Natural convection liquid desiccant loop as an auxiliary air conditioning system: investigating the operational parameters

被引:10
作者
Fazilati, Mohammad Ali [1 ]
Alemrajabi, Ali Akbar [2 ]
Sedaghat, Ahmad [2 ]
机构
[1] Islamic Azad Univ, Khomeinishahr Branch, Dept Mech Engn, Khomeinishahr Isfahan, Iran
[2] Isfahan Univ Technol, Dept Mech Engn, Esfahan 8415683111, Iran
关键词
MASS-TRANSFER; HEAT; DEHUMIDIFICATION; MODEL; PERFORMANCE; EXCHANGER; FLOW;
D O I
10.1007/s00231-017-2191-4
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid desiccant air conditioning system with natural convection was presented previously as a new generation of AC systems. The system consists of two three-fluid energy exchangers namely absorber and regenerator in which the action of air dehumidifying and desiccant regeneration is done, respectively. The influence of working parameters on system performance including the heat source and heat sink temperature, concentration of desiccant solution fills the system initially and humidity content of inlet air to regenerator is investigated experimentally. The heat source temperatures of 50 degrees C and 60 degrees C, heat sink temperatures of 15 degrees C and 20 degrees C and desiccant concentrations of 30% and 34%, are examined here. The inlet air to regenerator has temperature of 38.5 degrees C and three relative humidity of 14%, 38% and 44%. In all experiments, the inlet air to absorber has temperature of 31 degrees C and relative humidity of 75%. By inspecting evaluation indexes of system, it is revealed that higher startup desiccant concentration solution is more beneficial for all study cases. It is also observed although the highest/lowest temperature heat source/heat sink is most suitable for best system operation, increasing the heat source temperature should be accompanied with decreasing heat sink temperature. Using drier air stream for regenerator inlet does not necessarily improve system performance; and the air stream with proper value of humidity content should be employed. Finally after running the system in its best working condition, the coefficient of performance (COP) reached 4.66 which verified to be higher than when the same air conditioning task done by a conventional vapor compression system, in which case the COP was 3.38.
引用
收藏
页码:903 / 913
页数:11
相关论文
共 16 条
[1]  
ASHRAE, 2008, HVAC SYST EQ HDB AIR, P10
[2]  
Bergman T.L., 2011, Introduction to Heat Transfer, DOI DOI 10.1016/J.APPLTHERMALENG.2011.03.022
[3]  
Erb B, 2009, ASHRAE T, V115
[4]   Performance of a run-around system for HVAC heat and moisture transfer applications using cross-flow plate exchangers coupled with aqueous lithium bromide [J].
Fan, HS ;
Simonson, CJ ;
Besant, RW ;
Shang, W .
HVAC&R RESEARCH, 2006, 12 (02) :313-336
[5]  
Fazilati MA, 2017, HEAT MASS TRANSFER, P1
[6]   Liquid desiccant air conditioning system with natural convection [J].
Fazilati, Mohammad Ali ;
Alemrajabi, Ali Akbar ;
Sedaghat, Ahmad .
APPLIED THERMAL ENGINEERING, 2017, 115 :305-314
[7]   Natural induced flow due to concentration gradient in a liquid desiccant air dehumidifier [J].
Fazilati, Mohammad Ali ;
Sedaghat, Ahmad ;
Alemrajabi, Ali Akbar .
APPLIED THERMAL ENGINEERING, 2016, 105 :105-117
[8]   Comparison of experimental data and a model for heat and mass transfer performance of a liquid-to-air membrane energy exchanger (LAMEE) when used for air dehumidification and salt solution regeneration [J].
Ge, Gaoming ;
Moghaddam, Davood Ghadiri ;
Abdel-Salam, Ahmed H. ;
Besant, Robert W. ;
Simonson, Carey J. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2014, 68 :119-131
[9]   Steady-state performance of a run-around membrane energy exchanger (RAMEE) for a range of outdoor air conditions [J].
Hemingson, Howard B. ;
Simonson, Carey J. ;
Besant, Robert W. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2011, 54 (9-10) :1814-1824
[10]   On the application of a membrane air-liquid contactor for air dehumidification [J].
Isetti, C ;
Nannei, E ;
Magrini, A .
ENERGY AND BUILDINGS, 1997, 25 (03) :185-193