Deepwater Subsea Tie-Back Flow Assurance Overview M U R P H Y S A B A H O I L C O M P A N Y L T D.

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Transcription:

Deepwater Subsea Tie-Back Flow Assurance Overview 1

Contents Case Study Overview Flow Assurance Basis/Data Results Pre-FEED/FEED Considerations Flow Assurance Field Architecture Technologies 2

Preliminary Concept Preliminary Concept 15 km subsea tie-back 3 manifold locations 8 producers 8 injectors 3

Host Facilities Export Pump and Fiscal Meter Water Injection Production Systems Gas Compression 4 Open Riser Slots 2 Steam Turbines 3 Gas Turbines New Process System TEG and VRU Flare 4

Provisional FA Basis/Data Tie-back field distance from host: 10 to 15 km Water depths: 1250 to 1400 m Production flowrates: 0 to 40 kbpd (provisional) WI flowrates: 0 to 70 kbwpd (provisional) FPSO separator inlet pressures: 13 to 44 bar Water cuts: 0 to 95 % GORs: 500 to 1000 scf/bbl Minimum seabed temperature: 2-4 deg C FWHT: 60 O C 5

Preliminary Results Flowline Sizes Production (provisional 40 kbpd flowrate) 2 x 8-inch piggable loop, or Single 10-inch Water Injection (provisional 70 kbwpd flowrate) Single 12-inch 6

Preliminary Results Pressures FPSO Separator Pressure (barg) Production Flowline Inlet Pressure Requirements at Subsea Wellheads (FWHP) Boosting 44 140 190 bara for 0 90% water cuts - 13 95 150 bara for 0 90% water cuts - 44 165 bara for 90% water cut Riser base gas lift (RBGL) 13 115 bara for 90% water cut Riser base gas lift (RBGL) Potential 40 bar reduction in FWHP requirements with lower separator pressure. Potential 25-35 bar reduction in FWHP requirements with RBGL. Potential 75 bar reduction in FWHP requirements with RBGL + lower separator pressure. 7

Preliminary Results Pressures FWHP requirements are relatively insensitive to GOR, with a GOR of 1000 scf/bbl requiring a marginally lower FWHP than a GOR of 500 scf/bbl. A large proportion of the total system pressure loss is due to elevation head loss up the production risers, i.e. between 80 and 100 bar for a range of water cuts between 0% and 90%. 8

Preliminary Results Temperatures / Insulations Insulation System U Value (W/m 2 K) Minimum Flowrate for a 30 O C FPSO Arrival Temperature (each 8 flowline) Remark Pipe-in-Pipe 1.0 10 kbpd Represents 50% turndown for one flowline, 75% for two flowlines GSPU or Flexible Pipe 3.5 20 kbpd Represents no production turndown for 40 kbpd The 30 O C FPSO arrival temperature is provisional. Measured WATs range from 17 to 24 O C. Insulation selection depends on the wax appearance temperature (WAT) and production profile. 9

Pre-FEED/FEED FA Considerations Production Enhancement Assess feasibility and benefits of low FPSO separator pressure, subsea boosting, riser base gas lift, and any combinations of the EOR options Wax / Hydrate / Solids Mitigation and Management Evaluate dual piggable loop flowlines vs. single flowline Assess insulation requirements, e.g. GSPU, PIP Assess stabilized crude flushing requirements Assess direct electrical heating requirements Assess wax gel breaking requirements Assess wax appearance temperature sensitivity Assess wax/hydrate inhibitor injection requirements, e.g. low turndown rates 10

Field Architecture Considerations Seabed features and shallow hazards Existing man-made seabed infrastructures Seabed topography / properties Shallow gas, hydrates, active seabed channels Constructability, including requirement and sequence for installation, pre-commissioning, commissioning and start-up Subsurface/drilling requirements, e.g. rig movement, well placement Operability, including flow assurance, controls, normal operation, shutdown, pigging Through life conditions HSE during construction and operation New technology risks Reliability, Availability and Maintainability ROV intervention and inspection Flexibility for addition of manifolds and future tie-in Phased development allows re-appraisal Abandonment 11

Challenging Technologies Challenging technologies include: Pipe-in-Pipe (PIP) Direct electrical heating Towed bundle flowlines Riser base gas lift Direct water injection Subsea multiphase flow pump (MPFP) Glassflake syntactic polyurethane (GSPU) Consider and assess: Local capabilities, infrastructures and competition Fabrication and installation requirements Field proven experience 12