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An electrical generating system consists of a fuel cell, and an oxygen gas delivery. The fuel cell includes and anode channel having an anode gas inlet for receiving a supply of hydrogen gas, a cathode channel having a cathode gas inlet and a cathode gas outlet, and an electrolyte in communication w

An electrical generating system consists of a fuel cell, and an oxygen gas delivery. The fuel cell includes and anode channel having an anode gas inlet for receiving a supply of hydrogen gas, a cathode channel having a cathode gas inlet and a cathode gas outlet, and an electrolyte in communication with the anode and cathode channel for facilitating ion exchange between the anode and cathode channel. The oxygen gas delivery system is coupled to the cathode gas inlet and delivers oxygen gas to the cathode channel. The electrical current generating system also includes gas recirculation means couple to the cathode gas outlet for recirculating a portion of cathode exhaust gas exhausted from the cathode gas outlet to the cathode gas inlet.

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We claim: 1. An electrical current generating system comprising: a fuel cell including an anode channel including an anode gas inlet for receiving a supply of hydrogen gas, a cathode channel including a cathode gas inlet and a cathode gas outlet, and an electrolyte in communication with the anode a

We claim: 1. An electrical current generating system comprising: a fuel cell including an anode channel including an anode gas inlet for receiving a supply of hydrogen gas, a cathode channel including a cathode gas inlet and a cathode gas outlet, and an electrolyte in communication with the anode and cathode channel for facilitating ion exchange between the anode and cathode channel; and an oxygen gas delivery system coupled to the cathode gas inlet for delivering a gaseous stream enriched in oxygen gas to the cathode channel, the oxygen gas delivery system including a rotary pressure swing adsorption system for enriching oxygen in a gaseous feed, wherein the pressure swing adsorption system includes a first feed gas inlet for receiving air feed as a first gas feed, and a gas outlet coupled to the cathode gas inlet and the pressure swing adsorption system comprises a rotary module including a stator and a rotor rotatable relative to the stator, the rotor including a plurality of flow paths for receiving adsorbent material therein for preferentially adsorbing a first gas component in response to increasing pressure in the flow paths relative to a second gas component, and compression machinery coupled to the rotary module for facilitating gas flow through the flow paths for separating the first gas component from the second gas component, wherein the stator includes a first stator valve surface, a second stator valve surface, a plurality of first function compartments opening into the first stator valve surface, and a plurality of second function compartments opening into the second stator valve surface, and the rotor includes a first rotor valve surface in communication with the second stator valve surface, and a plurality of apertures provided in the rotor valve surfaces and in communication with respective ends of the flow paths and the function compartments; the oxygen gas delivery system includes a gas inlet for receiving a first portion of cathode gas exhausted from the cathode channel and a gas outlet for delivering the gaseous stream enrich in oxygen gas to the cathode channel; the gas separation system includes a second feed gas inlet; and the current generating system includes a first gas recirculation means coupled to the cathode gas outlet for recirculating a first portion of cathode exhaust gas exhausted from the cathode channel to the cathode gas inlet and a second gas recirculating means coupled to the cathode gas outlet for recirculating a second portion of the cathode exhaust gas to the second feed gas inlet. 2. The current generating system according to claim 1 where the oxygen gas delivery system includes a first gas recirculation means coupled to the cathode gas outlet for recirculating the first portion of cathode gas from the cathode channel to the cathode gas inlet. 3. The current generating system according to claim 2, wherein the first gas recirculating means comprises a compressor for supplying the first cathode exhaust gas portion under pressure to the cathode gas inlet. 4. The current generating system according to claim 3, wherein the first gas recirculation means includes a condensate separator coupled between the cathode gas outlet and the compressor for removing moisture from the first cathode exhaust gas portion. 5. The current generating system according to claim 3, wherein the first gas recirculating means directs the first cathode exhaust gas portion as feed gas to the gas separation system. 6. The current generating system according to claim 1 wherein the second gas recirculating means comprises a restrictive orifice for delivering the second cathode exhaust gas portion to the gas separation system at a pressure less than a pressure of the air feed. 7. The current generating system according to claim 1 wherein the plurality of flow paths are aligned with the axis of the rotor. 8. The current generating system according to claim 1 where the compression machinery is coupled to a portion of the function compartments for maintaining the portion of function compartments at a plurality of discrete respective pressure levels between an upper pressure and a lower pressure for maintaining uniform gas flow through the portion of function compartments. 9. The current generating system according to claim 1, wherein the function compartments include a light reflux exit compartment and a light reflux return compartment, the compression machinery comprises a light reflux expander coupled between the light reflux exit and return compartments, and the first gas recirculation means comprises a compressor coupled to the light reflux expander for supplying the first cathode exhaust gas portion under pressure to the cathode gas inlet. 10. The current generating system according to claim 9 wherein the rotary pressure swing adsorption system includes a heater disposed between the light reflux exit compartment and the light reflux expander for enhancing recovery of energy from light reflux gas exhausted from the light reflux exit compartment. 11. The current generating system according to claim 9 where the function compartments include a gas feed compartment and a countercurrent blowdown compartment, and the compression machinery comprises a compressor coupled to the first feed gas inlet for delivering compressed air to the gas feed compartment, and an expander coupled to the compressor for exhausting heavy product gas enriched in the first gas component from the countercurrent blowdown compartment. 12. The current generating system according to claim 9 where the function compartments include a countercurrent blowdown compartment and a heavy product compartment, and the compression machinery comprises an expander coupled to the countercurrent blowdown compartment. 13. The current generating system according to claim 1 where the function compartments include a gas feed compartment, and the gas recirculating means directs the first cathode exhaust gas portion as feed gas to the gas feed compartment. 14. The current generating system according to claim 1 where the function compartments include a gas feed compartment, and the current generating system includes second gas recirculating means coupled to the cathode gas outlet for recirculating a second portion of the cathode exhaust gas to the gas feed compartment. 15. The current generating system according to claim 14 where the second gas recirculating means comprises a restrictor orifice. 16. The current generating system according to claim 1 where the adsorbent material is one of Ca—X zeolite, Li—X zeolite, lithium chabazite zeolite, calcium -exchanged chabazite and strontium-exchanged chabazite. 17. The current generation system according to claim 1 where the rotary pressure swing adsorption system enriches oxygen and removes carbon dioxide from an air feed. 18. The current generation system according to claim 17 further comprising a hydrogen gas delivery system coupled to the anode gas inlet. 19. The current generation system according to claim 18 where the hydrogen gas delivery system enriches hydrogen gas in a gaseous feed. 20. The electrical current generation system according to claim 1 further where the pressure swing adsorption system generates a gaseous stream enriched in oxygen, the gaseous stream enriched in oxygen having a first oxygen purity and being fluidly coupled to the cathode gas inlet, the system further comprising a compressed air inlet for mixing compressed air with the gaseous stream enriched in oxygen upstream of the cathode gas inlet, thereby forming a cathode feed gas stream having a second oxygen purity lower than the first oxygen purity. 21. The electrical current generation system of claim 20, wherein the first oxygen purity is in the range of from about 70% to about 90% and the second oxygen purity is in the range of from about 30% to about 40%. 22. The system according to claim 1, wherein the rotary pressure swing adsorption system operates at an elevated temperature. 23. The system according to claim 1, wherein the rotary pressure swing adsorption system operates at a temperature greater than ambient temperature. 24. The system according to claim 1, wherein the rotary pressure swing adsorption system operates at a temperature of about 40° C. to about 60° C. 25. The system according to claim 1, wherein the rotary pressure swing adsorption system operates at a temperature greater than 100° C. 26. The system according to claim 20, wherein the first oxygen purity is in the range of about 60% to about 95%. 27. The system according to claim 20, wherein the second oxygen purity is in the range of about 30% to about 50%. 28. An electrical current generating system comprising: a fuel cell including an anode channel including an anode gas inlet for receiving a supply of hydrogen gas, a cathode channel including a cathode gas inlet and a cathode gas outlet, and an electrolyte in communication with the anode and cathode channel for facilitating ion exchange between the anode and cathode channel; and an oxygen gas delivery system coupled to the cathode gas inlet for delivering a gaseous stream enriched in oxygen gas to the cathode channel, the oxygen gas delivery system including a rotary pressure swing adsorption system for enriching oxygen in a gaseous feed, wherein the pressure swing adsorption system includes a first feed gas inlet for receiving air feed as a first gas feed, and a gas outlet coupled to the cathode gas inlet; the oxygen gas delivery system includes a gas inlet for receiving a first portion of cathode gas exhausted from the cathode channel, a gas outlet for delivering the gaseous stream enrich in oxygen gas to the cathode channel, a first gas recirculation means coupled to the cathode gas outlet for recirculating the first portion of cathode gas from the cathode channel to the cathode gas inlet, wherein the first gas recirculating means comprises a compressor for supplying the first cathode exhaust gas portion under pressure to the cathode gas inlet and directs the first cathode exhaust gas portion as feed gas to the gas separation system; and the rotary pressure swing adsorption system comprises a rotary module for implementing a pressure swing adsorption process having an operating pressure cycling between an upper pressure and a lower pressure, for extracting a first gas fraction and a second gas fraction from a gas mixture including the first and second fractions, the rotary module comprising: a stator including a first stator valve surface, a second stator valve surface a plurality of first function compartments opening into the first stator valve surface, and a plurality of second function compartments opening into the second stator valve surface; and a rotor rotatably coupled to the stator and including a first rotor valve surface in communication with the first stator valve surface, a second rotor valve surface in communication with the second stator valve surface, a plurality of flow paths for receiving adsorbent material therein, each said flow path including a pair of opposite ends, and a plurality of apertures provided in the rotor valve surfaces and in communication with the flow path ends and the functions ports for cyclically exposing each said flow path to a plurality of discrete pressure levels between the upper and lower pressure for maintaining uniform gas flow through the first and second function compartments, the function compartments comprising first and second gas feed compartments opening into the first stator valve surface for delivering the gas mixture to the flow paths for sequentially exposing the flow paths to the second feed gas prior to the first feed gas. 29. The current generation system according to claim 28 where the second feed gas is enriched in oxygen relative to the first feed gas.