首页> 外文期刊>International Journal of Heat and Mass Transfer >Film condensation in presence of non-condensable gases over horizontal tubes with progressively increasing radius of curvature in the direction of gravity
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Film condensation in presence of non-condensable gases over horizontal tubes with progressively increasing radius of curvature in the direction of gravity

机译:在水平管上存在不可凝气体的情况下的膜凝结,其重力方向上的曲率半径逐渐增大

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摘要

A theoretical study is executed to investigate the simultaneous influences of reduction in heat transfer rate on account of condensation in presence of non-condensables and its augmentation by the geometry of an horizontal tube surface with increasing radius of curvature in the direction of gravity. The tube surface profile considered for the present work is an equiangular spiral described in a polar form as: R = ae~(mθ) (a and m being parametric constants). It is observed that a very small bulk concentration (even less than 1%) of the non-condensable gas reduces considerably the heat transfer coefficient. However, there is an enhancement in heat transfer coefficient for condensation over a polar tube surface, as compared to that over a circular tube surface. This enhancement in heat transfer coefficient, with an increase in the value of m (a surface profile parameter), in presence of non-condensables is more than the corresponding proportional enhancement in the same in absence of any non-condensable species.
机译:进行了理论研究,以研究在不凝性存在的情况下由于凝结而导致的传热速率降低的同时影响,以及通过水平管表面的几何形状(随着重力方向曲率半径的增加)而增加传热的影响。本工作考虑的管表面轮廓是等角螺线,以极坐标形式表示为:R = ae〜(mθ)(a和m为参数常数)。可以看出,非常小的体积浓度(甚至小于1%)的不可冷凝气体会大大降低传热系数。然而,与在圆管表面上相比,在极管表面上的冷凝的传热系数有所提高。在存在不凝性的情况下,随着m值(表面轮廓参数)的增加,传热系数的这种增强大于在不存在任何不凝性物质的情况下相应的比例增强。

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