Wellhead compression - Petroleum Club
Transcript of Wellhead compression - Petroleum Club
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Wellhead compression Multi well – LP gas gathering With screw compressors
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General
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What is it ? Compression close to the wellhead lowers the flowing wellhead pressure, which increases production and prevents liquid
loading. Siemens wellhead compressor solution can thereby substantially enhance the recovery rate.
Why do I need it ? Valuable hydrocarbons will not be produced
Expensive field abandonment is needed soon
Production obligations/ambitions can not be met
New explorations necessary (high risk & investment)
Wellhead compression
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When do I need wellhead compression?
Xmas tree
Gas
Treatment Facility
Transport pipeline
Reservoir High
Pressure
Phase 1: Free flow, well pressure 100-300 bar. No compression needed
Xmas tree
Gas
Treatment Facility
Transport pipeline
Reservoir Medium Pressure
Central
Compression (Restaging)
Phase 2: Well pressure < 80 bar
Xmas tree
Gas
Treatment Facility
Transport pipeline
Reservoir Low
Pressure
Central
Compression (Restaging)
Wellhead compression
Phase 3: Well pressure < 10 bar
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0
Rat
e [M
SC
FD]
2 4 6 8 10 12 14 16 18 20
Time [year]
Dry Well Rate MSCFD
Critical flow rate “Wet” Well Rate MSCFD
Any Gas Well will flow to here…
With Siemens Well head Compression
Declining flow rate, well dies
Extra production potential
Siemens Wellhead Compression
Well life & production rate
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Single or multi well ?
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Main spec single and multi well compr unit
Single well compr Multi well compr No of wells 1 4 - 15 Min inlet pressure ~ atmospheric ~ atmospheric Max discharge pressure 30 bar 50 bar Capacity control 100%-50% 100%-15% Power ~ 35 kW 400 kW – 3 MW
Capacity @ 4 barg 20.000 m3/d 250.000 to 1.500.000 m3/d Peak liquid 8 m3/d [50 bbl] 50-200 m3/d [330-1300 bbl] Remark Piston compressor
Gas engine “combi” Screw compressor (oi) E-motor
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Application single and multi well compression unit
Single well compr Multi well compr Well plot Distributed Centralised (well pad or
cluster) Well size/capacity Small Medium/Large
Availability/reliability Medium High (>98%) Fleet management Complex Simple Transport pressure No Yes Remark Booster station
Electrification
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Case study
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Customer Gazprom
Location West Siberia
Oil injected screw compressor type
Power electric motor 450 kW
Capacity 8.500 MCF/day @ 60 PSI suction
Discharge pressure 100-150 PSI
Inlet pressure 30-100 PSI
Remote operated
Availability 95-98%
Results 5 wells connected:
2x killed wells produce continuously
3x well immediate boost of production
Customer Gazprom
Location West Siberia
Oil injected screw compressor
Power electric motor 450 kW
Capacity 240.000 mn3/day @ 4bara suction
Discharge pressure 7-10 bara
Inlet pressure 2-7 bara
Remote operated
Availability 95-98%
Results 5 wells connected:
2x killed wells produce continuously
3x well immediate boost of production
TCO based on 7 years of operation:
Added costs 0,01 euro / 1 mn3
Added costs 0,35 USD / 1000 CF
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Gazprom – Wellhead compressor for mature gas field
Many of Gazproms natural gas assetsin West Siberia have been producing since the seventies. These depleting assets face severe production decline and liquid loading. For revitalization of their mature wells Gazprom introduced wellhead compression
Multi well compression (5-7 wells hooked up) gives a significant reduction of required units, site preparations and service calls. Condensate, formation water and condensed water. Unit handles slugs and high LTG ratios Package tailored to Russian rules®ulations, Gazproms engineering principles and West Siberian climate (-55°C)
Siemens main contractor Complete functional unit, ready for hook up E-motor driven oil injected screw compressor Installation supervision, commissioning Service
Additional remarks Capacity 225.000 mn3/day @ 4 bara suction Capacity 8 MMSCFD @ 60 PSIa In operation since summer 2011
Customer benefits : Scope of supply: Operational back ground:
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Conceptual study
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Workflow
1. Production modelling
(sub-surface & surface)
2. Equipment (selection,
sizing, pricing CAPEX/OPEX)
3. TCO Economics (production
profiles, cash flows)
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Integrated production modelling
Gas Treatment Facility
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Integrated production modelling
Well cluster A consisting of 7 wells. Well inflow individually considered. Compressor in multi well operation simulated.
Three compressor configurations considered:
1. Actual capacity 4300 ma3/h – Max power 300kW
2. Actual capacity 7100 ma3/h – Max power 600kW
3. Actual capacity 9500 ma3/h – Max power 900kW
Assumptions:
• Start compression winter 2015
• End compression spring 2022
• Availability wells 95%
• Vertical wells
• Low intermediate/discharge pressure selected
• Flow data for a time window of 8 years
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Production modelling Multi-well; Concept 600kW
Killed well End of time frame
Time frame
= No Compression
= WH Compression
First day of operation Well no 1 Well no 2 Well no 3
Well no 4 Well no 5 Well no 6
Well no 7
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Economics
Three compressor configurations considered:
1. Actual capacity 4300 ma3/h – Max power 300kW
2. Actual capacity 7100 ma3/h – Max power 600kW
3. Actual capacity 9500 ma3/h – Max power 900kW
Three compressor drives considered:
A. Gas engine = reciprocating motor [ = Gas ]
B. E-motor; external power @ given MW/h price [ = E ]
C. E-motor; independent power generation 5 MW gas turbine [ = GT ]. Pro ratio usage.
10 concepts = 9 compression concepts + “do nothing scenario”
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Economics
1st killed well
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Economics
First day of
operation
Purchase
Do nothing
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Economics Cum AT cash flow
900kW PG
600kW PG
900 kW gas
300kW PG
600kW gas
600kW E
300kW E
300kW gas
900kW E
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Economics Economic indicators
Compression Scenario
300 kW Electrical
300 kW Elec Pgen 300 kW Gas 600 kW
Electrical 600 kW Elec
Pgen 600 kW Gas 900 kW Electrical
900 kW Elec Pgen 900 kW Gas
Gas Reserves (e6m3) 512,73 512,73 437,86 628,66 628,66 536,28 682,33 681,16 573,09
Total Capital (MRUB) 158,76 184,16 203,21 190,51 234,96 247,67 209,56 279,42 266,72
BT NPV at 0% (MRUB) 587,92 653,63 546,45 593,56 768,96 646,41 549,29 795,98 673,69
BT NPV at 10% (MRUB) 272,03 307,68 232,51 249,41 359,48 276,23 204,42 361,41 283,56
BT NPV at 15% (MRUB) 182,42 208,91 143,98 152,8 242,33 171,51 108,65 237,32 173,29
AT NPV at 0% (MRUB) 463,27 514,71 425,81 466,36 604,72 503,3 430,1 624,37 524,06
AT NPV at 10% (MRUB) 204,97 231,47 168,8 184,34 268,87 200 146,84 266,87 204,25
AT NPV at 15% (MRUB) 131,96 150,92 96,6 105,47 173,19 114,56 68,48 165,28 114,24
Payout BT (months) 51,4 49,26 56,14 57,35 49,18 55,35 62,43 51,2 55,99
Payout AT (months) 54,04 52,19 58,78 59,66 52,36 58,15 64,3 54,37 58,8
ROR BT (%) 39,4 40,98 30,98 30,39 39,55 31,08 24,42 35,99 30,02
ROR AT (%) 34,33 35,37 26,79 26,87 34 26,78 21,71 30,81 25,88
DPI BT at 0% 3,7 3,55 2,69 3,12 3,27 2,61 2,62 2,85 2,53
DPI BT at 10% 1,93 1,88 1,29 1,47 1,72 1,26 1,1 1,46 1,2
DPI BT at 15% 1,37 1,35 0,84 0,95 1,23 0,82 0,62 1,01 0,77
DPI AT at 0% 2,92 2,79 2,1 2,45 2,57 2,03 2,05 2,23 1,96
DPI AT at 10% 1,45 1,41 0,93 1,09 1,29 0,91 0,79 1,07 0,86
DPI AT at 15% 0,99 0,97 0,56 0,66 0,88 0,55 0,39 0,7 0,51
Legend BT = Before Tax AT = After Tax NPV = Net Present Value ROR = Rate Of Return DPI = Discounted Profit Index
CONFIDENTIAL
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Questions?