Simplified models for direct and indirect contact cooling towers and evaporative condensers

J. Lebrun, C. A. Silva, F. Trebilcock, E. Winandy
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引用次数: 33

Abstract

This paper presents a simplified method of analysing the combined heat and mass transfer phenomena in direct and indirect contact cooling towers and evaporative condensers. The theoretical basis of the model is Merkel's theory. The cooling towers, evaporative condensers and fluid coolers are considered as members of a classical heat exchanger family, working in wet regime. Here, the air side heat and mass transfer processes are governed by the same basic process. This paper shows that a `unified' theoretical treatment may be applied to all three evaporative exchangers. The key difference in the theory for each type relates to these exchangers unique characteristic, the global heat transfer coefcient AU, or the corresponding thermal resistances of the fluids. Specific correlations for the calculation of AU or of the equivalent thermal resistances, considering the influence of the water and air flow rates entering the exchangers, are discussed. An example for each case is shown, illustrating the validation of the models with catalogue data.
直接和间接接触冷却塔和蒸发式冷凝器的简化模型
本文提出了一种分析直接接触和间接接触冷却塔和蒸发式冷凝器传热传质联合现象的简化方法。该模型的理论基础是默克尔理论。冷却塔,蒸发式冷凝器和流体冷却器被认为是一个经典的热交换器家族的成员,在湿状态下工作。在这里,空气侧的传热和传质过程由相同的基本过程控制。本文表明,一个“统一”的理论处理可以适用于所有三个蒸发交换器。每种类型的理论的关键区别在于这些交换器的独特特性,即整体传热系数AU,或流体的相应热阻。考虑到进入交换器的水和空气流速的影响,讨论了计算AU或等效热阻的具体关系。给出了每种情况的一个示例,说明了使用目录数据验证模型。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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