1、Designator: Meta Bold 24/26Revision Note: Meta Black 14/16STP-PT-011INTEGRITY MANAGEMENT OF STRESS CORROSION CRACKING IN GAS PIPELINE HIGH CONSEQUENCE AREASSTP-PT-011 INTEGRITY MANAGEMENT OF STRESS CORROSION CRACKING IN GAS PIPELINE HIGH CONSEQUENCE AREAS Prepared by: R. R. Fessler BIZTEK Consulting
2、, Inc. A. D. Batte Macaw Engineering Ltd. M. Hereth PPIC Date of Issuance: October 31, 2008 This report was prepared as an account of work sponsored by ASME and the ASME Standards Technology, LLC (ASME ST-LLC). Neither ASME, ASME ST-LLC, the authors, nor others involved in the preparation or review
3、of this report, nor any of their respective employees, members, or persons acting on their behalf, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or r
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6、ency thereof. ASME ST-LLC does not take any position with respect to the validity of any patent rights asserted in connection with any items mentioned in this document, and does not undertake to insure anyone utilizing a publication against liability for infringement of any applicable Letters Patent
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8、th industry is not to be interpreted as government or industry endorsement of this publication. ASME is the registered trademark of the American Society of Mechanical Engineers. No part of this document may be reproduced in any form, in an electronic retrieval system or otherwise, without the prior
9、written permission of the publisher. ASME Standards Technology, LLC Three Park Avenue, New York, NY 10016-5990 ISBN No. 978-0-7918-3183-0 Copyright 2008 by ASME Standards Technology, LLC All Rights Reserved Integrity Management of SCC in HCAs STP-PT-011 iii TABLE OF CONTENTS Foreword .viii Abstract
10、. ix 1 SUMMARY. 1 2 BACKGROUND AND OBJECTIVES . 2 3 APPROACH 3 4 TASK 1 - CLARIFICATION OF ISSUES 4 5 TASK 2 - RESPONSES TO QUESTIONS . 6 5.1 Question 1: On what basis should HCAs and Segments be defined as SCC-susceptible?. 6 5.2 Question 2: How should SCC-susceptible HCAs and Segments be prioritiz
11、ed for assessment? . 6 5.3 Question 3: Where Hydrostatic Testing, SCC DA or Crack Detection ILI have been chosen as the assessment methods, what are the appropriate re-test intervals? 7 5.4 Question 4: What is the appropriate procedure for Hydrostatic Testing? . 8 5.5 Question 5: When using SCC DA,
12、where is the best place to dig and how many digs should be conducted? 8 5.6 Question 6: How should crack severity be defined and how should severity determine what kinds of remedial actions are appropriate? . 9 5.7 Question 7: What additional preventive and mitigative measures are appropriate for SC
13、C Condition Monitoring, and how are they to be used to enhance confidence in the management of SCC? 10 6 TASK 3 - INDUSTRY AND PEER REVIEWS . 12 7 TASK 4 - INTERACTIONS WITH DOT PHMSA 13 8 TASK 5 - INTERACTIONS WITH ASME 14 9 CONCLUDING REMARKS. 15 Appendix A - Field Experience of SCC in Gas Transmi
14、ssion Pipelines 16 Appendix B - Definition of SCC Susceptible HCAs and Segments . 39 Appendix C - Prioritizing SCC Susceptible HCAS and Segments. 48 Appendix D - ReAssessment Intervals. 57 Appendix E - Hydrostatic Test Procedure 80 Appendix F - Dig Locations for SCC DA 84 Appendix G - Number of Digs
15、 for SCC DA 101 Appendix H - Crack Severity . 103 Appendix I - Issues Related to Predicting Failure Pressure . 112 Appendix J - Issues Related to Estimating Remaining Life. 122 Appendix K - Condition Monitoring 132 Acknowledgments 141 STP-PT-011 Integrity Management of SCC in HCAs iv Abbreviations a
16、nd Acronyms .142 LIST OF TABLES Table 1 - Summary of Information Provided by the JIP Participants and Other Operators19 Table 2 - Effect of Proximity to Compressor Discharge on Failure Frequency (Datasets 1-6, 9) 22 Table 3 - Proportion of Hydrostatic Tests Failing due to High pH SCC in Each Valve S
17、ection (Dataset 2).22 Table 4 - Effect of Operating Stress on Failure Frequency for High pH SCC (Datasets 1, 3, 4, 5, 6, 9) .23 Table 5 - Frequency of In-Service Failures due to High pH SCC in the last 40 Years (Datasets 1, 3, 4, 5, 9) .23 Table 6 - Age of Pipelines When In-Service or Hydrostatic Te
18、st Failures Occurred due to High pH SCC (Datasets 1, 3, 4, 5, 6, 9).23 Table 7 - Effect of Proximity to Compressor Discharge on High pH SCC Found by Excavation (Dataset 11).24 Table 8 - Effect of Pipe Diameter and Operating Stress on High pH SCC Found by Excavation (Dataset 11).25 Table 9 - Occurren
19、ce of In-Service Ruptures and Leaks due to Near-Neutral pH SCC (Datasets 6, 7, 9) .26 Table 10 - Influence of Proximity to Compressor Discharge on In-Service Failures due to Near-Neutral pH SCC (Datasets 6, 7, 9) 26 Table 11 - Age at Which In-Service and Hydrostatic Test Failures Have Occurred due t
20、o Near-Neutral pH SCC (Datasets 6, 7, 9) 27 Table 12 - Proximity of Near-Neutral pH SCC Hydrostatic Test Failures to Compressor Discharges (Datasets 6, 7, 9).27 Table 13 - Relationship Between Coating Types and Near-Neutral pH SCC “Hits” from Excavations (Dataset 12) 28 Table 14 - Proximity of Near-
21、Neutral pH SCC “Hits” to Compressor Discharges (Dataset 12)28 Table 15 - Effect of Pipeline Age on Near-Neutral pH SCC Found by Excavation (Dataset 12) 29 Table 16 - Effect of Op. Stress on Near-Neutral pH SCC Found by Excavation (Dataset 12).29 Table 17 - Effect of Coating Type on Near-Neutral pH S
22、CC Found by Excavation (Dataset 13) .29 Table 18 - Proximity of Near-Neutral pH SCC “Hits” to Compressor Stations (Dataset 13) 29 Table 19 - Effect of Pipeline Age on Near-Neutral pH SCC Found by Excavation (Dataset 13) 30 Table 20 - Effect of Op. Stress on Near-Neutral pH SCC Found by Excavation (D
23、ataset 13).30 Table 21 - Distribution of Near-Neutral pH Stress Corrosion Crack Depths and Lengths Found by Excavation (Dataset 12)30 Table 22 - Distribution of Near-Neutral pH SCC Colony Depths and Lengths Found by Excavation (Dataset 13, Asphalt-Coated Pipe Only)31 Integrity Management of SCC in H
24、CAs STP-PT-011 v Table 23 - Summary of Near-Neutral pH SCC Results Obtained from ILI Crack Detection (Dataset 14) 31 Table 24 - Illustrative Example of Tier 1 Protocol. 55 Table 25 - Illustrative Example of Tier 2 Protocol. 56 Table 26 - Case Studies of Valve Sections with SCC and Multiple Hydrostat
25、ic Tests 66 Table 27 - Summary of Comparisons of Prediction from this Method with Actual Service Experiences 68 Table 28 - Various Ways to Calculate Flow Stress 73 Table 29 - Percent of Valve Sections Not Experiencing Failure Following First High-pH SCC Hydrotest (Based upon 38 valve sections) . 76
26、Table 30 - Percent of Valve Sections Not Experiencing Failure Following First NN-pH SCC Hydrotest (Based upon 11 valve sections, all tested 100% SMYS). 76 Table 31 RRF Topic Weights 86 Table 32 Graded Scale of RRF 87 Table 33 Graded Scale for Secondary Stress. 88 Table 34 RRFs for Drainage 89 Table
27、35 RRFs for Tier 1 and Tier 2 . 91 Table 36 - Summarized Illustration of Relative Risk Factors for Site Selection Tier 1 95 Table 37 - Summarized Illustration of Relative Risk Factors for Site Selection Tier 2 96 Table 38 - Factors to Consider in Prioritization of Segments and in Site Selection for
28、SCC DA (from NACE RP0204-2004). 97 Table 39 - Examples of Maximum Lengths of Category Zero Cracks. 105 Table 40 - Summary of Crack Severity Categories and Mitigation . 107 Table 41 - Cases for Sensitivity Study . 123 Table 42 - Predicted Failure Times for Category 1 and Category 2 Cracks, Using SURF
29、FLAW, CorLas and PAFFC 124 Table 43 - Life Predictions for Category 3 Cracks (Using SURFFLAW) . 128 Table 44 - Information Sources and their Relevance to Changes in SCC Risk . 134 LIST OF FIGURES Figure 1 - Questions Arising During SCC Integrity Management. 5 Figure 2 - Substituting the Average Crac
30、k Growth Rate for the Actual Variable Rate . 61 Figure 3 - Using Failure Pressure to Represent Flaw Size . 62 Figure 4 - Extrapolating the Maximum Prior Crack Growth Rate to Establish the Interval for the Next Re-Test. 63 Figure 5 - Establishing Subsequent Intervals Based upon Previous Intervals 64
31、STP-PT-011 Integrity Management of SCC in HCAs vi Figure 6 - Effects of Hydrostatic Test Pressure and Flow Stress on Length of Subsequent Intervals Between Re-Tests for an X52 Pipeline Operating at 72% SMYS .65 Figure 7 - Comparison of Service History with Predictions of this Method for Case 6 .67 F
32、igure 8 - Comparison of Service History with Predictions of this Method for Case 1 (Symbols are as described for Figure 7)68 Figure 9 - Log-Secant Failure Diagram for 30-inch-diameter, 0.312-inch wall-thickness X52 Pipe with a Flow Stress of 71,240 psi and a 2/3-size Charpy Energy of 20 ft.-lb. .71
33、Figure 10 - Ratio of Next Interval to Sum of Previous Intervals for Pipe in Figure 9 and Depth-wise Crack Growth with Constant Growth Rate.72 Figure 11 - Hypothetical Re-Test History to Illustrate Modification to Method Following a Re-Test Failure74 Figure 12 - Illustration of Modification to Re-Tes
34、t Intervals Following a Re-Test Failure .74 Figure 13 - Flaw Sizes that would be Critical at Various Pressures for Pipe from Figure 9 77 Figure 14 - Sequence of Failure Pressures in a Hydrostatic Test in which 20 Ruptures Initiated at Stress-Corrosion Cracks82 Figure 15 - Relation of Severity Catego
35、ries to Crack Lengths and Depths (Schematic)104 Figure 16 - Aspect Ratios of Small, Shallow Cracks 2 117 Figure 17 - Aspect Ratios of Coalesced Cracks Adjacent to In-Service and Hydrotest Failures 4117 Figure 18 - API 579/ASME FFS-1 Guidance for Assessing the Interaction of Coplanar and Non-Coplanar
36、 Cracks 16 118 Figure 19 - Comparisons of Predicted and Actual Failure Pressures for SCC-Containing Pipes using Different Prediction Methods 22 119 Figure 20 - PAFFC Full-Scale Validation Data for SCC 6120 Figure 21 - Comparisons of Failure Predictions using PAFFC and NG-18, for a 24 in. x 0.344 in.
37、 x X52 Pipe with 30 ft.-lb. Toughness .121 Figure 22 - Comparison of Predicted Lifetimes from CorLas and SURFFLAW for Category 1 and Category 2 Cracks.125 Figure 23 - Comparison of Predicted Lifetimes from PAFFC and SURFFLAW for Category 1 and Category 2 Cracks 125 Figure 24 - Comparison of Predicte
38、d Failure Times for Various Size Cracks in X52 Pipe of Typical Toughness 126 Figure 25 - Comparison of Predicted Failure Times for Various Size Cracks in X65 Pipe of Typical Toughness 126 Figure 26 - Effect of Wall Thickness on Predicted Lifetimes for Surviving Cracks in X52 Pipe with a Charpy Tough
39、ness of 20 ft.-lb. Assuming a Crack Growth Rate of 0.012 inch per year129 Figure 27 - Effect of Toughness on Minimum Wall Thickness Consistent with the Projected Lifetimes for X52 Pipe Assuming a Crack Growth Rate of 0.012 inch per year130 Figure 28 - Effect of Actual YS on Minimum Wall Thickness Co
40、nsistent with the Projected Lifetimes for X52 Pipe Assuming a Crack Growth Rate of 0.012 inch per year130 Integrity Management of SCC in HCAs STP-PT-011 vii Figure 29 - Minimum Wall Thickness to Meet Two Projected Lifetimes for Category 2 Cracks . 131 Figure 30 - Overall Flowchart for SCC Condition
41、Monitoring 136 STP-PT-011 Integrity Management of SCC in HCAs viii FOREWORD In response to concerns about managing the threat of stress corrosion cracking (SCC) in high-pressure gas transmission pipelines, and in the light of recently introduced legislation concerning integrity management plans focu
42、sing on high consequence areas (HCAs), a group of five major gas transmission companies initiated a joint industry project (JIP) in January 2006 to develop technical rationales to support the key processes of SCC integrity management, including hydrostatic testing, in-line inspection (ILI) and SCC d
43、irect assessment (DA). These partner companies include Spectra Energy (formerly Duke Energy Gas Transmission), El Paso Pipeline Group, Panhandle Energy, TransCanada Pipelines Ltd. and Great Lakes Gas Transmission. Established in 1880, the American Society of Mechanical Engineers (ASME) is a professi
44、onal not-for-profit organization with more than 127,000 members promoting the art, science and practice of mechanical and multidisciplinary engineering and allied sciences. ASME develops codes and standards that enhance public safety, and provides lifelong learning and technical exchange opportuniti
45、es benefiting the engineering and technology community. Visit www.asme.org for more information. The ASME Standards Technology, LLC (ASME ST-LLC) is a not-for-profit Limited Liability Company, with ASME as the sole member, formed in 2004 to carry out work related to newly commercialized technology.
46、The ASME ST-LLC mission includes meeting the needs of industry and government by providing new standards-related products and services, which advance the application of emerging and newly commercialized science and technology and providing the research and technology development needed to establish
47、and maintain the technical relevance of codes and standards. Visit www.stllc.asme.org for more information. Integrity Management of SCC in HCAs STP-PT-011 ix ABSTRACT This report includes a compilation of results obtained through a series of white papers developed as part of a gas transmission compa
48、ny JIP addressing specific issues related to SCC in gas pipeline HCAs. This report presents the overall project approach, findings and outcomes. The overall outcome of the JIP has been the development and collation of a significant body of supporting information, made available to pipeline operators
49、 and to the pipeline industry, providing the basis for sound decision making regarding the issues to be addressed when managing the integrity of pipelines that are potentially subject to the threat of SCC. In particular, this report includes: A review and update of SCC experience in 130,000 miles of high-pressure gas pipelines. Validation of the ASME B31.8S criteria for determining segments and HCAs most likely to be susceptible to high pH SCC. Demonstration that the modified ASME B31.8S criteria also are applicable to near-neutral pH SCC. Development of
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