Abstract
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.
Original language | English |
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Pages (from-to) | 851-858 |
Number of pages | 8 |
Journal | International Journal of Refrigeration |
Volume | 28 |
Issue number | 6 |
DOIs | |
Publication status | Published - 2005 Sept |
Keywords
- Experiment
- Finned tube
- Geometry
- Heat exchanger
- Heat transfer coefficient
ASJC Scopus subject areas
- Building and Construction
- Mechanical Engineering