Abstract:
This invention provides a means to increase the energy density of two  eleochemical systems by using the by-product of each system as one of the necessary ingredients of the reactants of the other system. For example: 
     
       (a) 2Li+H.sub.2 O.sub.2 →2LiOH 
     
     
       (b) 2LiOH+3H.sub.2 O.sub.2 +2Al→2LiAlO.sub.2 ↓+4H.sub.2 O 
     
     where the LiOH from (a) is used in (b) and the H 2  O from (b) is used to fulfill the dilution requirements of (a).

Description:
STATEMENT OF GOVERNMENT INTEREST 
     The invention described herein may be manufactured and used by or for the Government of the United States of America for governmental purposes without the payment of any royalties thereon or therefor. 
    
    
     BACKGROUND OF THE INVENTION 
     (1) Field of the Invention 
     Each of two electrochemical systems has its energy density increased by using the by-product of the other system as one of the necessary ingredients of the reactants. In this way ingredients that would otherwise constitute a burden on one or the other system if used separately, thus reducing the overall energy density, instead contribute to the conversion of energy by increasing the overall energy density. 
     (2) Description of the Prior Art 
     It has been determined that an electrochemical energy source based on the overall reaction, 2Li+H 2  O 2  →2LiOH, could on a systems basis compete favorably with a thermal energy source for such applications as helicopter propulsion. One of the major systems problems in the development of an electrochemical energy source system is the reaction shown above is self-limiting unless the excess LiOH is either eliminated from the reaction site or is diluted with water to a usable concentration. Prior art techniques for the elimination of the LiOH or its dilution require the use of space and weight allowances which, as penalties to the system, effectively reduce its overall volumetric and gravimetric energy density. 
     SUMMARY OF THE INVENTION 
     The present invention provides a way to use the excess LiOH formed in the above reaction to produce more energy and at the same time produce by-products which allow the relatively easy removal of the lithium compound while producing sufficient water to perform the necessary dilution of some of the LiOH and the H 2  O 2 . An example of the proposed reactions constitute two electrochemical systems working in tandem as follows: ##STR1## Thus the LiOH produced in (a) is used in this invention as an electrolyte constituent and as a reactant in (b), another electrical energy producing reaction that produces a separable precipitate LiAlO 2  and in addition has a by-product of water. The water provides the necessary dilution to allow the productive use of LiOH as an electrolyte constituent in each of the reactions. This mitigates the use of non-productive devices to eliminate the LiOH formed in reaction (a) or the carrying of excess water for its dilution. 
    
    
     BRIEF DESCRIPTION OF THE DRAWING 
     The FIGURE is a schematic representation of the dual electrochemical system of the present invention. 
    
    
     DESCRIPTION OF THE PREFERRED EMBODIMENT 
     Referring now to the FIGURE there is shown the operation of the present system in schematic form. A lithium cell stack 10 is comprised of an anode of bipolar plates of lithium, a metallic intercell connector and a cathode comprised of a carbon graphite with or without catalyst. An aluminum cell stack 12 is comprised of an anode of bipolar plates of aluminum, a metallic intercell connector and a cathode comprised of a carbon graphite with or without catalyst. A reservoir 14 contains a quantity of hydrogen peroxide. Reservoir 14 is connected to both cell stacks 10 and 12 by means of conduits through respective metering valves 15 and 17, and pumps 16 and 18. A first electrolyte reservoir 20 of lithium hydroxide and water has its contents mix with the hydrogen peroxide from reservoir 14 and pass through pump 16 to lithium cell stack 10. A second electrolyte reservoir 22 of lithium hydroxide and water has its contents mix with the hydrogen peroxide from the same reservoir 14 and pass through pump 18 to the aluminum cell stack 12. A line from the lithium cell stack 10 connects to a gas vent 24 whose purpose is to vent collected gases in a first loop of the system to the ambient. The gas vent 24 is then connected through a line to a heat exchanger 26 for removal of excess heat. Conduits then extend from heat exchanger 26 to reservoir 20 and to reservoir 22. A line from aluminum cell stack 12 connects to a gas vent 28 whose purpose is to vent collected gases in a second loop of the system to the ambient. The gas vent then connects to a solid disposal device 30 for the elimination of solid wastes. A line then connects to a heat exchanger 32 for the elimination of excess heat. Conduits then connect from heat exchanger 32 to both reservoir 22 and to the first loop for conveying water rich lithium hydroxide. 
     The reactions involved in the first loop at lithium cell stack 10 can be expressed by the following equation: ##STR2## 
     The reactions involved in the second loop at aluminum cell stack 12 are: ##STR3## 
     In the operation of the first loop, lithium hydroxide and water are conducted to lithium cell stack 10 from reservoir 20 through pump 16, and hydrogen peroxide is conducted from reservoir 14 to lithium cell stack 10 through pump 16. The reactions of (eq. 1) and (eq. 2) are performed in lithium cell stack 10. The H 2  gas formed in (eq. 2) is then vented at gas vent 24. The excess heat appearing in the lithium hydroxide of (eq. 1) is removed by heat exchanger 26. The lithium hydroxide formed in both (eqs. 1 and 2) is then provided to both electrolyte reservoirs 20 and 22. 
     In the second operation of the loop, lithium hydroxide and water are conducted to aluminum cell stack 12 through pump 18, and hydrogen peroxide is conducted from reservoir 14 to aluminum cell stack 12 through pump 18. The reactions of (eq. 3) and (eq. 4) are performed in aluminum cell stack 12. The H 2  gas formed in (eq. 4) is then vented at gas vent 24. The LiAlO 2  precipitate formed in (eqs. 3 and 4) is removed at solid disposal device 30. The excess heat is removed by heat exchanger 32. The water formed in (eqs. 3 and 4) is then provided to both electrolyte reservoirs 20 and 22. 
     There has therefore been described a means of improving the volumetric and gravimetric energy density in electrochemical systems. A new feature is the use of two interdependent electrochemical reactions as a single energy source and the uniqueness of the electrochemistry of equation (3). 
     An alternative method may be the use of an alloy of lithium and aluminum so as to allow the two electrochemical reactions to take place simultaneously in one fuel cell or battery. 
     
         2Li.Al+H.sub.2 O.sub.2 →2LiAlO.sub.2 +4H.sub.2 O    (eq. 5) 
    
     It will be understood that various changes in details, materials, steps and arrangement of parts, which have been herein described and illustrated in order to explain the nature of the invention, may be made by those skilled in the art within the principle and scope of the invention as expressed in the appended claims.