Analysis of heat and mass transfer in the adsorbent bed of a thermal wave adsorption cooling cycle

IF 1.3 Q3 THERMODYNAMICS
A. Çağlar, C. Yamali
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引用次数: 4

Abstract

A coupled heat and mass transfer analysis of the adsorbent bed of a thermal wave adsorption cooling cycle is performed. The adsorbent bed is modeled two dimensionally. Governing equations for energy, mass and momentum transfers are solved by Comsol Multiphysics simultaneously. Variations of temperature, pressure, adsorption capacity, equilibrium adsorption capacity and mass transfer coefficient for a finless tube adsorbent bed are presented with multicolored plots. Desorption process is simulated in the model. Results show that the adsorbent bed reaches the maximum cycle temperature uniformly after 5000s. Uniform pressure assumption can be used in the bed due to small pressure gradient during the process. Adsorption capacity decreases from 26.1% to 8.89% in 5000s. Temperature front progresses along the bed creating a thermal wave. The thermal wave length is needed to be short to enhance the bed effectiveness regenerating more heat between the beds of the thermal wave cycle. It can be concluded that a parametric study is recommended for a future work in order to investigate the effects of design and operational parameters on the dependent variables and thermal wave length.
热波吸附冷却循环吸附床的传热传质分析
对热波吸附冷却循环的吸附床层进行了传热传质耦合分析。对吸附床进行了二维建模。能量、质量和动量传递的控制方程由Comsol Multiphysics同时求解。用彩色图描述了无翅片管吸附床的温度、压力、吸附量、平衡吸附量和传质系数的变化规律。模型模拟了解吸过程。结果表明:吸附床在5000s后均匀达到最高循环温度;由于床层过程中压力梯度小,可以采用均匀压力假设。吸附量在5000s时由26.1%下降到8.89%。温度锋沿着河床前进,产生热波。为了提高床层效率,在热波循环的床层间再生更多的热量,需要较短的热波长度。可以得出结论,建议在未来的工作中进行参数化研究,以研究设计和操作参数对因变量和热波长度的影响。
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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来源期刊
CiteScore
2.70
自引率
6.70%
发文量
36
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