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Hydraulic and thermal studies on a chevron type plate heat exchanger

机译:人字形板式换热器的水力和热力研究

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The present work deals with the experimental study of a single pass U-type chevron plate heat exchanger using liquid-liquid combination in both the channels for the range of Reynolds numbers, 800-5900. The influence of Reynolds number, pumping power and number of plates on the hydraulic and thermal performance of PHE are presented. Results are predicted for a chevron angle of β=60o and fixed port size dp =25.4 mm for a different set of plates, namely, 15, 21 and 27 under two different conditions viz. (i) isothermal and (ii) non-isothermal. The present results of non-dimensional channel velocity and Nusselt number are compared with the analytical results of Bossiouny and Martin [3] and Nusselt number correlation of Wang and Sunden [19] respectively. At a Reynolds numbers of 3900, enhancement in Nusselt number on increasing number of plates from 15 to 21 and 21 to 27, is found to be 56% and 19% respectively. Based on experimental data, correlations for Nusselt number and friction factor are also developed.
机译:本工作涉及在雷诺数范围为800-5900的两个通道中使用液-液组合的单程U型人字形板式换热器的实验研究。提出了雷诺数,泵浦功率和塔板数对PHE的水力和热力性能的影响。对于不同的一组板,即在两个不同的条件下,即15、21和27,预测的人字形角度为β= 60o,固定孔尺寸dp = 25.4 mm,可以预测结果。 (i)等温和(ii)非等温。将目前无量纲通道速度和Nusselt数的结果与Bossiouny和Martin [3]的分析结果以及Wang和Sunden [19]的Nusselt数相关性进行了比较。在3900的雷诺数下,随着板数从15增至21和21增至27,努塞尔特数的增加分别为56%和19%。根据实验数据,还建立了努塞尔数与摩擦系数的相关性。

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