Effect of membrane properties and operational parameters on systems for seawater desalination using computational fluid dynamics simulations

被引:15
作者
Alwatban, Anas M. [1 ,2 ]
Alshwairekh, Ahmed M. [1 ,2 ]
Alqsair, Umar F. [1 ,3 ]
Alghafis, Abdullah A. [1 ,2 ]
Oztekin, Alparslan [1 ]
机构
[1] Lehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
[2] Qassim Univ, Coll Engn, Mech Engn Dept, Qasim 52571, Saudi Arabia
[3] Prince Sattam Bin Abdulaziz Univ, Coll Engn, Mech Engn Dept, Alkharj 11942, Saudi Arabia
基金
美国国家科学基金会;
关键词
Membrane distillation; Desalination; Direct contact; Knudsen diffusion; Molecular diffusion; COMMERCIAL PTFE MEMBRANES; MASS-TRANSFER; DISTILLATION PROCESS; NUMERICAL-SIMULATION; WATER DESALINATION; CFD; TRANSPORT; MODULES; FLOW;
D O I
10.5004/dwt.2019.24275
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Computational fluid dynamic simulations were conducted to investigate the effects of the membrane properties and operational parameters on the system performance in three-dimensional direct contact membrane distillation modules. The membrane thickness, porosity, pore size, feed flow rate, and the inlet feed temperature were considered in the parametric study. Water flux, temperature and concentration polarization characteristics of the membrane were determined. The net-type spacers were used in the feed and permeate channel to mitigate the polarization and enhance the flux performance of the separation module for various flow rates. The laminar model was employed to characterize the velocity, temperature and concentration field in the empty channels and the k-co shear stress turbulence model was employed in the module containing spacers. The permeation flux, intensity of temperature and concentration polarization increase as the thickness is reduced, and the porosity and the pore size are increased. The rate of permeation and polarizations are increased with increase in flow rate. The presence spacers enhance the membrane flux performance more than 50% and mitigate polarizations up to 30%.
引用
收藏
页码:92 / 107
页数:16
相关论文
共 48 条
[21]   Direct contact membrane distillation (DCMD): Experimental study on the commercial PTFE membrane and modeling [J].
Hwang, Ho Jung ;
He, Ke ;
Gray, Stephen ;
Zhang, Jianhua ;
Moon, Il Shik .
JOURNAL OF MEMBRANE SCIENCE, 2011, 371 (1-2) :90-98
[22]   Water desalination cost literature: review and assessment [J].
Karagiannis, Ioannis C. ;
Soldatos, Petros G. .
DESALINATION, 2008, 223 (1-3) :448-456
[23]   Membranes and theoretical modeling of membrane distillation: A review [J].
Khayet, Mohamed .
ADVANCES IN COLLOID AND INTERFACE SCIENCE, 2011, 164 (1-2) :56-88
[24]   Membrane distillation [J].
Lawson, KW ;
Lloyd, DR .
JOURNAL OF MEMBRANE SCIENCE, 1997, 124 (01) :1-25
[25]   A review of reverse osmosis membrane materials for desalination-Development to date and future potential [J].
Lee, Kali Peng ;
Arnot, Tom C. ;
Mattia, Davide .
JOURNAL OF MEMBRANE SCIENCE, 2011, 370 (1-2) :1-22
[26]   Microporous polypropylene and polyethylene hollow fiber membranes. Part 3. Experimental studies on membrane distillation for desalination [J].
Li, JM ;
Xu, ZK ;
Liu, ZM ;
Yuan, WF ;
Xiang, H ;
Wang, SY ;
Xu, YY .
DESALINATION, 2003, 155 (02) :153-156
[27]   Study of advancement to higher temperature membrane distillation [J].
Luo, Aoyi ;
Lior, Noam .
DESALINATION, 2017, 419 :88-100
[28]   2-EQUATION EDDY-VISCOSITY TURBULENCE MODELS FOR ENGINEERING APPLICATIONS [J].
MENTER, FR .
AIAA JOURNAL, 1994, 32 (08) :1598-1605
[29]   A review on fouling of membrane distillation [J].
Naidu, Gayathri ;
Jeong, Sanghyun ;
Vigneswaran, Saravanamuthu ;
Hwang, Tae-Mun ;
Choi, Yong-Jun ;
Kim, Seung-Hyun .
DESALINATION AND WATER TREATMENT, 2016, 57 (22) :10052-10076
[30]   Review of membrane distillation process for water purification [J].
Pangarkar, B. L. ;
Deshmukh, S. K. ;
Sapkal, V. S. ;
Sapkal, R. S. .
DESALINATION AND WATER TREATMENT, 2016, 57 (07) :2959-2981