those of skill in the art will appreciate that the invention may be embodied in other forms and manners not shown below . it is understood that the use of relational terms , if any , such as first , second , top and bottom , and the like are used solely for distinguishing one entity or action from another , without necessarily requiring or implying any such actual relationship or order between such entities or actions . although the concept of a gas battery is well established historically , the concept of an advanced , high - performance gas battery as claimed in this patent is made possible only by recent advances such as the creation of nano - materials . a practical format for storing in - situ developed gas in commercially competitive devices is provided only by materials with extremely high interfacial area such as nano - materials . many of these materials also are characterized by excellent electrochemical reversibility when used as substrates for gas production and consumption . gas batteries with these combined characteristics of high energy density and excellent catalytic reactivity can play a very important role in electric vehicle technology . for example , the charging time of gas batteries will be orders of magnitude shorter than that of solid - state based advanced batteries including lithium ion and nickel metal hydride batteries . gas batteries also may be deep - cycled unlike most existing advanced batteries . the major advantages of a gas battery , particularly for automotive applications , are tolerance to fast charging and deep discharging , simplicity , low cost , light weight , and long shelf life . most importantly a gas battery according to this disclosure can endure a high charging current . this means drastically reduced charging times . similarly , a gas battery can sustain high discharge currents and deep discharging . other batteries subjected to these conditions would suffer irreversible changes in electrode materials . in one embodiment , a gas battery operates using reversible oxidation and reduction reactions . during battery charging , electrolysis of the electrolyte takes place at the electrodes , which produces gases . these gases may be adsorbed on the electrodes if the electrodes are made of adsorbing material . one example of an adsorbing material is activated carbon . a reverse process takes place during battery discharge . fig1 shows an example of a gas battery that is constructed according to the techniques described herein . while specific materials and solutions are mentioned in the description of fig1 it will be apparent to one of skill in the art that other materials and solutions may be substituted and this description is in no way limiting . it will further be apparent that not all embodiments falling within the scope of this disclosure are specifically described . the example of fig1 includes electrodes 2 and 4 which can be either an anode or a cathode . the electrodes are preferably made from an adsorbing material such as , but not limited to , activated carbon . tunable nano - porous carbon , or another high surface area adsorbent created using nano - technology or other technology can be used to increase the adsorption of the gases created during charging . advances in nano - materials have led to materials with specific surface area much greater than 500 m 2 / g . the electrodes may be made of the same or different adsorbing materials to maximize adsorption capability thereby increasing battery capacity . similarly , the electrodes may be of the same or different geometry . different geometries can be used to attain greater adsorption of the working gas at the electrode . further , various geometries and configurations can be used to maximize charging current without bubble evolution . examples of electrode geometry include cylindrical , planar , and spherical electrodes ; examples of configurations are concentric and parallel electrodes . the electrodes 2 and 4 are housed in a gas tight vessel 8 . the vessel is sealed with gas tight fittings 10 . as will be appreciated , any suitable composition and structure for the vessel and gas tight fittings may be used . for , example , plastic would be suitable . in one embodiment the gas tight vessel 8 is filled with a liquid electrolyte 6 surrounding the electrodes 2 and 4 . this electrolyte can be any solution of chemical compounds which form positive and negative ions . the ions may be simple or complex . additives may be introduced into the electrolytes to improve performance . an example of electrolyte is a solution of nacl in water . working gases is this case could be hydrogen and chlorine . this combination of highly adsorbing electrodes and reversible reactions that generate and decompose adsorbed gases at the electrodes are key requirements for practicality of a gas battery . another key requirement is to provide enough ionic capacity in the form of electrolyte to achieve practically interesting levels . however , a large cell volume between the electrodes would result in poor power density . in principle , a compromise can be achieved by optimizing the shape and configuration of the electrodes . alternatively , a cell with flowing electrolyte ( flow battery ) can be used , however , the well - known drawbacks of flow - type batteries are various engineering , materials , and cost issues that may be hard to overcome . in another embodiment , the vessel can be divided by optional membrane 18 to create separate electrolyte compartments for the electrodes 2 and 4 . the membrane can be of any suitable construction . however , ideally the membrane should be impermeable to the liquid electrolyte 6 . the creation of separate electrolyte compartments for the anode and the cathode of the gas battery allows for use of electrolytes having different chemical compositions in each compartment . having different electrolytes in the anode and cathode compartments can maximize adsorption , and thereby battery capacity , by selecting ideal working gases for each electrode . in yet another embodiment , optional permselective membrane 16 can be disposed around the electrodes to prevent the adsorbed working gases from being spontaneously desorbed back into the electrolyte resulting in self discharge . the working gases considered to be effective for use in a high capacity gas battery are highly soluble in the electrolyte . for example , a gas battery constructed according to the example provided in this disclosure with a solution of nacl and water as electrolyte was found to have a self discharge rate approximately ten times higher than a commercial nimh battery . the permselective membrane 16 can be selected to be substantially impermeable to the working gas created in electrolyte 6 . further , if a different electrolyte is used in the anode and cathode compartments the permselective membrane surrounding each of the electrodes can be of different materials to optimize performance with the working gases found in each compartment . electrically conductive components 12 and 14 are electrically connected to the electrodes 2 and 4 and enable redox reactions at the electrodes . any suitable conductive material , such as graphite , can be used to construct these electrically conductive components . a simple , non - limiting , example of fig1 in operation is described below . the electrolyte for this example includes a simple water solution of table salt and the electrodes include activated carbon , preferably with a high surface area . in practice the electrolyte may be any solution which contains positive and negative ions . similarly , the electrodes may be of any composition or geometry as apparent to one skilled in the art . one advantage of the batteries according to this invention is the long shelf life . prior to operation this battery may be stored in one of several states including dry , charged , and discharged . if the battery is stored dry , the electrolyte must be introduced prior to usage . a current applied across the electrodes 2 and 4 , through the graphite rods 12 and 14 , charges the battery . during charging , the h + and cl − ions in simple electrolyte 6 of this example will be consumed to form hydrogen gas and chlorine gas at the electrodes . the hydrogen gas created during this charging cycle will be adsorbed on one electrode 2 and the chlorine gas will be adsorbed on the other electrode 4 . when a load , for example the electric motor of an automobile , is connected across the electrodes 2 and 4 through the graphite rods 12 and 14 , the battery is discharged . during discharge , or a load cycle , the gases will be desorbed from the electrodes and the reaction described above , with regard to the charge cycle , will proceed in the reverse direction . fig2 shows an example of a multi - cell battery 20 composed of multiple gas battery cells . in one embodiment the individual cells of the battery shown in fig2 can be constructed similarly to the battery described above in reference to fig1 . further , the individual battery cells in fig2 may be configured in series , parallel , or a combination of the two in order to deliver the desired voltage and current . in the example of fig2 the cells 24 a - 24 n and 26 a - 26 n of the multi - cell battery are contained in an outer enclosure 22 which may be of various constructions . the terminals of the various cells in the example of fig2 are connected in a series / parallel combination . the connecting elements 28 may be of any conductive material that is suitable for the application . the connecting elements connect the terminals of the various battery cells to external terminals 30 and 32 on the outer enclosure to provide for the load or charger to be connected . in other embodiments the multi - cell battery may contain cell balancing electronics to improve performance and battery life . fig3 shows a graph depicting a charge and discharge cycle of a gas battery constructed according to the example above with a simple nacl electrolyte solution . operation of the battery in the charging mode shows its ability for quick charge with minimal polarization . during discharge an almost ideal nernstian behavior is observed over long discharge times suggesting the potential for high energy density . further , the battery according to this invention allows for deep discharging without damage to the electrodes . a gas battery constructed according to this disclosure , having an electrolyte solution of water and nacl and activated carbon electrodes , was further tested for endurance over a series of charge - discharge cycles . the endurance testing was automated with a battery analyzer and charger controlled by a computer . prior to the endurance test the capacity of the battery was experimentally estimated as 0 . 5 ma - h . fig4 shows the data from the endurance test comprised of 1 , 000 charge - discharge cycles . the charge current was set at 25 ma or approximately 50 c . charging was stopped when the battery capacity of 0 . 5 ma - h was reached . the battery was then discharged at a current of 25 ma or approximately 50 c . discharging was stopped when the battery voltage dropped below 0 . 3 v . the battery voltage at the beginning of each discharge cycle was 1 . 5 - 2 v . discharge capacity was calculated for each charge - discharge cycle and round trip efficiency was estimated for each cycle as discharge capacity over charge capacity . fig5 shows the experimental data of fig4 approximated with a second order regression . the battery cycle life was calculated from the discharge capacity as a percentage of the initial discharge capacity . the battery lifetime was estimated as the number of charge / discharge cycles when the discharge capacity dropped below 80 % of its initial value . from the estimated data of fig5 the cycle life of the test battery was approximately 400 cycles . fig6 is a table showing the adsorption of various gases by one gram of activated carbon at 15 ° c . different electrolytes produce different gases . these working gases are adsorbed and desorbed at different capacities by different materials . for example the adsorption of carbon dioxide ( co 2 ) by activated carbon is an order of magnitude higher than adsorption of hydrogen ( h 2 ). selection of working gases is important in order to increase the specific energy density of gas batteries . data on adsorption of various gases by activated carbon suggest that gases with a higher boiling point may be more attractive candidates . examples of candidate working gases are , but are not limited to , so 2 , cl 2 , nh 3 , h 2 s , co 2 , o 2 , h 2 . preferably the electrodes have an adsorption capacity of the working gas as high as possible . the adsorption capacity of the working gas on the electrodes is preferably greater than 50 cm 3 / g . the effect of working gas selection on battery capacity was experimentally tested . a second example battery , using cl 2 and nh 3 as working gases instead of cl 2 and h 2 , was constructed . this was accomplished by using a saturated solution of nh 4 cl in water as electrolyte . the measured capacity of the example cl 2 / nh 3 battery was observed to be 5 . 5 times higher than for the cl 2 / h 2 battery . this increase in capacity is shown in fig7 . the observed increase in capacity demonstrates importance of selection of working gases to maximize battery capacity . in addition to using a single electrolyte compartment , anode and cathode compartments separated by a membrane may be used as described with reference to an embodiment of fig1 . the chemical composition of the electrolyte in the anode and cathode compartments may be different . in the case where different electrolytes are used in the anode and cathode compartments the membrane should be impermeable to the liquids comprising the electrolytes . another important parameter of any battery is self discharge rate . the example gas battery of fig1 with a nacl electrolyte was tested for self discharge by keeping the fully charged battery at open circuit and measuring self discharge current and voltage decline . self discharge tests were performed by charging the battery with a 25 ma current until the capacity of 0 . 5 ma - h was reached . discharge current and open circuit voltage were then monitored until the battery voltage dropped below 1 v . experimental results are shown in fig8 . a commercial nimh battery was tested for self discharge under the same conditions . the measured self discharge of gas battery was found to be 9 . 8 times higher than the measured self discharge of the commercial nimh battery . self discharge rate may be reduced by selection of active ingredients of the electrolyte . the operation of a gas battery with complex chemistry , such as cl 2 / nh 3 battery , for example , will require special measures to be taken against high self discharge . one option to reduce self discharge is to incorporate a permselective membrane surrounding the electrode . such a membrane should be impermeable to gases formed during electrolysis . operation of the battery at pressures above atmospheric and temperatures below or above room temperature may also improve performance by maximizing adsorption during charging and minimizing desorption in a no load state ( self discharge ). the description and drawings provided herein show exemplary embodiments of the invention . it will be appreciated to those skilled in the art that the preceding examples and embodiments are exemplary and not limiting to the scope of the present invention . it is intended that all permutations , enhancements , equivalents , combinations , and improvements thereto that are apparent to those skilled in the art upon a reading of the specification and a study of the drawings are included within the true spirit and scope of the present invention . it is therefore intended that the following appended claims include all such modifications , permutations and equivalents as fall within the true spirit and scope of the present invention .