G
Guest

Method Statement: Tie‑In Works Inside a Live Oil & Gas Plant (Shutdown, Isolation, SIMOPS, Testing, Reinstatement) – Method Statement
Method Statement: Tie‑In Works Inside a Live Oil & Gas Plant (Shutdown, Isolation, SIMOPS, Testing, Reinstatement) method statement and inspection test plan example.

Method Statement: Tie‑In Works Inside a Live Oil & Gas Plant (Shutdown, Isolation, SIMOPS, Testing, Reinstatement) – Method Statement

AI-assisted method statement with matching ITP, PDF download, and Excel export.

Published 10 Nov 2026 Rev. 00 15 views
About this method statement: This method statement details how to execute tie-ins inside a live oil and gas plant. It covers shutdown planning, isolations, SIMOPS, gas testing, welding, testing, reinstatement, and full QA/QC with hold points.

More than a static template

Unlike a downloadable Word or PDF template, this method statement is an AI-assisted editable starting point connected directly to a matching Inspection and Test Plan. Every section is structured, project-adaptable, and ready to export.

  • AI-assisted drafting — Customize every section with AI for your specific project scope.
  • Linked ITP — A matching inspection and test plan is generated alongside the method statement.
  • Multiple export formats — Download as a formatted PDF or editable Excel spreadsheet.
  • Editable starting point, not a final document — Review, verify, and adjust all content against your project requirements before use.

Static template vs. Quollnet workflow

FeatureStatic templateQuollnet
Project-specific contentManual fill-in requiredAI-assisted customization
Linked ITPSeparate document, no linkMatching ITP included
Export formatsUsually PDF onlyPDF and Excel
Structured sectionsFree-form layout13 standardized sections
Saved to your accountLocal file onlyCloud-saved, reusable
Content accuracyYou verify everythingAI-assisted, you still verify
CostOften free but time-intensiveFree to customize and download

What you can customize

When you save this method statement to your account, every section becomes editable. The following 13 sections are included:

  • Scope — Defines the activity and its boundaries.
  • References — Standards, specifications, and drawings.
  • Responsibilities — Roles and accountabilities.
  • Resources — Labour, plant, and equipment summary.
  • Materials — Materials and compliance requirements.
  • Equipment — Tools and equipment details.
  • Prerequisites — Hold points and pre-conditions.
  • Method sequence — Step-by-step construction sequence.
  • Safety controls — HSE risk controls and PPE.
  • Environmental controls — Environmental mitigation measures.
  • QA/QC — Quality inspection and test requirements.
  • ITP — Inspection and Test Plan table (has its own page).
  • Attachments — Referenced drawings and documentation.

Why this method statement is used

This method statement is used to define and communicate the approved procedure for carrying out method statement: tie‑in works inside a live oil & gas plant (shutdown, isolation, simops, testing, reinstatement) on site. It ensures the work is planned in advance, the correct resources and controls are in place, and all personnel understand responsibilities, sequence, quality requirements, and safety controls before work begins. It aligns site execution with the documented scope and acceptance expectations.

Who uses this method statement

This method statement is used by contractors, site supervisors, project engineers, QA/QC engineers, HSE officers, consultants, and client representatives. It serves as a shared reference for planning, execution, supervision, inspection, and approval of the activity on site.

When it is prepared and submitted

The method statement is prepared before the work activity starts and submitted as part of the pre-construction documentation package for review and approval.

Who reviews or approves it

The method statement is usually submitted to the client representative, consultant, resident engineer, or project management consultant for review and approval before the work commences.

Important approval note

This method statement is an AI-assisted editable starting point, not a pre-approved document. Before use on any project, all content must be reviewed and approved by the relevant parties (superintendent, principal contractor, or client representative) in accordance with your contract and project quality plan.

For example: if your specification requires a departure from a referenced standard, that departure must be documented and approved separately — this method statement will not capture that automatically. Always verify against your applicable drawings, specifications, and regulatory requirements.

Method statement content

Scope

Workscope

  • Planning and execution of tie-in works on existing process piping/equipment within a live oil & gas plant during a defined shutdown/turnaround window.
  • Development and approval of isolation philosophies (LOTO, DDB/DBB, spading/blinding), blind management, gas freeing and purging, and permit-to-work controls for SIMOPS.
  • Safe breaking of containment, removal/installation of spools, welding, NDE/NDT, pressure testing (hydrostatic or pneumatic), drying, leak checks, reinstatement, and system handback.
  • QA/QC control including hold and witness points, test packs, punchlist clearance, and as-built documentation.
  • HSE controls for hazardous area work, including continuous gas monitoring, ignition control, lifting near live equipment, and emergency preparedness.

Exclusions

  • Hot tapping and line stopping are excluded unless separately authorized and engineered; if required, comply with API RP 2201 [Verify per project].
  • New greenfield piping outside brownfield battery limits unless specified elsewhere.

Interfaces

  • Operations/Area Authority for isolations, depressurization, gas testing, and reinstatement.
  • Commissioning team for system acceptance, leak tests, flushing/drying criteria, and handover documentation.
  • Other SIMOPS contractors for congestion management, access, and crane movements.

Constraints

  • All works executed within approved shutdown window(s) and live plant constraints for hazardous areas (IEC 60079 zones). Tools and equipment must be suitable for the area classification or controls applied.

References

Document TypeReference / NumberRevisionNotes
Code ASME B31.3 – Process Piping Design, fabrication, examination, and testing requirements for process piping in hydrocarbon service.
Code ASME Boiler & Pressure Vessel Code, Section V – Nondestructive Examination NDE technique qualification, calibration, and reporting.
Code ASME Boiler & Pressure Vessel Code, Section IX – Welding Qualifications WPS/PQR and welder performance qualifications.
Recommended Practice API 570 – Piping Inspection Code Integrity requirements for existing piping systems during tie-in planning and post-work verification.
Recommended Practice API RP 2201 – Safe Hot Tapping Practices in the Petroleum and Petrochemical Industries Only if hot tapping is explicitly authorized [Verify per project].
Standard IEC 60079 Series – Explosive Atmospheres Selection of Ex-rated equipment, gas detectors, and controls for hazardous areas.
International Standard ISO 12944 – Paints and varnishes — Corrosion protection of steel structures Coating repair and DFT verification after tie-in works [Verify project system].
International Standard ISO 9712 – Non-destructive testing — Qualification and certification of NDT personnel NDT personnel certification levels II/III.
Standard ASME PCC‑1 – Guidelines for Pressure Boundary Bolted Flange Joint Assembly For gasket selection, bolt stress targets, tightening sequences, and leak avoidance.
Management Standards ISO 14001 / ISO 45001 Framework for environmental and occupational health & safety controls [Verify per project HSE plan].
Project Documents Project P&IDs, Isometrics, Line List, Tie‑in Index, Blind List, PTW Procedure, SIMOPS Plan Use latest AFC/IFI revisions and approved MOC.

Responsibilities

RoleResponsibilityName / Party
Project Manager Ensures method adherence and timely completion Contractor
Construction Manager / Mechanical Superintendent Implements sequence, supervises field teams, resolves site issues Contractor
PTW Coordinator / Area Authority (Operations) Issues/controls PTW, verifies gas tests, maintains isolation and blind lists Operations / Contractor
SIMOPS Coordinator Coordinates work windows, conflicts, lifting and access with other parties Operations / Contractor
Isolation Authority / Operations Supervisor Defines and approves isolation certificates and depressurization steps Operations
QA/QC Manager / Welding Inspector Approves ITP, WPS/PQR, NDE procedures; releases hold points; records Contractor
HSE Manager / HSE Officer Verifies task-specific controls, gas monitoring, emergency readiness Contractor
Authorized Gas Tester Performs initial/continuous gas tests; issues gas-free/N2-asphyxiation warnings Operations / Contractor
Lifting Supervisor / Appointed Person Develops lift plans, supervises rigging, sets exclusion zones Contractor
Commissioning Lead / Operations Representative Witnesses leak checks, reinstatement, and accepts system handback Operations / Contractor

Resources

Resource TypeDescriptionQuantityRemarks
Supervision Lead mechanical supervision 1
Labor Qualified pipefitters for carbon/stainless steel 6–12 [Verify per scope]
Labor ASME IX qualified welders (SMAW/GTAW) 4–8 [Verify per scope]
Labor Rigging and lifting crew 4–6
Labor NDT personnel Level II/III 2–4
Labor HSE officers and fire watch 2–4
Labor Authorized gas testers 1–2 per shift

Materials

MaterialSpecification / GradeQuantityRemarks
Spectacle blinds / Spades / Paddles Material grade per piping class; color-coded Per blind list +10% spares
Spiral wound SS/graphite or kammprofile Per ASME B16.20; piping class As per MTO + spares
ASTM A193 B7 / A194 2H (or per spec) Per ASME B16.5 dimensions As per MTO
CS/SS/Alloy per line class MTC EN 10204 3.1; PMI if alloy Per IFC isos
SMAW/GTAW fillers Per WPS/PQR [Verify] As required
Water/Nitrogen/Compressed air (pneumatic only if justified) Clean, oil-free; O2 < 1% for N2 purge [Verify] Per test volume + contingency
LEL mix (e.g., methane), H2S span gas, O2 Traceable calibration certificate As required

Equipment

EquipmentCapacity / TypeQuantityInspection Required
Gas detectors 1 per workface + standby
Portable radios Sufficient for crews
Cold cutter / beveller As required
Welding machines As required
Cranes / Hoists As per lift study Per lift plan
Test pump and manifold Up to test pressure +10% margin Per test pack
Bolting tools As required
Access systems As required

Prerequisites

  • Approved MOC and risk assessments covering tie-in scope, isolation method, and test method.
  • Current AFC P&IDs, isometrics, tie-in index, blind list, and line list; constructability walkdown completed and recorded.
  • Approved shutdown window and SIMOPS plan with clearly defined battery limits and exclusion zones.
  • Isolation certificates approved by Operations, with LOTO equipment available and serially controlled.
  • PTW package prepared: task-specific JSA, hot work permit (if any), confined space permit (if any), lifting plan, excavation permit (if any), and gas test requirements.
  • WPS/PQR approved; welders with valid WPQ for required materials, processes, positions.
  • NDE procedures approved; NDT personnel certifications verified (ISO 9712) and valid.
  • Calibration certificates for gas detectors, pressure gauges, torque tools, chart recorders (within validity).
  • Materials verified: CMTRs (EN 10204 3.1), PMI requirements defined for alloy lines, gasket/bolt kits available, spools preserved and dimensionally checked.
  • Emergency response plan briefed: firewater availability, extinguishers, spill kits, rescue plan, first aid, emergency communications.
  • Toolbox talks completed; workers inducted for hazardous areas and H2S awareness where applicable.
  • Interfaces confirmed: Commissioning/Operations availability for witness and hold points; inspectors assigned.
  • Waste management plan approved for hydrocarbons, test water, scrap, and contaminated materials.
  • Weather and environmental constraints considered (e.g., wind limits for crane operations).

Method Sequence

StepActivityDescriptionResponsibilityInspection / Hold Point
1 Pre-shutdown planning and tie-in dossier Compile tie-in package: scope, P&IDs mark-ups, isos, line list, tie-in index, blind list, test packs, WPS/NDE plan, lift plan, SIMOPS interfaces. Construction Manager / QA-QC Manager Document review (WP)
2 Site walkdown and constructability Joint operations/contractor survey; verify tie-in locations, hazards, access, scaffolds, lifting path, live lines proximity. SIMOPS Coordinator / HSE Field verification (WP)
3 Isolation planning and certificates Define isolation philosophy (DBB + bleed or positive isolation with blinds/spades). Prepare isolation certificates and LOTO plan. Isolation Authority Hold Point HP-1
4 Shutdown readiness review Confirm materials, blinds, gaskets, tools, test equipment, scaffolding, permits and inspectors are available for shutdown D-1. Project Manager / Operations Readiness review (WP)
5 Depressurization, draining, venting Operations de-inventory targeted lines per procedure: depressurize to flare or safe vent, drain liquids to closed system, open bleeds. Operations HP-2 Operations sign-off
6 Nitrogen purging/gas freeing (if required) Purge with N2 to displace hydrocarbons; vent to safe location/flare. Verify atmosphere: O2 19.5–23.5%, LEL <10%, H2S <10 ppm [Verify]. Operations / Gas Tester WP with gas test record
7 Install positive isolations (blinds/spades) Fit blinds per blind list with unique tags, torque bolts per ASME PCC‑1. Update blind board. Verify zero flow at bleeds after installation. Mechanical Supervisor HP-3 Blind inspection
8 Permit to Work activation / SIMOPS controls Issue PTW(s): cold work for breaking containment; hot work only if authorized; lifting permits. Establish exclusion zones and fire coverage. PTW Coordinator / HSE Permit audit (WP)
9 Breaking containment (cold cutting preferred) Bond/earth, set drip trays. Cold cut/remove existing spool. Capture residues; plug/blank open ends; maintain continuous gas monitoring. Mechanical Supervisor / Fire Watch HP-4 Before first break
10 Fit-up and alignment of new spools Verify material traceability; conduct PMI if specified. Align to tolerances: offset ≤3 mm, gap per WPS; ensure slope on drain/vent lines per design. Mechanical / QA-QC WP Dimensional check
11 Welding Execute welding per approved WPS/PQR (ASME IX). Control preheat/interpass (e.g., CS 75–150°C; SS per WPS) [Verify]. Purge SS/Alloy as required. Welding Supervisor WP + in-process surveillance
12 NDE of welds and joints VT 100%. RT/UT/PT/MT per service class: typical 10–100% based on criticality [Verify]. Hardness/ferite/replica if specified. NDT Technician / QA-QC HP-5 NDE release
13 Pressure test preparation Install test blinds, temporary vents/drains, calibrated gauges (≥2), relief valve set to ≤1.1× test pressure, barricade test area, brief crew. Hydrotest Supervisor HP-6 Pre-test check
14 Pressure testing Hydrotest per ASME B31.3: typically 1.5× design pressure adjusted for allowable stresses [Verify]. Hold per spec (e.g., 10 min stabilization + 30 min tightness). Pneumatic only with formal risk assessment at ~1.1× design pressure [Verify]. Hydrotest Supervisor / QA-QC / Operations HP-7 Test witness
15 Dewatering, drying, preservation Drain to closed system, blow with dry air/N2 to required dew point (e.g., ≤−20°C or per process) [Verify]. Install protective caps. Commissioning / Mechanical WP Dryness check
16 Coating and insulation reinstatement Surface prep per ISO 8501-1 (e.g., Sa 2.5), apply system per ISO 12944; verify DFT. Reinstall insulation with proper weather seals. Coating/Insulation Supervisor WP Coating inspection
17 Controlled reinstatement and blind removal In presence of Operations, remove temporary test blinds as per sequence. Install final gaskets/bolts, torque per PCC‑1. Stepwise pressurization and leak check (soap test if applicable). Mechanical / Operations HP-8 Reinstatement witness
18 Support adjustment and final alignment Verify pipe supports/springs, cold settings, and expansions; adjust as per design. Mechanical / QA-QC WP Support check
19 Documentation, punch closure, and handback Compile as-builts, weld/NDE dossiers, test certificates, torque logs, coating records, LOTO and blind list closeout, punchlist A/B/C clearance. QA-QC / Commissioning / Operations HP-9 Final handover
20 Demobilization and housekeeping Remove scaffolds, restore area, dispose of wastes per plan, remove barricades and signage. Construction Manager / HSE WP Area release
21 Emergency response (contingency) In the event of gas detection >10% LEL, H2S alarm, or leak: stop work, evacuate to muster, isolate ignition sources, inform control room, implement ER plan. All / HSE / Operations Drill (as planned)

Safety Controls

Task-Specific Hazards and Controls

1) Hazard: Residual hydrocarbons release during breaking containment
- Likely consequence: Fire/explosion, chemical exposure
- Engineering/procedural control: Positive isolation (blinds/spades) verified; DBB with open bleed; continuous gas monitoring; cold cutting preferred; bonding/earthing; drip trays and absorbents ready; firewater on standby
- Required PPE: FR coveralls, chemical-resistant gloves, goggles/face shield, anti-static safety boots, half-mask respirator (A2/P2) if indicated
- Collective preventive measure: Exclusion zone with fire watch and extinguishers (foam/dry powder) at points; no ignition sources; intrinsically safe tools
- Inspection/permit/supervision: Isolation certificate approval; PTW (cold/hot work); gas test record; supervisor and fire watch present

2) Hazard: Explosive atmosphere ignition (LEL exceedance)
- Likely consequence: Explosion, fatalities
- Engineering/procedural control: Maintain LEL <10% to proceed; stop work at ≥10% LEL; evacuate at ≥20% LEL [Verify per HSE plan]; use Ex-rated equipment; hot work ban unless specifically permitted
- Required PPE: FR clothing, intrinsically safe comms, hearing protection if alarms
- Collective measure: Fixed and portable gas detection; ignition source control; zoning and signage
- Inspection/permit/supervision: Continuous gas monitoring logs; PTW; HSE oversight

3) Hazard: Oxygen deficiency/asphyxiation from nitrogen purging
- Likely consequence: Loss of consciousness, fatality
- Engineering/procedural control: Control purge rates; vent to safe location; O2 monitoring; barriers and signage “N2 Purge – Asphyxiation Hazard”; rescue plan
- PPE: O2 monitor on person; FR clothing; harness if at height
- Collective measure: Access control and attendant; ventilation
- Inspection/permit/supervision: Gas test certificates; confined space permit if applicable; supervisor authorization

4) Hazard: Pressure testing energy release
- Likely consequence: Projectile/rupture injuries, fatalities
- Engineering/procedural control: Prefer hydrotest; pneumatic only with formal risk assessment and minimum personnel; barricade at calculated hazard radius; relief valve set ≤1.1× test pressure; remote pressurization
- PPE: Face shield, gloves, FR clothing, safety boots, hearing protection
- Collective measure: Exclusion zones and barriers; test control station
- Inspection/permit/supervision: Calibrated instruments; approved test diagram; HP witness by QA/QC and Operations

5) Hazard: Hot work (if authorized)
- Likely consequence: Fire, burns, ignition of vapors
- Engineering/procedural control: Hot work permit; pre/post fire watch (≥30 min or per spec); gas readings continuous; remove combustibles; screens and fire blankets; flashback arrestors
- PPE: FR clothing, leather gloves, face shield/welding hood, safety glasses
- Collective measure: Firewater hose and extinguishers; designated hot work area when possible
- Inspection/permit/supervision: PTW; gas test record; HSE supervision

6) Hazard: Lifting near live equipment
- Likely consequence: Dropped objects, plant damage, injury
- Engineering/procedural control: Approved lift plan; certified crane/rigging; tag lines; weather/wind limits; banksman
- PPE: Helmet with chin strap, gloves, safety boots, eye protection
- Collective measure: Exclusion zone; overhead hazard signage; tool tethering for work at height
- Inspection/permit/supervision: Pre-lift inspection; operator certification; lifting permit

7) Hazard: Confined space entry (pits, enclosed areas)
- Likely consequence: Toxic exposure, asphyxiation, entrapment
- Engineering/procedural control: Confined space permit; continuous gas monitoring; ventilation; standby attendant; rescue equipment
- PPE: Harness, retrieval line, gas monitor, FR clothing
- Collective measure: Barriers, entry log, rescue team on standby
- Inspection/permit/supervision: Permit authorization; periodic gas test; rescue plan drill [Verify]

8) Hazard: Noise/vibration from cutting and testing
- Likely consequence: Hearing loss, HAVS
- Engineering/procedural control: Time limits for vibrating tools; job rotation; maintain tools; noise mapping
- PPE: Ear plugs/muffs; anti-vibration gloves
- Collective measure: Acoustic screens; signage
- Inspection/permit/supervision: HAVS records; equipment inspection

9) Hazard: Chemical exposure from residues and coatings
- Likely consequence: Dermatitis, inhalation hazard
- Engineering/procedural control: Closed draining; MSDS review; use low-VOC systems where feasible
- PPE: Nitrile gloves, goggles, respirator as per SDS
- Collective measure: Spill kits and eyewash
- Inspection/permit/supervision: SDS available; COSHH assessments [Verify per local regs]

10) Hazard: Slips, trips, falls and working at height
- Likely consequence: Injury, fractures
- Engineering/procedural control: Proper scaffolds with toe boards and handrails; maintain housekeeping; 100% tie-off at height
- PPE: Harness and lanyard, non-slip FR boots, helmet
- Collective measure: Scafftags; fall arrest systems
- Inspection/permit/supervision: Scaffolding inspection by competent person; work at height permit where required

Note: Where exact thresholds/permit requirements vary, verify per project HSE plan and local regulations.

Environmental Controls

  • Hydrocarbon management: Drain to closed systems; no open discharge. Use drip trays and absorbents during breaking containment. Dispose of contaminated materials via licensed waste contractor.
  • Test water control: Use clean water; sample prior to discharge. Typical acceptance: pH 6–9, visible oil-free sheen, TSS per local consent (e.g., <30 mg/L) [Verify per permit]. Route via oily water separator if needed.
  • VOC emissions: Prefer cold cutting; control venting to flare where possible. If venting to atmosphere is permitted, use elevated safe vent points and monitor LEL downwind.
  • Nitrogen and air purging: Vent to designated safe locations; prevent wildlife/asphyxiation hazards with barriers and signage; avoid confined plumes.
  • Noise: Adhere to site noise windows; use acoustic screens for high dB tools; monitor dB(A) if required by consent.
  • Waste segregation: Metals, gaskets/bolts, coating wastes, used solvents, spent cartridges, rags managed in labeled containers. Maintain waste transfer notes and chain-of-custody.
  • Soil and water protection: Spill kits staged; booms for nearby drains; cover drains during cutting/washing. Immediate containment and reporting of spills.
  • Coating works: Control overspray and run-off; collect spent abrasives; comply with ISO 12944 system requirements.
  • Dust and particulate: Wet methods or local extraction for cutting where safe; Ex-rated vacuums in hazardous zones.
  • Environmental monitoring: Record volumes of drained product, test water, and purge gas; log any flaring or venting per Operations reporting.

QA/QC

  • ITP and Hold/Witness Points: Implement ITP with defined HP/WP as listed. No advancement past HP without approvals from QA/QC and Operations.
  • Material Control: Verify CMTRs to EN 10204 3.1. Heat numbers traceable to isometric weld map. PMI on alloy lines per project (typ. 10–100% on critical services) [Verify].
  • Welding Control: Approved WPS/PQR per ASME IX; welders WPQ current, process/material/position matched. Record preheat, interpass, heat input. Low-hydrogen controls for CS; purging for SS/Alloy.
  • NDE: Techniques and acceptance per ASME V and ASME B31.3. VT 100%. Additional NDE extent per criticality/class/service [Verify]. Calibrations current and traceable.
  • Flange Management: Assemble per ASME PCC-1. Use correct gasket type/size/class; lubricate threads; apply star-pattern torque; record final torque/tension. Flange face condition checked.
  • Pressure Testing: Boundaries confirmed; calibrated instruments; relief valve sized/set; hold times and pressures per ASME B31.3 and project. Pneumatic only with risk assessment and increased controls.
  • Drying/Cleanliness: Verify dew point/cleanliness where specified; protect open ends with caps; foreign material exclusion (FME) controls in place.
  • Coating/Insulation: Surface preparation verified (e.g., ISO 8501-1 Sa 2.5); DFT measured and recorded; cure times observed; insulation reinstated with correct jacketing and seals.
  • Documentation: Maintain rev-controlled test packs including checklists, isolation and blind records, weld/NDE logs, torque logs, calibration certs, gas test logs, permits, punchlists, and handover certificates.
  • Nonconformance: Log NCRs, corrective actions, and re-inspection records. Lessons learned captured for future shutdowns.

Attachments

  • Typical tie-in package table of contents (index, P&IDs, isos, blind list, weld map, ITP, permits, lift plans, test packs)
  • Sample blind list and tagging scheme
  • Example hydrotest diagram and calculation sheet
  • Example WPS/PQR summary sheet and welder matrix
  • Toolbox talk template for breaking containment and pressure testing
  • Emergency response flowchart for hydrocarbon release or gas alarm

This content is a read-only public reference. Download or customize to get an editable version.

ITP preview

The first inspection activities from the linked ITP for Method Statement: Tie‑In Works Inside a Live Oil & Gas Plant (Shutdown, Isolation, SIMOPS, Testing, Reinstatement):

ActivityInspection / TestAcceptance CriteriaResponsibilityRecord
Tie-in dossier and document reviewChecklist/document conformityAll required documents approved, current revisions, MOC/permits in placeQA/QC Manager (C), Operations Rep (W)ITR-00 Dossier Review Sign-off
Materials receipt and traceabilityVisual, CMTR verification, PMI (if specified)Materials per line class, CMTR EN 10204 3.1, PMI results acceptableQC Inspector (C), Client/Operations (W)ITR-MAT-01; PMI Report
Isolation and LOTO verificationIsolation certificate review; valve position check; bleed verificationApproved isolation certificate; DBB/Blind installed; zero energy confirmedOperations/Isolation Authority (C), QA/QC (W)ITR-ISO-02; LOTO Log

Showing 3 of 13 inspection activities. View full ITP →

Related Inspection and Test Plan

An Inspection and Test Plan (ITP) is available for Method Statement: Tie‑In Works Inside a Live Oil & Gas Plant (Shutdown, Isolation, SIMOPS, Testing, Reinstatement). The ITP defines the inspection activities, acceptance criteria, hold and witness points, responsible parties, and records required to verify the work described in this method statement.

View the Method Statement: Tie‑In Works Inside a Live Oil & Gas Plant (Shutdown, Isolation, SIMOPS, Testing, Reinstatement) ITP →

Frequently asked questions

Define scope windows, prepare tie-in dossiers, confirm materials and inspectors, obtain isolation and permit approvals, and coordinate SIMOPS and access.

Via approved isolation certificates, physical DBB/positive blinds/spades, open bleeds, zero pressure confirmation, and documented gas tests.

ASME Section IX for WPS/WPQ, ASME Section V for NDE, and ASME B31.3 for acceptance and pressure testing requirements.

Only when hydrotesting is impractical and after a formal risk assessment. Typical pressure is ~1.1× design pressure [Verify per project].

As-builts, ITRs, weld/NDE dossiers, test certificates, torque logs, coating records, blind/LOTO closeout, and the signed handover certificate.

Continue with related Quollnet resources connected to this method statement.

Related resources