLER Gautam Roy, ED Location: DMC or Site as perfeedback from SIC

First Successor PK Mandal, GM (HSE)Second Successor Sukumar Ray, GM (T)

Executive Director is the CIC & overall in-charge of the Refinery;Preparation, review, and updation of the ERDMP as per Chapter 27, Check List – 5

(As per ERDMP regulation 14.2.1 (a) );

Assessment of situation and declaration of emergency ;Activation of Emergency Control Centre (ECC) / Disaster Management Centre (DMC) ;Taking decision on seeking assistance from mutual aid members and external agencies like Police, Fire

Brigade, hospitals etc;Continuous review of situation and decide an appropriate response strategy;Taking stock of casualties and ensure timely medical attention;Ensuring correct accounting and position of the personnel after emergency;Ordering evacuation of personnel as and when necessary;Taking decision in consultation with District Aunthorities when an Off-site emergency to be declared;Mobilisation of main co-ordinators and key personnel;Communication with following external agencies will be through respective coordinators in consultation

with ED :

SN Communicate to Name NO. BY

1. RHQ, ED (Operation) SK Ghosh 011-243681050 8588830810

GM (HSE)

2. RHQ, ED (HSE) B.P.Baliga 011-243646610 96549 05150

GM (HSE)

3. Dy. Chief Controller ofExplosives, Vadodara

Dr. SanjanaSharma

22251592361035

GM (HSE)

4. GSFC, MD Atanu Chakraborty 22424512240855

GM (HSE)

5. OCR (Offsite IndustrialEmergency Control Room)

Shift in Charge 2232327, 2230556 DGM (HSE)

6. RIL, Site President KV Sheshadari 6692610 DGM (HSE)

7. GACL GK Agarwal 65404602240855 (direct)

DGM (HSE)

8. Regional Officer, GPCB,Vadodara

KC Pancholi 2354850 CM (HSE)

9. Collector & DM, Vadodara Vinod Rao 2423093(off)2313131(res)99784 06224

DGM (HR)

10. **(DEOC) District EmergencyOperation Centre, Vadodara

In-charge 24275921077

DGM (HR)

11. Chief Secretary, Governmentof Gujarat Gandhi nagar

Dr. Varesh Sinha 079-23250301079-23250304

DGM (HR)

12. Principal Secretary, Forest & HK Dash 079 – 23251051 DGM (HR)

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Environment Deptt. 982504828613. Joint Director (Industrial Safety

& Health), VadodaraPM Shah &Mayoor J Vaghela

24268482432543

DGM (HR)

14. Commissioner of Police,Vadodara for law & Ordersituation

Satish Sharma 2431414243151599784 06276

DGM (HR)

15. Local Police Station,(Jawaharnagar)

Mr. Rana 2232382 CHRM

16. District Chief Medical Officer,Vadodara

Dr. Babubhai Patel 2425715Extension -205

CMO

17. Superintendent,Central Excise& Custom, Vadodara

RM Parmar 22333289925242597

GM (F)

** In addition to above, written report is to be submitted to District EmergencyOperation Centre (DEOC).

IOC (R), RHQ, New Delhi will inform to the following agencies:

1. Oil Industry Safety Directorate, New Delhi;2. Ministry of Petroleum and Natural Gas, New Delhi;3. Chief Executives of other oil companies.

7.2 Functions of Technical advisor to ED

TECHNICAL ADVISOR to ED R Manvi, GM (TS) Location: DMCFirst Successor DK Garg, DGM (HSE)Second Successor AS Sahney, CTSM

Preparation of incident report in consultation with SIC. Keep records related to the incident site ready, namely

1. P&IDs2. Operating Manuals3. MSDS4. Environment Clearance5. Latest ESA report6. Latest SSA report

Sending information to RHQ after approval of ED. Deploy one officer from QC Laboratory to report at Main Fire Station

Control Room for additional manning / extending help incommunication & co-ordination activities during major emergency /on-site disaster.

Deploy additional manpower required for manning of Disaster ControlRoom on round the-clock basis, in case of prolonged operation ofDCR. DGM (Maint.) & DGM (HR) to ensure representatives in DCRround the clock.

Deployment of officers from Process Section at disaster / emergencysite to guide F&S, Production & Maintenance personnel.

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Liaison with all the functional coordinators & update status ofincident as well as refinery operations, inventory of products/crude toED.

Briefing status to RHQ after the approval of ED. Preparation for media briefing & get approval from ED. Assist Finance Coordinator for Excise and Insurance claim. Assist Finance Coordinator in preparing preliminary estimate of

damage to property.

7.3 Functions of Crisis management group:

CRISIS MANAGEMENT GROUP SK Chakraborthy , DGM (TS) Location: DMCFirst Successor S Sarkar, CTSMSecond Successor VM Ranalkar, CM (HSE)

Crisis management group is the “Think Tank group” of the Refinery. Besides functional Coordinators, a "Crisis management group '- will

also assist the Technical Advisor to ED. The Crisis management group will be consisting of officers with

complete knowledge of Refinery topography & process flow. They should be preferably of persons with maximum station seniority

not merely by designation. Crisis management group mainly assist the technical advisor to ED. Functions of Crisis management group are same as Technical advisor

to ED.

7.4 Functions of Site Incident Controller (SIC):

SITE INCIDENT CONTROLLER GM (P&U) / DGM (PN) Location:Emergency Site

First Successor CPUM/CPNMSecond Successor CPUM/SPNM/PNM

Overall in-charge of the emergency situation at site positions himselfat site and establishes communication with DCR and emergency site.

Take commands & control of functionaries reported at site. Liaisonwith the Functional Co-coordinators / DCR regarding resourcesrequired at site for mitigation of emergency / disaster situation.

Takes priority decisions on: Isolation of facilities / equipments Shutdown of plants, equipments as per requirement. Strategy for deployment of resources of fire fighting/rescue inside

the refinery Evacuation of personnel from affected zone to a safer area

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T 'put regulation / product routings Product storage and dispatch operations Crude oil receipts

Periodic assessment of actual disaster zone & resources requirement /deployment (both internal & external) and communicates accordinglyto Disaster Control Room regarding: Requirement of additional resources (Manpower, equipment &

appliances) required for Fire Fighting from: CISF, Mutual AidMembers (RIL, GSFC), (OCR), Vadodara Municipal Corporation(VMC) fire Services, Home Guards Civil Defence,

Medical Aid from neighbouring industries, District Medical Officer,Baroda, Superintendent of SSG Hospital, and other hospitals asper requirement

Regulation of rail traffic movement on Bajwa-Ranoli Section. Regulation of traffic pattern through various refinery gates.

7.5 Functions of Incident Co-ordinator (RSM):

INCIDENT CO-ORDINATOR RSM Location: Initially at site andthen at RSM office.

Reports immediately & takes charge directly at the scene of theincident till the arrival of Site Incident Controller (SIC).

Co-ordinate between Operation, Maintenance, Fire & Safety, Medical& CISF Personnel for effective handling of emergency during initialstages.

Providing guidance to the concerned Engineers / Sr. Engineers of theaffected area and workout for immediate isolation / shutdowns /product rerouting etc.

Assess the situation with production & F&S personnel andcommunicates to CPNM / CMF&S/ DGM (PN) regarding the type &severity of emergency (injury or accident of manpower, small or majorfire, vapour cloud, toxic release, or explosion etc.).

Receiving instructions from SIC for latest developments and takeactions with respect to plant operations accordingly.

7.6 Functions of Plant Co-ordinator:

PLANT CO-ORDINATOR MM Parmar, CPNM Location: RSM OfficeFirst Successor Bhaskar Sen, SPNMSecond Successor AK Roy , PNM

In charge of all plant operations;

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Takes stock of total plant operation and provides link between theprocess plants and DCR;

Takes instruction from SIC or DCR and implements decision on:

Isolation of plants / facilities /equipments, Throughput regulation (including shutdowns)/ product routings. Strategy for deployment of resources for fire fighting Product storage and Dispatch Operations. Crude Oil receipt.

Arrange monitoring of storm water drains for oil, if any; Ensure draining of flare knockout drums; Mobilize additional manpower required for plant isolation, shutdown,

fire fighting & rescue operation etc; Monitor stock of fire fighting materials and liaise with Material

coordinator; Liaise with engineering Coordinator for maintenance back up; Deploy additional help from external sources; Liaise with Finance Coordinator for Excise & Insurance; Assist the Finance Coordinator in preparing preliminary estimates of

damage to property.

7.7 Function of Fire & Safety Co-ordinator:

FIRE & SAFETY CO-ORDINATOR AK Singh, CM (F&S) Location: Emergency SiteFirst Successor BK Panda , SM (F&S)Second Successor IK Wanjari, SM (F&S)

In-charge of fire fighting and rescue operations inside the refinery.

Assess periodically the resources required viz,

Fire tenders. Fire fighting equipments. Safety and other equipments. Fire fighting/rescue personnel.

Develop strategy for containing the fire in consultation with SiteIncident controller and Plant Coordinator.

Deploy the resources made available for fire fighting/rescue. Be in constant contact with Plant Coordinator through wireless. Ensure water consumption in line with availability and apprise Plant

Coordinator in case of inadequacy supply/pressure/damage to firefighting water network.

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Monitor stock of Fire fighting materials & liase with MaterialCoordinator.

Deploy additional help from external source.7.8Functions of Mechnical Maintenance Co-ordinator

MECHANICAL MAINT.CO-ORDINATOR

SK Chakraborty, DGM (MN) Location: DMC

First Successor SK Das, CMNMSecond Successor Sunil Kanti, CMNM

Report the Disaster Control Room in case of disaster. Meet immediate maintenance (including Civil and Instrument)

requirements, if any, for: Isolations& Hot bolting Provision of diesel to fire tenders at site Critical equipments, particularly in Job-250. Removal of oil spillage/debris. Dewatering of areas flooded. Clearing road blockages. Local diversion of waste water to storm water channel. Fire water line leaks / damages, Fire Vehicles’ urgent repair &

maintenance, (if required). Provide maintenance supervision for firewater pumps. Provide Diesel pumps for hydrocarbon transfers. Arrange for CCTV viewing of emergency site through MAVIX system in

Disaster Control Room. Arrangement for additional Wireless sets through Inst. Maint. as per

requirement. Arrange for replenishment of diesel in the fire fighting appliances

deployed at site whenever Siren for Major Fire / Disaster is blown. Deployment of officers at Assembly Points for Evacuation.

7.9 Functions of Transport/Relief/Welfare Co-ordinator:

TRANSPORT/RELIEF/WELFARE CO-ORDINATOR

PT Solanki, DGM (HR) Location: DMC

First Successor Ms. PiyaliChakraborty,CHRM

Second Successor MVV Sharma, CM (A&W)

Establish Transport Centres at the Time Office and InformationCenters at Time Office / New Administration Building.

Organise transport link between Township & Refinery main gate. Redeployment of all available vehicles and advise coordinators of

vehicles availability. Hire private vehicles for transportation. Co-ordinate with CISF/Police for traffic control & security.

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Arrange ambulances from external sources and liaise with MedicalCoordinator /Engineering Coordinator for conversion of vehicles foruse as ambulances.

Deployment of SHRM as Evacuation Co-ordinator Interact with Coordinators for head count assessment. Arrange placement of drivers & refueling of vehicles. Arrange tea, snacks (Biscuits, Bread, Butter, Fruits etc.), Soft Drinks

for persons at site / Disaster Control room / Maintenance Controlroom at location / Transport Centres, Hospital.

Arrange adequate supply of meals for persons. Arrange materials (sheets, mattresses, food, blankets) for Hospital. Arrange post-mortem/disposal of dead bodies. Communicate with relatives of dead / injured / missing and keep

them advised on latest position. Arrange display of the status at New Administration Building. Update Casualty list and inform the latest position to Dy.

Commissioner of Police, Baroda. Contact DGM (RC) IOC (Mktg Divn.)/Sr. Operations Manager (PPL) for

volunteers. Organize/distribute volunteer force for Hospital and Relief Camps. Organize volunteers from GR & RIL townships for blood donation. Process sanction of emergency relief to the affected and arrange

distribution through District Administration.7.10 Functions of Evacuation Co-ordinator:

EVACUATION CO-ORDINATOR B Das, SM (A&W) Location: Time OfficeFirst Successor CG Surve, M (ER)Second Successor K Manivasagan,

DMER

Arrange for evacuation of employees & contractor workers by deputing Busor other transportation means to the Assembly Points inside refinery andtemporary sheltering at safe zone near time office, Koyali gate & Bitumengate, as per requirement for head count & accounting.

7.11 Functions of Communication & Utility Co-ordinator:

COMMUNICATION & UTILITYCO-ORDINATOR

D Sengupta, DGM (IT) Location: DMC

First Successor M Agarwal, CMNMELSecond Successor Manoj Nanda, CITM

Monitor firewater storage and to maintain adequate flow & pressure infirewater network.

Ensure maximum water supply from head works. Implement cuts for conservation of water.

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Provision of Telephone/Wireless in Disaster Control Room. Provide temporary intercoms at site. Ensure continuous operation of both the FW pump houses in case of

prolonged operation, regulate the flow & pressure of fire water pumpsas required to maintain pressure of 7.0 kg/cm2.

Liaise with Gujarat Electricity Board. Provide emergency lighting in battery area.

7.12 Functions of Medical Co-ordinator:

MEDICAL CO-ORDINATOR Dr. Vipin Sagar, CMO Location: DMCFirst Successor Dr. D Chakraborti, ACMOSecond Successor Dr. DN Nagpure, JCMO

Mobilise G.R. Medical & Para Medical staff. Arrange beds in other Hospitals/Nursing Homes. Arrange / Private Medical Staff

(Surgeons/Physicians/Specialists/Nurses). Liaise with Materials Coordinators for supplies. Arrange transfer of casualties to other hospitals as required. Prepare Shift rota for Medicai/Para-medicai staff. Organise Blood Donation Camp in GR Hospital /First Aid Centre. Arrange blood supplies from external agencies. Liaise with Transport Co-ordinator for getting additional vehicles for

use as ambulances.7.13 Functions of Security / Traffic Co-ordinator:

SECURITY / TRAFFIC CO-ORDINATOR

BS Vashist, Comm. (CISF) Location: DMC

First Successor M Manasseh, Insp. (CISF)Second Successor PK Payasi, Insp. (CISF)

Depute CISF jawans to assist in fire fighting/rescue. Arrange the manning of emergency gate near Bitumen tank truck

despatch & emergency gate near State Bank of India and Koyali Gate. Deploy CISF staff at Char Rasta, Southern Township bypass, Koyali -

Bajwa road junction, Undera crossing near ONGC Gas terminal fortraffic control.

Contact police for assistance in traffic management /law & order. Deploy CISF staff inside refinery to cordon off affected areas/traffic. Arrange movement of vehicles/persons through Bitumen gate/Gate

No. 10 after approval of Site Incident Controller. Organise orderly truck movement outside Gate No. 3, RIL Road -

Bitumen truck parking area and Gate No. 10 (Truck parking area). Arrange police patrolling in public areas to maintain Law & Order. Deploy personnel at Time Office for controlling personnel entering the

refinery.

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Provide manpower for navigation inside refinery at cross roads.

6.2.7.6 Functions of Materials Co-ordinator:

MATERIALS CO-ORDINATOR TK Mondal, GM (M&C) Location: DMC

First Successor AC Makwana, CMTMSecond Successor UK Prasad , CMTM

Emergency procurement of fire fighting and rescueequipment/materials.

Arrange fire-fighting materials (foam, dry chemical powder, hoses, firesuits etc.) from neighbouring industrial units and liaise with Plant co-ordinator.

Emergency procurement of Medical supplies (Purchase/Loan). Liaisewith Medical Coordinator.

Arrange trucks for transport of materials. Arrange manning of stores.

7.14 Functions of Project Co-ordinator:

PROJECT CO-ORDINATOR HS Atha, DGM (PJ) Location: DMCFirst Successor C Mahendra, CPJMSecond Successor BN Bendbar, SPJM (I/c)

Take stock of Refinery situation & at all project sites Decision regarding stopping of work at specific location in

consultation with SIC. Take Head count at all project sites. Arrange for assembly of project personnel at safe location /

Assembly Points Arrange for evacuation of project personnel in co-ordination with

SIC & Transport and Welfare Coordinator. Consult SIC for any assistance with respect to equipment,

materials & skilled manpower. Deployment of officers at Assembly Points for Evacuation

(designated officers from Project Deptt. as Assembly Point In-Charge as per Evacuation Procedure).

7.15 Functions of Finance Co-ordinator:

FINANCE CO-ORDINATOR G Murali, GM (F) Location: DMCFirst Successor VK Jain, DGM (F)Second Successor S Banik, CFM

Arrange manning of Cash section. Release finances with approval of ED/ GM / DGM(TS) to all

coordinators. Inform Insurance Company.

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Disaster Management Plan

at Gujarat Refinery, District Vadodara, Gujarat

Assess damage along with Engineering/Materials & PlantCoordinators for preparing preliminary estimates.

All actions needed to be taken up with the insurance claims of therefinery

To inform Finance at HQ and Corporate Level.

7.16 Functions of Media Co-ordinator:

MEDIA CO-ORDINATOR Ms. Anjali Bhave, SHRM Location: DMCFirst Successor Ms. Philip Ciny Mathew, DM (ER)Second Successor Ms. Dhanashree Patade, O (CC)

To ensure that appropriate local and national governmentauthorities are notified.

Preparation of media statements, obtaining approval from CIC andreleasing such statements once approval received.

7.17 Functions of Marketing Co-ordinator:

MARKETINGCO-ORDINATOR

MG Shaikh , GM (RC) Location: DCR

First Successor GM Parate , CM (RC)Second Successor Samir Saha, SM (RC)

Contacting Disaster Control Room to obtain detail informationabout disaster.

Keep in touch with OMS for instruction about loading operation. Coordinate with Refinery for evacuating personnel from Marketing

office, if required.

7.18 Functions of Pipeline Co-ordinator:

PIPELINES CO-ORDINATOR

Madan Lal, DGM Location: DMC

First Successor AN Kargaokar, COMSecond Successor SD Pande, CMNM

Contacting Disaster Control Room to obtain detail informationabout disaster.

Keep in touch with OMS for instruction about pipelines operation. Coordinate with Refinery for evacuating personnel from Pipelines

office, if required.

8. Maintenance of ERDMP Records(1) There shall be maintenance of ERDMP records for all kind of

emergencies covering near Miss, Level-I, Level-II and Level-III.

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Organisation shall maintain an Incident Record Register for the abovepurpose and post–disaster documentation like resources deployed,relief, rehabilitation measures and lesson learned to avoid re-occurrence of any such emergency. Head of HSE or any otherdesignated personnel by the CIC/SIC shall be responsible formaintenance of such records.

(2) A good public relations program is extremely important in anemergency situation. Inquiries will normally be received from themedia, government agencies, local organizations and the generalpublic.

(3) This section of the Response Plan shall include a public relations ormedia plan. It should identify an Information Officer that is well-equipped and trained in media relations.

(4) Initial releases shall be restricted to statements of facts such as thename of the installation involved, type and quantity of spill, time ofspill, and countermeasure actions being taken. All facts must bestated clearly and consistently to everyone.

Note- Plans shall also be developed to utilize local media and television stations forperiodic announcements during an emergency. This shall also assist in reducingrumours and speculation.

9. Recorder

The Recorder responsibility is to maintain an accurate time record of keyinformation received from the incident or emergency location and torecord the actions initiated by the site incident controller and forimplementing the emergency response actions below:

(a) to record key incident events/actions on incident statusboard/display manually or electronically;

(b) to maintain essential equipment checklist status;

(c) To ensure all status and information is up to date and correctlydisplayed;

(d) To take all necessary recorded material to the alternate ECC roomin the event of emergency in main ECC room; and

(e) To maintain a log book.

10. Communications Services

1) The Communication Co-ordinator shall ensure the following actionsbelow:

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a) Ensuring the ECC equipment and systems are maintained to highstandards and remain functional throughout the emergency.

b) Ensuring a back-up communication system is available in the eventof the ECC Room is not available.

c) Providing quality and diverse communication systems for use inroutine and emergency situations.

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A typical communication flow chart for notification of emergency is asgiven below:

COMMUNICATION FLOW CHART OF ERDMP(GUJARAT REFINERY)

Note: 1. Wherever communication exists for any level of emergency, it automatically implies thatthe communication exists for all higher levels of emergencies.

2) Flow of Information:

a) Emegency Control centre shall receive the information from fieldeither in person or from the various systems available in theinstallation

b) On receipt of information, the control room shift In-charge willactuate the ERDMP and notify the emergency to SIC

c) Control room shift In-charge will act as SIC till arrival of designatedperson

d) SIC or CIC depending upon the level of Emergency will actuate theERDMP and inform the concerned authorities as depicted above inCommunication Chart.

DISASTERMANAGEMENTCENTRE (DMC)

SITE INCIDENTCONTROLLER (SIC)[GM (P&U), DGM (PN)]

CHIEF INCIDENTCONTROLLER (CIC)

TECHNICALADVISOR TO ED

DistrictAdministration

and Centralagencies

CRISISMANAGE

MENTGROUP

FIRE & SAFETYCOORDINATOR

MUTUAL AIDPARTNERS

MEDICALCOORDINAT

OR

MEDIACOORDINATOR,SM (CC)

OFFSITECONTROL

ROOM (OCR) PIPELINE/MARKETING

COORDINATOR,

OTHERS(Required

Coordinators)

FIRSTRESPONDER

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11. SIREN CODES

SIREN for declaring the major emergency:The major emergency will be declared by blowing the siren from FireStation Control Room. The mode of siren is as under:

1) The Emergency siren/s should be located suitably to cover thewhole area with the operational control within the installation. Theseshould be tested at least once in a week to keep them in workingcondition.

2) Emergency siren code should be as follows:

(a) Emergency Level – I: A wailing siren for two minutes.

(b) Emergency Level-II and III: Same type of siren as in case ofLevel – I and II but the same will be sounded for three times atthe interval of one minutes i.e.( wailing siren 2min + gap 1min+ wailing siren 2min + gap 1min + wailing siren 2min) totalduration of Disaster siren to be eight minutes.

(c) ALL CLEAR: Straight run siren for two minutes.

(d) TEST: Straight run siren for two minutes at frequency at leastonce a week

(e) Public address system should be provided with message.

TYPE OF EMERGENCY SIREN CODEAIR RAID PROTECTION Siren for two minutes as per Civil Defence InstructionAll clear siren STRAIGHT RUN SIREN FOR TWO MINUTES.Small Fire NO SIRENMajor Fire Wailing type siren: Wailing type siren for two minutes

Disaster /Evacuation Siren

Same siren as in the case of Major Fire except that itwill be sounded three times with an interval of oneminute in between. (Total 8 minutes)

All Clear Straight run siren for two minutes.Siren testing Straight run siren for two minutes.

The sirens are located at the following locations and these are operableby single switch from Fire Station Control Room.

Location of siren placed is given below:

SR. NO. LOCATION NOS.

1. Shopping Complex 01

2. Community Hall 01

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3. Administrative Building 01

4. CGP-1 01

5. Technical Building 01

6. Old SRU C/R 01

7. North Block C/R 01

8. CETP 01

9. GRE C/R 01

10. TPS 01

11. Dumad Pump House 01

12. Calico 01

13. Second Fire Station 01

14. AU-V Cooling Tower 01

15. Bitumen Filling Station 01

TOTAL 15

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FIRE FIGHTING EQUIPMENT/ FACILITIES

1) The firefighting equipment facilities including emergency communication systems available atFire Station (GR) is shown in Table- 11.1A

11.2 MANPOWER

A) FIRE FIGHTING / RESCUE

It is estimated that a total of 328 men will have to be deployed for fire fighting / rescue workinside Gujarat Refinery. These include the crew of fire tenders of various organizations asdetailed in Table 11.2A As the fire fighting operations are expected to continue for a long time,relieving crew for each of the fire tenders have been considered. The relief crew will be fromCISF, (GR), Civil Defense / Home Guards. At any point of time the crew on a fire tender will bemixed i.e. regular fire fighting personnel and those from CISF / Civil Defense / Home Guards.

Requirement of laborers for the purpose of transfer of foam compound to fire tenders at site hasbeen included.

Fire fighting / rescue operations outside the refinery (viz. Karachiya / Bajwa villages) will beunder the control of District Administration The resources available with Vadodara MunicipalFire Services (VMFS) are adequate to cater to the needs of fire fighting inside (refer Table11.1B) and outside the refinery.

B) EVACUATION / RELIEF CAMPS

Evacuation of the population affected in Karachiya / Bajwa villages/other places outside thebattery area depending upon the emergency and provision of temporary shelter and supplies (inthe relief camps) will be under the overall control of the District Administration. Also evacuation,if necessary, will be done with the help of District Administration. Skeleton presence of GROfficers for the purpose of Co-ordination of relief supplies has been considered

C) MEDICAL

Arrangement for picking up casualties in areas inside as well as outside the refinery and theirtransportation to Medical Centres will be the responsibility of GR. Manpower requirement forthis has been included under Fire Fighting / Rescue.

Medical / Paramedical staff will have to be augmented from Private Sources. Availability of thesame from other hospitals has not been considered as large number of casualties is expected to bemoved to these hospitals.

Postmortem of dead bodies, if any, will be under the exclusive control of District Administration.Provision for manpower for the same has to be made from the existing set up/ HR dep’t.depending upon the situation.

It is assumed that cremation of the dead bodies, if any, will be done at electric crematorium,Baroda.

D) TRAFFIC CONTROL

Traffic control outside the refinery will be initially entrusted to CISF (GR). They will however berelieved by local police within one hour. Inside battery area, traffic movement will be regulatedby CISF (GR).

Details of manpower requirement as well as availability sources is given in Table -11.2A

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Annexure-15

11.3 WATER FOR FIRE FIGHTING

The most important resource (along with manpower) for handling the type of emergencydescribed in previous chapters is 'WATER' for fire fighting. Based on the scenario considered, itis expected that on an average approximately 20 firehydrants / monitors would be in use apartfrom the sprinkler systems. For this kind of deployment, water consumption is estimated atapprox. 5959 M3 / hrconsidering two fire scenarios.

Maximum capacity of four running artesian wells supplying water to the Refinery is6800 m3/hr(36 MGD). The average normal consumption is 1700 m3/Hr. During the emergency it would bepossible to reduce consumption in some areas so that a total of 5000 m3/hr can be made availablefor fire fighting as detailed earlier in Annexure 2.3.1 E.

As detailed, the total storage capacity of firewater tanks in the refinery is about 29700 m3.Therefore, if the consumption rate is 5959 m3/hr (as above), this rate can be maintained forapprox. 4 hrs. Thereafter also, water available for fire fighting will be sustained at 5000 M3/hr asgiven in Annexure-11.1E

11.4 FACILITIES FOR MEDICAL TREATMENT

A fully equipped 24 bed hospital is available in GR Township (less than 3 Km from disaster site.)The indoor treatment facilities can be stretched to 60 bed by converting the hospital conferenceroom / veranda into medical wards. Details of facilities at GR Hospital are given in Table -11.4A

Facilities for treating 75 indoor patients can be created quickly. All casualties from inside as wellas outside the refinery will be brought first to GR Hospital. After registration, they will beexamined and those requiring indoor treatment will be transported to GR Hospital / transported toother hospitals in Vadodara.

Lists of hospitals in Vadodara City, blood banks, day and night chemists, suppliers of hospitalequipments and hospitals having ambulance services are given in Table- 11.4B

Location of GR Hospital is shown on Refinery Township Layout Plan annexed with attachment.

11.5 TRANSPORT VEHICLES

Details of transport vehicles requirement / availability & deployment are given in Table 11.5 A&B.

11.6INFORMATION CENTRESFor the purpose of supply of official information to the population in GR Township in generaland the GR employees in particular about the nature of disaster, the INFORMATION CENTRESwill be created at locations given below:

A) REFINERY INFORMATION CENTRE :

At Time Office - Telephone No: 8132/7132

B) TOWNSHIP INFORMATION CENTRE:

At New Administration Building

Each of the information centres will be manned by a staff of 3, from P & A Deptt.

Each center will have display facilities for displaying important notices, instructions, shift Rota,casualty lists.

Regular transport service between the two information centers will be started at the earliest. Theofficers & staff will use this. Use of personal vehicles by the officers/staff will be discouraged toreduce congestion on the roads so as to allow free movement of fire tenders/relief vehicles.

Page 145 of 244

Requirement of additional staff/officers from the township will be channelised through thetownship information center, who will arrange to convey the messages to the employees at theirresidences.

11.7 COMMUNICATION

A disaster is the tragedy of a natural or human-made hazard (a hazard is a situation which poses a level ofthreat to life, health, property, or environment) that negatively affects society or environment. Emergencymanagement is the continuous process by which all individuals, groups, and communities manage hazardsin an effort to avoid or ameliorate the impact of disasters resulting from the hazards. Effectivecommunication is one of the first and foremost steps in disaster management. Following is the variouscommunication systems prevailing in the refinery.

Since a petroleum industry like IOCL handles a large variety of hazardous chemicals, there is always

potential danger which may lead to disaster. Thus, communication is of utmost importance in disaster

management. Details of the communication system are furnished below:

Type Description

PA Systems It is a centralized amplifier based system that has been designed to provide voicepaging and to broadcast alarm tone during emergencies.

The system can transmit alarm tone and routine voice messages, from a centrallocation, to all or selected areas of the facility, in a reliable and safe manner, by theuse of loudspeakers.

RadioCommunication

(Walkie-Talkie)

Rechargeable battery backed system working in the VHF (136-170 MHz) with aradius of ~1.5 km & enables communication with 16 channels, OR UHF (850MHz) with a radius of 35 km & ability to communicate with unlimited no. ofchannels.

Plant CommunicationSystems(PCS)

Microprocessor controlled S/W programmable, central exchange based “pagingsystem with talk back facility”.The system comprises of page channel and partychannels for two-way communication facility between the control room and thefield.

Page Channel provides loud speaking facility and is used for broadcastingmessages or issue instructions or to locate field operators in the plant. Theannouncements made by the users are heard over the field loudspeakers.

Dependence on UPS can be done away with Portable PA systems, consisting of a master S/W controller,battery backed placed in the control room which can communicate with field stations (also battery backed).

As most of the communication systems depend on UPS for power supply, a redundant UPS systemincreases the availability and reliability of the said communication system.

Page 146 of 244

A) SIRENS : (15 Nos.)

Location of siren placed is given below:

SR. NO. LOCATION NOS.1. Shopping Complex 012. Community Hall 013. Administrative Building 014. CGP-1 015. Technical Building 016. Old SRU C/R 017. North Block C/R 018. CETP 019. GRE C/R 0110. TPS 0111. Dumad Pump House 0112. Calico 0113. Second Fire Station 0114. AU-V Cooling Tower 0115. Bitumen Filling Station 01

TOTAL 15

All sirens are controlled from Fire Station Control Room.

Emergency siren code is as follows:

a) Emergency level-I: A wailing siren for two minutes

b) Emergency level-II& III: Same type of siren as in case of Level-I & Level-II but the samewill be sounded for three times at the interval of one minutes i.e.( wailing siren two minutes +gap one minute + wailing siren two minutes +gap one minute + wailing siren two minutes)Total duration of disaster siren to be eight minutes.

c) All clear : Straight run siren for two minutes

d) Test: Straight run siren for two minutes at frequency at least once a week.

B) FIRE ALARMS

At GR – 99, At GHC – 101,AU-5/DHDS/LAB/ MSQ-115, RUP Block-119Total: 434 Nos.

C) HOT LINESInternal : Between Main Fire Station & LPG Plant.

: Main Fire Station & Water Block Control Room.

: Main Fire Station & Second Fire Station.

: Main Fire Station & CISF Main Gate

External : Main Fire Station & GSFC

: Main Fire Station & HWP

: Main Fire Station & RIL

: Main Fire Station & Civil Defence Control room.

: Main Fire Station & GPL (Gujarat Petro Synthetic Ltd)

Page 147 of 244

D) WIRELESS

Fire Station Control Rooms -One (Base Set) at Main Fire Station

-One (Base Set) at Second Fire Station

-One ( Base Set) at Disaster C/R

E) TELEPHONES

Fire Calls -7333 / 6333

General -7490 / 7616 DOT-2372445

ARP System* -Linked with Auto telephones of Key personnel.

* On activation of ARP (Air Raid Precaution) warning System, all phones connected to this will

automatically.

It is first major form of communication, any failure in the plant UPS system will cause the

system to collapse.

11.8 SAFETY EQUIPMENT Nos.

Compressed Air breathing

Apparatus (BA)-40 Minutes duration 50

Blow Man BA Set 05

Safety Hand Lamps 100

Hand Gloves of Various Types 500

Gum Boots 100

Rain Coats 100

Helmets 400

On line BA Sets 07

Fire Entry Suits 06

Air Tight Suits 02

Page 148 of 244

TABLE 11.1 A

11.1 FIRE FIGHTING EQUIPMENTS / FACILITIES AVAILABLE

AT GUJARAT REFINERY

A) FIRE TENDERS

Sl .No.

FireTenderNo.

Type of FireTender

Capacity

Foam Tank

(Lt)

Water Tank

(Lt)

Pump

( LPM )

1 . FT- 1 Foam Tender 6000 4000 8000 at

10 Kg/ Cm2

2. FT- 2 Foam Nurser 12000 - 500

3. FT- 3 DCP Tender 3000 Kg (DCP) - -

4 FT 4 Foam Tender 6000 4000 8000 at

10 Kg/ Cm2

5 FT- 5 Foam Tender 6000 4000 8000 at

10 Kg/ Cm2

6 . FT- 6 Foam Tender 6000 4000 8000 at10 Kg/ Cm2

7. FT- 7 Foam Nurser 8000 - 500

8 FT- 8 Foam Tender 6000 4000 8000 at10 Kg/ Cm2

9 . FT- 9 Emergency Rescue Tender, Carries Emergency Lighting & Rescue

Equipments

10. FT- 10&11

Multi Purpose Fire Tender : Each with 5000 Ltr Foam Tank, 1000 Ltr Water Tank,1000 Kg DCP Vessel , 8000 LPM Pumps with mounted diesel engines, 2000 & 1000GPM Hydro-Chem Monitors

11 FT- 11 Multi Purpose Fire Tender : Each with 5000 Ltr Foam Tank, 1000 Ltr Water Tank,1000 Kg DCP Vessel , 8000 LPM Pumps with mounted diesel engines, 2000 & 1000GPM Hydro-Chem Monitors

12 FT 12 Hydraulic Fire Tender. Elevation upto 50 m height.

Page 149 of 244

B) FIRE JEEPS : 1 NUMBER

C) FIRE HOSES :

1 Hose Pipe - 2.5" dia. Type - I: 300 Nos each of 15.0 Meter Length

2 Hose Pipe - 2.5" dia. Type - II: 500 Nos each of 22.5 Meter Length

3 Hose Pipe - 4.0" dia 50 Nos each of 15.0 Meter Length

D) FIRE EXTINGUISHERS (Distributed all over battery area):

Dry Chemical Powder (DCP)

- 75 kg : 119Nos

- 25 kg : 555Nos

- 10 kg : 4110Nos

- 5 kg : 170Nos

Carbon Dioxide

- 4.5 kg : 642 Nos

- 6.8 kg : 155Nos

- 9.0 kg : 30Nos

- 22.5 kg : 08Nos

Clean Agent Extinguishers:

- 2.0 Kg. : 97 nos.

E) FIRE HYDRANTS : 1709 Nos

F) FIXED WATER MONITORS : 822 Nos + 54 HVLR -Remote

operated &181 HVLR- Maunaloperated)

G) Foam Connection Chambers (Storage Tanks): 214

(Fixed Roof + Foam Pourer Floating Roof Tank + Foam Flooding System in 6th Gantry)

H) FIRE SUITS

Entry Suits : 06 Nos

Proximity Suits : 10 Nos

Page 150 of 244

I) DRY CHEMICAL POWDER STOCK : 5200 Kg. (Potasium Bi-carbonate

Type ) for extinguishers

4500 kg(ABC Type) for FT-3 (DCP

Tender)

J) FOAM COMPOUND STOCK

- In Vehicles / Trailer : 40,000 Lit.

- In Stores of Fire Station : 143, 000 Lit

Total : 183,000 Litres #

- Water Jel Blankets : 30 Nos.

# Apart from this, 40000 liters of AFFF will be available under Mutual Aid Scheme

K) FIRE WATER STORAGE CAPACITY (M3)

Sl No. Tank No. No. Capacity Total Capacity, M31 T-101A/B 2 6000 12000

2 T-5/6 2 3600 7200

3 26-TC-A/B 2 3100 6200

4 26-TC-C 1 4500 4500

Total 29,900

L) FIRE WATER PUMPS:

A) DETAIL OF FIRE WATER PUMPS AT JOB 250 NEW PUMP HOUSE.

MAIN PUMPSSR. N0. PUMP NO. DRIVE CAPACITY HEAD1 250-P-02A ELECTRIC 1000 M3/hr 102 M2 250-P-02B ELECTRIC 1000 M3/hr 102 M3 250-P-03A DIESEL 1000 M3/hr 102 M4 250-P-03B DIESEL 1000 M3/hr 102 M5 250- P-03C --DO-- 1000 M3/hr 102 M6 250- P-03D --DO-- 1000 M3/hr 102 MJOCKEY PUMPS7 250—P 01A ELECTRIC 350 M3/hr 105 M8 250—P 01B ELECTRIC 350 M3/hr 105 M

B) DETAIL OF FIRE WATER PUMPS AT GHC PUMP HOUSE.

MAIN PUMPSSR.NO.

PUMP NO. DRIVE FLOW HEAD

1 26-PA-002A ELECT. 1000 M3/hr 102 M

Page 151 of 244

2 26-PA-002B ELECT. 1000 M3/hr 102 M

3 26-PA-003A DIESEL 1000 M3/hr 102 M

4 26-PA-003B DIESEL 1000 M3/hr 102 M

JOCKEY PUMPS

5 26-PA-01A ELECT. 350 M3/hr 70 M

6 26-PA-01B ELECT. 350 M3/hr 70 M

Page 152 of 244

Page 153 of 244

Consultancy

Typewritten text

Annexure-16

GR

EE

N B

EL

T -

2

GREEN BELT - 1

GR

EE

N B

EL

T-3

Total Plant Area - 925 Acres

Total Green Belt Area - 148.17 Acres

% Of Green Belt - 16%

Page 154 of 244

Consultancy

Typewritten text

Consultancy

Typewritten text

Annexure-17

Annexure – 18

Raw data of AAQ Monitoring for 12 weeks at 8 location

Page 155 of 244

Consultancy

Typewritten text

Annexure-18

Location: IOCL station (AAQ 1)

S.No Pollutant Units Min. Max. Average 98th CPCB No of Percentile Standard Observation Ind./Res./ Rural & Other

1 PM10 µg/m³ 24 77.89 87 82.96 87 100 2 PM2.5 µg/m³ 24 35.4 48.9 41.06 48.5 60 3 SOx µg/m³ 24 26 34.6 30.1 33.9 80 4 NOx µg/m³ 24 26.5 34.85 31.55 34.5 80 5 CO µg/m³ 24 0.31 0.48 0.40 0.5 400

6 Arsenic ng/m³ 24 BDL BDL BDL BDL 6.0

7 Nickel ng/m³ 24 BDL BDL BDL BDL 20

8 Ozone µg/m³ 24 26.5 36.5 31.5 36.5 100

9 Lead µg/m³ 24 BDL BDL BDL BDL 1.0

10 Ammonia µg/m³ 24 BDL BDL BDL BDL 400 11 Benz-ene µg/m³ 24 BDL BDL BDL BDL 5.0 12 Benzo (a) pyrene ng/m³ 24 BDL BDL BDL BDL 1.0 13 VOC µg/m³ 24 1.8 3.1 2.3 3.0 --

14 Total Hydrocarbon ppm 24 804.31 805.01 804.75 805 --

15 Methane Hydrocarbon ppm 24 1.8 2.4 2.1 2.3 --

16 Non Methane Hydrocarbon ppm 24 BDL BDL BDL BDL --

17 Vanadium Ng/m³ 24 BDL BDL BDL BDL -

Location : Anagad (AAQ 2)

S.No Pollutant Units Min. Max. Average 98th CPCB

No of Percentile Standard Observation Ind./Res./ Rural & Other

1

PM10 µg/m³ 24 58.69 70.5 63.97 70 100 2 PM2.5 µg/m³ 24

19.8 31.02 25.76 30.7 60 3

SOx µg/m³ 24 10.23 16.53 13.89 16.3 80 4

NOx µg/m³ 24 18.98 27.56 23.76 27.4 80 5 CO µg/m³ 24 0.02 0.12 0.08 0.1 400 6 Arsenic ng/m³ 24 BDL BDL BDL BDL 6.0 7 Nickel ng/m³ 24 BDL BDL BDL BDL 20 8 Ozone µg/m³ 24 18.5 30.2 24.1 29.8 100 9 Lead µg/m³ 24 BDL BDL BDL BDL 1.0 10 Ammonia µg/m³ 24 BDL BDL BDL BDL 400 11 Benz-ene µg/m³ 24 BDL BDL BDL BDL 5.0 12 Benzo (a) pyrene ng/m³ 24 BDL BDL BDL BDL 1.0 13 VOC µg/m³ 24 1.03 2.4 1.78 2.4 - 14 Total Hydrocarbon Ppppppm 24 BDL BDL BDL BDL - 15 Methane Hydrocarbon ppm 24 1.5 2.16 1.8 2.1 - 16 Non Methane Hydrocarbon ppm 24 BDL BDL BDL BDL - 17 Vanadium Ng/m³ 24 BDL BDL BDL BDL - Page 156 of 244

Location : Ganpatpura (AAQ 3)

S.No Pollutant Units Min. Max. Average 98th CPCB No of Percentile Standard Observation Ind./Res./ Rural & Other

1 PM10 µg/m³ 24 57.23 68.02 61.55 66.9 100 2 PM2.5 µg/m³ 24 20.7 30.2 25.61 30 60 3 SOx µg/m³ 24 11.2 16.8 13.63 16.7 80 4 NOx µg/m³ 24 19.95 26.9 24.32 26.8 80 5 CO µg/m³ 24 0.02 0.1 0.05 0.1 400

6 Arsenic ng/m³ 24 BDL BDL BDL BDL 6.0

7 Nickel ng/m³ 24 BDL BDL BDL BDL 20

8 Ozone µg/m³ 24

10.1 29.6 18.4 29.1 100


10 Ammonia µg/m³ 24

BDL BDL BDL BDL 400

11 Benz-ene µg/m³ 24 BDL BDL BDL BDL 5.0

12 Benzo (a) pyrene ng/m³ 24 BDL BDL BDL BDL 1.0

13 VOC µg/m³ 24 1.26 1.92 1.65 1.7 - 14 Total Hydrocarbon ppm 24 BDL BDL BDL BDL -

15 Methane Hydrocarbon ppm 24 0.85 1.2 1.1 1.2 -

16 Non Methane Hydrocarbon ppm 24 BDL BDL BDL BDL -


Location : Madinapark (AAQ4)

S.No Pollutant Units Min. Max Average 98th CPCB No of Percentile Standard Observation Ind./Res./ Rural & Other

1

PM10 µg/m³ 24 50.8 65 58.07 64.2 100

2

PM2.5 µg/m³ 24 18.14 31.2 24.86 31.1 60 3 SOx µg/m³ 24

10.52 14.63 13.04 14.4 80 4 NOx µg/m³ 24

20.45 24.60 22.52 24.20 80 5 CO µg/m³ 24 0.01 0.1 0.06 0.1 400 6 Arsenic ng/m³ 24 BDL BDL BDL BDL 6.0 7 Nickel ng/m³ 24 BDL BDL BDL BDL 20 8 Ozone µg/m³ 24 10.8 16.3 13.3 16.1 100 9 Lead µg/m³ 24 BDL BDL BDL BDL 1.0 10 Ammonia µg/m³ 24 BDL BDL BDL BDL 400 11 Benz-ene µg/m³ 24 BDL BDL BDL BDL 5.0 12 Benzo (a) pyrene ng/m³ 24 BDL BDL BDL BDL 1.0 13 VOC µg/m³ 24 1.2 1.45 1.34 1.4 - 14 Total Hydrocarbon ppm 24 BDL BDL BDL BDL - 15 Methane Hydrocarbon ppm 24 0.6 1.09 0.8 1.1 - 16 Non Methane Hydrocarbon ppm 24 BDL BDL BDL BDL - 17 Vanadium Ng/m³ 24 BDL BDL BDL BDL - Page 157 of 244

Location : Mahapura (AAQ5)


1 PM10 µg/m³ 24 56.32 72.56 63.8 71.9 100

2 PM2.5 µg/m³ 24 20.47 31.5 25.93 31.5 60 3 SOx µg/m³ 24 12.3 15.6 14.05 15.5 80 4 NOx µg/m³ 24 18.56 27.65 23.87 27.3 80 5 CO µg/m³ 24 0.01 0.08 0.04 0.1 400

6 Arsenic ng/m³ 24 BDL BDL BDL BDL

6.0

7 Nickel ng/m³ 24 BDL BDL BDL BDL

20

8 Ozone µg/m³ 24 9.12 12.4 10.5 12

100

9 Lead µg/m³ 24 BDL BDL BDL BDL

1.0

10 Ammonia µg/m³ 24 BDL BDL BDL BDL 400

Location : Royaka (AAQ6)


1 PM10 µg/m³ 24 50.8 68.9 59.17 68.2 100

2 PM2.5 µg/m³ 24 18.23 30.4 23.62 30.3

60 3 SOx µg/m³ 24 10.8 15.7 12.93 15.2 80

4 NOx µg/m³ 24 18.5 27.89 23.01 27.5 80 5 CO µg/m³ 24 0.02 0.1 0.06 0.1

400 6 Arsenic ng/m³ 24

BDL BDL BDL BDL 6.0

7 Nickel ng/m³ 24

BDL BDL BDL BDL 20

8 Ozone µg/m³ 24

9.36 14.5 11.2 14 100


11 Benz-ene µg/m³ 24 BDL BDL BDL BDL

5.0


13 VOC µg/m³ 24 1.76 2.5 2.05 2.5 -

14 Total Hydrocarbon ppm 24 BDL BDL BDL BDL -

15 Methane Hydrocarbon

ppm 24 1.78 2.1 2 2.1 -

16 Non Methane Hydrocarbon

ppm 24 BDL BDL BDL BDL -


Page 158 of 244

10

BDL BDL BDL BDL 400

11 Benz-ene µg/m³ 24

BDL BDL BDL BDL 5.0


13 VOC µg/m³ 24 0.89 1.23 1.14 1.2 -



ppm 24 1.28 1.6 1.4 1.6 -




Location : Asarma (AAQ7)

S.No Pollutant Units Min. Max Average 98th CPCB

No of Percentile Standard Observation Ind./Res./ Rural & Other

1 PM10 µg/m³ 24 50.98 64.8 58.22 64.7 100

2 PM2.5 µg/m³ 24 18.23 31.8 24.75 31.5 60 3 SOx µg/m³ 24 11.02 15.62 13.20 15.3 80 4 NOx µg/m³ 24 18.75 27.69 23.71 27.5 80 5 CO µg/m³ 24 0.02 0.1 0.05 0.1 400

6 Arsenic ng/m³ 24

BDL BDL BDL BDL 6.0

7 Nickel ng/m³ 24

BDL BDL BDL BDL 20

8 Ozone µg/m³ 24

10.23 16.2 13.1 16.2 100

9 Lead µg/m³ 24

BDL BDL BDL BDL 1.0

10 Ammonia µg/m³ 24

BDL BDL BDL BDL 400


BDL BDL BDL BDL 5.0


13 VOC µg/m³ 24 1.33 1.53 1.42 1.5 -



ppm 24 1.35 1.61 1.5 1.6 -



17 Vanadium Ng/m³ 24 BDL BDL BDL BDL - Location : Sokhda (AAQ8)


1

PM10 µg/m³ 24 52 66.12 60.01 65.6 100 2

PM2.5 µg/m³ 24 19.6 30.14 25.93 30.1 60 3

SOx µg/m³ 24 9.9 15.2 12.71 15 80 4 NOx

µg/m³ 24 18.36 27.36 23.32 27.2 80 5 CO µg/m³ 24 0.03 0.1 0.07 0.1 400 6 Arsenic ng/m³ 24 BDL BDL BDL BDL 6.0 7 Nickel ng/m³ 24 BDL BDL BDL BDL 20 8 Ozone µg/m³ 24 9.5 15.96 12.7 15.8 100 9 Lead µg/m³ 24 BDL BDL BDL BDL 1.0 10 Ammonia µg/m³ 24 BDL BDL BDL BDL 400 Page 159 of 244


BDL BDL BDL BDL 5.0

12 Benzo (a) pyrene ng/m³ 24

BDL BDL BDL BDL 1.0

13 VOC µg/m³ 24 0.85 1.28 1.08 1.3 -



ppm 24 1.09 1.32 1.2 1.3 -




Page 160 of 244

Development Report 2014-15

ENCON and APC

ENCON INITIATIVES

1. DEVELOPMENT OF INTEGRATED FLARE MANAGEMENT SYSTEM

(IFMS)

Common reason for flaring

Imbalance in fuel gas system

Process requirement where column overheads are operated at very low pressure( about 1Kg/cm2 )

Dumping from Hydrogen header.

Process abnormalities leading to flare

Process Equipment Abnormalities

Complexity involved in FG system at Gujarat Refinery

28 generation points

45 consumption points

2 disturbance in 73 parameters have lead to

2628 combinations of disturbance can occur

PRAGMATIC APPROACH TO FLARE MONITORING

3-1

Page 161 of 244

Consultancy

Typewritten text

Annexure-19


KPI-1: REDUCTION IN FUEL GAS TO FLARE

KPI-2: REDUCTION IN MAKE UP GAS

#1 (A) GJ A.2115FI2902.PV+GJ A10/20/2013 18:20:01 2600.20 (Av g @1 D ay ) N o D es c r iption D efined**

10000.00

0.00

10/16/2013 11:08:28 10/8/2014 11:08:28

New Plot Title @ 357d0h0m0s

#1 (A) GJ A.2115FI2902.PV+GJ A10/22/2014 23:24:28 1023.34 (Av g @1 D ay ) N o D es c r iption D efined**

10000.00

0.00

10/8/2014 11:08:28 1/10/2015 11:08:28

New Plot Title @ 94d0h0m0s

Before After

3-5

Page 162 of 244


FG SINK AVAILABILITY

SUGGESTION BY IFMS (AS AN EXAMPLE)

UNIT TAG DESCRIPTION UNITS VALUEcurrent value

KG/HR Maximum MinimumMargin

for decrease

TPS gja.51fi__1409.pv FG TO BOILER 4TONNE/H

R 2.062813 2.062813 2063 2269 500 1563


R -0.13184 0 0 0 500 0


R 0.37168 0.37168 372 409 500 0


R -0.13184 0 0 0 500 0

CGP-II GJA.4FG_FLOW.OUT FGTO HRSG-4 M3/HR 2371.216 2371.216 2646 2500 1400 1246

CGP-II GJA.5FG_FLOW.OUT FGTO HRSG-5 M3/HR 2040.489 2040.489 2277 2500 1000 1277

HCU GJA.6FI1501.PVFG SUPPLY HDR

FLOW KNM3/HR 4.389976 4.389976 4900 4780 3860 1040

DCU GJA.2095FI05750.PV 4132.809 4132.809 4133 5200 4000 133

DCU GJA.2095FI06207.PV KG/HR 3845.328 3845.328 3845 5200 3800 45

AU1 GJA.1FI2002.PV FG TO AU1 NM3/HR 1980.891 1980.891 2211 4800 1800 411

AU5 GJA.5FI1417.PV F1 FG FLOW KG/HR 1899.838 1899.838 1900 2500 1000 900

AU2 GJA.2FI2905.PV GJA.2FI2905.PV NM3/HR 1482.108 1482.108 1654 2500 1500 154

LAB

GJA.2063FT1205.PV

FG to LAB Hot Oil

Heater(2063-F-001) KG/HR 1517.357 1517.357 1517 2200 1500 17

UNIT TAG DESCRIPTION

FG to be decreased in

kg/hr

FG to be increased in

kg/hr

TPS gja.51fi__1409.pv FG TO BOILER 4 293 0




CGP-II GJA.4FG_FLOW.OUT FGTO HRSG-4 247 0

CGP-II GJA.5FG_FLOW.OUT FGTO HRSG-5 306 0

HCU GJA.6FI1501.PV FG SUPPLY HDR FLOW 164 0

DCU GJA.2095FI05750.PV 0 0

DCU GJA.2095FI06207.PV 0 0

AU1 GJA.1FI2002.PV FG TO AU1 0 0

AU5 GJA.5FI1417.PV F1 FG FLOW 294 0

AU2 GJA.2FI2905.PV GJA.2FI2905.PV 0 0

LABGJA.2063FT1205.PV

FG to LAB Hot Oil Heater(2063-F-001) 0 0

3-4

Page 163 of 244


NEED OF STRATEGY TO CONTROL GAS MAKE UP

Gas generation is in the range of 46000Kg/hr.

Make up gas is varying between -3000 and 3000kg/hr typically

Hence the variation is only typically 6%

If adjustment of FO burners done in too many areas , this may lead to either

more gas make up or more flaring

COKER GAS…..MAIN DRIVING FORCE FOR GAS MAKE UP

#1 (R ) GJ A.2095FI11401.PV 1/11/2015 15:47:09 18613.77 KG/H R (R aw ) FU EL GAS FR OM FU EL GAS PR OD U C T K.O. D R M, V-26**

20000.00

14000.00

1/11/2015 08:48:46 1/12/2015 08:48:46

Flaring points of refinery @ 1d0h0m0s

1 day 1 week 1 month

Mean 17400 15973 16130

Standard deviation 625 1341 1325

minimum 14592 10772 10772

maximum 19302 20695 25629

3-3

Page 164 of 244


A TYPICAL MONITORING TABLE

Attribute \flare source Point A

Point B Point C

Control valve size in inch(D) 1 10 6

% Opening 30 7 60 Upstream pressure in kg/cm2 g (P) 0.5 2 30

Split range No No Yes (>50% flaring) Dead band applied No NO Yes (+/- 5%) Actual control valve opening(%op) 30 7 10 (including dead band ((60-

55)*2) P*D3/100 0.3 140 648

IFMS AS A CONTROLLING AID

28 generation points

45 consumption points

1 make up point

13 Identified major consumption points

CV MV DV

1 13 73

MONITORING THROUGH IFMS SHEET

10 seconds away from problematic area

3-2

Page 165 of 244

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CHAPTER – 1

1.0 INTRODUCTION Gujarat Refinery of Indian Oil Corporation Limited has a capacity to refine 12.75 million Mts. per annum of Crude Oil. Four types of Crude Oil viz. Bombay high, Pursian Gulf, North Gujarat & South Gujarat are processed. The Oil Movement & Storage (OM&S) is a part of Production Department which is headed by Chief Production Manager. OM&S is supported by Senior Production Manager. The offsite facilities play an important role in maintaining the smooth and continuous operation of the refinery. OM&S is mainly responsible for activities in offsite area. The Objectives and functions of OM&S are as follows: -

1.1 OBJECTIVES 01. To receive crude oil and uninterrupted supply to processing units after proper

accounting and tank operations, in environment friendly manner, keeping internal customer’s satisfaction.

02. To receive intermediates and finished product streams ex units to prepare quality product in a safe & environment friendly manner.

03. Timely supplying the quality products to Marketing as per planning and schedule to meet the market demand.

04. To meet the statutory requirements of Central Excise & Customs w.r.t. Crude & Petroleum Products storage and movement.

05. To maintain safe and pollution free environment. To strive for internal and external customer satisfaction.

06. To conserve energy by controlling losses. 07. To ensure safety of personnel & equipments by adopting safe practices. 08. To continuously upgrade and assess the knowledge and skills of operating

personnel.

1.2 FUNCTIONS 1. Receipt, storage, accounting, sampling of crude oil. 2. Crude & LABFS tank preparation and uninterrupted feeding to processing units.

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3. Receipt, storage, accounting of finished products and intermediates ex. Units and

blending of intermediates and blending of MS at blending station to make HIGH QUALITY as EIV MS finished products with minimum quality give away and to delight customer and to protect environment..

4. Supply of intermediates (feed) to processing units. 5. Preparation of finished products tanks for dispatch. Sampling for Quality

Certificate and accounting. 6. Product dispatch by pipeline, T/W & TTL. 7. Excise & Customs formalities and co-ordination with central excise & custom officials

for carrying out day to day operations.

8. Unloading the rail wagons declared either sick by railway or contaminated by Marketing.

9. Unloading of Truck of different chemicals. e.g Benzene. 10. Slop recovery and reprocessing to units.

11. Preparation of Tank for cleaning, inspection, repair & maintenance.

12. Co-ordination with Technical Services & Marketing for planning and supply of

finished products.

13. Co-ordination with Railway and Marketing for availability and placement of rail wagons as per planning schedule.

14. Co-ordination with service departments (Maintenance /inspection/ Technical

services) for maintaining good house keeping and health of equipment, gantry area, and facilities, safe and in healthy condition for operation.

The Oil Movement & Storage Division consists of various sections like a) Receipt and Blending

b) Tank Wagon Handling

c) Tank Truck Loading

d) LPG

e) Bitumen

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Gujarat Refinery has following units: - PRIMARY UNITS a) Atmospheric Distillation Unit-I (AU-I)

b) Atmospheric Distillation Unit-II (AU-II)

c) Atmospheric Distillation Unit-III (AU-III)

d) Atmospheric Distillation Unit-IV(AU-IV)

e) Atmospheric Distillation Unit-V (AU-V)

SECONDARY UNITS

Catalytic Reforming Unit (CRU)

Udex

Merox

Visbreaker Unit (VBU)

Vacuum Distillation Unit (VDU)

Bitumen Blowing Unit

Feed Preparation Unit-I

Fluid Catalytic Cracking Unit

Food Grade Hexane Plant

MTBE

DHDS

LAB PLANT

MSQ

Plant commissioned uder RUP.

DHDT

ISOM

VGO-HDT

SRU-III

DCU

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LPG MEROX

ATF MEROX

The intermediate products are as follows:

a) Reformate for motor sprit blend b) Feed stock for Udex c) C5-70 naphtha cut. For blending station d) 90-140 naphtha cut for blending station e) Light Gas Oil (LGO) f) Heavy Gas Oil (HGO) g) Reduced Crude Oil (RCO) h) Light Vacuum Gas Oil (LVGO) i) Heavy Vacuum Gas Oil (HVGO) j) Vacuum Residue (VR) k) Visbreaker Gasoline l) Visbreaker Gas Oil m) Visbreaker Tar n) VB Naphtha o) ISOMARATE p) REORMATE

Various feeds to units for which offsite are required to receive, prepare and supply are as follows: Crude Oil to AU-I, AU-II, AU-III, AU-IV and AU-V The different types of crude oils received and processed are as follows: South Gujarat crude North Gujarat crude Bombay High crude Low sulfur crude High sulfur crude The modes of dispatches of finished products are as follows a) BY ROAD :- In Tank Truck Lorries, specially designed containers for bulk LPG, packed LPG and Bitumen in trucks.

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a) BY RAIL :- In Tank Wagon, packed LPG and Bitumen in Railway wagons. c) BY PIPELINES: - To Sabarmati IOC installation near Ahmadabad, to GSFC, to IPCL, to HPCL and BPCL installation at Nandesari, BPCL (OMC), and to GIPCL. The last four are next door to Gujarat Refinery. LSBFS to NIRMA, HSD/MS to IOTL (Dumad) HSD, MS, SK to KNPL, KVSSPL and KDPL & KRPL.

Waste Water from process area, Oily water and Oil spillages from loading areas, pump slabs and tank farms is brought through different collection pipe net-work to the GR/GRE effluent sump where oil is removed by Roto pump and is pumped to slop tanks 201 to 202. These slop tanks are under OM&S. The responsibilities of OM&S include receipt, preparation and feed of slops for reprocessing to GRE slop tanks. Scheme has been prepared for directly feeding this slop to crude units via GRE unit slop transfer pumps.

CHAPTER - 3

CRUDE OIL HANDLING

3.1 G E N E R A L Gujarat Refinery receives crude oil through three different pipelines, from different sources, directly into the crude oil tanks in the refinery. a) A 98-km long pipeline brings South Gujarat Crude oil from fields in Ankleshwar,

Gandhar, Nada etc. which is situated south of Gujarat Refinery.

b) A 135-km long pipeline brings North Gujarat crude oil from oil fields in the Cambay, Mehasana, Kalol, Navagam etc. region which is situated North of Gujarat Refinery.

c) A 416-km long Salaya-Viramgam-Koyali pipeline brings crude oil unloaded from oil tankers at Salaya -

The section between Salaya and Viramgam of pipeline is 275 km having 28” pipe dia and section between Viramgam and Koyali pipeline is 141 km having 18” pipe dia.

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Crude oil from Bombay High and crude oil imported from various sources comes through this pipeline in batches per the planning for procession.

Chapter- 1

1.0 DISPATCHES BY RAIL ( TANK WAGON GANTRY)

The bulk of the product dispatches from this refinery move by rail. For this reason elaborate facilities have been provided for this mode of dispatch.

The following products move by rail:

1) Naphtha 2) Motor Spirit 3) A.T.F 4) Kerosene 5) Diesel (Army, NAVY-LSHF, HSD EURO-III & EURO -IV ) 6) Light Diesel Oil 7) Furnace Oil, HVFO (GNFC grade) 8) Reformate

1.1 Product Distribution on Rail Gantries Naphtha

Naphtha can be loaded on gantry no.3, 5 & 6. The rakes of Naphtha wagons come in one hook. These rakes are placed from southern end by Railways. After loading the rake, it is released from northern end to Railway yard.

Benzene, Toluene, MTO

The facility is provided to load these products on sick T/W unloading gantry. T/Ws for these products are segregated from white oil gantry and then placed on loading points on sick T/W unloading gantry. There are three loading points on gantry Benzene and Toluene T/Ws are flushed with SK prior to bringing on sick T/W unloading for loading. This facility is not being used as loading of these products not done.

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LSHS Production stopped and Railway also not providing/ stopped to supply 4 wheeler wagons, so Gantry No. 4 (RCO) not in use. (Gantry no. 2 Converted for BTPN Wagons and HVFO loaded in this Gantry).

ATF ATF loading points are available on gantry number 5. ATF has independent loading points and they are not clubbed with any other product.

MS, Kero, HSD These products can be loaded on 3, 5, 6 gantries MS can be loaded thro’ a independent loading point, Whereas for SK/HSD there is a common loading point. MS loading point has been blinded in gantry no.5.

LDO, FO, HVFO (GNFC GRADE) FO can be loaded on gantry no.1 & 3. LDO can be loaded in gantry no. 1. HVFO (GNFC GRADE) is loaded on Gantry No-2

LSHF This product can be loaded on gantry no.1

Summary of product distribution on gantries

Gantry no.

Line no.

Products Hose Remarks

1 1&2 FO, LDO/LSHF (Short Length) RUBBER

MFM for FO

2 3&4 HVFO (GNFC GRADE) (Short Length) RUBBER

MFM

3 5&6 MS,REFORMATE ,SK, HSD,NAPHTHA, FO

RUBBER MFM FOR -NAP

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4 8&9 Gantry Not in use as LSHS production stopped.

METALLIC

5 11&12 MS, REFORMATE, SK, HSD, NAPHTHA, ATF.

RUBBER MFM EXCEPT NAP

6 15&16 MS, REFORMATE, SK, HSD, NAPHTHA.

METALLIC MFM

Chapter-1

1.0 General

For efficient functioning of the refinery one of the major factors is to regulate off take movement of products. Since large volumes of high priced products are involved, utmost care is called for in handling of products during Dispatch. Dispatch of products by the different modes depending upon a number of factors like market requirement, product availability etc. is an important exercise for the Oil Movement and Storage Section. To achieve the smooth functioning of Dispatch systems a close co-ordination between Marketing, Railways and other agencies involved in the process is called for. A product becomes ready for Dispatch only after getting the quality certificate from laboratory and after complying with the necessary excise formalities. There are three modes of transport operating in this refinery for the Dispatch of products. They are: 1) Pipeline 2) Road 3) Rail Each mode of transport is discussed in detail in the respective sub-sections of the chapter. The pipe line dispatch is discussed in detail in Receipt Section. Here in this volume-II tank wagon dispatch and TTL dispatch is taken in detail.

1.1 DISPATCHES BY ROAD (TTL – White Oil)

The following products are dispatched by road:

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1) Mineral Turpentine Oil (MTO) 2) A.T.F 3) Food Grade Hexane (FGH) 4) Polymer Grade Hexane (PGH) 5) Naphtha 6) Army HSD 7) Furnace Oil 8) MTBE 9) LAB-LMW 10) LAB-HMW 11) PFRCB 12) FO Bunker grade.

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Rain water harvesting wells: Artificial recharging of ground water is an augmentation of natural recharge of ground water. Rain water harvesting and Artificial recharging of ground water is essential as Need for Ground water is increasing day by day as it is a handy resource There is constant threat of depletion of ground water sources Natural recharging of ground water has diminished due to urbanization and construction of

buildings, pavements and roads As a step towards recharging ground water table, Gujarat Refinery has also constructed rain water harvesting wells inside as well as outside Refinery Battery limit, details of which have been indicated below. Total of 18 nos. of rain water harvesting wells have been constructed by Gujarat Refinery and additional 2 nos. are constructed each year. Maintenance of these wells along with checking of water table depth is being done on continuous basis. Additionally, actions are also being taken to comply with IOCL’s policy on rain water harvesting.

SNo Location Details Year 2003-04

1. Near IS building Recharge well 2. Opposite new Administration Building Recharge well 3. In 500 m Green Belt Recharge well 4. At OHC – GR Hospital Recharge well 5. At Gujarati medium school ground Recharge well 6. Near officer’s club Recharge well 7. Opposite Community Hall Recharge well

Year 2009 1. Sector 1 – CISF quarters Recharge well

(inlet from Main drainage)

2. Inside the Stadium towards Main Drainage Recharge well 3. Near Township nursery Recharge well 4. Behind ED’s bungalow Recharge well 5. Near GR hospital Recharge well

Year 2012-13 1. Roof top rain water harvesting of IS building Roof top rain water

harvesting 2. Roof top rain water harvesting of Technical building Roof top rain water

harvesting Year 2013-14

1. Roof top rain water harvesting of North block control room

Roof top rain water harvesting

2. Roof top rain water harvesting of South block control room

Roof top rain water harvesting

Year 2015-16 1. Administrative building (2 nos.) Recharge well Year 2016-17

1. Gujarat Refinery Township (2 nos.) Construction in progress

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Watering of stadium, through rain water harvesting system

A bore well dug in one corner of stadium which charged with the help

of storm water drain. Watering done through sprinkler system

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Details of Show Cause Notices received from GPCB in the year 2015 and 2016 (till date)

Sr. No.

Notice Reply

3.1

1

Notice No. GPCB/ID/21967/VRD-CCA-103(10) dtd 28.03.15.

Installation of online continuous stack as well as effluent monitoring system and linkage of data with GPCB/CPCB server.

Ref. No. HSE/GPCB/2015/05 dtd 31.05.15.

Complied. Effluent analysers at treated effluent analyser, CO and PM analyser in Stacks have been installed.

4.2

2

Notice No. GPCB-CCA-VRD-103 (10) /ID-21967/Outward No. 310480 dtd 15.04.15.

Discharge of water into storm water channel to be minimized.

Ref. No. HSE/GPCB/2015/07 dtd 03.06.15.

Actions already taken and those in progress to minimize discharge of water to open channel communicated to GPCB.

5.3

3

Notice No. SCN-341987 dtd 18.01.16

Discharge of wastewater from LAB (Linear Alkyl Benzene) plant to storm water channel to be stopped.

Ref. No: HSE/GPCB/2016/02 dtd 09.03.16.

Corrective measure of dechoking of Pump Bearing Cooling water return header to Cooling water header mentioned in the above communication. Subsequently, discharge of wastewater from LAB plant to storm water drain has been stopped.

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EIA for BS-IV & BS VI Project Compliance to TOR

Annexure 24 Terms of Reference (ToR) Compliance Report

ToR (Terms of Reference) was assigned for the EIA study by MoEF&CC vide F.No. J-

11011/96/2015-IA II (I) dated 13th July 2015 and J-11011/96/2015-IA II (I) dated 7th September

2016, copy of the same is enclosed in Annexure- 3. The consolidated compliance against TOR

points are stated below.

S.No Terms of Reference Compliance A. Standard ToR

1 Introduction i. Details of the EIA Consultant including

NABET accreditation Hubert Enviro Care Systems (P) Ltd. NABET Sr. No. 77.

ii. Information about the Project Proponent The Details are provided in Section 1.3 of Chapter 1.

2 Project Description and Project Benefits. The detail of project description is provided in Chapter 2, and the benefits are described in Chapter 8.

i. Products with capacities for the proposed project

The details are provided in Section 2.16 of Chapter 2.

ii. If expansion project, details of existing products with capacities and whether adequate land is available for expansion, reference of earlier EC if any.

The details are provided in Chapter 2 and the copy of earlier EC is attached in Annexure 1.

iii. List of Raw materials and their source with mode of transportation

The raw material used in this process is Crude oil and the transportation is through pipelines. Raw material inputs to various units are enclosed in Annexure 5. The details are given in Chapter 2.

iv. Other chemicals and materials required with quantities and storage capacities

No other chemicals are used in the process.

v. Details of emission, effluents, hazardous waste generation and their management

The details are given in Chapter 2 and Annexure 16.

vi. Requirement of water, power, with source of supply, status of approval, water balance diagram, man-power requirement (regular and contract)

The details are given in Chapter 2.

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S.No Terms of Reference Compliance vii. Process description along with major

equipments and machineries, process flow sheet (quantitative) from raw material to products to be provided

The details are provided in Chapter 2.

viii. Hazard identification and details of proposed safety systems

The Risk Assessment report is enclosed in Annexure 11. Disaster Management Plan is enclosed in Annexure 13. Fire Protection plan is enclosed in Annexure 15.

ix. Expansion/ modernization proposals (a) Copy of all Environmental Clearance(s)

including amendments thereto obtaining for the project from MoEF&CC/SEIAA shall be attached as an Annexure. A certified copy of the latest monitoring report of the Regional office of the Ministry of Environment and Forests as per circular dated 30th May, 2012 on the status of compliance of conditions stipulated in all existing environmental clearances including Amendments shall be provided. In addition status of compliance of Consent to Operate for the ongoing existing operation of the project from SPCB shall be attached with the EIA-EMP report

(b) In case the existing project has not obtained environmental clearance, reasons for not obtaining the provisions of the EIA notification 1994 and/or EIA notification 2006 shall be provided. Copies of Consent to Establish / No objection certificate and Consent to Operate (in case of units operating in prior to EIA notification 2006, CTE and CTO of FY 2005-2006) obtained from the SPCB shall be submitted. Further compliance report to the conditions of Consents from the SPCB shall be

Certified copy of latest monitoring report of the Regional Office of the Ministry of Environment and Forests ,Bhopal on the status of compliance of conditions stipulated in all existing Environmental Clearances is provided in Annexure 14.

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S.No Terms of Reference Compliance submitted.

3 Site Details i. Location of the project site covering

village, Taluka/Tehsil, District and State, justification for selecting the site. Whether other sites were considered

The site specific details are provided in Chapter 2 and Chapter 5.

ii. A Topo sheet of the study area of radius of 10 Km and site location on 1:50,000/ 1:25,000 scale on an A3/A2 sheet (including al eco-sensitive areas and environmentally sensitive places)

The detail of the study area is provided in Chapter 2 and there are no eco sensitive areas around the project.

iii. Details w.r.t option analysis for selection of site

No other alternate sites were considered for the project. The details are provided in Chapter 5.

iv. Co-ordinates (lat-long) of all four corners of the site

The co-ordinates along with the site details are provided in Chapter 2.

v. Google map Earth downloaded of the project site

The google earth image is enclosed in Chapter 2.

vi. Layout maps including existing unit as well as proposed unit indicating storage area, plant area, greenbelt area, utilities etc. If located within an industrial area/Estate/Complex, layout of Industrial indicating location of unit within the Industrial area/Estate.

The layout of Refinery at Koyali with the key units of operation marked are given in Annexure - 4

vii. Photographs of the proposed and existing (if applicable) plant site, existing, show photographs of plantations/greenbelt, in particular

Site photographs are enclosed in Chapter 2 & Greenbelt photographs are enclosed in Chapter 9.

viii. Land use break-up of total land of the project site (indicate and acquired), government/ private- agriculture, forest, wasteland, water bodies, settlements, etc shall be included (not required for industrial area)

The details are provided in Section 2.7 of Chapter 2.

ix. A list of major industries with name and type within the study area (10 km radius) shall be incorporated. Land use details of the study area)

IPCL – 2.3 km (North) Gujarat Alkalies and Chemicals – 3.6 km (North East) Reckona Pharmaceuticals – 9.2 km

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S.No Terms of Reference Compliance (North)

x. Geological features and Geo-hydrological status of the study area shall be included.

Topographically the area is flat in nature. The details of the same are provided in Chapter 3.

xi. Details of drainage of the project upto 5km radius of the study area. If the site is within 1Km radius of any major river, peak and lean season river discharge as well as flood occurrence frequency based on peak rainfall data of the past 30 years. Details of Flood Level of the project site and maximum of Flood of the river shall also be provided (mega green field projects)

No major river is within 1 km radius. The drainage details are enclosed in Chapter 3.

xii. Status of acquisition of land. If acquisition is not complete, stage of the acquisition process and expected time of complete procession of the land.

The project land site is within the existing acquired premises. Hence, no additional land is required for acquisition.

xiii. R&R details in respect of land in line with state Government policy

R&R not applicable.

4 Forest and wildlife related issues (if applicable) i. Permission and approvals for the use of

forest land (forestry clearance), if any, and recommendations of the State Forest Department (if applicable)

Not applicable

ii. Land use map based on High resolution satellite imagery (GPS) of the proposed site delineating the forest land (in case of projects involving forest land more than 40 Ha)

Land use details are provided in Chapter 2. Description of the Land Environment along with Land type map is enclosed in Chapter 3.

iii. Status of application submitted for obtaining the stage of Forest Clearance along with latest status shall be submitted

Not applicable

iv. The projects to be located within 10 Km of the National parks, Sanctuaries, Biosphere Reserves, Migratory Corridors of Wild Animals, the project proponent shall submit the map duly authenticated by Chief Wildlife Warden showing these features vis-à-vis the project location and

Not applicable

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S.No Terms of Reference Compliance the recommendations or comments of the Chief Wildlife Warden-thereon.

v. Wildlife Conservation Plan duly authenticated by the Chief Wildlife Warden of the State Government for conservation of schedule of fauna, if any exists in the study area.

Not applicable

vi. Copy of application submitted for clearance under the Wildlife (Protection) Act, 1972 to the Standing Committee of the National Board for Wildlife.

Not applicable

5 Environmental Status i. Determination of atmospheric inversion

level at the project site and site-specific micrometeorological data using temperature, relative humidity, hourly wind speed and direction and rainfall

The site specific micrometeorology is provided in Chapter 3.

ii. AAQ data (except monsoon) at 8 locations for PM10, PM2.5, SO2, NOx, CO and other parameters relevant to the project shall be collected. The monitoring stations shall be based on CPCB guidelines and take into account the pre-dominant wind direction, population zone, sensitive receptors including reserved forests.

The Details are provided in Chapter 3.

iii. Raw data of all AAQ measurement for 12 weeks of all stations as per frequency given in the NAAQM notification of Nov. 2009 along with- min-max, average and 98% values for each of the AAQ parameters from data of all AAQ stations should be provided as an annexure to the EIA report

The raw data of all AAQ for 12 weeks indicating the min, max, average and 98 % values are tabulated and enclosed in Annexure – 18.

iv. Surface water quality of nearby River (1000m upstream and downstream of discharge point) and other surface drains at

The details are provided in Chapter 3.

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S.No Terms of Reference Compliance eight locations as per CPCB/ MoEF&CC guidelines.

v. Whether the site falls near to polluted stretch of river identified by the CPCB/MoEF& CC, if yes give details

Not Applicable

vi. Ground water monitoring at minimum 8 locations shall be included

The Details are provided in Chapter 3.

vii. Noise level monitoring at minimum 8 locations shall be included

The details are given in Chapter 3.

viii. Soil characteristics as per CPCB guidelines

The soil characteristics are detailed in Chapter 3.

ix. Traffic study of the area, type of vehicles, frequency of vehicles for transportation of materials, additional traffic due to proposed project, parking arrangement etc.

The total refinery site area along with Refinery Township supports vehicles such as Mini trucks, Jeeps, Cars, Buses and bikes. The frequency of the above mentioned vehicles per day would be around 150 – 200 in total. The nearest highway is NH - 8 which is 3.0 Km in the east direction from the site. There would be no additional traffic for the proposed project.

x. Detailed description of flora and fauna (terrestrial and aquatic) existing in the study area shall be given with special reference to rare, endemic and endangered species. If schedule-I fauna and found within the study area, a Wildlife Conservation plan shall be prepared and furnished

No endangered species are found in the study area. The details of flora & fauna are provided in Chapter 3.

xi. Socio-economic status of the study area The details of Socio – economic status is given in Chapter 3.

6 Impact and Environmental Management Plan

i. Assessment of ground level concentration of pollutants from the stack emission based on site-specific meteorological features. In case the project is located on a hilly terrain, AQIP modeling shall be done using inputs of the specific terrain characteristics for determining the potential impacts of the

The ground level concentration of the emissions is enclosed in Chapter 4. AERMOD Software Version 7.5.0 was used for air dispersion modeling and is applicable to a wide range of buoyant or neutrally buoyant emissions. The details for air modeling software are provided in Chapter 4.

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S.No Terms of Reference Compliance project on the AAQ. Cumulative impact of all sources of emissions (including transportation) on the AAQ of the area shall be assessed. Details of the model used and the input data used for modeling shall also be provided. The air quality contours shall be plotted on a location map showing the location of the project site, habitation nearby, sensitive receptors, if any.

ii. Water quality modeling – in case of discharge in water body

There is no discharge of effluent from the property. Detailed in Chapter 2.

iii. Impact of the transport of raw material and end products on the surrounding environment shall be assessed and provided. In this regard, options for transport of raw materials and finished products and wastes (large quantities) by rail or rail-cum road transport or conveyor-cum-rail transport shall be examined.

Raw materials and end products of the process are transported through pipelines. The risks/impacts due to transportation is analyzed and enclosed as risk assessment in Annexure 11.

iv. A note on treatment of waste water from different plant operations, extent recycled and reused for different purposes shall be included. Complete scheme of effluent treatment, characteristics of untreated and treated effluent to meet the prescribed standards of discharge under E(P) rules.

Effluent from the process is treated and reutilized. Block diagram of CETP is provided in Annexure 8. The detail of waste water treatment is given in Chapter 4.

v. Details of stack emission and action plan for control of emissions to meet standards.

Details of emissions from the stack is given in Chapter 4 and also the stack emission reports are enclosed in Annexure 10

vi. Measures for fugitive emission control The details are provided in Chapter 9.

vii. Details of hazardous waste generation and their storage, utilization and management, Copies of MOU regarding utilization of solid and hazardous waste in cement plant

The details of hazardous waste generated are enclosed in Chapter 2. Consent has been granted from GPCB for each category of waste for storage and disposal.

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S.No Terms of Reference Compliance also be included. EMP shall include the concept of waste-minimization, recycle/ reuse/recover techniques, Energy conservation, and natural resource conservation.

Amended consent is enclosed in Annexure 2. The Hazardous waste management details are enclosed in Chapter 9.

viii. Proper utilization of fly ash shall be ensured as per Fly Ash notification, 2009. A detailed plan of action shall be provided.

No fly ash is produced in the process.

ix. Action plan for the green belt development plan in 33% area i.e., land with not less than 1500 trees per Ha. Giving details of Species, width of plantation, planning schedule etc. shall be included. The green belt shall be around the project boundary and a scheme for greening of the roads used for the project shall also be incorporated.

As there is no area in the existing plant for the development of green belt any further, greeneries has been developed in the 70% of head work area and 50% of Township area which in total exceeds 33% requirement of greenery coverage. The details are provided in Chapter 2.

x. Action plan for rain water harvesting measures at plant site shall be submitted to harvest rainwater from the roof tops and storm water drains to recharge the ground water and also to use for the various activities at the project site to conserve fresh water and reuse the water requirement from other sources.

Total of 18 nos. of rain water harvesting wells have been constructed by Gujarat Refinery and additional 2 nos. are constructed each year. Maintenance of these wells along with checking of water table depth is being done on continuous basis. The details are enclosed as Annxeure 21.

xi. Total capital cost and recurring cost /annum for environmental pollution control measures shall be included.

The total cost for all the environmental control measures is included in the budget for the Environmental Plan in Chapter 6.

xii. Action plan for Post-project environmental monitoring shall be submitted

The details of post project environmental monitoring programme are given in Chapter 6.

xiii. Onsite and offsite Disaster (natural and Man-made) preparedness and Emergency Management Plan including Risk Assessment and damage control. Disaster Management Plan should be linked with District Disaster Management Plan.

Risk Assessment is performed for the storage of solvents and is incorporated as Annexure 11. Disaster Management Plan is enclosed in Annexure 13.

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S.No Terms of Reference Compliance 7 Occupational Health

i. Plan and fund allocation to ensure the occupational health & safety of all contract and casual workers

The details of occupational health and safety are provided in Chapter 9.

ii. Details of exposure specific health status evaluation of worker. If the worker’s health

is being evaluated by pre-designed format, chest x-rays, Audiometry, Spirometry, Vision testing (Far and near vision, colour vision and any other ocular defect), ECG, during pre placement and periodical examinations give the details of the same. Details regarding last month analyzed data of above mentioned parameters as per age, sex, duration of exposure and department wise.

Regular health camps are conducted for all the workers alike. Details of Status of health checkup are provided in Chapter 9.

iii. Details of existing Occupational & Safety Hazards. What are the exposure levels of hazards and whether they are Permissible Exposure level (PEL) if these are not within PEL, what measures the company has adopted to keep them within PEL. So that health of the workers can be preserved.

The Health & Safety department makes sure all the workers are not exposed to any kind of toxicity and is within the prescribed limit. The details are provided in Chapter 9.

iv. Annual report of health status of workers with special reference to Occupational Health and Safety

Annual report of health status of workers is enclosed in Chapter 9.

8 Corporate Environment Policy i. Does the company have a well laid down

Environemntal Policy approved by its Board of Directors? If so, it may be detailed in the EIA report

Yes. Copy of the Corporate Environmental policy is provided in Chapter 9.

ii. Does the Environment Policy prescribe for standard operating process/procedures to bring into focus any infringement/ deviation/ violation of the environemnt or forest norms/ conditions? If so, it may be detailed in the EIA

Yes. Copy of the Environmental policy is provided in Chapter 9.

iii. What is the hierarchical system or Administrative order of the company to

The organogram is provided in Chapter 9.

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S.No Terms of Reference Compliance deal with the environmental issues and for ensuring compliance with the environmental clearance conditions? Details of this system may be given.

iv. Does the company have system of reporting of non-compliances/ violations of environemntal norms to the Board of Directors of the company and/or Stakeholders or stakeholders at large? This reporting mechanism shall be detailed in the EIA report

Yes. The roles and responsibilities of the administrative are given in Chapter 9.

9 Details regarding infrastructure facilities such as sanitation, fuel, restroom etc. to be provided to the labour force during construction as well as to the casual workers including truck drivers during operation phase.

Proper and sufficient sanitary facility already exists at the site in the form of Toilets & the biological treatment facility off CETP will be used for treatment of the sewage generated.

10 Enterprise Social Commitment (ESC) i. Adequate funds (at least 2.5% of the project

cost) shall be earmarked towards the Enterprise Social Commitment based on public Hearing issues and item-wise details along with the bound action plan shall be included. Socio-Economic development activities need to be elaborated upon.

Suitable activities will be done as per the ESC requirements. Around Rs 157.09 lakhs (Rs 15.71 Million) are spent towards Community development like Clean Drinking Water, Health and Medical Care and expansion of education and other related activities. The details are given in Chapter 9.

11 Any litigation pending against the project and/ or any direction/ order passed by any Court of Law against the project, if so, details thereof shall also be included. Has the unit received any notice under the section 5 of Environment (Protection) Act, 1986 or relevant Sections of Air and Water Acts? If so, details thereof and compliance /ATR to the notice(s) and present status of the case.

Details of Show Cause Notices received from GPCB in the year 2015 and 2016 are answered accordingly is attached as Annexure 22. No litigation pending against the project.

12 A tabular chart with index for point wise compliance of above TOR

Complied

B. Specific Terms of Reference

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S.No Terms of Reference Compliance 1 Complete process flow diagram describing each

unit, its capacity along with material & energy balance

The process description along with flow diagrams is given in Chapter 2.

2 Details of intermediate product, their storages & final products to be manufactured.

Raw materials/ intermediates/ products are stored in closed tanks/drums provided with breather arrangements to avoid fugitive emissions. Raw material quantities are attached as Annexure 5. Details of intermediate product and material balance are attached as Annexure 7. The details of Crude Oil handling is explained in Section 2.9.1 of Chapter 2. The storage and transportation details of raw materials and products are detailed in Section 9.5.6 of Chapter 9.

3 Sulphur balance giving input from crude, refinery fuel (if used) and any other outside fuel and output in various products & emissions.

Sulphur Recovery Unit downstream of Amine regenerator uses Off gas from the Amine Regenerator as feed and converts gaseous H2S into Solid elemental Sulfur thereby reducing atmospheric emissions. Sulphur balance for the existing refinery operations is given in Chapter 2.

4 Details of proposed source – specific pollution control schemes and equipment to meet the national standards for petroleum refinery.

The emission from existing stacks has been taken as basis for modeling and is shown in Chapter 4 and predicted GLC for existing stack is shown in Table 4-2. Low NOx burners, Cyclone separators have been provided in FCC reactor, Sulphur free natural gas as fuel etc. The pollution control measures are explained in details in Chapter 9.

5 Details of emissions from all the stacks including volumetric flow rate.

The stack emission reports are enclosed as Annexure 10.

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S.No Terms of Reference Compliance 6 Details on availability of raw materials (crude

oil, natural gas, chemicals, etc.), its source and storage at the plant.

The details of raw materials and the storage tank are provided in Chapter 2.

7 Details on mode of transportation of crude and products

Crude is transported through pipelines. Products are transported through Pipelines, Trucks & Railway wagons. The details of Crude Oil handling is explained in Chapter 2. The transportation details of raw materials and products are detailed in Section 9.5.6 of Chapter 9. The details mode of transportation of crude and products are attached as Annexure 20.

8 Details of storage capacity of crude and products

Details of Storage capacity of crude and product is given in Chapter 4.

9 Ambient air quality data should include hydrocarbon (methane andd non – methane), VOC, Ni & V etc.

The ambient air quality data is provided in Chapter 3.

10 Efforts to minimize water consumption, effluent discharge and to maintain quality of receiving water body.

Many measures have been taken to reduce the fresh water consumption at the refinery. The details of Waste water treatment facility are provided in Chapter 4.

11 Details of effluent treatment plant, inlet and treated water quality with specific efficiency of each treatment unit in reduction in respect of all concerned/regulated environmental parameters. Also, include treatment details such as primary (physico-chemical), secondary (biological) and tertiary (activated carbon filters) treatment systems.

The details of Central Effluent Treatment Plant (CETP) are given in Chapter 4.

12 Storm water management plan Storm water network in Gujarat Refinery has been constructed to collect rain water and surface run off within the Refinery premises. Open channel network is widely spread within the Refinery and finally discharged into Mahi River.

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S.No Terms of Reference Compliance A buffer tank of capacity 30,000 KL has been provided to take care of sudden additional influent load, during monsoon. The layout of storm water drain is given below in Annexure 9. The details are provided in Chapter 6.

13 Estimation SO2 and NOx emissions load The estimated details are provided in Chapter 4.

14 Details on flaring system Development of Integrated flare management system and location of flare is attached as Annexure 19.

15 Details of VOC recovery devices in the storage tanks

Activated Carbon Filter (ACF) is used to treat VOC before letting it to the environment.

16 Arrangement for spill management The oil spill collected through Gully Suckers andis taken to the nearby Oily Water Sewer (OWS). DAF, deoily polyelectrolyte methods are used to treat oily water. The details of the techniques are given in Chapter 9.

17 Oily sludge management plant The details are provided in Chapter 4. 18 Risk Assessment & Disaster Management Plan

(i) Identification of hazards (ii) Consequence Analysis (iii) Risk assessment should also include

leakages and location near to refinery & proposed measures for risk reduction

(iv) Arrangement for fire protection and control

The hazards, its consequences and the risks involved have been studied and the report is attached as Annexure 11. The Emergency Response and Disaster Management Plan and On – Site Emergency Plan is attached in Annexure 13.

Additional TORs 1 Public hearing to be conducted and issues raised

and commitments made by the project proponent on the same should be included in the EIA/EMP report in the form of tabular chart with financial budget for complying with the commitments made.

Public hearing conducted by GPCB on 05.11.2016

2 A separate chapter on status of compliance of Environmental Conditions granted by Centre to

Environmental Compliance provided in Chapter 10. The status of

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S.No Terms of Reference Compliance be provided by RO, MoEF on status of compliance of conditions on existing unit to be provided in EIA-EMP report.

compliance is enclosed in Annexure 14.

3 The layout of the expansion plant should be such that major consequences of any accidental release arecontained within plant boundary.

The Site layout plan is enclosed in Annexure 4. With the major units indicated. The risk assessment and consequence for different scenarios for accidental release are detailed in Annexure 11.

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GUJARAT POLLUTION CONTROL BOARDPARYAVARAN BHAVAN

Sector 10-A, Gandhinagar 382010Phone . (079) 23226295Fax: (079) 23232156Website : www.gpcb.gov.in

BY R.P.A.D.

"Consent'toEstablish"CTE NO:78414

NO: GPCB/CCA-YRD-I03(11)/ID-21967/

To,MIs. Indian Oil Corporation Ltd. (Gujarat Refinery)Refinery Division, HSE Department.PO- Jawaharnager,Tal: VadodaraDis!: Vadodara-391320.

Sub: Consent to Establish (NOC) under Section 25 of Water Act 1974 and Section21 of Air Act 1981.

Ref; 1. Your online CTE application. No; 105089, dated 08/03/2016.

2. CCA order nO.WH-52220. Date of issue 19/02/2013.

Sir,Without prejudice to the powers of this Board under the V./atcr (Prevention

and Control of Pollution) Act-1974, the Air Act-1981 and the Environment(Protection) Act-1986 and without reducing your responsibilities under the saidActs in any way, this is to inform you that this Board grants Consent to Establish

(NOC) for addition/inclusion of existing industrial plant/activities at- PO-Jawaharnager, Tal: Vadodara, Dist: Vadodara-391320, for revamp of existingDHDT, DHDS, VGO-HDT & HGU-llI units, (BS-IV expansion) with lallowingterms & conditions. The Validity period of the order \vill be up to 24/04/2023.

I Sr. No. Unit----

, Present

CapacityI

11. DHDT 2.2MMTPA

2. DHDS 1.7MMTPA

13 HGU-3 72.5 TMTPA

4 VGO-HDT 2.1 MMTP

1. SPECIFIC CONDITIONS:L 1. Applicant shall comply with the all the conditions of Environment Clearance

to be issued by the Ministry of Environment, Forcsts& Climate Change.New Delhi, with reference to your application/letter dated 09/01/2015.Applicant shall seek CTEwamendrnentif there is any change in Environment

Clearance ordcr.1.2. Applicant shall obtain the permission from all the relevant Agencies /

Authorities as appl icable.

GPCB ID', 21967

Clean Glljarat Green GlljaratISO-9001-2008 & ISO-14001 - 2004 Certified Organisation

Outward No:357706,01/06/2016

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http://www.gpcb.gov.in

1.3. Applicant shall obtain prior permission of Ground \Vater Authority lorwithdrawal of ground water/use of bore wells. (ifapplicable)

2. CONDITION LINDER THE WATER ACT:2.1 rhe quantity of the industrial eflluent to be generated from the

manufacturing process and other ancillary industrial operations shall not

exceed 15m3/hour from expansion. This additional eftluent shall be reused.

thus there shall be no change in discharge quantity of industrial enluent aswell as domestic effluent, quality of effluent and mode of disposal due toproposed project.

33.1

3.2

3.3

I ~~::,issible]DHDS (l010F-02) Particulate Maller 1150 mglNM !

, furnace SO,' 100ppm '

NO~ 5QjJ~j3.4 There shall be no additional process gas emission from the manufacturing

activities as well as any other ancillary industrial operations due to proposedproject.

3.5 Stack monitoring facilities like port hole. platform/ladder etc., shall beprovided with stacks/vents Chimney in order to facilitate sampling of gases

being emitted into the atmosphere.3.6. The applicant shall provide portholes, ladder. platform etc at chimney(s) for

monitoring the air emissions and the same shall be open for inspectionto/and for use of Board's staff. The chimney(s) vents attached to various

sources of emission shall be designed by numbers such as S-L S-2, etc. andthese shall be painted/ displayed to facilitate identitlcarion.

3.7. There shall no any fugitive emission and/or odour pollution due tomanufacturing activities and ancillary operations. Adequate measures shall

be taken thereof.

GPCB fD: 21967

Outward No:357706,01/06/2016

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GPCB3.8

3.9

GUJARAT POLLUTION CONTROL BOARDPARYAVARMJ BHAVAN

Sector 10-A, Gandhinagar 382 010Phone : (079) 23226295Fax . (079) 23232156Website : www.gpcb.gov.in

The concentration of the following parameters in the ambient air within thepremises of the industry and a distance of 10meters from the source (otherthan the stack/vent) shall not exceed the following levels. Applicant shall

comply "",jth the National Ambient Air Quality Standards notifiedbyCentral Pollution Control Board, Nev.,..Delhi time to time under the provisionof the Environment (Protection) Act-1986.

Parameter Permissible Limit'· i Permissi'biZLimit 24 I

I Annual H~s: Average _ _ I

Particulate rTmttcr-IO[PMIO] 60Micro ram/J\:JM-' lOOMiS:TS!gram /NT\-v]Particulate matter-2,~[PM2.5] 40Micro amINM '_ 60Microgram lNT\1'Oxides of SuI hur 50Microgram iNMJ "80Microgram /N~~

Oxides of Nitrogen 40Micro ram /NMJ- 801\Jicrogram iNM-1 !

The Industry shall take adequate measures for control or noisc levels from~

its own sources within the premises so as to maintain ambient air qualitystandards in respect of noise to less than 75 dB (a) during day' time and 70 dB(A) during night time. Daytime is reckoned in between 6a.m. andlO p.m.and nighttime is reckoned between 10 p.m. and 6 a.m

4 CONDITIONS UNDER HAZARDOUS WASTE:

4.1 The applicant shall provide temporary storage facilities for each type of HazWaste as per Hazardous and Other Waste (Management& TransboundaryMovement) Rules, 2016 as amended from time to timc.

4.2 The applicant shall be obtained membership of common lSDF site fordisposal Hazardous Waste as categorized in Hazardous and Other Waste(Management & TransboWldary Movement) Rules. 2016 as amended fromtime to time.

4.3 The applicant shall explore possibilities of Co-processing of hazardouswaste at authorized Cement kiln and make arrangement theraf. OR The

applicant shall obtained membership of common Hazardous \Vasteincinerator for disposal of incinerable waste.

4.4 Hazardous Waste generated shall be disposed off in accordance \\'ith the

Hazardous and Other Waste (Management& Transboundary Movcment)Rules, 2016 and unit shall have to obtain authorization of the Board for allapplicable categories of Hazardous vvastes.

4.5 The applicant shall explore possibility and apply for authorizationfiJfrecovery I reuses of any Hazardous Wastes.

5 GENERAL CONDITlONS:5.1 The applicant also comply with thc General conditions as per Annexurc - 1

attached herc\vith (No.1 to 38) (whichever applicable).

5.2 The Wlit shall install meters for measuring category \vise consumption ofwater (category as given in Water - Cess Act 1977, Schedule-11).

GP(B ID: 21967

Clean Gujarat Green GujaratISO-9001-2008 & ISO-14001 - 2004 Certified Organisation

Outward No:357706,01/06/2016

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5.3 The applicant shall have to subminhe returns in prescribed form regardingwater consumption and shall nave to make payment of water cess to the

Board under the Water Cess Act- 1977.SA Adequate plantation shall be carried out all along the peripheryor the

industrial premises in such a way that the density of plantation is at least1000 trees per acre of land and a green belt of 10 meters v,"idth is developed.

5.S In case of ehange of ownership/management the name and address of the

new owners/partners/direetors/proprietor should immediately be intimated tothe Board.

5.6 The applicant shall hO\vever, not without the prior consent to operate of theBoard bring into use any new or altered outlet for the discharge of dIluentor gaseous emission or sewage waste from the proposed industrial plant. Theapplicant is required to make applications to this Board for this purpose in

the prescribed forms under the provisions of the \Vater Act-1974. the AirAct-1981 and the Environment (Protection) Act-1986.

5.7 The concentration of Noise in ambient air within the premises of industrialunit shall not exceed following levels:

Between 6 A.M. and 10 P.M.: 75 dB (A)Between 10 P.M. and 6 A.M.: 70 dB (A)

5.8 Applicant is required to comply with the Manufacturing, Storage and Importof Hazardous Chemicals Rules-1989 framed under the Environment

(Protection) Act-1986.5.9 If it is established by any competent authority that the damage is caused due

to their industrial activities to any person or his property in that case they areobliged to pay the compensation as determined by the competent authority.

For and on behalf ofGujarat Pollution Control Board

~\~

(DipalfTank)Unit Head

GPCB ID: 21967

Outward No:357706,01/06/2016

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NO: GPCB/CCA-VRD-103(7)/lD: 21967/1.4-h-to

GUJARAT POLLUTION CONTROL BOARDPARYAVARAN BHAVAN

Sector 10-A, Gandhinagar 382010Phone (079) 23226295Fax (1)79) 23232156website www.gpcb.gov.in

ByR.P.A.D.

Date:.../.:j \o~\4"\.3

Amendment to CONSENTS AND AUTHORISATION Order No: WH - 52220. Date of Issue:19/02/2013.

(Under the provisionslrules of the aforesaid environmental acts)

To,M:Li(iNDlAN OIL CORPORATION LIMITED (IOCL) (21967),GUJARAT REFINERY,P.O. JAWAHARNAGAR,DlST: VADODARA - 391 320.

In exercise of the power conferred under section-25 of the Water (Prevention and Control of Pollution)Act-1974, under section-21 of the Air (Prevention and Control of Pollution) Act-1981 and Authorization underrule 5(4) of the Hazardous Waste (Management, Handling and Transboundary Movement) Rules -2008 framedunder the E (P) Act-1986. The Consolidated Consent Authorization (CC&A) granted toMis. INDIAN OILCORPORATION LIMITED (IOCL) located at GUJARAT REFINERY, P.O. JAW AHARNAGAR, DlST:VADODARA - 391 320, vide this office Consent order no: WH - 52220. Date of Issue:19/02/2013, is beingsubjected to amendment for the following conditions only.

And whereas Board has received your representation for the amendment of Consolidated Consent andAuthorization (CC&A) of this board under the provisionsI rules of the aforesaid Acts. Consents&Authorization are hereby amended as under subjected to amendment for the following conditions only.

I. The Condition No: 3, Sr. No: 3.10fthe above said consent order is amended as under from originalCC&A order.

The quantity of the Industrial wastewater disposed from the industry to VECL. shall not exceed 13680KL may after maximum recycling efforts.

2. The other conditions of the CC&A order no: WH - 52220. Date of Issue:19/02/2013, shall remainunchanged.

For and on behalf ofGujarat Pollution Control Board

{f0V-~v--\rl(M. V. PATEL)

ENVIRONMENT AL ENGINEER

Clean Gujarat Green GujaratISO - 9001 - 2008 & ISO - 14001 - 2004 Certified Organisation

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ANNEXURES - environmentclearance.nic.inenvironmentclearance.nic.in/.../online/EC/2911201693YUK3GLAnnexures.pdf · Gujarat Refinery AOR MATERIAL BALANCE OF PROCESS UNITS 2014-15 PAGE

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