Effects of mass transfer on heat and mass transfer characteristics between water surface and airstream

被引:16
作者
Gu, L. D. [1 ]
Min, J. C. [1 ]
Tang, Y. C. [1 ]
机构
[1] Tsinghua Univ, Dept Engn Mech, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Convective heat and mass transfer; Chilton-Colburn analogy; Water evaporation; Variable air property; High mass flux; LIQUID-FILM CONDENSATION; VERTICAL PLATE CHANNELS; THIN POROUS LAYER; CONVECTION HEAT; EVAPORATION RATE; AIR-FLOW; INVERSION TEMPERATURE; SUPERHEATED STEAM; RECTANGULAR DUCT; LAMINAR-FLOW;
D O I
10.1016/j.ijheatmasstransfer.2018.02.061
中图分类号
O414.1 [热力学];
学科分类号
摘要
A numerical study has been conducted to simulate the convective heat and mass transfer between water surface and air fluid flowing over it. The airflow is laminar and steady, and has a temperature much higher than the water, causing a combined heat and mass transfer accompanied with water evaporation into the airstream. Calculations are performed to investigate the effects of mass flux on heat and mass transfer coefficients and the applicability of the Chilton-Colburn analogy for 200 degrees C air temperature, 1-10 m/s air velocities, and 10-90 degrees C water temperatures. Calculations are implemented with and without consideration of the air property variations caused by the air temperature and humidity changes near the water surface and in the airflow direction. The results show that the heat and mass transfer coefficients both decrease with increasing water surface temperature, i.e. increasing mass flux. The Chilton-Colburn analogy holds only for low water temperature case, the deviation of the heat to mass transfer coefficient ratio given by the Chilton-Colburn analogy relative to that by the numerical simulation is less than 5% when the water surface temperature is below 60 degrees C. The air property variability has a notable and complex effect on heat transfer coefficient but an inconspicuous effect on mass transfer coefficient. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1093 / 1102
页数:10
相关论文
共 47 条
[1]   Evaporation rate as a function of water salinity [J].
Al-Shammiri, M .
DESALINATION, 2002, 150 (02) :189-203
[2]   Buoyancy effects on upward and downward laminar mixed convection heat and mass transfer in a vertical channel [J].
Azizi, Youssef ;
Benhamou, Brahim ;
Galanis, Nicolas ;
El-Ganaoui, Mohammed .
INTERNATIONAL JOURNAL OF NUMERICAL METHODS FOR HEAT & FLUID FLOW, 2007, 17 (03) :333-353
[3]  
Bird R B., 2002, Transportphenomena
[4]   Mass and heat transfer during water evaporation in laminar flow inside a rectangular channel - validity of heat and mass transfer analogy [J].
Boukadida, N ;
Ben Nasrallah, S .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2001, 40 (01) :67-81
[5]   Liquid film condensation from water vapour flowing downward along a vertical tube [J].
Charef, Adil ;
Feddaoui, M'barek ;
Najim, Monssif ;
Meftah, Hicham .
DESALINATION, 2017, 409 :21-31
[6]   Experimental and numerical study of mixed convection heat and mass transfer in a vertical channel with film evaporation [J].
Cherif, A. S. ;
Kassim, M. A. ;
Benhamou, B. ;
Harmand, S. ;
Corriou, J. P. ;
Ben Jabrallah, S. .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2011, 50 (06) :942-953
[7]   EVAPORATION OF WATER INTO A LAMINAR STREAM OF AIR AND SUPERHEATED STEAM [J].
CHOW, LC ;
CHUNG, JN .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1983, 26 (03) :373-380
[8]  
Colburn AP, 1937, T AM INST CHEM ENG, V33, P0197
[9]  
Higbie R, 1935, T AM INST CHEM ENG, V31, P365
[10]   Laminar mixed convection heat and mass transfer in vertical rectangular ducts with film evaporation and condensation [J].
Huang, CC ;
Yan, WM ;
Jang, JH .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2005, 48 (09) :1772-1784