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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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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Oil
Gas
Gas Risers
Gas Offshore Drilling
Oil Risers
Oil Offshore Drilling
FPSO Preprocessing
FPSO Vessel
Gas Landfall
Oil Landfall
GTU Plant
GTU Infrastructure
LNG Offloading Terminal
Gasprom Export Trunkline
LNG Plant
LNG Infrastructure
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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0
1
2
3
4
5
6
7
8
1 2 3 4 5 6 7 8 9 10Years
Daily Production (Gas) Штокман учебный
Production Units
Daily MMsm³/day
Annual Bsm³/yr
Cumulative Bsm³
1 2 3 4 5 6 7 8 9 10
3,823 7,646 7,646 7,646 7,646 6,442 4,527 3,181 2,236 1,571
1,338 2,676 2,676 2,676 2,676 2,255 1,585 1,113 0,782 0,550
1,338 4,014 6,690 9,366 12,042 14,297 15,881 16,995 17,777 18,327
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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0
0,05
0,1
0,15
0,2
0,25
0,3
0,35
0,4
0,45
0,5
1 2 3 4 5 6 7 8 9 10Years
Daily Production (Gross liquids) Штокман учебный
Production Units
Daily Mm³/day
Annual MMm³/yr
Cumulative MMm³
1 2 3 4 5 6 7 8 9 10
0,237 0,475 0,475 0,475 0,475 0,400 0,281 0,198 0,139 0,098
0,083 0,166 0,166 0,166 0,166 0,140 0,098 0,069 0,049 0,034
0,083 0,249 0,415 0,581 0,748 0,888 0,986 1,055 1,104 1,138
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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Project Штокман учебный Currency US Dollars
Location C.I.S.
Development type Gas
Sub total 468 884 000
Scrap -15 567 000 Procurement strategy Russia
Grand total 453 317 000
Cost centre Totals Materials Fabrication Decommissioning / removal Design Project management Ins. & cert. Contingency Scrap
FPSO Preprocessing 53 879 000 1 199 000 5 899 000 25 503 000 4 855 000 7 987 000 1 136 000 9 316 000 -2 016 000
FPSO Vessel 1 057 000 4 312 000 -3 255 000
Oil pipeline (offshore 1) 74 626 000 57 171 000 1 562 000 2 570 000 1 533 000 12 567 000 -777 000
Gas pipeline (offshore 2) 99 149 000 84 027 000 1 562 000 2 570 000 2 204 000 18 073 000 -9 287 000
Gas Offshore Drilling 38 258 000 38 258 000 0
Oil Offshore Drilling 31 232 000 31 232 000 0
Gas Risers 82 871 000 83 004 000 -133 000
Oil Risers 72 245 000 72 344 000 -99 000
TOTALS 453 317 000 1 199 000 5 899 000 395 851 000 7 979 000 13 127 000 4 873 000 39 956 000 -15 567 000
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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Project Штокман учебный Currency US Dollars
Location C.I.S.
Development type Gas
Sub total 15 845 000
Scrap -119 000 Procurement str rategy Russia
Grand total 15 726 000
Cost centre Totals Decommissioning / removal Scrap
GTU Plant 3 333 000 3 386 000 -53 000
LNG Plant 3 333 000 3 386 000 -53 000
LNG Offloading Terminal 2 282 000 2 295 000 -13 000
GTU Infrastructure 3 389 000 3 389 000 0
LNG Infrastructure 3 389 000 3 389 000 0
TOTALS 15 726 000 15 845 000 -119 000
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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Project Штокман учебный Currency US Dollars
Location C.I.S.
Development type Gas
Sub total 484 729 000 Procurement strategy: Of ffshore Russia
Scrap -15 686 000 Procurement strategy: O nshore Russia
Grand total 469 043 000
Cost centre Totals Materials Fabrication Decommissioning / removal Design Project management Ins. & cert. Contingency Scrap
FPSO Preprocessing 53 879 000 1 199 000 5 899 000 25 503 000 4 855 000 7 987 000 1 136 000 9 316 000 -2 016 000
FPSO Vessel 1 057 000 4 312 000 -3 255 000
GTU Plant 3 333 000 3 386 000 -53 000
LNG Plant 3 333 000 3 386 000 -53 000
Oil pipeline (offshore 1) 74 626 000 57 171 000 1 562 000 2 570 000 1 533 000 12 567 000 -777 000
Gas pipeline (offshore 2) 99 149 000 84 027 000 1 562 000 2 570 000 2 204 000 18 073 000 -9 287 000
LNG Offloading Terminal 2 282 000 2 295 000 -13 000
Gas Offshore Drilling 38 258 000 38 258 000 0
Oil Offshore Drilling 31 232 000 31 232 000 0
GTU Infrastructure 3 389 000 3 389 000 0
LNG Infrastructure 3 389 000 3 389 000 0
Gas Risers 82 871 000 83 004 000 -133 000
Oil Risers 72 245 000 72 344 000 -99 000
TOTALS 469 043 000 1 199 000 5 899 000 411 696 000 7 979 000 13 127 000 4 873 000 39 956 000 -15 686 000
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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 $) US Dollars boe/Mscf Gass 0,17 Cost/boe 12,78 Cost/boe 25,55
0 Drilling cost 321,09 Facilities cost 1 129,98 Operating co st 998,12 Decommissioon cost 453,310 Cost/boe 2,83 Cost/boe 9,95 Cost/boe 8,79 Cost/boe 3,99
Deesign productioon0,21 3,48
PROJECT EXPLORRATION & APPPRAISAL PROD. D DRILLING FACILITIEES COSTS OPERATINNG COSTS CO2 emitted PPRODUCTIONN
PROJECT COSTS Expl. Seismic Apprsl. Tangible Intangible Subsea Pipelines Topsides Structures Floaters Other
facilitiesFixed OPEX
Tariffs Leases CO2 tax DECOMM. 000s te/yr Oil MMm³/yr
Cond. MMm³/yr
Gas Bsm³/yr
1,71 2,67 41,1012,78 0,83 61,25 41,95 138,11 110,6811,77 159,75 222,00 263,41 176,63 74,85 7,09 2,21 0,01 0,11
1,21 130,37 85,25 29,51 0,09 1,4586,65 62,25 0,16 2,68
91,97 62,25 0,16 2,68145,18 62,25 0,16 2,68
88,40 61,17 0,16 2,6497,18 47,94 0,14 2,2090,72 31,16 0,09 1,55
143,45 21,52 0,07 1,0984,72 15,82 0,05 0,7677,51 25,18 11,48 0,03 0,50
302,21125,92
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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 $) US Dollars boe/Mscf Gass 0,17 Cost/boe 0 Cost/boe 0
0 Drilling cost 0 Facilities cost 86,14 Operating co st 200,37 Decommissioon cost 15,720 Cost/boe 0 Cost/boe 0 Cost/boe 0 Cost/boe 0
Deesign productioon0,21 348
PROJECT EXPLORRATION & APPPRAISAL PROD. D DRILLING FACILITIEES COSTS OPERATINNG COSTS CO2 emitted PPRODUCTIONN
PROJECT COSTS Expl. Seismic Apprsl. Tangible Intangible Production
facilitiesWellpad groups
Terminals Pipelines Infra-structure
Other facilities
Fixed OPEX
Tariffs Leases CO2 tax DECOMM. 000s te/yr Oil MMm³/yr
Cond. MMm³/yr
Gas Bsm³/yr
1,14 0,10 63,208,36 3,449,69 0,21 1,67 0,13
20,01 1,6020,12 2,30
20,12 2,3020,12 2,3020,12 2,2820,08 2,0320,01 1,66
19,95 1,4019,92 1,2118,25 0,87 1,00
10,484,37
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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 $) US Dollars boe/Mscf Gass 0,17 Cost/boe 13,53 Cost/boe 28,22
0 Drilling cost 321,09 Facilities costt 1 216,12 Operating co st 1 198,49 Decommissioon cost 469,030 Cost/boe 2,83 Cost/boe 10,71 Cost/boe 10,55 Cost/boe 4,13
Deesign productioon0,21 3,48
PROJECT EXPLORRATION & APPPRAISAL PROD. D DRILLING FACCILITIES COSSTS OPERATINNG COSTS CO2 emitted PPRODUCTIONN
PROJECT COSTS Expl. Seismic Apprsl. Tangible Intangible Facilities Pipelines
Other facilities
Fixed OPEX Tariffs Leases CO2 tax
DECOMM.000s te/yr
Oil MMm³/yr
Cond. MMm³/yr
Gas Bsm³/yr
1,71 2,67 105,54
12,78 0,83 321,84 41,95
11,77 159,75 483,38 263,41 8,76 2,34 0,01 0,11
1,21 130,37 105,26 31,11 0,09 1,45106,77 64,55 0,16 2,68
112,09 64,55 0,16 2,68
165,30 64,55 0,16 2,68
108,52 63,45 0,16 2,64
117,26 49,97 0,14 2,20110,73 32,82 0,09 1,55
163,40 22,92 0,07 1,09
104,64 17,03 0,05 0,76
95,76 26,05 12,48 0,03 0,50
312,69130,29
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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Warning Field level: Minimum monthly average ambient temperatureBelow water freezing point.
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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Rig Subsea wells (floater) Water depth 291 m
Generatioon Second generation semii-sub Reservoir deppth 2 050 m
Profile Build and holdd Reservoir presssure 207 bara
Design pressuure 345 barg
Maximum steppout 3 000 m
Wells Flowwrate Longest stepoout 941 m
Gas prodduction 5 5,52 MMsm³/day Trip speed 300 m/hr
Water inje ection 0 Mm³/day Rate of build d deg/30m 4,00 degrees
Gas injecction 0 MMsm³/day Acid gas No
Exploratioon - Use ESPs No
Total connductors 0 Multilaterals p per production h host 1
Pre-drille d wells 0 Drilling profiles s edited No
Well no. Well function
TVD from LAT
Kick off Horizontal Profile Horizontal Measured Maximum Rig t type Completion Duraationfunction from LAT shift type section depth deviation Drilling Completion Type Platfform Jackk-up Semi-sub
(degrees Drilling Completion Drilling Completion Drilling Completion
from
m m m m m vertical) days days days days days days
1 Prod. 2 050 0 0 Vertical 0 2 050 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,0 14,2
2 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 53,5 17,6
3 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 51,3 17,6
4 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,2 17,6
5 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 44,7 17,6
Total depth
Total p platform Total ja ack-up Total se emi-sub
m daays daays days
11 410 00 00 3330
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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Rig Subsea wells (floater) Water depth 291 m
Generatioon Second generation semii-sub Reservoir deppth 2 050 m
Profile Build and holdd Reservoir presssure 207 bara
Design pressuure 345 barg
Maximum steppout 3 000 m
Wells Flowwrate Longest stepoout 941 m
Gas prodduction 4 4,42 MMsm³/day Trip speed 300 m/hr
Water inje ection 0 Mm³/day Rate of build d deg/30m 4,00 degrees
Gas injecction 0 MMsm³/day Acid gas No
Exploratioon - Use ESPs No
Total connductors 0 Multilaterals p per production h host 1
Pre-drille d wells 0 Drilling profiles s edited No
Well no. Well function
TVD from LAT
Kick off Horizontal Profile Horizontal Measured Maximum Rig t type Completion Duraationfunction from LAT shift type section depth deviation Drilling Completion Type Platfform Jackk-up Semi-sub
(degrees Drilling Completion Drilling Completion Drilling Completion
from
m m m m m vertical) days days days days days days
1 Prod. 2 050 0 0 Vertical 0 2 050 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,0 14,2
2 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 53,5 17,6
3 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 51,3 17,6
4 Prod. 2 050 300 941 BH 0 2 340 36 Semi-sub Semi-sub Cased 0,0 0,0 0,0 0,0 48,2 17,6
Total depth
Total p platform Total ja ack-up Total se emi-sub
m daays daays days
9 070 00 00 2668
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 22 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 23 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 24 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 25 N/A
From FPSO Preprocessing Export end te ermination details
To Oil Landfall Export compoonent FPSO Preprocessing
Flow type Oil Export end wa ater depth 291 m
Length 120 km Export end te ermination type Riser
Export end te ermination sub-type Flexible lazy S
Pipeline details Export end di verless connections Yes
Material Carbon steel Export end su ubsea ESD valve No
Oil flowrate 0,611 Mm³/day
Water flowrate 0 Mm³/day Export end PL LET
Gas flowrate 0 MMsm³/day Required Yes
Pressure in 103 bara Valve Yes
Pressure out 15 bara Soil Conditionns Average
Fixed pressure Outlet pressure Pressure ratinng 207 barg
Fluid temperature 4 °C Trawler protection No
Buckle arrestors Yes Jumper type Rigid
Size Receiving end d termination details
Nominal diameter 102 mm Receiving com mponent Oil Landfall
Corrosion allowance 3mm Receiving end d water depth -
Wall thickness 6,02 mm Receiving end d termination type Shore approach
Receiving end d termination sub-type Shelving beach
Installation Receiving end d diverless connections -
Lay vessel type S-lay without DP Receiving end d subsea ESD valve No
Pipeline crossings 2
Buried length 5 km Receiving end d PLET
Required -
Specification Valve -
Coating Yes Soil conditionns -
Weight coat No Pressure ratinng -
Cathodic protection Yes Trawler protection -
Insulation material None Jumper type -
Insulation U value -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 26 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 27 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 28 N/A
Removal
Removal type Complete
Disposal
Dispose Yes
Disposal type Scrap
Distance to disposal site 120 km
Cleaning
Clean Yes
Flushing Yes
Pigging Yes
Chemical Yes
Pipeline details
Flow type Liquids
Material Carbon steel
Buckle arrestors Yes
Length 120 km
Nominal diameter 102 mm
Wall thickness 6,02 mm
Crossings 2
Buried length 5 km
Shore approach Yes
Insulation material None
Insulation U value -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 29 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 30 N/A
From FPSO Preprocessing Export end te ermination details
To Gas Landfall Export compoonent FPSO Preprocessing
Flow type Gas Export end wa ater depth 291 m
Length 120 km Export end te ermination type Riser
Export end te ermination sub-type Flexible lazy S
Pipeline details Export end di verless connections Yes
Material Carbon steel Export end su ubsea ESD valve No
Liquid flowrate 0 Mm³/day
Water flowrate 0 Mm³/day Export end PL LET
Gas flowrate 9,94 MMsm³/day Required Yes
Pressure in 113 bara Valve Yes
Pressure out 76 bara Soil Conditionns Average
Fixed pressure Outlet pressure Pressure ratinng 207 barg
Fluid temperature 4 °C Trawler protection No
Buckle arrestors Yes Jumper type Rigid
Size Receiving end d termination details
Nominal diameter 508 mm Receiving com mponent Gas Landfall
Corrosion allowance 3mm Receiving end d water depth -
Wall thickness 15,7 mm Receiving end d termination type Shore approach
Receiving end d termination sub-type Shelving beach
Installation Receiving end d diverless connections -
Lay vessel type S-lay without DP Receiving end d subsea ESD valve No
Pipeline crossings 2
Buried length 5 km Receiving end d PLET
Required -
Specification Valve -
Coating Yes Soil conditionns -
Weight coat Yes Pressure ratinng -
Cathodic protection Yes Trawler protection -
Insulation material None Jumper type -
Insulation U value -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 31 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 32 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 33 N/A
Removal
Removal type Complete
Disposal
Dispose Yes
Disposal type Scrap
Distance to disposal site 120 km
Cleaning
Clean Yes
Flushing Yes
Pigging Yes
Chemical Yes
Pipeline details
Flow type Gas
Material Carbon steel
Buckle arrestors Yes
Length 120 km
Nominal diameter 508 mm
Wall thickness 15,7 mm
Crossings 2
Buried length 5 km
Shore approach Yes
Insulation material None
Insulation U value -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 34 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 35 N/A
PR
TS
Link 011,34 km
PRLink 021,34 km
Riser base 01
Item 01Item 02
Cluster 4 1,34 km No -
S-lay without DP Steel No
Carbon steel - - Carbon steel - -
None - - None - -
- - - - - -
Yes - - Yes - -
Electro-hydraulic Duplex Yes No
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 36 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 37 N/A
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 38 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 39 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 40 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 41 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 43 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 44 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 45 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 46 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 47 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 48 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 49 N/A
PR
TS
Link 011,34 km
Riser base 01
Item 01
Cluster 4 1,34 km No -
S-lay without DP Steel No
Carbon steel - - Carbon steel - -
None - - None - -
- - - - - -
Yes - - Yes - -
Electro-hydraulic Duplex Yes No
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 50 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 51 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 52 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 53 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 54 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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 55 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 56 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 57 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 58 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 59 N/A
Tanker type Conversion
Tanker size (k dwt) Panamax, 0 - 73
Water depth 291 m
Production ratee 0,611 Mm³/day
Water injection n rate 0 Mm³/day
Gas export / in njection ratee 9,94 MMsm³/day
Days of storagge 10 day
Number of riseers 5
General upgraade 100 te
Marine upgradde 200 te
Tanker strengtthening 595 te
Length of sea trials 15 day
Mooring optionn Buoyant turret
Added producttion facilities s weight 7010 te
Elevated deck Yes
Gas lift No
Mooring type Chain
Anchor type Drag embedded
Soil condition Average
Environment c conditions Severe
Wave height 32,2 m
Wind speed 54,5 m/s
Tidal current 0,2 m/s
Mooring chain size 127 mm
Number of mooring lines 6
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 60 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 61 N/A
US Dollars
QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST
PER PER
UNIT MAN HOUR
Tanker strengthening 595 te 154 91 630 60 9 240 5 498 000
Marine / offloading 200 te 194 38 800 60 11 600 2 320 000
General upgrade 100 te 174 17 400 60 10 400 1 040 000
Turret 1 100 te 179 197 200 60 10 800 11 880 000
Riser porch (no. riserss) 0 1 723 0 60 103 400 0
Elevated deck 1 051 te 206 216 507 60 12 400 13 032 000
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 62 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 63 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 64 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 65 N/A
2
3
1
4
6
7
5
8
9
Sep 1
Heat Ex 1 Sep 2
Run Down Cooler
80 15,6 1,92 0,00633 9,56 0,688 17,7
80 15,6 - 0,00248 - - -
80 15,6 - - 9,56 - 17,7
80 15,6 1,92 0,00385 - 0,688 -
79,5 70 1,93 0,00365 0,0702 0,653 20,1
15 70 - - - - -
15 70 - - 0,213 - 24,1
15 70 1,6 0,000531 - 0,693 -
14,5 50 1,56 0,000525 - 0,71 -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 66 N/A
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.
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 67 N/A
Name FPSO Preprocessing
US D ollars
(7 007 te Op.)
Procured f from: Russia (Arctic)
QUANTITYY UNIT RATE COST
Manifolding 14 te 20 500 287 000
Separation 84 te 24 000 2 016 000
Dehydration 0 te 29 000 0
Heating 3 te 31 000 93 000
Shell & tube cooling 2 te 27 500 55 000
Fin fan cooling 0 te 14 800 0
Oil export 6 te 45 200 271 000
Shell & tube 0 te 27 500 0
Fin fan 0 te 14 800 0
Amine / physical solveent 0 te 26 500 0
Zinc oxide vessel 0 te 20 500 0
Zinc oxide bed 0 te 2 850 0
Glycol 77 te 26 500 2 041 000
Molecular sieve vesseel 0 te 20 500 0
Molecular sieve bed 0 te 8 000 0
LTS / exchanger 76 te 26 500 2 014 000
Refrigeration packagee 0 te 57 000 0
Turbo expander 20 te 60 000 1 200 000
Stabiliser 0 te 30 000 0
Gas metering 19 te 31 500 599 000
Compressors and turbinne drivers 137 te 122 400 16 769 000
Compressors and electrric motor dr rivers 9 te 79 000 711 000
Scrubbers 45 te 27 500 1 238 000
Shell & tube coolers 35 te 31 500 1 103 000
Fin fan coolers 0 te 14 800 0
Compressors and turbinne drivers 0 te 0 0
Compressors and electrric motor dr rivers 0 te 94 800 0
Scrubbers 0 te 27 500 0
Shell & tube coolers 0 te 31 500 0
Fin fan coolers 0 te 14 800 0
Fine filters 0 te 20 500 0
Deaerator 0 te 22 000 0
Pumps and turbine driveers 0 te 0 0
Pumps and electric motoor drivers 0 te 46 800 0
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 68 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 69 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 70 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 71 N/A
US Dollars
QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST
PER PER
UNIT MAN HOUR
Primary steel 1 401 te 147 205 947 60 8 820 12 357 000
Secondary steel 2 242 te 194 434 948 60 11 600 26 007 000
Equipment 996 te 40 39 840 60 2 400 2 390 000
Piping 454 te 400 181 600 60 24 000 10 896 000
Electrical 136 te 714 97 104 60 42 800 5 821 000
Instruments 133 te 734 97 622 60 44 000 5 852 000
Others 248 te 294 72 912 60 17 600 4 365 000
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 72 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 73 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 74 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 75 N/A
FFPSO PREPROCESSING EQ
Production manifold
Well kill manifold
Control package
Hydraulic power unit
1st stage separator
2nd stage separator
Heater 1
Run down cooler
Inlet scrubber
Glycol contactor
Gas / glycol exchanger
Lean glycol pump
Rich glycol flash drum
Glycol / glycol exchanger
Rich TEG filter
Glycol regenerator
Glycol regenerator reboiler
Glycol surge drum
Glycol regenerator reflux condenser
Glycol regenerator reflux accumulator
Glycol reflux pump
Cold finger condenser
Cold finger accumulator
Cold finger condensate pump
Dewpoint control exchanger
Low temperature separator 1
Low temperature separator 2
Expander / recompressor (turbo)
QUIPPMEENT LI ST
1 100 80 215 10,8
1 100 207 223 1,43
1 100 1
1 100 0,6
1 100 1,92 Mm³/day 80 84 15,6 12,2 2,45 80,8 3 Phase (Horizontal)
1 100 1,93 Mm³/day 15 15,4 70 4,94 1,65 3,57 3 Phase (Horizontal)
1 100 2,08 80 88 70 0,438 2,8 Shell & tube
1 100 -0,586 15 16,5 50 0,337 1,94 Shell & tube
2 50 9,77 MMsm³/day
2 50 9,77 MMsm³/day
2 50
4 50
2 50
2 50
2 50
2 50
2 50
2 50
2 50
2 50
4 50
2 50
2 50
4 50
1 100 9,77 MMsm³/day
1 100
1 100
1 100
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 76 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 77 N/A
FFPSO PREPROCESSING EQ
HP flare tip
HP flare drum
HP flare drum pump
HP ignition system
LP flare tip
LP flare drum
LP flare drum pump
LP ignition system
Vent tip
Vent KO drum
Halon snuffing system
Seawater lift pump
Chlorination package
Coarse seawater filter package
Jockey pump
Caisson
Fuel gas heater
KO drum
Fuel gas filter
Chemical injection pump
Chemical storage tank
Closed drain vessel
Closed drain pump
Reclaimed oil tank
Reclaimed oil return pump
Oily water tank
Oily water return pump
Non-hazardous caisson
Non-hazardous caisson return pump
Hazardous caisson
Hazardous caisson return pump
Oily water separation tank
QUIPPMEENT LI ST
1 100
1 100
2 100
1 100
1 100
1 100
2 100
1 100
1 100
1 100
1 100
2 100 15,2 Mm³/day
1 100
1 100 15,2 Mm³/day
2 100
1 100
1 100
1 100
1 100
Chemical injection is provided to the wellheads, oil and gas processing, gas compression and water injection systems.
1 100
2 100
1 100
2 100
1 100
2 100
1 100
2 100
1 100
2 100
1 100
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 78 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 79 N/A
FFPSO PREPROCESSING EQ
Firewater pump (diesel)
Firewater lift caisson
Diesel day tank
Firewater jockey pump
Hose reels
Monitors
Hydrants
Cranes
Local lifting devices
HVAC packages
Lifeboats
Conventional control
Remote monitoring
Operational voice radio
Microwave radio
Generator set
Power distribution
Emergency power generator
Flare structure
Quarters
Helideck
QUIPPMEENT LI ST
2 100
1 100
1 100
2 100
1,78
11,7
2 100 4,35 MW 77,8 Solar Centaur 50
54,8 Includes transformers, buses, power cabling between switchboards, switchboards and ancillary controls
0
9,94 MMsm³/day 243 Boom
64 beds 293 600
50
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 80 N/A
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 - - - - - --
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 81 N/A
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 -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 82 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 83 N/A
80 38,9 0,0185 0,000162 0,00163 0,737 16,7
80 38,9 - 0,000125 - - -
80 38,9 - - 0,00163 - 16,7
80 38,9 0,0185 - - 0,737 -
80 38,9 0,0185 - - 0,737 -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 84 N/A
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.
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 85 N/A
Name GTU Plant
US D ollars
Procureed from: N. America
QUANTITYY UNIT RATE COST
Manifolding 2 te 16 600 33 000
Separation 7 te 18 700 131 000
Dehydration 1 te 21 500 22 000
Dehydration (tankage) 0 m³ 48 0
Heating 0 te 24 000 0
Shell & tube cooling 0 te 24 400 0
Fin fan cooling 0 te 12 000 0
Desalting 0 te 21 500 0
Shell & tube 0 te 24 400 0
Fin fan 0 te 12 000 0
Amine / physical solveent 0 te 20 000 0
Zinc oxide vessel 0 te 16 400 0
Zinc oxide bed 0 te 2 700 0
Sulphur recovery 0 te 19 200 0
Tail gas clean up 0 te 18 600 0
Incineration 0 te 18 600 0
Glycol 0 te 20 000 0
Molecular sieve vesseel 0 te 16 400 0
Molecular sieve bed 0 te 7 400 0
LTS / exchanger 0 te 22 000 0
Refrigeration packagee 0 te 45 000 0
Turbo expander 0 te 48 500 0
NGL production / fractioonation 0 te 23 500 0
LPG production / fractioonation 0 te 23 500 0
Gas metering 0 te 28 500 0
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 86 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 87 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 88 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 89 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 90 N/A
US Dollars
QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST
PER PER
UNIT MAN HOUR
Equipment 0 te 30 0 38 1 140 0
Steelwork 20 te 116 2 320 38 4 410 88 000
Piping 13 te 410 5 330 38 15 600 203 000
Electrical 0 te 585 0 38 22 200 0
Instruments 0 te 880 0 38 33 400 0
Others 0 te 300 0 38 11 400 0
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 91 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 92 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 93 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 94 N/A
GGTTU PLANT EQUIPMENT LIS
Control package
Hydraulic power unit
1st stage separator
Dehydrator
Recycle pump
Fired heater package
Heating medium make-up tank
Heating medium make-up pump
Expansion vessel
Heating medium filter
Heating medium circulation pump
CCCW expansion / make-up tank
Water / CCCW exchanger
CCCW circulation pump
Cooling medium filter
HP flare tip
HP flare drum
HP flare drum pump
HP ignition system
LP flare tip
LP flare drum
LP flare drum pump
LP ignition system
Vent tip
Vent KO drum
Halon snuffing system
ST
1 100 1
1 100 0,6
1 100 0,0185 Mm³/day 80 84 38,9 5,23 1,05 6,73 3 Phase (Horizontal)
2 100 80 38,9 0,288 1,42 0,606 Molecular sieve
2 100
1 100
1 100
2 100
1 100
1 100
2 100
1 100
1 100
2 100
1 100
1 100
1 100
2 100
1 100
1 100
1 100
2 100
1 100
1 100
1 100
1 100
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 95 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 96 N/A
GGTTU PLANT EQUIPMENT LIS
Firewater pump
Foam unit
Firewater storage tank
Hose reels
Monitors
Hydrants
Cable / fibre
Conventional
Generator set
Power distribution
Emergency power generator
ST
2 100
100
2 100 0,23 MW 6,04 Diesel / gas engine
5,06 Includes transformers, buses, power cabling between switchboards, switchboards and ancillary controls
1,96
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 97 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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 98 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 99 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 100 N/A
Location Coastal
Terrain Grassland
Elevation 0 m
Oil Gasoline NGL LPG
Inlet flows 0 Mm³/day 0 Mm³/day 0 Mm³/day 0 Mm³/day
Method of expporting - - - -
Marine export t type --
Distance to m ooring --
Prefabricationn Other -
Piping spools Yes 75%
Steelwork Yes 75%
Increased gravel base depth No
Winterisation of facilities No
Product storagge Oil NGL LPG Gasoline
Number of day ys storage - - - -
Storage capaccity - - - -
Pressure vesssel type - - - -
Number of ves ssels - - - -
Vapour spacee - - - -
Design capacity / vessel - - - -
Number of tan nks - - - -
Design capacity / tank - - - -
Diameter - - - -
Height - - - -
Length - - - -
Product exporrt
Export rate - - - -
Pump differenntial pressure - - - -
Total pump po ower - - - -
Metering - - - -
Driver type - - - -
Derating factoor - - - -
Derating baseed on - - - -
Derated poweer - - - -
Elevation - - - -
Training - - - -
Sparing % - - - -
Driver model - - - -
Driver rating - - - -
Pump weight - - - -
Pump driver w weight - - - -
Metering capaacity - - - -
Metering weigght - - - -
Pipeline
Material - - - -
Liquid flowratee - - - -
Length - - - -
Pressure - - - -
Pressure in - - - -
Pressure out - - - -
Fluid temperature - - - -
Nominal diameter - - - -
Corrosion alloowance - - - -
Wall thicknesss - - - -
Control systemm Conventional
Communicatioon system Cable / fibre
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 101 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 102 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 103 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 104 N/A
US Dollars
QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST
PER PER
UNIT MAN HOUR
Equipment 0 te 30 0 38 1 140 0
Steelwork 4 te 116 478 38 4 410 18 000
Piping 2 te 410 769 38 15 600 31 000
Electrical 0 te 585 0 38 22 200 0
Instruments 0 te 880 0 38 33 400 0
Others 0 te 300 0 38 11 400 0
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 105 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 106 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 107 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 108 N/A
Location
Terrain Grassland
Field in existinng oil or gas p roducing are ea Yes
Production fa cility access is s good No
Terminal facillity access is g good No
Distances to m major populations
Production fa cility distance to major po pulation 250 km
Terminal facillity distance to o major popuulation 50 km
Roads
Distance from m production fa acilities to ro oad network 250 km
Distance from m terminal facilities to road d network 50 km
Distance from m production fa acilities to te rminal facilities 0 km
Distance from m production fa acilities to we ellpad groups 0 km
Distance from m regasification n facilities to o road network 0 km
Other 0 km
Total 300 km
Railway
Distance from m terminal facilities to rail n network --
Distance from m regasification n facilities to o rail network --
Other --
Total --
Airstrip
Number of air rstrips 1
Construction camp Construction (000s) Nominal duration Men
Wellpad groups 0 mhr 6 month 0
Production fa cilities 82,6 mhr 10,8 month 70
Terminal facillities 12,5 mhr 6,16 month 20
Regasification n facilities 0 mhr 6 month 0
Other 0
Total 90
Operations ca amp
Number of op perations persoonnel --
Company admministration off fices
Number of ad dministration st taff --
Permanent ho ousing
Number of ad dministration pe ersonnel --
Number of pro ojects personnnel --
Total permanent housing --
Medical / hospital facilities
Number of be eds --
Schools, placces of worship and commuunity buildings
Number of pe ersonnel to proovide for --
Power transmmission
Lines to produuction facilitiess 0 km
Lines to termiinal facilities 0 km
Lines to regassification facilitties 0 km
Total power li ne length 0 km
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 109 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 110 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 111 N/A
Terrain Grassland Manifolding Yes
Elevation 150 m Compression Yes
Production Yes
Water injection 0 Mm³/day Acid gas / HP / H HT No
Export / flared gas 0 MMsm³/day Ambient air temperature 22 °C
Gas injection 0 MMsm³/day Reservoir pressure 207 bara
Gas lift 0 MMsm³/day
Fluid capacities
Inlet high pressure fl uids Inlet medium pre essure fluids
Arrival temperature 38,9 °C Arrival temperatture 0 °C
Arrival pressure 80 bara Arrival pressure 0 bara
Well stream fluids Partially stabiliseed fluids
Oil / condensate 0,0159 Mm³/day Oil / condensatee 0 Mm³/day
Produced water 0 Mm³/day Produced water 0 Mm³/day
Gas 0 MMsm³/day Gas 0 MMsm³/day
Separated fluids Total capacities
Oil / condensate 0 Mm³/day Oil / condensatee 0,0159 Mm³/day
Produced water 0 Mm³/day Produced water 0 Mm³/day
Gas 0 MMsm³/day Gas 0 MMsm³/day
Prefabrication Winterisation
Type Other - Increased founddation No
Piping spools Yes 75% Winterisation of facilities No
Steelwork Yes 75%
Manifolding Flowlines Operating pressuree Design pressuree Weight
Production 0 - - --
Test 0 - - --
Water injection 0 - - --
Gas injection 0 - - --
Gas lift 0 - - --
Well kill - - --
Control package 1 te
Hydraulic power 0,6 te
Oil processing Trains Des. cap./train Pressure Temp. out Wt / train Duty Type
Separator 1 1 100% 80 bara 38,9 °C 6,73 te 3 Phase (Horizonttal)
Separator 2 - - - - - --
Separator 3 - - - - - --
Test separator - - - - - --
Dehydrator 2 100% 80 bara 38,9 °C 0,303 te - Molecular sieve
Desalter - - - - - - --
Stabiliser - - - - --
Heat exchanger 1 - - - - - --
Heat exchanger 2 - - - - - --
Heat exchanger 3 - - - - - --
Heat exchanger 4 - - - - - --
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 112 N/A
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 -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 113 N/A
Power generation
Wellpads 0 MW Water injection 0 MW
Export pumping 0 MW Custom equipmeent 0 MW
Oil processing Produced water treatment 0 MW
Oil pumps 0 MW Utilities 0,0743 MW
Oil and water pumps 0 MW Controls and commms 0,1 MW
NGL pumps 0 MW Base load 0,0174 MW
LPG pumps 0 MW Emergency power 0,152 MW
Gasoline pumps 0 MW
Water pumps 0 MW Type Power generation a and distribution
Gas processing Ambient temperaature 22 °C
Gas cooling 0 MW Derating factor --
Gas dehydration 0 MW Total power 0,192 MW
Acid gas removal 0 MW Design factor 1,2
Dewpoint control 0 MW Design power 0,23 MW
NGL production 0 MW Number of generators 2
LPG production 0 MW Design duty/generator % 100
Compressors Driver type Diesel / gas enginee
Flash gas 0 MW Model --
Export 0 MW Driver power --
Gas lift 0 MW Generator set we eight 6,04 te
Gas injection 0 MW Distribution weigght 5,06 te
Emergency power weight 1,96 te
Civils area
Manifolding 0 m² Export pumping
Oil processing Oil 0 m²
Separation / stabilisation 25,2 m² Oil and water 0 m²
Heating 0 m² NGL 0 m²
Cooling 0 m² LPG 0 m²
Dehydration (vesselss...) 0,332 m² Gasoline 0 m²
Dehydration tankage 0 m² Water 0 m²
Desalting 0 m² Metering
Gas processing Oil 0 m²
Cooling 0 m² Oil and water 0 m²
Gas dehydration 0 m² NGL 0 m²
Acid gas removal 0 m² LPG 0 m²
Dewpoint control 0 m² Gasoline 0 m²
NGL production 0 m² Water 0 m²
LPG production 0 m² Gas 0 m²
Others Storage
Gas compression 0 m² Atmospheric 0 m²
Water injection 0 m² Pressurised 0 m²
Custom equipment 0 m²
Produced water 0 m² Total foundation area 124 m²
Utilities 69,9 m² Total plot area 771 m²
Power generation 27 m² Vehicular accesss 62,2 m²
Power distribution 1,84 m² Buildings 24,9 m²
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 114 N/A
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 -
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 115 N/A
Cold finger
Number of trains 5
%Design cap/train 100
Pressure 70 bara
24 kg/MMsm³
-21,7 °CDewpt
Water
Incineration
Claus
Claus unit and tail ga
Tail gas unit only
Selexol
Number of trains 1
%Design cap/train 100
H2S 0 ppm
CO2 0 %
5421
Gas metering
Gas product spec. Flare / Fuel
Expander
Number of trains
Design cap/train
-
Dewpoint controlDehydrationAcid gas removalCooling
Coolant inlet temp.
20 °C
Ambient air temp.
22 °C
Shell & tube
Fin fan
41 °C
0,00163 0,00163 0,00163 0,00163 0,00163 - MMsm³/day
- - - - - 0,0185 Mm³/day
38,9 38,9 38,9 38,9 38,9 38,9 °C
80 80 80 80 80 80 bara
0 0 0 0 0 0 %
0 0 0 0 0 0 ppm
16,7 16,7 16,7 16,7 16,7 -
- - - - - 0,737 s.g.
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 116 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 117 N/A
Name LNG Plant
US D ollars
Atmospheric 0 m³ 47 0
Pressurised 0 te 4 900 0
Oil 0,0 te 41 500 0
Oil and water 0,0 te 41 500 0
NGL 0,0 te 41 500 0
LPG 0,0 te 41 500 0
Gasoline 0,0 te 41 500 0
Water 0,0 te 41 500 0
Liquid metering 0 te 20 500 0
Compressors and turbinne drivers 0 te 0 0
Compressors and electtric motor d drivers 0 te 64 300 0
Scrubbers 0 te 21 400 0
Shell & tube coolers 0 te 24 400 0
Fin fan coolers 0 te 12 000 0
Compressors and turbinne drivers 0 te 0 0
Compressors and electtric motor d drivers 0 te 64 300 0
Scrubbers 0 te 21 400 0
Shell & tube coolers 0 te 24 400 0
Fin fan coolers 0 te 12 000 0
Fine filters 0 te 19 200 0
Deaerator 0 te 20 000 0
Pumps and turbine drivvers 0 te 0 0
Pumps and electric mottor drivers 0 te 46 800 0
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 118 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 119 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 120 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 121 N/A
US Dollars
QUANTITY MAN HOURS MAN HOURS COST UNIT RATE COST
PER PER
UNIT MAN HOUR
Equipment 0 te 30 0 38 1 140 0
Steelwork 20 te 116 2 320 38 4 410 88 000
Piping 13 te 410 5 330 38 15 600 203 000
Electrical 0 te 585 0 38 22 200 0
Instruments 0 te 880 0 38 33 400 0
Others 0 te 300 0 38 11 400 0
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 122 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 123 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 124 N/A
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 $
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 125 N/A
LLNG PLANT EQUIPMENT LIS
Control package
Hydraulic power unit
1st stage separator
Dehydrator
Recycle pump
Fired heater package
Heating medium make-up tank
Heating medium make-up pump
Expansion vessel
Heating medium filter
Heating medium circulation pump
CCCW expansion / make-up tank
Water / CCCW exchanger
CCCW circulation pump
Cooling medium filter
HP flare tip
HP flare drum
HP flare drum pump
HP ignition system
LP flare tip
LP flare drum
LP flare drum pump
LP ignition system
Vent tip
Vent KO drum
Halon snuffing system
ST
1 100 1
1 100 0,6
1 100 0,0185 Mm³/day 80 84 38,9 5,23 1,05 6,73 3 Phase (Horizontal)
2 100 80 38,9 0,288 1,42 0,606 Molecular sieve
2 100
1 100
1 100
2 100
1 100
1 100
2 100
1 100
1 100
2 100
1 100
1 100
1 100
2 100
1 100
1 100
1 100
2 100
1 100
1 100
1 100
1 100
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 126 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 127 N/A
LLNG PLANT EQUIPMENT LIS
Firewater pump
Foam unit
Firewater storage tank
Hose reels
Monitors
Hydrants
Cable / fibre
Conventional
Generator set
Power distribution
Emergency power generator
ST
2 100
100
2 100 0,23 MW 6,04 Diesel / gas engine
5,06 Includes transformers, buses, power cabling between switchboards, switchboards and ancillary controls
1,96
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 128 N/A
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
QUE$TOR © IHS Штокман учебный 25 января 2016 г. - 20:21
Licence number: N/A Page 129 N/A
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
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