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Thermal hydraulic performance analysis of a printed circuit heat exchanger using a helium-water test loop and numerical simulations

机译:使用氦水测试回路和数值模拟的印刷电路板换热器热工水力性能分析

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摘要

A Printed Circuit Heat Exchanger (PCHE) is a promising candidate with excellent performance to satisfy the heat exchanger requirements of High Temperature Gas Cooled Reactors (HTGRs). These heat exchangers are composed of many micro-wavy channels, which cause an increase in both heat transfer and pressure drop. We investigated thermal-hydraulic performance of the PCHE in a helium-water condition through experimental tests and numerical simulations with horizontal and vertical arrangements. Experiments were performed in laminar region. Pressure drop and temperatures were measured during experiments at the inlet and outlet of the helium and the water sides, respectively. We obtained three-dimensional (3-D) numerical solutions with periodic boundary conditions using the computational fluid dynamics (CFD) code, FLUENT. The numerical simulation range was expanded to Reynolds number of 2500 through the 3-D CFD simulations, after the numerical solutions were validated against experimental data. A proposed Fanning factor correlation in the PCHE, in terms of Reynolds number and a correction factor, predicts the local pitch-averaged Fanning factor in the helium and the water sides in the range of less than 0.97% and 0.65%, respectively. A Nusselt number correlation with an average error of 3.589% was also developed in terms of Reynolds number and Prandtl number.
机译:印制电路换热器(PCHE)具有出色的性能,可以满足高温气冷堆(HTGRs)的换热器要求。这些热交换器由许多微波状通道组成,这会导致传热和压降的增加。我们通过实验测试和水平和垂直排列的数值模拟研究了氦气条件下PCHE的热工液压性能。实验在层流区域进行。在实验过程中分别在氦气的入口和出口以及水侧测量了压降和温度。我们使用计算流体力学(CFD)代码FLUENT获得了具有周期性边界条件的三维(3-D)数值解。在针对实验数据验证了数值解后,通过3-D CFD模拟将数值模拟范围扩展到2500雷诺数。根据雷诺数和校正因子,在PCHE中提议的扇形因子相关性预测氦和水侧局部沥青平均扇形因子分别在小于0.97%和0.65%的范围内。根据雷诺数和普朗特数,还建立了平均误差为3.589%的努塞尔数相关性。

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