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QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21 Licence number: N/A Page 1 N/A OFFSHOR RE PROJE ECT SU UMMARY Y Project n name Штокман у учебный Region C.I.S. Country Russia Basin South Bare ents Sea B Basin Procurem ment strategy Currency Rate/$ Procurem ment strategy Currency Rate/$ Offshore Russia $ 1,00 Onshore Russia $ 1,00 Contingency Russia (Arctic) $ 1,00 Contingency Russia $ 1,00 Equipment Russia (Arctic) $ 1,00 Equipment N. America $ 1,00 Materials Russia (Arctic) $ 1,00 Materials S. E. Asia $ 1,00 Fabrication Russia (Arctic) $ 1,00 Prefabrication S. E. Asia $ 1,00 Linepipe Russia (Arctic) $ 1,00 Linepipe S. E. Asia $ 1,00 Installation Russia (Arctic) $ 1,00 Construction Russia $ 1,00 Design & PM Russia (Arctic) $ 1,00 Design & PM Western Europe $ 1,00 Opex Russia (Arctic) $ 1,00 Certification Russia $ 1,00 Certification Russia (Arctic) $ 1,00 Opex Russia $ 1,00 Freight Russia (Arctic) $ 1,00 Technica al database Technica al database Offshore Russia (Arctic) Onshore Russia Unit set Metric Develop pment type Gas Develop pment concept FPSO + S ubsea Overall i nput Design g gas production flowrate 9,94 MMsm³/da ay Reserve es 18300,00 MMsm³ Design a associated liquids flowrate 0,61 Mm³/day Water de epth 291,00 m Design g gross liquids flowrate 0,62 Mm³/day Reservo oir depth 2050,00 m Water in njection capacity factor 0,00 Reservo oir pressure 207,00 bara Design w water injection flowrate 0,00 Mm³/day Reservo oir length 8,04 km Design g gas injection rate 0,00 MMsm³/da ay Reservo oir width 4,02 km Condens sate gas ratio 61,50 m³/MMsm³ ³ Swing fa actor 1,30 Fluid cha aracteristics Oil dens sity @ STP 0,79 s.g. H2S con ntent 0,00 ppm CO2 con ntent 0,00 % Gas mol lecular weight 19,00 Initial wa ater cut 1,00 % Producti on profile characteristics Plateau rate 7,65 MMsm³/da ay Years to o plateau 1,00 year Producti vity 2270,00 MMsm³/we ell Plateau duration 4,00 year Peak we ell flow 0,85 MMsm³/da ay Field life e 10,00 year Maximum m drilling stepout 3,00 km Onstrea m days 350,00 day Export m methods Condens sate export method pipeline to shore Gas exp port method pipeline to shore Distance e to delivery point 120,00 km Distance e to delivery point 120,00 km Number of wells Producti on wells 9 Gas inje ection wells - Water in njection wells - Field lev vel miscellaneous data Distance e to operations base 120,00 km Distance e to delivery point 120,00 km Maximum m drilling stepout 3,00 km Maximum m ambient temperature 22,00 °C

Offshore Project Report

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Page 1: Offshore Project Report

QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21

Licence number: N/A Page 1 N/A

OFFSHORRE PROJEECT SU UMMARYY

Project n name Штокман у учебный

Region C.I.S.

Country Russia

Basin South Bareents Sea B Basin

Procuremment strategy Currency Rate/$ Procuremment strategy Currency Rate/$

Offshore Russia $ 1,00 Onshore Russia $ 1,00Contingency Russia (Arctic) $ 1,00 Contingency Russia $ 1,00

Equipment Russia (Arctic) $ 1,00 Equipment N. America $ 1,00

Materials Russia (Arctic) $ 1,00 Materials S. E. Asia $ 1,00

Fabrication Russia (Arctic) $ 1,00 Prefabrication S. E. Asia $ 1,00

Linepipe Russia (Arctic) $ 1,00 Linepipe S. E. Asia $ 1,00

Installation Russia (Arctic) $ 1,00 Construction Russia $ 1,00

Design & PM Russia (Arctic) $ 1,00 Design & PM Western Europe $ 1,00

Opex Russia (Arctic) $ 1,00 Certification Russia $ 1,00

Certification Russia (Arctic) $ 1,00 Opex Russia $ 1,00

Freight Russia (Arctic) $ 1,00

Technicaal database Technicaal database

Offshore Russia (Arctic) Onshore Russia

Unit set Metric

Developpment type Gas

Developpment concept FPSO + S ubsea

Overall i nput

Design g gas production flowrate 9,94 MMsm³/daay Reservees 18300,00 MMsm³

Design a associated liquids flowrate 0,61 Mm³/day Water de epth 291,00 m

Design g gross liquids flowrate 0,62 Mm³/day Reservooir depth 2050,00 m

Water in njection capacity factor 0,00 Reservooir pressure 207,00 bara

Design w water injection flowrate 0,00 Mm³/day Reservooir length 8,04 km

Design g gas injection rate 0,00 MMsm³/daay Reservooir width 4,02 km

Condenssate gas ratio 61,50 m³/MMsm³³

Swing fa actor 1,30

Fluid cha aracteristics

Oil denssity @ STP 0,79 s.g. H2S conntent 0,00 ppm

CO2 conntent 0,00 % Gas mollecular weight 19,00

Initial wa ater cut 1,00 %

Production profile characteristics

Plateau rate 7,65 MMsm³/daay Years to o plateau 1,00 year

Productivity 2270,00 MMsm³/weell Plateau duration 4,00 year

Peak we ell flow 0,85 MMsm³/daay Field life e 10,00 year

Maximumm drilling stepout 3,00 km Onstream days 350,00 day

Export m methods

Condenssate export method pipeline to shore Gas expport method pipeline to shore

Distance e to delivery point 120,00 km Distance e to delivery point 120,00 km

Number of wells

Production wells 9 Gas injeection wells -

Water in njection wells -

Field lev vel miscellaneous data

Distance e to operations base 120,00 km

Distance e to delivery point 120,00 km

Maximumm drilling stepout 3,00 km

Maximumm ambient temperature 22,00 °C

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Oil

Gas

Gas Risers

Gas Offshore Drilling

Oil Risers

Oil Offshore Drilling

FPSO Preprocessing

FPSO Vessel

Gas Landfall

Oil Landfall

GTU Plant

GTU Infrastructure

LNG Offloading Terminal

Gasprom Export Trunkline

LNG Plant

LNG Infrastructure

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0

0,05

0,1

0,15

0,2

0,25

0,3

0,35

0,4

0,45

0,5

1 2 3 4 5 6 7 8 9 10Years

Daily Production (Hydrocarbon Liquids) Штокман учебный

Production Units

Daily Mm³/day

Annual MMm³/yr

Cumulative MMm³

1 2 3 4 5 6 7 8 9 10

0,235 0,470 0,470 0,470 0,470 0,396 0,278 0,196 0,137 0,097

0,082 0,164 0,164 0,164 0,164 0,139 0,097 0,068 0,048 0,034

0,082 0,247 0,411 0,576 0,740 0,879 0,976 1,045 1,093 1,126

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0

1

2

3

4

5

6

7

8

1 2 3 4 5 6 7 8 9 10Years

Daily Production (Gas) Штокман учебный

Production Units

Daily MMsm³/day

Annual Bsm³/yr

Cumulative Bsm³

1 2 3 4 5 6 7 8 9 10

3,823 7,646 7,646 7,646 7,646 6,442 4,527 3,181 2,236 1,571

1,338 2,676 2,676 2,676 2,676 2,255 1,585 1,113 0,782 0,550

1,338 4,014 6,690 9,366 12,042 14,297 15,881 16,995 17,777 18,327

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0

0,001

0,002

0,003

0,004

0,005

1 2 3 4 5 6 7 8 9 10Years

Daily Production (Water) Штокман учебный

Production Units

Daily Mm³/day

Annual MMm³/yr

Cumulative MMm³

1 2 3 4 5 6 7 8 9 10

0,002 0,005 0,005 0,005 0,005 0,004 0,003 0,002 0,001 0,001

0,001 0,002 0,002 0,002 0,002 0,001 0,001 0,001 0,000 0,000

0,001 0,002 0,004 0,006 0,007 0,009 0,010 0,011 0,011 0,011

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0

0,05

0,1

0,15

0,2

0,25

0,3

0,35

0,4

0,45

0,5

1 2 3 4 5 6 7 8 9 10Years

Daily Production (Gross liquids) Штокман учебный

Production Units

Daily Mm³/day

Annual MMm³/yr

Cumulative MMm³

1 2 3 4 5 6 7 8 9 10

0,237 0,475 0,475 0,475 0,475 0,400 0,281 0,198 0,139 0,098

0,083 0,166 0,166 0,166 0,166 0,140 0,098 0,069 0,049 0,034

0,083 0,249 0,415 0,581 0,748 0,888 0,986 1,055 1,104 1,138

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Project Штокман учебный Currency US Dollars

Location C.I.S.

Development type Gas

Sub total 1 247 245 000

Contingency 203 823 000 Procurement strategy Russia

Project costs 0

Grand total 1 451 068 000

Cost centre Totals Equipment Materials Fabrication Installation H.U. & C. Design Project management Ins. & cert. Contingency

FPSO Preprocessing 355 843 000 94 087 000 26 896 000 71 072 000 0 16 106 000 84 295 000 18 596 000 12 442 000 32 349 000

FPSO Vessel 185 533 000 46 758 000 23 178 000 33 770 000 3 920 000 3 300 000 16 740 000 16 830 000 10 115 000 30 922 000

Oil pipeline (offshore 1) 107 233 000 10 627 000 67 450 000 3 627 000 7 956 000 3 586 000 13 987 000

Gas pipeline (offshore 2) 198 129 000 71 737 000 82 340 000 3 627 000 7 956 000 6 626 000 25 843 000

Gas Offshore Drilling 176 861 000 3 445 000 8 818 000 127 525 000 856 000 1 071 000 5 669 000 29 477 000

Oil Offshore Drilling 144 223 000 2 755 000 6 989 000 104 107 000 763 000 949 000 4 623 000 24 037 000

Gas Risers 156 605 000 45 121 000 21 003 000 41 502 000 11 923 000 5 936 000 5 019 000 26 101 000

Oil Risers 126 641 000 36 060 000 15 483 000 36 172 000 9 170 000 4 590 000 4 059 000 21 107 000

TOTALS 1 451 068 000 228 226 000 184 731 000 104 842 000 463 016 000 19 406 000 131 001 000 63 884 000 52 139 000 203 823 000

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Project Штокман учебный Currency US Dollars

Location C.I.S.

Development type Gas

Sub total 468 884 000

Scrap -15 567 000 Procurement strategy Russia

Grand total 453 317 000

Cost centre Totals Materials Fabrication Decommissioning / removal Design Project management Ins. & cert. Contingency Scrap

FPSO Preprocessing 53 879 000 1 199 000 5 899 000 25 503 000 4 855 000 7 987 000 1 136 000 9 316 000 -2 016 000

FPSO Vessel 1 057 000 4 312 000 -3 255 000

Oil pipeline (offshore 1) 74 626 000 57 171 000 1 562 000 2 570 000 1 533 000 12 567 000 -777 000

Gas pipeline (offshore 2) 99 149 000 84 027 000 1 562 000 2 570 000 2 204 000 18 073 000 -9 287 000

Gas Offshore Drilling 38 258 000 38 258 000 0

Oil Offshore Drilling 31 232 000 31 232 000 0

Gas Risers 82 871 000 83 004 000 -133 000

Oil Risers 72 245 000 72 344 000 -99 000

TOTALS 453 317 000 1 199 000 5 899 000 395 851 000 7 979 000 13 127 000 4 873 000 39 956 000 -15 567 000

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Project Штокман учебный Currency US Dollars

Location C.I.S.

Development type Gas

Sub total 69 686 000

Contingency 16 466 000 Procurement strategy Russia

Project costs 0

Grand total 86 152 000

Cost centre Totals Equipment Materials Prefabrication Construction Design Project management Ins. & cert. Contingency

GTU Plant 9 598 000 3 572 000 1 002 000 349 000 2 071 000 601 000 324 000 79 000 1 600 000

LNG Plant 9 598 000 3 572 000 1 002 000 349 000 2 071 000 601 000 324 000 79 000 1 600 000

LNG Offloading Terminal 3 756 000 1 927 000 274 000 59 000 623 000 134 000 82 000 31 000 626 000

GTU Infrastructure 31 600 000 22 595 000 1 102 000 1 333 000 250 000 6 320 000

LNG Infrastructure 31 600 000 22 595 000 1 102 000 1 333 000 250 000 6 320 000

TOTALS 86 152 000 9 071 000 47 468 000 757 000 4 765 000 3 540 000 3 396 000 689 000 16 466 000

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Project Штокман учебный Currency US Dollars

Location C.I.S.

Development type Gas

Sub total 15 845 000

Scrap -119 000 Procurement str rategy Russia

Grand total 15 726 000

Cost centre Totals Decommissioning / removal Scrap

GTU Plant 3 333 000 3 386 000 -53 000

LNG Plant 3 333 000 3 386 000 -53 000

LNG Offloading Terminal 2 282 000 2 295 000 -13 000

GTU Infrastructure 3 389 000 3 389 000 0

LNG Infrastructure 3 389 000 3 389 000 0

TOTALS 15 726 000 15 845 000 -119 000

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Project Штокман учебный Currency US Dollars

Location C.I.S.

Development type Gas

Sub total 1 316 931 000 Procurement strategy: Of ffshore Russia

Contingency 220 289 000 Procurement strategy: O nshore Russia

Project costs 0

Grand total 1 537 220 000

Cost centre Totals Equipment Materials Fabrication Prefabrication Installation/Construction H.U. & C. Design Project management Ins. & cert. Contingency

FPSO Preprocessing 355 843 000 94 087 000 26 896 000 71 072 000 0 16 106 000 84 295 000 18 596 000 12 442 000 32 349 000

FPSO Vessel 185 533 000 46 758 000 23 178 000 33 770 000 3 920 000 3 300 000 16 740 000 16 830 000 10 115 000 30 922 000

Oil pipeline (offshore 1) 107 233 000 10 627 000 67 450 000 3 627 000 7 956 000 3 586 000 13 987 000

Gas pipeline (offshore 2) 198 129 000 71 737 000 82 340 000 3 627 000 7 956 000 6 626 000 25 843 000

Gas Offshore Drilling 176 861 000 3 445 000 8 818 000 127 525 000 856 000 1 071 000 5 669 000 29 477 000

Oil Offshore Drilling 144 223 000 2 755 000 6 989 000 104 107 000 763 000 949 000 4 623 000 24 037 000

Gas Risers 156 605 000 45 121 000 21 003 000 41 502 000 11 923 000 5 936 000 5 019 000 26 101 000

Oil Risers 126 641 000 36 060 000 15 483 000 36 172 000 9 170 000 4 590 000 4 059 000 21 107 000

GTU Plant 9 598 000 3 572 000 1 002 000 349 000 2 071 000 601 000 324 000 79 000 1 600 000

LNG Plant 9 598 000 3 572 000 1 002 000 349 000 2 071 000 601 000 324 000 79 000 1 600 000

LNG Offloading Terminal 3 756 000 1 927 000 274 000 59 000 623 000 134 000 82 000 31 000 626 000

GTU Infrastructure 31 600 000 22 595 000 1 102 000 1 333 000 250 000 6 320 000

LNG Infrastructure 31 600 000 22 595 000 1 102 000 1 333 000 250 000 6 320 000

TOTALS 1 537 220 000 237 297 000 232 199 000 104 842 000 757 000 467 781 000 19 406 000 134 541 000 67 280 000 52 828 000 220 289 000

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Project Штокман учебный Currency US Dollars

Location C.I.S.

Development type Gas

Sub total 484 729 000 Procurement strategy: Of ffshore Russia

Scrap -15 686 000 Procurement strategy: O nshore Russia

Grand total 469 043 000

Cost centre Totals Materials Fabrication Decommissioning / removal Design Project management Ins. & cert. Contingency Scrap

FPSO Preprocessing 53 879 000 1 199 000 5 899 000 25 503 000 4 855 000 7 987 000 1 136 000 9 316 000 -2 016 000

FPSO Vessel 1 057 000 4 312 000 -3 255 000

GTU Plant 3 333 000 3 386 000 -53 000

LNG Plant 3 333 000 3 386 000 -53 000

Oil pipeline (offshore 1) 74 626 000 57 171 000 1 562 000 2 570 000 1 533 000 12 567 000 -777 000

Gas pipeline (offshore 2) 99 149 000 84 027 000 1 562 000 2 570 000 2 204 000 18 073 000 -9 287 000

LNG Offloading Terminal 2 282 000 2 295 000 -13 000

Gas Offshore Drilling 38 258 000 38 258 000 0

Oil Offshore Drilling 31 232 000 31 232 000 0

GTU Infrastructure 3 389 000 3 389 000 0

LNG Infrastructure 3 389 000 3 389 000 0

Gas Risers 82 871 000 83 004 000 -133 000

Oil Risers 72 245 000 72 344 000 -99 000

TOTALS 469 043 000 1 199 000 5 899 000 411 696 000 7 979 000 13 127 000 4 873 000 39 956 000 -15 686 000

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Project nameCurrency (mi

E & A costCost/boe

Year

TOTAL

123456789

101112131415

boe/bbl Oil 1e Штокман учеебный boe/bbl Conddensate 0,8 Capital cost 1 451,07 Lifecycle cost 2 902,5llions $) US Dollars boe/Mscf Gass 0,17 Cost/boe 12,78 Cost/boe 25,55

0 Drilling cost 321,09 Facilities cost 1 129,98 Operating co st 998,12 Decommissioon cost 453,310 Cost/boe 2,83 Cost/boe 9,95 Cost/boe 8,79 Cost/boe 3,99

Deesign productioon0,21 3,48

PROJECT EXPLORRATION & APPPRAISAL PROD. D DRILLING FACILITIEES COSTS OPERATINNG COSTS CO2 emitted PPRODUCTIONN

PROJECT COSTS Expl. Seismic Apprsl. Tangible Intangible Subsea Pipelines Topsides Structures Floaters Other

facilitiesFixed OPEX

Tariffs Leases CO2 tax DECOMM. 000s te/yr Oil MMm³/yr

Cond. MMm³/yr

Gas Bsm³/yr

1,71 2,67 41,1012,78 0,83 61,25 41,95 138,11 110,6811,77 159,75 222,00 263,41 176,63 74,85 7,09 2,21 0,01 0,11

1,21 130,37 85,25 29,51 0,09 1,4586,65 62,25 0,16 2,68

91,97 62,25 0,16 2,68145,18 62,25 0,16 2,68

88,40 61,17 0,16 2,6497,18 47,94 0,14 2,2090,72 31,16 0,09 1,55

143,45 21,52 0,07 1,0984,72 15,82 0,05 0,7677,51 25,18 11,48 0,03 0,50

302,21125,92

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Project nameCurrency (mi

E & A costCost/boe

Year

TOTAL

123456789

101112131415

boe/bbl Oil 1e Штокман учеебный boe/bbl Conddensate 0,8 Capital cost 86,14 Lifecycle cost 302,23llions $) US Dollars boe/Mscf Gass 0,17 Cost/boe 0 Cost/boe 0

0 Drilling cost 0 Facilities cost 86,14 Operating co st 200,37 Decommissioon cost 15,720 Cost/boe 0 Cost/boe 0 Cost/boe 0 Cost/boe 0

Deesign productioon0,21 348

PROJECT EXPLORRATION & APPPRAISAL PROD. D DRILLING FACILITIEES COSTS OPERATINNG COSTS CO2 emitted PPRODUCTIONN

PROJECT COSTS Expl. Seismic Apprsl. Tangible Intangible Production

facilitiesWellpad groups

Terminals Pipelines Infra-structure

Other facilities

Fixed OPEX

Tariffs Leases CO2 tax DECOMM. 000s te/yr Oil MMm³/yr

Cond. MMm³/yr

Gas Bsm³/yr

1,14 0,10 63,208,36 3,449,69 0,21 1,67 0,13

20,01 1,6020,12 2,30

20,12 2,3020,12 2,3020,12 2,2820,08 2,0320,01 1,66

19,95 1,4019,92 1,2118,25 0,87 1,00

10,484,37

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Project nameCurrency (mi

E & A costCost/boe

Year

TOTAL

1

2

3

4

5

6

7

8

9

10

11

12

13

1415

boe/bbl Oil 1

e Штокман учеебный boe/bbl Conddensate 0,8 Capital cost 1 537,21 Lifecycle costt 3 204,73llions $) US Dollars boe/Mscf Gass 0,17 Cost/boe 13,53 Cost/boe 28,22

0 Drilling cost 321,09 Facilities costt 1 216,12 Operating co st 1 198,49 Decommissioon cost 469,030 Cost/boe 2,83 Cost/boe 10,71 Cost/boe 10,55 Cost/boe 4,13

Deesign productioon0,21 3,48

PROJECT EXPLORRATION & APPPRAISAL PROD. D DRILLING FACCILITIES COSSTS OPERATINNG COSTS CO2 emitted PPRODUCTIONN

PROJECT COSTS Expl. Seismic Apprsl. Tangible Intangible Facilities Pipelines

Other facilities

Fixed OPEX Tariffs Leases CO2 tax

DECOMM.000s te/yr

Oil MMm³/yr

Cond. MMm³/yr

Gas Bsm³/yr

1,71 2,67 105,54

12,78 0,83 321,84 41,95

11,77 159,75 483,38 263,41 8,76 2,34 0,01 0,11

1,21 130,37 105,26 31,11 0,09 1,45106,77 64,55 0,16 2,68

112,09 64,55 0,16 2,68

165,30 64,55 0,16 2,68

108,52 63,45 0,16 2,64

117,26 49,97 0,14 2,20110,73 32,82 0,09 1,55

163,40 22,92 0,07 1,09

104,64 17,03 0,05 0,76

95,76 26,05 12,48 0,03 0,50

312,69130,29

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Warning Field level: Minimum monthly average ambient temperatureBelow water freezing point.

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Rig Subsea wells (floater) Water depth 291 m

Generatioon Second generation semii-sub Reservoir deppth 2 050 m

Profile Build and holdd Reservoir presssure 207 bara

Design pressuure 345 barg

Maximum steppout 3 000 m

Wells Flowwrate Longest stepoout 941 m

Gas prodduction 5 5,52 MMsm³/day Trip speed 300 m/hr

Water inje ection 0 Mm³/day Rate of build d deg/30m 4,00 degrees

Gas injecction 0 MMsm³/day Acid gas No

Exploratioon - Use ESPs No

Total connductors 0 Multilaterals p per production h host 1

Pre-drille d wells 0 Drilling profiles s edited No

Well no. Well function

TVD from LAT

Kick off Horizontal Profile Horizontal Measured Maximum Rig t type Completion Duraationfunction from LAT shift type section depth deviation Drilling Completion Type Platfform Jackk-up Semi-sub

(degrees Drilling Completion Drilling Completion Drilling Completion

from

m m m m m vertical) days days days days days days

1 Prod. 2 050 0 0 Vertical 0 2 050 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,0 14,2

2 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 53,5 17,6

3 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 51,3 17,6

4 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,2 17,6

5 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 44,7 17,6

Total depth

Total p platform Total ja ack-up Total se emi-sub

m daays daays days

11 410 00 00 3330

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Name GGas Offshore Drilling

US D ollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Production xmas tree 0 3 951 400 0

Production wellhead 5 613 100 3 066 000

Production completion 5 43 000 215 000

Production downhole ESPP 0 0 0

Water injection xmas treee 0 3 150 000 0

Water injection wellhead 0 572 500 0

Water injection completioon 0 0 0

Gas injection xmas tree 0 3 150 000 0

Gas injection wellhead 0 572 500 0

Gas injection completion 0 0 0

Sub Total 3 281 000

Freight 5,00% 3281000 164 000

Total Equipment $

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

30 in casing 0 m 1 140 0

20 in casing 500 m 470 235 000

13 3/8 in casing 2 990 m 170 508 000

9 5/8 in casing 7 960 m 120 955 000

7 in liner 2 290 m 71 163 000

5 in tubing 9 950 m 55 547 000

3 1/2 in tubing 0 m 42 0

Cement 9 950 m 71 706 000

Mud 9 950 m 142 1 413 000

Brine 9 950 m 70 697 000

Bits 9 950 m 205 2 040 000

Conductors 0 te 2 050 0

Drilling template 90 te 12 600 1 134 000

Sub Total 8 398 000

Freight 5,00% 8398000 420 000

Total Materials $

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Name GGas Offshore Drilling

US D ollars

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Floating bare rig charter 331 day 266 000 88 046 000

Floating drill crew 331 day 31 200 10 327 000

Floating marine crew 331 day 12 900 4 270 000

Floating consumables 331 day 23 600 7 812 000

Floating helicopter servicces 331 day 5 500 1 821 000

Floating supply boats 331 day 20 700 6 852 000

Floating supply base 331 day 12 700 4 204 000

Specialist service loggingg 0 840 000 0

Specialist service cementing 5 315 000 1 575 000

Specialist service testing 0 415 000 0

Transport 7 day 374 000 2 618 000

Site preparation 0 day 200 000 0

Total Installation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 4 600 mhr 186 856 000

Project management 3 500 mhr 306 1 071 000

Total Design & Project m anagemennt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 141715000 0

Insurance 4,00% 141715000 5 669 000

Total Insurance & Certificcation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 147384000 29 477 000

Total Contingency $

Page 20: Offshore Project Report

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Name GGas Offshore Drilling

US D ollars

CAPITAL COOST % COST

Equipment 3 445 000 0 0

Total Equipment $

CAPITAL COOST % COST

Materials 8 818 000 0 0

Total Materials $

CAPITAL COOST % COST

Installation 127 525 000 30 38 258 000

Total Installation $

CAPITAL COOST % COST

Design & Project manageement 1 927 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 5 669 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 29 477 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 0 te -350 0

Total Scrap steel $

Page 21: Offshore Project Report

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Rig Subsea wells (floater) Water depth 291 m

Generatioon Second generation semii-sub Reservoir deppth 2 050 m

Profile Build and holdd Reservoir presssure 207 bara

Design pressuure 345 barg

Maximum steppout 3 000 m

Wells Flowwrate Longest stepoout 941 m

Gas prodduction 4 4,42 MMsm³/day Trip speed 300 m/hr

Water inje ection 0 Mm³/day Rate of build d deg/30m 4,00 degrees

Gas injecction 0 MMsm³/day Acid gas No

Exploratioon - Use ESPs No

Total connductors 0 Multilaterals p per production h host 1

Pre-drille d wells 0 Drilling profiles s edited No

Well no. Well function

TVD from LAT

Kick off Horizontal Profile Horizontal Measured Maximum Rig t type Completion Duraationfunction from LAT shift type section depth deviation Drilling Completion Type Platfform Jackk-up Semi-sub

(degrees Drilling Completion Drilling Completion Drilling Completion

from

m m m m m vertical) days days days days days days

1 Prod. 2 050 0 0 Vertical 0 2 050 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,0 14,2

2 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 53,5 17,6

3 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 51,3 17,6

4 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,2 17,6

Total depth

Total p platform Total ja ack-up Total se emi-sub

m daays daays days

9 070 00 00 2668

Page 22: Offshore Project Report

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Name Oil Offshore Drilling

US D ollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Production xmas tree 0 3 951 400 0

Production wellhead 4 613 100 2 452 000

Production completion 4 43 000 172 000

Production downhole ESPP 0 0 0

Water injection xmas treee 0 3 150 000 0

Water injection wellhead 0 572 500 0

Water injection completioon 0 0 0

Gas injection xmas tree 0 3 150 000 0

Gas injection wellhead 0 572 500 0

Gas injection completion 0 0 0

Sub Total 2 624 000

Freight 5,00% 2624000 131 000

Total Equipment $

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

30 in casing 0 m 1 140 0

20 in casing 400 m 470 188 000

13 3/8 in casing 2 370 m 170 403 000

9 5/8 in casing 6 320 m 120 758 000

7 in liner 1 820 m 71 129 000

5 in tubing 7 910 m 55 435 000

3 1/2 in tubing 0 m 42 0

Cement 7 910 m 71 562 000

Mud 7 910 m 142 1 123 000

Brine 7 910 m 70 554 000

Bits 7 910 m 205 1 622 000

Conductors 0 te 2 050 0

Drilling template 70 te 12 600 882 000

Sub Total 6 656 000

Freight 5,00% 6656000 333 000

Total Materials $

Page 23: Offshore Project Report

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Name Oil Offshore Drilling

US D ollars

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Floating bare rig charter 269 day 266 000 71 554 000

Floating drill crew 269 day 31 200 8 393 000

Floating marine crew 269 day 12 900 3 470 000

Floating consumables 269 day 23 600 6 348 000

Floating helicopter servicces 269 day 5 500 1 480 000

Floating supply boats 269 day 20 700 5 568 000

Floating supply base 269 day 12 700 3 416 000

Specialist service loggingg 0 840 000 0

Specialist service cementing 4 315 000 1 260 000

Specialist service testing 0 415 000 0

Transport 7 day 374 000 2 618 000

Site preparation 0 day 200 000 0

Total Installation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 4 100 mhr 186 763 000

Project management 3 100 mhr 306 949 000

Total Design & Project m anagemennt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 115563000 0

Insurance 4,00% 115563000 4 623 000

Total Insurance & Certificcation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 120186000 24 037 000

Total Contingency $

Page 24: Offshore Project Report

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Name Oil Offshore Drilling

US D ollars

CAPITAL COOST % COST

Equipment 2 755 000 0 0

Total Equipment $

CAPITAL COOST % COST

Materials 6 989 000 0 0

Total Materials $

CAPITAL COOST % COST

Installation 104 107 000 30 31 232 000

Total Installation $

CAPITAL COOST % COST

Design & Project manageement 1 712 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 4 623 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 24 037 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 0 te -350 0

Total Scrap steel $

Page 25: Offshore Project Report

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From FPSO Preprocessing Export end te ermination details

To Oil Landfall Export compoonent FPSO Preprocessing

Flow type Oil Export end wa ater depth 291 m

Length 120 km Export end te ermination type Riser

Export end te ermination sub-type Flexible lazy S

Pipeline details Export end di verless connections Yes

Material Carbon steel Export end su ubsea ESD valve No

Oil flowrate 0,611 Mm³/day

Water flowrate 0 Mm³/day Export end PL LET

Gas flowrate 0 MMsm³/day Required Yes

Pressure in 103 bara Valve Yes

Pressure out 15 bara Soil Conditionns Average

Fixed pressure Outlet pressure Pressure ratinng 207 barg

Fluid temperature 4 °C Trawler protection No

Buckle arrestors Yes Jumper type Rigid

Size Receiving end d termination details

Nominal diameter 102 mm Receiving com mponent Oil Landfall

Corrosion allowance 3mm Receiving end d water depth -

Wall thickness 6,02 mm Receiving end d termination type Shore approach

Receiving end d termination sub-type Shelving beach

Installation Receiving end d diverless connections -

Lay vessel type S-lay without DP Receiving end d subsea ESD valve No

Pipeline crossings 2

Buried length 5 km Receiving end d PLET

Required -

Specification Valve -

Coating Yes Soil conditionns -

Weight coat No Pressure ratinng -

Cathodic protection Yes Trawler protection -

Insulation material None Jumper type -

Insulation U value -

Page 26: Offshore Project Report

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Name Oil p pipeline (offshore 1)

US D ollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Linepipe 120,00 km 47 743 5 729 000

Coating 120,00 km 22 000 2 640 000

Weight coating 0,00 km 54 000 0

None 0,00 km 0 0

Sub Total 8 369 000

Onshore welding and reelling 0,00% 8369000 0

Anodes 43 te 5 400 232 000

Riser linepipe (D = 10 2 mm) 478 m 1 190 569 000

Riser arch buoy system 1 197 000 197 000

Spools, flanges & fittinngs 1 38 000 38 000

Subsea emergency sh hutdown va alve system 0 230 000 0

Shore approach materials 0 0 0

Subsea emergency sh hutdown va alve system 0 230 000 0

PLETs 1 716 000

Sub Total 10 121 000

Freight 5,00% 10121000 506 000

Total Materials $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Pipelay spread 58 day 520 000 30 160 000

Pipelay spread mob / demmob 20 day 520 000 10 400 000

Diving support vessel tie i ns 34 day 180 000 6 120 000

Diving support vessel test t & commisssioning 11 day 180 000 1 980 000

Diving support vessel mob b / demob 20 day 180 000 3 600 000

Testing & commissioning equipmentt 23 day 50 000 1 150 000

Dredging & rock dumping 0 day 128 000 0

Dredging & rock dumping mob / demmob 0 day 128 000 0

Trenching 2 day 180 000 360 000

Trenching mob / demob 20 day 180 000 3 600 000

Surveying 27 day 128 000 3 456 000

Surveying sail and return 8 day 128 000 1 024 000

Shore approach 5 600 000

Total Installation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 19 500 mhr 186 3 627 000

Project management 26 000 mhr 306 7 956 000

Total Design & Project ma anagementt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 89660000 0

Insurance 4,00% 89660000 3 586 000

Total Insurance & Certificaation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 15,00% 93246000 13 987 000

Total Contingency $

Page 27: Offshore Project Report

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Name Oil pipeline (offsshore 1) PLETs

US D ollars

QUANTITYY UNIT RATE COST

Structure 6 te 39 400 236 000

Valve 1 82 000 82 000

Protection structure 0 te 11 600 0

Mudmat 12 te 2 940 35 000

Jumper (Rigid) 80 m 57 5 000

Jumper connectors 2 179 000 358 000

Total Export end PLET $

QUANTITYY UNIT RATE COST

Structure 0 te 0 0

Valve 0 0 0

Protection structure 0 te 0 0

Mudmat 0 te 0 0

Jumper 0 m 0 0

Jumper connectors 0 0 0

Total Receiving end PLETT $

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Removal

Removal type Complete

Disposal

Dispose Yes

Disposal type Scrap

Distance to disposal site 120 km

Cleaning

Clean Yes

Flushing Yes

Pigging Yes

Chemical Yes

Pipeline details

Flow type Liquids

Material Carbon steel

Buckle arrestors Yes

Length 120 km

Nominal diameter 102 mm

Wall thickness 6,02 mm

Crossings 2

Buried length 5 km

Shore approach Yes

Insulation material None

Insulation U value -

Page 29: Offshore Project Report

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Name Oil p pipeline (offshore 1)

US D ollars

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

DSV 31 day 135 000 4 185 000

Pigging and pumping 29 day 42 000 1 218 000

Flushing and chemicals 38 day 55 000 2 090 000

Jetting 22 day 63 000 1 386 000

Pipelay 60 day 730 000 43 800 000

Tanker 33 day 12 000 396 000

Surveys 32 day 128 000 4 096 000

Waste disposal 0 day 0 0

Total Decommissioning / removal $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 8 400 mhr 186 1 562 000

Project management 8 400 mhr 306 2 570 000

Total Design & project ma anagemennt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 61303000 0

Insurance 2,50% 61303000 1 533 000

Total Insurance & certification $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 62836000 12 567 000

Total Contingency $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Scrap 2 100 te -370 -777 000

Total Scrap $

Page 30: Offshore Project Report

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From FPSO Preprocessing Export end te ermination details

To Gas Landfall Export compoonent FPSO Preprocessing

Flow type Gas Export end wa ater depth 291 m

Length 120 km Export end te ermination type Riser

Export end te ermination sub-type Flexible lazy S

Pipeline details Export end di verless connections Yes

Material Carbon steel Export end su ubsea ESD valve No

Liquid flowrate 0 Mm³/day

Water flowrate 0 Mm³/day Export end PL LET

Gas flowrate 9,94 MMsm³/day Required Yes

Pressure in 113 bara Valve Yes

Pressure out 76 bara Soil Conditionns Average

Fixed pressure Outlet pressure Pressure ratinng 207 barg

Fluid temperature 4 °C Trawler protection No

Buckle arrestors Yes Jumper type Rigid

Size Receiving end d termination details

Nominal diameter 508 mm Receiving com mponent Gas Landfall

Corrosion allowance 3mm Receiving end d water depth -

Wall thickness 15,7 mm Receiving end d termination type Shore approach

Receiving end d termination sub-type Shelving beach

Installation Receiving end d diverless connections -

Lay vessel type S-lay without DP Receiving end d subsea ESD valve No

Pipeline crossings 2

Buried length 5 km Receiving end d PLET

Required -

Specification Valve -

Coating Yes Soil conditionns -

Weight coat Yes Pressure ratinng -

Cathodic protection Yes Trawler protection -

Insulation material None Jumper type -

Insulation U value -

Page 31: Offshore Project Report

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Name Gas p pipeline (offshore 2)

US D ollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Linepipe 120,00 km 397 685 47 722 000

Coating 120,00 km 58 000 6 960 000

Weight coating 120,00 km 58 000 6 960 000

None 0,00 km 0 0

Sub Total 61 642 000

Onshore welding and reelling 0,00% 61642000 0

Anodes 192 te 5 400 1 037 000

Riser linepipe (D = 50 8 mm) 478 m 4 450 2 127 000

Riser arch buoy system 1 540 000 540 000

Spools, flanges & fittinngs 1 390 000 390 000

Subsea emergency sh hutdown va alve system 0 2 350 000 0

Shore approach materials 0 0 0

Subsea emergency sh hutdown va alve system 0 2 350 000 0

PLETs 1 2 585 000

Sub Total 68 321 000

Freight 5,00% 68321000 3 416 000

Total Materials $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Pipelay spread 82 day 520 000 42 640 000

Pipelay spread mob / demmob 20 day 520 000 10 400 000

Diving support vessel tie i ns 41 day 180 000 7 380 000

Diving support vessel test t & commisssioning 16 day 180 000 2 880 000

Diving support vessel mob b / demob 20 day 180 000 3 600 000

Testing & commissioning equipmentt 28 day 50 000 1 400 000

Dredging & rock dumping 0 day 128 000 0

Dredging & rock dumping mob / demmob 0 day 128 000 0

Trenching 2 day 180 000 360 000

Trenching mob / demob 20 day 180 000 3 600 000

Surveying 27 day 128 000 3 456 000

Surveying sail and return 8 day 128 000 1 024 000

Shore approach 5 600 000

Total Installation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 19 500 mhr 186 3 627 000

Project management 26 000 mhr 306 7 956 000

Total Design & Project ma anagementt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 165660000 0

Insurance 4,00% 165660000 6 626 000

Total Insurance & Certificaation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 15,00% 172286000 25 843 000

Total Contingency $

Page 32: Offshore Project Report

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Name Gas pipeline (offfshore 2) PLETs

US D ollars

QUANTITYY UNIT RATE COST

Structure 24 te 39 400 946 000

Valve 1 397 000 397 000

Protection structure 0 te 11 600 0

Mudmat 52 te 2 940 153 000

Jumper (Rigid) 80 m 532 43 000

Jumper connectors 2 523 000 1 046 000

Total Export end PLET $

QUANTITYY UNIT RATE COST

Structure 0 te 0 0

Valve 0 0 0

Protection structure 0 te 0 0

Mudmat 0 te 0 0

Jumper 0 m 0 0

Jumper connectors 0 0 0

Total Receiving end PLETT $

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Removal

Removal type Complete

Disposal

Dispose Yes

Disposal type Scrap

Distance to disposal site 120 km

Cleaning

Clean Yes

Flushing Yes

Pigging Yes

Chemical Yes

Pipeline details

Flow type Gas

Material Carbon steel

Buckle arrestors Yes

Length 120 km

Nominal diameter 508 mm

Wall thickness 15,7 mm

Crossings 2

Buried length 5 km

Shore approach Yes

Insulation material None

Insulation U value -

Page 34: Offshore Project Report

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Name Gas p pipeline (offshore 2)

US D ollars

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

DSV 31 day 135 000 4 185 000

Pigging and pumping 44 day 42 000 1 848 000

Flushing and chemicals 68 day 55 000 3 740 000

Jetting 24 day 63 000 1 512 000

Pipelay 93 day 730 000 67 890 000

Tanker 63 day 12 000 756 000

Surveys 32 day 128 000 4 096 000

Waste disposal 0 day 0 0

Total Decommissioning / removal $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 8 400 mhr 186 1 562 000

Project management 8 400 mhr 306 2 570 000

Total Design & project ma anagemennt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 88159000 0

Insurance 2,50% 88159000 2 204 000

Total Insurance & certification $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 90363000 18 073 000

Total Contingency $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Scrap 25 100 te -370 -9 287 000

Total Scrap $

Page 35: Offshore Project Report

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PR

TS

Link 011,34 km

PRLink 021,34 km

Riser base 01

Item 01Item 02

Cluster 4 1,34 km No -

S-lay without DP Steel No

Carbon steel - - Carbon steel - -

None - - None - -

- - - - - -

Yes - - Yes - -

Electro-hydraulic Duplex Yes No

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Cluster 4 0 0 0 4 291 m Yes No No

Satellite 1 0 0 0 1 291 m No No No

291 m Riser Flexible lazy S 1 478 m

1,34 km 291 m

1,34 km 291 m

Production 0,271 Mm³/day 0,00274 Mm³/day 4,42 MMsm³/day

Production 0,0679 Mm³/day 0,000686 Mm³/day 1,1 MMsm³/day

Production 1 Carbon steel Yes Yes Yes None -

Test service 1 Carbon steel Yes No Yes None -

Production 1 Carbon steel Yes No Yes None -

Production 1 Item 01 Yes Yes Average 207 barg No Rigid

Test service 1 Item 01 Yes Yes Average 207 barg No Rigid

Production 1 Item 02 Yes Yes Average 207 barg No Rigid

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Page 38: Offshore Project Report

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Name Gas Risers

US D ollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Item 01 30 918 000

Item 02 7 199 000

Riser base 01 3 523 000

Platform controls - main 1 516 000 516 000

Platform controls - additional 5 82 100 411 000

Sub Total 42 567 000

Freight 6,00% 42567000 2 554 000

Total Equipment $

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Link 01 8 202 000

Link 02 3 004 000

Riser 01 8 097 000

Riser systems ( arch/buoy y ) 1 700 000 700 000

Sub Total 20 003 000

Freight 5,00% 20003000 1 000 000

Total Materials $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Semi-submersible crane v vessel 0 day 690 000 0

Semi-submersible drilling vessel 21 day 370 000 7 770 000

Pipelay spread ( S-lay without DP ) 41 day 520 000 21 320 000

Diving support vessel tie i ns 49 day 180 000 8 820 000

Diving support vessel test t & commisssioning 8 day 180 000 1 440 000

Testing & commissioning equipmentt 20 day 50 000 1 000 000

Dredging & rock dumping 0 day 128 000 0

Trenching 0 day 180 000 0

Surveying 9 day 128 000 1 152 000

Total Installation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 64 100 mhr 186 11 923 000

Project management 19 400 mhr 306 5 936 000

Total Design & Project ma anagementt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 125485000 0

Insurance 4,00% 125485000 5 019 000

Total Insurance & Certificaation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 130504000 26 101 000

Total Contingency $

Page 39: Offshore Project Report

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Name Item 01

US D ollars

QUANTITYY UNIT RATE COST

Structure 60 te 12 915 775 000

Protection structure 0 te 11 555 0

Piles 35 te 3 979 139 000

Total Main structure $

QUANTITYY UNIT RATE COST

Production 4 3 951 400 15 806 000

Water injection 0 3 150 000 0

Gas injection 0 3 150 000 0

Total Xmas trees $

QUANTITYY UNIT RATE COST

Production 10 te 72 210 722 000

Test 4 te 72 210 289 000

Total Manifolding (piping & valves) $

QUANTITYY UNIT RATE COST

152 mm 8 265 000 2 120 000

203 mm 1 320 000 320 000

305 mm 1 445 000 445 000

Umbilical / flying lead connnectors 17 132 000 2 244 000

Total Connectors / pull-inns $

QUANTITYY UNIT RATE COST

Guide base 4 381 700 1 527 000

Protection structure 0 te 11 555 0

Well jumpers - 4 x (D = 15 52 mm) 120 m 920 110 000

Hydraulic flying leads (x 4 4) 120 m 2 900 348 000

Electrical flying leads (x 4 4) 120 m 80 10 000

Total Cluster satellites $

QUANTITYY UNIT RATE COST

Subsea controls 4 1 468 500 5 874 000

System testing 4 47 300 189 000

Total Control and testing $

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Name Item 02

US D ollars

QUANTITYY UNIT RATE COST

Structure 40 te 12 915 517 000

Guide base 1 381 700 382 000

Protection structure 0 te 11 555 0

Total Main structure $

QUANTITYY UNIT RATE COST

Production 1 3 951 400 3 951 000

Water injection 0 3 150 000 0

Gas injection 0 3 150 000 0

Total Xmas trees $

QUANTITYY UNIT RATE COST

152 mm 1 265 000 265 000

Umbilical / flying lead connnectors 5 132 000 660 000

Total Connectors / pull-inns $

QUANTITYY UNIT RATE COST

Hydraulic (x 1) 30 m 2 900 87 000

Electrical (x 1) 30 m 80 2 000

Total Flying leads $

QUANTITYY UNIT RATE COST

Subsea controls 1 1 335 000 1 335 000

Total Control $

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Name Link 01

US D ollars

QUANTITYY UNIT RATE COST

Linepipe - 1 x (D = 305 m mm, t = 11,1 1 mm, Carboon steel) 1,34 km 249 000 334 000

Coating 1,34 km 36 500 49 000

Weight coat 1,34 km 54 000 72 000

Anodes 1,40 te 5 400 8 000

Subsea crossings 0 650 000 0

PLETs 2 2 932 000

Total Production flowline $

QUANTITYY UNIT RATE COST

Linepipe - 1 x (D = 203 m mm, t = 8,48 8 mm, Carboon steel) 1,34 km 128 400 172 000

Coating 1,34 km 28 500 38 000

Anodes 0,90 te 5 400 5 000

Subsea crossings 0 650 000 0

PLETs 2 2 114 000

Total Test service flowlinee $

QUANTITYY UNIT RATE COST

4 x D = 19 mm 5,36 km 69 000 370 000

4 x D = 19 mm 5,36 km 69 000 370 000

4 x XSA = 2,5 mm² 5,36 km 9 200 49 000

2 x XSA = 25 mm² 2,68 km 108 000 289 000

UTA 1 1 400 000 1 400 000

Total Umbilicals $

Page 42: Offshore Project Report

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Licence number: N/A Page 42 N/A

Name Link 01 Productiion flowline PLETs

US D ollars

QUANTITYY UNIT RATE COST

Structure 12 te 39 400 473 000

Valve 1 181 000 181 000

Protection structure 0 te 11 600 0

Mudmat 24 te 2 940 71 000

Jumper (Rigid) 80 m 257 21 000

Jumper connectors 2 360 000 720 000

Total Well end PLET $

QUANTITYY UNIT RATE COST

Structure 12 te 39 400 473 000

Valve 1 181 000 181 000

Protection structure 0 te 11 600 0

Mudmat 24 te 2 940 71 000

Jumper (Rigid) 80 m 257 21 000

Jumper connectors 2 360 000 720 000

Total Tie-back end PLET $

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Name Link 01 Test serrvice flowline PLETs

US D ollars

QUANTITYY UNIT RATE COST

Structure 9 te 39 400 355 000

Valve 1 122 000 122 000

Protection structure 0 te 11 600 0

Mudmat 17 te 2 940 50 000

Jumper (Rigid) 80 m 122 10 000

Jumper connectors 2 260 000 520 000

Total Well end PLET $

QUANTITYY UNIT RATE COST

Structure 9 te 39 400 355 000

Valve 1 122 000 122 000

Protection structure 0 te 11 600 0

Mudmat 17 te 2 940 50 000

Jumper (Rigid) 80 m 122 10 000

Jumper connectors 2 260 000 520 000

Total Tie-back end PLET $

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Name Link 02

US D ollars

QUANTITYY UNIT RATE COST

Linepipe - 1 x (D = 152 m mm, t = 7,21 1 mm, Carboon steel) 1,34 km 83 500 112 000

Coating 1,34 km 25 000 34 000

Anodes 0,70 te 5 400 4 000

Subsea crossings 0 650 000 0

PLETs 2 1 708 000

Total Production flowline $

QUANTITYY UNIT RATE COST

4 x D = 9,52 mm 5,36 km 39 000 209 000

4 x D = 9,52 mm 5,36 km 39 000 209 000

4 x XSA = 2,5 mm² 5,36 km 9 200 49 000

2 x XSA = 25 mm² 2,68 km 108 000 289 000

UTA 1 390 000 390 000

Total Umbilicals $

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Name Link 02 Productiion flowline PLETs

US D ollars

QUANTITYY UNIT RATE COST

Structure 7 te 39 400 276 000

Valve 1 100 000 100 000

Protection structure 0 te 11 600 0

Mudmat 14 te 2 940 41 000

Jumper (Rigid) 80 m 86 7 000

Jumper connectors 2 215 000 430 000

Total Well end PLET $

QUANTITYY UNIT RATE COST

Structure 7 te 39 400 276 000

Valve 1 100 000 100 000

Protection structure 0 te 11 600 0

Mudmat 14 te 2 940 41 000

Jumper (Rigid) 80 m 86 7 000

Jumper connectors 2 215 000 430 000

Total Tie-back end PLET $

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Name Riser 01

US D ollars

QUANTITYY UNIT RATE COST

Riser linepipe (D = 15 52 mm) 478 m 1 690 808 000

Riser arch buoy systeems 0 0 0

Spools, flanges & fittings 1 77 000 77 000

Subsea emergency s hutdown v valve system 1 480 000 480 000

Riser linepipe (D = 30 05 mm) 478 m 3 600 1 721 000

Riser arch buoy systeems 0 0 0

Spools, flanges & fittings 1 215 000 215 000

Subsea emergency s hutdown v valve system 1 1 400 000 1 400 000

Riser linepipe (D = 20 03 mm) 478 m 2 150 1 028 000

Riser arch buoy systeems 0 0 0

Spools, flanges & fittings 1 108 000 108 000

Subsea emergency s hutdown v valve system 1 800 000 800 000

Total Flowline risers $

QUANTITYY UNIT RATE COST

4 x D = 9,52 mm 1 912 m 49 94 000

4 x D = 19 mm 1 912 m 90 172 000

4 x D = 9,52 mm 1 912 m 49 94 000

4 x D = 19 mm 1 912 m 90 172 000

8 x XSA = 2,5 mm² 3 824 m 30 115 000

4 x XSA = 25 mm² 1 912 m 425 813 000

Total Umbilical risers $

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Name Riser base 01

US D ollars

QUANTITYY UNIT RATE COST

Structure 20 te 12 915 258 000

Protection structure 0 te 11 555 0

Piles 15 te 3 979 60 000

Total Main structure $

QUANTITYY UNIT RATE COST

Production 3 te 72 210 217 000

Total Manifolding (piping & valves) $

QUANTITYY UNIT RATE COST

152 mm 2 265 000 530 000

203 mm 2 320 000 640 000

305 mm 2 445 000 890 000

Umbilical connectors 4 132 000 528 000

Total Connectors / pull-inns $

QUANTITYY UNIT RATE COST

Subsea controls 400 000

Total Control $

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Name Gas Risers

US D ollars

CAPITAL COOST % COST

Equipment 45 121 000 0 0

Total Equipment $

CAPITAL COOST % COST

Materials 21 003 000 0 0

Total Materials $

CAPITAL COOST % COST

Installation 41 502 000 200 83 004 000

Total Installation $

CAPITAL COOST % COST

Design & Project manageement 17 859 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 5 019 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 26 101 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 380 te -350 -133 000

Total Scrap steel $

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PR

TS

Link 011,34 km

Riser base 01

Item 01

Cluster 4 1,34 km No -

S-lay without DP Steel No

Carbon steel - - Carbon steel - -

None - - None - -

- - - - - -

Yes - - Yes - -

Electro-hydraulic Duplex Yes No

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Cluster 4 0 0 0 4 291 m Yes No No

291 m Riser Flexible lazy S 1 478 m

1,34 km 291 m

Production 0,271 Mm³/day 0,00274 Mm³/day 4,42 MMsm³/day

Production 1 Carbon steel Yes Yes Yes None -

Test service 1 Carbon steel Yes No Yes None -

Production 1 Item 01 Yes Yes Average 207 barg No Rigid

Test service 1 Item 01 Yes Yes Average 207 barg No Rigid

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Name Oil Risers

US D ollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Item 01 30 918 000

Riser base 01 2 251 000

Platform controls - main 1 516 000 516 000

Platform controls - additioonal 4 83 600 334 000

Sub Total 34 019 000

Freight 6,00% 34019000 2 041 000

Total Equipment $

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Link 01 8 202 000

Riser 01 6 079 000

Riser systems ( arch/buo y ) 1 465 000 465 000

Sub Total 14 746 000

Freight 5,00% 14746000 737 000

Total Materials $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Semi-submersible crane vessel 0 day 690 000 0

Semi-submersible drilling g vessel 18 day 370 000 6 660 000

Pipelay spread ( S-lay wit thout DP ) 36 day 520 000 18 720 000

Diving support vessel tie ins 40 day 180 000 7 200 000

Diving support vessel tes st & commissioning 8 day 180 000 1 440 000

Testing & commissioning g equipmennt 20 day 50 000 1 000 000

Dredging & rock dumpingg 0 day 128 000 0

Trenching 0 day 180 000 0

Surveying 9 day 128 000 1 152 000

Total Installation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 49 300 mhr 186 9 170 000

Project management 15 000 mhr 306 4 590 000

Total Design & Project m anagemennt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 101475000 0

Insurance 4,00% 101475000 4 059 000

Total Insurance & Certificcation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 105534000 21 107 000

Total Contingency $

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Name Item 01

US D ollars

QUANTITYY UNIT RATE COST

Structure 60 te 12 915 775 000

Protection structure 0 te 11 555 0

Piles 35 te 3 979 139 000

Total Main structure $

QUANTITYY UNIT RATE COST

Production 4 3 951 400 15 806 000

Water injection 0 3 150 000 0

Gas injection 0 3 150 000 0

Total Xmas trees $

QUANTITYY UNIT RATE COST

Production 10 te 72 210 722 000

Test 4 te 72 210 289 000

Total Manifolding (piping & valves) $

QUANTITYY UNIT RATE COST

152 mm 8 265 000 2 120 000

203 mm 1 320 000 320 000

305 mm 1 445 000 445 000

Umbilical / flying lead connnectors 17 132 000 2 244 000

Total Connectors / pull-inns $

QUANTITYY UNIT RATE COST

Guide base 4 381 700 1 527 000

Protection structure 0 te 11 555 0

Well jumpers - 4 x (D = 15 52 mm) 120 m 920 110 000

Hydraulic flying leads (x 4 4) 120 m 2 900 348 000

Electrical flying leads (x 4 4) 120 m 80 10 000

Total Cluster satellites $

QUANTITYY UNIT RATE COST

Subsea controls 4 1 468 500 5 874 000

System testing 4 47 300 189 000

Total Control and testing $

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Name Link 01

US D ollars

QUANTITYY UNIT RATE COST

Linepipe - 1 x (D = 305 m mm, t = 11,1 1 mm, Carboon steel) 1,34 km 249 000 334 000

Coating 1,34 km 36 500 49 000

Weight coat 1,34 km 54 000 72 000

Anodes 1,40 te 5 400 8 000

Subsea crossings 0 650 000 0

PLETs 2 2 932 000

Total Production flowline $

QUANTITYY UNIT RATE COST

Linepipe - 1 x (D = 203 m mm, t = 8,48 8 mm, Carboon steel) 1,34 km 128 400 172 000

Coating 1,34 km 28 500 38 000

Anodes 0,90 te 5 400 5 000

Subsea crossings 0 650 000 0

PLETs 2 2 114 000

Total Test service flowlinee $

QUANTITYY UNIT RATE COST

4 x D = 19 mm 5,36 km 69 000 370 000

4 x D = 19 mm 5,36 km 69 000 370 000

4 x XSA = 2,5 mm² 5,36 km 9 200 49 000

2 x XSA = 25 mm² 2,68 km 108 000 289 000

UTA 1 1 400 000 1 400 000

Total Umbilicals $

Page 54: Offshore Project Report

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Name Link 01 Productiion flowline PLETs

US D ollars

QUANTITYY UNIT RATE COST

Structure 12 te 39 400 473 000

Valve 1 181 000 181 000

Protection structure 0 te 11 600 0

Mudmat 24 te 2 940 71 000

Jumper (Rigid) 80 m 257 21 000

Jumper connectors 2 360 000 720 000

Total Well end PLET $

QUANTITYY UNIT RATE COST

Structure 12 te 39 400 473 000

Valve 1 181 000 181 000

Protection structure 0 te 11 600 0

Mudmat 24 te 2 940 71 000

Jumper (Rigid) 80 m 257 21 000

Jumper connectors 2 360 000 720 000

Total Tie-back end PLET $

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Name Link 01 Test serrvice flowline PLETs

US D ollars

QUANTITYY UNIT RATE COST

Structure 9 te 39 400 355 000

Valve 1 122 000 122 000

Protection structure 0 te 11 600 0

Mudmat 17 te 2 940 50 000

Jumper (Rigid) 80 m 122 10 000

Jumper connectors 2 260 000 520 000

Total Well end PLET $

QUANTITYY UNIT RATE COST

Structure 9 te 39 400 355 000

Valve 1 122 000 122 000

Protection structure 0 te 11 600 0

Mudmat 17 te 2 940 50 000

Jumper (Rigid) 80 m 122 10 000

Jumper connectors 2 260 000 520 000

Total Tie-back end PLET $

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Name Riser 01

US D ollars

QUANTITYY UNIT RATE COST

Riser linepipe (D = 30 05 mm) 478 m 3 600 1 721 000

Riser arch buoy systeems 0 0 0

Spools, flanges & fittings 1 215 000 215 000

Subsea emergency s hutdown v valve system 1 1 400 000 1 400 000

Riser linepipe (D = 20 03 mm) 478 m 2 150 1 028 000

Riser arch buoy systeems 0 0 0

Spools, flanges & fittings 1 108 000 108 000

Subsea emergency s hutdown v valve system 1 800 000 800 000

Total Flowline risers $

QUANTITYY UNIT RATE COST

4 x D = 19 mm 1 912 m 90 172 000

4 x D = 19 mm 1 912 m 90 172 000

4 x XSA = 2,5 mm² 1 912 m 30 57 000

2 x XSA = 25 mm² 956 m 425 406 000

Total Umbilical risers $

Page 57: Offshore Project Report

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Name Riser base 01

US D ollars

QUANTITYY UNIT RATE COST

Structure 10 te 12 915 129 000

Protection structure 0 te 11 555 0

Piles 7 te 3 979 28 000

Total Main structure $

QUANTITYY UNIT RATE COST

203 mm 2 320 000 640 000

305 mm 2 445 000 890 000

Umbilical connectors 2 132 000 264 000

Total Connectors / pull-inns $

QUANTITYY UNIT RATE COST

Subsea controls 300 000

Total Control $

Page 58: Offshore Project Report

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Name Oil Risers

US D ollars

CAPITAL COOST % COST

Equipment 36 060 000 0 0

Total Equipment $

CAPITAL COOST % COST

Materials 15 483 000 0 0

Total Materials $

CAPITAL COOST % COST

Installation 36 172 000 200 72 344 000

Total Installation $

CAPITAL COOST % COST

Design & Project manageement 13 760 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 4 059 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 21 107 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 283 te -350 -99 000

Total Scrap steel $

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Tanker type Conversion

Tanker size (k dwt) Panamax, 0 - 73

Water depth 291 m

Production ratee 0,611 Mm³/day

Water injection n rate 0 Mm³/day

Gas export / in njection ratee 9,94 MMsm³/day

Days of storagge 10 day

Number of riseers 5

General upgraade 100 te

Marine upgradde 200 te

Tanker strengtthening 595 te

Length of sea trials 15 day

Mooring optionn Buoyant turret

Added producttion facilities s weight 7010 te

Elevated deck Yes

Gas lift No

Mooring type Chain

Anchor type Drag embedded

Soil condition Average

Environment c conditions Severe

Wave height 32,2 m

Wind speed 54,5 m/s

Tidal current 0,2 m/s

Mooring chain size 127 mm

Number of mooring lines 6

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Name FPSO Vessel

US D Dollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Vessel purchase 29 000 000

6 inch swivels 1 4 600 000 4 600 000

12 inch swivels 1 9 300 000 9 300 000

Disconnect 5 600 000 3 000 000

Anchors (drag embedded)) 78 te 11 000 858 000

Total Equipment $

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Tanker strengthening 595 te 1 710 1 017 000

Marine / offloading 200 te 33 000 6 600 000

General upgrade 100 te 13 800 1 380 000

Mooring chain (127 mm) 5 389 m 1 170 6 305 000

Mooring other 0 m 355 0

Mooring terminations 0 34 000 0

Frame / mooring arm 200 te 2 600 520 000

Turret / riser 400 te 3 400 1 360 000

Chain table / buoy 500 te 5 900 2 950 000

Riser porch (no. risers) 0 390 000 0

Elevated deck 1 051 te 1 650 1 734 000

Sub Total 21 866 000

Freight 6,00% 21866000 1 312 000

Total Materials $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Tanker strengthening 595 te 9 240 5 498 000

Marine / offloading 200 te 11 600 2 320 000

General upgrade 100 te 10 400 1 040 000

Turret 1 100 te 10 800 11 880 000

Riser porch (no. risers) 0 103 400 0

Elevated deck 1 051 te 12 400 13 032 000

Total Fabrication $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Mob / Demob and tow outt 10 day 245 000 2 450 000

Installation 6 day 245 000 1 470 000

Total Installation $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Sea trials and marine commmissioningg 15 day 220 000 3 300 000

Total Hook-up & commisssioning $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 90 000 mhr 186 16 740 000

Project management 55 000 mhr 306 16 830 000

Total Design & Project ma anagement $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 144496000 0

Insurance 7,00% 144496000 10 115 000

Total Insurance & Certificaation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 154611000 30 922 000

Total Contingency $

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US Dollars

QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST

PER PER

UNIT MAN HOUR

Tanker strengthening 595 te 154 91 630 60 9 240 5 498 000

Marine / offloading 200 te 194 38 800 60 11 600 2 320 000

General upgrade 100 te 174 17 400 60 10 400 1 040 000

Turret 1 100 te 179 197 200 60 10 800 11 880 000

Riser porch (no. riserss) 0 1 723 0 60 103 400 0

Elevated deck 1 051 te 206 216 507 60 12 400 13 032 000

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Name FPSO Vessel

US D ollars

CAPITAL COOST % COST

Equipment 46 758 000 0 0

Total Equipment $

CAPITAL COOST % COST

Materials 23 178 000 0 0

Total Materials $

CAPITAL COOST % COST

Fabrication 33 770 000 0 0

Total Fabrication $

CAPITAL COOST % COST

Installation 3 920 000 110 4 312 000

Total Installation $

CAPITAL COOST % COST

Hook-up & commissioning 3 300 000 0 0

Total Hook-up & commisssioning $

CAPITAL COOST % COST

Design & Project manageement 33 570 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 10 115 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 30 922 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 9 300 te -350 -3 255 000

Total Scrap steel $

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Facilities: CPQW

Oil / condensate cappacity 0,611 Mm³/day Gas export / flarre cap. 9,94 MMsm³/day

Water injection capaacity 0 Mm³/day Gas injection ca apacity 0 MMsm³/day

Gas lift capacityy 0 MMsm³/day

Oil to: Pipeline to shore Gas to: Pipeline to shore

Distance: 120 km Distance: 120 km

Oil/condensate API 0,786 s.g. Substructure typ pe Tanker

CO2 content: 0 % Substructure su b type Conversion

H2S content: 0 ppm Configuration Pre-assembled units

Acid gas / HP / HT: No Nominal module e weight -

Integrate existinng systems Yes

Manifolding Platform wells Remote wells Risers Op. press. Des. press. Weight

Production wells: 0 9 3 80 bara 215 barg 10,8 te

Water injection wellss: 0 0 0 - - -

Gas injection wells: 0 0 0 - - -

Gas lift wells: 0 0 0 - - -

Test manifold/separaator: - - -

Well kill: 207 bara 223 barg 1,4 te

Control package: 1 te

Hydraulic power unitt: 0,6 te

Well bays: 1

Oil processing Trains Des. cap./train Pressure Temp. out Wt / train Duty Type

Separator 1 1 100% 80 bara 15,6 °C 80,8 te 3 Phase (Horizontal)

Separator 2 1 100% 15 bara 70 °C 3,6 te 3 Phase (Horizontal)

Separator 3 - - - - - -

Test separator - - - - - -

Dehydrator - - - - - - -

Desalter - - - - - - -

Stabiliser - - - - -

Heat exchanger 1 - 80 bara 70 °C 2,8 te 2,08 MW Shell & tube

Heat exchanger 2 - 15 bara 50 °C 1,9 te -0,586 MW Shell & tube

Heat exchanger 3 - - - - - -

Heat exchanger 4 - - - - - -

Oil export Pipe size Capacity Power Type Pumps x duty/pump

Export pumps 120 km x 102 mm 0,611 Mm³/day 0,0851 MW Electric 2 100,00%

Pump discharge presssure 103 bara Pipeline outlet presssure 15 bara Fixed pressure Outlet pressure

Metering Yes Derating factor - Derating based on -

Driver model - Driver rating - Derated power -

Gas processing Capacity Trains x duty Process Specification

Gas cooling - - Shell and tube 41 °C -

Acid gas removal - - - - -

Gas dehydration 9,77 MMsm³/day 2 x 50% Cold finger -21,7 °C 70 bara

Dewpoint control 9,77 MMsm³/day 1 x 100% Expander -20 °C -

Stabiliser - - Gas metering: Yes

Gas compression Capacity Suction p Discharge p Power Model Comp. x duty/comp.

Flash gas compression: - - - 0,792 MW - 1 x 100%

Export gas: 9,94 MMsm³/day 59,8 bara 113 bara 9,85 MW Solar Mars 100 2 x 100%

Lift gas: - - - - - -

Gas injection: - - - - - -

Ambient temperaturee 22 °C Derating factor 0,91

Pipeline size: 120 km x 508 mm Pipeline outlet presssure: 76 bara Fixed pressure Outlet pressure

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Compressor weights (te) Compressors Scrubbers Shell & tube Fin fan Totals

coolers coolers

Flash gas compression: 9,1 te 1,2 te 1,7 te - 11,9 te

Export gas: 137,2 te 43,9 te 33,1 te - 214,2 te

Lift gas: - - - - -

Gas injection: - - - - -

Water injection Weights

Number of pumps - Driver type - Capacity - Pump -

Duty / pump - Driver model - Discharge p - Pump driver -

Derating factor - Derated power - Pump duty - Fine filter -

Fine filters - Deaerator - Deaerator -

Control & communicaations

Control: Conventional control Operational voice r adio: Yes Cable: No

Monitoring: Remote moonitoring Entertainment and TV: No Microwave: Yes

PABX telephone: No Satellite: No

Drilling

No. of drilling rigs: - Tender assisted: - Power: -

Quarters

No. of beds: 64 Cabin size: Two man Helideck weight: 50 te

Quarters upgrade: No Helideck: Existing

Process utilities Design capacities Weight Weight Weight

Produced water: 0,00617 Mm³/day 1 te Closed drains: 18 te Mech. handling: 97,3 te

Heating medium: 2,29 MW 7,1 te Open drains: 3,6 te HVAC: 1,8 te

Cooling medium: 21,6 MW 63 te Diesel storage: 1 te Lifeboats: 11,7 te

Flare and vent: 9,94 MMsm³/day 34,1 te Aviation fuel: 15 te

Seawater lift: 15,2 Mm³/day 16 te Inst & plant air: 2,4 te

Fuel gas: 8,4 te Inert gas: 15,2 te

Chemical inj and storrage: 5,3 te Potable water: 8,2 te

Sewage treatment: 2,6 te

Firefighting: 11,7 te

Other: -

Flare

Flare type: Boom Structure weight: 243,2 te Gas rate: 9,94 MMsm³/day

Tower type: -

Power generation

Oil processing 0 MW Base load 0 MW

Oil export pumps 0,0851 MW Total demand 3,29 MW

Gas processing

Gas cooling 0 MW Emergency power 0 MW

Gas dehydration 0,382 MW

Acid gas removal 0 MW

Dewpoint control 0 MW Generation and distribution

Stabilisation 0 MW Ambient temperaturee 22 °C

Gas compression Derating factor 0,909

Flash gas compressoors 0,808 MW Total power (derated) 3,62 MW

Export compressors 0,197 MW Design factor 1,2

Gas lift compressors 0 MW Design power 4,35 MW

Gas injection compreessors 0 MW Number of generatorrs 2Others Design duty/generatoor % 100,00%

Water injection 0 MW Driver type Turbine

Custom equipment 0 MW Model Solar Centaur 50

Quarters 0,293 MW Driver power 4,6 MW

Drilling 0 MW Generator set weightt 77,8 te

Downhole equipmentt 0 MW Distribution weight 54,8 te

Utilities 1,32 MW Emergency power we eight 0 te

Seawater lift 0,21 MW

Hookup and commisssioning Atshore % Inshore % Offshore %

Manhours split 80 0 20

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2

3

1

4

6

7

5

8

9

Sep 1

Heat Ex 1 Sep 2

Run Down Cooler

80 15,6 1,92 0,00633 9,56 0,688 17,7

80 15,6 - 0,00248 - - -

80 15,6 - - 9,56 - 17,7

80 15,6 1,92 0,00385 - 0,688 -

79,5 70 1,93 0,00365 0,0702 0,653 20,1

15 70 - - - - -

15 70 - - 0,213 - 24,1

15 70 1,6 0,000531 - 0,693 -

14,5 50 1,56 0,000525 - 0,71 -

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Selexol

Number of trains 1

%Design cap/train 100

H2S 4 ppm

CO2 2,5 %

Stabiliser

9

7

5421

WaterGas metering

Gas product spec. Gas Grid

Expander

Number of trains 1

Design cap/train 100

-20 °C

Dewpoint control

Cold finger

Number of trains 2

%Design cap/train 50

Pressure 70 bara

24 kg/MMsm³

-21,7 °CDewpt

Water

DehydrationAcid gas removalCooling

Coolant inlet temp.

8 °C

Ambient air temp.

22 °C

Shell & tube

Fin fan

41 °C

9,77 9,77 9,77 9,77 - - 9,73 - MMsm³/day

- - - - 0,137 0,137 - 1,56 Mm³/day

17,2 17,2 17,2 17,2 7,21 7,21 1,17 50 °C

80 80 80 79 8 8 59,8 14,5 bara

0 0 0 0 0 0 0 0 %

0 0 0 0 0 0 0 0 ppm

17,8 17,8 17,8 17,8 - - 17,6 -

- - - - 0,73 0,73 - 0,711 s.g.

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Name FPSO Preprocessing

US D ollars

(7 007 te Op.)

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Manifolding 14 te 20 500 287 000

Separation 84 te 24 000 2 016 000

Dehydration 0 te 29 000 0

Heating 3 te 31 000 93 000

Shell & tube cooling 2 te 27 500 55 000

Fin fan cooling 0 te 14 800 0

Oil export 6 te 45 200 271 000

Shell & tube 0 te 27 500 0

Fin fan 0 te 14 800 0

Amine / physical solveent 0 te 26 500 0

Zinc oxide vessel 0 te 20 500 0

Zinc oxide bed 0 te 2 850 0

Glycol 77 te 26 500 2 041 000

Molecular sieve vesseel 0 te 20 500 0

Molecular sieve bed 0 te 8 000 0

LTS / exchanger 76 te 26 500 2 014 000

Refrigeration packagee 0 te 57 000 0

Turbo expander 20 te 60 000 1 200 000

Stabiliser 0 te 30 000 0

Gas metering 19 te 31 500 599 000

Compressors and turbinne drivers 137 te 122 400 16 769 000

Compressors and electrric motor dr rivers 9 te 79 000 711 000

Scrubbers 45 te 27 500 1 238 000

Shell & tube coolers 35 te 31 500 1 103 000

Fin fan coolers 0 te 14 800 0

Compressors and turbinne drivers 0 te 0 0

Compressors and electrric motor dr rivers 0 te 94 800 0

Scrubbers 0 te 27 500 0

Shell & tube coolers 0 te 31 500 0

Fin fan coolers 0 te 14 800 0

Fine filters 0 te 20 500 0

Deaerator 0 te 22 000 0

Pumps and turbine driveers 0 te 0 0

Pumps and electric motoor drivers 0 te 46 800 0

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Name FPSO Preprocessing

US D ollars

(7 007 te Op.)

Control and communicatioons 13 te 708 700 9 213 000

Drilling facilities 0 te 0 0

Quarters and helideck 650 te 39 500 25 675 000

Process utilities 323 te 14 429 000

Flare structure 243 te 9 100 2 211 000

Power generation 78 te 67 400 5 257 000

Power distribution 55 te 50 000 2 750 000

Emergency power 0 te 0 0

Sub Total 87 932 000

Freight 7,00% 87932000 6 155 000

Total Equipment $

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Name FPSO Preprocessing

US D ollars

(7 007 te Op.)

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Primary steel 1 401 te 1 820 2 550 000

Secondary steel 2 242 te 1 610 3 610 000

Piping 454 te 15 000 6 810 000

Electrical 136 te 20 500 2 788 000

Instruments 133 te 50 000 6 650 000

Others 248 te 11 000 2 728 000

Sub Total 25 136 000

Freight 7,00% 25136000 1 760 000

Total Materials $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Primary steel 1 401 te 8 820 12 357 000

Secondary steel 2 242 te 11 600 26 007 000

Equipment 996 te 2 400 2 390 000

Piping 454 te 24 000 10 896 000

Electrical 136 te 42 800 5 821 000

Instruments 133 te 44 000 5 852 000

Others 248 te 17 600 4 365 000

Sub Total 67 688 000

Loadout and seafasten 5,00% 67688000 3 384 000

Total Fabrication $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Tugs transport 0 day 48 000 0

Tugs mob/demob 0 day 48 000 0

Barge transport 0 day 6 700 0

Barge mob/demob 0 day 6 700 0

Installation spread 0 day 210 000 0

Installation spread mob/deemob 0 day 210 000 0

Total Installation $

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Name FPSO Preprocessing

US D ollars

(7 007 te Op.)

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Atshore HUC 110 035 mhr 65 7 152 000

Inshore HUC 0 mhr 106 0

Offshore HUC 48 140 mhr 186 8 954 000

HUC accommodation (flottel) 0 day 250 000 0

Total Hook-up and commiissioning $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 453 200 mhr 186 84 295 000

Project management 60 770 mhr 306 18 596 000

Total Design & Project ma anagementt $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 311052000 0

Insurance 4,00% 311052000 12 442 000

Total Insurance & Certificaation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 10,00% 323494000 32 349 000

Total Contingency $

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US Dollars

QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST

PER PER

UNIT MAN HOUR

Primary steel 1 401 te 147 205 947 60 8 820 12 357 000

Secondary steel 2 242 te 194 434 948 60 11 600 26 007 000

Equipment 996 te 40 39 840 60 2 400 2 390 000

Piping 454 te 400 181 600 60 24 000 10 896 000

Electrical 136 te 714 97 104 60 42 800 5 821 000

Instruments 133 te 734 97 622 60 44 000 5 852 000

Others 248 te 294 72 912 60 17 600 4 365 000

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Name Process utilities

US D ollars

QUANTITYY UNIT RATE COST

Produced water 1,0 te 29 500 29 500

Heating medium 7,1 te 34 500 244 950

Cooling medium 63,0 te 83 000 5 229 000

Flare and vent 34,1 te 31 500 1 074 150

Seawater lift 16,0 te 74 000 1 184 000

Fuel gas 8,4 te 54 000 453 600

Chemical injection and st torage 5,3 te 51 000 270 300

Total Process support uti lities $

QUANTITYY UNIT RATE COST

Closed drains 18,0 te 21 000 378 000

Open drains 3,6 te 21 000 75 600

Diesel storage 1,0 te 38 500 38 500

Aviation fuel 15,0 te 52 000 780 000

Instrument and plant air 2,4 te 55 000 132 000

Inert gas 15,2 te 76 000 1 155 200

Potable water 8,2 te 41 000 336 200

Sewage treatment 2,6 te 24 000 62 400

Firefighting 11,7 te 41 000 479 700

Other 0,0 te 44 500 0

Total General utilities $

QUANTITYY UNIT RATE COST

Mechanical handling 97,3 te 22 000 2 140 600

HVAC 1,8 te 23 500 42 300

Lifeboats 11,7 te 27 500 321 750

Total Ancillaries $

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Details

Topsides weight 6500 te Crane size Medium

Maximum lift weight 6000 te Number of lifts 2

Disposal distance 120 km Temporary piping weighht 45,4 te

Padeyes weight 4 te

Equipment weights

Wellhead 14 te Oil processing 89 te Oil export 6 te

Gas processing 192 te Gas compression 226 te Gas injection / lift compression 0 te

Water injection 0 te Drilling facilities 0 te Communications and co ontrol 13 te

Quarters 650 te Utilities 323 te Power generation and d distribution 133 te

Material weights

Steel 3640 te Piping 454 te Electrical 136 te

Instruments 133 te Others 248 te

Equipment hazardous v volumes

Wellhead 8,4 m³ Oil processing 134 m³ Oil export 0 m³

Gas processing 202 m³ Gas compression 147 m³ Gas injection / lift compression 0 m³

Water injection 0 m³ Drilling facilities 0 m³ Communications and co ontrol 0 m³

Quarters 0 m³ Utilities 58,2 m³ Power generation and d distribution 6,65 m³

Material hazardous voluumes

Steel 0 m³ Piping 227 m³ Electrical 0 m³

Instruments 0 m³ Others 0 m³

Equipment flushing and d inerting timee

FFlushing days Inerting g days

Wellhead 0,504 0,084

Oil processing 8,01 1,34

Oil export 0 0

Gas processing 10,1 2,02

Gas compression 1,84 1,47

Gas injection / lift compression 0 0

Water injection 0 0

Communications and co ontrol 0 0

Drilling facilities 0 0

Quarters 0 0

Utilities 3,49 0,728

Power generation and d distribution 0,166 0,0665

Materials flushing and in nerting time

FFlushing days Inerting g days

Steel 0 0

Piping 11,4 5,68

Electricals 0 0

Instruments 0 0

Others 0 0

Equipment dismantle / r removal timee

Dismantle mhrs Remova al mhrs

Wellhead 14 0

Oil processing 89 0

Oil export 12 0

Gas processing 192 0

Gas compression 226 0

Gas injection / lift compression 0 0

Water injection 0 0

Communications and co ontrol 39 0

Drilling facilities 0 0

Quarters 65 65

Utilities 647 0

Power generation and d distribution 133 0

Materials dismantle / re moval time

Dismantle mhrs Remova al mhrs

Steel 0 1 820

Piping 454 0

Electricals 13,6 0

Instruments 13,3 0

Others 49,6 0

Temporary pipework 0 454

Padeyes 0 10

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Name FPSO Preprocessing

US D ollars

Procured f from: Russia (Arctic)

QUANTITYY UNIT RATE COST

Padeyes 4 te 1 610 6 000

Temporary piping 45 te 6 700 302 000

Bracing / lifting frames 165 te 1 700 281 000

Seafastenings 325 te 1 700 553 000

Sub Total 1 142 000

Freight 5,00% 1142000 57 000

Total Materials $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Padeyes 4 te 16 300 65 000

Temporary piping 45 te 8 300 374 000

Bracing / lifting frames 165 te 10 900 1 799 000

Seafastenings 325 te 10 400 3 380 000

Sub Total 5 618 000

Freight 5,00% 5618000 281 000

Total Fabrication $

Locaation: Russia (Arctic)

QUANTITYY UNIT RATE COST

Labour 4 500 mhr 140 630 000

Pumping / flushing 42 day 35 000 1 470 000

Inerting 17 day 55 000 935 000

Multi-service / DSV 60 day 180 000 10 800 000

Tanker 42 day 12 000 504 000

Crane spread 11 day 920 000 10 120 000

Transport spread 9 day 108 000 972 000

Landing / dumping 1 day 72 000 72 000

Waste disposal 0 day 0 0

Total Decommissioning / r removal $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Design 26 100 mhr 186 4 855 000

Project management 26 100 mhr 306 7 987 000

Total Design & project maanagement $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Certification 0,00% 45443000 0

Insurance 2,50% 45443000 1 136 000

Total Insurance & certificaation $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Contingency 20,00% 46579000 9 316 000

Total Contingency $

Russia (Arctic)

QUANTITYY UNIT RATE COST

Scrap 6 503 te -310 -2 016 000

Total Scrap $

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FFPSO PREPROCESSING EQ

Production manifold

Well kill manifold

Control package

Hydraulic power unit

1st stage separator

2nd stage separator

Heater 1

Run down cooler

Inlet scrubber

Glycol contactor

Gas / glycol exchanger

Lean glycol pump

Rich glycol flash drum

Glycol / glycol exchanger

Rich TEG filter

Glycol regenerator

Glycol regenerator reboiler

Glycol surge drum

Glycol regenerator reflux condenser

Glycol regenerator reflux accumulator

Glycol reflux pump

Cold finger condenser

Cold finger accumulator

Cold finger condensate pump

Dewpoint control exchanger

Low temperature separator 1

Low temperature separator 2

Expander / recompressor (turbo)

QUIPPMEENT LI ST

1 100 80 215 10,8

1 100 207 223 1,43

1 100 1

1 100 0,6

1 100 1,92 Mm³/day 80 84 15,6 12,2 2,45 80,8 3 Phase (Horizontal)

1 100 1,93 Mm³/day 15 15,4 70 4,94 1,65 3,57 3 Phase (Horizontal)

1 100 2,08 80 88 70 0,438 2,8 Shell & tube

1 100 -0,586 15 16,5 50 0,337 1,94 Shell & tube

2 50 9,77 MMsm³/day

2 50 9,77 MMsm³/day

2 50

4 50

2 50

2 50

2 50

2 50

2 50

2 50

2 50

2 50

4 50

2 50

2 50

4 50

1 100 9,77 MMsm³/day

1 100

1 100

1 100

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FFPSO PREPROCESSING EQ

Gas fiscal metering package

Oil export pump

Oil export metering package

1st stage flash gas aftercooler

2nd stage flash gas aftercooler

1st stage flash gas suction scrubber

2nd stage flash gas suction scrubber

1st stage flash gas compressor + driver

2nd stage flash gas compressor

1st stage export aftercooler

1st stage export suction scrubber

1st stage export compressor + driver

HP hydrocyclone

MP hydrocyclone

Produced water flash drum

Oily water recycle pump

Fired heater package

Heating medium make-up tank

Heating medium make-up pump

Expansion vessel

Heating medium filter

Heating medium circulation pump

CCCW expansion / make-up tank

Seawater / CCCW exchanger

CCCW circulation pump

Cooling medium filter

QUIPPMEENT LI ST

1 100 9,73 MMsm³/day 18,5

2 100 0,611 Mm³/day 85,1 3,17 Electric

1 100 0,611 Mm³/day 2,42

1 100 0 MMsm³/day

1 100 0,213 MMsm³/day

1 100 0 MMsm³/day

1 100 0,213 MMsm³/day

1 100 0 MMsm³/day 792 Electric

1 100 0,213 MMsm³/day

2 100 9,94 MMsm³/day

2 100 9,94 MMsm³/day

2 100 9,94 MMsm³/day 9850 Turbine: Solar Mars 100

1 100 0,00617 Mm³/day

1 100

1 100

2 100

1 100 2,29

1 100

2 100

1 100

1 100

2 100

1 100

1 100 21,6

2 100

1 100

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FFPSO PREPROCESSING EQ

HP flare tip

HP flare drum

HP flare drum pump

HP ignition system

LP flare tip

LP flare drum

LP flare drum pump

LP ignition system

Vent tip

Vent KO drum

Halon snuffing system

Seawater lift pump

Chlorination package

Coarse seawater filter package

Jockey pump

Caisson

Fuel gas heater

KO drum

Fuel gas filter

Chemical injection pump

Chemical storage tank

Closed drain vessel

Closed drain pump

Reclaimed oil tank

Reclaimed oil return pump

Oily water tank

Oily water return pump

Non-hazardous caisson

Non-hazardous caisson return pump

Hazardous caisson

Hazardous caisson return pump

Oily water separation tank

QUIPPMEENT LI ST

1 100

1 100

2 100

1 100

1 100

1 100

2 100

1 100

1 100

1 100

1 100

2 100 15,2 Mm³/day

1 100

1 100 15,2 Mm³/day

2 100

1 100

1 100

1 100

1 100

Chemical injection is provided to the wellheads, oil and gas processing, gas compression and water injection systems.

1 100

2 100

1 100

2 100

1 100

2 100

1 100

2 100

1 100

2 100

1 100

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FFPSO PREPROCESSING EQ

Inlet strainer

Raw diesel fuel storage tank

Diesel transfer pump

Diesel centrifuge

Diesel filter / coalescer

Treated diesel tank

Aviation fuel storage tank

Aviation fuel charging pump

Aviation fuel hand operated pump

Filter / coalescer

Hose reel and earthing clip

Filter / silencer

Air compressor

Plant air receiver

Instrument air dryer

Filter

Instrument air receiver

Air inlet filter

Pressure swing absorber

Inert gas receiver

Inert gas outlet filter

RO unit booster pump

RO filter

Reverse osmosis unit

Palatability unit

Potable water filter

Potable water holding tank

Sterile storage tank

UV steriliser

Comminutor

Sewage surge tank

Sewage pump

QUIPPMEENT LI ST

1 100

1 100

2 100

1 100

1 100

1 100

1 100

2 100

2 100

1 100

1 100

1 100

1 100

2 100

2 100

1 100

1 100

2 100

1 100

1 100

2 100

2 100

1 100

1 100

1 100

1 100

1 100

1 100

2 100

1 100

2 100

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FFPSO PREPROCESSING EQ

Firewater pump (diesel)

Firewater lift caisson

Diesel day tank

Firewater jockey pump

Hose reels

Monitors

Hydrants

Cranes

Local lifting devices

HVAC packages

Lifeboats

Conventional control

Remote monitoring

Operational voice radio

Microwave radio

Generator set

Power distribution

Emergency power generator

Flare structure

Quarters

Helideck

QUIPPMEENT LI ST

2 100

1 100

1 100

2 100

1,78

11,7

2 100 4,35 MW 77,8 Solar Centaur 50

54,8 Includes transformers, buses, power cabling between switchboards, switchboards and ancillary controls

0

9,94 MMsm³/day 243 Boom

64 beds 293 600

50

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Terrain Grassland Manifolding Yes

Elevation 150 m Compression Yes

Production Yes

Water injection 0 Mm³/day Acid gas / HP / H HT No

Export / flared gas 0 MMsm³/day Ambient air temperature 22 °C

Gas injection 0 MMsm³/day Reservoir pressure 207 bara

Gas lift 0 MMsm³/day

Fluid capacities

Inlet high pressure fl uids Inlet medium pre essure fluids

Arrival temperature 38,9 °C Arrival temperatture 0 °C

Arrival pressure 80 bara Arrival pressure 0 bara

Well stream fluids Partially stabiliseed fluids

Oil / condensate 0,0159 Mm³/day Oil / condensatee 0 Mm³/day

Produced water 0 Mm³/day Produced water 0 Mm³/day

Gas 0 MMsm³/day Gas 0 MMsm³/day

Separated fluids Total capacities

Oil / condensate 0 Mm³/day Oil / condensatee 0,0159 Mm³/day

Produced water 0 Mm³/day Produced water 0 Mm³/day

Gas 0 MMsm³/day Gas 0 MMsm³/day

Prefabrication Winterisation

Type Other - Increased founddation No

Piping spools Yes 75% Winterisation of facilities No

Steelwork Yes 75%

Manifolding Flowlines Operating pressuree Design pressuree Weight

Production 0 - - --

Test 0 - - --

Water injection 0 - - --

Gas injection 0 - - --

Gas lift 0 - - --

Well kill - - --

Control package 1 te

Hydraulic power 0,6 te

Oil processing Trains Des. cap./train Pressure Temp. out Wt / train Duty Type

Separator 1 1 100% 80 bara 38,9 °C 6,73 te 3 Phase (Horizonttal)

Separator 2 - - - - - --

Separator 3 - - - - - --

Test separator - - - - - --

Dehydrator 2 100% 80 bara 38,9 °C 0,303 te - Molecular sieve

Desalter - - - - - - --

Stabiliser - - - - --

Heat exchanger 1 - - - - - --

Heat exchanger 2 - - - - - --

Heat exchanger 3 - - - - - --

Heat exchanger 4 - - - - - --

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Gas processing Capacity Trains x duty Process Specification

Gas cooling - - Fin fan 41 °C -

Acid gas removal - - -- - -

Gas dehydration - - -- - -

Dewpoint control - - -- - -

Stabiliser - - Gas metering: No

Product storage Oil Oil and water NGL LPG Gasoline Water

Number of days storaage - - - - - -

Storage capacity - - - - - -

Pressure vessel type - - - - - -

Number of vessels - - - - - -

Vapour space - - - - - -

Design capacity / vesssel - - - - - -

Number of tanks - - - - - -

Design capacity / tank - - - - - -

Diameter - - - - - -

Height - - - - - -

Length - - - - - -

Product export Oil Oil and water NGL LPG Gasoline Water

Export rate - - - - - -

Pump differential presssure - - - - - -

Total pump power - - - - - -

Metering - - - - - -

Driver type - - - - - -

Derating factor - - - - - -

Derating based on - - - - - -

Derated power - - - - - -

Elevation - - - - - -

Training - - - - - -

Sparing % - - - - - -

Driver model - - - - - -

Driver rating - - - - - -

Pump weight - - - - - -

Pump driver weight - - - - - -

Metering capacity - - - - - -

Metering weight - - - - - -

Pipeline length Oil Oil and water NGL LPG Gasoline Water

Length - - - - - -

Gas compression Capacity Suction Discharge Power Model Design duty /

pressure pressure compressor %

Flash gas - - - - - -

Export gas - - - - - -

Lift gas - - - - - -

Gas injection - - - - - -

Ambient temperaturee 22 °C Derating factor 0,89

Pipeline size - Pipeline outlet presssure -

Gas compression weiights Compressors Scrubbers Shell & tube Fin fan Totals

coolers coolers

Flash gas compressioon - - - - -

Export gas - - - - -

Lift gas - - - - -

Gas injection - - - - -

Water injection Weights

Number of pumps 0 Driver type Electric motor Capacity 0 Mm³/day Pump 0 te

Duty / pump 100% Driver model - Discharge p 42,5 bara Pump driver 0 te

Derating factor - Derated power - Pump duty 0 MW Fine filter -

Fine filters No Deaerator No Deaerator -

Produced water treatmment

Design capacity 0 Mm³/day

Residual oil in water 40 ppm

Induced gas flotation unit No

Control & communicaations

Control Conventional Communications Cable / fibre

Utilities Weight Weight

Heating medium 1 te Closed drains 1 te

Cooling medium 1 te Open drains 1 te

Flare and vent 1 te Diesel storage 1 te

Fuel gas 1 te Instrument and plannt air 1 te

Chemical injection an nd storage 1 te Inert gas -

Plant water -

Plant steam -

Firefighting 6,99 te

Other -

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Power generation

Wellpads 0 MW Water injection 0 MW

Export pumping 0 MW Custom equipmeent 0 MW

Oil processing Produced water treatment 0 MW

Oil pumps 0 MW Utilities 0,0743 MW

Oil and water pumps 0 MW Controls and commms 0,1 MW

NGL pumps 0 MW Base load 0,0174 MW

LPG pumps 0 MW Emergency power 0,152 MW

Gasoline pumps 0 MW

Water pumps 0 MW Type Power generation a and distribution

Gas processing Ambient temperaature 22 °C

Gas cooling 0 MW Derating factor --

Gas dehydration 0 MW Total power 0,192 MW

Acid gas removal 0 MW Design factor 1,2

Dewpoint control 0 MW Design power 0,23 MW

NGL production 0 MW Number of generators 2

LPG production 0 MW Design duty/generator % 100

Compressors Driver type Diesel / gas enginee

Flash gas 0 MW Model --

Export 0 MW Driver power --

Gas lift 0 MW Generator set we eight 6,04 te

Gas injection 0 MW Distribution weigght 5,06 te

Emergency power weight 1,96 te

Civils area

Manifolding 0 m² Export pumping

Oil processing Oil 0 m²

Separation / stabilisation 25,2 m² Oil and water 0 m²

Heating 0 m² NGL 0 m²

Cooling 0 m² LPG 0 m²

Dehydration (vesselss...) 0,332 m² Gasoline 0 m²

Dehydration tankage 0 m² Water 0 m²

Desalting 0 m² Metering

Gas processing Oil 0 m²

Cooling 0 m² Oil and water 0 m²

Gas dehydration 0 m² NGL 0 m²

Acid gas removal 0 m² LPG 0 m²

Dewpoint control 0 m² Gasoline 0 m²

NGL production 0 m² Water 0 m²

LPG production 0 m² Gas 0 m²

Others Storage

Gas compression 0 m² Atmospheric 0 m²

Water injection 0 m² Pressurised 0 m²

Custom equipment 0 m²

Produced water 0 m² Total foundation area 124 m²

Utilities 69,9 m² Total plot area 771 m²

Power generation 27 m² Vehicular accesss 62,2 m²

Power distribution 1,84 m² Buildings 24,9 m²

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80 38,9 0,0185 0,000162 0,00163 0,737 16,7

80 38,9 - 0,000125 - - -

80 38,9 - - 0,00163 - 16,7

80 38,9 0,0185 - - 0,737 -

80 38,9 0,0185 - - 0,737 -

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Cold finger

Number of trains 5

%Design cap/train 100

Pressure 70 bara

24 kg/MMsm³

-21,7 °CDewpt

Water

Incineration

Claus

Claus unit and tail ga

Tail gas unit only

Selexol

Number of trains 1

%Design cap/train 100

H2S 0 ppm

CO2 0 %

5421

Gas metering

Gas product spec. Flare / Fuel

Expander

Number of trains

Design cap/train

-

Dewpoint controlDehydrationAcid gas removalCooling

Coolant inlet temp.

20 °C

Ambient air temp.

22 °C

Shell & tube

Fin fan

41 °C

0,00163 0,00163 0,00163 0,00163 0,00163 - MMsm³/day

- - - - - 0,0185 Mm³/day

38,9 38,9 38,9 38,9 38,9 38,9 °C

80 80 80 80 80 80 bara

0 0 0 0 0 0 %

0 0 0 0 0 0 ppm

16,7 16,7 16,7 16,7 16,7 -

- - - - - 0,737 s.g.

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Name GTU Plant

US D ollars

Procureed from: N. America

QUANTITYY UNIT RATE COST

Manifolding 2 te 16 600 33 000

Separation 7 te 18 700 131 000

Dehydration 1 te 21 500 22 000

Dehydration (tankage) 0 m³ 48 0

Heating 0 te 24 000 0

Shell & tube cooling 0 te 24 400 0

Fin fan cooling 0 te 12 000 0

Desalting 0 te 21 500 0

Shell & tube 0 te 24 400 0

Fin fan 0 te 12 000 0

Amine / physical solveent 0 te 20 000 0

Zinc oxide vessel 0 te 16 400 0

Zinc oxide bed 0 te 2 700 0

Sulphur recovery 0 te 19 200 0

Tail gas clean up 0 te 18 600 0

Incineration 0 te 18 600 0

Glycol 0 te 20 000 0

Molecular sieve vesseel 0 te 16 400 0

Molecular sieve bed 0 te 7 400 0

LTS / exchanger 0 te 22 000 0

Refrigeration packagee 0 te 45 000 0

Turbo expander 0 te 48 500 0

NGL production / fractioonation 0 te 23 500 0

LPG production / fractioonation 0 te 23 500 0

Gas metering 0 te 28 500 0

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Name GTU Plant

US D ollars

Atmospheric 0 m³ 47 0

Pressurised 0 te 4 900 0

Oil 0,0 te 41 500 0

Oil and water 0,0 te 41 500 0

NGL 0,0 te 41 500 0

LPG 0,0 te 41 500 0

Gasoline 0,0 te 41 500 0

Water 0,0 te 41 500 0

Liquid metering 0 te 20 500 0

Compressors and turbinne drivers 0 te 0 0

Compressors and electtric motor d drivers 0 te 64 300 0

Scrubbers 0 te 21 400 0

Shell & tube coolers 0 te 24 400 0

Fin fan coolers 0 te 12 000 0

Compressors and turbinne drivers 0 te 0 0

Compressors and electtric motor d drivers 0 te 64 300 0

Scrubbers 0 te 21 400 0

Shell & tube coolers 0 te 24 400 0

Fin fan coolers 0 te 12 000 0

Fine filters 0 te 19 200 0

Deaerator 0 te 20 000 0

Pumps and turbine drivvers 0 te 0 0

Pumps and electric mottor drivers 0 te 46 800 0

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Name GTU Plant

US D ollars

Produced water treatmen nt & dispossal 0 te 18 900 0

Process utilities 16 te 379 000

Control and communications 2 149 000

Power generation 6 te 52 000 312 000

Power distribution 5 te 43 000 215 000

Emergency power 2 te 18 200 36 000

Sub Total 3 277 000

Freight 9,00% 3277000 295 000

Total Equipment $

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Name GTU Plant

US D ollars

Procuured from: S. E. Asia

QUANTITYY UNIT RATE COST

Steelwork 26 te 1 810 47 000

Piping 17 te 12 600 214 000

Electrical 11 te 18 500 204 000

Instruments 9 te 29 500 266 000

Others 14 te 8 600 120 000

Civils 771 m² 88 68 000

Sub Total 919 000

Freight 9,00% 919000 83 000

Total Materials $

Location: S. E. Asia

QUANTITYY UNIT RATE COST

Equipment 0 te 1 140 0

Steelwork 20 te 4 410 88 000

Piping 13 te 15 600 203 000

Electrical 0 te 22 200 0

Instruments 0 te 33 400 0

Others 0 te 11 400 0

Sub Total 291 000

Load out & transport 20,00% 291000 58 000

Total Prefabrication $

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Name GTU Plant

US D ollars

Location: Russia

QUANTITYY UNIT RATE COST

Site preparation 771 m² 73 56 000

Civils 771 m² 240 185 000

Skid / spool erection 33 te 2 000 66 000

Equipment installation 47 te 2 000 94 000

Tank erection 0 m³ 77 0

Steelwork 6 te 12 500 75 000

Piping 4 te 27 500 110 000

Electrical 11 te 55 000 605 000

Instruments 9 te 55 000 495 000

Others 14 te 27 500 385 000

Total Construction $

Western Europe

QUANTITYY UNIT RATE COST

Design 3 600 mhr 167 601 000

Project management 1 190 mhr 272 324 000

Total Design & Project m anagemennt $

Russia

QUANTITYY UNIT RATE COST

Certification 0,00% 7919000 0

Insurance 1,00% 7919000 79 000

Total Insurance & Certificcation $

Russia

QUANTITYY UNIT RATE COST

Contingency 20,00% 7998000 1 600 000

Total Contingency $

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US Dollars

QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST

PER PER

UNIT MAN HOUR

Equipment 0 te 30 0 38 1 140 0

Steelwork 20 te 116 2 320 38 4 410 88 000

Piping 13 te 410 5 330 38 15 600 203 000

Electrical 0 te 585 0 38 22 200 0

Instruments 0 te 880 0 38 33 400 0

Others 0 te 300 0 38 11 400 0

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US Dollars

QUANTITY PRODUCTIVITY MAN HOURS MAN HOURS MAN HOURS COST UNIT RATE COST

TERRAIN PER COST TERRAIN PER

FACTOR UNIT FACTOR MAN HOUR

Site preparation 771 m² 1,0 1,32 1 018 1,0 55 73 56 000

0

General 771 m² 1,0 1,54 1 187 1,0 50 77 59 000

Foundations 124 m² 1,0 11 1 364 1,0 50 550 68 000

Roads 62 m² 1,0 8,00 496 1,0 50 400 25 000

Buildings 25 m² 1,0 26 650 1,0 50 1 300 33 000

Skid / spool erection 33 te 1,0 40 1 320 1,0 50 2 000 66 000

Equipment installationn 47 te 1,0 40 1 880 1,0 50 2 000 94 000

Tank erection 0 m³ 1,0 1,54 0 1,0 50 77 0

Steelwork 6 te 1,0 250 1 500 1,0 50 12 500 75 000

Piping 4 te 1,0 550 2 200 1,0 50 27 500 110 000

Electrical 11 te 1,0 1 100 12 100 1,0 50 55 000 605 000

Instruments 9 te 1,0 1 100 9 900 1,0 50 55 000 495 000

Others 14 te 1,0 550 7 700 1,0 50 27 500 385 000

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Name Process utilities

US D ollars

QUANTITYY UNIT RATE COST

Heating medium 1,0 te 27 000 27 000

Cooling medium 1,0 te 65 000 65 000

Flare and vent 1,0 te 28 000 28 000

Fuel gas 1,0 te 43 000 43 000

Chemical injection and st torage 1,0 te 40 000 40 000

Total Process support uti lities $

QUANTITYY UNIT RATE COST

Closed drains 1,0 te 16 500 16 500

Open drains 1,0 te 16 500 16 500

Diesel storage 1,0 te 30 000 30 000

Instrument and plant air 1,0 te 42 000 42 000

Inert gas 0,0 te 59 000 0

Plant water 0,0 te 26 500 0

Plant steam 0,0 te 37 500 0

Firefighting 7,0 te 10 000 70 000

Other 0,0 te 34 500 0

Total General utilities $

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Name GTU Plant

US D ollars

CAPITAL COOST % COST

Equipment 3 572 000 60 2 143 000

Total Equipment $

CAPITAL COOST % COST

Materials 1 002 000 0 0

Total Materials $

CAPITAL COOST % COST

Prefabrication 349 000 0 0

Total Prefabrication $

CAPITAL COOST % COST

Construction 2 071 000 60 1 243 000

Total Construction $

CAPITAL COOST % COST

Design & Project manageement 925 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 79 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 1 600 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 124 te -425 -53 000

Total Scrap steel $

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GGTTU PLANT EQUIPMENT LIS

Control package

Hydraulic power unit

1st stage separator

Dehydrator

Recycle pump

Fired heater package

Heating medium make-up tank

Heating medium make-up pump

Expansion vessel

Heating medium filter

Heating medium circulation pump

CCCW expansion / make-up tank

Water / CCCW exchanger

CCCW circulation pump

Cooling medium filter

HP flare tip

HP flare drum

HP flare drum pump

HP ignition system

LP flare tip

LP flare drum

LP flare drum pump

LP ignition system

Vent tip

Vent KO drum

Halon snuffing system

ST

1 100 1

1 100 0,6

1 100 0,0185 Mm³/day 80 84 38,9 5,23 1,05 6,73 3 Phase (Horizontal)

2 100 80 38,9 0,288 1,42 0,606 Molecular sieve

2 100

1 100

1 100

2 100

1 100

1 100

2 100

1 100

1 100

2 100

1 100

1 100

1 100

2 100

1 100

1 100

1 100

2 100

1 100

1 100

1 100

1 100

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GGTTU PLANT EQUIPMENT LIS

Fuel gas heater

KO drum

Fuel gas filter

Chemical injection pump

Chemical storage tank

Closed drain vessel

Closed drain pump

Reclaimed oil tank

Reclaimed oil return pump

Oily water tank

Oily water return pump

Non-hazardous open drains tank

Non-hazardous open drains tank return pump

Hazardous open drains tank

Hazardous open drains tank return pump

Oily water separation tank

Diesel storage tank

Diesel transfer pump

Diesel filter

Filter / silencer

Air compressor

Plant air receiver

Instrument air dryer

Filter

Instrument air receiver

ST

1 100

1 100

1 100

Chemical injection is provided to the wellheads, oil and gas processing, gas compression and water injection systems.

1 100

2 100

1 100

2 100

1 100

2 100

1 100

2 100

1 100

2 100

1 100

1 100

2 100

1 100

1 100

1 100

1 100

2 100

2 100

1 100

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GGTTU PLANT EQUIPMENT LIS

Firewater pump

Foam unit

Firewater storage tank

Hose reels

Monitors

Hydrants

Cable / fibre

Conventional

Generator set

Power distribution

Emergency power generator

ST

2 100

100

2 100 0,23 MW 6,04 Diesel / gas engine

5,06 Includes transformers, buses, power cabling between switchboards, switchboards and ancillary controls

1,96

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Location

Terrain Grassland

Field in existinng oil or gas p roducing are ea Yes

Production fa cility access is s good No

Terminal facillity access is g good No

Distances to m major populations

Production fa cility distance to major po pulation 250 km

Terminal facillity distance to o major popuulation 50 km

Roads

Distance from m production fa acilities to ro oad network 250 km

Distance from m terminal facilities to road d network 50 km

Distance from m production fa acilities to te rminal facilities 0 km

Distance from m production fa acilities to we ellpad groups 0 km

Distance from m regasification n facilities to o road network 0 km

Other 0 km

Total 300 km

Railway

Distance from m terminal facilities to rail n network --

Distance from m regasification n facilities to o rail network --

Other --

Total --

Airstrip

Number of air rstrips 1

Construction camp Construction (000s) Nominal duration Men

Wellpad groups 0 mhr 6 month 0

Production fa cilities 82,6 mhr 10,8 month 70

Terminal facillities 12,5 mhr 6,16 month 20

Regasification n facilities 0 mhr 6 month 0

Other 0

Total 90

Operations ca amp

Number of op perations persoonnel --

Company admministration off fices

Number of ad dministration st taff --

Permanent ho ousing

Number of ad dministration pe ersonnel --

Number of pro ojects personnnel --

Total permanent housing --

Medical / hospital facilities

Number of be eds --

Schools, placces of worship and commuunity buildings

Number of pe ersonnel to proovide for --

Power transmmission

Lines to produuction facilitiess 0 km

Lines to termiinal facilities 0 km

Lines to regassification facilitties 0 km

Total power li ne length 0 km

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Name GTU Infrastructure

US D ollars

QUANTITYY UNIT RATE COST

Road construction 300 km 70 000 21 000 000

Rail construction 0 km 250 000 0

Construction camp (numbber of menn) 90 15 000 1 350 000

Operations camp (numbe er of men) 0 44 500 0

Administration buildings ( (number of f men) 0 17 500 0

Permanent housing (nummber of menn) 0 113 000 0

Medical facilities (numbe r of beds) 0 61 000 0

School, places of worship p (number of men) 0 15 000 0

Power transmission 0 km 54 000 0

Airstrips 1 245 000 245 000

Community projects 0 0 0

Others 0 0 0

Total Materials & Construuction $

Western Europe

QUANTITYY UNIT RATE COST

Design 6 600 mhr 167 1 102 000

Project management 4 900 mhr 272 1 333 000

Total Design & Project m anagemennt $

Russia

QUANTITYY UNIT RATE COST

Certification 0,00% 25030000 0

Insurance 1,00% 25030000 250 000

Total Insurance & Certificcation $

Russia

QUANTITYY UNIT RATE COST

Contingency 25,00% 25280000 6 320 000

Total Contingency $

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Name GTU Infrastructure

US D ollars

CAPITAL COOST % COST

Materials 22 595 000 15 3 389 000

Total Materials $

CAPITAL COOST % COST

Design & Project manageement 2 435 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 250 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 6 320 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 0 te -425 0

Total Scrap steel $

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Location Coastal

Terrain Grassland

Elevation 0 m

Oil Gasoline NGL LPG

Inlet flows 0 Mm³/day 0 Mm³/day 0 Mm³/day 0 Mm³/day

Method of expporting - - - -

Marine export t type --

Distance to m ooring --

Prefabricationn Other -

Piping spools Yes 75%

Steelwork Yes 75%

Increased gravel base depth No

Winterisation of facilities No

Product storagge Oil NGL LPG Gasoline

Number of day ys storage - - - -

Storage capaccity - - - -

Pressure vesssel type - - - -

Number of ves ssels - - - -

Vapour spacee - - - -

Design capacity / vessel - - - -

Number of tan nks - - - -

Design capacity / tank - - - -

Diameter - - - -

Height - - - -

Length - - - -

Product exporrt

Export rate - - - -

Pump differenntial pressure - - - -

Total pump po ower - - - -

Metering - - - -

Driver type - - - -

Derating factoor - - - -

Derating baseed on - - - -

Derated poweer - - - -

Elevation - - - -

Training - - - -

Sparing % - - - -

Driver model - - - -

Driver rating - - - -

Pump weight - - - -

Pump driver w weight - - - -

Metering capaacity - - - -

Metering weigght - - - -

Pipeline

Material - - - -

Liquid flowratee - - - -

Length - - - -

Pressure - - - -

Pressure in - - - -

Pressure out - - - -

Fluid temperature - - - -

Nominal diameter - - - -

Corrosion alloowance - - - -

Wall thicknesss - - - -

Control systemm Conventional

Communicatioon system Cable / fibre

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Utilities

Process support utilities

Flare and vent 1 te

Fuel gas -

Chemical injecction and storage -

General utilitiees

Closed drainss 1 te

Open drains 0 te

Diesel storagee 0 te

Instrument an d plant air -

Inert gas -

Plant water -

Plant steam -

Firefighting 0 te

Other -

Power Distribution only

Power requireements Derating

Export pumpinng Ambient temperature -

Oil pumps 0 kW Derating factor -

NGL pumpss 0 kW

LPG pumps 0 kW Capacity

Gasoline pu umps 0 kW Total power (derated) 0,14 MW

Control and co omms 125 kW Design factor 1,2

Utilities 2,7 kW Design power 0,169 MW

Base load 12,8 kW Number of generators -

Total demand 140 kW Design duty / generatorr -

Emergency po ower 127 kW

Driver

Driver type -

Driver model -

Driver power -

Weights

Generator set weight 0 te

Distribution weight 3,71 te

Emergency power weigght 1,87 te

Civils

Atmospheric s storage 0 m²

Pressurised s torage 0 m²

Oil NGL LPG Gasoline

Export pumpinng 0 m² 0 m² 0 m² 0 m²

Metering 0 m² 0 m² 0 m² 0 m²

Product loadinng Road Rail Marine

0 m² 0 m² 0 m²

Utilities 7 m²

Power generaation 7,9 m²

Power distribuution 1,35 m²

Total foundations 16,2 m²

Vehicular acceess 8,12 m²

Buildings 3,25 m²

Total plot areaa 101 m²

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Name LNG Offloading Terminal

US D ollars

Procureed from: N. America

QUANTITYY UNIT RATE COST

Atmospheric 0 m³ 47 0

Pressurised 0 te 5 000 0

Oil 0,0 te 41 500 0

NGL 0,0 te 41 500 0

LPG 0,0 te 41 500 0

Gasoline 0,0 te 41 500 0

Liquid metering 0 te 20 500 0

Road 0 154 000 0

Rail 0 164 000 0

Marine 0 485 000 0

Control and communications 1 519 000

Process utilities 2 te 45 000

Generation 0 te 0 0

Distribution 4 te 43 000 172 000

Emergency 2 te 15 900 32 000

Sub Total 1 768 000

Freight 9,00% 1768000 159 000

Total Equipment $

Procuured from: S. E. Asia

QUANTITYY UNIT RATE COST

Steelwork 5 te 1 810 9 000

Piping 2 te 12 600 25 000

Electrical 5 te 18 500 93 000

Instruments 3 te 29 500 89 000

Others 3 te 8 600 26 000

Offloading buoy (marine) 0 8 400 000 0

Offloading pipeline 0 km 0 0

Jetty materials 0 m 21 500 0

Civils materials 101 m² 88 9 000

Sub Total 251 000

Freight 9,00% 251000 23 000

Total Materials $

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Name LNG Offloading Terminal

US D ollars

Location: S. E. Asia

QUANTITYY UNIT RATE COST

Equipment 0 te 1 140 0

Steelwork 4 te 4 410 18 000

Piping 2 te 15 600 31 000

Electrical 0 te 22 200 0

Instruments 0 te 33 400 0

Others 0 te 11 400 0

Sub Total 49 000

Load out & transport 20,00% 49000 10 000

Total Prefabrication $

Location: Russia

QUANTITYY UNIT RATE COST

Site preparation 101 m² 73 7 000

Civil construction 101 m² 240 24 000

Tank erection 0 m³ 77 0

Equipment erection 8 te 2 000 16 000

Skid/spool erection 6 te 2 000 12 000

Steelwork 1 te 12 500 13 000

Piping 1 te 27 500 28 000

Electrical 5 te 55 000 275 000

Instruments 3 te 55 000 165 000

Others 3 te 27 500 83 000

Buoy installation 0 day 30 000 0

Pipeline installation 0 day 30 000 0

Jetty construction 0 m 15 700 0

Total Construction $

Western Europe

QUANTITYY UNIT RATE COST

Design 800 mhr 167 134 000

Project management 300 mhr 272 82 000

Total Design & Project m anagemennt $

Russia

QUANTITYY UNIT RATE COST

Certification 0,00% 3099000 0

Insurance 1,00% 3099000 31 000

Total Insurance & Certificcation $

Russia

QUANTITYY UNIT RATE COST

Contingency 20,00% 3130000 626 000

Total Contingency $

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US Dollars

QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST

PER PER

UNIT MAN HOUR

Equipment 0 te 30 0 38 1 140 0

Steelwork 4 te 116 478 38 4 410 18 000

Piping 2 te 410 769 38 15 600 31 000

Electrical 0 te 585 0 38 22 200 0

Instruments 0 te 880 0 38 33 400 0

Others 0 te 300 0 38 11 400 0

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US Dollars

QUANTITY PRODUCTIVITY MAN HOURS MAN HOURS MAN HOURS COST UNIT RATE COST

TERRAIN PER COST TERRAIN PER

FACTOR UNIT FACTOR MAN HOUR

Site preparation 101 m² 1,0 1,32 133 1,0 55 73 7 000

0

General 101 m² 1,0 1,54 155 1,0 50 77 8 000

Foundations 16 m² 1,0 11 179 1,0 50 550 9 000

Roads 8 m² 1,0 8,00 65 1,0 50 400 3 000

Buildings 3 m² 1,0 26 84 1,0 50 1 300 4 000

Tank erection 0 m³ 1,0 1,54 0 1,0 50 77 0

Equipment erection 8 te 1,0 40 303 1,0 50 2 000 16 000

Skid/spool erection 6 te 1,0 40 240 1,0 50 2 000 12 000

Steelwork 1 te 1,0 250 343 1,0 50 12 500 13 000

Piping 1 te 1,0 550 344 1,0 50 27 500 28 000

Electrical 5 te 1,0 1 100 5 193 1,0 50 55 000 275 000

Instruments 3 te 1,0 1 100 3 592 1,0 50 55 000 165 000

Others 3 te 1,0 550 1 840 1,0 50 27 500 83 000

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Name Process utilities

US D ollars

QUANTITYY UNIT RATE COST

Flare and vent 1,0 te 28 000 28 000

Fuel gas 0,0 te 43 000 0

Chemical injection and st torage 0,0 te 40 000 0

Total Process support uti lities $

QUANTITYY UNIT RATE COST

Closed drains 1,0 te 16 500 16 500

Open drains 0,0 te 16 500 0

Diesel storage 0,0 te 30 000 0

Instrument and plant air 0,0 te 42 000 0

Inert gas 0,0 te 59 000 0

Plant water 0,0 te 26 500 0

Plant steam 0,0 te 37 500 0

Firefighting 0,0 te 10 000 0

Other 0,0 te 34 500 0

Total General utilities $

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Name LNG Offloading Terminal

US D ollars

CAPITAL COOST % COST

Equipment 1 927 000 90 1 734 000

Total Equipment $

CAPITAL COOST % COST

Materials 274 000 0 0

Total Materials $

CAPITAL COOST % COST

Prefabrication 59 000 0 0

Total Prefabrication $

CAPITAL COOST % COST

Construction 623 000 90 561 000

Total Construction $

CAPITAL COOST % COST

Design & Project manageement 216 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 31 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 626 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 31 te -425 -13 000

Total Scrap steel $

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Licence number: N/A Page 108 N/A

Location

Terrain Grassland

Field in existinng oil or gas p roducing are ea Yes

Production fa cility access is s good No

Terminal facillity access is g good No

Distances to m major populations

Production fa cility distance to major po pulation 250 km

Terminal facillity distance to o major popuulation 50 km

Roads

Distance from m production fa acilities to ro oad network 250 km

Distance from m terminal facilities to road d network 50 km

Distance from m production fa acilities to te rminal facilities 0 km

Distance from m production fa acilities to we ellpad groups 0 km

Distance from m regasification n facilities to o road network 0 km

Other 0 km

Total 300 km

Railway

Distance from m terminal facilities to rail n network --

Distance from m regasification n facilities to o rail network --

Other --

Total --

Airstrip

Number of air rstrips 1

Construction camp Construction (000s) Nominal duration Men

Wellpad groups 0 mhr 6 month 0

Production fa cilities 82,6 mhr 10,8 month 70

Terminal facillities 12,5 mhr 6,16 month 20

Regasification n facilities 0 mhr 6 month 0

Other 0

Total 90

Operations ca amp

Number of op perations persoonnel --

Company admministration off fices

Number of ad dministration st taff --

Permanent ho ousing

Number of ad dministration pe ersonnel --

Number of pro ojects personnnel --

Total permanent housing --

Medical / hospital facilities

Number of be eds --

Schools, placces of worship and commuunity buildings

Number of pe ersonnel to proovide for --

Power transmmission

Lines to produuction facilitiess 0 km

Lines to termiinal facilities 0 km

Lines to regassification facilitties 0 km

Total power li ne length 0 km

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Name LNG Infrastructure

US D ollars

QUANTITYY UNIT RATE COST

Road construction 300 km 70 000 21 000 000

Rail construction 0 km 250 000 0

Construction camp (numbber of menn) 90 15 000 1 350 000

Operations camp (numbe er of men) 0 44 500 0

Administration buildings ( (number of f men) 0 17 500 0

Permanent housing (nummber of menn) 0 113 000 0

Medical facilities (numbe r of beds) 0 61 000 0

School, places of worship p (number of men) 0 15 000 0

Power transmission 0 km 54 000 0

Airstrips 1 245 000 245 000

Community projects 0 0 0

Others 0 0 0

Total Materials & Construuction $

Western Europe

QUANTITYY UNIT RATE COST

Design 6 600 mhr 167 1 102 000

Project management 4 900 mhr 272 1 333 000

Total Design & Project m anagemennt $

Russia

QUANTITYY UNIT RATE COST

Certification 0,00% 25030000 0

Insurance 1,00% 25030000 250 000

Total Insurance & Certificcation $

Russia

QUANTITYY UNIT RATE COST

Contingency 25,00% 25280000 6 320 000

Total Contingency $

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Name LNG Infrastructure

US D ollars

CAPITAL COOST % COST

Materials 22 595 000 15 3 389 000

Total Materials $

CAPITAL COOST % COST

Design & Project manageement 2 435 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 250 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 6 320 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 0 te -425 0

Total Scrap steel $

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Terrain Grassland Manifolding Yes

Elevation 150 m Compression Yes

Production Yes

Water injection 0 Mm³/day Acid gas / HP / H HT No

Export / flared gas 0 MMsm³/day Ambient air temperature 22 °C

Gas injection 0 MMsm³/day Reservoir pressure 207 bara

Gas lift 0 MMsm³/day

Fluid capacities

Inlet high pressure fl uids Inlet medium pre essure fluids

Arrival temperature 38,9 °C Arrival temperatture 0 °C

Arrival pressure 80 bara Arrival pressure 0 bara

Well stream fluids Partially stabiliseed fluids

Oil / condensate 0,0159 Mm³/day Oil / condensatee 0 Mm³/day

Produced water 0 Mm³/day Produced water 0 Mm³/day

Gas 0 MMsm³/day Gas 0 MMsm³/day

Separated fluids Total capacities

Oil / condensate 0 Mm³/day Oil / condensatee 0,0159 Mm³/day

Produced water 0 Mm³/day Produced water 0 Mm³/day

Gas 0 MMsm³/day Gas 0 MMsm³/day

Prefabrication Winterisation

Type Other - Increased founddation No

Piping spools Yes 75% Winterisation of facilities No

Steelwork Yes 75%

Manifolding Flowlines Operating pressuree Design pressuree Weight

Production 0 - - --

Test 0 - - --

Water injection 0 - - --

Gas injection 0 - - --

Gas lift 0 - - --

Well kill - - --

Control package 1 te

Hydraulic power 0,6 te

Oil processing Trains Des. cap./train Pressure Temp. out Wt / train Duty Type

Separator 1 1 100% 80 bara 38,9 °C 6,73 te 3 Phase (Horizonttal)

Separator 2 - - - - - --

Separator 3 - - - - - --

Test separator - - - - - --

Dehydrator 2 100% 80 bara 38,9 °C 0,303 te - Molecular sieve

Desalter - - - - - - --

Stabiliser - - - - --

Heat exchanger 1 - - - - - --

Heat exchanger 2 - - - - - --

Heat exchanger 3 - - - - - --

Heat exchanger 4 - - - - - --

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Gas processing Capacity Trains x duty Process Specification

Gas cooling - - Fin fan 41 °C -

Acid gas removal - - -- - -

Gas dehydration - - -- - -

Dewpoint control - - -- - -

Stabiliser - - Gas metering: No

Product storage Oil Oil and water NGL LPG Gasoline Water

Number of days storaage - - - - - -

Storage capacity - - - - - -

Pressure vessel type - - - - - -

Number of vessels - - - - - -

Vapour space - - - - - -

Design capacity / vesssel - - - - - -

Number of tanks - - - - - -

Design capacity / tank - - - - - -

Diameter - - - - - -

Height - - - - - -

Length - - - - - -

Product export Oil Oil and water NGL LPG Gasoline Water

Export rate - - - - - -

Pump differential presssure - - - - - -

Total pump power - - - - - -

Metering - - - - - -

Driver type - - - - - -

Derating factor - - - - - -

Derating based on - - - - - -

Derated power - - - - - -

Elevation - - - - - -

Training - - - - - -

Sparing % - - - - - -

Driver model - - - - - -

Driver rating - - - - - -

Pump weight - - - - - -

Pump driver weight - - - - - -

Metering capacity - - - - - -

Metering weight - - - - - -

Pipeline length Oil Oil and water NGL LPG Gasoline Water

Length - - - - - -

Gas compression Capacity Suction Discharge Power Model Design duty /

pressure pressure compressor %

Flash gas - - - - - -

Export gas - - - - - -

Lift gas - - - - - -

Gas injection - - - - - -

Ambient temperaturee 22 °C Derating factor 0,89

Pipeline size - Pipeline outlet presssure -

Gas compression weiights Compressors Scrubbers Shell & tube Fin fan Totals

coolers coolers

Flash gas compressioon - - - - -

Export gas - - - - -

Lift gas - - - - -

Gas injection - - - - -

Water injection Weights

Number of pumps 0 Driver type Electric motor Capacity 0 Mm³/day Pump 0 te

Duty / pump 100% Driver model - Discharge p 42,5 bara Pump driver 0 te

Derating factor - Derated power - Pump duty 0 MW Fine filter -

Fine filters No Deaerator No Deaerator -

Produced water treatmment

Design capacity 0 Mm³/day

Residual oil in water 40 ppm

Induced gas flotation unit No

Control & communicaations

Control Conventional Communications Cable / fibre

Utilities Weight Weight

Heating medium 1 te Closed drains 1 te

Cooling medium 1 te Open drains 1 te

Flare and vent 1 te Diesel storage 1 te

Fuel gas 1 te Instrument and plannt air 1 te

Chemical injection an nd storage 1 te Inert gas -

Plant water -

Plant steam -

Firefighting 6,99 te

Other -

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Power generation

Wellpads 0 MW Water injection 0 MW

Export pumping 0 MW Custom equipmeent 0 MW

Oil processing Produced water treatment 0 MW

Oil pumps 0 MW Utilities 0,0743 MW

Oil and water pumps 0 MW Controls and commms 0,1 MW

NGL pumps 0 MW Base load 0,0174 MW

LPG pumps 0 MW Emergency power 0,152 MW

Gasoline pumps 0 MW

Water pumps 0 MW Type Power generation a and distribution

Gas processing Ambient temperaature 22 °C

Gas cooling 0 MW Derating factor --

Gas dehydration 0 MW Total power 0,192 MW

Acid gas removal 0 MW Design factor 1,2

Dewpoint control 0 MW Design power 0,23 MW

NGL production 0 MW Number of generators 2

LPG production 0 MW Design duty/generator % 100

Compressors Driver type Diesel / gas enginee

Flash gas 0 MW Model --

Export 0 MW Driver power --

Gas lift 0 MW Generator set we eight 6,04 te

Gas injection 0 MW Distribution weigght 5,06 te

Emergency power weight 1,96 te

Civils area

Manifolding 0 m² Export pumping

Oil processing Oil 0 m²

Separation / stabilisation 25,2 m² Oil and water 0 m²

Heating 0 m² NGL 0 m²

Cooling 0 m² LPG 0 m²

Dehydration (vesselss...) 0,332 m² Gasoline 0 m²

Dehydration tankage 0 m² Water 0 m²

Desalting 0 m² Metering

Gas processing Oil 0 m²

Cooling 0 m² Oil and water 0 m²

Gas dehydration 0 m² NGL 0 m²

Acid gas removal 0 m² LPG 0 m²

Dewpoint control 0 m² Gasoline 0 m²

NGL production 0 m² Water 0 m²

LPG production 0 m² Gas 0 m²

Others Storage

Gas compression 0 m² Atmospheric 0 m²

Water injection 0 m² Pressurised 0 m²

Custom equipment 0 m²

Produced water 0 m² Total foundation area 124 m²

Utilities 69,9 m² Total plot area 771 m²

Power generation 27 m² Vehicular accesss 62,2 m²

Power distribution 1,84 m² Buildings 24,9 m²

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80 38,9 0,0185 0,000162 0,00163 0,737 16,7

80 38,9 - 0,000125 - - -

80 38,9 - - 0,00163 - 16,7

80 38,9 0,0185 - - 0,737 -

80 38,9 0,0185 - - 0,737 -

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Cold finger

Number of trains 5

%Design cap/train 100

Pressure 70 bara

24 kg/MMsm³

-21,7 °CDewpt

Water

Incineration

Claus

Claus unit and tail ga

Tail gas unit only

Selexol

Number of trains 1

%Design cap/train 100

H2S 0 ppm

CO2 0 %

5421

Gas metering

Gas product spec. Flare / Fuel

Expander

Number of trains

Design cap/train

-

Dewpoint controlDehydrationAcid gas removalCooling

Coolant inlet temp.

20 °C

Ambient air temp.

22 °C

Shell & tube

Fin fan

41 °C

0,00163 0,00163 0,00163 0,00163 0,00163 - MMsm³/day

- - - - - 0,0185 Mm³/day

38,9 38,9 38,9 38,9 38,9 38,9 °C

80 80 80 80 80 80 bara

0 0 0 0 0 0 %

0 0 0 0 0 0 ppm

16,7 16,7 16,7 16,7 16,7 -

- - - - - 0,737 s.g.

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Name LNG Plant

US D ollars

Procureed from: N. America

QUANTITYY UNIT RATE COST

Manifolding 2 te 16 600 33 000

Separation 7 te 18 700 131 000

Dehydration 1 te 21 500 22 000

Dehydration (tankage) 0 m³ 48 0

Heating 0 te 24 000 0

Shell & tube cooling 0 te 24 400 0

Fin fan cooling 0 te 12 000 0

Desalting 0 te 21 500 0

Shell & tube 0 te 24 400 0

Fin fan 0 te 12 000 0

Amine / physical solveent 0 te 20 000 0

Zinc oxide vessel 0 te 16 400 0

Zinc oxide bed 0 te 2 700 0

Sulphur recovery 0 te 19 200 0

Tail gas clean up 0 te 18 600 0

Incineration 0 te 18 600 0

Glycol 0 te 20 000 0

Molecular sieve vesseel 0 te 16 400 0

Molecular sieve bed 0 te 7 400 0

LTS / exchanger 0 te 22 000 0

Refrigeration packagee 0 te 45 000 0

Turbo expander 0 te 48 500 0

NGL production / fractioonation 0 te 23 500 0

LPG production / fractioonation 0 te 23 500 0

Gas metering 0 te 28 500 0

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Name LNG Plant

US D ollars

Atmospheric 0 m³ 47 0

Pressurised 0 te 4 900 0

Oil 0,0 te 41 500 0

Oil and water 0,0 te 41 500 0

NGL 0,0 te 41 500 0

LPG 0,0 te 41 500 0

Gasoline 0,0 te 41 500 0

Water 0,0 te 41 500 0

Liquid metering 0 te 20 500 0

Compressors and turbinne drivers 0 te 0 0

Compressors and electtric motor d drivers 0 te 64 300 0

Scrubbers 0 te 21 400 0

Shell & tube coolers 0 te 24 400 0

Fin fan coolers 0 te 12 000 0

Compressors and turbinne drivers 0 te 0 0

Compressors and electtric motor d drivers 0 te 64 300 0

Scrubbers 0 te 21 400 0

Shell & tube coolers 0 te 24 400 0

Fin fan coolers 0 te 12 000 0

Fine filters 0 te 19 200 0

Deaerator 0 te 20 000 0

Pumps and turbine drivvers 0 te 0 0

Pumps and electric mottor drivers 0 te 46 800 0

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Name LNG Plant

US D ollars

Produced water treatmen nt & dispossal 0 te 18 900 0

Process utilities 16 te 379 000

Control and communications 2 149 000

Power generation 6 te 52 000 312 000

Power distribution 5 te 43 000 215 000

Emergency power 2 te 18 200 36 000

Sub Total 3 277 000

Freight 9,00% 3277000 295 000

Total Equipment $

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Name LNG Plant

US D ollars

Procuured from: S. E. Asia

QUANTITYY UNIT RATE COST

Steelwork 26 te 1 810 47 000

Piping 17 te 12 600 214 000

Electrical 11 te 18 500 204 000

Instruments 9 te 29 500 266 000

Others 14 te 8 600 120 000

Civils 771 m² 88 68 000

Sub Total 919 000

Freight 9,00% 919000 83 000

Total Materials $

Location: S. E. Asia

QUANTITYY UNIT RATE COST

Equipment 0 te 1 140 0

Steelwork 20 te 4 410 88 000

Piping 13 te 15 600 203 000

Electrical 0 te 22 200 0

Instruments 0 te 33 400 0

Others 0 te 11 400 0

Sub Total 291 000

Load out & transport 20,00% 291000 58 000

Total Prefabrication $

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Name LNG Plant

US D ollars

Location: Russia

QUANTITYY UNIT RATE COST

Site preparation 771 m² 73 56 000

Civils 771 m² 240 185 000

Skid / spool erection 33 te 2 000 66 000

Equipment installation 47 te 2 000 94 000

Tank erection 0 m³ 77 0

Steelwork 6 te 12 500 75 000

Piping 4 te 27 500 110 000

Electrical 11 te 55 000 605 000

Instruments 9 te 55 000 495 000

Others 14 te 27 500 385 000

Total Construction $

Western Europe

QUANTITYY UNIT RATE COST

Design 3 600 mhr 167 601 000

Project management 1 190 mhr 272 324 000

Total Design & Project m anagemennt $

Russia

QUANTITYY UNIT RATE COST

Certification 0,00% 7919000 0

Insurance 1,00% 7919000 79 000

Total Insurance & Certificcation $

Russia

QUANTITYY UNIT RATE COST

Contingency 20,00% 7998000 1 600 000

Total Contingency $

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US Dollars

QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST

PER PER

UNIT MAN HOUR

Equipment 0 te 30 0 38 1 140 0

Steelwork 20 te 116 2 320 38 4 410 88 000

Piping 13 te 410 5 330 38 15 600 203 000

Electrical 0 te 585 0 38 22 200 0

Instruments 0 te 880 0 38 33 400 0

Others 0 te 300 0 38 11 400 0

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US Dollars

QUANTITY PRODUCTIVITY MAN HOURS MAN HOURS MAN HOURS COST UNIT RATE COST

TERRAIN PER COST TERRAIN PER

FACTOR UNIT FACTOR MAN HOUR

Site preparation 771 m² 1,0 1,32 1 018 1,0 55 73 56 000

0

General 771 m² 1,0 1,54 1 187 1,0 50 77 59 000

Foundations 124 m² 1,0 11 1 364 1,0 50 550 68 000

Roads 62 m² 1,0 8,00 496 1,0 50 400 25 000

Buildings 25 m² 1,0 26 650 1,0 50 1 300 33 000

Skid / spool erection 33 te 1,0 40 1 320 1,0 50 2 000 66 000

Equipment installationn 47 te 1,0 40 1 880 1,0 50 2 000 94 000

Tank erection 0 m³ 1,0 1,54 0 1,0 50 77 0

Steelwork 6 te 1,0 250 1 500 1,0 50 12 500 75 000

Piping 4 te 1,0 550 2 200 1,0 50 27 500 110 000

Electrical 11 te 1,0 1 100 12 100 1,0 50 55 000 605 000

Instruments 9 te 1,0 1 100 9 900 1,0 50 55 000 495 000

Others 14 te 1,0 550 7 700 1,0 50 27 500 385 000

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Name Process utilities

US D ollars

QUANTITYY UNIT RATE COST

Heating medium 1,0 te 27 000 27 000

Cooling medium 1,0 te 65 000 65 000

Flare and vent 1,0 te 28 000 28 000

Fuel gas 1,0 te 43 000 43 000

Chemical injection and st torage 1,0 te 40 000 40 000

Total Process support uti lities $

QUANTITYY UNIT RATE COST

Closed drains 1,0 te 16 500 16 500

Open drains 1,0 te 16 500 16 500

Diesel storage 1,0 te 30 000 30 000

Instrument and plant air 1,0 te 42 000 42 000

Inert gas 0,0 te 59 000 0

Plant water 0,0 te 26 500 0

Plant steam 0,0 te 37 500 0

Firefighting 7,0 te 10 000 70 000

Other 0,0 te 34 500 0

Total General utilities $

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Name LNG Plant

US D ollars

CAPITAL COOST % COST

Equipment 3 572 000 60 2 143 000

Total Equipment $

CAPITAL COOST % COST

Materials 1 002 000 0 0

Total Materials $

CAPITAL COOST % COST

Prefabrication 349 000 0 0

Total Prefabrication $

CAPITAL COOST % COST

Construction 2 071 000 60 1 243 000

Total Construction $

CAPITAL COOST % COST

Design & Project manageement 925 000 0 0

Total Design & project ma anagemennt $

CAPITAL COOST % COST

Insurance & certification 79 000 0 0

Total Insurance & certification $

CAPITAL COOST % COST

Contingency 1 600 000 0 0

Total Contingency $

QUANTITYY UNIT RATE COST

Scrap steel 124 te -425 -53 000

Total Scrap steel $

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LLNG PLANT EQUIPMENT LIS

Control package

Hydraulic power unit

1st stage separator

Dehydrator

Recycle pump

Fired heater package

Heating medium make-up tank

Heating medium make-up pump

Expansion vessel

Heating medium filter

Heating medium circulation pump

CCCW expansion / make-up tank

Water / CCCW exchanger

CCCW circulation pump

Cooling medium filter

HP flare tip

HP flare drum

HP flare drum pump

HP ignition system

LP flare tip

LP flare drum

LP flare drum pump

LP ignition system

Vent tip

Vent KO drum

Halon snuffing system

ST

1 100 1

1 100 0,6

1 100 0,0185 Mm³/day 80 84 38,9 5,23 1,05 6,73 3 Phase (Horizontal)

2 100 80 38,9 0,288 1,42 0,606 Molecular sieve

2 100

1 100

1 100

2 100

1 100

1 100

2 100

1 100

1 100

2 100

1 100

1 100

1 100

2 100

1 100

1 100

1 100

2 100

1 100

1 100

1 100

1 100

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LLNG PLANT EQUIPMENT LIS

Fuel gas heater

KO drum

Fuel gas filter

Chemical injection pump

Chemical storage tank

Closed drain vessel

Closed drain pump

Reclaimed oil tank

Reclaimed oil return pump

Oily water tank

Oily water return pump

Non-hazardous open drains tank

Non-hazardous open drains tank return pump

Hazardous open drains tank

Hazardous open drains tank return pump

Oily water separation tank

Diesel storage tank

Diesel transfer pump

Diesel filter

Filter / silencer

Air compressor

Plant air receiver

Instrument air dryer

Filter

Instrument air receiver

ST

1 100

1 100

1 100

Chemical injection is provided to the wellheads, oil and gas processing, gas compression and water injection systems.

1 100

2 100

1 100

2 100

1 100

2 100

1 100

2 100

1 100

2 100

1 100

1 100

2 100

1 100

1 100

1 100

1 100

2 100

2 100

1 100

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LLNG PLANT EQUIPMENT LIS

Firewater pump

Foam unit

Firewater storage tank

Hose reels

Monitors

Hydrants

Cable / fibre

Conventional

Generator set

Power distribution

Emergency power generator

ST

2 100

100

2 100 0,23 MW 6,04 Diesel / gas engine

5,06 Includes transformers, buses, power cabling between switchboards, switchboards and ancillary controls

1,96

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Decommissioning scenario name: Offshhore decommmissioning sce enario

Jacket Topsides Offshorepipelines

Subsea Offshoredrilling

TLP Tanker Semi-sub

Sparbuoy

GBS Barge Offshoreloading

Userdefined

Bridgelink

Detailed decommissioning

Equipment 45% 0% 0% 0% 0% 0% 0% 20% 0%

Materials 65% 0% 0% 0% 0% 40% 0% 0% 50% 50% 0% 0% 20% 0%

Fabrication 0% 0% 0% 0% 0% 0% 0% 20%

Installation 65% 45% 80% 200% 30% 40% 110% 110% 50% 0% 125% 80% 20% 140%

Hook-up and commissioning 0% 0% 0% 20%

Design and project management 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 20% 0%

Insurance and certification 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 20% 0%

Contingency 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 20% 0%

Scrap steel

Schedule duration: 18 months

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Decommissioning scenario name: Onshhore decommisssioning scenarioo

Productionfacilities

Onshorepipelines

Onshoredrilling

Wellpadgroup

Terminal Infrastructure

Userdefined

Equipment 60% 0% 30% 90% 20%

Materials 0% 35% 0% 30% 0% 15% 20%

Prefabrication 0% 0% 0% 20%

Construction 60% 35% 20% 30% 90% 20%

Design and project management 0% 0% 0% 0% 0% 0% 20%

Insurance and certification 0% 0% 0% 0% 0% 0% 20%

Contingency 0% 0% 0% 0% 0% 0% 20%

Scrap steel

Schedule duration: 18 months