Performance study of a solar-assisted hollow-fiber-membrane-based air humidification-dehumidification desalination system: Effects of membrane properties

被引:27
作者
Li, Guo-Pei [1 ]
Qi, Rong-hui [1 ]
Zhang, Li-Zhi [1 ,2 ]
机构
[1] South China Univ Technol, Sch Chem & Chem Engn, Educ Minist, Key Lab Enhanced Heat Transfer & Energy Conservat, Guangzhou 510640, Guangdong, Peoples R China
[2] South China Univ Technol, State Key Lab Subtrop Bldg Sci, Guangzhou 510640, Guangdong, Peoples R China
关键词
Desalination; Solar-assisted; Hollow fiber membrane; Heat and moisture transfer; Membrane characteristics; DISTILLATION-BASED DESALINATION; MASS-TRANSFER; THERMAL EFFICIENCY; COMPOSITE MEMBRANE; HEAT-EXCHANGERS; CHALLENGES; EQUATIONS; ENERGY; SCALE; COST;
D O I
10.1016/j.ces.2019.05.040
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hollow-fiber membrane humidifiers were used in solar-assisted and membrane-based air humidification-dehumidification desalination systems (SMHDD) because of their greater packing density and thus better transfer efficiency. A dynamic mathematical model containing the major components of this system was established, including the membrane humidifier, dehumidifier and solar heating unit. The model was validated with test data from an experimental platform where three kinds of membranes with different membrane thickness, heat conductivity, etc., were tested. To understand the role of membrane characteristics in the proposed desalination system, the effects of the membrane moisture diffusivity (D-m), heat conductivity (lambda(m)), membrane thickness (delta(m)) and membrane area (A(tot)) on the system performance were analyzed numerically. Of the three factors, D-m and A(tot) show the most significant effect on the accumulated freshwater production (AP) and coefficient of performance (COP), and the effects of delta(m) on the system performance are far less pronounced than that of D-m and delta(m). In summary, membranes with higher moisture diffusivity and smaller thickness can improve system performance without much attention to the heat conductivity. However, further raising D-m above 3.0 x 10(6) m(2)/s has a slight benefit to the performance improvement. Findings in this paper are useful in guiding the preparation of membranes used for application-scale membrane-based desalination systems operating in real-world environmental conditions. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:164 / 179
页数:16
相关论文
共 40 条
[1]   Potential of membrane distillation in seawater desalination: Thermal efficiency, sensitivity study and cost estimation [J].
Al-Obaidani, Sulaiman ;
Curcio, Efrem ;
Macedonio, Francesca ;
Di Profio, Gianluca ;
Ai-Hinai, Hilal ;
Drioli, Enrico .
JOURNAL OF MEMBRANE SCIENCE, 2008, 323 (01) :85-98
[2]   Effects of membrane properties on water production cost in small scale membrane distillation systems [J].
Ali, Mohamed I. ;
Summers, Edward K. ;
Arafat, Hassan A. ;
Lienhard, John H. .
DESALINATION, 2012, 306 :60-71
[3]   Membrane-distillation desalination: status and potential [J].
Alklaibi, AM ;
Lior, N .
DESALINATION, 2005, 171 (02) :111-131
[4]   Numerical simulation and experimental studies on heat and mass transfer using sweeping gas membrane distillation [J].
Charfi, K. ;
Khayet, M. ;
Safi, M. J. .
DESALINATION, 2010, 259 (1-3) :84-96
[5]   The relation of collector and storage tank size in solar heating systems [J].
Comakli, Kemal ;
Cakir, Ugur ;
Kaya, Mehmet ;
Bakirci, Kadir .
ENERGY CONVERSION AND MANAGEMENT, 2012, 63 :112-117
[6]   Analysis of a solar-powered membrane distillation system [J].
Ding, ZW ;
Liu, LY ;
El-Bourawi, MS ;
Ma, RY .
DESALINATION, 2005, 172 (01) :27-40
[7]  
Duffie J.A., 1974, SOLAR ENERGY THERMAL
[8]   Steady-state analysis of multi-stage flash desalination process [J].
ElDessouky, H ;
Shaban, HI ;
AlRamadan, H .
DESALINATION, 1995, 103 (03) :271-287
[9]   Technical review and evaluation of the economics of water desalination: Current and future challenges for better water supply sustainability [J].
Ghaffour, Noreddine ;
Missimer, Thomas M. ;
Amy, Gary L. .
DESALINATION, 2013, 309 :197-207
[10]  
GNIELINSKI V, 1976, INT CHEM ENG, V16, P359