At-a-Glance — Practical, end-to-end workflow to plan and execute subsea pipeline NDT using ROV/diver external methods and internal ILI, with clear KPIs, target ranges, checklists, formulas, and verification gates for safe, reliable outcomes.
I. Objective & Key KPIs
I.1 Objective: Execute a risk-based, code-compliant NDT program for subsea pipelines (rigid lines and risers) covering external and internal integrity threats, while minimizing vessel time, safety exposure, and production impact.
- I.2 Primary threats addressed: external corrosion/Coating damage, internal corrosion/erosion, cracking (SCC/FCG at welds), dents/ovality/free spans, buckle/strain, anode depletion/CP shorting, leaks.
- I.3 Key KPIs:
- I.3.1 Inspection coverage = 95% by length and = 98% of girth welds and appurtenances.
- I.3.2 Probability of Detection (POD) 90/95 for target flaws: e.g., metal loss = 10% WT (UT/MFL), surface-breaking cracks = 1 mm (ACFM).
- I.3.3 Sizing accuracy: metal loss ±0.3–0.5 mm (UT/UTWM), MFL ±10% WT, crack depth ±1–2 mm (UTCD/EMAT), geometry dents ±0.5% OD.
- I.3.4 Data quality: usable frames > 90%, UT signal-to-noise ratio (SNR) > 12 dB, CP readings every 10–25 m; calibration checks at start/end of shifts.
- I.3.5 Operational: vessel/ROV utilization > 80%, ILI first-run success, pig speed 0.5–2.0 m/s stable, zero stuck-pig events.
- I.3.6 HSE: zero LTI; SIMOPS incidents = 0; diving hours ALARP.
- I.3.7 Cost & emissions: vessel days/km, CO2e/km; optimize by campaign bundling.
Assumptions (estimated): piggable 10–30 in. export line; depth 100–1,500 m; carbon steel with 3LPE/PP coating; occasional CRA spools; typical current = 1 m/s; launcher/receiver available; standard DSV/ROV spread.
II. Critical Parameters & Target Ranges
| Parameter | Target/Range | Notes |
|---|---|---|
| Water depth, visibility, current | Depth 10–3,000 m; vis = 1 m; current = 1.0 m/s | Currents > 1.5 m/s degrade ROV station-keeping and UT coupling |
| Pipeline geometry | OD 4–48 in.; WT 6–40 mm; bend radius = 3D | Confirm buckle arrestors, buckle detection history |
| Coating & marine growth | Coating intact; growth = 20 mm | Plan cleaning where growth > 5–10 mm for UT/ACFM/PEC |
| CP potentials (Ag/AgCl/seawater) | -0.80 to -1.05 V | IR-free (off) preferred; log anode condition/spacing |
| ROV capability | Class II–III; tooling skid | HD video, lasers, CP probe, UT thickness, ACFM/PEC scanners |
| Piggability | No-bore restrictions; min ID = 95% nominal | Trap, valves, tees, wye; temporary spool if needed |
| Product & flow | Stable; temp 4–70 °C; gas/liquid per tool | UTWM needs liquid coupling; EMAT/MFL for gas |
| Feature density | Welds ~ every 12 m; crossings/tees mapped | Drive scan density and speed control |
| Free spans | Length = critical span per VIV criteria | Survey with MBES/DVL; remediate if over limit |
III. Step-by-Step Procedure / Workflow / Checklist
III.1 Planning and Risk-Based Scope
- III.1.1 Gather history: design data, previous ILI/ROV, repairs, CP logs, excursions, pigging records, geohazards, trawl interference, SIMOPS constraints.
- III.1.2 Threat/RBI matrix: map credible threats to NDT methods (see III.2). Set flaw size thresholds and required POD/sizing accuracy.
- III.1.3 Define acceptance criteria: MAOP/SMYS basis, metal loss/crack limits, dent/strain limits, CP criteria, anode wastage limits.
- III.1.4 Logistics: vessel and ROV class, weather window, diving vs ROV, permits, MOC, emergency response (pig stuck, leak, DP loss).
- III.1.5 Calibration plan: UT velocity blocks, ACFM reference notches, PEC lift-off shims, CP probe calibration, video/laser scale checks.
III.2 Technique Selection (External vs Internal)
- III.2.1 External (ROV/diver):
- III.2.1.1 General/close visual inspection (GVI/CVI) with HD video, dual lasers, photogrammetry; span and seabed contact checks.
- III.2.1.2 CP survey: contact/surface cell at 10–25 m intervals; log anode potentials and consumption.
- III.2.1.3 UT thickness (0° A-scan) on cleaned spots; for coated lines, use local coating removal or EMAT if applicable; water couplants acceptable subsea.
- III.2.1.4 ACFM for surface-breaking cracks at weld toes and stress raisers; works through thin coatings.
- III.2.1.5 Pulsed Eddy Current (PEC) for corrosion under coatings/insulation; provides average WT over footprint.
- III.2.1.6 MBES/DVL for route, burial, free spans; magnetometer if required for ferrous signature changes.
- III.2.1.7 Leak detection: acoustic hydrophone, ROV methane/hydrocarbon “sniffer,” bubble plume imaging in low current.
- III.2.2 Internal (ILI):
- III.2.2.1 Geometry/caliper and mapping (IMU/XYZ).
- III.2.2.2 Metal loss: MFL for gas/liquid; UTWM for liquid systems; PEC/EC arrays as needed for CRA/cladding interfaces.
- III.2.2.3 Cracks: EMAT or UT crack detection (UTCD); consider axial vs circumferential crack sensitivity.
- III.2.2.4 Deformation/strain: high-res caliper/IMU; dent/ovalization, bending strain near crossings/landfalls.
III.3 Pre-Mobilization Checklist
- III.3.1 Verify launcher/receiver readiness; pig passage drawings; vent/drain; isolation/permit plan.
- III.3.2 Cleaning program: foam, brush, magnetic, and gauging pigs; wax control; debris handling plan; chemical inhibition if needed.
- III.3.3 Tool readiness: bench test sensors; battery burn; odometer calibration; data storage redundancy; topside DAQ.
- III.3.4 ROV tooling: CP probe, UT probe, ACFM/PEC scanners, cleaning brushes/HP water jet, laser scaler, cathodic contact lead.
- III.3.5 Diving (if used): saturation vs air, habitat plans, NDT procedures, bailout/marine growth management.
III.4 External Survey & NDT (ROV/Diver)
- III.4.1 Route survey: MBES side-scan for burial, free spans, scour; tag KP/feature locations with DVL/USBL and laser scaling.
- III.4.2 Visual: full-length GVI; CVI at crossings, supports, clamps, repairs, FLETs/PLETs, riser TDPs, touch-down zones (TDZs).
- III.4.3 CP: potentials every 10–25 m, at welds, anodes, supports; measure “on” and “off” where feasible; record temperature/conductivity.
- III.4.4 Cleaning: localized brush/HP water jet to bare metal for UT/ACFM spots; log cleaned area and location.
- III.4.5 UT thickness: spot grid at every Nth weld (e.g., every 10th) and at damage indications; at least 3–5 points around circumference per location.
- III.4.6 ACFM at suspect weld toes/attachments; PEC over coated sections to screen for general wall loss; expand UT at PEC hotspots.
- III.4.7 Leak checks: hydrophone passes; ROV sniffer sweeps at flanges/valves/repair clamps; observe plume in low-current windows.
- III.4.8 Risers/TDZs: increase scan density; monitor for fretting, coating loss, fatigue hotspots.
III.5 Internal ILI Execution
- III.5.1 Sequence: cleaning ? gauging ? caliper/geometry/IMU ? metal loss (MFL/UTWM) ? crack (EMAT/UTCD) as required.
- III.5.2 Pig speed control: use flow/drag control; target 0.5–2.0 m/s; avoid stalls; log differential pressure and speed.
- III.5.3 Launch/receive: pressure envelope, isolation and venting steps; debris capture; verify tool status and full data download.
- III.5.4 Onboard QA/QC: quick-look POD checks, tool health, distance tally, magnetization level (MFL), UT gain/time-corrected gain (TCG) verification.
III.6 Data QA/QC, Analysis, and Assessment
- III.6.1 Calibration verification: pre/post NDT blocks; UT velocity in steel; ACFM notch response; PEC lift-off sensitivity.
- III.6.2 Anomaly classification: metal loss, dents, wrinkles, cracks; correlate ILI callouts with ROV coordinates and features.
- III.6.3 Integrity assessment: calculate remaining strength and repair priorities per governing standard; set dig/repair thresholds for next intervention.
III.7 Reporting & Close-Out
- III.7.1 Deliverables: anomaly spreadsheet with KP/clock position/sizing, heat maps, CP profile plots, free-span table, weld-by-weld summary, POD curves, uncertainty budgets.
- III.7.2 Repair plan: sleeves/clamps/coating repairs; CP retrofit; span rectification; reinspection intervals based on corrosion rate and uncertainty.
IV. Key Formulas and Engineering Checks
- IV.1 UT thickness from time-of-flight:
\( t = \dfrac{v \,\Delta t}{2} \) where v ˜ 5,900 m/s for carbon steel; ensure correct temperature compensation.
- IV.2 Corrosion rate and predicted remaining life:
\( \text{CR} = \dfrac{t_0 - t_1}{\Delta t} \) and \( \text{RL} = \dfrac{t_1 - t_{\min}}{\text{CR}} \)
- IV.3 Hoop stress and MAOP (Barlow, elastic thin-wall approximation):
\( \sigma_h = \dfrac{P D}{2 t} \Rightarrow P \approx \dfrac{2 t S}{D} \) with S = allowable stress per code and t = effective wall (account for corrosion allowance and metal loss).
- IV.4 Crack driving force (screening):
\( K_I = Y \,\sigma \sqrt{\pi a} \) where Y is geometry factor, a is crack depth; if \( K_I \ge K_{IC} \), risk of fast fracture. Use UT/EMAT crack sizing with stress estimates (including thermal/pressure cycling).
- IV.5 POD curve (hit/miss model):
\( \text{POD}(a) = \Phi\!\left(\dfrac{\ln a - \mu}{\sigma}\right) \) where F is standard normal CDF; report a at 90/95 with sizing uncertainty.
- IV.6 Mass-balance leak check (steady-state):
\( \dot{m}_{\text{leak}} \approx \dot{m}_{\text{in}} - \dot{m}_{\text{out}} - \dfrac{d(\rho V)}{dt} \) corroborated with pressure/temperature compensation and acoustic sensing.
- IV.7 CP acceptance (Ag/AgCl/seawater reference):
Accept if \( E_{\text{pipe}} \in [-1.05,\,-0.80]\, \text{V} \) (IR drop minimized). Values more negative than -1.10 V risk coating disbondment/hydrogen effects on high-strength steels.
V. Risk & Mitigation
- V.1 HSE:
- V.1.1 Diving hazards, DP excursions, dropped objects, high-pressure pigging, hydrocarbon/H2S release.
- V.1.2 Mitigation: SIMOPS plan, exclusion zones, ESD and emergency disconnect sequences, leak response kit, inerting where needed, ALARP dive time, toolbox talks per shift.
- V.2 Technical:
- V.2.1 Stuck pig or tool failure; poor data quality due to debris/scale/coating; ROV station-keeping limits.
- V.2.2 Mitigation: progressive cleaning program, dummy run, bi-directional tools where possible, contingency retrieval, speed control valves/bypasses, schedule during neap tides.
- V.3 Environmental:
- V.3.1 Discharges from cleaning; seabed disturbance; marine life interactions.
- V.3.2 Mitigation: debris capture/filtration, minimal contact skids, environmental monitors, timing to avoid sensitive seasons.
- V.4 Data integrity:
- V.4.1 Mitigation: dual recording, real-time QC dashboards, calibration checks pre/post shift, chain-of-custody for raw data.
VI. Optimization Levers
- VI.1 Campaign bundling: combine multiple assets/routes; align ILI with ROV window for rapid anomaly verification.
- VI.2 Targeted external NDT: use PEC to screen through coating; deploy UT only at hotspots to reduce cleaning time.
- VI.3 Tool selection: gas lines favor MFL/EMAT; liquid lines enable UTWM for superior sizing; CRA/Clad may favor EMAT/EC array.
- VI.4 Autonomy & analytics: AUV for long transits; AI-assisted video defect detection; GIS-based anomaly management with digital twin of pipeline.
- VI.5 Speed management: flow/pigging speed control to maintain SNR and sizing; dynamic setpoints by feature density.
- VI.6 CP performance: retrofit anodes or impressed current where potentials trend > -0.80 V; verify continuity across spools and isolation joints.
- VI.7 Emissions/cost: minimize vessel days via parallel ROV/ILI prep teams; pre-clean to extend ILI run reliability.
VII. Verification & Monitoring Plan
VII.1 What to Measure and How Often
- VII.1.1 Coverage: % length and welds inspected per campaign; accept = 95% length, = 98% welds.
- VII.1.2 Data quality: UT SNR, ACFM lift-off, CP probe stability, video quality; per shift with pre/post calibration.
- VII.1.3 POD & sizing: produce POD curves by flaw type; annual/biannual review after each campaign.
- VII.1.4 CP trend: KP-by-KP potential plots; annual survey or after coating repairs.
- VII.1.5 Anomaly population: counts by severity class; growth rates; reassess reinspection interval via CR and uncertainty.
- VII.1.6 Operational health: pig speed variance, differential pressure, tool telemetry reliability, vessel utilization.
- VII.1.7 Leak surveillance: mass-balance variance thresholds, acoustic baseline updates, periodic ROV fly-bys over TDZs and crossings.
VII.2 Acceptance & Close-Out
- VII.2.1 Acceptance criteria met (KPIs in Section I.3); document deviations and corrective actions.
- VII.2.2 Repair verification: post-repair NDT (UT/ACFM/CP), pressure test if required, updated MAOP check using effective wall thickness.
- VII.2.3 Update integrity management system: anomaly register, RBI model, next due dates, lessons learned.
VIII. Field Tips (Operator-Proven)
- VIII.1 Clean small, scan smart: rapid PEC screen first; deploy UT/ACFM only where PEC/visual flags exist.
- VIII.2 Control pig speed with bypass and flow adjustments; avoid hills/low points that stall tools.
- VIII.3 Schedule TDZ and riser base scans at slack water for best UT/ACFM coupling and image stability.
- VIII.4 Always correlate ILI to weld tallies and field joints; clock position errors often come from IMU drift—correct with known features.
- VIII.5 For gas lines requiring UTWM, consider temporary batch liquid slug and careful speed control; validate coupling early with witness coupons.
- VIII.6 Use dual lasers for accurate scale in video; photogrammetry can quantify dent depth and ovality where caliper data is unavailable.


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