Page 181 - Lindens Handbook of Batteries
P. 181

7.6        PRINCIPLES OF OPERATION

                             can be quite large when very high surface area activated carbons are used and can have a much more
                             rapid response than the lead electrode. The electrolyte phase is similar to that of the standard lead-
                             acid battery so the reader is referred to Chaps. 16 and 17. Further information on the use of this type
                             of battery in microhybrid vehicles is found in Chap. 29.
                                Sulfuric acid has also been used in the vanadium and other redox types of batteries. Here the
                             solution also contains vanadium ions of different valence states (uranium ions and other ions have
                             also been tested) with a vanadium (II–III) couple used on the negative electrode side and a vana-
                             dium (IV–V) couple used on the positive electrode side. A simple microporous separator can be
                             used to separate the two solutions when they are in the interelectrode space, although sometimes an
                             ion-specific separator is used (proton conductive). No particular harm occurs when the solutions
                             interdiffuse except in lowering the round-trip energy efficiency of the process since both solutions
                             contain vanadium ions. When the system is not undergoing charge or discharge, the solutions are
                             pumped into storage containers, and when the system is operating, the solutions are pumped into
                             the interelectrode space in a flow-through cell. Even in these systems, one must be concerned about
                             gas evolution since the overpotential of the charging regime can carry the cell into the gassing range
                             (see Chap. 30 for details).
                                Occasionally other acids have been employed for acid battery types. For example, a HBF  elec-
                                                                                                 4
                             trolyte has been used with lead/lead dioxide electrodes. These types are not in current production,
                             however, so they will not be discussed.


                 7.3  NONAqUeOUs eleCTROlyTes

                             This section is arbitrarily separated into organic solvent-based electrolytes, inorganic solvent-based
                             electrolytes, ionic liquids, solid polymer electrolytes, and ceramic/glassy electrolytes. The use of
                             polymeric materials to cause gelation of the electrolyte (used mainly with organic solvents) has
                             little  effect  on  the  basic  electrolyte  properties  such  as  conductivity  and  diffusivity,  except  for  a
                             major effect on viscosity. However, the electrolyte in most modern batteries has very little convec-
                             tive flow, so viscosity has little effect on battery operation. The greatest development has been with
                             organic solvent-based electrolytes as they have been used in numerous primary lithium batteries
                             and many variations of the lithium-ion battery type. Inorganic solvent-based electrolytes have been
                             used mainly in liquid cathode batteries. The others are still in the development stage, but will be
                             discussed briefly.


                 7.3.1  Organic-Solvent Electrolytes
                             The greatest electrochemical use for organic-solvent electrolytes has been in the fields of primary
                             lithium batteries and rechargeable lithium-ion batteries. The successful application in primary lithium
                             batteries predates that of the rechargeable batteries by several decades, even though work was insti-
                             tuted on both primary and secondary batteries at about the same time in the early 1960s. Techniques
                             for  handling  and  purifying  the  organic  liquids  had  to  be  developed  first,  with  special  attention
                             to the contamination of water and other impurities. More than a decade of work was required to
                             understand the importance of reducing impurities to the ppm level from salts and solvents. Cathode
                             materials and other cell components often have much more adsorbed water than was commonly
                             realized so that methods to remove water from all components had to be developed as well. A good
                             compilation of the techniques required to study nonaqueous electrochemistry is given in Ref. 9.
                             In addition, it was necessary to develop an understanding of the stability of purified solvents and
                             salts with active materials of both electrodes, especially the negative electrode. Studies of the
                             electrochemical window on materials such as conductive diamond, platinum, or glassy carbon
                             during  cyclic  voltammetric  sweeps  in  the  negative  direction  (cathodic  scans)  required  much
                             interpretation because the film-forming properties of these materials was very different from that of
                             lithium metal (or in later work on carbons or graphites). Likewise, anodic scans on inert substrates
   176   177   178   179   180   181   182   183   184   185   186