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9/10  Lithium batteries
               to  that  of  the  lithium-sulphur  dioxide  cell,  except   W
               that hermetically sealed cells are mandatory at present.   -  L 4.0-   Cathode
               The  lithium-thionyl  chloride  system  is  a  very  low-   2 3.0
               pressure system and, because of  that, it is potentially   2  'E  2.0
                                                           .-
               superior to lithium-sulphur  dioxide  systems in high-   f  .3 1.0
                                                           E5
                                                                                                  I
               temperature  and/or  unusual  form  factor  applications.   2 2  0   1.5  3.0  4.5  6.0  7.5  9.0  10.5  12.0
               The cells are manufactured without any initial internal   8
               gas pressure and, because the discharge reaction gen-   0
                                                           W
                                                           E
               erates  only  a  limited  amount  of  gas,  the  need  for
               venting is eliminated. The  system appears to be  safe
               in  low-rate  cell  designs,  and  may  be  safe,  if  prop-
               erly vented, in high-rate cell  designs; however, there
               is an insufficient database on the system (particularly   I   I   I   I   I   I   I   I   J
               in the high-rate configuration) to make that claim with   0   1.5  3.0  4.5   6.0  7.5  9.0  10.5  12.0
               a high degree of confidence. One manufacturer claims            Time (h)
               to supply cells that have an energy density in excess of
               1100  W h/dm3 and 660 W Wkg. Another manufacturer   Figure 9.6  Honeywell  lithium-thionyl  chloride  cell:  polarization
                                                           and voltage delay of a lithium-thionyl chloride cell at 24°C after 3
               claims  an  energy density  of  800 Wh/dm3, compared   weeks' storage at 24°C; loads 120 mA (30 min) to 45 mA (30 min);
               to  400 W h/dm3 for  zinc-mercury,  200 W h/dm3  for   electrolyte 1.5 M  LiAICI4 (commercial grade) SOCln (Courtesy of
               zinc-carbon  and 300 W h/dm3 for alkaline manganese   Honeywell)
               dioxide  (the  corresponding W hkg data  for  the  four
               types of  cell are 420,  100, 80 and  100).      A,
                 Yet  another  manufacturer  claims  the  following   -   -0cv
               energy densities at low rates of  discharge:   1 >3                           n
               Small cells   500Whflcgp1
                           100owwdm-~                        -  -
               Large cells   700 W h/kg-'                    J  1-      /  ,tlO%SO,
                           1000 w ww3                                    -e---
               Theory      1489 W fig-'                              1  1  1  1  1  1  1  1  1  1  1  1  1  1  1
                           2000 W h/dm-3
               Cells operate at temperatures between -55  to  150°C.
                They have a shelf life of up to 10 years due to their
               negligibly low self-discharge rate, e.g. 97% of original
               capacity  is  retained  after  five years'  storage. Earlier
               versions of this battery exhibited severe passivation of
               the  lithium  anode,  which  severely limited  shelf  life.
               For  example,  at  discharge  current  density  as  low  as   greater  than  5  weight  %  level.  At  these  higher  sul-
               0.6 mA/cm2, significant initial voltage drop and volt-   phur dioxide levels after 2 weeks at 74"C, cells were
               age delay were observed at 25°C after storage periods   found to be anode limited and showed severe polariza-
               as short as  1 week at 72°C. The primary cause of  the   tion under a  120mA load when they were discharged
               voltage drop is the formation of a film. which results in   at -29°C.
               excessive anode passivation. This becomes evident on   Short  circuiting  of  lithium-thionyl  chloride  cells
               closed circuit as a sharp initial voltage drop and a long   with  the  risk  of  subsequent cell  explosions have  led
               recovery before the voltage stabilizes (that is, voltage   to a limited use of  these cells in particular areas, e.g.
               delay). This is clearly illustrated in Figure 9.6, which   military and medical applications.
               shows  the  strong  anode  polarization  and  initial  cell   These  cells  are  available  in  small  prismatic  and
               voltage drop followed by a slow recovery to a useful   cylindrical cell designs with capacities up to 1 Ah and
               cell voltage. Investigations by  workers at Honeywell   in flat, cylindrical and prismatic designs with capacities
               have shown that the passivation film on the anode pro-   up  to  20000Ah. Twenty year  reserve  cells  are  also
               duced  in  the  lithium-aluminium  chloride  electrolyte   available.
               consists  of  lithium  chloride.  They  have  also  shown
               that the formation of this film can be prevented by the   9.4  Lithium-vanadium pentoxide
               inclusion of 5% sulphur dioxide in the electrolyte. It is
               significant that effective control of lithium passivation   primary batteries
               appears to be critically dependent on the sulphur diox-   This  system  utilizes  the  lithium  anode,  a  car-
               ide concentration. As  shown in Figure 9.7, discharge   bon-vanadium  pentoxide  cathode  and  a  double-salt
               performance after storage can be adversely affected at   metal  fluoride electrolyte  (lithium hexafluoroarsenate
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