1997
DOI: 10.1016/0017-9310(96)00116-0
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A generalized heat transfer correlation for Iouver fin geometry

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Cited by 367 publications
(42 citation statements)
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“…The effect is due the larger deviation between the lowest and highest velocities in the flow maldistribution profiles with high standard deviation. Hence, there is a larger net reduction in heat transfer capacity due to the lower heat transfer performance caused by the lower refrigerant velocities which is supported by Chang and Wang [30]. From Figure 5, D is almost equal to zero when the standard deviation approaches 0.1.…”
Section: Pressure Drop Correlationmentioning
confidence: 73%
See 1 more Smart Citation
“…The effect is due the larger deviation between the lowest and highest velocities in the flow maldistribution profiles with high standard deviation. Hence, there is a larger net reduction in heat transfer capacity due to the lower heat transfer performance caused by the lower refrigerant velocities which is supported by Chang and Wang [30]. From Figure 5, D is almost equal to zero when the standard deviation approaches 0.1.…”
Section: Pressure Drop Correlationmentioning
confidence: 73%
“…The air side heat transfer coefficient was calculated using the Colburn factor, j, recommended by Chang and Wang [30] for louvered fins. The single-phase refrigerantside Nusselt number for laminar flow was calculated using the equation provided by Subramaniam [31].For single phase turbulent flow, the Nusselt number can be obtained by using the equation developed by Subramaniam [31].…”
Section: Heat Transfer Correlationmentioning
confidence: 99%
“…For condensation, the correlation given by [25] combines the influences of the forced convection Nu F and gravity controlled convection Nu B using an asymptotic expression Nu ¼ ðNu 2 F þ Nu 2 B Þ 1=2 . The correlations to calculate the heat transfer coefficients on the air side are specific to cross-flow compact heat exchangers with louvers and fins [26] and [27]. This simplifies the calibration process to identifying two multipliers, k ae,a and k ac,a , which correct the heat transfer …”
Section: Refrigerant Dynamicsmentioning
confidence: 99%
“…For condensation, the correlation given by [29] combines the influences of the forced convection N u F and gravity controlled convection N u B using an asymptotic expression N u = (N u 2 F + N u 2 B ) 1/2 . On the external air side, specific heat transfer coefficients are defined for compact heat exchangers with louvers and fins, as noted by [30,31].…”
Section: Model Calibration and Validationmentioning
confidence: 99%