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Imagination at work
Subsea Production Systems Engineers Ireland – Dublin Tony Pincombe – Regional Sales Leader Ashish Jain – Principal Engineer 7th October 2015
SUBSEA TREES SUBSEA CONTROLS POWER & PROCESSING SUBSEA WELLHEAD SYSTEMS
INTEGRATED INTELLIGENCE FROM FLOOR TO SHORE
Subsea products and services
SPS (Subsea Production Systems) = Trees+ Controls + Manifolds + Power & Processing
Power, boosting, and compression solutions for both mature and new field developments
Complete portfolio to cover diverse field types, water depths, and operating environments
Industry leading technology to enable safe and reliable operation of subsea production systems
SPECIALTY CONNECTORS & PIPE
FLOATING PRODUCTION SYSTEMS
WELLSTREAM FLEXIBLE PIPE SERVICE & SUPPORT
• Field service • Fleet and equipment • Storage and asset management • Triple S • SmartCenter
Dynamic risers, static flowlines, subsea and topside jumpers and fluid transfer lines to meet the demands of subsea and FPSO production.
TECHN
OLO
GY SO
LUTIO
NS
MANIFOLDS & CONNECTION SYSTEMS
Production Manifolds and connections portfolio to handle various field configurations
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Subsea Production Trees Subsea Controls Systems
EPC Field Development
Subsea Drilling Systems
Platform Aftermarket Products &
Services
Capital Drilling
Equipment TLP & SPAR
Systems
Subsea Processing, Boosting, Compression,
Subsea Manifolds Subsea Connections
The GE Oil & Gas World Surface Drilling & Completions
Onshore Surface Drilling &
Completions Offshore
Onshore Aftermarket
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0 – 100m
“S Series”
SVXT
SHXT
100 – 750m
“M Series” MVXT MHXT
750 – 3000m
“D Series” DVXT
DHXT
Depth Vertical Horizontal
Subsea Tree Structured Product Landscape
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https://youtu.be/x8dXonwMjYw
Deep Water Vertical Tree Installation
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Downhole Pressure & Temp (DHPT) Cards
Transformer Module
Power Supply and Diplexer Cards
Data Acquisition & Control Cardframe
Power Supply Cardframe
Front End Assembly
Electrical Connectors
SemStar5 – the Brain behind subsea
GE’s Subsea Power & Processing Toolbox
Boosting Compression
Prezioso -92
Power Separation
KBS -92 Troll Pilot -99 Tyrihans -07
Increase Oil Recovery and production rate from maturing subsea wells
Remove water from oil stream at the seabed – and re-inject back into reservoir
Drive gas from matured subsea wells to host ..and all these systems
need power, delivered at the seabed
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Imagination at work
Subsea Compression Game Changer for the Atlantic Margin
Ashish Jain – Principal Engineer 7th October, 2015
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© 2015 General Electric Company - All rights reserved
Atlantic Margin - Introduction
Offshore west of Ireland is largely unexplored and least understood region of Europe
The Irish Atlantic Margin Basins share similarities to Atlantic Margin hydrocarbon basins in the UK and Norway
The Corrib Gas Field in the Slyne Basin was successfully appraised and opened up a new play in the region. The field has estimated gas reserve of 1.0 TCF.
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“The Atlantic Margin from Norway to Ireland: geological review of a frontier continental margin province”, Shannon et. al., Petroleum Geology Conference 2005.
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Atlantic Margin - Prospect Drilling by Providence in Dunquin North demonstrated presence of working petroleum system Ref: offshoreenergytoday
Recoverable resources at Spanish Point between 100 mmbo and 202 mmbo Ref: www.rigzone.com
Kosmos Energy identified two new prospects, Doyle A and Doyle B, prospective resources of 123 mmbo and 69mmbo
Europa Oil & Gas also identified two prospects, named Beckett, Wilde & Shaw, prospective resources of 760 mmbo and 493 mmbo Ref: offshore-technology
High interest by several operating companies in recently concluded licensing round further indicates the potential in the region
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Water depth range from 400m – 3000m, step out in excess of 100km
Ref: www.energy-pedia.com
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Challenges for deep water field development
Deepwater and a harsh environment, is a high-cost environment for designing and development of any discovery
Conventional platforms are not feasible in deeper water
With offshore activities, personnel risk exposure is multifold
Flow assurance is a critical challenge,
o High pressure, high temperature developments
o Low ambient temperature
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Brage platform, North Sea, Norway Ref: offshore-technology
Field development with subsea system can offer techno economic viable solution
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Subsea production system
The exploitation of subsea oil and gas fields is a mature industry that relies on qualified components and systems like subsea trees, flowlines, manifolds and electro-hydraulic control systems.
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Why subsea processing?
Subsea Processing Adding Value Green Fields
Long offsets Increased Recovery by Boosting
Deep waters Increased Recovery by Separation
Near shore Development Enabler
Small field Tie-in Alternative
Brown fields Increased recovery
Deck space alternative
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The evolution of more than 50 years of increased oil recovery
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Challenging market dynamics for technology investment
No. of subsea trees installed /yr [Quest]
0
150
300
450
600
1960 1980 2000 2020
20 years to adopt
Subsea boosting is at same stage as subsea trees were in c1981
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50
100
150
0 10 20 30 40
Subsea boosting just reaching the
20 year mark
? Can we use the past to predict the future?
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GE … Subsea, Processing and Power
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Power Conversion
Turbomachinery
Power Conversion
• Gas compression • Pumping
Power & Water • Water treatment
System design and integration: Components: • Controls • MECON connectors • Electrical actuators
• P/T sensors • Leak detection • Acoustic monitoring • Flow metering • RM&D
Measurement & Control
Subsea Systems
Drilling & Surface • Electrical submersible pumps
Processing System • Gas compression • Full Wellstream boosting • Seawater injection • Separation & boosting
• Topside power supply • VSD • UPS • Switchgear • Electrical motors
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Title or Job Number | XX Month 201X 16
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What is subsea compression?
Compression system on sea bed
Increased recovery by reducing back-pressure on the reservoir
Typically less pressure ratio compared to compressor at host facility, lower power need
Enable transport of wellstream over long distances (flow assurance concerns)
Reduces need for offshore manning
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Technology development based on conventional compression system
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Marinization of topside system Mainly suitable for larger fields
https://youtu.be/Ew1h9aU4odo
Ormen Lange Pilot , Nyhamna
Photo: Svein Roger Ivarsen / Norske Shell
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Exploring the subsea compression business case
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• Simple reservoir, production and pipeline model
• Rystad Energy … water depth, reservoir depth, step-out, reservoir size, plateau production rates
• CAPEX and OPEX for entire system from topside to subsea
• Time period 2012-2030
• Run on >1100 gas fields around the world
KEY CRITERIAOverall system CAPEX (Station with cables) (MUSD) 251 176 177 177 158 159 159 189Unavailability - A 0,050 0,036 0,036 0,036 0,031 0,031 0,031 0,037Unavailability - B 0,0005 0,0003 0,000 0,000 0,000 0,000 0,000 0,000System availability 0,950 0,963 0,963 0,963 0,969 0,969 0,969 0,963Cost of maintenance per year 1,8 1,6 1,6 1,6 1,2 1,2 1,2 1,6Minimum TRL 0 0 0 0 0 0 0 0Average TRL 6 5 5 5 5 5 5 5Development cost (MUSD) 0 0 0 0 0 0 0 0Time to market (year) 0 0 0 0 0 0 0 0
INTERVENTION VESSEL CALCULATIONNo of days for light vessel per year 7 6 6 6 5 5 5 6No of days for heavy vessel per year 15 12 12 12 12 12 12 12Days of lost production based on availability 18 13 13 13 11 11 11 14
PRESENT COST AFTER TAXESPresent cost of power MUSD 5 6 6 6 6 6 6 6Present cost of CO2 tax MUSD 1 2 1 1 2 1 1 1Present cost of NOX tax MUSD 0 0 0 0 0 0 0 0Present cost intervention MUSD 8 7 7 7 7 7 7 7Present cost of maintenance 2 2 2 2 1 1 1 2Present cost lost production MUSD 29 21 21 21 18 18 18 22Present cost insurance MUSD 8 6 6 6 5 5 5 6Present cost facility and personell MUSD 3 3 3 3 2 2 2 3CAPEX after tax 251 176 177 177 158 159 159 189Company cost on CAPEX after tax 25 18 18 18 16 16 16 19Total present cost 333 240 240 240 216 216 216 254
SAVINGS ESTIMATE TOWARDS BENCHMARKSavings only on compression station CAPEX (%) 31 % 31 % 31 % 42 % 41 % 41 % 24 %Savings on total CAPEX (%) 30 % 30 % 30 % 37 % 37 % 37 % 25 %Savings on total present cost (%) 28 % 28 % 28 % 35 % 35 % 35 % 24 %Savings on total CAPEX (MUSD) 75 74 74 93 92 92 62Savings on total present cost (MUSD) 93 93 93 117 117 117 79
Subsea compression concept evaluation tool
Market Need Technology choice
• Holistic view required while evaluating different system options
• Avoid simply moving cost around the system or shifting CAPEX to OPEX
Key findings from business case analyses
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Simplified, robust, low cost centrifugal wet gas compression system best option
• 245 target candidates between 2012-2030
• 217 fields profitable with compression
• 82 profitable with subsea compression
• 11 subsea compression best option
• 3 early subsea compression best option
• Almost 100% of profitable subsea cases
• <1500m, <2% LVF
• The largest savings are obtained with a system having only a wet gas compressor
• Lower savings on longer step-outs since the cable cost becomes dominant .
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Next generation subsea compression
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• Dry gas compressor • Separate pump • Scrubber • AMB, AMBCS, UPS • Subsea VSD ~50km
• Wet gas compressor • No pump • Simple slug catcher/distributer • Topside VSD for longer stepouts
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BlueC™ Subsea Motor-compressor
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• Vertical configuration
• Configurable from 4-20 MW
• Closed loop cooling system
• Single shaft line (rigid coupling)
• Canned Active Magnetic Bearings
Compressor designed for subsea
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Wet gas compression challenges
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Technical Challenges
• Performance prediction
• Rotor dynamics
• Mechanics
• Droplets erosion
• Fouling
Considerable amount of experience from compression in wet conditions Strong foundation to develop centrifugal wet gas compression
Droplet erosion
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3rd generation system design
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System and technology development by one integrated team
• Base design case … two train station for long step-out with two inlets
• Subsea power distribution
• All electric
• Integrated manifold providing full flexibility
• Active cooling
• Standard module sizes ... Simple intervention and sparing
• 6m x 6m x 12m (LxWxH): 60 tons
• 12m x 6m x 12m (LxWxH): 250 tons
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Main wet gas compression system modules
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Three standard modules that can be used to build field specific systems
6 x 6 x 12 m 60 tons
Cooler Module HV Power Module
12 x 6 x 12 m 250 tons
Compressor Module
12 x 6 x 12 m 168 tons
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Title or Job Number | XX Month 201X 26
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Hypothetical Case study Corrib gas field Using web based information
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Corrib gas field facts
Pipeline 20” (510 mm)
Design pressure 345 bara, Operating pressure of pipeline 90-110 bara
Composition: 97% methane and ethane
Onshore processing capacity 9.0MSCMD, About 10 years field life
Estimated GIIP, 1.0 TCF
Estimated recoverable reserves, 0.6 TCF
Onshore arrival pressure 85 bara
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Ref: offshoreenergytoday
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Subsea compressor for Corrib gas field Prediction using GE in-house tool
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Additional 18% recovery achievable with subsea compressor One subsea compressor of about 8MW
Normalized production curves Normalized cumulative production
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Possible solution for Corrib
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