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HEAT TRANSFER ENHANCEMENT IN SPLIT AND RECOMBINE FLOW CONFIGURATIONS: A NUMERICAL AND EXPERIMENTAL STUDY

机译:分流和重组流动配置中的传热增强:数值和实验研究

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Heat transfer enhancement in laminar regime by split and recombine (SAR) mechanism, based on. the baker's transformation, is investigated. Two different heat exchangers, called SARI and SAR2, are studied. Their geometries are inspired from the previous studies reported in the literature. The working fluid on both, shell and tube side, is water and the temperature on the shell side is kept constant. Experiments are carried out for the Reynolds number range 100<Re<3000 when the Prandtl number is between 4.5 and 7.5. The results show that the convective heat transfer coefficient in the first element of heat exchanger SARI is higher than that in the second one, i.e. SAR2. However, the variation in the convective heat transfer coefficient from the first to the third element along the heat exchanger SAR2 is less significant than that observed for SARI. Moreover, SAR2 causes a higher pressure drop, especially when Re>1000, and provides a less uniform temperature field at the outlet.
机译:基于MATLAB的分裂和重组(SAR)机制,层流制度的热传递增强。贝克的转型是调查的。研究了两个不同的热交换器,称为SARI和SAR2。他们的几何形状受到文学中报告的先前研究的启发。壳体和管侧的工作流体是水,壳侧的温度保持恒定。当Prandtl数在4.5和7.5之间时,对雷诺数范围100 1000时,并在出口处提供更均匀的温度场。

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