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A fuel processor system is provided including an autothermal reactor (ATR), a pressure swing adsorber (PSA) located downstream of the ATR, and a methanation reactor located downstream of the PSA. A method of operating of proton exchange membrane fuel cell stack involves cooling the methanator output

A fuel processor system is provided including an autothermal reactor (ATR), a pressure swing adsorber (PSA) located downstream of the ATR, and a methanation reactor located downstream of the PSA. A method of operating of proton exchange membrane fuel cell stack involves cooling the methanator output and feeding it into the stack as an anode fuel.

대표청구항 ▼

We claim: 1. A system comprising: a first reactor that produces a first hydrogen-rich gas stream containing carbon monoxide; an adsorbent apparatus comprising multiple staged fixed beds where the adsorbent apparatus is located downstream from the first reactor comprising a vessel housing an adsorbe

We claim: 1. A system comprising: a first reactor that produces a first hydrogen-rich gas stream containing carbon monoxide; an adsorbent apparatus comprising multiple staged fixed beds where the adsorbent apparatus is located downstream from the first reactor comprising a vessel housing an adsorbent adapted to adsorb carbon monoxide and further wherein the adsorbent apparatus comprises rotating valves to direct the flow of gases into and out of the multiple staged fixed beds, wherein the apparatus reduces the amount of carbon monoxide in the first gas stream to produce a second hydrogen-rich gas stream containing carbon monoxide; a methanation reactor downstream from the adsorbent apparatus; and a heat exchanger disposed between the adsorbent apparatus and the methanation reactor that raises the temperature of the second hydrogen rich stream before entry into the methanation reactor, wherein the downstream components are sized to reduce the concentration of carbon monoxide to a level suitable for use in a PEM fuel cell stack. 2. A system according to claim 1, wherein the adsorbent apparatus comprises a pressure swing adsorber. 3. A system according to claim 1, wherein the adsorbent removes carbon dioxide from the first gas stream. 4. A system according to claim 1, further comprising one or more water gas shift reactors disposed between the first reactor and the adsorbent apparatus. 5. A system according to claim 1, wherein the methanation reactor comprises an active metal-containing catalyst. 6. A system according to claim 5, wherein the methanation reactor catalyst is supported on an oxide. 7. A system according to claim 5, wherein the methanation reactor catalyst is coated on a substrate. 8. A system according to claim 1, further comprising a recuperator disposed in such a way that the output stream of the pressure swing adsorber is heated in the recuperator by the methanator output stream before input into the methanator. 9. A fuel processor system to produce hydrogen from a liquid or gaseous fuel for use in a PEM fuel cell, comprising: an autothermal reactor that produces a hydrogen-rich first gas stream containing carbon monoxide; a pressure swing adsorber downstream of the autothermal reactor sized to reduce the carbon monoxide level in the first stream and produce a second hydrogen-rich gas stream containing greater than 5 ppm carbon monoxide wherein the pressure swing adsorber further comprises rotating valves to direct the flow of gases into and out of multiple staged fixed beds therein; a methanation reactor downstream of the pressure swing adsorber that is sized to reduce the carbon monoxide level of the second stream below 5 ppm; and a heat exchanger disposed between the pressure swing adsorber and the methanation reactor that raises the temperature of the second hydrogen rich stream before entry into the methanation reactor. 10. A system according to claim 9, wherein the pressure swing adsorber is sized to produce a stream containing less than 400 ppm carbon monoxide. 11. A system according to claim 9, wherein the pressure swing adsorber is sized to produce a stream containing less than 100 ppm carbon monoxide. 12. A system according to claim 9, wherein the pressure swing adsorber contains an adsorbent that removes carbon dioxide. 13. A system according to claim 9, further comprising a recuperator in which the output stream of the pressure swing adsorber is heated by the output stream of the methanation reactor before being input into the methanation reactor. 14. A system according to claim 9, further comprising a fuel cell stack disposed to receive the methanator output stream as anode fuel. 15. A system comprising: a first reactor that produces a first hydrogen-rich gas stream containing carbon monoxide; an adsorbent apparatus downstream from the first reactor comprising a vessel housing an adsorbent adapted to adsorb carbon monoxide, wherein the apparatus reduces the amount of carbon monoxide in the first gas stream to produce a second hydrogen-rich gas stream containing carbon monoxide; a methanation reactor downstream from the adsorbent apparatus, wherein the downstream components are sized to reduce the concentration of carbon monoxide to a level suitable for use in a PEM fuel cell stack; and a heat exchanger disposed between the adsorbent apparatus and the methanation reactor that raises the temperature of the second hydrogen rich stream before entry into the methanation reactor. 16. A fuel processor system to produce hydrogen from a liquid or gaseous fuel for use in a PEM fuel cell, comprising: an autothermal reactor that produces a hydrogen-rich first gas stream containing carbon monoxide; a pressure swing adsorber downstream of the autothermal reactor sized to reduce the carbon monoxide level in the first stream and produce a second hydrogen-rich gas stream containing greater than 5 ppm carbon monoxide; a methanation reactor downstream of the pressure swing adsorber that is sized to reduce the carbon monoxide level of the second stream below 5 ppm; and a heat exchanger that raises the temperature of the second stream before input into the methanation reactor.