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heat balance test heat balance heat treatment furnace heat balance test test phaserequirements heat balance project calculation model examples sichuan peppercorns allowable leakage flows shore tanks
GB/T 33957-2017 in English

GB/T 33957-2017 in English

VALID

Methods of determination and calculation of heat balance in heat treatment furnace

  • Issued on:2017-07-12
  • Implemented on:2018-04-01
  • File Format:PDF
  • Delivery:Via email within 5 business days
Price(USD): $370.00
$359.00
Standard No: GB/T 33957-2017
Document status: VALID
Title in English: Methods of determination and calculation of heat balance in heat treatment furnace
Title in Chinese: 热处理炉热平衡测试与计算方法
Language: English
File Format: Electronic (PDF)
Delivery: Via email within 5 business days
Issued on: 2017-07-12
Implemented on: 2018-04-01
Chinese Classification: H04-Basic standards and general methods
Professional Classification: GB-National Standard
Related Keywords: heat balance test
heat balance
heat treatment furnace
heat balance test test phaserequirements
heat balance project calculation model examples
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《GB/T 33957-2017热处理炉热平衡测试与计算方法》由TC183(全国钢标准化技术委员会)归口,TC183SC2(全国钢标准化技术委员会基础分会)执行,主管部门为中国钢铁工业协会。


Introduction

Analysis of the core content of the standard

This standard systematically regulates the reference temperature setting, calorific value calculation of fuel and delimitation of test range of the heat balance test of the heat treatment furnace. The reference temperature adopts the average temperature of the environment 1m away from the furnace wall, and the calorific value of the fuel is divided into gas fuel (low calorific value of wet coal gas) and liquid fuel (low calorific value of received base).


Key processes of heat balance test

Test phaseRequirements for continuous furnacesRequirements for intermittent furnaces
Test duration≥2 times, ≥2h each timeComplete heating cycle
Stable conditions24h insulation required for shutdown and restartFurnace lining temperature must be consistent with the previous cycle
Calculation unitkJ/t (heat consumption per ton of material)

Heat balance project calculation model

Examples of typical calculation formulas

Chemical heat of fuel combustion: Q₁=B·Qdw (B is the amount of fuel used, Qdw is the low calorific value)

Physical heat loss of flue gas: Q₂'=(BbVnS-ΣV₁/Gp)(cyty-cyctc)


Key points for improving thermal efficiency

  • Furnace heat dissipation control: surface temperature monitoring point density ≥5/m²
  • Outgassing loss optimization: furnace door opening time recording is accurate to seconds
  • Error control: thermal balance allows relative error ≤±5%

Implementation suggestions

  1. Preliminary tests are required to verify the reliability of the instrument before testing
  2. Continuous furnaces should be run stably for 8 hours after process changes before testing
  3. It is recommended to use non-contact temperature measurement equipment such as infrared thermal imagers

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