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首页> 外文期刊>Science and Technology for the Built Environment >Variable geometry microchannel heat exchanger modeling under dry, wet, and partially wet surface conditions accounting for tube-to-tube heat conduction
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Variable geometry microchannel heat exchanger modeling under dry, wet, and partially wet surface conditions accounting for tube-to-tube heat conduction

机译:干燥,潮湿和部分潮湿的表面条件下的可变几何结构微通道换热器模型,说明了管对管的热传导

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摘要

Numerical models for microchannel heat exchangers are favored in the research and development process due to their cost effectiveness as opposed to prototype development and testing. A literature survey suggests that a unified air-to-surface heat and mass transfer modeling approach is lacking for microchannel heat exchangers, especially under dehumidifying conditions with tube-to-tube heat conduction. This research presents an air-to-fin heat and mass transfer model for a microchannel heat exchanger operating under dry, wet, and partially wet conditions. Typically, there are two boundary conditions for the fins in microchannel heat exchangers. The adiabatic fin tip boundary condition is applied to the extended fins on the top and bottom of the microchannel slab. The second boundary condition is the prescribed surface temperature, applicable to a fin bounded by two tubes. The proposed fin analysis method accounts for both boundary conditions and tube-to-tube conduction. The modeling approach is capable of locating the boundary between a dry and wet surface if a fin is partially wet. The model is verified against simulation results for air-to-surface heat transfer on a fin obtained using a commercially available computational fluid dynamics package. A new finite-volume microchannel heat exchanger model is developed using the proposed fin analysis method. The model is capable of predicting the performance of a variable geometry microchannel heat exchanger under both dry and dehumidifying conditions and is validated against experimental data. The average absolute capacity deviation between the predicted and measured values is 2.44% for condensers and 2.92% for evaporators. The absolute difference in sensible heat ratio for evaporators between predicted and measured values is 0.018. The proposed model allows for the most comprehensive and accurate analysis of microchannel evaporators and condensers.
机译:由于微通道换热器的数值模型具有成本效益,而不是原型开发和测试,因此其在研究和开发过程中受到青睐。文献调查表明,微通道热交换器缺乏统一的空气-表面传热和传质建模方法,尤其是在具有管对管导热的除湿条件下。这项研究提出了一种在干燥,湿润和部分湿润条件下运行的微通道换热器的空气到翅片的传热传质模型。通常,微通道热交换器中的散热片有两个边界条件。绝热翅片尖端边界条件应用于微通道板顶部和底部的延伸翅片。第二个边界条件是规定的表面温度,适用于以两个管为边界的散热片。拟议的鳍分析方法考虑了边界条件和管对管的传导。如果鳍片部分湿润,则建模方法能够确定干燥表面和湿润表面之间的边界。对照通过使用市售计算流体动力学软件包获得的散热片上的空气到表面传热的仿真结果验证了该模型。利用提出的鳍片分析方法,建立了一个新的有限体积微通道换热器模型。该模型能够预测在干燥和除湿条件下可变几何形状的微通道换热器的性能,并针对实验数据进行了验证。冷凝器的预测值和测量值之间的平均绝对容量偏差为2.44%,而蒸发器为2.92%。预测值和测量值之间的蒸发器显热比的绝对差为0.018。提出的模型可以对微通道蒸发器和冷凝器进行最全面,最准确的分析。

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