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Heat transfer and fluid flow in a plate heat exchanger. Part II: Assessment of laminar and two-equation turbulent models

机译:板式换热器中的热传递和流体流动。第二部分:层流和两方程湍流模型的评估

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摘要

This paper presents a comparison of experimental data and numerical predictions for the hydrodynamic and thermal fields in a two-channel plate heat exchanger. The temperature distributions on the first and the last of the three plates, the friction factor and the Nusselt number for each channel as well as the outlet temperatures of the two streams are compared. The laminar model has satisfactorily been validated for Reynolds numbers less than 400. For the turbulent flow regime, several two-equation models were tested and the Realizable κ-ε model with non-equilibrium wall functions has been found to give the closest results to the experimental data. The flow distribution in cross-sections of the channels was studied numerically. Streams of higher velocities on the channels' sides, where two narrow vertical smooth passages are located, were observed.
机译:本文介绍了两通道板式换热器中流体动力学和热场的实验数据和数值预测的比较。比较了三个板中第一个和最后一个板上的温度分布,每个通道的摩擦因数和Nusselt数,以及两个流的出口温度。对于小于400的雷诺数,已经成功验证了层流模型。对于湍流状态,测试了几个两方程模型,发现具有非平衡壁函数的Realizableκ-ε模型可以得出与该方程最接近的结果。实验数据。数值研究了通道横截面的流量分布。在两个狭窄的垂直平滑通道所在的通道侧面观察到了较高的流速。

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