Will subsea production make topside obsolete
Transcription
Will subsea production make topside obsolete
“Will subsea production make topside obsolete” Floating Production 2010 Ove Jahnsen Manager – Early Phase and Market [email protected] 1 Content • Subsea market development • Subsea Processing • New enabling subsea technology breaking boundaries • Subsea Today's and Future solutions • Major Projects 2 FMC Offshore Capabilities Light Well Intervention Metering & Control Systems Surface Well Systems Subsea Drilling Systems Standard Subsea Trees Subsea Processing Subsea Manifold Smart Well Control Systems Subsea Template Systems 3 Guidelineless Deepwater Trees ROV Tie-In Systems Subsea Development last 10 years • Number of wells per year since 2000 (x-mas trees) 1,200 # of Subsea Trees 1,000 800 600 400 200 0 2000 2001 2002 2003 2004 2005 2006 2007 2008 2009e 2010e 2011e 2012e 2013e Award Year Tree Orders (High) Tree Orders (Mean) 4 Tree Orders (Base) ©2009 Quest Offshore Resources, Inc. Supply growth from offshore Global production of oil, condensate and gas - Thousand boe/d 120000 100000 Onshore wells 80000 60000 Subsea wells 40000 Topside wells offshore 1990 1992 1994 1996 1998 2000 2002 2004 2006 2008 2010 2012 2014 2016 2018 2020 2022 2024 2026 2028 2030 20000 5 Will subsea wells be preferred – Yes, driven by deeper waters.. 02.01.1980 200 100 0 -100 -200 -300 -400 -500 -600 -700 -800 -900 -1000 -1100 -1200 -1300 -1400 -1500 -1600 -1700 -1800 -1900 -2000 -2100 -2200 -2300 -2400 -2500 -2600 -2700 -2800 -2900 -3000 02.01.1990 03.01.2000 03.01.2010 Zakum Gullfaks Troll Gas Troll Oil Åsga rd Shah Deniz Zafiro Girassol Dry Trees Partly subsea wells Only subsea wells Most deepwater fields with subsea wells Ormen Dalia Roncador (however compliant towers, TLPs, spars have dry trees to 530, 1500 and 1700m respectively) Marlim Sul 6 6 Moving into Deeper Waters Strong subsea track record World record water depths achieved by FMC Technologies 7 Subsea vs Topside • Most floating production system would required a subsea production system. • Most of subsea production systems have a host, majority of these are floating production units. • “Subsea to the beach” is a fairly new term, but not widely applied today. The few examples are Snøhvit and Ormen Lange in the Norwegian North Sea, both gas fields. – Snøhvit approx 150 km tie back – Ormen Lange approx 120 km tie back • The trend is that an increased number of marginal satellite fields are tied into already existing topside, i.e. utilize topside to its optimum capacity to avoid to build new and expensive platforms. 8 Ormen Lange – Subsea to the beach • Supplied by FMC • Tie back distance 120 km • Water Depth 900 -1100 m • Start production 2007 • Gas filed with condensate • Depleting pressure - Gas compression required 9 Subsea Scope Expansion Expanding subsea solutions strategy Core Products New Products • • • • • • • • Subsea Processing − Separation − Boosting − Gas Compression Light Well Intervention Trees Manifolds Control Systems Template Systems Flowline Connection Systems Umbilicals & Flowlines Workover systems 10 Subsea Processing Enhancing brownfield oil recovery and enabling greenfield development • Brownfield challenges: − − − • Greenfield challenges: − − − • Declining oil & gas production Increasing water production Constrained topside facilities Heavy oil Low reservoir pressure Hydrate formation Subsea processing solutions: − − − − − − − − 3 phase separation Gas & Liquid Separation Sand Removal Water removal and reinjection Gas removal and reinjection Single and Multiphase Boosting Gas compression Raw Seawater Injection 11 SUBSEA PROCESSING “Subsea Processing – Todays and future solutions” 12 Subsea Processing Evolution Subsea to Market Subsea Compression Compact Separation Raw Seawater Injection Gravity Separation Boosting 13 Why Subsea Processing • Increased recovery • Accelerate production • Reduced Capital Expenditure • Makes it possible to: – connect satellite fields to existing infrastructure – exploit fields that are normally inaccessible – exploit costly infrastructure fully throughout the systems operational period – depressurize system as a hydrate strategy • Influence on the environment will decrease • Reduces water disposal to sea • Enhances flow management What influence selection of separation technology? • Drivers for subsea processing station – System considerations, not only component considerations – Flexibility over the life of field, need to cover changes in conditions and uncertainties • Fluid properties – Density, viscosity, mixed viscosity, inversion point etc at operational conditions, asphaltenes, ”schmoo”, creation of foam, emulsions etc. • Production profile – Water cut (WC), gas volume fraction (GVF) as function of time – Pressure, temperature profile as function of time • Sand production – During ”normal” conditions and ”worst case” conditions (e.g. screen failure) • Field layout – Field layout of wells/drilling centers/existing infrastructure – Sizes of pipelines – Location of processing station compared to wells 15 Future Solutions • Moving from bulk gravity separation …… Tordis oil/water separator Pazflor gas/liquid separator 16 ……to slimmer and more compact solutions…… Caisson separator cluster in deep water PipeSeparator Caisson separator in GoM 17 ……to inline, ultra-compact solutions • Proven topside technology • Ongoing qualification for subsea use CDS Inline deliquilizer 18 Subsea pumping •Multi Phase pump - Helicoaxial or Twin Screw •Single phase pump - Centrifugal •Hybrid pump - Helicoaxial + Centrifugal •Seabed ESP – Horizontal or Vertical •Applications: •Single Phase Oil/water •Single Phase Water Injection •Single phase Raw Seawater injection •Multiphase Oil/Water/gas Sulzer/FMC 19 Subsea compression - What are the drivers • IOR – Accelerated production – Reservoir depletion – Maintain production – Utilize existing infrastructure and extend the field life time • Flow assurance – Maintain gas velocity to avoid liquid accumulation in multiphase flow. • Subsea to beach – Compensating pressure drop in transport system – Avoid surface installations – Environmental issues as harsh conditions • CAPEX / OPEX considerations 20 FMC’s Subsea Processing Major Projects Activity in every major deepwater basin Tordis • Brownfield • Gas/Oil/Water/Sand Separation • Boosting/Water Injection • Installed 2007 Cascade • Greenfield • Boosting • To be Installed 2010 Pazflor • Greenfield • Gas/Liquid Separation • Boosting • First oil 2011 Perdido • Greenfield • Gas/Liquid Separation • Boosting • Installed 1Q 2010 Marlim • Brownfield • Gas/Oil/Water/Sand Separation • Water Injection • First oil 2011 Greenfield BC-10 • Greenfield • Gas/Liquid Separation • Boosting • Installed 3Q 2009 Brownfield 21 Statoil Tordis LANDMARK: FIRST SEMI-COMPACT SEPARATOR WITH SAND MANAGMENT Project Overview Contract Award: Water Depth: Step Out: Design Pressure: 2005 220 meter 12 km 3,000 psi Project Scope of Supply Subsea Separation, Injection & Boosting Station Process Capacity: 220 000 bbl/day MultiPhase Pump: Helico-Axial to 68% GVF 1.8 MW 450 psid Water Injection Pump : Single Phase 2.3 MW 1100 psid Sand Removal System Tordis Project Challenges: • Increasing water production • Declining pressure in wells • Limited topside water handling capacity • Sand production 23 StatoilHydro – Tordis Project Enhancing Brownfield Oil Recovery • First full-scale subsea separation system • Gas/Oil/Water/Sand Separation • Increase recovery from 49% to 55% • Potential to recover additional 35 million barrels of oil Project Partners: 24 Project Status • Tordis Subsea Separation has been running more that 2000 hours with success. • Problem during start up solved and normal operation achieved. • Experience so far is very positive. • Experienced problems with disposal reservoir shut down in 3Q 2008 • Phased restart of system in 3Q 2009 25 Shell Perdido LANDMARK: FIRST GoM FULL FIELD SEPARATION & BOOSTING SYSTEM Project Overview Contract Award: Water Depth: Step Out: Design Pressure: 2007 2.800 meter 0 mi 4,500 psi Project Scope of Supply 5 Gas-Liquid Separator DVA Caissons Systems Process Capacity : 25,000 bopd and 1600 MSm3/d Gas Tolerant ESP: ESP to 15% GVF 25,000 bopd pump systems Centrifugal gas inlet and large slug handling capacity Shell design subsea boosting system Total Pazflor LANDMARK: FIRST WEST AFRICAN GAS-LIQUID GRAVITY SEPARATION SYSTEM Project Overview Contract Award: Water Depth: Step Out: Design Pressure: 2007 900 meter 14 Km 2,750 psi Project Scope of Supply 3 Gas-Liquid Separation Systems Process Capacity : 110,000 bopd and 1.0 MMSm3/d Gas Tolerant Pump: Hybrid to 18% GVF 2 x 55,000 bopd pump systems Hybrid pump system with subsea barrier fluid control Pazflor Project 3 Gas-Liquid Separator Stations in 800m water depth, 2-4 km step-out » » » Client: Total Location: Angola,W.Africa Delivery: 2011 » Challenges: • • • • • • Deliveries: 3 Gas-Liquid Separator Stations 6 hybrid pump modules (+ 2 spares) Combined Power and service umbilicals Vertical separator with CDS inlet and internals 3 G/L separation station as part of Green Field development Low energy reservoir Highlights Deep water ~ 800m High viscosity and stable emulsion » First Seabed Gas-Liquid Gravity Separation system » Enabling Technology for oil production Large pressure drop in flowlines » Enabling Technology for hydrate andstrategy risers using simplified field architecture High water production from year 4 » Size: 21 x 21 x 19 meters Large amounts of methanol needed for hydrate prevention FREE FLOW NOT POSSIBLE Power Control Module Separator tank 28 Separation Unit The Solution: Subsea Processing • Gas / Liquid Separation and Liquid Boosting: – Gas flows freely to the FPSO • • – Liquid out of separator with relative low GVF • – Hydrate preventions of flowlines by means of depressurization is possible Reduced cost due to elimination of circular flow line Efficient pumps with high ∆P can be used Ô Increased recovery Boosting of liquid • Stabilized flow regime in risers Ô Reduced slugging 29 Petrobras Marlim LANDMARK: FIRST BRAZILIAN FULL FIELD SEPARATION & INJECTION SYSTEM Project Overview Contract Award: Water Depth: Step Out: Design Pressure: 2009 900 meter 5 Km 5,000 psi Project Scope of Supply Subsea separation station with water processing Process Capacity : Pipe Separator 22,000 bpd, 67% water-cut Water Injection Pump: 20,000 bwpd/system 1.9 MW Motor, DP 3000 psi Compact Separators for de-oiling and de-sanding Petrobras – Marlim project Enhancing brownfield oil recovery • First deepwater subsea oil/water separation system • Mature field (brownfield) with heavy oil and increasing water production • Gas/oil/water/sand separation at 3,000 ft. depth • Water reinjected into reservoir to boost production 31 Challenges: Project Operator: • Increasing water production • Limited topside water handling capacity • Sand production Brazil Why FMC? Uniquely Positioned to Deliver Results • Extensive Global Processing Experience and Project Track Record Providing subsea processing solutions since 1992 • Experienced Organization Dedicated Team of Discipline Engineers for SSP • Technology Building Blocks FMC owns separation, meters, subsea motor, fiber optic controls technology etc. • Technology Development and Qualification Qualified numerous subsea processing systems / sub-systems • Front End Engineering Capabilities Feasibility, concept selection, FEED, project execution, installation and operation, flow assurance • Life of Field Services Condition and Performance Monitoring; installation, operation and maintenance support Future? Subsea Production and Subsea Processing will not make topside obsolete. Thank You! www.fmctechnologies.com 33