Coupled heat and mass transfer characteristic in packed bed dehumidifier/regenerator using liquid desiccant

被引:47
作者
Liu, X. H. [1 ]
Jiang, Y. [1 ]
机构
[1] Tsinghua Univ, Sch Architecture, Dept Bldg Sci, Beijing 100084, Peoples R China
基金
高等学校博士学科点专项科研基金; 中国国家自然科学基金;
关键词
liquid desiccant; coupled heat and mass transfer; reachable handling region; flow pattern;
D O I
10.1016/j.enconman.2008.01.009
中图分类号
O414.1 [热力学];
学科分类号
摘要
. The dehumidifier and regenerator are two key components in liquid desiccant air conditioning systems. The heat transfer driving force and the mass transfer driving force influence each other, the air and desiccant outlet temperatures or humidity ratio may exceed the air and desiccant inlet parameters in the dehumidifier/regenerator. The uncoupled heat and mass transfer driving forces, enthalpy difference and relative humidity difference between the air and desiccant are derived based oil the available heat and mass transfer model and validated by the experimental and numerical results. The air outlet parameter reachable region is composed of the air inlet isenthalpic line, the desiccant inlet equivalent relative humidity line and the linkage of the air and desiccant inlet statuses. Except the mass flow rate ratio and the heat and mass transfer coefficients, the air and desiccant inlet statuses and flow pattern have great effects on the dehuimidifier/regenerator performance. The counter flow configuration expresses the best mass transfer performance in the dehumidifier and the hot desiccant driven regenerator, while the parallel flow configuration performs best in the hot air driven regenerator. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1357 / 1366
页数:10
相关论文
共 18 条
[1]   Improved thermodynamic property fields of LiBr-H2O solution [J].
Chua, HT ;
Toh, HK ;
Malek, A ;
Ng, KC ;
Srinivasan, K .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2000, 23 (06) :412-429
[2]   Comparison between random and structured packings for dehumidification of air by lithium chloride solutions in a packed column and their heat and mass transfer correlations [J].
Chung, TW ;
Ghosh, TK ;
Hines, AL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (01) :192-198
[3]   Comparison between spray towers with and without fin coils for air dehumidification using triethylene glycol solutions and development of the mass-transfer correlations [J].
Chung, TW ;
Wu, H .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (06) :2076-2084
[4]   Properties of aqueous solutions of lithium and calcium chlorides: formulations for use in air conditioning equipment design [J].
Conde, MR .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2004, 43 (04) :367-382
[5]   A PACKED-BED DEHUMIDIFIER-REGENERATOR FOR SOLAR AIR-CONDITIONING WITH LIQUID DESICCANTS [J].
FACTOR, HM ;
GROSSMAN, G .
SOLAR ENERGY, 1980, 24 (06) :541-550
[6]   Study of an aqueous lithium chloride desiccant system: Air dehumidification and desiccant regeneration [J].
Fumo, N ;
Goswami, DY .
SOLAR ENERGY, 2002, 72 (04) :351-361
[7]   CALCULATION OF HEAT AND MASS-TRANSFER COEFFICIENTS IN A PACKED TOWER OPERATING WITH A DESICCANT-AIR CONTACT SYSTEM [J].
GANDHIDASAN, P ;
KETTLEBOROUGH, CF ;
ULLAH, MR .
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME, 1986, 108 (02) :123-128
[8]   Experimental investigation of a LiCl-water open absorption system for cooling and dehumidification [J].
Gommed, K ;
Grossman, G ;
Ziegler, F .
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME, 2004, 126 (02) :710-715
[9]  
Li W. Y., 2000, ACTA ENERG SOLARIS S, V21, P391
[10]   Experimental investigation of the heat and mass transfer between air and liquid desiccant in a cross-flow regenerator [J].
Liu, X. H. ;
Jiang, Y. ;
Chang, X. M. ;
Yi, X. Q. .
RENEWABLE ENERGY, 2007, 32 (10) :1623-1636