Experimental Study of Heat Transfer for Supercritical Carbon Dioxide with Upward Flow in Vertical Tube

J. Hsieh, Boreum Lee, M. Chung, D. T. Lin, Shu Guo
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引用次数: 3

Abstract

In this study heat transfer of supercritical carbon dioxide in vertical tube with 10 mm of inner diameter and 1800 mm of length was investigated experimentally. The initial temperature of tube wall was set to 150 and 200°C. The system pressures of supercritical carbon dioxide are 1100, 1500 and 2000 psi, respectively. The experimental results show that the heat transfer coefficient and heat transfer rate increase with Reynolds number. The maximum heat transfer coefficient and heat transfer rate was occurred in 1500 psi of system pressure. The heat transfer coefficient for 150°C is higher than that of 200°C resulted from effect of specific heat.
超临界二氧化碳垂直管内向上流动换热实验研究
本文对超临界二氧化碳在内径为10mm、长度为1800mm的垂直管内的传热进行了实验研究。管壁初始温度分别设置为150℃和200℃。超临界二氧化碳的系统压力分别为1100psi、1500psi和2000psi。实验结果表明,传热系数和传热速率随雷诺数的增加而增大。在系统压力为1500psi时,传热系数和传热速率达到最大值。由于比热的影响,150℃时的换热系数高于200℃时的换热系数。
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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