초록 ▼

The object of the present invention is to obtain a carbon-monoxide removing technique capable of very effectively reducing/removing carbon monoxide present at one thousand of ppm to several % in a hydrogen-rich treatment-object gas such as a reformed gas obtained by reforming of a fuel such as natur

The object of the present invention is to obtain a carbon-monoxide removing technique capable of very effectively reducing/removing carbon monoxide present at one thousand of ppm to several % in a hydrogen-rich treatment-object gas such as a reformed gas obtained by reforming of a fuel such as natural gas, methanol, etc. to a concentration of several tens of ppm (preferably 10 ppm) or lower without excessive loss of hydrogen, even when carbon dioxide, methane are co-existent For accomplishing this object, there are provided two stages of CO removers for removing carbon monoxide from a hydrogen-containing treatment-object gas, the first-stage CO remover removing a portion of the carbon monoxide by methanation thereof through a catalyst reaction, the second-stage CO remover removing the remaining portion of the carbon monoxide mainly by oxidation thereof through a further catalyst reaction involving addition of an oxidizing agent.

대표청구항 ▼

1. A method of removing carbon monoxide from a hydrogen-containing treatment-object gas containing hydrogen as its major component and carbon dioxide, the method comprising:a first step of causing the treatment-object gas to contact a first metal catalyst comprising one or more kinds selected from t

1. A method of removing carbon monoxide from a hydrogen-containing treatment-object gas containing hydrogen as its major component and carbon dioxide, the method comprising:a first step of causing the treatment-object gas to contact a first metal catalyst comprising one or more kinds selected from the group consisting of Ru, Pt, Rh, and Pd and capable of methanating carbon monoxide at a temperature where methanation of carbon monoxide takes place by the first metal catalyst so that a portion of the carbon monoxide is removed through carbon monoxide methanation and where methanation of the carbon dioxide is restricted; and a second step of causing the treatment-object gas from the first step together with an oxidizing agent to contact a second metal catalyst capable of oxidizing carbon monoxide so that a remaining portion of carbon monoxide is removed mainly through carbon monoxide oxidation, wherein in the first step, a carbon monoxide concentration of the treatment-object gas is reduced to 30% or lower of an original carbon monoxide concentration of the treatment-object gas charged into the first step. 2. The method of removing carbon monoxide, according to claim 1, wherein in the second step, the second metal catalyst comprising one or more kinds selected from the group consisting of Ru, Pt, Rh and Pd is employed; andin the second step, a catalyst reaction layer is maintained at a temperature where oxidation of carbon monoxide takes place by the second metal catalyst involving addition of an oxidizing agent. 3. The method of removing carbon monoxide, according to claim 1, wherein a total amount of the oxidizing agent supplied at the second step is below about 3 chemical equivalents in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.4. The method of removing carbon monoxide, according to claim 1, wherein a total amount of the oxidizing agent supplied at the second step is below the chemical equivalent in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.5. The method of removing carbon monoxide, according to claim 1, wherein said hydrogen-containing treatment-object gas comprises a reformed gas supplied to a fuel cell as a fuel gas.6. The method of removing carbon monoxide, according to claim 1, wherein in the second step, the second metal catalyst comprising one or more kinds selected from the group consisting of Ru, Pt, Rh and Pd is employed; andin the second step, a catalyst reaction layer is maintained at a temperature where oxidation of carbon monoxide takes place by the second metal catalyst involving addition of an oxidizing agent. 7. The method of removing carbon monoxide, according to claim 1, wherein a total amount of the oxidizing agent supplied at the second step is below about 3 chemical equivalents in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.8. The method of removing carbon monoxide, according to claim 2, wherein a total amount of the oxidizing agent supplied at the second step is below about 3 chemical equivalents in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.9. The method of removing carbon monoxide, according to claim 6, wherein a total amount of the oxidizing agent supplied at the second step is below about 3 chemical equivalents in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.10. The method of removing carbon monoxide, according to claim 1, wherein a total amount of the oxidizing agent supplied at the second step is below the chemical equivalent in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.11. The method of removing carbon monoxide, according to claim 2, wherein a total amount of the oxidizing agent supplied at the second step is below the chemical equivalent in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.12. The method of removing carbon monoxide, according to claim 6, wherein a total amount of the oxidizing agent supplied at the second step is below the chemical equivalent in oxygen conversion relative to an amount of carbon monoxide originally contained in the treatment-object gas introduced in the first step.13. The method of removing carbon monoxide, according to claim 1, wherein said hydrogen-containing treatment-object gas comprises a reformed gas supplied to a fuel cell as a fuel gas.14. The method of removing carbon monoxide, according to claim 2, wherein said hydrogen-containing treatment-object gas comprises a reformed gas supplied to a fuel cell as a fuel gas.15. The method of removing carbon monoxide, according to claim 3, wherein said hydrogen-containing treatment-object gas comprises a reformed gas supplied to a fuel cell as a fuel gas.16. The method of removing carbon monoxide, according to claim 4, wherein said hydrogen-containing treatment-object gas comprises a reformed gas supplied to a fuel cell as a fuel gas.17. The method of removing carbon monoxide, according to claim 6, wherein said hydrogen-containing treatment-object gas comprises a reformed gas supplied to a fuel cell as a fuel gas.18. A method of operating a fuel cell system, where carbon monoxide is removed from a hydrogen-containing treatment-object gas containing hydrogen as its major component and carbon dioxide, comprising:a first step of causing the treatment-object gas to contact a first metal catalyst comprising one or more kinds selected from the group consisting of Ru, Pt, Rh, and Pd and capable of methanating carbon monoxide at a temperature where methanation of carbon monoxide takes place by the first metal catalyst so that a portion of the carbon monoxide is removed through carbon monoxide methanation and methanation of the carbon dioxide is restricted; a second step of causing the treatment-object gas from the first step together with an oxidizing agent to contact a second metal catalyst capable of oxidizing carbon monoxide so that a remaining portion of carbon monoxide is removed mainly through carbon monoxide oxidation; and using methane produced at the first step as a reforming fuel, wherein in the first step, a carbon monoxide concentration of the treatment-object gas is reduced to 30% or lower of an original carbon monoxide concentration of the treatment-object gas charged into the first step.