以乙二醇为试验流体的波纹板换热器的热性能

Sreedhar Rao Battula, Keerthana Reddy Chittireddy, Meena Pullurwar, Kishore Kumar Sriramoju
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引用次数: 0

摘要

本文以乙二醇为试验流体,对不同波纹角的平板换热器和波纹板换热器进行了实验对比热分析。实验以75°C的水为热流体,采用逆流模式进行。每个板上设计有11个热电偶传感器来确定温度,其中7个用于测量板的表面温度,4个用于测量冷热流体的进出口体积温度。测试流体的质量流量在每分钟0.5至4升之间变化,并测量相应的稳态温度。利用实验读数,确定了进出口流温差(DT)、对数平均温差(LMTD)和总传热系数(U)。得到了CPHE波纹角(300、500)的DT和U值,并与平板换热器进行了比较。当波纹角为30°和50°时,DT和U值随流体质量流量的增大而增大。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Thermal performance of corrugated plate heat exchanger using ethylene glycol as test fluid
This paper reports an experimental comparative thermal analysis of a flat plate heat exchanger and corrugated plate heat exchanger (CPHE) of different corrugation angles using ethylene glycol as test fluid. The experiments were carried out counter current mode using water as hot fluid at 75°C.  Design of each plate provided with eleven thermocouple sensors to determine the temperatures, in which seven were used to measure the surface temperature of plate and four were used to measure the inlet and outlet bulk temperature of cold and hot fluids.  The mass flow rate of test fluid, varied between 0.5 to 4 liters per minute and corresponding steady state temperatures is measured. Using experimental readings, temperature difference between the inlet and outlet streams (DT), logarithmic mean temperature difference (LMTD) and overall heat transfer coefficient (U) are determined. The obtained DT and U values of corrugation angles (300, 500) of CPHE were compared with those of flat plate heat exchangers. For corrugation angle of 30° and 50°, the DT and U values increases with increase of mass flow rate of the fluid.
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