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炉膛高度对步进式轧钢加热炉性能的影响

Effect of Furnace Height on Performance of Walking-beam Reheating Furnace
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摘要 以能量平衡为基础,采用辐射段法模型建立了炉气段、炉围段和钢坯表面段的能量方程组,通过钢坯表面的热流与内部导热方程耦合求解,其中炉气和炉围的温度场采用主变量修正法求解,钢坯温度场采用隐式有限差分求解,与现场实测板坯温度对比验证模型的准确性,分析了上炉膛各段高度对钢坯温度场及排烟温度的影响.结果表明,预热段高度在0.5~0.9 m,高度每增加0.2 m,钢坯出炉时上表面温度升高约2.8℃,排烟温度降低约10℃;加热一段高度在0.9~1.9 m,高度每增加0.2 m,钢坯出炉时上表面温度平均增加2.5℃,排烟温度平均降低8.5℃;加热二段和均热段高度变化对钢坯出炉时表面温度及排烟温度影响不大.合理确定预热段和加热一段高度有利于钢坯加热并节省燃料消耗. Based on energy balance, energy-balance equations for gas volume zones, furnace surface zones and slab surface zones were set up by radiation zonal method, by the slab surface heat flow and internal thermal equations coupling solution. And the temperature profiles of gas volume zones and furnace surface zones were obtained by using the main variable correction method, the slabs temperature profiles by finite difference method. The correctness of the model was verified by comparing the slab temperature with the actual situation. The influence of the height of the upper furnace on the temperature field and the exhaust gas temperature of the slab were analyzed. The results showed that for the preheating section height of 0.5~0.9 m, with the height of each increase of 0.2 m, the upper surface temperature before the slab released increased by about 2.8℃, the exhaust temperature decreased by about 10℃. For the first heating section of height of 0.9~1.9 m, with the height of each increase of 0.2 m, the upper surface temperature before the slab released increased by about 2.5℃, the average exhaust gas temperature decreased by 8.5℃. The influence of the height on the temperature of the second heating section and the soaking section were not significant. It can be seen that it was reasonable to determine the height of the preheating section and the heating section to facilitate the heating of the slab and fuel consumption saving.
作者 李浩 戴方钦 丁翠娇 郭悦 Hao LI;Fangqin DAI;Cuijiao DING;Yue GUO(Key Lab for Ferrous Metallurgy and Resources, Utilization of Ministry of Education, Wuhan University of Science and Technology, Wuhan, Hubei 430081, China;Baowu Iron and Steel Group, Wuhan Branch of Baosteel Central Research Institute, Wuhan, Hubei 430080, China)
出处 《过程工程学报》 CAS CSCD 北大核心 2018年第3期551-556,共6页 The Chinese Journal of Process Engineering
关键词 炉膛高度 步进式轧钢加热炉 段法 水冷梁 钢坯温度 排烟温度 furnace height walking-beam reheating furnace zone method water-cooled beam slab temperature exhaust temperature
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  • 1葛永斌,田振夫,吴文权.含源项非定常对流扩散方程的高精度紧致隐式差分方法[J].水动力学研究与进展(A辑),2006,21(5):619-625. 被引量:25
  • 2Sika J. Evaluation of Direct-Exchange Areas for a Cylindrical Enclosure[J]. Journal of Heat Transfer, 1991, 113 (11): 1040.
  • 3Selcuk N, Siddall G R. Two-Flux Spherical Harmonic Modeling of Two Dimensional Radiative Transfer in Furnace[J]. Int J of Heat and Mass Transfer, 1976,19:313.
  • 4Kim T K, Lee H S. Radiative Transfer in Two-Dimensional Anisotropie Scattering Media with Collimated Incidence[J].J of Quantitative Spectroscopy and Radiative Transfer, 1989,42 (3):225.
  • 5Chai J C, Lee tt S, Patankar S V. Finite Volume Method for Radiative Heat Transfer[J]. J of Thermophysics and Heat Transfer,1994,8(3) :419.
  • 6Kim S H, Huh K Y. A New Angular Discretization Scheme of the Finite Volume Method for 3-D Radiative Heat Transfer in Absorbing, Emitting and Anistropically Scattering Media[J]. Int J of Heat and Mass Transfer,2000,43:1233.
  • 7Murty C V S. Evaluation of Radiation Reception Factors in a Rotory Kiln Using a Modified Monte-Carlo Seheme[J]. Int J Heat Mass Transfer, 1993,36 : 119.
  • 8Hottel H C, Cohen E S. Radiant Heat Transfer in a Gas Filled Enclosure:Allowance for Non Uniformity of Gas Temperature [J].AIChE Int J,1958,4(1):3.
  • 9Modest M F. Radiative Heat Transfer[M]. New York; McGraw- Hill Inc. ,1993:639.
  • 10陈海耿 宁宝林.段法能量平衡方程组的主变量修正解法.东北工学院学报,1986,47(2):1-1.

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