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GB/T 42177-2022Technical requirements and test methods for gaseous hydrogen valves used in hydrogen fuelling stations (English PDF)

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Issued by

SAMR; SAC

Level / Type

National · Recommended

Issue date

December 30, 2022

Implementation date

April 1, 2023

Scope

GB/T 42177-2022 (Technical requirements and test methods for gaseous hydrogen valves used in hydrogen fuelling stations) is available as an English-translated PDF.

GB/T 42177-2022 — This document specifies the technical requirements, test methods, marks and other requirements for gaseous hydrogen valves used in hydrogen fuelling stations (hereinafter referred to as "valves"). This document applies to gaseous hydrogen valves used in hydrogen fuelling stations that meet the following conditions: a) The ambient temperature is -40 degrees C~60 degrees C; b) The hydrogen charging pressure does not exceed 70 MPa at 15°C.

Document preview — GB/T 42177-2022

National Standard of the People's Republic of China

Issued by: SAMR; SAC

Contents

  • Foreword5
  • 1 Scope6
  • 2 Normative references6
  • 3 Terms and definitions7
  • 4 Technical requirements8
  • 4.1 Basic requirements8
  • 4.2 Materials9
  • 4.3 Working pressure level9
  • 5 General test methods and qualification indicators10
  • 5.1 Basic requirements10
  • 5.2 Test conditions11
  • 5.3 Extreme temperature hydrogen cycle test12
  • 5.4 Leakage test12
  • 5.5 Overpressure hydrogen cycle test13
  • 5.6 Hydrostatic test14
  • 5.7 Hydraulic strength test14
  • 5.8 Torque test14
  • 5.9 Bending test14
  • 5.10 Non-metal seal test16
  • 5.11 Precooled hydrogen exposure test16
  • 6 Check valves17
  • 6.1 Extreme temperature hydrogen cycle test17
  • 6.2 Leakage test17
  • 6.3 Overpressure hydrogen cycle test17
  • 6.4 Hydrostatic test18
  • 6.5 Hydraulic strength test18
  • 6.6 Bending test18
  • 6.7 Non-metal seal test18
  • 7 Excess flow valves18
  • 7.1 Extreme temperature hydrogen cycle test18
  • 7.2 Leakage test18
  • 7.3 Overpressure hydrogen cycle test18
  • 7.4 Hydrostatic test18
  • 7.5 Hydraulic strength test18
  • 7.6 Torque test19
  • 7.7 Bending test19
  • 7.8 Non-metal seal test19
  • 7.9 Action test19
  • 7.10 Action cycle test19
  • 7.11 Pressure pulse test19
  • 8 Control valves20
  • 8.1 Extreme temperature hydrogen cycle test20
  • 8.2 External leakage test20
  • 8.3 Overpressure hydrogen cycle test20
  • 8.4 Hydrostatic test20
  • 8.5 Hydraulic strength test21
  • 8.6 Torque test21
  • 8.7 Bending test21
  • 8.8 Non-metal seal test21
  • 8.9 Action test21
  • 8.10 Action cycle test21
  • 9 Break away coupling22
  • 9.1 Extreme temperature hydrogen cycle test22
  • 9.2 External leakage test22
  • 9.3 Overpressure hydrogen cycle test23
  • 9.4 Hydrostatic test23
  • 9.5 Hydraulic strength test23
  • 9.6 Torque test24
  • 9.7 Bending test24
  • 9.8 Non-metal seal test24
  • 9.9 Axial separation pull test24
  • 9.10 Impact test25
  • 9.11 Drop test26
  • 9.12 Torsion cycle test27
  • 9.13 Precooled hydrogen exposure test27
  • 10 Manual valves28
  • 10.1 Extreme temperature hydrogen cycle test28
  • 10.2 Leakage test28
  • 10.3 Overpressure hydrogen cycle test28
  • 10.4 Hydrostatic test28
  • 10.5 Hydraulic strength test28
  • 10.6 Torque test28
  • 10.7 Bending test28
  • 10.8 Non-metal seal test28
  • 10.9 Maximum flow shutdown test28
  • 10.10 Open and close cycle test29
  • 10.11 Torque cycle test29
  • 11 Filters30
  • 11.1 Extreme temperature hydrogen cycle test30
  • 11.2 Structural integrity and initial bubble point test30
  • 11.3 Filtration characteristic test of filter element30
  • 11.4 Pressure drop flow characteristic test30
  • 11.5 Flow fatigue characteristics test31
  • 11.6 Rated axial load test31
  • 11.7 Anti-rupture property test31
  • 12 Safety valves31
  • 12.1 Extreme temperature hydrogen cycle test31
  • 12.2 Leakage test32
  • 12.3 Overpressure hydrogen cycle test32
  • 12.4 Hydrostatic test32
  • 12.5 Torque test33
  • 12.6 Bending test33
  • 12.7 Non-metal seal test33
  • 12.8 Action test33
  • 13 Globe valve34
  • 13.1 Extreme temperature hydrogen cycle test34
  • 13.2 Leakage test34
  • 13.3 Overpressure hydrogen cycle test34
  • 13.4 Hydrostatic test34
  • 13.5 Hydraulic strength test34
  • 13.6 Torque test34
  • 13.7 Bending test34
  • 13.8 Non-metal seal test35
  • 13.9 Open and close cycle test35
  • 13.10 Maximum flow shutdown test35
  • 13.11 Precooled hydrogen exposure test35
  • 14 Marks36
  • 14.1 Mark information36
  • 14.2 Marking method37
  • Bibliography38

1 Scope

This document specifies the technical requirements, test methods, marks and other requirements for gaseous hydrogen valves used in hydrogen fuelling stations (hereinafter referred to as "valves").

This document applies to gaseous hydrogen valves used in hydrogen fuelling stations that meet the following conditions:

a) The ambient temperature is -40 degrees C~60 degrees C;

b) The hydrogen charging pressure does not exceed 70 MPa at 15°C.

2 Normative references

The following referenced documents are indispensable for the application of this document. For dated references, only the edition cited applies. For undated references, the latest edition of the referenced document (including any amendments) applies.

GB/T 528, Rubber, vulcanized or thermoplastic -- Determination of tensile stress-strain properties

GB/T 4213, Pneumatic industrial process control valves

GB/T 12220, Industrial valves -- Marking

GB/T 12241, Safety valves -- General requirements

GB/T 14041.1, Hydraulic fluid power -- Filter elements -- Part 1: Verification of fabrication integrity and determination of the first bubble point

GB/T 14041.3, Hydraulic fluid power -- Filter elements -- Part 3: Verification of collapse/burst pressure rating

GB/T 14041.4, Hydraulic fluid power -- Filter elements -- Part 4: Method for rated end load test

GB/T 17486, Hydraulic fluid power -- Filters -- Evaluation of differential pressure versus flow characteristics

GB/T 17488, Hydraulic fluid power -- Filter elements -- Determination of resistance to flow fatigue using particulate contaminant

GB/T 18853, Hydraulic fluid power filters -- Multi-pass method for evaluating filtration performance of a filter element

GB/T 21465, Terminology for valves

GB/T 24499, Technology glossary for gaseous hydrogen, hydrogen energy and hydrogen energy system

GB/T 32808, Valves -- Model designation method

GB/T 34542.2, Storage and transportation systems for gaseous hydrogen -- Part 2:

Test methods for evaluating metallic material compatibility in hydrogen atmosphere

GB/T 34542.3, Storage and transportation systems for gaseous hydrogen -- Part 3:

Test method for determination of the susceptibility of metallic materials to hydrogen gas embrittlement (HGE)

GB 50156, Code for design and construction of filling station

GB 50516, Technical code for hydrogen fuelling station

3 Terms and definitions

For the purposes of this document, the terms and definitions defined in GB/T 12241,

GB/T 21465, GB/T 24499 as well as the followings apply.

3.1 nominal size

An alphanumeric dimensional designation for valves, consisting of the letters DN followed by a dimensionless integer number.

NOTE: This dimensionless number is directly related to characteristic dimensions such as the bore diameter or outer diameter (expressed in millimeters) of the end fitting. Unless otherwise specified in the relevant standard, the dimensionless number following DN does not represent a measured value and shall not be used in calculations.

[Source: GB/T 1047-2019, 2.1, modified]

3.2 check valve

A valve that the opening and closing parts (valve disc) automatically prevent the reverse flow of the medium with the help of the force of the medium.

3.3 excess flow valve

4.1.2 Valves made of the same material under similar design conditions may not be re-

tested according to the items specified in this document.

4.1.3 In addition to the test items specified in this document, other reliable test methods

can be used to test the service performance of the valve in a high-pressure hydrogen environment.

4.1.4 The performance of pneumatic control valves shall comply with the requirements

specified in GB/T 4213. Electrically controlled valves shall adopt explosion-proof electric mechanisms. The selection of explosion-proof grade shall comply with the requirements specified in GB 50156 and GB 50516.

4.1.5 The valve shall be reliably sealed and clean to prevent internal and external

impurities from contaminating the hydrogen.

4.2 Materials

4.2.1 Valve materials shall consider corrosion resistance, wear resistance, aging

resistance, electrical conductivity, impact strength, heat resistance, low temperature impact resistance, ultraviolet radiation resistance and hydrogen embrittlement resistance.

4.2.2 Metal materials shall have good hydrogen compatibility. The test methods shall

be implemented in accordance with the requirements specified in GB/T 34542.2 and

GB/T 34542.3.

4.2.3 Non-metallic materials shall have good hydrogen compatibility. Its fatigue

performance, durability limit and creep strength shall meet the requirements of the design documents within the design life of the valve.

4.2.4 The service temperature range of non-metallic seal materials shall meet the

requirements of the valve operating temperature. Its tensile strength and elongation after break shall be measured according to the requirements specified in GB/T 528 and meet the requirements of the design documents.

4.3 Working pressure level

Working pressure level (HSL) is represented by "H+ value", in MPa. Its relationship with nominal working pressure (NWP), maximum working pressure (1.25 NWP), and maximum allowable working pressure (1.375 NWP) is shown in Table 1 .

5.2.3 Test medium

The test medium shall meet the following requirements:

a) The medium for the extreme temperature hydrogen cycle test, leakage test, overpressure hydrogen cycle test, bending test, non-metal seal test, pre-cooled hydrogen exposure test, action cycle test, pressure pulse test and opening and closing cycle test is hydrogen;

b) The medium of hydrostatic test is water;

c) The medium for other tests can be helium, nitrogen or dry clean air.

5.3 Extreme temperature hydrogen cycle test

5.3.1 Test method

Block the valve outlet. Connect the valve inlet to the hydrogen source. The lower limit of circulating pressure shall not exceed 0.05 times the maximum allowable working pressure of the valve. The upper limit of circulating pressure shall be within the range of (1~1.03) times the maximum allowable working pressure of the valve. The frequency shall not exceed 10 times/min. Valve seals can be replaced after 16,000 pressure cycles.

The test shall be carried out according to the following steps:

a) Normal temperature: At normal temperature, the valve is continuously tested for 100,000 cycles;

b) High temperature: The valve is continuously tested for 1,000 cycles at a test temperature of no less than 85°C;

c) Low temperature: The valve is continuously tested for 1,000 cycles at a test temperature not higher than -40°C.

5.3.2 Qualification indicators

The valve shall not leak or rupture within 102,000 pressure cycle tests.

5.4 Leakage test

5.4.1 Test methods
5.4.1.1 Test preparation

Before testing, purge the valve with nitrogen. And seal it at 0.3 times the maximum allowable working pressure of the valve. For high and low temperature tests, the valve shall be left to stand at the specified temperature for at least 1 h before the test.

shall comply with the requirements specified in 5.4.2.

5.10 Non-metal seal test

5.10.1 Test method

Block the valve outlet. Connect the valve air inlet to the air source. At normal temperature, fill with hydrogen to the maximum allowable working pressure of the valve. After maintaining the pressure for 70 h, the test pressure was quickly reduced to atmospheric pressure. Afterwards, conduct a leakage test on the valve according to the test method specified in 5.4.1.

5.10.2 Qualification indicators

Use special leak detection fluid to detect leaks. There shall be no bubbles generated within the specified test time.

5.11 Precooled hydrogen exposure test

5.11.1 Test method

The test steps are as follows:

a) Fill the valve with pre-cooled hydrogen gas at a temperature not higher than -40°C at a flow rate of not less than 30 g/s at normal temperature for at least 3 min. After that, stop inflating for 2 min. Repeat the above operation 10 times;

b) Fill the valve with pre-cooled hydrogen gas at a temperature not higher than -40°C at a flow rate of not less than 30 g/s at normal temperature for at least 3 min.

After that, stop inflating for 15 minutes. Repeat the above operation 10 times;

c) The valve shall be tested for leakage according to the test method specified in 5.4.1.

NOTE: Only suitable for valves through which pre-cooled hydrogen flows.

5.11.2 Qualification indicators

Use special leak detection fluid for leak detection, and no bubbles shall be generated within the specified test time.

a) Connect the air inlet and outlet of the overflow valve to the pipeline. The air inlet pipeline is connected to the air source. The length of the connecting pipeline between the air inlet and the air outlet is at least 1 m;

b) Before the test, the pressure at the air outlet and air inlet of the overflow valve shall be atmospheric pressure;

c) Quickly charge hydrogen to the maximum allowable working pressure of the valve. Then release the pressure to atmospheric pressure. The number of cycles is 100 times;

d) Fill the hydrogen gas in the opposite flow direction to c) to the maximum allowable working pressure of the valve. Then release the pressure to atmospheric pressure. The number of cycles is 100 times;

e) Carry out action cycle test according to the provisions of 7.10.

7.11.2 Qualification indicators Use special leak detection fluid for leak detection, and no bubbles shall be generated within the specified test time.

8 Control valves

8.1 Extreme temperature hydrogen cycle test Carry out extreme temperature hydrogen cycle test in accordance with the provisions of 5.3.

8.2 External leakage test Carry out external leakage test according to the test method specified in 5.4.1.2. The test results shall comply with the requirements specified in 5.4.2.

8.3 Overpressure hydrogen cycle test Carry out overpressure hydrogen cycle test in accordance with the provisions of 5.5.

8.4 Hydrostatic test Carry out hydrostatic test in accordance with the provisions of 5.6.

Where, t - the resting time, in hours (h);

dmax - the maximum diameter of the break away coupling, in millimeters (mm).

9.2.2 Qualification indicators Use special leak detection fluid to detect leaks, and no bubbles shall be generated within the specified test time.

9.3 Overpressure hydrogen cycle test Carry out overpressure hydrogen cycle test in accordance with the provisions of 5.5.

9.4 Hydrostatic test Carry out hydrostatic test in accordance with the provisions of 5.6.

9.5 Hydraulic strength test

9.5.1 Test method Carry out the hydraulic strength test of the breakaway valve in accordance with the following requirements:

a) For the assembled break away coupling: After purging the break away coupling with nitrogen, seal the outlet of the break away coupling. Apply a hydraulic pressure of 2.4 times the maximum allowable working pressure of the valve to its inlet at normal temperature, and maintain the pressure for 3 min;

b) For the input side and output side of the break away coupling: The relief hole on the output side of the break away coupling shall be blocked. After purging the input and output sides of the break away coupling with nitrogen, apply a hydraulic pressure of 2.4 times the maximum allowable working pressure of the valve to the input and output sides at normal temperature, and maintain the pressure for 5 min.

9.5.2 Qualification indicators The break away coupling shall not break. When performing a hydraulic strength test on the assembled break away coupling, if the break away coupling separates during the pressurization process, and the pressure during separation is not less than 1.5 times the maximum allowable working pressure of the valve, a clamp shall be used to secure the input and output sides of the break away coupling. Repeat the hydraulic strength test.

In addition, the assembled break away coupling shall not leak when the test pressure is gas to not less than 0.8 times the maximum allowable working pressure of the valve.

Allow the manual valve to reach maximum flow and then close the valve. Afterwards, conduct a leakage test on the manual valve according to the test method specified in 5.4.1.

10.9.2 Qualification indicators The manual valve shall be able to be completely closed and shall meet the requirements specified in 5.4.2.

10.10 Open and close cycle test

10.10.1 Test method At the test temperatures of not higher than -40 degrees C and not lower than 85 degrees C, follow the following steps:

a) Connect the air inlet of the manual valve to the air source, and the air outlet to a ventilated place;

b) Close the manual valve;

c) Fill the hydrogen gas to the maximum allowable working pressure of the valve.

Afterwards, open the valve to relieve pressure to atmospheric pressure;

d) Repeat operations b) and c) 150 times;

e) Carry out leakage test according to the test method specified in 5.4.1.

10.10.2 Qualification indicators Manual valves shall be free from leakage and rupture.

10.11 Torque cycle test

10.11.1 Test method Secure the manual valve with a clamp. Use a torque wrench or other device capable of setting torque to apply 1.5 times the design maximum torque to the closed manual valve to fully open it. The number of cycles is 20 times. Afterwards, perform a leakage test on the manual valve according to the test method specified in 5.4.1.

NOTE: This test does not apply to manual ball valves.

10.11.2 Qualification indicators The manual valve shall not be deformed or broken, and shall meet the requirements

......
This preview omits tables, figures, formulas and parts of the technical clauses. The complete document — all pages — is available in the English PDF.

Referenced standards

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