1. 2 Industry Integrity Efforts Have Reduced Incidents in Key Areas  Corrosion incidents are down 76% –Enhanced “smart pig” ILIs –Strengthened corrosion.

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Presentation transcript:

1

2 Industry Integrity Efforts Have Reduced Incidents in Key Areas  Corrosion incidents are down 76% –Enhanced “smart pig” ILIs –Strengthened corrosion management programs  Third-party damage incidents are down 78% –Improved public awareness campaigns  Opportunity now to address need for better crack detection, analysis and response –Especially for seam-related cracks Right of Way Incidents Source: 2015 API-AOPL Annual Liquids Pipeline Safety Performance Report & Strategic Plan

3 RP 1176 Incorporated Expertise from Across the Industry  A Task Group within API's Pipeline Integrity Work Group (PIWG) led the RP development process –Integrity managers from 20+ companies –Five subcommittees  Retained counsel from some of the leading pipeline experts –Kiefner & Associates served as technical consultants  Incorporated work from –AOPL, INGAA and CEPA –R&D by industry and regulators –Existing standards and documents  Sought review and input from state and federal regulators

4 RP 1176 Scope  applicable to any pipeline system used to transport hazardous liquid or natural gas –including those defined in U.S. Title 49 CFR Part 195 and 192.  provides the operator with a description of industry-proven practices in the integrity management of cracks –and threats that give rise to cracking mechanisms  largely targeted to the line pipe along the right-of-way –some of the processes and approaches can be applied to pipeline facilities

5 Crack Management RP Philosophy  Augments operators existing IMP  Address all types of crack failure mechanisms  Flexible  Requires an in-depth knowledge of each system’s characteristics  Requires the integration of data

6 Mike Stackhouse – Plains - Overall RP Leader Five Subcommittees Focused on Key Topics  Bruce Dupuis – TransCanada –Mechanical Damage –SCC  Jake Haase – Enterprise Products –ILI Assessment –Response Criteria –Assessment Selection  Ken Bagnoli – Exxon Mobil –Manufacturing defects –ERW Seams  Benny Mumme – Koch Pipeline –Remediation –Performance Metrics –Reassessment  Rich Dalasio – Sunoco Logistics –Consistency across RP and with other standards –Coordination and Alignment –Research  Kiefner & Associates –SMEs

7 RP 1176 Outlines the Core Disciplines of Crack Management Programs 1. Understanding the threat mechanisms associated with pipeline cracking A. SCC and other environmental cracking B. Long-seam defects: ERW & EFW, DSAW C. Mechanical damage 2. Applying the most appropriate integrity assessment technology and modeling A. Integrity assessment method selection B. ILI technology review C. Hydrostatic testing D. In-the-ditch NDE E. Defect growth and re-assessment 3. Employing the appropriate repair strategies 4. Establishing preventative and mitigative practices 5. Evaluating program performance

8 Table of Contents - Sections 1-3 Scope, Normative References and Terms, Definitions Acronyms, and Abbreviations 4Guiding Principles 5Crack Management Program 6Threat Mechanisms Associated with Cracking 7Fitness-for-Service of Crack-Like Flaws 8Crack Growth 9Gathering, Reviewing and Integrating Data 10Methods of Integrity Assessment 11In-Line Inspection for Integrity Assessment 12Hydrostatic Testing 13SCC Direct Assessment 14In-the-Ditch Assessment 15Repair Methods 16Preventive and Mitigative 17Crack Management Program Performance Evaluation Over 160 pages in length

9 Table of Contents - Annexes Annex A SCC Additional Information Annex B Longitudinal Seam Prioritization for ERW and EFW Pipe Annex C Assessment Methods for Crack-like Flaws Annex D Yield Strength and Tensile Strength Annex E Toughness Annex F Hydrogen Effects Annex G Fatigue C and n Values Annex H Prediction of Crack Growth with Consideration of Variable Loading Conditions on Oil and Gas Pipelines in Near-Neutral pH Environments Annex I UT and Magnetic ILI Technology Annex J Capabilities of In-Line Inspection Tools for Specific Types of Axial Cracks and Anomalies Annex K In-the-Ditch Technology Annex L Example of an ILI Response Protocol

10 “provide general guidelines for application of inspection technology” 11.1 General 11.2 In-Line Inspection Tool Types 11.3 ILI Tool Utilization Considerations 11.4 Capabilities of In-Line Inspection Tools for Axial Cracks 11.5 Verification of ILI Results 11.6 Crack Tool Response Methodology 11.7 Crack ILI Response Criteria Section 11 In-Line Inspection for Integrity Assessment

11 Requires balance between:  Prioritized response similar to corrosion  Avoiding onerous excavation program that provides little risk reduction and large negative impact on all stakeholders Crack response

12 Current (and proposed version) of 49 CFR Part 195 stipulates a 180 day (270 day) response for the criteria: A potential crack indication that when excavated is determined to be a crack. Similarly, current version of API 1160 stipulates a 365 day response for the criteria: A potential crack indication that when excavated is determined to be a crack. Issues:  Provides no assessment/prioritization guidance  Implies no crack merits an immediate response Current Crack Response

13 a) A Likely Crack whose predicted depth is greater than 70% of nominal pipe wall. b) A Likely Crack with an FPR less than 1.1. c) A Likely Crack or Possible Crack indication predicted to interact with a dent. action required by an operator regardless of whether they are found within a segment of pipeline that could potentially impact an HCA or not Crack Response: RP Immediate Conditions

14 Create a flexible framework provides for operators to develop a crack response criteria in which different operators can leverage their experience and understanding of:  Inspection technology –Detection –Characterization –Sizing  Susceptibility  Growth mechanism Crack Response Approach

15 Section 11.6 Crack Tool Response Methodology  Map ILI features into a common frame of reference - integrity relevance: –Likely Crack –Possible Crack –Unlikely Crack  Valid cracking mechanism (susceptibility), to account for the presence of the ILI anomaly.  “Likely Crack” directly proceeds to remediation per the prescribed timeline.  “Possible” and “Unlikely” reflect the potential of an iterative field correlation program with a protracted timeline.

16 a) A crack ILI indication whose predicted depth is greater than 50 % of nominal pipe wall that has been determined to be one of the following: 1) A Likely Crack that is time-dependent or potentially time-dependent 2) A Possible Crack that is time-dependent b) A crack ILI indication with an FPR less than 1.25 that has been determined to be one of the following: 1) A Likely Crack that is time-dependent or potentially time-dependent 2) A Possible Crack that is time-dependent c) If not already available through previous correlation data or required excavations, a representative sample of the crack ILI indications that considers both the likelihood and time-dependency characterizations identified by the operator. Crack Response: 365-day Conditions

17  When a time-to-failure analysis of a crack ILI indication that DOES include tool tolerances reaches an FPR less than 1.1, is determined to be time-dependent, and is a Likely Crack or Possible Crack. OR  When the half-life of a time-to-failure analysis of a crack ILI indication that DOES include tool tolerances that reaches an FPR of 1.0, is determined to be time-dependent, and is a Likely Crack or Possible Crack. Crack Response: Scheduled Conditions

18 Crack Length  isolated cracks (river bottom): L = length of crack tip to crack tip  isolated cracks (elliptical profile): L= length of the effective area  colony or field of cracks: L = interlinking crack length –In many cases, the interlinked length is shorter than the length of the crack colony or field.  Annex C - Assessment Methods for Crack-like Flaws  Annex E - Toughness  Annex G - Fatigue C and n Values Crack Response

19 Fatigue Growth  Paris Law

20 Stress Corrosion Cracking  6 Threat Mechanisms Associated with Cracking –6.2 Environmentally Assisted Cracking Stress Corrosion Cracking  8 Crack Growth –8.3 Stress Corrosion Cracking and Corrosion Fatigue Growth  13 SCC Direct Assessment  Annex A - SCC Additional Information  Annex H - Prediction of Crack Growth with Consideration of Variable Loading Conditions on Oil and Gas Pipelines in Near-Neutral pH Environments

21 Section 14 In-the-Ditch Assessment  14 In-the-Ditch Assessment –14.1 General –14.2 Assessment of SCC and Other Pipe Body Cracks –14.3 Assessment of Longitudinal Seam Cracks  Annex K - In-the-Ditch Technology

22 API RP 1176’s Development Timeline  Work teams began in 2/2014  Version 5 sent to API PIWG, API OTG, PHMSA, and INGAA on 11/3/14 for review  Version 5 comments were resolved by 12/31/14  Version 6 was balloted 5/2015 –Extensive engagement across industry generated hundreds of comments and proposed edits  Version 7 (edits to version 6) will be balloted in 12/2015 –Anticipating late Q1/16 to early Q2/16 final release

23 RP 1176 Implementation Plan Objectives and Tactics  Create awareness of relevance of RP 1176 –Align industry around importance of implementing RP 1176 –Panel sessions at API Conf, Enbridge Cracking Forum, Banff Pipeline Integrity Workshop, Rosen Roundtable –Publishing information in technical journals –Finalizing communication materials for external audiences: taking points, pamphlet etc  Improve understanding –Provide additional API Conf. sessions to communicate content –Hold technical sessions to support implementation effectiveness  Assist institutionalizing –Developing a abridged companion document to support operator implementation –Communicate leadership roles  Leverage external communications –Increase appreciation of industry’s proactive approach to mitigate cracking-related integrity concerns