Model-based investigation of a heat pump driven, internally cooled liquid desiccant dehumidification system

被引:38
|
作者
Liu, Jun [1 ]
Zhang, Tao [1 ]
Liu, Xiaohua [1 ]
机构
[1] Tsinghua Univ, Dept Bldg Sci, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Liquid desiccant; Internally-cooled; Dehumidification; Heat pump; Heat and mass transfer; AIR-CONDITIONING SYSTEM; MASS-TRANSFER PROCESSES; PERFORMANCE; DEHUMIDIFIER/REGENERATOR;
D O I
10.1016/j.buildenv.2018.07.027
中图分类号
TU [建筑科学];
学科分类号
0813 ;
摘要
Liquid desiccant dehumidification system is regarded as a promising and energy-saving solution for dehumidification. A heat pump driven internally cooled desiccant dehumidification system is investigated in this paper. Dehumidifier and regenerator are both internally cooled/heated types compared to previous adiabatic ones, and heating and cooling capacities of a heat pump cycle are utilized for regeneration and dehumidification respectively. System model is established and validated to investigate system performance and effects of different influencing parameters. Its indicated that two main issues, which are restricting the system performance, are encountered, i.e. mismatching property among the three fluids inside the dehumidifier/regenerator and heat offset due to solutions circulating between dehumidifier and regenerator. Heat transfer mismatching ratio (x(t)) and mass transfer mismatching ratio (x(omega)) are defined to indicate the degree of mismatching property. A lower solution flow rate and a solution-solution heat exchanger with a better recovery efficiency are highly recommended to obtain a better system performance. Further, an improved system with external pre-cooler and pre-heater was proposed to improve the matching property among the three fluids, and COP(sys )is found to be increased from 5.96 to 6.68 with an increasing ratio of 12%. x(t) is found to be reduced from 0.357 to 0.168, and x(omega) from 0.282 to 0.127.
引用
收藏
页码:431 / 442
页数:12
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