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GB/T 4213-2024 PDF English

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GB/T 4213-2024: Pneumatic control valves
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GB/T 4213: Evolution and historical versions

Standard IDContents [version]USDSTEP2[PDF] deliveryName of Chinese StandardStatus
GB/T 4213-2024English515 Add to Cart 0-9 seconds. Auto-delivery Pneumatic control valves Valid
GB/T 4213-2008English85 Add to Cart 0-9 seconds. Auto-delivery Pneumatic Industrial Process Control Valves Valid
GB/T 4213-1992English559 Add to Cart 4 days Pneumatic industrial process control valves Obsolete

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GB/T 17213.16   GB/T 17213.18   GB/T 17213.9   

GB/T 4213-2024: Pneumatic control valves

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GB NATIONAL STANDARD OF THE PEOPLE’S REPUBLIC OF CHINA ICS 23.060.01 CCS N 16 Replacing GB/T 4213-2008 Pneumatic Control Valves Issued on: DECEMBER 31, 2024 Implemented on: JULY 1, 2025 Issued by. State Administration for Market Regulation; Standardization Administration of the People’s Republic of China.

Table of Contents

Foreword... 4 1 Scope... 7 2 Normative References... 7 3 Terms and Definitions... 7 4 Product Classification and General Requirements... 8 5 Technical Requirements... 11 5.1 Compressive Strength... 11 6 Test methods... 20 7 Inspection Rules... 29 7.1 Exit-factory test... 29 7.2 Type Test... 29 Appendix A (informative) Correlation of Nominal Diameters... 33 Appendix B (informative) Examples of Valve Seat Leakage Calculation... 34

1 Scope

This document specifies the product classification and general requirements, technical requirements, test methods, inspection rules, marking, packaging and storage of pneumatic control valves for industrial process control systems. This document applies to various types of pneumatic control valves consisting of pneumatic actuators and valves (hereinafter referred to as “control valves”). This document also applies to stand-alone pneumatic actuators and valve assemblies. Control valves with specific working conditions in countries with radioactive working environments or other hazardous working environments may refer to this document for implementation.

2 Normative References

The contents of the following documents constitute indispensable clauses of this document through the normative references in the text. In terms of references with a specified date, only versions with a specified date are applicable to this document. In terms of references without a specified date, the latest version (including all the modifications) is applicable to this document. GB/T 12224 General Requirements for Industrial Steel Valves GB/T 13384 General Specifications for Packing of Mechanical and Electrical Product GB/T 17213 (all parts) Industrial-process Control Valves GB/T 17213.2-2017 Industrial-process Control Valves - Part 2-1.Flow Capacity - Sizing Equations for Fluid Flow under Installed Conditions GB/T 26640 Specification for Minimal Thickness of the Shell of Valves GB/T 26815 Terminologies for Industrial-process Measurement and Control Instruments - Terms of Final Controlling Elements

3 Terms and Definitions

The terms and definitions defined in GB/T 17213 (all parts) and GB/T 26815 are applicable to this document.

4 Product Classification and General Requirements

4.1 Classification by Control Valve Functions In accordance with the functions of control valves, they can be classified into. a) Adjustable type; b) Switching type. 4.2 Classification by Control Valve Motion Mode In accordance with the control valve motion mode, they can be classified into. a) Linear motion; b) Rotary motion. 4.3 Classification by Control Valve Action Mode In accordance with the control valve action mode, they can be classified into. a) Air-to-close type; b) Air-to-open type. 4.4 Classification by Control Valve Actuator Type In accordance with the type of control valve actuator, they can be classified into. a) Pneumatic diaphragm type; b) Pneumatic piston type. NOTE 1.in accordance with their structure, pneumatic actuators are classified into. a) Pneumatic diaphragm actuator; b) Pneumatic piston actuator. NOTE 2.in accordance with their output mode, pneumatic actuators are classified into. a) Linear motion pneumatic actuator; b) Rotary motion pneumatic actuator. 4.5 Nominal diameter (DN or NPS) An alphanumeric designation consisting of the letters DN or NPS, followed by a dimensionless number. The value following the nominal diameter DN of the control valve shall be selected from the following preferred values. 6, 8, 10, 15, 20, 25, 32, 40, 50, 65, 80, 100, 125, 150, 200, 250, 300, 350, 400, 450, 500, etc. The value following the nominal diameter NPS of the control valve shall be selected from the following preferred values. 4.6 Nominal Pressure (PN series) or Pressure Class (Class series) An alphanumeric designation consisting of the letters PN or Class, followed by a dimensionless number. The value following the nominal pressure (PN) of the control valve shall be selected from the following preferred values. 2.5, 6, 10, 16, 25, 40, 63, 100, 160, 250, 320, 400, etc. The value following the pressure class (Class) of the control valve shall be selected from the following preferred values. 150, 300, 400, 600, 900, 1,500, 2,500, etc. NOTE 1.the letters PN or Class have no meaning except in conjunction with the relevant piping element standards. NOTE 2.unless otherwise specified in the relevant standards, dimensionless numbers do not represent measured values and are not used in calculations. NOTE 3.the maximum allowable working pressure depends on the PN value or Class value, materials, element design and working temperature, etc. 4.7 Input Signal The input signal type and range are determined by the manufacturer or as required by the order contract. 4.8 Gas Source 4.8.1 Maximum gas source pressure The maximum values of the gas source pressure are as follows. a) Pneumatic diaphragm control valve. 600 kPa; b) Pneumatic piston control valve. 1,000 kPa. NOTE. special gas source pressure is allowed to be used upon agreement between the user (buyer) and the manufacturer. 4.8.2 Humidity of gas source The dew point of the gas source at operating pressure shall be at least 10 °C lower than the working environment temperature of the control valve. 4.8.3 Quality of gas source The quality requirements of the gas source are as follows. a) The gas source shall be free of obvious oils (liquid oil, suspended oil, oil vapor) and other liquids, the oil concentration shall not exceed 5 mg/m3, and the liquid water concentration shall not exceed 10 g/m3; b) The gas source should not contain corrosive gases, vapor and solvents; c) Explosive gas shall not be used as the gas source; d) The solid particle concentration in the gas source of the control valve with a positioner shall not exceed 5 mg/m3, and the particle diameter shall not exceed 5 m. 4.9 Normal Working Conditions Unless otherwise specified, the control valve shall be able to normally operate in the following atmospheric conditions. a) Temperature. 25 C ~ +55 C, 40 C ~ +70 C or 30 C ~ +80 C; special working temperature ranges may be used, but the temperature value shall be an integral multiple of 5 C. b) Relative humidity. 5% ~ 100%. 4.10 Signal Pipe Thread

5 Technical Requirements

5.1 Compressive Strength The control valve shall be subjected to the compressive strength test using room temperature water as the medium at a test pressure of 1.5 times the nominal pressure or 1.5 times the maximum allowable working pressure at 38 °C. During the test, there shall be no visible leakage from the valve body. If agreed upon by the user (buyer) and the manufacturer, the test may be carried out on the pressure-bearing parts, but the assembled control valve shall also be subjected to a gas test at a pressure not exceeding 0.6 MPa, and the valve body shall not have any visible leakage. 5.2 Sealing of Packing Boxes and Other Joints Procedure A. the test medium is room temperature water. The packing boxes and other joints of the control valve shall ensure that there is no leakage at a test pressure of 1.1 times the maximum allowable working pressure at 38 C. The test pressure value of special-purpose control valves shall be agreed upon by the manufacturer and the user (buyer). Procedure B. if agreed upon by the user (buyer) and the manufacturer, Procedure B may be adopted. The test medium is gas. The packing boxes and other joints of the control valve shall ensure that there is no leakage under the test pressure of 0.35 MPa. When the maximum allowable working pressure of the valve is lower than 0.35 MPa, the test pressure is the maximum allowable working pressure. 5.3 Leakage 5.3.1 The leakage of the control valve under the specified test conditions shall comply with the provisions of Table 1. 5.3.2 The leakage level I of the control valve is required to be determined by the user (buyer) and the manufacturer. However, the leakage level of the control valve with a single-seat valve structure shall not be lower than Level IV, and the leakage level of the control valve with a double-seat valve structure shall not be lower than Level II. Level VI is applicable to control valves with elastic sealing valve seats. 5.3.3 When the leakage is greater than 5  103 the rated capacity of the valve, it shall be ensured by the structural design, and the product can be exempted from testing. 5.3.4 Leakage shall be specified by the following codes. 5.3.5 When calculating and determining the allowable value of leakage, the rated capacity of the control valve shall be calculated in accordance with the method specified in GB/T 17213.2- 2017 (see Table 3). 5.5 Intrinsic Error The intrinsic error of the control valve shall not exceed the intrinsic error limit specified in Table 4.The intrinsic error is expressed as a percentage of the rated stroke. The switching type control valves are exempted from testing. 5.6 Hysteresis Plus Dead Band The hysteresis plus dead band of the control valve shall not exceed the hysteresis plus deadband limit specified in Table 4.The hysteresis plus dead band is expressed as a percentage of the rated stroke. Control valves without positioners and the switching type control valves are exempted from testing. 5.7 Start and End Point Deviation When the input signal in the pneumatic actuator is at the upper and lower limit values, the end point deviation of the air-to-close control valves and the start point deviation of the air-to-open control valves shall not exceed the provisions of Table 4.The start and end point deviation is expressed as a percentage of the rated stroke. The switching type control valves are exempted from testing. 5.8 Dead Band The dead band of the control valve shall not exceed the dead band limit specified in Table 4. The dead band is expressed as a percentage of the input signal range. The switching type control valves are exempted from testing. 5.9 Rated Stroke Deviation The rated stroke deviation of the air-to-close control valves shall comply with the provisions of Table 4.The rated stroke deviation of the control valves is expressed as a percentage of the rated stroke.

6 Test methods

6.1 Test Conditions and Instructions 6.1.1 Reference working conditions Except for surface quality inspection and other provisions in the clauses, the test shall be carried out under the following reference conditions. 6.1.2 Recommended atmospheric conditions Tests which are not necessary or impossible to be carried out under reference working conditions should be carried out under the following atmospheric conditions. 6.1.3 Recommended test sequence The recommended test sequence is specified in Table 7. 6.3 Sealing of Packing Boxes and Other Joints Procedure A. the test medium is room temperature water (which may contain water-soluble oil or rust inhibitor), which is injected into the valve body of the control valve in the specified inlet direction, and the other end is closed. The test pressure is 1.1 times the maximum allowable working pressure at 38 °C. At the same time, make the valve stem (shaft) reciprocate 1 ~ 3 times per minute for a duration of not less than 3 minutes. Observe the control valve packing NOTE. for nominal diameters or nominal pressures (pressure classes) not listed, the test time shall be the higher-class value. 6.4 Leakage 6.4.1 The test medium shall be clean gas or room temperature water. 6.4.2 Test medium pressure. 6.4.3 Test gas source signal pressure. the pneumatic actuator shall be adjusted to the specified working state. In Test Procedure 1, the input gas source pressure of the air-to-open control valve actuator shall be zero; the input gas source pressure of the air-to-close control valve actuator shall not exceed 1.2 times the upper limit of the spring pressure range; the input gas source pressure of the switching type control valve actuator shall be the rated gas source pressure. In Test Procedure 2, the gas source pressure of the actuator shall be the same as in Test Procedure 1. When testing a valve that has not yet been equipped with a pneumatic actuator, a thrust device shall be added to the test, and the force applied shall not exceed the maximum valve seat sealing force specified by the manufacturer. 6.4.4 Test medium flow direction. the test medium shall be injected into the valve in accordance with the specified direction. The control valve outlet shall be directly connected to the atmosphere or connected to a low-pressure head loss measurement device whose outlet is connected to the atmosphere. Only after it is confirmed that the valve and all downstream connecting pipelines are completely filled with the medium and the leakage is stable can the leakage be measured. 6.4.5 Measurement error. the measurement error of leakage and pressure shall be less than 10% of the reading value. Appendix B gives examples of leakage calculation. 6.5 Sealing of Air Chamber Introduce a gas source with the rated pressure specified in the design into the sealed air chamber, cut off the gas source, and observe the pressure drop in the diaphragm air chamber or each air chamber in the cylinder within 5 minutes. For actuator air chambers with no possibility of internal leakage, soapy water can be applied to the seals of the air chamber to check for leakage. For small-sized actuators, they can also be directly immersed in water to check for leakage. 6.6 Intrinsic error When conducting the test of intrinsic error, it shall be ensured that the packing is compacted and satisfies the requirements of 5.2. Smoothly input the specified input signal into the actuator air chamber (or positioner) in the increasing or decreasing direction and measure the stroke value corresponding to each point. In accordance with Formula (1), calculate the error at each point between the actual “signalstroke” relations and the theoretical relations. The maximum value is the intrinsic error. 6.7 Hysteresis Plus Dead Band When conducting the test of hysteresis plus dead band, it shall be ensured that the packing is compacted and satisfies the requirements of 5.2. The test procedures are the same as that in 6.6.The ratio of the absolute value of the maximum difference between the positive and negative strokes measured on the same input signal to the rated stroke is the hysteresis plus dead band. 6.8 Start and End Point Deviation When conducting the test of start and end point deviation, it shall be ensured that the packing is compacted and satisfies the requirements of 5.2. The test procedures are the same as that in 6.6.In accordance with Formula (1), calculate the start and end point deviation. 6.9 Dead Band When conducting the test of dead band, it shall be ensured that the packing is compacted and satisfies the requirements of 5.2. a) Starting from 0% or 100% of the control valve input signal, change the input signal (by 25%, 50% and 75% of the input signal range), until the valve stem (shaft) stroke stabilizes. b) In the same direction, slowly change the input signal, until a perceptible change in stroke is observed, and record the input signal value (A) at this time. c) Continue to slowly change the input signal in the opposite direction, until a perceptible change in stroke is observed, and record the input signal value (B) at this time. d) In accordance with the input signal values recorded in b) and c), and Formula (2), calculate the dead band. The test shall be respectively performed at three points (25%, 50% and 75% of the input signal range). 6.10 Rated Stroke Deviation When conducting the rated stroke deviation test, it shall be ensured that the packing is compacted and satisfies the requirements of 5.2. Smoothly input the input signal of the rated range into the actuator air chamber (or positioner) in the increasing direction, respectively record the actual stroke of the control valve in the fully closed position and the fully open position, and in accordance with Formula (3), calculate the rated stroke deviation. 7.1 Exit-factory test Each product shall pass the inspection by the manufacturer’s quality inspection department and obtain an issued product certificate before it is allowed to exit the factory. When the complete control valve product, actuator or valve body separately exits the factory, the exit-factory test items are shown in Table 11. 7.2 Type Test Type test shall be carried out under one of the following circumstances. a) When conducting trial production and appraisal of new products or old products transferred to other factories for production; b) For products in normal production, when there are major changes in structure, materials or processes that may affect product performance; c) When the production has been suspended for more than one year and resumed; d) When the national quality supervision institution or other administrative department proposes a request for type test; e) When the user (buyer) requests (for a fee) a type test. The type test items are shown in Table 11.During the validity period of the complete product type test, the actuator or valve body can be exempted from the type test when it separately exits the factory. 8 Marking, Packaging and Storage 8.1 Marking 8.1.1 Valve body marking NOTE. M stands for mandatory and S stands for supplementary. The valve body marking should include but not be limited to the following contents. For valve bodies smaller than DN50 (NPS2) and other valve bodies without sufficient space, the marking is allowed to be installed on the valve body or valve cover in the form of metal marking plates. a) Manufacturer’s name or trademark (M); b) Nominal pressure (M); c) Nominal diameter (M); d) Medium flow direction (except where no flow direction requirement is specified) (M); e) Valve body material (M); f) Valve body material batch number (casting furnace number or forging batch number) (M); g) Product production serial number (S); h) Thread or flange marking (S). 8.1.2 Nameplate marking A nameplate shall be fixed at an appropriate position on the pneumatic actuator and shall at least indicate. a) Manufacturer’s name or trademark (M); b) Product model (M); c) Nominal diameter (M); d) Nominal pressure (M); e) Working temperature (only mandatory in certain special cases when it is not possible to mark the nominal pressure and flange) (S/M); f) Input signal range (S); g) Rated stroke (S); h) Rated flow coefficient (S); i) Flow characteristics (not required for the switching type) (S); j) Valve body material (M); k) Design number (may also be marked on a separate nameplate) (S); l) Product manufacturing number (M); m) Year and month of product manufacturing (S). For small-sized control valves, when due to the limitation of nameplate size, all markings cannot be accommodated, some markings may be omitted, but items a), b), h), l), and m) shall be marked on the nameplate. Other mandatory markings. c), d) and j) shall be marked on the valve body. 8.2 Packaging Before packaging, all uncoated and rust-prone external machined surfaces of the control valve shall be coated with anti-rust oil or other anti-rust measures shall be taken. The valve inlet and outlet ports and the threaded holes of the signal transmission pipe shall be sealed and properly packaged in accordance with GB/T 13384 to ensure that they are not damaged during transportation. The technical documents packed with the control valve are. a) Product exit-factory certification documents; b) Product instruction manual; c) Packing list; d) Other documents required by the user (buyer). 8.3 Storage The control valves shall be stored in a room with an air temperature of 5 C ~ 40 C and a relative humidity of not greater than 90%. The air shall not contain harmful impurities that may corrode the control valves. ......
Source: Above contents are excerpted from the full-copy PDF -- translated/reviewed by: www.ChineseStandard.net / Wayne Zheng et al.


      

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