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EXPERIMENTAL INVESTIGATION OF MICRO HEAT EXCHANGERS USING POROUS MEDIA OR MICROCHANNELS

机译:多孔介质或微通道微型换热器的实验研究

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The flow and heat transfer performance of a micro-channel heat exchanger and a micro-porous heat exchanger are investigated experimentally and compared with two other heat exchanger designs. The results revealed that the heat transfer performance of the micro-porous heat exchanger is better than that of the micro-channel heat exchanger, but the pressure drop increases correspondingly. For the conditions investigated, the maximum volumetric heat transfer coefficient of the micro-porous heat exchanger is 86.3 MW/(m{sup}3K), the corresponding mass flow rate is 0.067 kg/s and the pressure drop is 4.66 bar. The maximum volumetric heat transfer coefficient of the micro-channel heat exchanger is 38.4 MW/(m{sup}3K), the corresponding mass flow rate is 0.34 kg/s and the pressure drop is 0.9 bar. The overall performance considering both the heat transfer and pressure drop of the micro heat exchanger using deeper microchannels is better than the micro heat exchangers using shallow microchannels or porous media.
机译:微通道热交换器的流动和传热性能和微孔热交换器进行实验研究,并与另外两个热交换器设计进行比较。结果表明,微孔热交换器的传热性能优于微通道热交换器的传热性能,但压降相应地增加。对于所研究的条件,微多孔热交换器的最大体积传热系数是86.3mw /(m {sup} 3k),相应的质量流量为0.067kg / s,压降为4.66巴。微通道热交换器的最大体积传热系数是38.4mW /(m {sup} 3k),相应的质量流量为0.34kg / s,压降为0.9巴。考虑使用深层微通道的微型热交换器的传热和压降的整体性能优于使用浅微通道或多孔介质的微热交换器。

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