Chronopotentiometric Characterization of Electrodialysis Module

[1]Kołtuniewicz A.B., Drioli E.; Membranes in Clean Technologies, Theory and Practice, Wiley -VCH Verlag GmbH & Co. KGaA, Weinheim, 2008 Search in Google Scholar

[2]Koter S.; Ion-Exchange Membranes for Electrodialysis. A Patents Review, Recent Patents on Chemical Engineering, 2011, 4; p.141-16010.2174/1874478811104020141 Search in Google Scholar

[3]Block M., Kitchener J.A.; Polarization phenomena in commercial ion-exchange membranes, J. Electrochem. Soc., 1966, 113, p.947-95310.1149/1.2424162 Search in Google Scholar

[4]Brennen K.R., Hills G.J.; Chronopotentiometric evaluation of membrane performance, in: Biological Aspects of Electrochemistry, Vol.18 of the series Experientia Supplementum, G.Milazzo, P. Jones, L. Rampazzo (Eds.), Springer Basel AG, 1971; pp.183-19410.1007/978-3-0348-5848-9_13 Search in Google Scholar

[5]Gnusin N.P., Zabolotskii V.I., Shel’deshov N.V., Krikunova N.D.; Study of the bipolar membrane MB-1 in salt solutions by a chronopotentiometric method, Electrokhimiya, 1980, 21; p.152 Search in Google Scholar

[6]Audinos R., Pichelin G.; Characterization of electrodialysis membranes by chronopotentiometry, Desalination 68 (1988) p.251-263 Search in Google Scholar

[7]Taky M., Pourcelly G., Gavach C., Elmidaoui A.; Chronopotentiometric response of a cation exchange membrane in contact with chromium(III) solutions, Desalination, 1996, 105; p.219-22810.1016/0011-9164(96)00079-3 Search in Google Scholar

[8]Sistat P., Pourcelly G.; Chronopotentiometric response of an ion-exchange membrane In the underlimiting current-range. Transport phenomena within the diffusion layers, J. Membr. Sci., 1997, p.123, 121-13110.1016/S0376-7388(96)00210-4 Search in Google Scholar

[9]Długołęcki P., Anet B., Metz S.J., Nijmeijer K., Wessling M.; Transport limitations in ion exchange membranes at low salt concentrations, J. Membr. Sci., 2010, 346, p.163-17110.1016/j.memsci.2009.09.033 Search in Google Scholar

[10]Krol J.J., Wessling M., Strathmann H.; Chronopotentiometry and overlimiting ion transport through monopolar ion exchange membranes, J. Membr. Sci., 1999, 162, p.155-16410.1016/S0376-7388(99)00134-9 Search in Google Scholar

[11]Pawlowski S., Sistat P., Crespo J.G., Velizarov S.; Mass transfer in reverse electrodialysis: Flow entrance effects and diffusion boundary layer thickness, J. Membr. Sci., 2014, 471, p.72-8310.1016/j.memsci.2014.07.075 Search in Google Scholar

[12]Mitko K., Turek M.; Concentration distribution along the electrodialyzer, Desalination, 2014, 341, p.94-10010.1016/j.desal.2014.02.040 Search in Google Scholar

[13]Cowan D.A., Brown J.H.; Effect of turbulence on limiting current in electrodialysis cells, Industrial And Engineering Chemistry, 1959, 51(12), p.1445-144810.1021/ie50600a026 Search in Google Scholar

[14]Geraldes, V., Afonio M. D.; Limiting current density in the electrodialysis of multi-ionic solutions, J. Membr. Sci., 2010, 360(1-2), p.499-50810.1016/j.memsci.2010.05.054 Search in Google Scholar

[15]Koter, S., Chojnowska, P., Szynkiewicz, K., Koter, I.; Batch electrodialysis of ammonium nitrate and sulfate solutions, J. Membr. Sci., 2015, 496; p.219-22810.1016/j.memsci.2015.08.064 Search in Google Scholar

[16]Koter S.; Analysis of an electrodialysis unit on the basis of irreversible thermodynamics, Desalination, 1994, 95; p.139-15310.1016/0011-9164(94)00010-7 Search in Google Scholar