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Optimization of Wave Inclination Angle in Parallel Wavy‑Channel Heat Exchangers

机译:平行波道式换热器的波倾角优化

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摘要

Effects of the wave inclination angle on the performance of a parallel wavy-channel heat exchanger are investigated threedimensionally.Computations have been carried out in various Reynolds numbers in the laminar range from 100 to 600 bymeans of the finite volume approach. On the other hand, several wave inclination angles such as α = 0°, 20°, 40°, 60°, and80° with respect to the spanwise direction have been examined to find the optimum value. The applied numerical methodhas been validated against the available data of the conventional parallel flat-channel heat exchanger. Several quantitativeand qualitative results are presented in this investigation. It is demonstrated that deflection of waves of plates from zero tononzero values onsets the three-dimensional flow in the heat exchanger. In addition, maximum heat transfer enhancementof 108% is achieved for Re = 600 at the wave inclination angle of 20°. Moreover, except at Re = 100, the wave inclinationangle of 40° can be introduced as an optimum inclination angle for a wavy-channel heat exchanger from the perspective ofthermal–hydraulic performance. At the end of this study, values of pressure drop penalty and thermal–hydraulic performanceof all cases under consideration have been determined accordingly.
机译:从三维角度研究了波浪倾斜角对平行波浪通道换热器性能的影响。在有限体积法的层流范围内,从100到600层流范围内的各种雷诺数进行了计算。另一方面,已经检查了相对于翼展方向的几个波倾斜角,例如α= 0°,20°,40°,60°和80°,以找到最佳值。已针对常规并联平流道热交换器的可用数据验证了所应用的数值方法。这项研究提出了一些定量和定性的结果。已经证明,板的波从零值到非零值的偏转使热交换器中的三维流动开始。此外,在波倾角为20°时,Re = 600时,可实现最大传热增强108%。此外,除了Re = 100之外,从热工-液压性能的角度来看,可以将40°的波倾角作为波浪通道热交换器的最佳倾角。在研究结束时,已确定了所有考虑中的情况下的压降损失值和热工水力性能值。

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