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干式蒸发器制冷剂分配与传热性能研究

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创建干式蒸发器的耦合传热模型并模拟了R410A和水的流动情况,通过计算支管的相对标准方差STD研究蒸发器内部的制冷剂分配与流动传热性能。结果表明,均流板可显著降低管程制冷剂的流速分布不均并降低载冷剂出口温度;支管换热量受管内外侧的传热系数影响,管侧传热系数分布与制冷剂流量分布特征一致,而壳侧传热系数主要受工况和壳程结构的影响。最佳均流板方案可使制冷剂不均匀度降低72。0%,同时总换热量提高了 37。4%。
Research on Refrigerant Distribution and Heat Transfer Performance of Dry Evaporator
A coupled heat transfer model for a dry evaporator was established,and the flow distribution of R410A and water were simulated.The refrigerant distribution and flow heat transfer performance inside evaporator were studied by calculating the relative standard deviation STD of branch pipes.The results show that an equalizing plate can significantly reduce the uneven flow rate distribution of refrigerant in the tube and lower the outlet temperature of the refrigerant carrier.The heat transfer of branch pipe is affected by heat transfer coefficient inside and outside the pipe.The heat transfer coefficient distribution on pipe side is consistent with the refrigerant flow distribution characteristics.While the heat transfer coefficient on the shell side is mainly affected by working conditions and shell side structure.The optimal flow equalizing plate scheme can reduce refrigerant unevenness by 72.0%,the total heat exchange increased simultaneously by 37.4%.

Dry EvaporatorUnevennessHeat Transfer PerformanceNumerical Simulation

宋哲、胡博文、苟盼、徐进兵、李伟、刘杰

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合肥通用机械研究院有限公司,安徽合肥,230071

干式蒸发器 不均匀度 传热性能 数值模拟

2024

制冷
广东省制冷学会,福建省制冷学会,河南省制冷学会,云南省制冷学会,广西区制冷学会

制冷

影响因子:0.432
ISSN:1005-9180
年,卷(期):2024.43(2)