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Category  >>  Operational Questions  >>  How to conduct integrity checks for FPSO facilities?
OPERATIONAL QUESTIONS
Updated : September 17, 2025

How to conduct integrity checks for FPSO facilities?

Published By Rigzone

At-a-Glance: A robust FPSO integrity check blends risk-based inspection, continuous monitoring, and targeted intrusive surveys across hull, mooring/turret, risers/umbilicals, topsides pressure systems, marine and offloading systems to maximize uptime and safety while minimizing OPEX and emissions.

I. Objective & KPIs

I.1 Objective: Assure mechanical, structural, and safety integrity of the FPSO to sustain safe production at design rates with controlled risk and optimized lifecycle cost.

  • I.2 Throughput KPIs: Production uptime = 98.0%; offloading availability = 99.0%.
  • I.3 Reliability KPIs: Availability \(A = \dfrac{\text{MTBF}}{\text{MTBF} + \text{MTTR}} \ge 0.98\) for safety-critical elements (SCEs); SIS proof test coverage = 90% within interval.
  • I.4 Integrity KPIs: No loss-of-containment (LOC) Tier 1 events; corrosion allowance margin = 2.0 mm; mooring line availability = 99.5%; flexible riser annulus “green” status = 95% of time.
  • I.5 OPEX KPIs: Inspection cost = 1.5% of annual OPEX while meeting RBI targets; unplanned maintenance ratio = 20% of total maintenance hours.
  • I.6 HSE & Emissions KPIs: TRIR = 0.5; fugitive methane emissions = 0.2% of gas handled; produced-water discharge oil-in-water = 30 mg/L average (estimated).

II. Critical Parameters & Target Ranges

System Parameter Target/Limit Method Primary Risk
Hull & Tanks Steel thickness loss Remaining = t_min + 2.0 mm UT gaugings, PAUT/TOFD at hot spots Structural failure, flooding
Hull & Tanks CP potential (Ag/AgCl) -0.80 to -1.10 V Permanent/readers, ROV survey Under-protection corrosion
Mooring/Turret Line tension Alarm at 60% MBL; trip at 80% MBL (estimated; site-specific) Load cells, fairlead sensors Line failure, station-keeping loss
Mooring/Turret Turret bearing temp/vibration Within OEM baseline; no growth trend CBM sensors, grease analysis Seizure, swivel damage
Risers (flexible) Annulus vent rate/pressure No sustained pressure; rate within baseline Annulus monitoring, gas sampling Armor wire corrosion, burst
Risers (rigid) Wall thickness/corrosion MAWT = design; RL = inspection interval ILI/EMAT/UT clamp, CP Rupture, leak
Topside Pressure Systems PRV set/testing Pop at 100% set; = 110% accumulation Bench test, in-situ lift Overpressure LOC
Topside Piping Corrosion rate CR = 0.3 mm/y (estimated) UT CMLs, coupons, ER probes Leak, fire
E&I / SIS ESD/SIS proof test Coverage = 90% per interval Cause & effect, partial/full stroke Demand failure
Gas Detection LEL setpoints A1: 10% LEL; A2: 20% LEL Bump test, calibration Delayed detection
Cargo/IG Tank O2 content < 8% v/v (preferably = 5%) IG analyzer, portable meter Explosion risk
Offloading Hoses Hydrotest/burst/continuity Hydrotest = 1.5× MOP; continuity < 1 O Hydro/Vac test, IR Spill, ignition
Marine Ballast Valve actuation, leakage Full stroke = 10 s; seat leak within class Function test, PSV on lines Stability/control loss

II.A Key Equations

  • II.A.1 Corrosion rate: \( \displaystyle CR = \frac{t_0 - t_1}{\Delta t} \quad [\text{mm/y}] \)
  • II.A.2 Remaining life: \( \displaystyle RL = \frac{t_1 - t_{\min}}{CR} \quad [\text{years}] \)
  • II.A.3 Fatigue cumulative damage (Miner): \( \displaystyle D = \sum_i \frac{n_i}{N_i} \) (acceptable if \(D < 1\))
  • II.A.4 Risk metric: \( \displaystyle \text{Risk} = \text{PoF} \times \text{CoF} \)
  • II.A.5 Availability: \( \displaystyle A = \frac{\text{MTBF}}{\text{MTBF}+\text{MTTR}} \)

III. Step-by-Step Procedure / Workflow / Checklist

III.1 Plan & Scope (Risk-Based)

  • 1.1 Build/validate the Asset Register and tag critical Safety-Critical Elements (SCEs): hull/tanks, mooring/turret/swivel, risers/umbilicals, topsides pressure boundaries, ESD/SIS, marine/offloading.
  • 1.2 Perform RBI: define Damage Mechanisms (CO2/H2S/erosion/MIC/SCC/fatigue); assign PoF/CoF; set inspection techniques and intervals aligned to RL = 2× interval.
  • 1.3 Define SIMOPS and campaign windows: UWILD, rope access, ROV/AUV, class survey windows, production constraints.
  • 1.4 Develop Inspection Test Plan (ITP) with acceptance criteria, CML list, hold points, and reporting templates.

III.2 Pre-Mobilization & Readiness

  • 2.1 Permits: Confined Space Entry, Work at Height, Hot Work, Over-side work; verify gas testing equipment calibration.
  • 2.2 Isolation/LOTO: verify pressure/energy isolation plans for pressurized equipment and electrical systems.
  • 2.3 NDT/ROV tooling: UT, PAUT, TOFD, ACFM, MFL, RT (where justified), CP readers, annulus monitors, hydrotest pumps.
  • 2.4 Baseline data: last survey thicknesses, CP potentials, mooring tensions, swivel logs, PRV history, SIS proof test records.

III.3 Hull, Structure, and Tanks

  • 3.1 External UWILD: ROV general visual inspection (GVI) and close visual inspection (CVI) of shell plating, bilge keels, fairleads, sea chests; measure CP at representative locations; clean and gauge at hot spots.
  • 3.2 Internal tanks: gas-free and ventilate; verify safe atmospheres (O2 20–21% v/v; HC = 1% LEL; H2S = 10 ppm); conduct close-up survey, coating assessment (NACE 0–4), UT gaugings on grids; assess pitting depth/area.
  • 3.3 Structural hot spots: deck penetrations, turret interface, crane pedestals; PAUT/TOFD of weld toes and suspected cracks; calculate utilization ratios vs. design.
  • 3.4 Ballast and bilge systems: function test remote valves; verify segregation; test Hi-Hi level alarms and pumps auto-start.

III.4 Mooring, Turret, Swivel

  • 4.1 Mooring lines: verify line tensions vs. metocean; inspect chain links for corrosion/elongation; measure stud loss; ROV CVI on connectors; check fairlead sheaves and brake holding.
  • 4.2 Turret bearing: trend temperature/vibration; grease sampling for wear particles; inspect seals; verify lubrication system interlocks.
  • 4.3 Fluid/electrical swivel: check leak detection drains; pressure boundary NDE where accessible; torque and tension checks; verify electrical slip ring integrity.
  • 4.4 Position keeping: validate GNSS offsets; heading weathervaning friction checks; alarm setpoints and FMEA bypass register clean.

III.5 Risers, Umbilicals, Subsea Interface

  • 5.1 Flexible risers: annulus vent monitoring (rate, composition); end-fitting CVI; strakes/buoyancy condition; ACFM on tensile armors where accessible; check bend stiffeners and I-tubes.
  • 5.2 Rigid risers/pipelines: ILI or external UT/EMAT; verify CP potentials; review VIV suppression; check supports/clamps and free-spans.
  • 5.3 Umbilicals: insulation resistance tests; pressure hold on hydraulic lines; function test safety-critical actuators (SSIV, ESDVs).
  • 5.4 Leak detection: deploy acoustic/pressure-balance checks; verify leak detection thresholds and response logic.

III.6 Topside Pressure Systems

  • 6.1 Piping/pressure vessels: CML UT; profile RT/PAUT at supports and dead legs; corrosion under insulation (CUI) screening (thermal imaging, lift cladding at suspect zones); verify MAWP vs. operating envelopes.
  • 6.2 PRVs/PSVs: remove and bench test by criticality; in-situ lift test where permissible; verify relieving capacity vs. scenarios; tag/traceability check.
  • 6.3 Leak testing: nitrogen/helium or soap for low-pressure; hydrotest only where required by code or post-repair; verify reinstatement with calibrated gauges and charts.
  • 6.4 Rotating equipment: vibration, thermography, lube oil analysis (particles, TAN/TBN); shaft alignment and coupling integrity.

III.7 E&I, Safety, and Automation

  • 7.1 SIS/ESD: execute cause & effect tests; proof test logic solvers; partial/full stroke test of ESD/SDV/HIPPS; verify bypass discipline.
  • 7.2 Gas/fire detection: bump test, calibration; verify alarm setpoints (10%/20% LEL) and shutdown voting; firewater pumps auto-start and ring-main pressure tests.
  • 7.3 Electrical: IR/PI tests on motors/transformers; thermography of switchboards; earthing/bonding continuity, especially on offloading systems.

III.8 Cargo Handling, Inert Gas, and Offloading

  • 8.1 Cargo tanks: IG system performance, O2 < 8% v/v; PV valves test and seat leakage; gauging/overfill alarms functional test.
  • 8.2 Offloading hoses/hawser: hydro/vacuum test; electrical continuity; visual inspection for kinks/cover damage; scheduled changeout by condition or time.
  • 8.3 Tandem/buoy offloading: ESD interlocks, QCDC function, emergency release testing in safe window; verify communication and DP/heading control logic.

III.9 Documentation & Closeout

  • 9.1 Record as-found/as-left data; update digital twin and corrosion circuits; recalculate RL and RBI intervals using equations in II.A.
  • 9.2 Raise and risk-rank anomalies (A–D); implement immediate mitigations; plan permanent repairs.
  • 9.3 Management of Change (MOC) for any design/operating envelope change; update SCE performance standards.

IV. Risks & Mitigations (HSE, Reliability, Redundancy)

  • IV.1 Confined space/tank entry: Gas test continuous; rescue plan; intrinsically safe equipment; cold-work standard—HC = 1% LEL, O2 20–21%.
  • IV.2 Over-side/height work: Use certified access systems; weather limits; standby recovery; permit-to-work with SIMOPS review.
  • IV.3 Hydrocarbon release: Double isolation and bleed; blind lists; temporary spades tracking; gas testing during reinstatement.
  • IV.4 Mooring/turret criticality: Weather window for intrusive work; temporary line load sharing; heading control readiness.
  • IV.5 Electrical arc/ignition: Live work minimized; ESD zoning; hot work management; verify bonding/continuity of offloading strings.
  • IV.6 Reliability: Spares for SCEs; redundancy in firewater, power, control; maintain bypass logs with time limits and compensatory measures.

V. Optimization Levers (OPEX, Debottlenecking, Data)

  • V.1 Condition-based monitoring: Permanent CP, mooring tension, swivel leak and vibration monitoring; flexible riser annulus gas sensors with alarms and trending.
  • V.2 Advanced NDT targeting: Data-driven selection of CMLs; phased-array and guided-wave for hidden corrosion; risk hot-spot mapping for supports and dead legs.
  • V.3 Digital twin & analytics: Integrate inspection findings, process data, and metocean loads; compute PoF/CoF trajectories; auto-update remaining life and inspection priorities.
  • V.4 Coatings/CP strategy: Early spot repairs, anode retrofits via ROV; optimize tank coating specs to extend survey intervals.
  • V.5 Campaign bundling: Combine ROV/UWILD, topsides NDT, and hose changeouts to reduce logistics and POB; align with class survey windows.
  • V.6 Spare/repair readiness: Hose strings, swivel seals, PRV spares, mooring connectors in stock; framework repair procedures pre-approved.

VI. Verification & Monitoring Plan

System What to Measure Frequency Method Linked KPI
Hull external (UWILD) GVI/CVI, CP potentials, anode wastage Annual GVI; 5-year CVI (estimated) ROV/AUV survey Uptime, Integrity
Internal tanks Coatings, pitting, UT grid 2–5 years by RBI (estimated) Entry survey, UT Integrity
Mooring Line tension/angles, connector condition Continuous tension; CVI annually Sensors/ROV Availability
Turret/swivel Bearing temp/vibe; leak drains Continuous; weekly checks CBM, operator rounds Uptime
Flexible risers Annulus pressure/vent rate Continuous; monthly analysis Annulus monitoring Integrity
Piping/vessels CR, thickness at CMLs 6–12 months trending; 2–3 years full UT, PAUT, RT LOC prevention
PRVs/PSVs Set pressure, seat tightness 1–5 years by criticality Bench/in-situ test Overpressure safety
SIS/ESD Proof test coverage, SIF PFDavg Quarterly to annual C&E testing Risk reduction
Gas/Fire systems Detector response, pump start Monthly functional; annual full Bump/cal tests; flow tests HSE
Offloading hoses Hydro/vacuum, continuity Annual; changeout 2–3 years Hydro/IR Spill prevention
Electrical Thermography, IR/PI Quarterly–annual Thermal scan, IR tests Uptime
Produced water Oil-in-water ppm Daily composite Online analyzer/lab Emissions

VI.A Acceptance & Escalation

  • VI.A.1 If \(RL < \) next inspection interval, escalate to mitigation: chemical treatment, clamps, operating envelope reduction, or repair.
  • VI.A.2 If mooring tension = 60% MBL persistently, initiate metocean review and operational heading control; at = 80% MBL, execute contingency plan.
  • VI.A.3 Any sustained flexible riser annulus pressure: reduce operating pressure, perform gas characterization, plan detailed inspection/repair.
  • VI.A.4 Any PSV test out-of-tolerance: replace/retest; review overpressure scenarios.

Disclaimer: The information provided here is for informational and educational purposes only. These insights are intended as general guides and may not reflect your specific circumstances. Salary figures are approximate and can vary by region, employer, and individual experience. Career, educational, and industry guidance offered here should not replace consultation with qualified professionals, employers, or educational institutions. Nothing presented should be interpreted as legal, financial, or investment advice, nor as a recommendation for commodity or securities trading. Always seek advice from appropriate professionals before making career, educational, or financial decisions.

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