非牛顿流体充填床的传热研究

D. Priyadharisani, M. Thirumarimurugan, T. Kannadasan
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引用次数: 0

摘要

本项目旨在通过测定不同体积组分的水-水体系和羧甲基纤维素-水体系的总体换热系数、效率、冷侧效率和热侧效率,研究和比较填料床逆流流动和平行流动的换热特性。在填充床中,冷热流体的入口温度保持恒定。在性能分析中,水-水系统和cmc -水系统的冷流体流量在3lpm到8lpm之间变化。水-水系统和cmc -水系统的热流体流速均保持恒定。在本研究中,cmc -水体系的体积组成在0.05% ~ 0.20%之间变化。分别对并联和逆流两种流型进行了实验,并进行了比较和报道。利用量纲分析建立了物理模型,并与实验数据进行了拟合。利用该物理模型进行了仿真研究,并与实验值进行了比较。仿真结果与实验结果吻合较好。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Heat Transfer Studies on Packed Bed Using Non Newtonian Fluid
This project aims to study and compare the heat transfer characteristics for Counter-current flow and Parallel Flow through Packed Bed by determining the overall heat transfer coefficient, effectiveness, cold side efficiency and hot side efficiency for water-water system and Carboxymethylcellulose (CMC)-water system with various compositions on volume basis. In Packed Bed, the inlet temperatures of both hot and cold fluids are maintained constant. In performance analysis the flow rate of cold fluid was varied from 3 lpm to 8 lpm for both water-water system and CMC-water system. The flow rate of hot fluid was maintained constant for both water-water system and CMC-water system. In this work the composition of the CMC-water system were varied from 0.05% to 0.20% on volume basis. The experiments were carried out for both parallel and counter current flow pattern, compared and reported. A physical model was developed using dimensional analysis and fitted with the experimental data. Simulation studies were done using this physical model and compared with the experimental values. The simulation studies were found to agree well with the experimental results.
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