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Modeling and determination of total heat exchange factor of regenerative reheating furnace based on instrumented slab trials

机译:基于仪表板试验的再生再加热炉总热交换因子的建模与测定

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摘要

Regenerative heating furnace as a high-effciency and energy-saving heating equipment is widely applied in iron and steel industry. Accurate knowledge of total heat exchange factor of regenerative heating furnace is of great signifcance to improve its on-line control performance. Therefore, determination of total heat exchange factor of regenerative reheating furnace is investigated in this work. A three-dimensional mathematical model of regenerative reheating furnace based on the analysis of heat transfer process is established. The zonal method is used to solve the temperatures of gas zone, slab surface zone and wall surface zone, in which the Monte Carlo method is used to compute the total radiant exchange areas of thermocouple to all other zones in the furnace. The total heat exchange factors of regenerative reheating furnace are determined and the effects of thermal and operational parameters, such as productivity, fuel consumption and slab hot charging temperature are analyzed. The results show that the total heat transfer factor increases with the decrease of fuel consumption or slab hot charging temperature, and increases with the increase of productivity. The present work is valuable for dynamical compensation of total heat exchange factor of the online control mathematical models in regenerative reheating furnace.
机译:再生加热炉作为高效率和节能加热设备广泛应用于钢铁工业。准确了解再生加热炉的总热交换因子是很大的意义,以改善其在线控制性能。因此,在这项工作中研究了再生再加热炉的总热交换系数的测定。建立了基于传热过程分析的再生再加热炉的三维数学模型。区间方法用于解决气体区,板式表面区和壁面区域的温度,其中蒙特卡罗方法用于将热电偶的总辐射交换区域与炉内的所有其他区域计算。分析了再生再加热炉的总热交换因子,分析了热和操作参数的影响,例如生产率,燃料消耗和板坯热充电温度。结果表明,总传热因子随燃料消耗或板坯热充电温度的降低而增加,随着生产率的增加而增加。本作本作有价值在再生再加热炉中在线控制数学模型的总热交换因子的动态补偿。

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