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GB/T 47007-2026Energy efficiency test and evaluation rules for plate heat exchangers (English PDF)

板式热交换器能效测试与评价规则

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Issued by

SAMR; SAC

Level / Type

National · Recommended

Issue date

January 28, 2026

Implementation date

January 28, 2026

Scope

GB/T 47007-2026 is the English-translated version of 板式热交换器能效测试与评价规则.

GB/T 47007-2026 establishes the test system and the procedure for measuring the energy efficiency of plate heat exchangers under water-to-water conditions, and specifies the test platform, the measurement items, data processing, the energy efficiency calculation and evaluation and the report.

It applies to detachable plate heat exchangers, including semi-welded ones, and to brazed ones working with liquid on both sides.

It defines the energy efficiency index (EEI), asks for a dedicated rig fed with clean fresh water in counter-flow without phase change, and sets instrument accuracy at level 0.2 for pressure, level 0.5 for flow and 0.5 degrees Celsius for temperature.

Test units must have at least 17 plates, and the corrugation, geometry, spacing, thickness and flow parameters that force a fresh test are listed. It was issued on 28 January 2026 and has applied since 28 January 2026.

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Document preview — GB/T 47007-2026

National Standard of the People's Republic of China

ICS
27.010
Classification
J 75

Issued by: State Administration for Market Regulation; Standardization Administration of the PRC

Contents

  • Foreword3
  • 1 Scope4
  • 2 Normative references4
  • 3 Terms and definitions4
  • 4 Symbols and units5
  • 5 Basic requirements6
  • 6 Test product preparation7
  • 7 Performance testing8
  • 8 Energy efficiency evaluation11
  • 9 Testing and evaluation report13
  • Annex A (informative) Examples for energy efficiency testing and evaluation report15

1 Scope

This document establishes the test system and procedures for energy efficiency testing of plate heat exchangers under water-to-water operating conditions. It specifies the requirements for the test platform, measurement items, data processing, energy efficiency calculation and evaluation, as well as the test and evaluation report for such testing.

This document applies to the energy efficiency testing and evaluation of detachable plate heat exchangers (including semi-welded detachable plate heat exchangers) and brazed plate heat exchangers operating under liquid-liquid conditions.

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 27698.1, Test methods for the performance of heat exchangers and heat exchange elements -- Part 1: General requirements

GB/T 27698.2, Test methods for the performance of heat exchangers and heat exchange elements -- Part 2: Heat exchangers

GB/T 27698.3, Test methods for the performance of heat exchangers and heat exchange elements -- Part 3: Heat exchanger elements

GB/T 27698.4, Test methods for the performance of heat exchangers and heat exchange elements -- Part 4: Measurement of noise from air-cooled heat exchangers

NB/T 47004.1, Plate heat exchangers -- Part 1: Plate-and-frame heat exchangers

NB/T 47045, Brazed plate heat exchanger

3 Terms and definitions

For the purposes of this document, the terms and definitions defined in GB/T 27698.1~27698.4, NB/T 47004.1, NB/T 47045 as well as the followings apply.

3.1 Energy efficiency index

Parameters used to assess the energy efficiency of plate heat exchangers, determined by integrating their heat transfer and flow resistance characteristics - and based on the First Law of Thermodynamics - through methods such as the mathematical and statistical analysis of test data.

NOTE: The English abbreviation and parameter symbol are EEI.

4 Symbols and units

The symbols and units listed in Table 1 are applicable to this document.

5 Basic requirements

5.1 Test platform

5.1.1 The platform utilized for conducting energy efficiency tests on plate heat exchangers shall be equipped with a dedicated test site and the requisite supporting facilities, including water, electricity, heat sources, and cold sources. The test system shall comply with the requirements specified in GB/T 27698.1. The test fluid shall consist of clean fresh water, and the testing shall be conducted under water-to-water counter-flow conditions without phase change. The flow rates of both the cold and hot fluids within the test system shall fall within the specified flow rate range required for testing the plate heat exchanger. The test conditions shall be adjustable and capable of being maintained in a steady state. Furthermore, the test data shall be accurate, reliable, and capable of being automatically acquired and stored.

5.1.2 The accuracy of pressure and differential pressure measuring instruments shall be no lower than level 0.2. The accuracy of flow measuring instruments shall be no lower than level 0.5. The permissible error of fluid temperature measuring instruments shall not exceed ±0.5°C. Measuring instruments shall be used within the validity period of their verification (calibration).

5.2 Testing and evaluation institution

Organizations engaged in the energy efficiency testing and evaluation of plate heat exchangers shall possess the capability to verify the structural parameters of the heat exchanger plates, as well as the capability to conduct energy efficiency testing and evaluation. They shall be equipped with the necessary instrumentation, equipment, and personnel to meet the requirements for such testing and evaluation, strictly control the quality of the energy efficiency tests, and assume responsibility for the accuracy, impartiality, and traceability of the test results.

6 Test product preparation

6.1 The test product shall comply with the requirements of the applicable product standards. To ensure that the test results accurately reflect the actual operating characteristics of the heat exchanger, the number of plates in the plate heat exchanger under test shall be no fewer than 17.

6.2 When conducting energy efficiency testing and evaluation for plate heat exchangers, the assessment shall include, at a minimum, the product model and the following parameters.

a) Plate corrugation parameters (corrugation angle, corrugation depth, corrugation pitch, mixing angle, and mixing ratio);

b) Plate geometric dimensions [length, width, port diameter (or equivalent port diameter), and longitudinal and transverse center distances];

c) Single plate heat transfer area;

d) Plate spacing;

e) Plate thickness;

f) Flow configuration (single-pass flow or diagonal flow);

g) Plate material;

h) Flow channel cross-sectional area;

i) Number of plates;

j) Flow arrangement.

6.3 Whenever the product model or any of the parameters specified in 6.2 a)~f) changes, energy efficiency testing and evaluation shall be conducted anew.

7 Performance testing

7.1 Test methods

7.1.1 Measurement parameters

During testing, at least the following parameters shall be measured.

a) Volumetric flow rate or mass flow rate of the cold and hot fluids;

b) Inlet and outlet temperatures of the cold and hot fluids;

c) Inlet pressure of the cold and hot fluids, and the pressure drop between the inlet and outlet.

7.1.2 Test procedure

The inlet temperatures of the hot and cold fluids shall be adjusted - using a heater or cooler, respectively - to 60°C ±0.5°C and 30°C ±0.5°C. Once the flow and heat transfer have stabilized, the test shall be conducted under the following conditions.

a) For the first set of operating conditions, the fluid velocities on both sides shall vary uniformly. The velocity variation range shall be between 0.1 m·s-1~0.9 m·s-1, with increments of 0.1 m·s-1.The number of distinct velocity conditions tested shall be no fewer than seven, and the specific test velocities shall be mutually agreed upon by the supplier and the purchaser.

b) For the second set of operating conditions, the flow velocity of the fluid on one side (either the hot or cold side) is held constant; this fixed point shall be set at 0.5 m·s-1.The flow velocity of the fluid on the other side shall be varied within the range of 0.1 m·s-1~0.9 m·s-1, with increments of 0.1 m·s-1.The number of distinct flow velocity conditions tested shall be no fewer than seven, and the specific test velocities shall be mutually agreed upon by the supplier and the purchaser.

c) Measurements shall be repeated at least 3 times for each test condition, with an […]

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This preview omits tables, figures, formulas and parts of the technical clauses. The complete document — 15 pages — is available in the English PDF.

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