1975
DOI: 10.1007/bf02559682
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Neue Gleichungen für den Wärme- und den Stoffübergang in turbulent durchströmten Rohren und Kanälen

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Cited by 354 publications
(136 citation statements)
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“…In fact, some well-known texts do not recognize that a Prandtl number less than 0.6 can occur for gas mixtures. Several relations have been reported which differ considerably from Colburn and are suggested for use over a wide range of Prandtl numbers, some as low as 0.1 [Kays, 1966;Petukhov, 1970;Sleicher and Rouse, 1975;Gnielinski, 1975;and Churchill, 1977]. The relations recommended by these investigators are tabulated in Table 1.…”
Section: Abstracmentioning
confidence: 99%
“…In fact, some well-known texts do not recognize that a Prandtl number less than 0.6 can occur for gas mixtures. Several relations have been reported which differ considerably from Colburn and are suggested for use over a wide range of Prandtl numbers, some as low as 0.1 [Kays, 1966;Petukhov, 1970;Sleicher and Rouse, 1975;Gnielinski, 1975;and Churchill, 1977]. The relations recommended by these investigators are tabulated in Table 1.…”
Section: Abstracmentioning
confidence: 99%
“…2. The initial-boundary value problem defined by equations (1)(2)(3)(4)(5)(6)(7)(8)(9)(10)(11)(12)(13)(14) applies to heat exchangers made of bare or finned tubes. For bare tubes, m f is equal to zero because there are no fins.…”
Section: T X T T X Y T Dymentioning
confidence: 99%
“…The correlation for the Nusselt number at the water side was taken in a form similar to the formulae developed by Petukhov & Kirillov [14] and Gnielinski [10]. …”
Section: Experimental Correlations For Water-and Air-side Nusselt Nummentioning
confidence: 99%
“…The convective heat transfer coefficient is calculated according to the Gnielinski correlation [40], The latent heat transfers are calculated using the Lewis heat-mass transfer analogy. The former sensible heat (Eq.…”
Section: Numerical Modelmentioning
confidence: 99%