Modelling and experiments of falling film break-up characteristics considering mass transfer for liquid desiccant dehumidification

被引:11
|
作者
Qi, Ronghui [1 ]
Dong, Chuanshuai [1 ]
Yu, Songning [1 ]
Zhang, Li-Zhi [1 ,2 ]
机构
[1] South China Univ Technol, Sch Chem & Chem Engn, Key Lab Enhanced Heat Transfer & Energy Conservat, Educ Minist, Guangzhou, Peoples R China
[2] South China Univ Technol, State Key Lab Subtrop Bldg Sci, Guangzhou, Peoples R China
基金
中国国家自然科学基金;
关键词
Liquid desiccant dehumidification; Falling film rupture; Analytical model; Mass transfer; Marangoni effect; Experiment; CO2; ABSORPTION; FLOW BEHAVIOR; FLAT-PLATE; PERFORMANCE; PATTERN;
D O I
10.1016/j.ijheatmasstransfer.2021.122027
中图分类号
O414.1 [热力学];
学科分类号
摘要
The falling film flow pattern and heat/mass transfer severely interact. Considering the unbalanced forces caused by liquid-gas mass transfer and Marangoni effect, this paper developed a theoretical model to predict the break-up characteristics of gas-liquid falling film convective absorption such as dehumidification. Analytical solutions were provided by calculating the uneven distribution of falling film parameters such as film thickness, interface temperature and concentration. Full consideration was also given to the influence of liquid film fluctuations and liquid-gas mass transfer coefficients that vary with operation and design conditions. Experiments of liquid desiccant dehumidification with LiCl saline aqueous were conducted for model validation. Though the model cannot reflect the volatility of film break-up positions, the trend was close and the error was less than 20% between the calculated and experimental results. Results showed that under absorbtion, except for the top of liquid film, the force caused by the surface tension difference due to liquid-gas mass transfer dominated, and its increase was most obvious as the flow distance increased. Liquid/solid friction was also significant, while gas/liquid shear force had little effect. Thus, since the upward force on film edge increased with the flow distance and mass transfer, where it was equal to gravity, the possibility of film rupture was very high (0.6-0.7 m in the conditions of this paper). All forces acting on the falling film increased, while the largest increment with liquid Re was liquid/solid friction and that with air Re was liquid/gas friction. Besides, reducing the liquid contact angle can efficiently relieve film rupture and enhance mass transfer, mainly by reducing the liquid/solid friction. This study provided a theoretical explanation for the coupling of falling film rupture and gas liquid mass transfer, which helps to improve the performance of dehumidification and other wetted-wall absorptions. (c) 2021 Elsevier Ltd. All rights reserved.
引用
收藏
页数:11
相关论文
共 50 条
  • [41] Critical falling heights for the first break-up of liquid drops impacting on immiscible liquids
    Lee, KY
    Lee, HG
    Hayes, PC
    ISIJ INTERNATIONAL, 1998, 38 (11) : 1242 - 1247
  • [42] Experimental investigations on heat and mass transfer performances of a liquid desiccant cooling and dehumidification system
    Ou, Xianhua
    Cai, Wenjian
    He, Xiongxiong
    Zhai, Deqing
    APPLIED ENERGY, 2018, 220 : 164 - 175
  • [43] Experimental study on mass transfer performances of the ultrasonic atomization liquid desiccant dehumidification system
    Yang, Zili
    Lin, Beibei
    Zhang, Kaisheng
    Lian, Zhiwei
    ENERGY AND BUILDINGS, 2015, 93 : 126 - 136
  • [44] Heat and Mass Transfer Characteristics of a Desiccant Dehumidification System Operating by Low Regeneration Temperature
    Yaningsih, Indri
    Wijayanta, Agung Tri
    Miyazaki, Takahiko
    HEAT TRANSFER ENGINEERING, 2022, 43 (19) : 1639 - 1651
  • [45] EFFECT OF MASS-TRANSFER ON DROP SIZE FROM JET BREAK-UP IN LIQUID-SYSTEMS
    NIEDZIALKOWSKI, W
    INZYNIERIA CHEMICZNA I PROCESOWA, 1993, 14 (02): : 279 - 292
  • [46] Theoretical Analysis and Numerical Simulation of Coupled Relationship of Heat and Mass Transfer between Air and Desiccant in Liquid Desiccant Dehumidification
    Huang, Zhijia
    Jiang, Ping
    PROCEEDINGS OF THE 8TH INTERNATIONAL SYMPOSIUM ON HEATING, VENTILATION AND AIR CONDITIONING, VOL 2: HVAC&R COMPONENT AND ENERGY SYSTEM, 2014, 262 : 829 - 839
  • [47] Level-set method for the modelling of liquid bridge formation and break-up
    Deganello, D.
    Williams, A. J.
    Croft, T. N.
    Lubansky, A. S.
    Gethin, D. T.
    Claypole, T. C.
    COMPUTERS & FLUIDS, 2011, 40 (01) : 42 - 51
  • [48] New mass transfer performance data of a cross-flow liquid desiccant dehumidification system
    Moon, C. G.
    Bansal, P. K.
    Jain, Sanjeev
    INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2009, 32 (03): : 524 - 533
  • [49] Dehumidification of air by chemical liquid desiccant in a packed column and its heat and mass transfer effectiveness
    Elsarrag, E
    HVAC&R RESEARCH, 2006, 12 (01): : 3 - 16
  • [50] An experimental study on the dehumidification performance of a low-flow falling-film liquid desiccant air-conditioner
    Bouzenada, S.
    McNevin, C.
    Harrison, S.
    Kaabi, A. N.
    6TH INTERNATIONAL CONFERENCE ON AMBIENT SYSTEMS, NETWORKS AND TECHNOLOGIES (ANT-2015), THE 5TH INTERNATIONAL CONFERENCE ON SUSTAINABLE ENERGY INFORMATION TECHNOLOGY (SEIT-2015), 2015, 52 : 796 - 803