Effect of module design and flow patterns on performance of membrane distillation process

被引:49
作者
Ali, A. [1 ,2 ,4 ]
Aimar, P. [4 ,6 ]
Drioli, E. [1 ,2 ,3 ,5 ]
机构
[1] Univ Calabria, Natl Res Council, Inst Membrane Technol ITM CNR, I-87036 Arcavacata Di Rende, CS, Italy
[2] Univ Calabria, Dept Chem Engn & Mat, I-87036 Arcavacata Di Rende, CS, Italy
[3] Hanyang Univ, WCU Energy Engn Dept, Seoul 133791, South Korea
[4] Univ Toulouse, INPT, UPS, Lab Genie Chim, F-31062 Toulouse, France
[5] KAU CEDT, Jeddah, Saudi Arabia
[6] CNRS, Lab Genie Chim, F-31062 Toulouse, France
关键词
Hollow fiber configurations; Flow patterns; Membrane distillation; Energy efficiency; Packing density; Enhancement factors; MASS-TRANSFER IMPROVEMENT; DEAN VORTICES; HEAT-TRANSFER; FLUX ENHANCEMENT; SECONDARY FLOWS; PULSATING FLOW; PART I; ULTRAFILTRATION; WATER; CHANNEL;
D O I
10.1016/j.cej.2015.04.108
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The present study highlights the effect of different hollow fiber membrane configurations and flow patterns on performance of membrane distillation (MD) process. The modules with helical and wavy conformations have been tested under various hydrodynamic conditions and their performance has been compared with conventional straight fiber modules. The effect of flow patterns has been studied by applying the intermittent and pulsating flows to straight hollow fiber membranes. A flux enhancement of 47% and 52% with respect to the straight fibers has been observed for helical and wavy configurations, respectively, though packing density of such modules is significantly less than their straight counterparts. For intermittent flow, an improvement of 30% has been recorded. The difference is more prominent at low flow rates and approaches to the straight fiber performance under steady flow at high Reynolds numbers (Re) for all hollow fiber configurations and flow patterns studied. The intermittent flow and wavy fibers exhibit an energy efficiency enhancement of 180% and 90% over their conventional counter parts, respectively. In terms of surface and volume based enhancement factor and packing density, intermittent and pulsating flow exhibited the most optimal performance. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:368 / 377
页数:10
相关论文
共 50 条
[31]   Experimental characterization of the temperature gradient inside a membrane distillation module [J].
Dalle, Marie-Alix ;
Janasz, Filip ;
Leyer, Stephen .
ENERGY REPORTS, 2022, 8 :7870-7883
[32]   PERFORMANCE ANALYSIS OF THE DIRECT CONTACT MEMBRANE DISTILLATION USING SONICATION EFFECT [J].
Ali, Ussama ;
Sajjad, Muhammad ;
Janajreh, Isam .
PROCEEDINGS OF ASME 2021 INTERNATIONAL MECHANICAL ENGINEERING CONGRESS AND EXPOSITION (IMECE2021), VOL 1, 2021,
[33]   Distillate flux enhancement of the concentric circular direct contact membrane distillation module with spiral wired flow channel [J].
Ho, Chii-Dong ;
Chen, Luke ;
Tsai, Feng-Chi ;
Lin, Guan-Hong ;
Lim, Jun-Wei .
JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2019, 94 :70-80
[34]   Investigation of different hollow fiber module designs for flux enhancement in the membrane distillation process [J].
Teoh, May May ;
Bonyadi, Sina ;
Chung, Tai-Shung .
JOURNAL OF MEMBRANE SCIENCE, 2008, 311 (1-2) :371-379
[35]   A review on membrane distillation in process engineering: design and exergy equations, materials and wetting problems [J].
Capizzano, Stefano ;
Frappa, Mirko ;
Macedonio, Francesca ;
Drioli, Enrico .
FRONTIERS OF CHEMICAL SCIENCE AND ENGINEERING, 2022, 16 (05) :592-613
[36]   Enhanced Performance of Membrane Distillation Using Surface Heating Process [J].
Han, Fei ;
Liu, Shuxun ;
Wang, Kang ;
Zhang, Xiaoyuan .
MEMBRANES, 2021, 11 (11)
[37]   CFD simulation of a membrane distillation module channel [J].
Cipollina, A. ;
Di Miceli, A. ;
Koschikowski, J. ;
Micale, G. ;
Rizzuti, L. .
DESALINATION AND WATER TREATMENT, 2009, 6 (1-3) :177-183
[38]   Performance comparison between overlapped and woven spacers for membrane distillation [J].
Gurreri, Luigi ;
Tamburini, Alessandro ;
Cipollina, Andrea ;
Micale, Giorgio ;
Ciofalo, Michele .
DESALINATION AND WATER TREATMENT, 2017, 69 :178-189
[39]   Performance comparison of rotating disk ultrafiltration membrane module, a high shear device with cross-flow module [J].
Dutta, Suman ;
Sarkar, Projjwal ;
Bhattacharjee, Chiranjib ;
Datta, Siddhartha .
INTERNATIONAL JOURNAL OF ENVIRONMENT AND POLLUTION, 2012, 49 (3-4) :197-209
[40]   Determination of membrane properties for use in the modelling of a membrane distillation module [J].
Guijt, CM ;
Rácz, IG ;
Reith, T ;
de Haan, AB .
DESALINATION, 2000, 132 (1-3) :255-261