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Tutorial Course

PETE 1021 · Pipeline Integrity Engineering

Led by Senior Pipeline Integrity Engineer Simulacrum

5 modules 5 modules · ~30 hours Engineering Updated 6 days ago

Pipeline integrity engineering from threat identification and integrity management programmes through ILI, NDT, fitness-for-service assessment, corrosion management, SCC, risk-based decision making, repair methods, life extension, and emerging technologies.

Pipeline Systems, Th…1Inspection and Testi…2Corrosion Management…3Risk Assessment, Rep…4Monitoring, Complian…5
  1. Module 1

    Pipeline Systems, Threats, and Integrity Management Programmes

    Led by Senior Pipeline Integrity Engineer Simulacrum

    The question

    A pipeline system is more than a pipe — it includes coatings, cathodic protection, valves, compressor stations, pig traps, and SCADA. This module covers the system components and design standards (API 5L grades, ASME B31.8 wall thickness design with Class location factors), the five threat categories from ASME B31.8S (time-dependent, stable, time-independent, interactive), the integrity management programme as a plan-do-check-act lifecycle, risk assessment methodology (probability and consequence, semi-quantitative matrix and quantitative methods), and four international regulatory frameworks (PHMSA, CSA Z662, ASME B31.8S, API 1160).

    Outcome

    The student can describe system components, name the five threats, describe the IMP lifecycle, apply the risk matrix, and name four regulatory frameworks. (Pipeline systems, threats, and IMP)

    Sub-units

    1. 1.1 Pipeline System Components and Design Standards
    2. 1.2 Threat Categories: Time-Dependent, Stable, and Time-Independent
    3. 1.3 The Integrity Management Programme: Framework and Lifecycle
    4. 1.4 Risk Assessment: Probability, Consequence, and Prioritisation
    5. 1.5 Regulatory Frameworks and Industry Standards
  2. Module 2

    Inspection and Testing: ILI, NDT, and Corrosion Assessment

    Led by Senior Pipeline Integrity Engineer Simulacrum

    The question

    The pipeline is buried — the defects that threaten it are invisible without inspection. This module covers the four ILI tool types (MFL for metal loss, geometry for dents, ultrasonic for cracks, caliper for restrictions) with their sizing accuracy, ILI data analysis (the unity plot for validation, calibration factors for bias), fitness-for-service assessment using B31G, RSTRENG, and API 579, four NDT methods (UT, MPI, radiography, phased array), hydrostatic testing and its limitation (proves absence above threshold but does not size surviving defects), and direct assessment for unpigable pipelines.

    Outcome

    The student can describe four ILI tools, explain the unity plot, apply B31G assessment, describe four NDT methods, and explain hydrostatic testing and direct assessment. (Inspection and testing)

    Sub-units

    1. 2.1 Inline Inspection: MFL, Geometry, Crack Detection, and Caliper
    2. 2.2 ILI Data Analysis: Defect Listing, Validation, and Response
    3. 2.3 Fitness-for-Service: B31G, RSTRENG, and API 579
    4. 2.4 NDT Methods: UT, MPI, Radiography, and Phased Array
    5. 2.5 Hydrostatic Testing and Direct Assessment
  3. Module 3

    Corrosion Management: External CP, Internal Corrosion, and Cracking

    Led by Senior Pipeline Integrity Engineer Simulacrum

    The question

    Corrosion accounts for more than half of all pipeline failures — managed through prevention, detection, and assessment. This module covers external corrosion prevention (three coating systems and cathodic protection with the −850 mV criterion), CP monitoring (CIPS and DCVG surveys), three internal corrosion mechanisms (CO₂, H₂S, MIC) with the de Waard-Milliams model and four management methods, stress corrosion cracking (near-neutral pH and high-pH SCC — environment, crack morphology, and management), and fatigue crack growth modelled by the Paris law with remaining life prediction.

    Outcome

    The student can describe the coating + CP strategy, describe CIPS and DCVG surveys, describe three internal corrosion mechanisms, describe both SCC types, and apply the Paris law for remaining life. (Corrosion management)

    Sub-units

    1. 3.1 External Corrosion Prevention: Coatings and Cathodic Protection
    2. 3.2 CP Monitoring: CIPS and DCVG Surveys
    3. 3.3 Internal Corrosion: Mechanisms, Modelling, and Management
    4. 3.4 Stress Corrosion Cracking: Near-Neutral pH and High-pH SCC
    5. 3.5 Fatigue Crack Growth and Remaining Life Prediction
  4. Module 4

    Risk Assessment, Repair, and Life Extension

    Led by Senior Pipeline Integrity Engineer Simulacrum

    The question

    Once defects are found and assessed, the integrity engineer must decide: repair, monitor, de-rate, or replace — and the decision depends on risk, economics, and regulation. This module covers the risk matrix and the ALARP principle, five repair methods (Type A and B steel sleeves, composite wrap, pipe replacement, hot tapping, grinding) and the conditions for each, managing aging pipelines (coating degradation, CP system aging, life extension measures, the end-of-life criterion), emergency response for pipeline incidents (detection, classification, isolation, notification, environmental containment), and incident investigation with metallurgical failure analysis.

    Outcome

    The student can apply the risk matrix and ALARP, describe five repair methods, describe the life extension strategy, describe the emergency response plan, and explain the metallurgical failure analysis. (Risk, repair, and life extension)

    Sub-units

    1. 4.1 Risk-Based Decision Making: The Risk Matrix and ALARP
    2. 4.2 Repair Methods: Sleeves, Composites, Replacement, and Hot Tapping
    3. 4.3 Managing Aging Pipelines and Life Extension
    4. 4.4 Emergency Response for Pipeline Incidents
    5. 4.5 Incident Investigation and Lessons Learned
  5. Module 5

    Monitoring, Compliance, Environmental Management, and Future Trends

    Led by Senior Instrumentation & Control Engineer Simulacrum

    The question

    Between major inspections, monitoring systems provide continuous surveillance. This module covers SCADA hydraulic profile monitoring, CPM leak detection with its 1–3% sensitivity threshold, CP telemetry for real-time corrosion protection monitoring, compliance documentation (five record categories with defect lifecycle traceability), environmental management (minimum cover, HDD watercourse crossings, right-of-way management, decommissioning options), three case studies of pipeline failures, and four emerging technologies — distributed fibre optic sensing, drone inspection, digital twins, and AI-driven analytics for defect prioritisation.

    Outcome

    The student can describe four monitoring technologies, explain the compliance documentation, describe the environmental management programme, identify root causes in the case studies, and describe four emerging technologies. (Monitoring, compliance, environment, and future)

    Sub-units

    1. 5.1 Pipeline Monitoring: SCADA, Leak Detection, and CP Telemetry
    2. 5.2 Compliance, Documentation, and Record Keeping
    3. 5.3 Environmental Management and Land Use
    4. 5.4 Case Studies: Pipeline Failures and Integrity Lessons
    5. 5.5 Future Trends: Fibre Optics, Drones, Digital Twins, and AI