Conjugate heat and mass transfer in membrane parallel-plates ducts for liquid desiccant air dehumidification: Effects of the developing entrances

被引:41
作者
Huang, Si-Min [1 ]
Zhang, Li-Zhi [2 ]
Yang, Minlin [1 ]
机构
[1] Dongguan Univ Technol, Dept Energy & Chem Engn, Key Lab Distributed Energy Syst Guangdong Prov, Dongguan 523808, Peoples R China
[2] S China Univ Technol, Sch Chem & Chem Engn, Key Lab Enhanced Heat Transfer & Energy Conservat, Educ Ministry, Guangzhou 510640, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
Conjugate heat and mass transfer; Membrane parallel-plates ducts; Liquid desiccant air dehumidification; Cross-flow; Developing entrances; ENTHALPY EXCHANGER; FLOW;
D O I
10.1016/j.memsci.2013.02.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Effects of the developing entrances on the fluid flow and conjugate heat and mass transfer in membrane-formed parallel-plates ducts used for liquid desiccant air dehumidification are investigated. The air and the liquid desiccant streams are separated by the semi-permeable membrane to prevent liquid droplets from crossing over. The two streams exchange heat and water vapor through the membrane in a cross-flow arrangement. In practical applications, due to the confinements in noises and pressure drops, the duct lengths are limited. The developing entrance lengths account for a large proportion of the duct lengths. Any assumption of either hydraulically fully developed, or thermally or/and concentrationally fully developed flow would underestimate performances seriously. In this study, a more accurate method is proposed. The equations governing the fluid flow and conjugate heat and mass transfer in the membrane ducts are established and solved directly considering the influences of the flow, and heat mass transfer developing entrances. The friction factors, Nusselt and Sherwood numbers along the duct lengths are obtained. The effects of the developing entrances on the fundamental data are investigated. Experimental work is conducted to validate the results. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:82 / 89
页数:8
相关论文
共 17 条
[1]   Temperature polarization in pervaporation [J].
Favre, E .
DESALINATION, 2003, 154 (02) :129-138
[2]   Experimental comparison and analysis on silica gel and polymer coated fin-tube heat exchangers [J].
Ge, T. S. ;
Dai, Y. J. ;
Wang, R. Z. ;
Peng, Z. Z. .
ENERGY, 2010, 35 (07) :2893-2900
[3]   Turbulent Heat and Mass Transfer Across a Hollow Fiber Membrane Tube Bank in Liquid Desiccant Air Dehumidification [J].
Huang, Si-Min ;
Zhang, Li-Zhi ;
Tang, Kai ;
Pei, Li-Xia .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 2012, 134 (08)
[4]   Fluid flow and heat mass transfer in membrane parallel-plates channels used for liquid desiccant air dehumidification [J].
Huang, Si-Min ;
Zhang, Li-Zhi ;
Tang, Kai ;
Pei, Li-Xia .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2012, 55 (9-10) :2571-2580
[5]  
Incropera FrankP., 2002, INTRO HEAT TRANSFER, V4th
[6]  
Kays W. M., 1990, CONVECTIVE HEAT MASS
[7]   The elastic and moisture transfer properties of polyethylene and polypropylene membranes for use in liquid-to-air energy exchangers [J].
Larson, Michael D. ;
Simonson, Carey J. ;
Besant, Robert W. ;
Gibson, Phillip W. .
JOURNAL OF MEMBRANE SCIENCE, 2007, 302 (1-2) :136-149
[8]   Dehumidification and humidification of air by surface-soaked liquid membrane module with triethylene glycol [J].
Li, Jinlong ;
Ito, Akira .
JOURNAL OF MEMBRANE SCIENCE, 2008, 325 (02) :1007-1012
[9]   Heat and mass transfer model of cross flow liquid desiccant air dehumidifier/regenerator [J].
Liu, X. H. ;
Jiang, Y. ;
Qu, K. Y. .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (02) :546-554
[10]   Performance testing of a counter-cross-flow run-around membrane energy exchanger (RAMEE) system for HVAC applications [J].
Mahmud, Khizir ;
Mahmood, Gazi I. ;
Simonson, Carey J. ;
Besant, Robert W. .
ENERGY AND BUILDINGS, 2010, 42 (07) :1139-1147