...
首页> 外文期刊>Numerical Heat Transfer, Part A. Application: An International Journal of Computation and Methodology >Forced convection laminar film condensation of downward flowing vapor on a single horizontal elliptic cylinder or a bank of elliptical tubes
【24h】

Forced convection laminar film condensation of downward flowing vapor on a single horizontal elliptic cylinder or a bank of elliptical tubes

机译:向下对流的蒸汽在单个水平椭圆圆柱或一排椭圆管上的强制对流层流膜冷凝

获取原文
获取原文并翻译 | 示例
   

获取外文期刊封面封底 >>

       

摘要

A numerical study is performed on the laminar film condensation of pure saturated vapor flowing in the direction of gravity on a single horizontal elliptic cylinder or a bank of elliptical tubes. Temperature, velocity distribution, and heat transfer coefficient of the fully developed flow are carried out with a fully implicit finite difference scheme. The equality of shear stress at the liquid-vapor interface is used as the coupling condition between the two phases. The inertia and convection term are retained in the analysis. Outside of the vapor boundary layer, the vapor phase velocity is obtained from potential flow. The method of source density distribution on the body surface is used for determination of the external vapor velocity in elliptical tube banks. The effect of inundation produced by condensate on upper ellipses is taken into account by assuming that the vapor velocity field is not affected by the condensate flow from one elliptic cylinder to another. Based on the obtained solutions of flow field, the effect of surface tension, the interaction because of the ellipse spacing, and the inundation on the heat transfer coefficient and the boundary layer separation point have been evaluated. The results of this analysis are discussed especially in function of eccentricity e (effect of the surface tension). The heat transfer in interellipse space is analyzed and compared with the theoretical and experimental results of other authors. Good agreement is shown. [References: 27]
机译:在单个水平椭圆圆柱或一排椭圆管上,对沿重力方向流动的纯饱和蒸气的层流膜冷凝进行了数值研究。完全展开的流的温度,速度分布和传热系数采用完全隐式的有限差分方案进行。液-气界面处的剪应力相等被用作两相之间的耦合条件。惯性和对流项保留在分析中。在蒸气边界层之外,从势流获得蒸气相速度。体表上的源密度分布方法用于确定椭圆形管束中的外部蒸气速度。通过假设蒸汽速度场不受冷凝水从一个椭圆形圆柱体流到另一个椭圆形圆柱体的影响,可以考虑冷凝水对上椭圆形的淹没影响。根据获得的流场解,评估了表面张力,椭圆间距引起的相互作用以及淹没对传热系数和边界层分离点的影响。特别是在偏心率e(表面张力的影响)的函数中讨论了该分析的结果。分析了椭圆间空间中的热传递,并将其与其他作者的理论和实验结果进行了比较。显示出良好的协议。 [参考:27]

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号