GB/T 34476-2017 in English
VALIDMethods of determination and calculation of heat balance in converter
- Issued on:2017-10-14
- Implemented on:2018-07-01
- File Format:PDF
- Delivery:Via email within 5 business days
$359.00
《GB/T 34476-2017转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
| Test dimension | Benchmark requirements | Measurement method | Calculation unit |
|---|---|---|---|
| Temperature benchmark | Average temperature of workshop environment | Infrared thermometer/thermocouple | ℃ |
| System boundary | Furnace mouth or gas recovery system | Boundary delineation method | - |
| Test cycle | 3 smeltings within 8 hours | Complete smelting cycle record | min |
Key Test Technical Points
Material Balance Calculation Specifications
The calcium-magnesium balance method is used to calculate the amount of furnace lining erosion, and the oxidation weight of molten iron elements is calculated according to the formula:
Gi = (G1+G3)wi - G1''wi'
The relative error is allowed to be ≤5%, and 12 items of income materials and 8 items of expenditure materials must be included.
Heat balance calculation system
| Heat income item | Calculation formula | Typical proportion |
|---|---|---|
| Physical heat of molten iron | Q1=G1(C1t1-C1ete+217.44) | 45-55% |
| Element oxidation heat | Oxidation reaction containing C/Si/Mn/P | 30-40% |
| Slag reaction heat | 2 103.34GSi×60/28 | 5-8% |
Implementation suggestions
- Test preparation phase: Equipment maintenance and instrument calibration need to be completed, and preliminary tests need to be carried out to verify the feasibility of the solution
- Data collection specifications: Furnace gas composition is sampled every 1-2 minutes, and molten steel temperature needs to be measured at multiple points using fast micro-thermocouples
- Error control: It is recommended to use the cross-validation method, combining DCS system data with manual measurement results
Technology evolution analysis
This standard extends the boundary of the heat balance system to the gas recovery system for the first time and introduces the calculation of the heat of the vaporization flue steam (Q14'), reflecting the development of modern converter waste heat utilization technology.

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