At-a-Glance: Safe wireline logging hinges on verified well barriers, rigorously tested pressure-control equipment, clean rig-up with controlled access, disciplined line/tension control, radiation stewardship, and clear shutdown contingencies. The measures below are field-proven to prevent loss of containment, line/tool failures, and exposure incidents while keeping operations efficient.
I. Objective and Key KPIs
- I.1 Objective: Execute wireline logging in live or static wells without loss of containment, personnel injury, NPT, or environmental release, while maintaining tool data quality and operational efficiency.
- I.2 Safety/Operational KPIs:
- Zero HSE incidents; TRIR = 0; High Potential (HiPo) events = 0.
- Barrier integrity: Pressure tests pass on first attempt; no unplanned bleed-offs; well secure time < 5 minutes from event to shut-in.
- Line/tool integrity: Stuck tool events = 0.5 per 100 runs; unplanned weakpoint breaks = 0.
- Radiation safety: Personal dose = administrative limit; controlled area breaches = 0; source accounting 100%.
- Operational efficiency: Planned runs/day achieved = 95%; wireline-related NPT = 2% of job time.
- Environmental: Flaring/venting minimized; zero hydrocarbon spills; closed-loop bleed-down utilization = 95%.
II. Critical Parameters and Target Ranges
| Parameter | Target/Limit (estimated where noted) | Purpose |
|---|---|---|
| Wellhead pressure (WHP) | Maintain within design; confirm stable trend pre-open | Sets pressure-control configuration |
| Lubricator/valve WP rating | = 1.1× expected max surface pressure; test to 1.1–1.25× (hold 10–15 min, = 3% or = 10 psi drop) [estimated] | Barrier verification |
| Dual wireline valve/BOP functions | Close/open, seal test to full WP; shear/seal verified for line size | Emergency isolation/cut |
| Grease head differential | Grease pressure = WHP + 500–1,000 psi; flow tubes sized to line OD/roughness [estimated] | Dynamic seal on e-line |
| Sheave D/d ratio | D/d = 40 (e-line); fleet angle = 1.5°; guard installed [estimated] | Line fatigue/trauma prevention |
| Weakpoint rating | 60–80% of minimum line break strength; < fish-neck/pulling sub rating | Controlled release if stuck |
| Line speed | Typically 20–60 m/min logging; = 30 m/min through wellhead; adjust for deviation | Tool/line protection, data quality |
| Tension limits | Alarm at 70–80% of weakpoint; E-stop = 90% | Prevent parting |
| Bleed-down rate | = 300 psi/min to closed system [estimated] | JT cooling/hydrate mitigation, tool safety |
| Gas/H2S monitors | Fixed + personal calibrated; alarms active | Toxic/explosive atmosphere control |
| Radiation control area | = 5–10 m exclusion as per dose rate survey | ALARA compliance |
| Electrical isolation | Surface power off before hands near head/line; lockout/tagout verified | Shock/arc prevention |
III. Step-by-Step Safety Procedure / Checklist
III.1 Plan and Permit
- 3.1.1 PTW/JSA: Approve permit to work, SIMOPS review, confined space and lifting plans. Toolbox talk covers well status, H2S, radiation, pressure control, cut-line contingencies, and ESD actions.
- 3.1.2 Barriers: Confirm primary and secondary well barriers; document well barrier schematic (primary: hydrostatic or packer; secondary: wireline valve/BOP stack and wellhead).
- 3.1.3 Contingency: Stuck tool plan, fishing tools on site, weakpoint selection, pump-in provision, kill fluid availability (estimated), emergency source recovery plan, and muster/evac routes.
III.2 Equipment Preparation and Testing
- 3.2.1 Pressure-control stack: Redress and inspect from wellhead up: dual wireline valve/BOP (shear/seal), pump-in/bleed-off sub, quick test sub, tool catcher (if used), lubricator, grease head (for live e-line). Verify correct ring gaskets/elastomers (sour service if needed).
- 3.2.2 Pressure test:
- Low-pressure test (~250–300 psi) then high-pressure test per Section II; record charts; test both directions if applicable.
- Function test all rams; verify shear capability for line size with manufacturer table (estimated).
- 3.2.3 Electrical and surface gear: Calibrate depth encoder, tension load cell; verify winch brakes/ESD; test line wiper; ensure power supplies isolated; check line resistance/insulation.
- 3.2.4 Sheaves and rigging: Inspect groove profile, bearings, guards; certify slings/shackles; install tag-lines; confirm D/d and fleet angle compliance; barricade under-suspended loads; require working-at-height protection.
- 3.2.5 Gas/radiation: Bump-test gas detectors; set fixed sensors near bleed points; verify radiation package—source lock test, survey meter, TLDs, transport docs, secure storage.
III.3 Rig-up and Well Interface
- 3.3.1 Exclusion zones: Rope off red zone around well center, sheaves, and source; access control with a single spotter.
- 3.3.2 Lifts: Use certified crane/man-lift; no personnel under suspended lubricator; tag-line control; weather/sea-state check (offshore).
- 3.3.3 Make-up: Clean, dope, and torque flanges/unions; align to prevent side-load; install bleed-off to closed drain or flare.
- 3.3.4 Pressure verification: Re-function and leak-check all connections; document valve positions; verify equalizing valves operate.
III.4 Run-in-Hole (RIH) and Logging
- 3.4.1 Pre-open sequence: Confirm personnel clear, BOPs open, grease system primed (e-line), WHP stable, bleed-off valves closed, ESD functional, comms check.
- 3.4.2 Opening the well: Equalize carefully, open master(s) per procedure, maintain control of line; monitor gas readings continuously.
- 3.4.3 Line control: Respect speed limits; prevent slack; maintain head tension above tool weight minus buoyancy; use soft start/stops across restrictions.
- 3.4.4 Tension management: Set winch alarms; stop if tension spikes or drops unexpectedly; compare measured vs modeled drag to detect sticking or cuttings bridges.
- 3.4.5 Grease head: Maintain differential; adjust flow rate and viscosity; monitor for hydrocarbon show at wiper—stop if continuous show.
- 3.4.6 Electrical safety: De-energize before handling cable head; lockout power for any wet connector work; keep connectors dry/clean.
- 3.4.7 Radiation: Only qualified operators handle sources; keep non-essential personnel outside controlled area; continuous dose-rate survey when tool at surface; source lock verified before leaving well center.
III.5 Pull-out-of-Hole (POOH) and Shut-down
- 3.5.1 Well closure: Close wellhead valves as per plan; bleed-down to closed system at controlled rate; monitor temperature to avoid hydrate formation.
- 3.5.2 Lubricator handling: Equalize trapped pressure; verify zero pressure; apply locks/pins; then break connections. Never loosen under pressure.
- 3.5.3 Source and tool control: Confirm source into shielded container; perform post-run survey; complete source inventory log.
- 3.5.4 Demobilization: Remove barriers and signage only after all energy sources isolated and verified safe; conduct debrief and lessons learned.
IV. Risks and Mitigations
- IV.1 Loss of containment: Mitigate via dual barriers, full pressure testing, closed-loop bleed-off, trained valve operations, and immediate shut-in protocol. Keep shear/seal BOP ready to cut and seal on line.
- IV.2 Line parting/trauma: Control tension/speed, use correct sheave D/d and fleet angle, protect line from sharp edges, verify weakpoint sizing, keep red zone clear of snap-back arc.
- IV.3 Tool sticking: Pre-model drag/sag; clean-out if needed; limit overpull; avoid stationary logging in swelling shales; have jars/fishing package and pump-in contingency.
- IV.4 H2S/CO2/toxic gas: Fixed and personal monitors, escape sets, SCBA standby for sour wells, windsock and muster plan, non-sparking equipment in classified zones.
- IV.5 Radiation exposure: ALARA—time, distance, shielding; controlled area/badges; source lock checks; lost-source recovery plan; never cut line with source across shear rams—position tool above rams before shearing when feasible.
- IV.6 Electrical hazards: De-energize for any handling; insulated gloves/mats; lockout/tagout; discharge capacitors prior to tool work.
- IV.7 Lifting/working at height: Certified lifting plan, exclusion zones, fall protection, weather limits, and communication with banksman.
- IV.8 SIMOPS conflicts: Permit coordination with drilling, pumping, or crane ops; radio channel discipline; shared ESD logic reviewed.
V. Optimization Levers
- V.1 Digital modeling: Pre-job tension/drag and temperature/pressure modeling to set alarm thresholds and speed profiles; compare live vs model to detect anomalies early.
- V.2 Rapid-rig-up kits: Quick-test subs, pre-assembled lubricator sections, standardized unions, and color-coded elastomer kits reduce exposure time aloft.
- V.3 Condition monitoring: Online grease pressure control, line-tension trending, brake temperature sensors, and vibration on sheaves to predict failures.
- V.4 Maintenance strategy: Time-in-service and pressure-cycle-based elastomer replacement; post-job teardown inspections with photographic records; load cell and encoder calibration per runs/hours.
- V.5 Training and drills: Quarterly cut-and-seal drills, radiation emergency drills, and mock stuck-tool exercises to maintain crew response readiness.
- V.6 Data quality first time right: Real-time QC with decision trees to avoid re-runs, minimizing exposure duration and NPT.
VI. Verification & Monitoring Plan
- VI.1 Continuous monitoring:
- Tension, line speed, depth correlation, head voltage/current (SCADA or job logger).
- Grease pressure vs WHP differential; BOP hydraulic pressures; brake status.
- Gas detectors (LEL, H2S) and ambient noise/temperature; radiation dose rate near well center and truck.
- VI.2 Recorded tests:
- Pressure-test charts (low/high), function tests, shear capability verification log.
- Pre/post job electrical tests: line resistance/insulation, tool surface tests.
- Radiation logs: source serials, leak tests, dose records.
- VI.3 KPI tracking cadence:
- Per run: barrier checks, tension excursions, event log.
- Daily: NPT %, near-misses, gas alarms, dose tallies.
- Post-job: lessons learned, equipment condition, maintenance actions.
Key Formulas Used in Planning and Operations
- Tool apparent weight (buoyancy):
$W_{app} = W_{air} \left(1 - \dfrac{\rho_f}{\rho_s}\right)$ where $\rho_f$ = fluid density, $\rho_s$ = tool material density (steel ˜ 7{,}850 kg/m^3). Buoyancy factor $BF = 1 - \rho_f/\rho_s$.
- Tension envelope (simplified):
$T(z) = W_{app} + F_{drag}(z) \pm F_{hydro}(z)$ with alarms set so $T_{max} \le 0.8 \times T_{weakpoint}$.
- Sheave sizing:
$D/d \ge 40$ to limit bending strain and extend line fatigue life.
- Hydrostatic pressure:
$P_h = \rho_f g h$; confirm $P_{surface} + P_h \le$ equipment WP; pressure tests typically $1.1$–$1.25 \times P_{max}$ [estimated].
- Joule–Thomson cooling (hydrate risk indicator):
$\Delta T \approx JT \times \Delta P$; manage bleed-down to limit $\Delta P/\Delta t$ and keep $\Delta T$ within hydrate-free envelope.
- Electrical stored energy (capacitors):
$E = \dfrac{1}{2} C V^2$; always discharge before handling downhole electronics.
- Radiation inverse square law:
$I \propto \dfrac{1}{r^2}$; for a source with dose rate $I_1$ at $r_1$, distance for target dose $I_2$ is $r_2 = r_1 \sqrt{\dfrac{I_1}{I_2}}$.
Recommended Emergency Actions (Cheat Sheet)
- Loss of containment: Cease movement; close wireline valve/BOP; secure wellhead; evacuate red zone; bleed to closed system if safe; notify control room.
- Approaching weakpoint tension: Stop, slack off, attempt to free with controlled jar/pump-down as per plan; never exceed alarmed limits.
- Need to isolate/cut: Position tool above rams when feasible; shear/seal; verify shut-in; manage line ends; initiate recovery plan.
- Radiation abnormality: Establish 10 m hot zone, account for sources, call RPO, secure tool in shielded container, suspend ops.


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