Lithium chlorine battery containing thionyl halide
CROSS-REFERENCE TO RELATED APPLICATION 
     This is a Continuation-in-Part application of our co-pending application Ser. No. 106,868, filed Dec. 26, 1979, now abandoned, entitled &#34;LITHIUM CHLORINE BATTERY CONTAINING THIONYL HALIDE&#34;, and assigned to the same assignee as the present invention. 
    
    
     BACKGROUND OF THE INVENTION 
     The present invention relates generally to an improved electrochemical cell, and more specifically to such a cell utilizing a lithium anode and a non-aqueous electrolyte, and wherein the cell is capable of delivering power at a substantially constant voltage over extended periods of time. 
     Electrochemical cells utilizing lithium anodes have found particular utility in certain of those long-life applications in which a relatively flat voltage output is required, with a relatively low or modest current requirement. Such electrochemical cells are particularly adapted for use in delivering power over extended periods of time to devices which may be implanted within the human body, and as such, require such extended lifetimes. An example of such a device is an implantable cardiac pacer device, although other electrically powered devices such as implanted infusion pumps or the like may utilize the improved power source of the present invention. 
     SUMMARY OF THE INVENTION 
     Briefly, in accordance with the present invention, a primary electrochemical cell is provided which comprises a receptacle housing a lithium anode, an iodine trichloride cathode, these being immersed in a non-aqueous electrolyte. The electrolyte comprises a thionyl chloride to which iodine monochloride, lithium aluminum chloride, or mixtures thereof have been added. The electrolyte is primarily thionyl chloride to which between about 5% to 90% iodine monochloride has been added, with the lithium aluminum chloride being present in a rather modest concentration, up to a saturable solution level. The molar concentrations of the individual components within the combination are selected such that the primary reaction occurs between the lithium anode and the iodine trichloride cathode, which reaction may be followed by reactions occurring between the iodine component of the reactant product of the iodine trichloride in its resultant reduced oxidation states. The voltage outputs are related, one to another, in order that a first modest drop in voltage will occur at a point when substantially all of the iodine trichloride available for reaction has been exhausted from the system. At a selected point in time, and depending upon the specific application, steps may be taken to replace the power source, as well as any other component of the system, which are of the type which are normally replaced along with the power source. 
     Therefore, it is a primary object of the present invention to provide an improved electrochemical cell which is particularly adapted for use on those applications requiring low to modest current drain, but which require a relatively flat voltage output over extended periods of time, with the improved electrochemical cell of the present invention utilizing a lithium anode and iodine trichloride cathode together with an electrolyte system comprising thionyl chloride containing iodine monochloride, lithium aluminum chloride, or mixtures thereof. 
     It is a further object of the present invention to provide an improved primary electrochemical cell comprising a lithium anode, an iodine trichloride cathode together with a thionyl chloride electrolyte, the electrolyte containing substantial quantities of iodine trichloride, lithium aluminum chloride, or mixtures thereof. 
     Other and further objects of the present invention will become apparent to those skilled in the art upon a study of the following specification, appended claims, and accompanying drawing. 
    
    
     IN THE DRAWING 
     FIG. 1 is a front elevational view of an electrochemical cell prepared in accordance with the present invention, and which is shown partially cut away in order to expose certain of the cell components; and 
     FIG. 2 is a detail exploded view showing the individual components of the anode as typically employed in an electrochemical cell prepared in accordance with the present invention. 
    
    
     DESCRIPTION OF THE PREFERRED EMBODIMENT 
     In accordance with the preferred embodiment of the present invention, a primary electrochemical cell is prepared utilizing a lithium anode together with a non-aqueous electrolyte formulation of the following general characteristics: 
     GENERAL CHARACTERISTICS OF EXAMPLES 
     Each of the cells contain a 1 gram lithium anode with a surface area of 15 cm 2  for 5.22 cc of cathode material. The total external volume of the cells in each case was a 9.6 cc. Reagent or better grade chemicals were used without further treatment being required. The iodine monochloride was de-gassed for 10-15 minutes by bubbling Ar through it in an Ar filled dry box with such dry boxes being commercially available. All cell preparation and construction was also done in the dry box where the Ar atmosphere was maintained at less than 10 ppm H 2  O, 10 ppm O 2  and 50 ppm N 2 . Reference is made to the following specific examples for a more complete comprehension of the concepts of the present invention. 
     
                       EXAMPLE I                                                   
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Component                 Quantity                                        
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(A) Anode-lithium metal   1 gram                                          
(B) Cathode (ICl.sub.3)   7 grams                                         
(C) Electrolyte (SOBr.sub.2 and containing                                
  LiAlBr.sub.3 in a 1.6 molar                                             
  concentration with the                                                  
  electrolyte being saturated                                             
  with ICl.sub.3)         2 ml.                                           
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     This cell prepared in accordance with Example I provided an open circuit potential greater than 3.92 volts. The open circuit potential calculated from the free energies of formation at 37° C. of formation at 37° C. for a probable reaction wherein the calculated voltage: 
     
         6Li+2ICl.sub.3 →6LiCl+I.sub.2 is 3.89 volts. 
    
     Since the precise mechanism of the reaction or reactions is not known, it is believed that the actual measured potential may be higher due to the disassociation reaction of iodine trichloride and the subsequent use of chlorine in the cell. 
     
                       EXAMPLE II                                                  
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Component                 Quantity                                        
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(A) Anode-lithium metal   1 gram                                          
(B) Cathode (ICl.sub.3)   7 grams                                         
(C) Electrolyte (SOCl.sub.2 with 10% ICl;                                 
  and containing LiAlCl.sub.4 in a                                        
  1.6 molar concentration)                                                
                          3 ml.                                           
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     The cell prepared in accordance with this Example had an open circuit potential ranging from 3.75-3.82 volts. It appeared that the open circuit potential depended on the 3.75-3.82 volts. It appeared that the open circuit potential depended upon the interhalogen concentration which, in accordance with the studies, varied between 10-50% by volume. This cell had a somewhat higher open circuit potential and had substantially increased discharge efficiency as compared with the same cell without the iodine chloride and lithium aluminum chloride in the electrolyte. 
     
                       EXAMPLE III                                                 
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Component                 Quantity                                        
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(A) Anode-lithium metal   1 gram                                          
(B) Cathode (ICl.sub.3)   8 grams                                         
(C) Electrolyte (SOCl.sub.2 with 10% ICl;                                 
  and containing LiAlCl.sub.4 in a                                        
  1.5 molar concentration)                                                
                          3 ml.                                           
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     The cell prepared in accordance with this Example III provided an initial open circuit voltage of 3.94 volts, and with more than 50% utilization of the iodine trichloride, the cell continued to produce a voltage of 3.7 volts across a 3 Kohm load. While the present structure contemplates utilizing essentially pure lithium, it will be appreciated that cells may be prepared utilizing lithium alloys, including, for example, 90:10 lithium magnesium alloys. The term &#34;lithium&#34; as employed herein accordingly contemplates reference to substantially pure lithium however, it is understood that the term is used in a comprehensive sense so as to include those lithium alloys containing, for example, 10% or so of magnesium or another element. 
     
                       EXAMPLE IV                                                  
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Component                 Quantity                                        
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(A) Anode-lithium metal   1 gram                                          
(B) Cathode (ICl.sub.3)   8 grams                                         
(C) Electrolyte (SOCl.sub.2 with 10% ICl)                                 
                          3 ml.                                           
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     The cell of Example IV functioned adequately, with an open circuit voltage of 3.92 volts, and with an output across a 10 Kohm load being initially approximately 3.8 volts. 
     
                       EXAMPLE V                                                   
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Component                 Quantity                                        
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(A) Anode-lithium metal   1 gram                                          
(B) Cathode (ICl.sub.3)   8 grams                                         
(C) Electrolyte (SOCl.sub.2 containing                                    
  lithium aluminum chloride                                               
  (LiAlCl.sub.4 in a 1.6 molar                                            
  concentration)          3 ml.                                           
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     The cell of Example V functioned adequately, with an initial open circuit voltage output of 3.93 volts. The initial output across a 3 Kohm load was approximately 3.6 volts, and upon utilization of more than 50% of the iodine trichloride, the cell continued to produce approximately 3.8 volts across a 5 Kohm load. 
     
                       EXAMPLE VI                                                  
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Component                 Quantity                                        
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(A) Anode-lithium metal   1 gram                                          
(B) Cathode (ICl.sub.3)   3 grams                                         
(C) Electrolyte (SOBr.sub.2 with 10% ICl;                                 
  and containing LiAlCl.sub.4 in a                                        
  1 molar concentration)  3 ml.                                           
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     The cell of Example VI functioned adequately, with an initial open circuit voltage output of 3.92 volts. The initial output across a 3 Kohm load was approximately 3.6 volts, and upon utilization of more than 50% of the iodine trichloride, the cell continued to produce approximately 3.5 volts initially across a 3 Kohm load. 
     
                       EXAMPLE VII                                                 
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Component                 Quantity                                        
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(A) Anode-lithium metal   1 gram                                          
(B) Cathode (ICl.sub.3)   8 grams                                         
(C) Electrolyte (SOB.sub.2 with 10% ICl;                                  
  and containing LiAlBr.sub.4 in a                                        
  1 molar concentration)  3 ml.                                           
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     The operational performance of this cell is substantially similar to that of Example VI. 
     The Electrolyte 
     As has been indicated, the electrolyte contemplated for use in cells fabricated pursuant to the present invention includes mixtures of thionyl chloride, thionyl bromide, along with iodine monochloride. Typically, cells may be prepared utilizing thionyl chloride containing from between about 5% and 20% of iodine monochloride. Electrolytes of this formulation are normally liquid at room temperature, and remain liquid at body temperature. Thionyl bromide may be substituted for the thionyl chloride. 
     Electrolyte Additives 
     As has been indicated, two additives may be present, including iodine trichloride and lithium aluminum chloride. Iodine trichloride is present as the cathode in substantial quantities and normally in excess of theoretical. Lithium aluminum chloride, when present, is provided in relatively modest quantities, such as in the range of between about 1 and 2 molar, based upon the volume of the electrolyte. However, the cells are useful when the electrolyte contains lithium aluminum chloride to saturation. 
     Assembly Considerations 
     It will be appreciated that primary electrochemical cells prepared in accordance with the present invention may utilize receptacle housings of a wide variety of configurations. Essentially, the configuration selected is dictated by the application of the cell, and the constraints placed thereupon by the specific application. The present invention is one which permits the utilization of a cell having a wide variety of potential configurations, with the cell structure being one which poses little, if any, difficulties on cell configuration. 
     Electrolyte Formulations 
     As has been indicated above, the thionyl chloride electrolyte may contain from between about 5% and 20% of iodine monochloride. The solutes utilized are compatible within these ranges. 
     Likewise, the various ranges of lithium aluminum chloride set forth are useful within the systems. It remains, however, that these ranges are selected in order to provide the desired flat voltage output curves which are achieved with low to modest loads. 
     Typical Cell Design 
     With attention now being directed to FIGS. 1 and 2 of the drawing, it will be seen that the electrochemical cell generally designated 10 comprises a receptacle or housing 11 enclosing a lithium anode generally designated 12, which is immersed in a non-aqueous electrolyte as present at 13. Means for delivering an electrical current flow from the cell are provided through terminals 14 and 15, with terminal 14 being in the form of a terminal pin, and with terminal 15 being in the form of a collapsed fill-tube assembly. 
     With attention being directed to FIG. 2 of the drawing, the detail structure of lithium anode 12 is shown, with the anode 12 including a total of two plates of lithium metal, including plates 18 and 19. These lithium plates are pressed together against nickel grid member 20, with the surface area of the lithium in the completed cell, as set forth in the general discussion concerning the examples, being in the area of 15 cm 2 . 
     As is apparent from a review of FIGS. 1 and 2, the grid 20 comprises an expanded grid of nickel, with nickel being preferred in this application. 
     For most purposes, receptacle 11 is fabricated from a stainless steel, specifically No. 304L stainless, with this material being desirable for most purposes. 
     In preparing the finished cell, the container 11 will, of course, include a cover 22 which has a pair of spaced apart openings or bores formed therein as at 23 and 24 for receiving the terminals 14 and 15 therewithin. Terminal 15 functions as a fill-tube during preparation. In the completed assembly, the terminal pin 14 will be hermetically sealed, using an outer sleeve 26, with internal sealing components as shown. The balance of the seal assembly includes sealing sleeve 27 which has a threaded cap end or portion as at 28. Member 27 is insulatively isolated from terminal 14 by means of an inner insulating barrier as at 29. Inner insulating sleeve 30 is provided for the lower portion of terminal pin 14, and outwardly thereof is cup and sleeve member 31. Members 30 and 31 are preferably fabricated from an electrical insulating material such as molded polytetrafluoroethylene (Teflon), molded nylon, or the like. Member 31 is internally threaded as at 32 for engagement with the lower end 28 of member 27. In order to complete the assembly, sealing sleeve 33 is provided which is press-fit over the outer circumference of the cup portion of member 31. The details of processing utilized in preparing the finished cell are set forth in the general discussion preceding the description of the specific examples hereinabove. 
     Terminal 15 is preferably a hollow sleeve, one end of which is bonded, such as by welding, brazing, or the like to cover 22, as at 35. After the filling operation, terminal 15 is sealed off by a suitable sealant as at 36. 
     The technique for bonding the inner wall of member 26 to the outer wall surface of member 27 is not critical, it being understood that any suitable sealing operation may be acceptable, including soldering or the like. Also, in order to assure hermetic sealing conditions, a bead of sealant is preferably provided adjacent the mating threads of the cup portion of member 31 and threaded area as at 32, with such a sealant being disposed in the zone as at 37. 
     The electrolyte is normally prepared prior to filling the cell, with the material being added as a liquid as one of the steps in the overall preparation, as will be more fully disclosed hereinbelow. 
     Cell Construction Procedure 
     In preparing the cell, the sealing assembly including pin 14 is secured to sleeve member 26 which is welded to cover member 22, with sleeve member 26 providing the necessary strength for such sealing. Following this step, the fill-tube terminal 15 is welded into the cover. 
     Thereafter, the circumferential insulator or spacer element 39 is pierced adjacent the ends thereof and installed, together with the grid current collector 19 and lithium elements pressed thereon. These components may be spot-welded into place as required. 
     The individual pieces of lithium, including lithium elements 18 and 19 are installed within the circumferential insulator 39. Lithium members 19 and 20 provide conductivity for current flow from the battery assembly. The circumferential insulator 39 is placed within the cell in order to permit the electrolyte to flow and fill all areas of the cell, and make appropriate physical and electrical contact with the lithium anode. 
     The cap member 22, together with its completed anode appendage is then welded into receptacle chamber or body 11, and the electrolyte is then added through the fill-tube. The fill-tube is then clamped off for sealing, and the assembly is then ready for cleaning and inspection.