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SIMULATION OF TWO-PHASE FLOW AND HEAT TRANSFER FOR PRACTICAL DESIGN OF MINI-AND MICRO-CHANNEL HEAT EXCHANGERS

机译:小型和微通道换热器实用设计的两相流和传热模拟

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Mini- and micro-scale heat exchangers provide the means for large heat transfer coefficients with single phase flow due to the inverse proportionality of Nusselt number with respect to the hydraulic diameter. For very high heat flux situations, single phase forced convection in micro-channels may not be sufficient and hence convective flow boiling in small scale heat exchangers has gained wider scrutiny due to the much higher achievable heat transfer coefficients due to latent heat of vaporization and convective boiling. The purpose of this investigation is to explore a practical and accurate modeling approach for simulating multiphase flow and heat transfer in stacked mini- and micro-channel heat exchangers. The work is specifically aimed at providing the framework for the optimization of such devices. The model algorithm is described in detail and the effects of channel hydraulic diameter ranging from 150-300 |j.m and number of stacked layers on the thermal and hydrodynamic performance of the heat sinks are explored. The results from the two parameter study are used to suggest a design path for creating an optimal two-phase stacked microchannel heat exchanger.
机译:微型和微型换热器由于Nusselt数与水力直径成反比,因此可以在单相流中提供较大的传热系数。对于非常高的热通量情况,微通道中的单相强制对流可能不足,因此,由于潜在的汽化和对流热传递系数高得多,因此小型热交换器中的对流沸腾受到了广泛的关注。沸腾。这项研究的目的是探索一种实用且准确的建模方法,以模拟堆叠式微型和微通道换热器中的多相流和传热。这项工作专门针对提供用于优化此类设备的框架。详细描述了模型算法,并研究了通道水力直径范围为150-300μm的通道水力和堆叠层数对散热器的热力学和流体力学性能的影响。来自两个参数研究的结果被用来为创建最佳的两相堆叠式微通道换热器提供设计路径。

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