Method Article

Generation and Control of Electrohydrodynamic Flows in Aqueous Electrolyte Solutions

DOI:

10.3791/57820

⸱

September 7th, 2018

 ,  ,  ,  , 
1Department of Mechanical Science and Bioengineering, Graduate School of Engineering Science, Osaka University, 2Division of Mechanical Science and Technology, Faculty of Science and Technology, GUNMA University

In This Article

Summary

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The rectification of ion transport pathways is an effective method to generate one-directional ion-dragged electrohydrodynamic flows. By setting an ion-exchange membrane in a flow channel, an electrically polarized condition is generated and causes a liquid flow to be driven when an electric field is externally applied.

Abstract

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To drive electrohydrodynamic (EHD) flows in aqueous solutions, the separation of cation and anion transport pathways is essential because a directed electric body force has to be induced by ionic motions in liquid. On the other hand, positive and negative charges attract each other, and electroneutrality is maintained everywhere in equilibrium conditions. Furthermore, an increase in an applied voltage has to be suppressed to avoid water electrolysis, which causes the solutions to become unstable. Usually, EHD flows can be induced in non-aqueous solutions by applying extremely high voltages, such as tens of kV, to inject electrical charges. In this study, two methods are introduced to generate EHD flows induced by electrical charge separations in aqueous solutions, where two liquid phases are separated by an ion-exchange membrane. Due to a difference in the ionic mobility in the membrane, ion concentration polarization is induced between both sides of the membrane. In this study, we demonstrate two methods. (i) The relaxation of ion concentration gradients occurs via a flow channel that penetrates an ion-exchange membrane, where the transport of the slower species in the membrane selectively becomes dominant in the flow channel. This is a driving force to generate an EHD flow in the liquid. (ii) A long waiting time for the diffusion of ions passing through the ion-exchange membrane enables the generation of an ion-dragged flow by externally applying an electric field. Ions concentrated in a flow channel of a 1 x 1 mm2 cross-section determine the direction of the liquid flow, corresponding to the electrophoretic transport pathways. In both methods, the electric voltage difference required for an EHD flow generation is drastically reduced to near 2 V by rectifying the ion transport pathways.

Introduction

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Recently, liquid flow control techniques have attracted much attention because of interest in the applications of micro- and nanofluidic devices1,2,3,4,5,6,7,8,9,10,11,12,13,14,15. In polar solutions, such as aqueous solutions and ionic liquids, ions and electrically charged particles usually bring about electrical charges in liquid flows. The transport of such polarized particles provides an expansion of various applications, such as single-molecule manipulation6,10,11,13,14,15,16,17, ion diode devices12,18, and liquid flow control19,20,21,22. EHD flow has been an applicable phenomenon for liquid flow control systems since Stuetzer1,2 invented the ion drag pump. Melcher and Taylor3 published an important article in which the theoretical framework of EHD flow was well reviewed and some outstanding experiments were also demonstrated. Saville4 and his coworkers23,24 contributed to the following expansion of EHD technologies in liquids. However, there were some limitations to inducing liquid flows driven by electric forces, because tens of kV have to be applied in liquids to inject electrical charges in non-polar solutions, such as oils, to polarize them1,2,3. This is a disadvantage for aqueous solutions because the water electrolysis that is induced by an electric potential higher than 1.23 V changes the characteristics of solutions and makes the solutions unstable.

In micro- and nanofluidic channels, surface charges of channel walls cause the concentration of counterions that effectively induce electroosmotic flows (EOFs) under externally applied electric fields25,26,27,28,29. Using EOFs, some liquid pumping techniques have been applied in aqueous solutions, reducing the electric voltages30,31,32. On the other hand, EOFs are limited to being generated in micro- and nanospaces in which surface areas become more dominant than liquid volumes. Furthermore, depending on the transport of highly concentrated ions very near the wall surfaces, such as in electric double layers, the slip boundary only causes the liquid flow, which may not be sufficient to make pressure gradients7,8,22,26,27. Fine tuning, such as to channel dimensions and salt concentrations, is required for the applications of EOF. In contrast, EHD flows driven by body forces seem to be available to transport masses and energies if the application voltages can be reduced to avoid degrading solvents. Recently, some researchers have suggested applications of EHD flows with low voltages33,34,35,36. Although these technologies have not yet been implemented, the frontiers are expected to expand.

In previous studies, we also conducted experimental and theoretical work on EHD flows in aqueous solutions37,38,39,40. It was supposed that the rectification of ion transport pathways was effective to generate electrically charged solutions that cause electric body forces under electric fields. By using an ion-exchange membrane and a flow channel crossing the membrane, we were able to rectify ionic currents. When applying an anion-exchange membrane, cations concentrated in the flow channel dragged the solvents and developed an EHD flow37,38,39. A difference in the mobility of ion species was an important factor when separating the cationic and anionic currents. Ion-exchange membranes effectively worked to modulate the mobility due to the ion selectivity. Ion transport phenomena were also investigated from the viewpoint of ionic current density influenced by applied electric fields41. These studies have been fruitful for developing manipulation techniques for single molecules, namely, micro- and nanoparticles, whose motions are strongly affected by thermal fluctuations11,16,17. EOFs and EHD flows are expected to expand the variety of precise flow control methods as well as pressure gradients.

In this study, we demonstrate two methods to drive EHD flows in aqueous solutions. First, an NaOH solution is used for a working fluid to drive an EHD flow37,38,39. An anion-exchange membrane separates the liquid into two parts. A polydimethylsiloxane (PDMS) flow channel with a cross-section of 1 x 1 mm and a length of 3 mm penetrates the membrane. By applying an electric potential of 2.2 V, the electrophoretic transport of Na+, H+, and OH− ions is induced along the electric fields. An anion-exchange membrane and a flow channel effectively work to separate the ion transport pathways, where anions dominantly pass through the membrane and cations concentrate in the flow channel, although both species usually move in opposite directions, maintaining the electroneutrality. Thus, such a condition does not cause a driving force for liquid flows. This structure is crucial to generating an EHD flow whose flow speed reaches on the order of 1 mm/s in the channel because highly concentrated cations accelerated by external electric fields drag solvent molecules. EHD flows are observed and recorded by using a microscope and a high-speed camera as shown in Figure 1. Second, a concentration difference between two liquid phases separated by an ion-exchange membrane causes an electrically polarized condition to be generated crossing an ion-exchange membrane40. In this study, we find the importance of a considerable waiting time to equilibrate ion distributions and a corresponding electric potential, which cause preferable conditions to apply to a body force in a liquid. Crossing the ion-exchange membrane, a weakly polarized condition is achieved. In such a condition, an externally applied electric field induces directional ion transport that generates a body force in a liquid, and as a result, the momentum transfer from the ions to the solvent develops an EHD flow.

As mentioned above, the present devices succeed in drastically decreasing the applied voltage difference to a few volts, and thus this method is can be used for aqueous solutions, although the conventional electrical charge injection methods required tens of kV and are limited to an application to non-aqueous solutions.

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Protocol

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1. EHD Flow Induced by Rectified Ion Transport

  1. Development of a flow channel device to rectify ion transport pathways
    1. Make a PTFE mold of the reservoir:
      1. Cut a 13 x 30 x 10 mm3 mold from a polytetrafluoroethylene (PTFE) block using a milling machine (see Figure 2). Alternatively, purchase a custom-made product.
      2. Adhere acrylic plates of 15 x 18 x 1 mm3 at both ends of the PTFE mold with a plastic adhesive, which will make slits in the reservoir to settle the bias electrodes. These parts can be cut out from a large plate or purchased.
      3. Adhere the acrylic plates of 13 x 30 x 1 mm3 at the top and bottom surfaces of the PTFE mold with a plastic adhesive to make planar surfaces for clear observation.
    2. Mix a silicone elastomer base and curing agent in the ratio of 10:1 in a 50 mL tube and shake the tube by hand.
    3. Settle the liquid PDMS in a vacuum vessel and degas it by using a rotary pump.
    4. Remove the tube from the vessel. Pour the PDMS into a 40 x 50 x 24 mm3 plastic vessel to mold the outer shape of the reservoir and place the reservoir mold (see step 1.1.1) in it.
    5. Bake the whole body of the liquid PDMS on a hotplate at 80 °C for about 4 h.
    6. After the bake, isolate the PDMS reservoir from the PTFE mold and the outer vessel by hand. Make a slit across the center of the reservoir by using a surgical knife. This will be used to put the edges of an anion-exchange membrane (prepared in step 1.1.16) into it using tweezers.
      NOTE: The PDMS reservoir is filled with electrolyte solutions later, as shown in Figure 2.
    7. Obtain glass plates (made by special order) with a circular shape of 18 mm in diameter or in a square with 18 mm edges.
    8. Wash the glass plates by soaking them in acetone, ethanol, and pure water (in that order) in an ultrasonication bath for 15 min each.
    9. Blow any residual liquids away with an air gun or heat the glass plates with a hotplate for 5 min at about 473 K.
    10. Using radio frequency sputtering, coat the glass surface with Cr or Ti exposed to Ar plasma for 1 min at 75 W and successively, deposit an Au thin film for 5 min at 75 W, setting the thickness at approximately 100 nm.
      NOTE: Before coating the glass surface with the target metals, the samples were set in a vacuum chamber that was evacuated with a rotary pump and a molecular diffusion pump until the pressure decreased to 1 x 10−2 Pa.
    11. Solder a lead on the Au electrode surface using a soldering iron.
      NOTE: The shape of the Au electrode may possibly be replaced by squares and helical wires, maintaining surface areas large enough to generate ionic currents.
    12. With tweezers, set the glass plates coated with an Au thin film at both ends of the reservoir. These are the bias electrodes.
    13. Cut an anion-exchange membrane into a rectangular shape of 20 x 18 mm2 by using scissors. A surface area of 13 mm in width and 10 mm in height is exposed to a liquid. Here, a box cutter or surgical knife may also be used to cut the membrane.
    14. Cut out a rectangular piece of 3 x 5.5 mm2 from one edge of the membrane with scissors.
      NOTE: The thickness of the anion-exchange membrane is 220 µm. The membrane is easily cut with scissors or a box cutter. The edges of the membrane are partly fixed with the slits in the chamber.
    15. Solidify a PDMS block with a stainless rod of a 1 x 1 mm2 cross-section in the same way as in steps 1.1.4 - 1.1.5, to create a flow channel that penetrates the membrane. Leave the construction overnight and then pull the stainless rod out of the PDMS block.
    16. Cut the PDMS block with a square flow channel into a 3 x 6 x 4.5 mm piece (see Figure 2) using a surgical knife. Make slits along the outer edges, then attach it to the membrane within the rectangular cutout.
      NOTE: The top face of the channel has to be set horizontally for a clear observation of the particles in the flow channel via the transparent wall.
  2. Preparation of solutions and pretreatments for experiments
    1. Prepare NaOH aqueous solutions at concentrations of 1 x 10−1, 1 x 10−2, and 1 x 10−3 mol/L by diluting the stock solution.
    2. Make a dispersion of polystyrene particles of 2.93 µm on average in diameter in each of the NaOH solutions prepared in step 1.2.1 by setting the concentration to 4.2 x 10−3 vol%.
      NOTE: The size of the tracer particles may be changed appropriately to improve observability.
    3. Ultrasonicate the formatted anion-exchange membrane of 20 x 18 mm2 with a slit of 3 x 5.5 mm2 2x for 10 min in pure water at a power of 100 W.
    4. With tweezers, set the anion-exchange membrane with the PDMS flow channel into the PDMS reservoir. Fill the reservoir with 4 mL of NaOH solution using a micropipette.
      NOTE: The membrane surface and flow channel are immersed in the solution, where the membrane surface exposed to the solution is at least 100x larger than the cross-section of the flow channel.
    5. Apply an electric potential of 2.2 V by using a DC power source in forward and backward directions for 2 h each in series, to improve the conductivity of the membrane before observation.
    6. Pull the Au electrodes out with tweezers. Remove the solution from the reservoirs using a micropipette.
    7. Set new Au electrodes in the reservoirs with tweezers. Fill the reservoirs with 4 mL of NaOH solution using a micropipette. Start observations when the solution is equilibrated.
      NOTE: It may take a few minutes of waiting time until the natural convection settles down, which can be judged by observing the behavior of tracer particles.
  3. Experimental setup and measurement systems
    1. Set the frame rate and the exposure time of a high-speed complementary metal-oxide-semiconductor (CMOS) camera to 500 fps and 1 ms, respectively.
      NOTE: As shown in Figure 1, the experimental device is set on the stage of a microscope connected to a high-speed CMOS camera to record the particle motions. The view is magnified in a 15 in monitor with a 100X lens.
    2. Remove any bubbles from the channel by inserting the tip of a micropipette into the channel end to push or pull out them, before applying an electric potential.
    3. Externally apply an electric potential of 2.2 V to the Au bias electrodes. Simultaneously monitor the electrical responses by using a potentiostat or a DC power source with a digital multimeter.
      NOTE: The voltage value is determined to be the upper limit, avoiding the water electrolysis that generates O2 and H2 bubbles in the solution.
    4. Record the behavior of the tracer particles on the computer.
    5. Measure an electric potential difference between both ends of the flow channel by using Au probe electrodes and a digital multimeter to confirm that the concentration gradient of ions triggers an EHD flow38,39.
    6. Determine the origin of the Cartesian coordinate system at the center of the channel.
      NOTE: The x-axis is along the longitudinal direction of the flow channel, and the y- and z-axes are in the horizontal and vertical directions in the cross-section of the channel, respectively, as shown in Figure 2. The transparent PDMS channel allows liquid flows to be visualized along the x-axis. The view is focused on the xy plane at z = 0 by controlling the depth of focus. The flow data are independent of x in the test section except just near the inlet and outlet of the channel, and the observation point is set at approximately 0.75 mm downstream from the origin, such that x = 0.75, y = 0, and z = 0 mm.
    7. After a single measurement (of 15 s), short-circuit the electrodes by connecting them to each other with a lead for 20 min until the solution is equilibrated.
    8. Next, move the entirety of the solution to another vessel (e.g., a 10 mL sample bottle) and stir it with a micropipette.
    9. Pour the stirred solution into the chamber again using a micropipette when iteratively performing the experiment.
      NOTE: After observation, the EHD flow velocity is evaluated by using the particle image velocimetry (PIV) method39, which can be done by using the appropriate software to trace the displacement of particles and numerically evaluate the velocity. A detailed explanation of PIV methods and how to use them is omitted here because PIV analyses have been widely used and the procedures of computations depend on the software and operating system that is being used.

2. Observation of Cation-induced EHD Flows

  1. Development of experimental device
    1. Form Au bias electrodes with a 26 x 10 mm2 surface on the bottom glass plate according to procedures similar to those previously described in steps 1.1.5 - 1.1.7.
    2. Using radio frequency sputtering, coat a glass surface with Cr or Ti exposed to Ar plasma for 2 min at 75 W and deposit an Au thin film for 5 min at 75 W.
      NOTE: This shape of electrode is determined in order to highly concentrate electric fields in the narrowest channel region. The ratio of the electrode surface, whose area of 10 x 10 mm2 is exposed to a liquid, to the cross-section of the channel is ideally 100:1; this ratio is predicted to be sufficient to drop the electric potential at the channel by a large amount16.
    3. Solder a lead line at an edge of the electrodes by using a soldering iron.
    4. From a large silicone rubber sheet, cut out 2 chambers, each made of a 1 x 1 x 1 mm3 flow channel placed between two 10 x 10 x 1 mm3 reservoirs, using a surgical knife (see Figure 3). These parts may be replaced by PDMS.
    5. Cut out a cation-exchange membrane with an average thickness of 127 µm to 20 x 30 mm using a box cutter or surgical knife, as shown in Figure 3.
    6. Ultrasonicate each part in pure water for 15 min by applying 100 W.
    7. Insert a cation-exchange membrane between the chambers using tweezers, as shown in Figure 3. This will separate 2 electrolyte solutions of different concentrations.
    8. Press and seal the stack of the chambers and cation-exchange membrane with glass plates whose dimensions are 26 mm in width and 38 mm long.
  2. Preparation of solutions
    1. Prepare a dispersion of polystyrene particles of an average diameter of 1.01 µm in a 1 x 10−2 mol/L tris(hydroxymethyl)aminomethane ethylenediaminetetraacetic acid (Tris-EDTA) buffer solution, where the volume ratio is adjusted to 1 x 10−2 vol%.
    2. Prepare a mixture of 1 mol/L of KCl and 1 x 10−2 mol/L of Tris-EDTA.
    3. Inject the Tris-EDTA/polystyrene particle and the Tris-EDTA/KCl solutions into the lower and upper chambers, respectively, via syringe needles inserted from the side walls of the chambers.
      NOTE: The quantity of the solutions injected into each chamber is about 210 µL.
    4. Wait for about 18 h until the solution is equilibrated as a result of a diffusion of the ions to relax the ion concentration difference between the upper and lower layers.
      NOTE: In the diffusion process, K+ in the upper solution and H+ in the membrane are expected to penetrate the membrane first, and Cl− is expected to follow them.
  3. Experimental setup and measurement systems
    1. Set the experimental device developed in step 2.1 on the stage of the inverted microscope by hand, as shown in Figure 3. Connect the microscope to a high-speed CMOS camera to monitor the trajectories of the particle motions and record the observation data on a computer.
    2. Apply an electric potential difference of 2 V for 6 s between the two electrodes by using a function generator as a power source.
    3. To confirm that EHD flows are induced by ion transport, measure the ionic currents simultaneously by using an ammeter40.
    4. Analyze the recorded trajectories of the particles by the particle tracking velocimetry (PTV) method39.
      NOTE: After the observations, the EHD flow velocity is evaluated by the PTV method, which is possible by using appropriate software, to trace the displacement of particles and numerically evaluate the velocity. A detailed explanation of PTV methods and how to use them is omitted here because PTV analyses have been widely used and the procedures of the computations depend on the software and operating system that is being used.

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Results

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Figure 4 (video figure) presents a representative result of an EHD flow generation, resulting from the rectification of ion transport pathways and highly concentrated cations that induced a liquid flow in the channel, according to step 1 of the protocol. Figure 5 shows a result of the PIV analysis, where 20 data points near the center of the channel (y = z = 0 mm) were averaged. In the case of the 1 x 10−1<...

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Discussion

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The purpose of this study was to separate cations and anions in aqueous solutions in terms of spatial distributions and transport numbers. Using an anion-exchange membrane, the transport of anions and cations could be rectified in the membrane and in a flow channel that penetrates the membrane, respectively. Alternatively, a cation-exchange membrane that separated high and low concentration solutions worked to generate electrically polarized solutions after a considerable waiting time. As a result, rectified ionic curren...

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Disclosures

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The authors have nothing to disclose.

Acknowledgements

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The authors have no acknowledgments.

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Materials

List of materials used in this article
NameCompanyCatalog NumberComments
Sylgard 184Dow Corning Corp.3097366-0516, 3097358-1004PDMS
AcetoneWako Pure Chemical Industries, Ltd.012-00343
EthanolWako Pure Chemical Industries, Ltd.054-00461
0.1 mol/L Sodium Hydroxide SolutionWako Pure Chemical Industries, Ltd.196-02195
Pottasium ChlorideWako Pure Chemical Industries, Ltd.163-03545
Tris-EDTA buffer 100x concentrateSigma-Aldrich Co. LLC.T9285-10014L
2.93 μm polystyrene particleMerck KGaAL300 RougeTracer particle
1.01 μm polystyrene particleMerck KGaAK100(23716)Tracer particle
Anion exchange membraneASTOM Corp.Neosepta AHA
Gold (Au)Furuuchi Chemical Corp.AUT-13301XSputtering target metal
TitaniumFuruuchi Chemical Corp.TIT-72301XSputtering target metal
ChromiumFuruuchi Chemical Corp.CRT-24301XSputtering target metal
Hight-speed CMOS cameraKeyence Corp.VW-600M
MicroscopeKeyence Corp.VW-9000
Data loggerKeyence Corp.NR-500, NR-HA08
Laser displacement meterKeyence Corp.LK-G5000, LK-H008W
PIV and PTV softwareDITECT Co. Ltd.Flownizer 2D
PotentiostatAMTEK Inc. VersaSTAT4
Inverted microscopeOlympus Corp.IX73
High-speed CMOS cameraAndor Technology Ltd.Zyla 5.5 sCMOS
Function generatorNF Corp. WF1945B
Function generatorNF Corp. WF1973
Ultrasonic cleanerAS ONE Corp.AS22GTU
Rotary pumpULVAC, Inc.G-100SDegas liquid PDMS
Rotary pumpULVAC, Inc.GLD-201ASputtering 
Molecular diffusion pumpULVAC, Inc.VPC-400Sputtering

References

$$\rightleftharpoonup{xx}$$ $$\longleftharp{xx}$$, $$\longrightharp{xx}$$,
  1. Stuetzer, O. M. Ion drag pressure generation. Journal of Applied Physics. 30, 984-994 (1959).
  2. Stuetzer, O. M. Ion drag pumps. Journal of Applied Physics. 31, 136-146 (1960).
  3. Melcher, J. R., Taylor, G. I. Electrohydrodynamics: A review of the role of interfacial shear stresses. Annual Review of Fluid Mechanics. 1, 111-146 (1969).
  4. Saville, D. A. Electrohydrodynamics: The Taylor-Melcher leaky dielectric model. Annual Review of Fluid Mechanics. 29, 27-64 (1997).
  5. Stein, D., Kruithof, M., Dekker, C. Surface-charge-governed ion transport in nanofluidic channels. Physical Review Letters. 93, 035901(2004).
  6. Dekker, C. Solid-state nanopores. Nature Nanotechnology. 2, 209-215 (2007).
  7. Schoch, R. B., Han, J., Renaud, P. Transport phenomena in nanofluidics. Reviews of Modern Physics. 80, 839-883 (2008).
  8. Iverson, B. D., Garimella, S. V. Recent advances in microscale pumping technologies: A review and evaluation. Microfluidics and Nanofluidics. 5, 145-174 (2008).
  9. Sparreboom, W., van den Berg, A., Eijkel, J. C. T. Principles and applications of nanofluidic transport. Nature Nanotechnology. 4, 713-720 (2009).
  10. Venkatesan, B. M., Bashir, R. Nanopore sensors for nucleic acid analysis. Nature Nanotechnology. 6, 615-624 (2011).
  11. Uehara, S., Shintaku, H., Kawano, S. Electrokinetic flow dynamics of weakly aggregated λDNA confined in nanochannels. Journal of Fluids Engineering. 133, 121203(2011).
  12. Guan, W., Reed, M. A. Electric field modulation of the membrane potential in solid-state ion channels. Nano Letters. 12, 6441-6447 (2012).
  13. Yasui, T., et al. DNA manipulation and separation in sublithographic-scale nanowire array. ACS Nano. 7, 3029-3035 (2013).
  14. Ren, Y., et al. Particle rotational trapping on a floating electrode by rotating induced-charge electroosmosis. Biomicrofluidics. 10, 054103(2016).
  15. Ren, Y., et al. Flexible particle flow-focusing in microchannel driven by droplet-directed induced-charge electroosmosis. ELECTROPHORESIS. 39, 597-607 (2018).
  16. Qian, W., Doi, K., Uehara, S., Morita, K., Kawano, S. Theoretical study of the transpore velocity control of single-stranded DNA. International Journal of Molecular Sciences. 15, 13817-13832 (2014).
  17. Qian, W., Doi, K., Kawano, S. Effect of polymer length and salt concentration on the transport of ssDNA in nanofluidic channels. Biophysical Journal. 112, 838-849 (2017).
  18. Liu, W., et al. A universal design of field-effect-tunable microfluidic ion diode based on a gating cation-exchange nanoporous membrane. Physics of Fluids. 29, 112001(2017).
  19. Liu, W., et al. Control of two-phase flow in microfluidics using out-of-phase electroconvective streaming. Physics of Fluids. 29, 112002(2017).
  20. Osman, O. O., Shintaku, H., Kawano, S. Development of micro-vibrating flow pumps using MEMS technologies. Microfluidics and Nanofluidics. 13, 703-713 (2012).
  21. Osman, O. O., Shirai, A., Kawano, S. A numerical study on the performance of micro-vibrating flow pumps using the immersed boundary method. Microfluidics and Nanofluidics. 19, 595-608 (2015).
  22. Daiguji, H. Ion transport in nanofluidic channels. Chemical Society Reviews Home. 39, 901-911 (2010).
  23. Ristenpart, W. D., Aksay, I. A., Saville, D. A. Assembly of colloidal aggregates by electrohydrodynamic flow: Kinetic experiments and scaling analysis. Physical Review E. 69, 021405(2004).
  24. Ristenpart, W. D., Aksay, I. A., Saville, D. A. Electrohydrodynamic flow around a colloidal particle near an electrode with an oscillating potential. Journal of Fluid Mechanics. 575, 83-109 (2007).
  25. Schoch, R. B., Hann, J., Renaud, P. Effect of the surface charge on ion transport through nanoslits. Physics of Fluids. 17, 100604(2005).
  26. Ross, D., Johnson, T. J., Locascio, L. E. Imaging of electroosmotic flow in plastic microchannels. Analytical Chemistry. 73, 2509-2515 (2001).
  27. Hsieh, S. -S., Lin, H. -C., Lin, C. -Y. Electroosmotic flow velocity measurements in a square microchannel. Colloid and Polymer Science. 284, 1275-1286 (2006).
  28. Rubinstein, I., Zaltzman, B. Electro-osmotically induced convection at a permselective membrane. Physical Review E. 62, 2238-2251 (2000).
  29. Bard, A. J., Faulkner, L. R. Electrochemical methods, 2nd ed. , John Wiley & Sons. Danvers, MA. 362-363 (2001).
  30. Brask, A., Goranović, G., Jensen, M. J., Bruus, H. A novel electro-osmotic pump design for nonconducting liquids: theoretical analysis of flow rate-pressure characteristics and stability. Journal of Micromechanics and Microengineering. 15, 883-891 (2005).
  31. Takamura, Y., et al. Low-voltage electroosmosis pump for stand-alone microfluidics devices. Electrophoresis. 24, 185-192 (2003).
  32. Zeng, S., Chen, C. -H., Mikkelsen, J. C., Santiago, J. G. Fabrication and characterization of electroosmotic micropumps. Sensors and Actuators B: Chemical. 79, 107-114 (2001).
  33. Bhaumik, S. K., Roy, R., Chakraborty, S., DasGupta, S. Low-voltage electrohydrodynamic micropumping of emulsions. Sensors and Actuators B: Chemical. 193, 288-293 (2014).
  34. El Moctar, A. O., Aubry, N., Batton, J. Electro-hydrodynamic micro-fluidic mixer. Lab on a Chip. 3, 273-280 (2003).
  35. Bart, S. F., Tavrow, L. S., Mehregany, M., Lang, J. H. Microfabricated electrohydrodynamic pumps. Sensors and Actuators A: Physical. 21, 193-197 (1990).
  36. Ashikhmin, I. A., Stishkov, Y. K. Effect of insulating walls on the structure of electrodynamic flows in a channel. Technical Physics. 57, 1181-1187 (2012).
  37. Yano, A., Doi, K., Kawano, S. Observation of electrohydrodynamic flow through a pore in ion-exchange membrane. International Journal of Chemical Engineering and Applications. 6, 254-257 (2015).
  38. Doi, K., Yano, A., Kawano, S. Electrohydrodynamic flow through a 1 mm2 cross-section pore placed in an ion-exchange membrane. The Journal of Physical Chemistry B. 119, 228-237 (2015).
  39. Yano, A., Shirai, H., Imoto, M., Doi, K., Kawano, S. Concentration dependence of cation-induced electrohydrodynamic flow passing through an anion exchange membrane. Japanese Journal of Applied Physics. 56, 097201(2017).
  40. Nagura, R., Doi, K., Kawano, S. Characterisation of microparticle transport driven by ionic current conditions in electrically polarized aqueous solutions. Micro & Nano Letters. 12, 526-531 (2017).
  41. Doi, K., et al. Nonequilibrium ionic response of biased mechanically controllable break junction (MCBJ) electrodes. The Journal of Physical Chemistry C. 118, 3758-3765 (2014).

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Tags

Electrohydrodynamic FlowsIon Exchange MembraneIon Concentration PolarizationAqueous Electrolyte SolutionsElectric Potential ApplicationTracer Particle TrackingHigh Speed CameraPDMS ReservoirGold Bias ElectrodesPIV Analysis

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