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波纹管管外冷凝传热系数计算模型 被引量:1

Calculation Model of the Condensation Heat Transfer Coefficients Outside Bellows
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摘要 推导了波纹管表面张力液膜滞流冷凝传热系数计算式,引入重力修正系数校正重力的影响,并通过实验确定了重力修正系数,得到波纹管冷凝传热系数计模型。计算值与实验结果较为一致,误差小于6%。计算模型物理意义较为明确,可以清楚地分析波纹管强化传热的主要因素。研究表明,传热系数的提高是由表面张力和波纹表面结构使波纹表面冷凝负荷降低这两方面决定。 The formula of the condensation heat transfer coefficient of the fluid film laminar flow of the surface tension of the bellows was deduced. The gravity correction coefficient was introduced to modify the influence of gravity, the gravity correction coefficient was determined with experiments, and the calculation model of the condensation heat transfer coefficients of the bellows was obtained. The calculated value basically agreed with the experimental value, the error was less than 6% , the physical meaning of the calculation model was definite, the major factors of the reinforced heat transfer of the bellows could be clearly analyzed. The investigation shows that the increase of the heat transfer coefficients was determined with the reasons that the surface tension was higher than the gravity and the surface structure of corrugation decreased the condensation load of the corrugation surface.
出处 《化工机械》 CAS 2007年第6期313-316,共4页 Chemical Engineering & Machinery
关键词 波纹管 冷凝传热 表面张力 传热系数 Bellows, Condensation Heat Transfer, Surface Tension, Heat Transfer Coefficient
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参考文献8

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二级参考文献2

  • 1西安交通大学热工教研室.在换热器传热试验中用Wilson图解法确定给热系数[J].化工与通用机械,1974,7:24-35.
  • 2上海交通大学热工教研组.用Wilson图解法确定给热系数时应注意的问题[J].化工与通用机械,1978,7:19-26.

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