Computational study of sweeping gas membrane distillation process - Flux performance and polarization characteristics

被引:29
作者
Alqsair, Umar F. [1 ,2 ]
Alshwairekh, Ahmed M. [3 ]
Alwatban, Anas M. [3 ]
Oztekin, Alparslan [1 ]
机构
[1] Lehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
[2] Prince Sattam Bin Abdulaziz Univ, Coll Engn, Mech Engn Dept, Alkharj 11942, Saudi Arabia
[3] Qassim Univ, Coll Engn, Mech Engn Dept, Qasim 52571, Saudi Arabia
基金
美国国家科学基金会;
关键词
Sweeping gas membrane distillation; Vapor flux; Polarization; Module performance; Moisture polarization; SPACER-FILLED CHANNELS; MASS-TRANSFER; WATER DESALINATION; HEAT-TRANSFER; NUMERICAL-SIMULATION; WASTE-WATER; OSMOSIS; OPTIMIZATION; MODEL; FLOW;
D O I
10.1016/j.desal.2020.114444
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Computational fluid dynamics simulations were conducted in a three-dimensional sweeping gas membrane distillation (SGMD) desalination module. The module flux performance and polarization characteristics were investigated for a wide range of flow rates spanning the laminar and turbulent flow regime in the feed and permeate channel. The membrane was treated as a functional surface with zero thickness, and the membrane permeability was determined by a combination of Knudsen and molecular diffusion using the Dusty Gas model. The mathematical model and numerical method was validated against existing experimental work. It was shown that low membrane thickness, high porosity, and low tortuosity yield high vapor flux. It was demonstrated that high vapor flux can be achieved in a SGMD module by increasing the permeate flow rate to avoid temperature and moisture polarization in the permeate channel. By increasing the feed flow rate, the flux also increased, and temperature and concentration polarization decreased. It was shown that the SGMD process, as effective as other MD processes, could be used as an alternative method for water desalination. The model developed here can be utilized for design and optimization of full-scale SGMD modules.
引用
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页数:14
相关论文
共 90 条
[11]   Effect of membrane properties and operational parameters on systems for seawater desalination using computational fluid dynamics simulations [J].
Alwatban, Anas M. ;
Alshwairekh, Ahmed M. ;
Alqsair, Umar F. ;
Alghafis, Abdullah A. ;
Oztekin, Alparslan .
DESALINATION AND WATER TREATMENT, 2019, 161 :92-107
[12]   Continuous juice concentration by integrating forward osmosis with membrane distillation using potassium sorbate preservative as a draw solute [J].
An, Xiaochan ;
Hu, Yunxia ;
Wang, Ning ;
Zhou, Zongyao ;
Liu, Zhongyun .
JOURNAL OF MEMBRANE SCIENCE, 2019, 573 :192-199
[13]   An experimentally optimized model for heat and mass transfer in direct contact membrane distillation [J].
Andrjesdottir, Oloef ;
Ong, Chin Lee ;
Nabavi, Majid ;
Paredes, Stephan ;
Khalil, A. S. G. ;
Michel, Bruno ;
Poulikakos, Dimos .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2013, 66 :855-867
[14]  
Anqi A.E., PROC IDA WORLD C DES, DOI [DOI 10.13140/RG.2.1.4452.6565, 10.13140/RG.2.1.4452.6565.]
[15]  
Anqi AE, 2017, PROCEEDINGS OF THE ASME INTERNATIONAL MECHANICAL ENGINEERING CONGRESS AND EXPOSITION, 2016, VOL. 7
[16]   Exploitation of solar energy collected by solar stills for desalination by membrane distillation [J].
Banat, F ;
Jumah, R ;
Garaibeh, A .
RENEWABLE ENERGY, 2002, 25 (02) :293-305
[17]   Concentration of must through vacuum membrane distillation [J].
Bandini, S ;
Sarti, GC .
DESALINATION, 2002, 149 (1-3) :253-259
[18]   A DESALINATION PROCESS THROUGH SWEEPING GAS MEMBRANE DISTILLATION [J].
BASINI, L ;
DANGELO, G ;
GOBBI, M ;
SARTI, GC ;
GOSTOLI, C .
DESALINATION, 1987, 64 :245-257
[19]   Direct contact membrane distillation [J].
Burgoyne, A ;
Vahdati, MM .
SEPARATION SCIENCE AND TECHNOLOGY, 2000, 35 (08) :1257-1284
[20]   Membrane distillation for water desalination: how to chose an appropriate membrane? [J].
Cabassud, C ;
Wirth, D .
DESALINATION, 2003, 157 (1-3) :307-314