Analysis of the suction effect on the mass transfer when using the heat and mass transfer analogy

被引:31
作者
de la Rosa, J. C. [1 ]
Herranz, L. E. [2 ]
Munoz-Cobo, J. L. [3 ]
机构
[1] Nucl Serv Business, Initec Westinghouse Technol Serv SA, Dept PRA & Fluid Syst, Tarragona 43890, Spain
[2] Unit Nucl Safety Res CIEMAT, Madrid 28040, Spain
[3] Univ Politecn Valencia, Dept Chem & Nucl Engn, Valencia 46022, Spain
关键词
CONDENSATION; CONTAINMENT; LAYER;
D O I
10.1016/j.nucengdes.2009.06.003
中图分类号
TL [原子能技术]; O571 [原子核物理学];
学科分类号
0827 ; 082701 ;
摘要
The transport phenomenon between a fluid in movement and a wall is strongly affected by the permeability of the wall. The application of a correction factor standing for the transpiration effect will be required whenever a heat transfer model is based either on the use of heat, mass or momentum analogies or on the use of empirical correlations for the computation of the heat transfer coefficient. The suction factor commonly used when solving as a function of either mass or molar fractions is called the Bird suction factor. The validity of this factor rests on the hypothesis of the film theory or Couette flow. This paper reviews the Bird suction factor in laminar regime, extending the analysis to turbulent flow conditions and finding thereby that Bird's equation can overestimate the suction factor under turbulent condensation conditions in the gas phase. Finally, an alternative formulation for the suction factor under turbulent condensation conditions has been proposed and compared with Bird's original formulation. In doing this, both data and models developed by other authors and the UW-Madison test facility database have been used. The results show the suitability of the alternative formulation when calculating the condensation rate in turbulent natural circulation scenarios, whereas Bird's formulation seems to be more appropriate for laminar regimes. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:2042 / 2055
页数:14
相关论文
共 50 条
[11]   A Computational Analysis of Heat and Mass Transfer in an Indirect Evaporative Cooler Using the Spray Dryer Model [J].
Berning, Torsten ;
Sorensen, Henrik ;
Nielsen, Mads Pagh .
ENERGIES, 2024, 17 (11)
[12]   Dependence of wettability of microtextured wall on the heat and mass transfer: Simple estimates for convection and heat transfer [J].
Misyura, S. Y. .
INTERNATIONAL JOURNAL OF MECHANICAL SCIENCES, 2020, 170
[13]   Effect of Mesoscopic Structure of Interface on Heat and Mass Transfer in a Partially Porous Cavity [J].
Chen, Baoming ;
Wang, Li ;
Liu, Fang ;
Yun, Heming ;
Geng, Wenguang .
MNHMT2009, VOL 2, 2010, :699-705
[14]   Unsteady Heat and Mass Transfer in Structured Media and Gel [J].
Pokusaev, B. G. ;
Nekrasov, D. A. ;
Zakharov, N. S. ;
Khramtsov, D. P. ;
Karlov, S. P. ;
Vyazmin, A. V. .
THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2020, 54 (01) :91-103
[15]   Heat and mass transfer analysis on peristaltic transport of PTT fluid with wall properties [J].
Channakote, M. M. ;
Siddabasappa, C. .
LATIN AMERICAN APPLIED RESEARCH, 2024, 54 (04) :545-553
[16]   Heat and mass transfer at condensate-vapor interfaces [J].
Kryukov, A. P. ;
Levashov, V. Yu ;
Zhakhovskii, V. V. ;
Anisimov, S., I .
PHYSICS-USPEKHI, 2021, 64 (02) :109-140
[17]   NUMERICAL SIMULATION OF HEAT AND MASS TRANSFER IN AN EJECTION APPARATUS [J].
Kologrivov, M. M. ;
Buzovskii, V. P. .
JOURNAL OF ENGINEERING PHYSICS AND THERMOPHYSICS, 2016, 89 (01) :167-178
[18]   Numerical modelling of heat and mass transfer in finned dehumidifier [J].
Croce, Giulio ;
De Candido, Erika ;
D'Agaro, Paola .
APPLIED THERMAL ENGINEERING, 2009, 29 (07) :1366-1374
[19]   Heat and mass transfer during the warming of a bottle of beer [J].
Barbosa Monteiro, Claudio Vinicius ;
Righetto, Aderson Roberto ;
de Sousa, Leonardo Cesar ;
Paraiso, Paulo Roberto ;
de Matos Jorge, Luiz Mario .
ACTA SCIENTIARUM-TECHNOLOGY, 2010, 32 (02) :153-157
[20]   Mass and heat transfer model of Tubular Solar Still [J].
Ahsan, Amimul ;
Fukuhara, Teruyuki .
SOLAR ENERGY, 2010, 84 (07) :1147-1156