Review on Subsea Pipeline Integrity Management: An Operator’s Perspective
Abstract
:1. Introduction
- Inspection (including ILI, monitoring, and surveillance) if the pipeline is piggable.
- Pressure testing (unpiggable pipeline).
- Direct assessment (unpiggable pipeline). Pipelines that cannot be pigged are the most likely candidates for integrity assessment by direct assessment.
- Other integrity assessment methods (i.e., Visual Inspection).
2. Industry Guidance on Pipeline Integrity Management
- To promote high standards and continuous improvement.
- To ensure safe and reliable delivery of the products to their customers, without adverse effects on employees, the public, customers, the environment, and incident free operation.
- To ensure that all reasonably practicable steps are taken to prevent loss of technical integrity.
- To establish adequate controls over relevant business activities with the aim of achieving incident-free working conditions.
- To ensure any future legislative compliance.
- Gathering, reviewing and integrating data.
- Risk assessment.
- Integrity assessment.
- Responses to integrity assessments and mitigation (repair and prevention).
- The use of comprehensive, systematic, and integrated processes for operation and maintenance.
- Programs shall continuously evolve.
- Programs shall be customised to meet operators’ unique conditions.
Pipeline “Industry Best Practice”
- Implementation and (ISO, OSHAS, etc.) certification of integrated management systems, in particular the adoption of risk management and subsequent risk-based inspection and maintenance regimes.
- Ensure safe and reliable delivery of the products to their customers, without adverse effects on employees, the public, customers, the environment and incident free operation.
- Ensure that all reasonably practicable steps are taken to prevent loss of technical integrity.
- Establish adequate controls over relevant business activities with the aim of achieving incident-free working conditions.
- Ensure any future legislative compliance.
- Promote high standards and continuous improvement.
- External corrosion metal loss.
- Internal corrosion metal loss and erosion.
- SCC (Sulphide Corrosion Cracking) colonies.
- Dents.
- Gouges.
- Cracks and crack-like defects (principally in welds).
- Buckles.
- Freespans.
- Sinkage and floatation.
- Corrosion Under Insulation.
- The roles and responsibilities of the Assessment/Inspection Engineers, the Pipeline Integrity Engineers (including Corrosion Engineers), and Operations in the management, administration, and progressing of anomaly resolution
- How anomaly registers are administered
- How an anomaly’s severity is assessed
- How the anomaly is reviewed
- How remediation of the anomaly is undertaken
- How the remediation actions are reviewed
- The reporting and progressing and closing out of activities arising from the resolution of anomalies
- Design.
- Construction.
- Commissioning.
- Operation and Maintenance (including modifications).
- Decommissioning.
- Abandonment (Removal/Recovery).
3. Pipeline Integrity Review
- To assess the likelihood and consequences of failure of the offshore pipeline system.
- To identify the level of operational risk related to the offshore pipelines and to detail risk mitigation strategies to ensure that risks are within acceptable industry levels.
- Data gathering, review and integration of the pipeline system data.
- Implementation of a geographic information system (GIS) based Pipeline Integrity Management System (PIMS) software application.
- Evaluation of the condition of the offshore pipeline system, determination of their fitness-for-purpose (FFP) and need for remedial work.
- Determination of the level of risk involved in extending the design life of the offshore pipeline system.
- Identification of the mitigation measures and the costs required to lower the operational risks to an acceptable level in accordance with standard industry practice levels.
- Preparing different study reports for each pipeline (condition, FFP, risk and integrity management plans).
- Cathodic protection measurement
- Direct wall thickness measurement
- Route and ROW surveys. For offshore pipelines this includes ROV surveys of pipeline position, length of unsupported spans, and the extent to which pipeline are protected by trenching or burial
- Corrosion Coupons/Probes and Sand Probes
- Product analysis. Analysis includes the following in liquid/gas phases:
- ○
- Water
- ○
- CO2
- ○
- Dissolved salts
- ○
- Soluble iron
- ○
- Corrosion inhibitor chemicals
- ○
- Methanol
- ○
- PH
- ○
- Chlorides
- ○
- Bacteria
3.1. Task 1: Data Gathering, Review and Data Integration
- Pipeline alignment sheets.
- Pipeline route data (centerlines) for input into a GIS database.
- Pipeline condition assessment data. Data sets are often by multiple vendors and may include:
- ○
- In-line inspection (ILI) data.
- ○
- Survey data, often by Remotely Operated Vehicle (ROV).
- ○
- Direct examination/NDE (including for unpiggable pipelines).
- Pipeline operating chemistry/composition of production fluids.
- Operational and forecast production rate data.
- Corrosion control data (i.e., CP readings).
- Data relating to platform lifting activities, vessel movements and dropped/dragged anchor related damage was collected and evaluated to generate a bespoke offshore probability model for failure from mechanical damage incidents.
- Information on the detection/isolation/repair times, Emergency shut-down valve (ESDV’s), platform populations, the financial losses and the environmental impact associated with small leaks, leaks and rupture releases was collected.
- Additional data elements of pipeline attributes (related to design, operation, maintenance, threats and consequences for use in the risk assessment and FFP) were entered for multiple line segments per pipeline.
- The methodologies to be used and the outcome to be obtained.
- The basic data, including assumptions.
- Listing of the software tools to be used.
- Listing of the industry codes and standards to be used.
3.2. Task 2: Establishment of the GIS Based PIMS
3.3. Task 3: Engineering Evaluation of the Pipeline Fitness-for-Purpose (FFP)
- A review of historical and any ongoing inspection, repair, and maintenance activity records (I.e., in-line inspection (ILI), caliper, Automated Ultrasonic Testing (Auto-UT), corrosion and ROV inspections). This process included: Providing feature and significant event summaries for each pipeline based on the available and most recent Auto-UT, ROV, Caliper and ILI surveys, and accounting for any remedial and intervention work conducted since the last survey. This effort ensured that known anomalies, and where they exist, are catalogued as either remediated, or un-remediated anomalies. Utilising this database allowed for the following engineering assessments to be performed:
- ○
- FFP evaluation of the most recently known condition of the pipeline, utilising industry best practice and including.
- ○
- Determination of the current and historical operational parameters.
- ○
- Assessment of the criticality internal and external corrosion based on the feature dimensions as reported by the most recent ILI and/or automated UT inspections.
- ○
- Assessment of the criticality of other reported anomalies, including dents, manufacturing defects and girth weld anomalies, and the assessment of the maximum allowed (critical) span lengths and respective limit state criteria for spanning pipelines.
- ○
- Identification and recommendation of the necessary actions that should be taken to ensure the pipeline is fit-for-purpose based on the known condition.
- Review of external corrosion with the main objective to assess of the pipeline corrosion protection system, including a review of the external survey data of existing Cathodic Protection Systems, and assessment of sacrificial anode depletion. This scope included:
- ○
- Assessment of the current Cathodic Protection (CP) levels based on data from the last CP and anode potential surveys.
- ○
- Comparison of the current potential levels against industry recommended best practices.
- ○
- Summary listing of all anodes including comments on the observed condition.
- ○
- Assessment of the anode depletion rate, determination of the remaining life for each anode and the estimated time to replacement.
- ○
- Prediction of the current anode condition based on the last anode inspection, and extrapolation of the data to determine replacement timelines.
- Review of internal corrosion with the main objective to review the on-going risk from pipeline internal corrosion mechanisms. This included an in-depth operational analysis of the pipelines taking into consideration; product composition, operating conditions (temperature, pressure, flowrate), inhibition, produced water, solids, bacterial contamination, leak history in order to evaluate the internal corrosion threat to each of the pipelines and to estimate deterioration rates.
3.4. Task 4: Probabilistic Assessment of Pipeline Failures, Consequence Analysis and Risk Assessment
- (i)
- A classical probabilistic approach (load vs. resistance) has been utilised where there is sufficient data available to define probability distributions that describe load and resistance, e.g., this approach is adopted for the Internal Corrosion threat (for the lines with ILI data) and is referred to as an analytical method.
- (ii)
- Where sufficient defect data is not available or the threat does not lend itself to the classical probabilistic approach, the failure probability has been estimated from baseline failure rate estimates which are then adjusted to reflect the impact of pipeline specific attributes (factors which cause or resist the threat), e.g., this approach has been adopted for the Internal Corrosion threat for the lines which do not have ILI data and is referred to as an empirical method.
- ○
- Internal Corrosion.
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- External Corrosion.
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- Mechanical Damage (sub-divided into ship impact to riser, dropped objects and anchor handling threats).
- ○
- Sour Cracking.
- ○
- Fatigue.
- ○
- Weather and Outside Force.
- ○
- Equipment Failure.
- ○
- Incorrect Operations (upset conditions)
- ○
- Start riser.
- ○
- Safety zone 1.
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- Main subsea section.
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- Safety zone 2 (or shore approach).
- ○
- End riser.
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- Health and safety.
- ○
- Environmental.
- ○
- Financial.
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- Health and safety risk.
- ○
- Environmental risk.
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- Financial risk.
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- Overall risk.
3.5. Task 5: Recommendations of the PIR Study
- ○
- Required rectification works.
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- Free span Rectifications.
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- Pipeline Stabilisation Rectifications.
- ○
- Pipeline Crossing Rectifications.
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- Sacrificial Anode Retrofits.
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- Anomaly repairs.
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- Replacement of a damaged pipeline section.
- ○
- Installation of pipeline protection.
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- ESDV installation.
- ○
- ROV, ILI and auto-UT surveys.
4. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Amaechi, C.V.; Hosie, G.; Reda, A. Review on Subsea Pipeline Integrity Management: An Operator’s Perspective. Energies 2023, 16, 98. https://doi.org/10.3390/en16010098
Amaechi CV, Hosie G, Reda A. Review on Subsea Pipeline Integrity Management: An Operator’s Perspective. Energies. 2023; 16(1):98. https://doi.org/10.3390/en16010098
Chicago/Turabian StyleAmaechi, Chiemela Victor, Grant Hosie, and Ahmed Reda. 2023. "Review on Subsea Pipeline Integrity Management: An Operator’s Perspective" Energies 16, no. 1: 98. https://doi.org/10.3390/en16010098
APA StyleAmaechi, C. V., Hosie, G., & Reda, A. (2023). Review on Subsea Pipeline Integrity Management: An Operator’s Perspective. Energies, 16(1), 98. https://doi.org/10.3390/en16010098