努塞尔数
传热系数
普朗特数
板式换热器
雷诺数
材料科学
机械
动态刮削表面换热器
传热
湍流普朗特数
热交换器
热力学
V形(解剖学)
对流换热
同心管换热器
湍流
物理
临界热流密度
地质学
古生物学
作者
Tariq S. Khan,M. Adam Khan,M.-C. Chyu,Zahid H. Ayub
标识
DOI:10.1016/j.applthermaleng.2010.01.021
摘要
Corrugated plate heat exchangers have larger heat transfer surface area and increased turbulence level due to the corrugations. In this study, experimental heat transfer data are obtained for single phase flow (water-to-water) configurations in a commercial plate heat exchanger for symmetric 30°/30°, 60°/60°, and mixed 30°/60° chevron angle plates. Experiments were carried out for Reynolds number ranging from 500 to 2500 and Prandtl number from 3.5 to 6.5. Experimental results show significant effect of chevron angle and Reynolds number on the heat transfer coefficient. Based on the experimental data, a correlation to estimate Nusselt number as a function of Reynolds number, Prandtl number and chevron angle has been proposed.
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