水平管束冷凝换热设计计算问题讨论 |
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引用本文: | 王银龙,;邓科,;杨明辉,;黄卫星. 水平管束冷凝换热设计计算问题讨论[J]. 化工设备与管道, 2014, 0(3): 25-29 |
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作者姓名: | 王银龙, 邓科, 杨明辉, 黄卫星 |
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作者单位: | [1]四川大学化学工程学院,成都610065; [2]东方锅炉公司技术中心,成都611731 |
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基金项目: | 国家科技重大专项子课题(2010ZX06004-013). |
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摘 要: | 针对大型水平管束冷凝换热设计计算,对水平管束膜状冷凝换热系数典型公式进行了对比分析;结合管束结构及冷凝液膜流动行为,阐明了相关公式的适用条件、计算结果差异及原因。然后通过工程实例计算对比和壳程蒸汽流动模拟进一步表明,现有相关公式因未能充分考虑冷凝加热器中蒸汽流动的多方向性及其对冷凝液膜的扰动,其换热系数计算值明显低于实际;并针对大型水平管束冷凝换热工程计算模型的完善,对进一步的研究工作提出了建议。
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关 键 词: | 换热器 水平管束 蒸汽冷凝 换热系数 |
Discussion of Calculation and Design for Heat Transfer under Condensation with Horizontal Tube Bundles |
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Affiliation: | WANG Yinlong,DENG Ke,YANG Minghui,HUANG Weixing(School of Chemical Engineering, Sichuan University, Chengdu 610065, China;Technology Center, Dongfang Boiler Co., Chengdu 611731, China) |
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Abstract: | For heat transfer design under condensation condition for large horizontal tube bundles,several typical equations used in calculating film coefficients were compared and analyzed.Combined with bundle structure and flow of condensed liquid film,the applicable conditions,differences in calculation results and causes for the creation of these differences were explained in this article.With engineering examples and simulation of steam flow in shell side,it was further shown that the heat transfer coefficient resulted from currently applied equation is apparently lower than practical value because in this equation the multi directions of steam flowing in condensation heater and disturbing effect to condensed liquid film are not taken into account.Then,with respect to the improvement of engineering heat transfer calculation model for large horizontal tube bundle condenser,the proposal for further research was presented. |
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Keywords: | heat exchanger horizontal tube bundle steam condensation heat transfer coefficient |
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