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MAGNETO-SCIENCE 2009Study of the influ<strong>en</strong>ce of magnetic forces on the mass transferof paramagnetic particles in electrochemistryThe context of our work is the characterization of the magneticforces which influ<strong>en</strong>ce the processes of mass transferin electrochemistry. It appears experim<strong>en</strong>tally that in thepres<strong>en</strong>ce of a magnetic field in solutions, where a gradi<strong>en</strong>tof conc<strong>en</strong>tration of paramagnetic ions is pres<strong>en</strong>t, ev<strong>en</strong> if theaction of Lor<strong>en</strong>tz forces is not effective, a driving force actingon the solution will arise. This force, referred to as theconc<strong>en</strong>tration gradi<strong>en</strong>t force, is oft<strong>en</strong> writt<strong>en</strong>,−→ B 2−→ ∇CF m = χ m , (18)2µ 0where χ m (m 3 /mol) is the molar magnetic susceptibility,B(T) the magnetic flux d<strong>en</strong>sity, C(mol/m 3 ) the bath conc<strong>en</strong>trationand µ 0 (Hm −1 ) the permeability of vacuum. Theexperim<strong>en</strong>t was performed using a 10 MW resistive magnetwhich g<strong>en</strong>erates a homog<strong>en</strong>eous a magnetic field of 6 T ina 286 mm diameter. The experim<strong>en</strong>tal device is a rectangularchannel with platinum electro<strong>des</strong> on the upper and lowerwalls, betwe<strong>en</strong> which a voltage drop is applied (figure 152).The channel is closed with insulating walls to eliminate theedge effects. The cell is immersed in an electrolytic bathprepared with an equimolar solution of 0.05 mol/m 3 Ferriferro-cyanide with 0.5 mol/m 3 and K 2 SO 4 as the supportingelectrolyte. The temperature condition was about 17 ◦ Cand an Ag/AgCl refer<strong>en</strong>ce electrode was used to control theelectro<strong>des</strong> pot<strong>en</strong>tial.of the boundary layer. As a result, an additional mechanismof transport of the solution is g<strong>en</strong>erated. Correspondingly,the limiting curr<strong>en</strong>ts of reactions proceeding in the electrochemicalsystem will become a function of the appliedmagnetic flux d<strong>en</strong>sity. The influ<strong>en</strong>ce of magnetic field onthe evolution of the mean limiting curr<strong>en</strong>t d<strong>en</strong>sity is plottedusing logarithmic coordinates in figure 153. We can showsthat for the two mo<strong>des</strong>, anodic and cathodic, the limitingcurr<strong>en</strong>t d<strong>en</strong>sity follows a law in B 2/3 . Note that this lawstarts at 0.5 T for the anodic mode and at 2 T for the cathodicmode due to the paramagnetic forces which drivesa more important flow than the gravity. This ph<strong>en</strong>om<strong>en</strong>ologicalbehaviour was observed by many authors [Waskaas,Acta Chimica 50, 516 (1996)], Rabahand et al., Journal ofElectroanalytical Chemistry 571, 85 (2004)].Figure 152:Experim<strong>en</strong>tal configuration.The results were obtained by the polarographic method.Wh<strong>en</strong> the two electro<strong>des</strong> located on the faces of the channelare submitted to a voltage drop, controlled by a pot<strong>en</strong>tiostat,an electric curr<strong>en</strong>t is imposed and in the pres<strong>en</strong>ce ofan homog<strong>en</strong>eous magnetic field, the gradi<strong>en</strong>t of paramagneticions due to electrode reaction will cause a redistributionof velocities in the bath which th<strong>en</strong> acts on the depthFigure 153: Evolution of the limiting curr<strong>en</strong>t d<strong>en</strong>sities with thework electrode (WE) in the (a) cathodic mode and (b) anodicmode.F. DebrayD. Baaziz, A. Alemany, (EPM-SIMAP Laboratory, Gr<strong>en</strong>oble, France), D. Kalache (Fluids Mechanics Laboratory,University of USTHB, Algiers)108

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