Controlling ion transport with pattern structures on ion exchange membranes in electrodialysis

被引:22
作者
Kim, Joonhyeon [1 ]
Kim, Sangha [1 ]
Kwak, Rhokyun [1 ,2 ]
机构
[1] Hanyang Univ, Dept Mech Convergence Engn, Seoul, South Korea
[2] Hanyang Univ, Inst Nano Sci & Technol, Seoul, South Korea
基金
新加坡国家研究基金会;
关键词
Electrodialysis; Electroconvection; Spacer; Ion exchange membrane; Patterned membrane; SPACER-FILLED CHANNELS; OF-THE-ART; REVERSE-ELECTRODIALYSIS; MASS-TRANSFER; DESALINATION; ELECTROCONVECTION; OPTIMIZATION; PERFORMANCE; SYSTEMS; DESIGN;
D O I
10.1016/j.desal.2020.114801
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In electrodialysis (ED), ion transport through ion exchange membranes governs its desalination performance. In this paper, we decipher the effects of non-conductive pattern structures on the membrane in ED and identify two factors to control conductive/convective ion transports: i) electric "view factor" (deduced from the analogy of view factor of radiative heat flux) representing the possibility of ion conduction, and ii) vortex intensity representing the strength of ion convection. To do this, we build a two-dimensional ED platform with six different pattern structures on the membrane, and then visualize in situ ion concentration and fluid flow over these patterns in Ohmic, limiting, and overlimiting current regimes. In the Ohmic-limiting regime (V 2 V), the electric view factor determines current, Ohmic conductance, and salt removal. In the overlimiting regime (V 2 V), electroconvection (EC) occurs on the membranes, so the vortex intensity of EC determines current and salt removal. Moreover, overlimiting conductance can be predicted by the density of this vortex intensity. Lastly, taken together, we develop new scaling law for the electric Nusselt number, which presents the degree of ion convection vs. ion conduction, as a function of the pattern shape and EC strength.
引用
收藏
页数:10
相关论文
共 45 条
[1]   Multi-layer spacer geometries with improved mass transport [J].
Balster, J. ;
Punt, I. ;
Stamatialis, D. F. ;
Wessling, A. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 282 (1-2) :351-361
[2]   EXPERIMENTAL STUDY OF ELECTRODIALYSIS HYDRODYNAMICS [J].
BELFORT, G ;
GUTER, GA .
DESALINATION, 1972, 10 (03) :221-&
[3]   Static turbulence promoters in cross-flow membrane filtration: a review [J].
Bhattacharjee, Chiranjit ;
Saxena, V. K. ;
Dutta, Suman .
CHEMICAL ENGINEERING COMMUNICATIONS, 2020, 207 (03) :413-433
[4]   Electrodialysis for water desalination: A critical assessment of recent developments on process fundamentals, models and applications [J].
Campione, A. ;
Gurreri, L. ;
Ciofalo, M. ;
Micale, G. ;
Tamburini, A. ;
Cipollina, A. .
DESALINATION, 2018, 434 :121-160
[5]  
Cengel YunusA., 2020, HEAT MASS TRANSFER F
[6]   SPACER CHARACTERIZATION AND PRESSURE-DROP MODELING IN SPACER-FILLED CHANNELS FOR ULTRAFILTRATION [J].
DACOSTA, AR ;
FANE, AG ;
WILEY, DE .
JOURNAL OF MEMBRANE SCIENCE, 1994, 87 (1-2) :79-98
[7]   On the Dynamical Regimes of Pattern-Accelerated Electroconvection [J].
Davidson, Scott M. ;
Wessling, Matthias ;
Mani, Ali .
SCIENTIFIC REPORTS, 2016, 6
[8]   Ion conductive spacers for increased power generation in reverse electrodialysis [J].
Dlugolecki, Piotr ;
Dabrowska, Joanna ;
Nijmeijer, Kitty ;
Wessling, Matthias .
JOURNAL OF MEMBRANE SCIENCE, 2010, 347 (1-2) :101-107
[9]   Statistical analysis of electroconvection near an ion-selective membrane in the highly chaotic regime [J].
Druzgalski, Clara ;
Mani, Ali .
PHYSICAL REVIEW FLUIDS, 2016, 1 (07)
[10]   Unsteady flows with mass transfer in narrow zigzag spacer-filled channels: A numerical study [J].
Fimbres-Weihs, G. A. ;
Wiley, D. E. ;
Fletcher, D. F. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (19) :6594-6603