Heat transfer and friction correlations for plate finned-tube heat exchangers having plain fins
DL Gray, RL Webb - International Heat Transfer Conference …, 1986 - dl.begellhouse.com
This paper is concerned with heat exchangers having continuous, flat fins on a staggered
array of circular tubes. Correlations are developed to predict the air-side heat transfer …
array of circular tubes. Correlations are developed to predict the air-side heat transfer …
Air-side heat transfer and friction correlations for plain fin-and-tube heat exchangers with staggered tube arrangements
NH Kim, B Youn, RL Webb - 1999 - asmedigitalcollection.asme.org
This paper deals with heat exchangers having plain fins on a staggered array of circular
tubes. Correlations are developed to predict the air-side heat transfer coefficient and friction …
tubes. Correlations are developed to predict the air-side heat transfer coefficient and friction …
Nucleate pool boiling data for five refrigerants on plain, integral-fin and enhanced tube geometries
RL Webb, C Pais - International Journal of Heat and Mass Transfer, 1992 - Elsevier
Data are presented for nucleate pool boiling on five different horizontal tube geometries using
five refrigerants at two saturation temperatures. The refrigerants tested are R-11, R-12, R-…
five refrigerants at two saturation temperatures. The refrigerants tested are R-11, R-12, R-…
Air-side heat transfer in finned tube heat exchangers
RL Webb - Heat Transfer Engineering, 1980 - Taylor & Francis
Because of the low heat transfer coefficient of gases, it is necessary to use extended surfaces
on the gas side when exchanging heat with liquids or two-phase fluids. Such finned tube …
on the gas side when exchanging heat with liquids or two-phase fluids. Such finned tube …
Performance evaluation criteria for use of enhanced heat transfer surfaces in heat exchanger design
RL Webb - international journal of heat and mass transfer, 1981 - Elsevier
… This study extends previous work of Bergles and Webb to establish a broad range of
Performance Evaluation Criteria (PEC) applicable to single phase flow in tubes. The equations …
Performance Evaluation Criteria (PEC) applicable to single phase flow in tubes. The equations …
Calculation of fin efficiency for wet and dry fins
KT Hong, RL Webb - HVAC&R Research, 1996 - Taylor & Francis
… The authors provide an empirical modification to the Schmidt equation (Hong and Webb …
Use of the sector method with the Hong and Webb equation is recommended. Cases for …
Use of the sector method with the Hong and Webb equation is recommended. Cases for …
The evolution of enhanced surface geometries for nucleate boiling
RL Webb - Heat Transfer Engineering, 1981 - Taylor & Francis
This paper surveys the evolution of special surface geometries that promote high-performance
nucleate boiling. Early work by Jakob and Fritz in 1931 showed that emery paper …
nucleate boiling. Early work by Jakob and Fritz in 1931 showed that emery paper …
Enhanced heat transfer
RL Webb, NY Kim - Taylor and Francis, NY, 2005 - dl.begellhouse.com
… Webb@psu.edu. Authors may also electronically submit manuscripts to any of the
regional editors listed on the inside Journal cover or on the Begell House website http://www.…
regional editors listed on the inside Journal cover or on the Begell House website http://www.…
Donald Q. Kern lecture award paper: odyssey of the enhanced boiling surface
RL Webb - J. Heat Transfer, 2004 - asmedigitalcollection.asme.org
… growth period were modeled separately and are given in Chien and Webb 31. This work
was supported by measurement of the bubble dynamic parameters by Chien and Webb 34. …
was supported by measurement of the bubble dynamic parameters by Chien and Webb 34. …
Heat transfer and friction in tubes with repeated-rib roughness
RL Webb, ERG Eckert, RJ Goldstein - International journal of heat and mass …, 1971 - Elsevier
… A more complete description of the apparatus is given by Webb [27]. … RL WEBB, Turbulent
heat transfer in tubes having twodimensional roughness, including the effect of Prandtl number…
heat transfer in tubes having twodimensional roughness, including the effect of Prandtl number…