text: fig1 and fig2 show schematic views of an embodiment of a single flow regenerative electrochemical cell 100 with an evolved oxygen recovery system 200 . the regenerative electrochemical cell 100 may have the same or substantially similar configuration as the electrochemical cell described in u . s . provisional patent application no . 61 / 054 , 364 , filed on may 19 , 2008 , and u . s . patent application ser . no . 12 / 385 , 489 , filed on apr . 9 , 2009 , the contents of both of which are incorporated herein by reference in their entireties . fig1 shows the electrochemical cell 100 and the evolved oxygen recovery system 200 in a discharge mode , connected to an external load 300 . the regenerative electrochemical cell 100 of the illustrated single flow embodiment includes an oxygen reduction cathode 110 , an electrolyte solution 120 , an oxygen evolution anode 130 ( also referred to as a charging anode ), a metal fuel electrode 140 , an electrolyte path 150 , and a flow generator 160 for circulating the electrolyte solution 120 . in the illustrated embodiment , the flow generator 160 is a pump . in such a single flow embodiment , the oxygen evolution anode 130 is disposed within the electrochemical cell 100 between the oxygen reduction cathode 110 and the metal fuel electrode 140 , thereby allowing the electrochemical cell 100 to operate in discharge and recharge modes without needing to reverse the circulation of the electrolyte solution 120 . electricity is generated through an oxidation / reduction reaction that occurs between the oxygen reduction cathode 110 and the metal fuel electrode 140 . the oxygen reduction cathode 110 may be a passive or “ breathing ” cathode that passively accepts gasses it is exposed to . the oxygen reduction cathode 110 is generally gas permeable , but not liquid permeable , thereby allowing the intake of gasses such as oxygen , without releasing the electrolyte solution 120 from the electrochemical cell 100 . the oxygen reduction cathode 110 may include a catalyst material , such as manganese oxide , nickel , silver , pyrolized cobalt , activated carbon , platinum , or any other catalyst material or mixture of materials with high oxygen reduction activity in the electrolyte for catalyzing reduction of an oxidizer . during discharge , or electricity generating , mode , as depicted in the embodiment of fig1 , the metal fuel electrode 140 acts as an anode . in an embodiment , the metal fuel electrode 140 may contain a filter body ( not shown ) made of any formation able to capture and retain , through filtering , electrodepositing , or otherwise , particles or ions of metal fuel from the electrolyte solution 120 . in addition , the filter body may be formed from a conductive material . embodiments of such a filter body are discussed in greater detail in u . s . provisional patent application no . 61 / 064 , 955 , filed apr . 4 , 2008 , and u . s . patent application ser . no . 12 / 385 , 217 , filed apr . 1 , 2009 , the contents of both of which are incorporated herein by reference in their entireties . electricity that can be drawn by the external load 300 is generated when an oxidizer at the oxygen reduction cathode 110 is reduced , while the metal fuel at the metal fuel electrode 140 is oxidized to an oxidized form . the external load 300 is electrically connected to both the oxygen reduction cathode 110 and the metal fuel electrode 140 to complete an electrical circuit . the electrical potential of the electrochemical cell 100 is depleted once the metal fuel at the metal fuel electrode 140 is entirely oxidized . the electrolyte solution 120 can be circulated passively , such as through gravity , through motion of the device , or any other process that transports the oxidized metal fuel ions away from the metal fuel electrode 140 and through a gap towards the oxygen reduction cathode 110 . this “ transport flow ” of the electrolyte solution 120 , can also be accomplished in some embodiments with the flow generator 160 . when the flow generator 160 is a pump , it may have any suitable construction or configuration , including but not limited to piezoelectric , centrifugal , gear , flexible impeller , peristaltic , or any other type of pump . any other method of circulating the electrolyte solution 120 from the metal fuel electrode 140 towards the oxygen reduction cathode 110 during discharge mode may be used . the electrolyte solution 120 will then enter the electrolyte path 150 , which has an entrance in the discharge direction of flow of the electrolyte solution 120 disposed between the electrolyte side of the oxygen reduction cathode 110 and the metal fuel electrode 140 , where it directs the electrolyte solution 120 back to the metal fuel electrode 140 . in some embodiments , the flow generator 160 may be disposed between the electrolyte path 150 and the metal fuel electrode 140 , or within the electrolyte path 150 . while the illustrated embodiment is operating in discharge mode , as described above , the oxygen evolution anode 130 is inoperative and is configured to allow the electrolyte solution 120 to flow therethrough . the oxygen evolution anode 130 , which can also be described as a charging electrode , is depicted as a separate electrode in the illustrated embodiment because generally most electrodes suitable for function as an oxygen reduction cathode do not perform well as an anode when being used for charging purposes . the electrochemical cell is not intended to be limited , however , and it is possible for the oxygen evolution anode 130 and the oxygen reduction cathode 110 to be the same electrode , with the flow of the electrolyte solution 120 modified accordingly . in embodiments where the oxygen evolution anode 130 is separate , it should be permeable to the electrolyte solution 120 , thereby allowing for the flow of the electrolyte solution 120 from the metal fuel electrode 140 through the oxygen evolution anode 130 , and to the oxygen reduction cathode 110 . in charging mode , as depicted in fig2 , a power supply 310 is connected to the metal fuel electrode 140 , which becomes a cathode , and to the oxygen evolution anode 130 , and the circuit to the external load 300 is intercepted . details of the charging mode are provided in u . s . provisional patent application no . 61 / 054 , 364 , filed may 19 , 2008 , and u . s . patent application ser . no . 12 / 385 , 489 , filed on apr . 9 , 2009 , the contents of both of which are incorporated herein by reference in their entireties . by supplying an electrical current across the metal fuel electrode 140 and the oxygen evolution anode 130 , the metal fuel of the metal fuel electrode 140 , which was converted from a metal to an oxidized form , including but not limited to spent metal fuel oxide , metal fuel hydroxide , and metal fuel hydroxide anions , during discharge mode , is reduced from the oxidized form back to the metal fuel . at the same time , the oxygen evolution anode 130 oxidizes hydroxide ions that are generated during the reduction of the oxidized metal fuel , and are present in the electrolyte solution 120 . oxidation of the hydroxide ions evolves oxygen , which flows within the electrolyte solution 120 . the evolved oxygen may be recycled by the evolved oxygen recovery system 200 . the evolved oxygen recovery system 200 contains an oxygen separator 210 that is configured to separate evolved oxygen from the electrolyte solution 120 . in the illustrated embodiments , the oxygen separator 210 is disposed within the electrolyte path 150 . the oxygen separator 210 may alternatively be located anywhere within the electrochemical cell 100 that is in contact with the electrolyte solution 120 . the oxygen separator 210 may be of any suitable construction or configuration , including but not limited to a reversed u - tube which may provide space for the evolved oxygen to bubble out of the electrolyte solution 120 . the evolved oxygen recovery system 200 additionally has an oxygen recovery path 220 , through which separated oxygen 230 is directed back to the air side of the oxygen reduction cathode 110 for use as an oxidizer during the discharge mode as discussed above . the oxygen recovery path 220 can be of any suitable construction or configuration . in an embodiment , the separated oxygen 230 is not released to the ambient air outside of the electrochemical cell 100 or the evolved oxygen recovery system 200 , but is instead fully contained within the combination of the electrochemical cell 100 and the evolved oxygen recovery system 200 . in an embodiment , the evolved oxygen recovery system 200 may include a recovery flow generator 240 , configured to generate a flow of the separated oxygen 230 within the oxygen recovery path 220 . the recovery flow generator 240 can be of any suitable construction or configuration , including but not limited to a pump , a vacuum , a turbine , a fan , or any other suitable flow generating device . in an embodiment , the evolved oxygen recovery system 200 may include an accumulating vessel 250 . the accumulating vessel 250 can be of any construction or configuration configured to provide space for the separated oxygen 230 to gather without releasing the separated oxygen 230 to the ambient air outside of the electrochemical cell 100 or the evolved oxygen recovery system 200 . in an embodiment , the evolved oxygen recovery system 200 may have a flow regulator 260 , configured to selectively limit the flow of the separated oxygen 230 within the oxygen recovery path 220 to the oxygen reduction cathode 110 . the flow regulator 260 may have any suitable construction or configuration , including a valve , a pressure regulator , a gate , a clamp , or any other such device that can limit the flow of the separated oxygen 230 . in an embodiment that contains both a flow regulator 260 and a recovery flow generator 240 , there may be a controller ( not shown ) that can selectively control the operation of both the recovery flow generator 240 and the flow regulator 260 . such a controller may be used to prevent excessive buildups of oxygen within the evolved oxygen recovery system 200 , such as between the flow regulator 260 and the oxygen separator 210 . although the oxidizer that the oxygen reduction cathode 110 is initially exposed to will eventually become separated oxygen 260 that is evolved during operation of the electrochemical cell 100 , the initial supply of oxidizer may come from oxygen that is sealed in the evolved oxygen recovery system 200 at the time of the manufacture or assembly of the system and electrochemical cell 100 . the evolved oxygen recovery system 200 may also be assembled with an initial supply of pure oxygen , or any other gaseous mixture containing oxygen contained within it , for use by the cell , and ultimate separation by the oxygen separator 210 . in an embodiment , air may be used during initial operation of the electrochemical cell 100 until enough oxygen is separated from the electrolyte solution 120 to support further operation of the electrochemical cell 100 , or until the metal fuel is fully oxidized . once enough oxygen has been accumulated , the external air may be shut off from the oxygen reduction cathode 110 . fig3 and fig4 show schematic views of an embodiment of a reversible flow regenerative electrochemical cell 400 with an evolved oxygen recovery system 200 . as illustrated , operation of the evolved oxygen recovery system is as described above for the electrochemical cell 100 . in the reversible flow regenerative electrochemical cell 400 , the metal fuel electrode 440 is disposed between the oxygen reduction cathode 410 and the oxygen evolution anode 430 . details of the embodiment of the regenerative electrochemical cell 400 are discussed in u . s . provisional patent application no . 61 / 054 , 364 , filed may 19 , 2008 and u . s . patent application ser . no . 12 / 385 , 489 , filed on apr . 9 , 2009 , the contents of both of which are incorporated herein by reference in their entireties . fig3 shows the electrochemical cell 400 and the evolved oxygen recovery system 200 in a discharge mode , connected to an external load 300 . the regenerative electrochemical cell 400 of the illustrated reversible flow embodiment includes an oxygen reduction cathode 410 , an electrolyte solution 420 , an oxygen evolution anode 430 , a metal fuel electrode 440 , an electrolyte path 450 , and a reversible flow generator 460 for circulating the electrolyte solution 420 . in the illustrated embodiment , the reversible flow generator 460 is a pump . in such an embodiment , the metal fuel electrode 440 is disposed within the electrochemical cell 400 between the oxygen reduction cathode 410 and the oxygen evolution anode 430 , thereby making a flow reversal desirable to allow the electrochemical cell 400 to operate in discharge and recharge modes . as illustrated in fig3 , the electrolyte solution 420 flows from the metal fuel electrode 440 to the oxygen reduction cathode 410 during discharge mode . generation of electricity occurs through an oxidation / reduction reaction occurring between the oxygen reduction cathode 410 and the metal fuel electrode 440 . the oxygen reduction cathode 410 may be a passive or “ breathing ” cathode that passively accepts gasses it is exposed to . the oxygen reduction cathode 410 is generally gas permeable , but not liquid permeable , thereby allowing the intake of gasses such as oxygen , without releasing the electrolyte solution 420 from the electrochemical cell 400 . the oxygen reduction cathode 410 may include a catalyst material , such as manganese oxide , nickel , silver , pyrolized cobalt , activated carbon , platinum , or any other catalyst material or mixture of materials with high oxygen reduction activity in the electrolyte for catalyzing reduction of an oxidizer . during discharge mode , as depicted in the embodiment of fig3 , the metal fuel electrode 440 acts as an anode . in an embodiment , the metal fuel electrode 440 may contain a filter body ( not shown ) made of any formation able to capture and retain , through filtering , electrodepositing , or otherwise , particles of metal fuel from the electrolyte solution 420 . embodiments of such a filter body are discussed in greater detail in u . s . provisional patent application no . 61 / 064 , 955 , filed apr . 4 , 2008 , and u . s . patent application ser . no . 12 / 385 , 217 , filed apr . 1 , 2009 , the contents of both of which are incorporated herein by reference in their entireties . in addition , the filter body may be formed from a conductive material . electricity that can be drawn by the external load 300 is generated when an oxidizer at the oxygen reduction cathode 410 is reduced , while the metal fuel at the metal fuel electrode 440 is oxidized to a metal oxidized form , as described above . the external load 300 is electrically connected to both the oxygen reduction cathode 410 and the metal fuel electrode 440 to complete an electrical circuit . the electrical potential of the electrochemical cell 400 is depleted once the metal fuel at the metal fuel electrode 440 is entirely oxidized . the electrolyte solution 420 can be circulated passively , such as through gravity , through motion of the device , or any other process that transports the oxidized metal fuel ions away from the metal fuel electrode 440 and through a gap towards the oxygen reduction cathode 410 . this “ transport flow ” of the electrolyte solution 420 , can also be accomplished in some embodiments with the reversible flow generator 460 . when the reversible flow generator 460 is a pump , it may have any suitable construction or configuration , including but not limited to piezoelectric , centrifugal , gear , flexible impeller , peristaltic , or any other type of pump . any other method of circulating the electrolyte solution 420 from the metal fuel electrode 440 towards the oxygen reduction cathode 410 during discharge mode may be used . the electrolyte solution 420 will then enter the electrolyte path 450 , which has an entrance in the discharge direction of flow of the electrolyte solution 420 disposed between the electrolyte side of the oxygen reduction cathode 410 and the metal fuel electrode 440 , where it directs the electrolyte solution 420 back to the metal fuel electrode 440 , passing through the oxygen evolution anode . in some embodiments , the reversible flow generator 460 may be disposed between the electrolyte path 450 and the metal fuel electrode 440 , or within the electrolyte path 450 . while the illustrated embodiment is operating in discharge mode , as described above , the oxygen evolution anode 430 is inoperative . the oxygen evolution anode 430 , which can also be described as a charging electrode , is depicted as a separate electrode in the illustrated embodiment because generally most electrodes suitable for function as an oxygen reduction cathode do not perform well as an anode when being used for charging purposes . the electrochemical cell is not intended to be limited , however , and it is possible for the oxygen evolution anode 430 and the oxygen reduction cathode 410 to be the same electrode , with the flow of the electrolyte solution 420 modified accordingly . in embodiments where the oxygen evolution anode 430 is separate , it should be permeable to the electrolyte solution 420 , thereby allowing for the flow of the electrolyte solution 420 from the electrolyte path 450 to the metal fuel electrode 440 through the oxygen evolution anode 430 . as illustrated in fig4 , during recharge mode the electrolyte solution 420 must flow opposite to that of discharge mode , from the metal fuel electrode 440 to the oxygen evolution anode 430 . the reversible flow generator 460 may be configured to switch the flow of the electrolyte solution 420 during operation of the reversible flow electrochemical cell 400 , and may include a means for reversing the flow . flow reversal can be achieved through any suitable construction , including but not limited to a controllable electrolyte gate system , or the use of multiple pumps facing opposite directions of flow , wherein only one is activated to achieve the desired flow direction . in recharge mode , a power supply 310 is connected to the metal fuel electrode 440 and to the oxygen evolution anode 430 , and the circuit to the external load 300 is intercepted . by supplying an electrical current across the metal fuel electrode 440 and the oxygen evolution anode 430 , the metal fuel of the metal fuel electrode 440 , which was converted from a metal to an oxidized fowl , including but not limited to spent metal fuel oxide , metal fuel hydroxide , and metal fuel hydroxide anions , during discharge mode , is reduced from the oxidized form back to the metal fuel . at the same time , the oxygen evolution anode 430 oxidizes hydroxide ions generated during the reduction of the oxidized metal fuel , and are present in the electrolyte solution 420 . oxidation of the hydroxide ions evolves oxygen , which travels within the electrolyte solution 420 , before entering the evolved oxygen recovery system 200 as described above . the foregoing illustrated embodiments have been provided solely for illustrating the structural and functional principles of the present invention are not intended to be limited . for example , the electrochemical cell in the present invention maybe practiced using different fuels , oxidizers , electrolytes , and or different overall structural configuration or materials . thus , the present invention is intended to encompass all modifications , substitutions , alternations , and equivalents within the spirit and scope of the following appended claims .