Page 627 - Handbook of Battery Materials
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17.4 Bulk Properties  601

               electrolysis or high currents. It is practically difficult to achieve these currents, be-
               cause nonaqueous electrolytes show relatively low conductivities and consequently
               high resistances. Secondly, for a correct procedure, mixing between the different
               compartments has to be avoided. This is ensured, for example, by sophisticated
               cell design, such as increased cell length or uniform shape. Decreased polariza-
               tion time guarantees elimination of diffusion. Temperature control is essential to
               prevent density differences that cause convective stirring. Another problem is the
               assignment of unknown ionic species that are moved in the electrolyte. If only two
               ionic species exist in the solution, that is, the electrolyte is completely dissociated,
               the transference number can be easily calculated. The definition of transference
               numbers (see above) has to be kept in mind: after electrolysis, the concentration
               change of an ionic constituent is measured, not of a free ion [445]. Because of these
               huge experimental problems, few data for nonaqueous electrolytes are available.
               Reger et al. measured for LiBr and Al 2 Br 6 in toluene a cation transference number
                                               +
               of 0.53 for the existing species [Li 2 (Al 2 Br 7 )] and [Li(Al 2 Br 7 ) 2 ] [444], and Paul et al.
                                                             −
               measured a lithium-ion transference number of 0.295 for LiCl in DMF [446].
                As dissociated ions are always solvated, electrolysis entails transport of solvate
               with the ions. This phenomenon has been known for a long time; in 1900, Nernst
               determined the transport of water in, for example, sulfuric acid [447]. Washburn
               quantified it in the so-called Washburn number [440], which simply expresses the
               net number of moles of solvent carried by the electrolyte.
                               a a
                          c c
                      F
                     n = t n − t n S                                     (17.61)
                            S
                      S
                     F
               with  n as number of moles of solvent transferred from anode to cathode, t c,a  as
                     S
               transference number of cation and anion respectively, and n c,a  number of moles of
                                                             S
               solvent combined with one equivalent of cation and of anion.
                The method is based on the addition of an inert substance remaining stationary:
               its concentration after electrolysis gives information about possible dilution or
               increase of concentration and therefore errors in concentration determination.
               But the work of Washburn has come under criticism, because the used reference
               systems raffinose and sucrose are polar and consequently no longer stationary
               [436].
               17.4.6.3 Electromotive Force (emf) Method
               Transference cells of the form

                                     C|CA·(m 1 )·||CA·(m 2 )|C
               with molalities of the monovalent electrolyte CA m 2 > m 1 and C the reversible
               electrode, have a potential difference E trans described in a simplified form by Basili
               et al. [448]:
                            2RT    	  m 2 γ 2
                    E trans =−  t + ln                                   (17.62)
                             F       m 1 γ 1
               with γ as the activity coefficient. If the activity coefficient is available for the
               system the transference number can be measured easily by electromotive force
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