2003
DOI: 10.1016/s0140-7007(02)00161-5
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Condensation heat transfer coefficients of R22, R407C, and R410A on a horizontal plain, low fin, and turbo-C tubes

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Cited by 53 publications
(17 citation statements)
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“…In fact, however, the condensate film is wavy even at low Reynolds numbers causing a convection current and also reducing the film thickness, which was observed through the sight glass. This phenomenon that measured HTCs were higher than those calculated by Nusselt's equation was also observed for other fluids as well [9,10,14]. This comparison showed that the present data for the flammable refrigerants are quite reasonable.…”
Section: Resultssupporting
confidence: 87%
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“…In fact, however, the condensate film is wavy even at low Reynolds numbers causing a convection current and also reducing the film thickness, which was observed through the sight glass. This phenomenon that measured HTCs were higher than those calculated by Nusselt's equation was also observed for other fluids as well [9,10,14]. This comparison showed that the present data for the flammable refrigerants are quite reasonable.…”
Section: Resultssupporting
confidence: 87%
“…2, HTCs of HCFC22 and HFC134a from Refs. [9,10] are included for reference. Data of various flammable refrigerants of different vapor pressures exhibited a typical trend that external condensation HTCs decrease as the wall subcooling increases.…”
Section: Resultsmentioning
confidence: 99%
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“…The heat transfer coefficient given by Holman [18] and Jung et al [19] and considered the tilt angle (q), the inner diameter of fin tube (D i ) and the fin tube length (L c ). Therefore, the film-condensation thermal resistance can be expressed as:…”
Section: The Film-condensation Thermal Resistance Of the Work Fluidmentioning
confidence: 99%