GB/T 21448-2017 English PDFUS$679.00 · In stock
Delivery: <= 6 days. True-PDF full-copy in English will be manually translated and delivered via email. GB/T 21448-2017: Specification of cathodic protection for underground steel pipelines Status: Valid GB/T 21448: Historical versions
Basic dataStandard ID: GB/T 21448-2017 (GB/T21448-2017)Description (Translated English): Specification of cathodic protection for underground steel pipelines Sector / Industry: National Standard (Recommended) Classification of Chinese Standard: E98 Classification of International Standard: 75.200 Word Count Estimation: 34,337 Date of Issue: 2017-12-29 Date of Implementation: 2018-07-01 Older Standard (superseded by this standard): GB/T 21448-2008 Regulation (derived from): National Standards Bulletin 2017 No. 32 Issuing agency(ies): General Administration of Quality Supervision, Inspection and Quarantine of the People's Republic of China, Standardization Administration of the People's Republic of China GB/T 21448-2017: Specification of cathodic protection for underground steel pipelines---This is a DRAFT version for illustration, not a final translation. Full copy of true-PDF in English version (including equations, symbols, images, flow-chart, tables, and figures etc.) will be manually/carefully translated upon your order.Specification of cathodic protection for underground steel pipelines ICS 75.200 E98 National Standards of People's Republic of China Replace GB/T 21448-2008 Technical specification for cathodic protection of buried steel pipelines (ISO 15589-1.2015, Petroleum, petrochemical and naturalgasindustries- Cathodicprotectionofpipelinesystems-Part 1. On-landpipelines, NEQ) Released on.2017-12-29 2018-07-01 implementation General Administration of Quality Supervision, Inspection and Quarantine of the People's Republic of China China National Standardization Administration issued ContentForeword I 1 Scope 1 2 Normative references 1 3 Terms, definitions and abbreviations 1 4 General 3 5 forced current system 7 6 sacrificial anode system 11 7 Testing and Monitoring 15 8 Additional measures 17 9 Construction and commissioning 19 10 Management and Maintenance 22 Appendix A (informative) Cathodic protection calculation formula 27ForewordThis standard was drafted in accordance with the rules given in GB/T 1.1-2009. This standard replaces GB/T 21448-2008 "Technical Specifications for Cathodic Protection of Buried Steel Pipelines", compared with GB/T 21448-2008, The main technical changes except editorial changes are as follows. --- further clarified the requirements for temporary cathodic protection (see 4.1.3); --- Modified the "Cathode Protection Guidelines" and added "Cathode Protection Guidelines under AC Interference" and "Cathode Protection Guidelines under DC Interference" The provisions of "" (see 4.4); --- Increased requirements for forced current system power supply equipment (see 5.1); --- Increased the main performance requirements of graphite anodes, conductive polymer linear anodes and MMO-Ti linear anodes (see 5.2.5.2, 5.2.5.3 and 5.2.5.4); --- Added "Cathodic Protection for Parallel Pipes" requirements (see 5.3); --- Modified sacrificial anode performance specifications (see 6.2 and 6.3); increased design requirements for sacrificial anode systems (see 6.4.1); Changed the selection requirements of the sacrificial anode type and the requirements for filling materials (see 6.4.2 and 6.5); --- Refined the special requirements of the test device (see 7.1.2), increased the type of test piles (see 7.1.3), added "check films, Polarized probe and resistance probe" (see 7.1.4); --- Refined the requirements related to casing, lightning protection and surge protectors in "Additional Measures" (see 8.2, 8.3 and 8.4); --- Added "construction and commissioning" (see Chapter 9); ---Modified the contents of "Management and Maintenance" (see Chapter 10); --- Revised Appendix A and removed Appendix B. Appendix A was revised from a normative appendix to an informative appendix (see Appendix A). This standard uses the redrafting method to refer to ISO 15589-1.2015 "Cathodic protection of pipeline systems for petroleum, petrochemical and natural gas industries" Part 1. The Onshore Pipeline is compiled, and the degree of conformity with ISO 15589-1.2015 is non-equivalent. This standard is proposed and managed by the National Oil and Gas Standardization Technical Committee (SAC/TC355). This standard was drafted. China Petroleum Pipeline Engineering Co., Ltd., China Petroleum Planning Institute, China National Petroleum Pipeline Branch, Southwest Branch of China National Petroleum Corporation Engineering Design Co., Ltd., Sinopec Pipeline Storage and Transportation Co., Ltd. The main drafters of this standard. Huang Liuqun, Zhang Wenwei, Liao Wei, Luo Feng, Huang Li, Zheng Ansheng, Yan Mingzhen, Li Guohui, Teng Yanping, Zhang Ping, Huang Chunrong, Ma Xiaocheng, Liu Jia, Ding Jie, Wang Jie, Guo Juanli, Chen Shasha, Fu Wei, Pan Huailiang, Fu Pingping, Cheng Ming, Zhang Yanfeng. The previous versions of the standards replaced by this standard are. ---GB/T 21448-2008. Technical specification for cathodic protection of buried steel pipelines1 ScopeThis standard specifies the design, construction, testing, management and maintenance of the external surface cathodic protection system for land-buried steel pipelines (hereinafter referred to as pipelines). Minimum technical requirements for protection. This standard applies to land-buried steel oil, gas, water pipelines.2 Normative referencesThe following documents are indispensable for the application of this document. For dated references, only dated versions apply to this article. Pieces. For undated references, the latest edition (including all amendments) applies to this document. GB/T 4208 enclosure protection grade GB/T 4950 zinc-aluminum-cadmium alloy sacrificial anode GB/T 10123 Metal and alloy corrosion basic terms and definitions GB/T 17731 magnesium alloy sacrificial anode GB/T 21246 buried steel pipeline cathodic protection parameter measurement method GB 50058 Explosion Hazardous Environment Power Equipment Design Specification GB 50217 Power Engineering Cable Design Specification GB/T 50698 buried steel pipeline AC interference protection technical standards GB 50991 buried metal pipeline DC interference protection technical standards SY/T 0029 Buried steel inspection sheet application technical specification SY/T 0086 Cathodic Protection Pipe Electrical Insulation Standard SY/T 0087.1 Corrosion Evaluation Criteria for Steel Pipelines and Storage Tanks Direct Evaluation of External Corrosion of Buried Steel Pipelines SY/T 0096 forced current deep anode bed technical specification SY/T 0516 Technical Specifications for Insulated Joints and Insulated Flanges SY/T 6964 Technical Specification for Cathodic Protection of Oil and Gas Stations 3 Terms, definitions and abbreviations 3.1 Terms and definitions The following terms and definitions as defined in GB/T 10123 apply to this document. 3.1.1 Anode filler anodebackfil A low-resistivity material filled around the buried anode to maintain humidity, reduce electrical resistance between the anode and the electrolyte, and prevent yang Extremely polarized. 3.1.2 Jumper bond Use metal conductors (mostly copper conductors) to connect two points on the same metal structure or different metal structures to ensure the between two points Electrical continuity. 3.1.3 Decoupling direct device directcurrentdecouplingdevice A device that provides low impedance for AC current and high resistance channels for DC current. For example. polarized batteries, capacitors, diodes. 3.1.4 Confluence point drainpoint The connection point between the cathode cable and the protected pipe in the cathodic protection system, through which the protection current flows back to the power source. 3.1.5 Equipotential bonding equipotential bonding The separate metal structure is directly connected to the lightning protection device by a conductor or via a surge protector to reduce the potential difference caused by the lightning current. 3.1.6 Ground bed Buried sacrificial anode or forced current auxiliary anode system. 3.1.7 Auxiliary anode impressed-currentanode An electrode used to supply current in a forced current cathodic protection system. 3.1.8 Power-off potential instant-OFFpotential Instantaneous power-off potential To test the no-IR drop potential, the potential measured immediately after the short-term delay of the loop current interruption. 3.1.9 IR drop IRdrop The product of all current and loop resistance (mainly electrolyte resistance and pipe resistance) in the cathodic protection circuit. 3.1.10 Polarized potential No IR drop potential Eliminate the potential of the tube to the electrolyte after the IR drop caused by the cathodic protection current or other current. 3.1.11 Insulation device isolating/insulatingdevices It is used to isolate electrical continuity between metals, and refers to special accessories and processed parts. 3.1.12 Linear anode linearauxiliaryanode The anode body consists of a linear, continuous anode material filled with coke filler around the anode material and pre-packaged in the fabric overlay and Wear-resistant woven mesh. For example, a conductive polymer linear anode, a mixed metal oxide (MMO-Ti) linear anode. 3.1.13 Test pile testpost A facility located along the buried pipeline for monitoring and testing the cathodic protection parameters of the pipeline. 3.1.14 Power-on potential ONpotential The pipe-to-electrolyte potential measured during continuous operation of the cathodic protection system. 3.1.15 Pitting resistance equivalent number fittingsistanceequivalentnumber; PREN According to the chromium, molybdenum, tungsten and nitrogen components contained in the chemical composition of the stainless steel alloy, the value of the pitting resistance of the stainless steel is reflected and predicted. 3.1.16 Polarization polarization The change in the electrolyte potential of the pipe caused by an external current. 3.1.17 Protection potential protectionpotential The metal corrosion rate of the pipe can be accepted in the state of the pipe to the electrolyte potential. 3.1.18 Potentiostat potentiostatunit A power supply device that automatically maintains a constant electrolyte potential to the pipe. 3.1.19 Power supply equipment rated output voltage ratedoutputvoltage UdN The highest output voltage specified by the power supply unit. 3.1.20 Power supply equipment rated output current ratedoutputcurrent IdN The maximum output current specified by the power supply unit. 3.1.21 Stray current Current flowing in a non-designated loop. 3.2 Abbreviations The following abbreviations apply to this document. CCVT. Closed-cycle steam generator set. CSE. Copper/saturated copper sulfate reference electrode. SCC. Stress corrosion cracking. SCE. Saturated KCl calomel electrode. SRB. sulfate reducing bacteria. TEG. Thermoelectric generator.4 General4.1 Basic requirements 4.1.1 Cathodic protection shall be adopted for buried oil and gas long-distance pipelines, oil and gas field pipelines and buried pipelines in oil and gas fields; other buried areas The pipeline should be protected by a cathode. 4.1.2 Cathodic protection shall be implemented in conjunction with the coating. 4.1.3 The cathodic protection project shall be surveyed, designed, constructed and put into operation at the same time as the main project. When the cathodic protection system is buried in the pipeline for three months Temporary cathodic protection measures should be taken to protect the pipeline when it cannot be put into operation; in a highly corrosive soil environment, temporary should be applied when the pipeline is buried Cathodic protection measures; temporary cathodic protection measures should be maintained until the permanent cathodic protection system is put into operation; for the influence of DC stray current interference Pipelines, cathodic protection systems and drainage protection measures should be commissioned within three months. 4.1.4 Cathodic protection of buried pipelines can be carried out by forced current method, sacrificial anode method or a combination of two methods, depending on the scale of the project and the soil. The environment, the insulation performance of the pipeline anti-corrosion layer and other factors are economically and rationally selected. 4.1.5 Cathodic protection for special conditions such as high temperature, anti-corrosion layer peeling, thermal insulation layer, shielding, bacterial erosion and abnormal electrolyte pollution Protection may be ineffective or partially ineffective and should be considered during design. 4.1.6 Cathodic protection of buried pipelines in stations shall comply with the provisions of SY/T 6964. 4.2 Pipeline conditions 4.2.1 Electrical insulation 4.2.1.1 General requirements The cathodic protection pipe shall be electrically insulated from the unprotected metal structure and the common or field grounding system. Cathodic protection circuit piping should be electrically connected to metal structures such as pipelines in the process station, wellsite facilities, non-cathodic protected pipelines and steel casings. insulation. The cathodic protection pipeline can be installed with electrical insulation device in the stray current interference interference zone. When electrical insulation is not possible, the cathodic protection design should provide adequate cathodic protection current and effective current distribution. The design, materials, dimensions and construction of electrical insulation shall be in accordance with SY/T 0516 and SY/T 0086. Insulated joints should be used The overall type. For pipes conveying conductive medium, the inner surface of the insulated joint and the inner surface of the pipe connected to the insulated joint shall be coated with an inner coating. The length of the coating should be calculated according to the resistivity of the transport medium to correct the corrosion caused by the potential difference between the two sides. The sealing material used, The anti-corrosion material and the insulating material should be adapted to the medium to be transported. 4.2.1.2 Installation position of electrical insulation device Insulation can be placed at the following locations in the pipeline. --- Connection with the station pipe; --- Connection with the branch line pipe; ---Between different metal materials; --- on the pipe segment affected by AC and DC interference; --- Cathodic protection between the pipeline and the unprotected metal structure. The insulating device should not be placed in a position where it is easy to form conductive condensate or free water. 4.2.1.3 Installation of electrical insulation The installation of electrical insulation shall comply with the relevant provisions of SY/T 0086. Insulation joints and insulation flanges shall be tested for insulation resistance before installation. The performance shall comply with the requirements of SY/T 0516. Test facilities should be installed at the insulation joint installation. When installing the insulation flange, it is recommended to adopt dustproof and waterproof sealing measures. 4.2.1.4 Protection of electrical insulation Insulated joints and insulating flanges shall be provided with surge protectors. Surge protector settings should not affect the performance of insulated joints or insulated flanges. Anti-surge protector can adopt solid state decoupler Lightning device, spark gap, electrolytic grounded battery, polarized battery, equipotential connector, etc. 4.2.2 Electrical continuity 4.2.2.1 Cathodic protection piping shall have good electrical continuity. 4.2.2.2 Electrical continuity jumpers may be placed on both sides of the electrical insulation device. For non-welded steel pipelines, electrical continuity spans shall be provided in the pipeline Joint. 4.2.2.3 Electrical continuity bridging shall be carried out in the test device. 4.2.3 Grounding 4.2.3.1 When the cathodic protection pipeline needs to be grounded, the grounding system should be compatible with the cathodic protection system, and the decoupling isolation can be installed in the grounding loop. Device. When the pipe is partially grounded, a zinc or galvanized grounding electrode can be used to connect directly to the pipe. 4.2.3.2 All grounding facilities should not adversely affect the cathodic protection system. 4.3 Design information and site survey 4.3.1 When designing the pipeline cathodic protection system, the following technical data should be collected. ---Pipe parameters, including length, diameter, wall thickness, material type and grade, type and grade of anti-corrosion layer; ---Conveying medium, design temperature, design pressure, operating temperature and operating pressure; --- Pipeline routing strip drawing; --- Distribution of process stations and valve rooms; --- Crossing the location and structure of rivers, railways, and highways; --- Distribution of existing buried cables, metal structures and steel pipes along the line; ---Casing position and structure; ---Type of trench backfill material; ---Other electric equipment on the pipeline; --- Topography and soil characteristics, including soil resistivity, pH, bacteria causing corrosion, frozen soil; ---Climatic conditions; ---The position, direction and rated voltage of high voltage transmission lines or buried high voltage cables; --- Characteristic parameters of adjacent AC and DC electrified traction systems, substation locations and characteristic parameters of other interference current sources; ---Type and location of the grounding system; --- Cathodic protection system design life; ---Environmental conditions for the installation of cathodic protection facilities; ---Insulation type and location; ---The availability of the power supply; --- Type and location of telemetry systems that can be used for remote monitoring. 4.3.2 The site surveyed project should include the following contents. --- The soil resistivity of different depths in the optional area of the anode bed; --- Corrosion conditions for bacterial activity; --- AC and DC interference source characteristic parameters and relative position relationship with the pipeline; -- The data collected in -4.3.1 does not meet the design requirements of the project. 4.4 Cathodic protection criteria 4.4.1 No IR drop cathodic protection potential The no-IR reduction cathodic protection potential EIRfree should meet the requirements of equation (1). El≤EIRfree≤Ep (1) In the formula. El --- limit critical potential; EIRfree---no IR drop cathodic protection potential; Ep --- The minimum protection potential when the metal corrosion rate is less than 0.01 mm/a. 4.4.2 Cathodic protection potential The cathodic protection potential should meet the requirements of Table 1. During the life of the pipeline, consideration should be given to the cathodic protection of the dielectric resistivity changes around the pipe. The effect of the potential. Table 1 Natural potential, minimum protection potential and limiting critical potential of metallic materials in soil and water Metal or alloy environmental conditions Natural potential ECOR (Reference) Minimum protection potential Ep (no IR drop) Limiting critical potential El (no IR drop) Carbon steel, low alloy steel And cast iron General soil and water environment -0.65~-0.40 -0.85 Eal T >60°C soil and water environment c -0.80~-0.50 -0.95 Eal T< 40°C, 100< ρ< 1000Ω·m Oxygen-containing soil and water environment -0.50~-0.30 -0.75 Eal T< 40°C, ρ>1000Ω·m Oxygen-containing soil and water environment -0.40~-0.20 -0.65 Eal Sulfate-reducing bacteria (SRB) rot Oxidized soil and water environment -0.80~-0.65 -0.95 Eal Austenitic PREN< 40 Stainless steel PREN >40 Aussie Stainless steel Martensite or austenitic-iron Prime (double phase) stainless steel Neutral and alkaline at ambient temperature Soil and water environment -0.10~ 0.20 -0.50 Edl -0.10~ 0.20 -0.30 - -0.10~ 0.20 -0.50 Edl stainless steel At ambient temperature, acidic Soil and water environment -0.10~ 0.20 Eep Edl Galvanized steel At ambient temperature, soil and water environment -0.20~0.00 -0.20 - -1.10~0.00 -1.20 - Note. All potentials are relative to copper/saturated copper sulfate reference electrodes (CSE, the same below). a For high-strength non-alloy steels and low-alloy steels with yield strengths exceeding 550 N/mm2, the critical limiting potential values should be documented or passed through experim......Tips & Frequently Asked Questions:Question 1: How long will the true-PDF of GB/T 21448-2017_English be delivered?Answer: Upon your order, we will start to translate GB/T 21448-2017_English as soon as possible, and keep you informed of the progress. The lead time is typically 4 ~ 6 working days. The lengthier the document the longer the lead time.Question 2: Can I share the purchased PDF of GB/T 21448-2017_English with my colleagues?Answer: Yes. The purchased PDF of GB/T 21448-2017_English will be deemed to be sold to your employer/organization who actually pays for it, including your colleagues and your employer's intranet.Question 3: Does the price include tax/VAT?Answer: Yes. 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