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Heat transfer characteristics of flat plate finned-tube heat exchangers with large fin pitch

机译:翅片节距大的平板翅片管式换热器的传热特性

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The objective of this study is to provide experimental data that can be used in the optimal design of flat plate finned-tube heat exchangers with large fin pitch, In this study, 22 heat exchangers were tested with a variation of fin pitch, number of tube row, and tube alignment. The air-side heat transfer coefficient decreased with a reduction of the fin pitch and an increase of the number of tube row. The reduction in the heat transfer coefficient of the four-row heat exchanger coil was approximately 10% as the fin pitch decreased from 15.0 to 7.5 mm over the Reynolds number range of 500-900 that was calculated based on the tube diameter. For all fin pitches, the heat transfer coefficient decreased as the number of tube row increased from 1 to 4. The staggered tube alignment improved heat transfer performance more than 10% compared to the inline tube alignment. A heat transfer correlation was developed from the measured data for flat plate finned-tubes with large fin pitch, The correlation yielded good predictions of the measured data with mean deviations of 3.8 and 6,2% for the inline and staggered tube alignment, respectively.
机译:本研究的目的是提供实验数据,以用于大翅片节距的平板翅片管式换热器的优化设计。在本研究中,测试了22个换热器,其翅片节距,管数均变化排和管对齐。空气侧传热系数随着翅片间距的减小和管排数量的增加而减小。在基于管径计算的雷诺数范围500-900上,当翅片节距从15.0减小到7.5毫米时,四排热交换器盘管的传热系数降低约10%。对于所有散热片节距,随着管排数从1增加到4,传热系数降低。与直列式管排列相比,交错的管排列将传热性能提高了10%以上。从大翅片节距的平板翅片管的测量数据中得出了传热相关性。该相关性可以很好地预测测量数据,对于直列管和交错管对准,平均偏差分别为3.8%和6.2%。

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