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Experimental correlation of combined heat and mass transfer for NH{sub}3-H{sub}2O falling film absorption

机译:传热传质与NH {sub} 3-H {sub} 2O降膜吸收的实验相关性

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摘要

In this article, experimental analysis was performed for ammonia-water falling film absorption process in a plate heat exchanger with enhanced surfaces such as offset strip fin. This article examined the effects of liquid and vapor flowcharacteristics, inlet subcooling of the liquid flow and inlet concentration difference on heat and mass transfer performance. The inlet liquid concentration was selected as 5%, 10% and 15% of ammonia by mass while the inlet vapor concentration was varied from 64.7% to 79.7%. It was found that before absorption started, there was a rectification process at the top of the test section by the inlet subcooling effect. Water desorption phenomenon was found near the bottom of the test section. It was found that the lower inlet liquid temperature and the higher inlet vapor temperature, the higher Nusselt and Sherwood numbers are obtained. Nusselt and Sherwood number correlations were developed as functions of falling film Reynolds Re1, vapor Reynolds number Re,,inlet subcooling and inlet concentration difference with±15% and±20% error bands, respectively.
机译:在本文中,对平板表面热交换器(如带状翅片)表面氨水降膜吸收过程进行了实验分析。本文研究了液体和蒸气流动特性,液体流动的入口过冷以及入口浓度差对传热和传质性能的影响。入口液体浓度选择为按质量计的5%,10%和15%的氨,而入口蒸气浓度在64.7%至79.7%之间变化。发现在吸收开始之前,由于入口过冷效应,在测试部分的顶部有一个精馏过程。在测试部分的底部附近发现了水的解吸现象。发现较低的入口液体温度和较高的入口蒸气温度,获得了较高的努塞尔特数和舍伍德数。 Nusselt和Sherwood数的相关性是作为降膜雷诺Re1,蒸气雷诺数Re,入口过冷和入口浓度差分别具有±15%和±20%误差带的函数而开发的。

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