Patent Publication Number: US-4221849-A

Title: Iron-lithium anode for thermal batteries and thermal batteries made therefrom

Description:
FIELD OF THE INVENTION 
     The present invention relates to an anode material comprising iron-lithium for use in battery applications and, in particular, to an iron-lithium anode for use in lithium anode thermal batteries and to thermal batteries made therefrom. 
     BACKGROUND OF THE INVENTION 
     The present invention is an improvement in thermal batteries of the type disclosed and taught in U.S. Pat. Nos. 3,677,822, 3,425,872, 3,527,615, 3,367,800, 3,891,460, 3,930,888 and 4,119,769. Thermal batteries typically comprise a plurality of thermal cells each of which includes an anode, cathode, electrolyte and an integral igniteable heat source. The electrolyte is usually a eutectic mixture of LiCl and KCl and the cathode (depolarizer) comprises a material which is reduced in the electrochemical cell such as phosphates, metal oxides, borates and chromates. The most common depolarizer material is calcium chromate or vanadium pentoxide. Recently, a mixture of iron pyrite and binder have been shown to have significant advantages over conventional depolarizer materials, U.S. Pat. No. 4,119,769. 
     In the present state of the art thermal cells, the anode comprises a fusable metal normally selected from the group consisting of alkali metals, alkaline earth metals and alloys thereof which melt below the operating temperature of the battery. Of these, lithium and lithium alloys are preferred. 
     The anode, in practice, comprises a metal cup into which the active metal is positioned. Positioned adjacent to the active metal is an asbestos insulator or separator. The electrolyte, normally in the form of a wafer, is positioned adjacent to the separator in the cup. The depolarizer, preferably consisting of an analyte and catholyte layered wafer, is positioned in stacked array against the electrolyte. 
     Use of lithium in thermal batteries provides a number of advantages not the least of which is its capability of providing high current densities as a liquid metal anode. The reactive nature of lithium and its low melting point, however, have caused a number of associated difficulties, the most serious of which is leakage of the molten metal. Such leakage causes short circuits and premature failure in such batteries. An asbestos separator or other fibrous material is typically used to prevent or reduce such leakage by direct reaction with the molten metal, but such means occupy precious space and expose workers to asbestos material. 
     It is, therefore, an object of the present invention to provide an improved thermal anode which includes the advantages of lithium without its inherent disadvantages. It is a further object to provide an anode which results in a thermal cell having decreased weight and thickness by eliminating the need for asbestos or other separator materials. A yet further object is to achieve the aforementioned benefits and at the same time improve the electrical characteristics of the batteries. 
     DESCRIPTION OF THE INVENTION 
     The invention comprises a pyrometallurically combined iron/lithium anode. The ratio of lithium to iron is about 15% to 35% and preferably about 30% by weight. Preferably, the lithium is heated to about 500° to 600° F. and the iron added in particulate form while stirring the molten mixture. Preferably, the iron has a particle size of from about 1.3 to 2.1μ with a density of 0.2 to 0.8 gms/cc and a surface area of approximately 30 to 70 m 2  /gm. 
     As the iron is added to the molten lithium the mixture becomes very viscous. Vigorous stirring is desired to wet the iron particles with the lithium. The mixture of lithium and wetted iron is preferably poured into a mold to cool. While only about 10% by volume of the material is lithium, the material retains the essential characteristics of lithium. It is easily rolled and shaped, and has reactivity essentially that of lithium. Unlike conventional thermal battery lithium anodes, the anode material of the present invention softens but does not liquify at normal battery operating temperatures. The anode thus maintains its dimensional stability during battery operation and does not flow as in conventional thermal batteries. 
     In the preferred range of lithium to iron described above, it is not believed to make a difference if there is no particle to particle contact between iron particles. In the present invention, the iron particles are held together by the surface tension of the lithium rather than being alloyed as is normally the case. Accordingly, it is contemplated that materials other than iron which are capable of being wetted by molten lithium, for example stainless steel, nickel and nichrome (to which lithium alloys slightly) are useful in the present invention. 
     In thermal battery application, the iron/lithium anode material of the present invention provides a number of advantages. In addition to affording an anode which is dimensionally stable during battery operation, a higher efficiency battery can be fabricated. Such efficiency results from being able to utilize more active material within a given volume by the elimination of the asbestos separator means. Elimination of the asbestos separator also provides a significant health advantage to employees making such batteries inasmuch as it does away with a possible carcinogen or cocarcinogenic material. When used in a thermal battery having a depolarizer of iron pyrite (U.S. Pat. No. 4,119,796) rather than chromates, a thermal battery can be manufactured having no suspected carcinogen or cocarcinogen present. 
     Better electrical parameters have been obtained using the iron/lithium anode material of the present invention. Basically, it is believed that such improvements are due to a more efficient utilization of lithium. Such improvements also result from the elimination of the asbestos separator which adds complexity to the design. 
     The above-described advantages result in an improved thermal battery as well as method for manufacture. However, other advantages will become apparent from a perusal of the following detailed description of the best mode contemplated for the use and manufacture of the iron/lithium anode of the present invention taken in connection with the accompanying drawings. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     FIG. 1 is a sectional elevation of the iron/lithium anode positioned in a prior art cup conventionally used in thermal batteries; and 
     FIG. 2 is an enlarged breakaway sectional elevation of such iron/lithium anode positioned in a modified stack array for use in the battery disclosed in U.S. Pat. No. 4,119,796. 
    
    
     DESCRIPTION OF THE PREFERRED EMBODIMENT 
     Preferably, the iron/lithium anode of the present invention is used in the thermal battery described in U.S. Pat. No. 4,119,796 incorporated by reference herein. With reference to FIG. 1, iron/lithium anode disc 10 is positioned in metal cup 11 by means of insulator ring 12, preferably made from Fiberfrax®. A thermal battery 15 utilizing the iron/lithium anode of the present invention comprises a metal housing 16, usually in cylindrical configuration and a plurality of cells 17 in stacked array. Each cell comprises an anode cup 11 in which iron/lithium anode 10 is positioned. Between metal housing 16 and cells 17 is a layer 18 of thermal and electrical insulation. Positioned between each of the cells 17 is an ignitable chemical heat source 20 which is ignited by fuse strip 21 which in turn is connected to an electrical match or squib (not shown) to activate the battery. 
     As described above, the asbestos separators disclosed in U.S. Pat. No. 4,119,796 can be eliminated. However, the depolarizer binder (Cab-O-Sil®) used in the preferred embodiment of the battery disclosed in that patent is not suitable for use with the anode material of the present invention. It has been found that SiO 2  reacts with the iron/lithium anode creating a self-discharge. Instead of a binder such as Cab-O-Sil® it is desirable to use a material such as MgO as the depolarizer binder. In such case approximately 50% by weight of MgO is preferred rather than 15% by weight of Cab-O-Sil® used in U.S. Pat. No. 4,119,796. 
     Also, it has been determined that it is preferable to use two layer anolyte-catholyte depolarizer 22 in each cell 17. The two layer depolarizer prevents the cell from short circuiting which has been found to be the case with homogeneous single layer depolarizer wafers when used without a separator with the anode material of the present invention. 
     Thermal batteries comprising a plurality of stacked cells as disclosed in U.S. Pat. No. 4,119,796 may thus be made using the iron/lithium anode by making the above modifications. The following examples are illustrative of the preferred method of making the anode material and the referenced modifications. 
     EXAMPLE 1 
     Method for Making Anode Strip 
     1640 grams of iron powder (apparent density 0.3 to 0.4 g/cc and Fisher sub-sieve size of 1.8 to 2.1 microns and having a surface area of about 50 m 2  /gm), 360 grams of lithium metal are weighed and placed in an argon purged glove box. The lithium is melted in a stainless steel crucible at 316° C. Approximately 700 to 800 grams of powdered iron are added to the molten lithium. The lithium is permitted to permeate the iron powder and mixed to obtain a homogeneous mass. The remaining iron powder is added and mixed until a homogeneous mass is obtained. 
     Thereafter the scrap anode strip is added to the homogeneous mixture and permitted to melt and mix therein. The materials balance comprises: 
     
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             Parts by weight                                              
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powdered iron  82.0                                                       
lithium metal  18.0                                                       
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     The molten mixture is poured into a graphite or boron-nitride mold and permitted to cool. After the material has cooled it is removed from the mold as an ingot and stored in a sealed container of argon gas or in an atmosphere of less than 5% relative humidity until rolled into sheets or strips. 
     The chemical analysis of the resulting sheet in this example is: 
     
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       Iron   82 ± 2%                                                  
       Lithium                                                            
              18 ± 1%                                                  
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     with an apparent density of 2.0 to 2.5 g/cc. 
     EXAMPLE 2 
     A preferred method for making the anolyte and catholyte layer of the depolarizer for use in the battery disclosed in U.S. Pat. No. 4,119,769 with the anode material of Example 1 is described below: 
     Anolyte Layer 23 
     A mixture of LiCl (45%) and KCl (55%) eutectic is blended with magnesium oxide (calcine @ 600° C. for 4 hours) in a ratio of 1 to 1 and fused at a temperature of from 380° to 395° C. for about 16 hours. The fused material is granulated and seived &lt;60 mesh screen. To the granulated powder is preferably added 2.5% by weight LiF which is mixed into the powder. The resulting mixture is placed in a press cavity together with the catholyte material and pressed into a wafer. 
     Catholyte Layer 24 
     The catholyte layer 24 comprises 25% (by wt.) electrolyte binder mix (LiCl-KCl eutectic) and 75% iron pyrite. 
     EXAMPLE 3 
     Thermal Battery 
     A thermal battery (A) was prepared in accordance with the disclosure of U.S. Pat. No. 4,119,769. A second battery 15 (B) was prepared in accordance with such disclosure, but modified in accordance with this disclosure using the iron/lithium anode material 10 prepared in accordance with Example 1 and the anolyte/catholyte depolarizer 22 material of Example 2. 
     Physical Dimensions 
     
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Number of Cells = 28  Load = 4 OHMS                                       
WEIGHT (GMS)     HEIGHT (INS) DIAM (INS)                                  
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Battery A                                                                 
Cell Assem                                                                
        8.08         .09          1.73                                    
Stack   265          2.49         1.73                                    
Battery 439          2.89         2                                       
Cell Anode                                                                
         .14 lithium                                                      
         .48 iron substrate                                               
        screen                                                            
Cathode 1.01                                                              
Asbestos                                                                  
         .87         .022                                                 
Cup     1.05                                                              
Battery B                                                                 
Cell Assem                                                                
        7.65         0.7          1.73                                    
Stack   251          2.25         1.73                                    
Battery 394          2.63         2                                       
Cell Anode                                                                
         .18 lithium                                                      
         .72 iron                                                         
Cathode 1.01 (50% MgO)                                                    
Cup     1.05                                                              
Fiber Ring                                                                
(to position                                                              
anode in                                                                  
cup)                                                                      
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     Table I compares the voltages of Batteries A and B at various times after ignition. Not only does Battery B of the present invention have a higher peak voltage, but supplies its specified minimum voltage (38 volts) for a greater period of time. 
     
                       TABLE 1                                                     
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A                 B                                                       
SEC      VOLTS        SEC        VOLTS                                    
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15       52.600       15         53.600                                   
30       45.200       30         51.600                                   
45       32.000       45         49.800                                   
60       16.600       60         46.000                                   
                      90         39.800                                   
                      120        30.600                                   
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     Tables II and III compare the electrical parameters of the Batteries A and B, respectively. 
     
                       TABLE II                                                    
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Cutoff Volts                                                              
            48         38 (Specifi-                                       
                                  16.6                                    
                       cation)                                            
Time, Seconds                                                             
            24.3243    38.1818    60                                      
Avg Volts   51.7183    48.7893    41.1                                    
Avg Amps    12.9296    12.1973    10.275                                  
Avg Amps/Sq In                                                            
            5.50051    5.18899    .677535                                 
Watt-Hours  4.51822    6.31165    7.03837                                 
Watt-Hrs/Lb                                                               
Cell Assem  9.05865    12.6543    14.1113                                 
Stack       7.73369    10.8035    12.0474                                 
Battery     4.6684     6.52144    7.27232                                 
Watt-Hrs/Cu In                                                            
Cell Assem  .762755    1.06552    1.1882                                  
Stack       .771945    1.07836    1.20252                                 
Battery     .497645    .695177    .77522                                  
PCT Efficiency                                                            
Anode       20.5116    30.3736    40.2076                                 
Cathode     19.3649    28.6755    37.9597                                 
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                       TABLE III                                                   
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Cutoff Volts                                                              
            48         38(specifi-                                        
                                  30.6                                    
                       cation)                                            
Time, Seconds                                                             
            52.1053    95.8696    120                                     
Avg Volts   51.8364    47.8497    45.125                                  
Avg Amps    12.9591    11.9624    11.2813                                 
Avg Amps/Sq In                                                            
            5.51306    5.08906    .743887                                 
Watt-Hours  9.72273    15.2432    16.9689                                 
Watt-Hrs/Lb                                                               
Cell Assem  20.5889    32.2791    35.9335                                 
Stack       17.5703    27.5466    30.6651                                 
Battery     11.1933    17.5487    19.5354                                 
Watt-Hrs/Cu In                                                            
Cell Assem  2.11033    3.30855    3.68312                                 
Stack       1.83833    2.88212    3.2084                                  
Battery     1.17675    1.84489    2.05375                                 
PCT Efficiency                                                            
Anode       26.9743    45.8135    54.0795                                 
Cathode     41.5763    70.6183    83.3544                                 
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