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Experimental investigation of single phase convective heat transfer coefficient in a corrugated plate heat exchanger for multiple plate configurations

机译:多板式波纹板式换热器中单相对流换热系数的实验研究

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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.
机译:波纹板式换热器由于波纹而具有更大的热传递表面积和增加的湍流度。在这项研究中,获得了商用板式热交换器中对称30°/ 30°,60°/ 60°和30°/ 60°人字形混合的单相流(水到水)配置的实验传热数据角板。进行了雷诺数为500至2500和普朗特数为3.5至6.5的实验。实验结果表明,人字形角和雷诺数对传热系数有显着影响。在实验数据的基础上,提出了相关的估计努塞尔数与雷诺数,普朗特数和人字形角的函数关系。

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