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GB/T 31405-2025: Test method for cathodic disbonding of pipeline protection coatings subjected to elevated temperatures
Status: Valid
GB/T 31405: Evolution and historical versions
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| GB/T 31405-2025 | English | 379 |
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Test method for cathodic disbonding of pipeline protection coatings subjected to elevated temperatures
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| GB/T 31405-2015 | English | 259 |
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Standard test method for cathodic disbonding of pipeline coatings subjected to elevated temperatures
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Standard similar to GB/T 31405-2025 GB/T 37309 | GB/T 35505 | GB/T 31554 | GB/T 19824 | GB/T 31404 | Basic data | Standard ID | GB/T 31405-2025 (GB/T31405-2025) | | Description (Translated English) | Test method for cathodic disbonding of pipeline protection coatings subjected to elevated temperatures | | Sector / Industry | National Standard (Recommended) | | Classification of Chinese Standard | A29 | | Classification of International Standard | 25.220.99 | | Word Count Estimation | 18,174 | | Date of Issue | 2025-12-02 | | Date of Implementation | 2026-07-01 | | Older Standard (superseded by this standard) | GB/T 31405-2015 | | Issuing agency(ies) | State Administration for Market Regulation, Standardization Administration of China | GB/T 31405-2025: Test method for cathodic disbonding of pipeline protection coatings subjected to elevated temperatures
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ICS 25.220.99
CCSA29
National Standards of the People's Republic of China
Replaces GB/T 31405-2015
High-Temperature Cathodic Disbondment Test Method for Pipeline Anticorrosion Coating
elevated temperatures
Implemented on July 1, 2026
State Administration for Market Regulation
The State Administration for Standardization issued a statement.
Table of contents
Preface III
1.Scope 1
2 Normative References 1
3.Terms and Definitions 1
4.Principle 1
5.Test medium 2
6.Test equipment 2
7 specimens 5
8.Experimental Procedure 5
9.Experimental Results and Data Processing 7.
10 Test Reports 8
Appendix A (Informative) Data Recording Table for High-Temperature Cathodic Disbondment Test of Pipeline Anticorrosion Coating 9
References 10
Foreword
This document complies with the provisions of GB/T 1.1-2020 "Standardization Work Guidelines Part 1.Structure and Drafting Rules of Standardization Documents".
Drafting.
This document supersedes GB/T 31405-2015 "High-Temperature Cathodic Disbondment Test Method for Corrosion-Resistant Coatings for Pipelines" and is consistent with GB/T 31405-2015.
In comparison, aside from structural adjustments and editorial changes, the main technical changes are as follows.
a) The scope has been changed (see Chapter 1, Chapter 1 of the.2015 edition);
b) The method overview (see Chapter 3 of the.2015 edition) has been removed;
c) Added terms and definitions (see Chapter 3);
d) The principle has been added (see Chapter 4);
e) Reagents and materials have been changed (see Chapter 5, Chapter 5 of the.2015 edition);
f) The experimental setup was modified (see Chapter 6, Chapter 4 of the.2015 edition);
g) The test specimen was modified (see Chapter 7, Chapter 6 in the.2015 edition);
h) The experimental procedures have been changed (see Chapter 8, Chapter 7 of the.2015 edition);
i) Added experimental results and data processing (see Chapter 9);
j) The report has been amended (see Chapter 10, Chapter 8 of the.2015 edition);
k) Precision and bias have been removed (see Chapter 9 of the.2015 edition).
Please note that some content in this document may involve patents. The issuing organization of this document assumes no responsibility for identifying patents.
This document was proposed by the China Petroleum and Chemical Industry Federation.
This document is under the jurisdiction of the National Technical Committee on Corrosion Control Standardization (SAC/TC381).
This document was drafted by. North China Electric Power Research Institute Co., Ltd., Zhejiang Gangxin Testing Technology Co., Ltd., and CNNC Nuclear Power Operation.
Management Co., Ltd., Zhejiang Yuxi Corrosion Control Co., Ltd., Langfang Aigema Xinli Materials Technology Co., Ltd., Ningbo Institute of Technology, Chinese Academy of Sciences
Institute of Materials Technology and Engineering, Changyuan Changtong New Materials Co., Ltd., Suzhou Thermal Power Research Institute Co., Ltd., China National Petroleum Corporation
Southwest Oil and Gas Field Branch Safety, Environmental Protection and Technical Supervision Research Institute of [Company Name], Hunan Anguang Inspection and Testing Co., Ltd., Qingdao Shangyu Environment
Technology Co., Ltd., Jiangsu Yihao Plastics Industry Co., Ltd., Hengyang Steel Pipe Keying Co., Ltd., Jiangsu Yulong Steel Pipe Technology Co., Ltd., China Railway
22nd Bureau Group Electrification Engineering Co., Ltd., China Corrosion International Corrosion Control Engineering Technology Research Institute (Beijing) Co., Ltd., Langfang Baichuan Wisdom
Energy Technology Development Co., Ltd., Guanghan Huaqi Anticorrosion Engineering Co., Ltd., Hubei Keying New Material Technology Co., Ltd., Guangdong Special Equipment
Maoming Testing Institute, China Corrosion Control Technology Association.
The main drafters of this document are. Wang Xijun, Zhang Wei, Wang Guangyong, Wu Huacheng, Huang Jinguang, Wang Liping, Cui Zhigang, Zhao Wanxiang, Feng Shaoguang, and Li Jie.
Wang Shuiyong, Xu Huanhui, Shu Ziqian, Li Jing, Zhang Peng, Ge Jie, Kong Quanxing, Tan Nanshu, Liu Shuan, Luo Zhongjiang, Yao Yuansheng, Chen Wenkui, Gao Jian, Zhang Tongsong
Wang Kai, Zhang Lihui, Wang Guiming, Xing Jun, Ren Zhifeng, Xu Keyu, Yang Jiahong, Wen Guosong, Guo Xiaoping, Qi Hongyang, Wang Long, Wang Wanyu, Liu Xuan.
This document was first published in.2015, and this is its first revision.
High-Temperature Cathodic Disbondment Test Method for Pipeline Corrosion Protection Coating
1 Scope
This document specifies the principle, test medium, test equipment, test specimens, test procedures, and test parameters for the high-temperature cathodic disbondment test of pipeline anti-corrosion coatings.
Test results, data processing, and test reports.
This document applies to the testing of the high-temperature cathodic disbondment resistance of the anti-corrosion coating of buried pipelines with cathodic protection and operating temperatures above 25°C.
2 Normative references
The contents of the following documents, through normative references within the text, constitute essential provisions of this document. Dated citations are not included.
For references to documents, only the version corresponding to that date applies to this document; for undated references, the latest version (including all amendments) applies.
This document.
GB/T 1266 Sodium Chloride Chemical Reagent
GB/T 6682 Specifications and test methods for water used in analytical laboratories
3 Terms and Definitions
The following terms and definitions apply to this document.
3.1
Reference electrode
An electrode with a stable, reproducible potential, used as a reference when measuring the potential of other electrodes.
[Source. GB/T 33373-2016, 3.12]
3.2
auxiliary electrode
When an external power source provides the applied protective current, the electrode is used to form a current-carrying circuit with the protected object.
[Source. GB/T 33373-2016, 4.3.6, with modifications]
3.3
test temperature
Temperature of the metal substrate during high-temperature cathode stripping tests on pipelines.
4.Principles
In high-temperature environments, after cathodic protection is applied to anti-corrosion pipelines, cathodic current may occur at defects in the pipeline's anti-corrosion layer.
The reduction reaction produces gases and OH- ions, which peel off the anti-corrosion layer. By artificially creating defects in the pipeline's anti-corrosion layer, the corrosion can be simulated.
Under high-temperature conditions and cathodic protection, a constant potential is applied to the pipeline for a specified time, causing a reduction reaction at the defect site, producing...
Gases such as OH- are used to peel off the anti-corrosion layer. After the test, eight evenly spaced radial scratches are made outward from the edge of the test hole to remove the anti-corrosion layer.
Cut the line, pry off the anti-corrosion layer with a blade, measure the peeling area along the edge of the defect, calculate the average radius, and characterize the cathodic stripping degree of the pipeline anti-corrosion layer.
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