Water Molecules and Electroconvection on Salt Ion Transport: History
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Electrodialysis has gained global recognition as a water purification method with the potential to enhance the overall efficiency of the purification process. The efficiency of electrodialysis depends strongly on the hydrodynamics of the process, as the advent of new high performance membranes on the world market removes the kinetic limitations associated with membranes and shifts the stage that determines the economic efficiency of desalination towards the liquid phase.
  • electrodialysis
  • desalting
  • electroconvection
  • dissociation/recombination of water molecules
  • quasi-stationary state

1. Introduction

Water stands out as humanity’s most vital resource and is crucial for all forms of life. However, at present, sustainable consumption is jeopardized in half of the world’s river basins [1]. The most precious form of water, clean drinking water, remains virtually inaccessible to around one billion people in developing countries.
The future scenario looks grim, not only due to climate change [2][3][4] but also because of the anticipated global population surge to 10 billion by 2050 and the rise in living standards accompanied by changing consumption patterns [5][6][7]. With a constrained supply of reliable drinking water, global water scarcity emerges as the foremost challenge for the world community [8]. The primary solution to address water scarcity involves economically and environmentally viable desalination methods [9][10].
Studies in recent years show that there are two approaches that reduce the mass transfer limitations on the electrolyte solution side [11][12]. The first is the use of spacers with which the flow of the solution can be controlled. Researchers have investigated this approach in researchers' study [13][14]. Secondly, the use of electroconvection under intense current modes. However, in this case, such destructive processes as the long-known dissociation reaction of water molecules and the recently discovered space charge breakdown [15][16] arise, which lead to the problem of a joint study of all these processes and their complex influence on salt ions.

2. Impact of the Dissociation/Recombination Reaction of Water Molecules on the Transport of Salt Ions

The papers [17][18] showed that the dissociation reaction of water molecules occurs intensively at current densities higher than the limiting one. Works by Sokirko and Harkatz [19][20] showed that the salt ion fluxes get exalted with the change of the electric field.
At the same time, in [21], it was first shown that the recombination reaction causes the appearance of a space charge region (SCR) in the central part of the desalination channel of the electrodialysis apparatus. The formation of SPZ in electrochemistry is associated with the presence of an interfacial boundary (solution/electrode or solution/ion exchange membrane). In [21], it was theoretically shown that H+ and OH ions move from the near-membrane regions to the central part of the channel, where a recombination zone appears, in which an SCR is formed from the terminal rate of the recombination reaction. The positive spatial charge of this SCR is due to the local excess of H+ ions moving away from the anion exchange membrane, and the negative spatial charge is due to the local excess of OH ions moving away from the anion exchange membrane and not having time to recombine due to the finiteness of the recombination reaction rate, although it is large. The dissociation reaction and formation of SCR in the recombination region affect the transport of salt ions as well as electroconvection. Moreover, a number of authors believe that the appearance of new charge carriers H+ and OH can lead to a decrease, or even disappearance of the space charge, which is the basis for other transport mechanisms, such as electroconvection.
Thus, accounting for the effect of the dissociation/recombination reaction of water molecules is important for understanding transport processes in electromembrane systems.

3. Effects of Electroconvection on Salt Ion Transport

During studies of super-limit transport, several interesting phenomena were discovered. One of them is electroconvection, the existence of which was proved experimentally and theoretically by Rubinstein and colleagues [22]. Electroconvection makes it possible to deliver “fresh” solutions from the center of the desalting channel to the membrane surface and to withdraw the desalinated solution from the membrane. It keeps a relatively high concentration of electrolytes at the membrane surface, which restrains the development of the process of generation of H+ and OH ions [23][24]. A smaller pH shift of the solution and its better mixing significantly reduce the rate of sludge formation in desalting and concentration chambers [25][26].
At present, electroconvection is the key mechanism of mass transfer intensification in EMS. Electroconvection also plays an important role in numerous microfluidic devices [27], such as electrokinetic micropumps [28], microconcentrators in analytical chemistry [29], shock electrodialysis [30][31], and others [32][33][34].
In the works of Rubinstein I. [35][36][37], Demekhin E.A., Kalaidin E.N. [38][39], the problems of occurrence and stability of electroconvection in micro- and nanofluidics in the absence of forced convection are investigated on the basis of mathematical modeling.
The works by Kwak R. [40], Pham V.S., Han J. [41], and others are devoted to the study of the patterns of transfer of salt ions taking into account electroconvection and the forced flow of solution. The peculiarity of electroconvection in the presence of forced convection is the presence of a different potential drop at which it occurs. In addition, electroconvection, which initially develops as a stable process, gradually becomes unstable with increasing potential drop, passing through a number of stages of bifurcations of electroconvective vortices and their interaction [42][43][44][45][46].
In [15][16], researchers first theoretically investigated the CVC characteristics for high current densities. The results show the presence of several modes of EMS operation associated with the development of electroconvective vortices arising near the cation exchange membrane (CEM) and subsequently near the anion exchange membrane (AEM). Then the vortices begin to actively interact, which leads to a breakdown of the space charge. Later vortices start to interact, which leads to space charge breakdown. This breakdown occurs when regions with positive and negative space charge detach from the membrane, move deep into the solution, meet, and their mutual neutralization occurs.
In [15][16], it was found that the effect of space charge breakdown restrains the development of electroconvective vortices, and leads to a decrease in the size and number of vortices in the breakdown region. This restrains a possible further increase in mass transfer due to electroconvection.
Thus, researchers have discovered a second limiting phenomenon at over limited current densities, which has never been analyzed before either experimentally or theoretically by simulations. The obtained results were published in [15][16].

4. Effects of Spacers on Salt Ion Transport

One of the effective methods to significantly increase the mass transport rate through membranes is the use of spacers, which allow the convective ion flux to be directed to the membrane surface [47][48][49].
Thus, the diffusion layer is significantly reduced in the channels with spacers and this leads to the current increase. This raises the question whether electroconvective vortices appear at high currents in such small diffusion layers.

This entry is adapted from the peer-reviewed paper 10.3390/membranes14010020

References

  1. Hoekstra, A.Y.; Wiedmann, T.O. Humanity’s unsustainable environmental footprint. Science 2014, 344, 1114–1117.
  2. Petersen, L.; Heynen, M.; Pellicciotti, F. Freshwater Resources: Past, Present, Future. Int. Encycl. Geogr. 2016, 3, 1–12.
  3. Dinar, A.; Tieu, A.; Huynh, H. Water scarcity impacts on global food production. Glob. Food Secur. 2019, 23, 212–226.
  4. UNESCO. UN-Water: United Nations World Water Development Report 2020: Water and Climate Change; UNESCO: Paris, France, 2020.
  5. Mekonnen, M.; Hoekstra, A.Y. Four billion people facing severe water scarcity. Sci. Adv. 2016, 2, e1500323.
  6. Gude, V.G. Desalination and water reuse to address global water scarcity. Rev. Environ. Sci. Bio/Technol. 2017, 16, 591–609.
  7. Djehdian, L.A.; Chini, C.M.; Marston, L.; Konar, M.; Stillwell, A.S. Exposure of urban food-energy-water (FEW) systems to water scarcity. Sustain. Cities Soc. 2019, 50, 101621.
  8. Jones, E.; Qadir, M.; van Vliet, M.T.; Smakhtin, V.; Kang, S.M. The state of desalination and brine production: A global outlook. Sci. Total Environ. 2019, 657, 1343–1356.
  9. Ali, A.; Tufa, R.A.; Macedonio, F.; Curcio, E.; Drioli, E. Membrane technology in renewable-energy-driven desalination. Renew. Sustain. Energy Rev. 2018, 81, 1–21.
  10. Tzanakakis, V.A.; Paranychianakis, N.V.; Angelakis, A.N. Water Supply and Water Scarcity. Water 2020, 12, 2347.
  11. Kim, B.; Kwak, R.; Kwon, H.J.; Pham, V.S.; Kim, M.; Al-Anzi, B.; Lim, G.; Han, J. Purification of High Salinity Brine by Multi-Stage Ion Concentration Polarization Desalination. Sci. Rep. 2016, 6, 31850.
  12. Joonhyeon, K.; Sangha, K.; Rhokyun, K. Controlling ion transport with pattern structures on ion exchange membranes in electrodialysis. Desalination 2021, 499, 114801.
  13. Kovalenko, A.; Evdochenko, E.; Stockmeier, F.; Köller, N.; Uzdenova, A.; Urtenov, M. Influence of spacers on mass transport in electromembrane desalination systems. J. Phys. Conf. Ser. 2021, 2131, 022011.
  14. Kovalenko, A.V.; Uzdenova, A.M.; Ovsyannikova, A.V.; Urtenov, M.H.; Bostanov, R.A. Mathematical modeling of the effect of spacers on mass transfer in electromembrane systems. J. Samara State Tech. Univ. Ser. Phys. Math. Sci. 2022, 26, 520–543.
  15. Kovalenko, A.V.; Wessling, M.; Nikonenko, V.V.; Mareev, S.A.; Moroz, I.A.; Evdochenko, E.; Urtenov, M.K. Space-Charge breakdown phenomenon and spatio-temporal ion concentration and fluid flow patterns in overlimiting current electrodialysis. J. Membr. Sci. 2021, 636, 119583.
  16. Kovalenko, A.; Chubyr, N.; Uzdenova, A.; Urtenov, M. Theoretical Investigation of the Phenomenon of Space Charge Breakdown in Electromembrane Systems. Membranes 2022, 12, 1047.
  17. Varentsov, V.K.; Pevnitskaya, M.V. Transfer of ions through ion-exchange membranes during electrodialysis. Izv. SO AS USSR. Ser. Chem. Sci. 1973, 4, 134–138.
  18. Kononov, Y.A.; Vrevskiy, B.M. The role of water dissociation products in the transfer of electric current through ionic membranes. Zhurn. Priklykl. Chem. 1971, 44, 929–932.
  19. Sokirko, A.V.; Harkatz, Y.I. To the theory of the migration current exaltation effect with consideration of water dissociation. Electrochemistry 1988, 24, 1657–1663.
  20. Kharkats, Y.I. About the mechanism of the forbidden currents occurrence on the ion-exchange membrane/electrolyte boundary. Electrochemistry 1985, 21, 974–977.
  21. Kovalenko, A.V.; Nikonenko, V.V.; Chubyr, N.O.; Urtenov, M.K. Mathematical modeling of electrodialysis of a dilute solution with accounting for water dissociation-recombination reactions. Desalination 2023, 550, 116398.
  22. Rubinstein, I.; Maletzki, F. Electroconvection at an electrically inhomogeneous permselective membrane surface. J. Chem. Soc. Faraday Trans. 1991, 87, 2079.
  23. Belova, E.I.; Lopatkova, G.Y.; Pismenskaya, N.D.; Nikonenko, V.V.; Larchet, C.; Pourcelly, G. The effect of anion-exchange membrane surface properties on mechanisms of overlimiting mass transfer. J. Phys Chem B 2006, 110, 13458–13469.
  24. Sharafan, M.V.; Zabolotskii, V.I.; Bugakov, V.V. Electric mass transport through homogeneous and surface-modified heterogeneous ion-exchange membranes at a rotating membrane disk. Rus. J. Electrochem. 2009, 45, 1162.
  25. Mikhaylin, S.; Nikonenko, V.; Pismenskaya, N.; Han, J.; Bazinet, L. How physico-chemical and surface properties of cation-exchange membrane affect membrane scaling and electroconvective vortices: Influence on performance of electrodialysis with pulsed electric field. Desalination 2016, 393, 102–114.
  26. Bazant, L.N.; Mikhaylin, S.; Bazinet, L. Voltage spike and electroconvective vortices generation during electrodialysis under pulsed electric field: Impact on demineralization process efficiency and energy consumption. Innov. Food Sci. Emerg. Technol. 2019, 52, 221–231.
  27. Bazant, M.Z.; Kilic, M.S.; Storey, B.D.; Ajdari, A. Towards an understanding of induced-charge electrokinetics at large applied voltages in concentrated solutions. Adv. Colloid Interface Sci. 2009, 152, 48–88.
  28. Olesen, L.H.; Bruus, H.; Ajdari, A. Ac electrokinetic micropumps: The effect of geometrical confinement, Faradaic current injection, and nonlinear surface capacitance. Phys. Rev. E 2006, 73, 056313.
  29. Wang, Y.-C.; Stevens, A.L.; Han, J. Million-fold preconcentration of proteins and peptides by nanofluidic filter. Anal. Chem. 2005, 77, 4293.
  30. Mani, A.; Bazant, M.Z. Deionization shocks in microstructures. Phys. Rev. E 2011, 84, 061504.
  31. Yaroshchuk, A. Over-limiting currents and deionization shocks in current-induced polarization: Local equilibrium analysis. Adv. Colloid Interface Sci. 2012, 183–184, 68–81.
  32. Sackmann, E.K.; Fulton, A.L.; Beebe, D.J. The present and future role of microfluidics in biomedical research. Nature 2014, 507, 181–189.
  33. Wessling, M.; de Jong, J.; Lammertink, R.G.H. Membranes and microfluidics: A review. Lab Chip. 2006, 6, 1125.
  34. Slouka, Z.; Senapati, S.; Chang, H.C. Microfluidic Systems with Ion-Selective Membranes. Annu. Rev. Anal. Chem. 2014, 7, 317.
  35. Rubinstein, I.; Zaltzman, B. Electro-osmotically induced convection at a permselective membrane. Phys. Rev. E 2000, 62, 2238–2251.
  36. Zaltzman, B.; Rubinstein, I. Electro-osmotic slip and electroconvective instability. J. Fluid Mech. 2007, 579, 173.
  37. Abu-Rjal, R.; Prigozhin, L.; Rubinstein, I.; Zaltzman, B. Equilibrium electro-convective instability in concentration polarization: The effect of non-equal ionic diffusivities and longitudinal flow. Russ. J. Electrochem. 2017, 53, 903–918.
  38. Demekhin, E.A.; Shelistov, V.S.; Polyanskikh, S.V. Linear and nonlinear evolution and diffusion layer selection in electrokinetic instability. Phys. Rev. E. 2011, 84, 1722036318.
  39. Demekhin, E.A.; Ganchenko, G.S.; Kalaydin, E.N. Transition to electrokinetic instability near imperfect charge-selective membranes. Phys. Fluids 2018, 30, 082006.
  40. Kwak, R.; Pham, V.S.; Lim, K.M.; Han, J. Shear ow of an electrically charged uid by ion concentration polarization: Scaling laws for electroconvective vortices. Phys. Rev. Lett. 2013, 110, 114501.
  41. Pham, S.V.; Kwon, H.; Kim, B.; White, J.K.; Lim, G.; Han, J. Helical vortex formation in three-dimensional electrochemical systems with ionselective Membranes. Phys. Review. E 2016, 93, 033114.
  42. Davidson, S.; Wessling, M.; Mani, A. On the Dynamical Regimes of Pattern-Accelerated Electroconvection. Sci. Rep. 2016, 6, 22505.
  43. Hernández-Pérez, L.; Martí-Calatayud, M.C.; Montañés, M.T.; Pérez-Herranz, V. Interplay between Forced Convection and Electroconvection during the Overlimiting Ion Transport through Anion-Exchange Membranes: A Fourier Transform Analysis of Membrane Voltage Drops. Membranes 2023, 13, 363.
  44. Kovalenko, A.V.; Yzdenova, A.M.; Sukhinov, A.I.; Chubyr, N.O.; Urtenov, M.K. Simulation of galvanic dynamic mode in membrane hydrocleaning systems taking into account space charge. AIP Conf. Proc. 2019, 2188, 050021.
  45. Uzdenova, A.M.; Kovalenko, A.V.; Urtenov, M.K.; Nikonenko, V.V. Theoretical Analysis of the Effect of Ion Concentration in Solution Bulk and at Membrane Surface on the Mass Transfer at Overlimiting Currents. Russ. J. Electrochem. 2017, 53, 1254–1265.
  46. Urtenov, M.K.; Kovalenko, A.V.; Sukhinov, A.I.; Chubyr, N.O.; Gudza, V.A. Model and numerical experiment for calculating the theoretical current-voltage characteristic in electro-membrane systems. IOP Conf. Ser. Mater. Sci. Eng. 2019, 680, 012030.
  47. Winograd, Y.; Solan, A.; Toren, M. Mass transfer in narrow channels in the presence of turbulence promoters. Desalination 1973, 13, 171–186.
  48. Kim, Y.; Walker, W.S.; Lawler, D.F. Electrodialysis with spacers: Effects of variation and correlation of boundary layer thickness. Desalination 2011, 274, 54–63.
  49. La Cerva, M.L.; Di Liberto, M.; Gurreri, L.; Tamburini, A.; Cipollina, A.; Micale, G.; Ciofalo, M. Coupling CFD with a one-dimensional model to predict the performance of reverse electrodialysis stacks. J. Memb. Sci. 2017, 541, 595–610.
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