Abstract
The state of the problem of mathematical modeling of the heat and mass transfer during film condensation of a gas is considered.
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Abbreviations
- Ck :
-
relative mass concentration of the k-th component
- G:
-
flow rate
- g:
-
acceleration of gravity
- H=h+w 2x /2:
-
total stream enthalpy
- h:
-
enthalpy
- hk :
-
enthalpy of the k-th component
- Δhk :
-
specific heat of condensation
- jk :
-
diffusion flux of the k-th component
- P:
-
pressure
- T:
-
temperature
- TS :
-
saturation temperature
- S:
-
cross-sectional area
- q:
-
specific heat flux
- wx, wy :
-
velocity components
- x, y:
-
coordinates
- δ :
-
condensate film thickness
- μ:
-
viscosity
- Π:
-
perimeter
- ρ:
-
density
- τ :
-
tangential stress
- eff:
-
effective
- f:
-
“frozen”
- in:
-
input
- w:
-
wall
- l :
-
liquid
- c:
-
cooling medium
- δ :
-
phase interface
- 4:
-
O2 component in the system N2O4 ⇄ 2NO2 ⇄ 2NO+O2
Literature cited
W. Nusselt, “Die Oberflachen Kondensation des Wasserdampfes,” Zeitschrift VDI,60, 541–546, 568–575 (1916).
G. G. Chernyi, “Laminar gas and fluid motion in a boundary layer with a discontinuity surface,” Izv. Akad. Nauk SSSR, Otd. Tekh. Nauk, No. 12, 38–67 (1954).
W. J. Minkowycz and E. M. Sparrow, “Condensation heat transfer in presence of noncondensables, interfacial resistance, superheating, variable properties, and diffusion,” Int. J. Heat Mass Transfer,9, 1125–1144 (1966).
E. M. Sparrow, W. J. Minkowycz, and M. Saddy, “Forced convection condensation in the presence of noncondensables and interfacial resistance,” Int. J. Heat Mass Transfer,10, 1829–1845 (1967).
V. P. Gribkova, A. A. Mikhalevich, and V. B. Nesterenko, “Condensation of a chemically reacting gas on a vertical surface,” Inzh.-Fiz. Zh.,22, 1012–1019 (1972).
J. C. Y. Koh, “Film condensation in a forced-convection boundary-layer flow,” Int. J. Heat Mass Transfer,5, 941–954 (1962).
Suhatme and Rosenow, “Heat transfer in film condensation of a liquid metal,” Trans. ASME, Ser. C,88, No. 1, 20–30 (1966).
A. A. Mikhalevich and V. K. Fedosova, “Condensation of a chemically reacting gas on a horizontal tube,” Inzh.-Fiz. Zh.,40, No. 5, 793–799 (1981).
A. A. Mikhalevich, V. B. Nesterenko, and V. I. Volodin, “Resistance and condensation heat and mass transfer in turbulent flow,” Second Symposium of Turbulent Shear Flows, London (1979), pp. 924–934.
Yan Zhi-U, “Influence of a constant suction rate on film condensation in a laminar condensate flow on a porous vertical wall,” Heat Transfer, Trans. ASME, Ser. C,92, No. 2, 43–48 (1970).
A. A. Mikhalevich, Mathematical Modeling of Mass and Heat Transfer during Condensation [in Russian], Nauka i Tekhnika, Minsk (1982).
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Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 45, No. 5, pp. 843–849, November, 1983.
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Mikhalevich, A.A. Mathematical modeling of heat and mass transfer in film condensation. Journal of Engineering Physics 45, 1331–1337 (1983). https://doi.org/10.1007/BF01254746
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DOI: https://doi.org/10.1007/BF01254746