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When the production of hydrogen and the recovery of carbon dioxide are simultaneously performed by using as a raw material a carbon-containing fuel, the increase of the system cost is suppressed and the efficiency is improved. Disclosed is a method for producing hydrogen and recovering carbon dioxid

When the production of hydrogen and the recovery of carbon dioxide are simultaneously performed by using as a raw material a carbon-containing fuel, the increase of the system cost is suppressed and the efficiency is improved. Disclosed is a method for producing hydrogen and recovering carbon dioxide which method produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, including: a hydrogen-containing gas producing step of obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel; a PSA step of separating, by using a pressure swing adsorption apparatus, the hydrogen-containing gas into a first hydrogen-enriched gas that is a gas enriched in hydrogen and a PSA offgas that is a gas enriched in the components other than hydrogen; and a step of obtaining, by treating the PSA offgas with a hydrogen separation membrane and a carbon dioxide separation membrane, a second hydrogen-enriched gas that is a gas enriched in hydrogen and a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide. Also disclosed is an apparatus for embodying the method.

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1. A method for producing hydrogen and recovering carbon dioxide which method produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, the method comprising the combination of steps of: a hydrogen-containing gas producing step of obtaining a hydrogen-containing gas that contains

1. A method for producing hydrogen and recovering carbon dioxide which method produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, the method comprising the combination of steps of: a hydrogen-containing gas producing step of obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel;a PSA step of separating the hydrogen-containing gas with the use of a pressure swing adsorption apparatus into a first hydrogen-enriched gas that is a gas enriched in hydrogen and a PSA offgas that is a gas enriched in the components other than hydrogen;a carbon dioxide membrane-separating step of separating the PSA offgas with the use of a carbon dioxide separation membrane into a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide and a carbon dioxide separation membrane offgas that is a gas enriched in the components other than carbon dioxide;a hydrogen membrane-separating step of separating the carbon dioxide separation membrane offgas with the use of a hydrogen separation membrane into a second hydrogen-enriched gas that is a gas enriched in hydrogen and a hydrogen separation membrane offgas that is a gas enriched in the components other than hydrogen; anda step of obtaining liquefied carbon dioxide by liquefying the carbon dioxide-enriched gas. 2. The method claim 1 comprising a step of recycling the second hydrogen-enriched gas to the hydrogen-containing gas producing step or to the PSA step. 3. The method of claim 1, wherein the ratio α of the carbon dioxide permeability coefficient to the hydrogen permeability coefficient of the carbon dioxide separation membrane is 5 or more. 4. An apparatus for producing hydrogen and recovering carbon dioxide which apparatus produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, the apparatus comprising: a hydrogen-containing gas producing apparatus for obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel;a pressure swing adsorption apparatus for separating the hydrogen-containing gas into a first hydrogen-enriched gas that is a gas enriched in hydrogen and a PSA offgas that is a gas enriched in the components other than hydrogen;a carbon dioxide separation membrane for separating the PSA offgas into a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide and a carbon dioxide separation membrane offgas that is a gas enriched in the components other than carbon dioxide;a hydrogen separation membrane for separating the carbon dioxide separation membrane offgas into a second hydrogen-enriched gas that is a gas enriched in hydrogen and a hydrogen separation membrane offgas that is a gas enriched in the components other than hydrogen; anda carbon dioxide liquefier for obtaining liquefied carbon dioxide by liquefying the carbon dioxide-enriched gas. 5. The apparatus of claim 4, comprising a recycle line for recycling the second hydrogen-enriched gas to the hydrogen-containing gas producing step or to the PSA step. 6. The apparatus of claim 4, wherein the ratio α of the carbon dioxide permeability coefficient to the hydrogen permeability coefficient of the carbon dioxide separation membrane is 5 or more. 7. A method for producing hydrogen and recovering carbon dioxide which method produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, the method comprising the combination of steps of: a hydrogen-containing gas producing step of obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel;a PSA step of separating the hydrogen-containing gas with the use of a pressure swing adsorption apparatus into a first hydrogen-enriched gas that is a gas enriched in hydrogen and a PSA offgas that is a gas enriched in the components other than hydrogen;a hydrogen membrane-separating step of separating the PSA offgas with the use of a hydrogen separation membrane into a second hydrogen-enriched gas that is a gas enriched in hydrogen and a hydrogen separation membrane offgas that is a gas enriched in the components other than hydrogen;a carbon dioxide membrane-separating step of separating the hydrogen separation membrane offgas with the use of a carbon dioxide separation membrane into a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide and a carbon dioxide separation membrane offgas that is a gas enriched in the components other than carbon dioxide; anda step of obtaining liquefied carbon dioxide by liquefying the carbon dioxide-enriched gas. 8. The method of claim 7, comprising a step of recycling the second hydrogen-enriched gas to the hydrogen-containing gas producing step or to the PSA step. 9. The method of claim 7, wherein the ratio α of the carbon dioxide permeability coefficient to the hydrogen permeability coefficient of the carbon dioxide separation membrane is 5 or more. 10. The method of claim 7, wherein the ratio α of the carbon dioxide permeability coefficient to the hydrogen permeability coefficient of the carbon dioxide separation membrane is 100 or less. 11. An apparatus for producing hydrogen and recovering carbon dioxide which apparatus produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, the apparatus comprising: a hydrogen-containing gas producing apparatus for obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel;a pressure swing adsorption apparatus for separating the hydrogen-containing gas into a first hydrogen-enriched gas that is a gas enriched in hydrogen and a PSA offgas that is a gas enriched in the components other than hydrogen;a hydrogen separation membrane for separating the PSA offgas into a second hydrogen-enriched gas that is a gas enriched in hydrogen and a hydrogen separation membrane offgas that is a gas enriched in the components other than hydrogen;a carbon dioxide separation membrane for separating the hydrogen separation membrane offgas into a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide and a carbon dioxide separation membrane offgas that is a gas enriched in the components other than carbon dioxide; anda carbon dioxide liquefier for obtaining liquefied carbon dioxide by liquefying the carbon dioxide-enriched gas. 12. The apparatus of claim 11, comprising a recycle line for recycling the second hydrogen-enriched gas to the inlet of the hydrogen-containing gas producing apparatus or to the inlet of the PSA apparatus. 13. The apparatus of claim 11, wherein the ratio α of the carbon dioxide permeability coefficient to the hydrogen permeability coefficient of the carbon dioxide separation membrane is 5 or more. 14. The apparatus of claim 11 wherein the ratio α of the carbon dioxide permeability coefficient to the hydrogen permeability coefficient of the carbon dioxide separation membrane is 100 or less. 15. A method for producing hydrogen and recovering carbon dioxide which method produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, the method comprising the combination of steps of: a hydrogen-containing gas producing step of obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel;a adsorption step of adsorbing, with the use of a pressure swing adsorption apparatus provided with an adsorption tower containing an adsorbent, the components other than hydrogen contained in the hydrogen-containing gas on the adsorbent to yield a hydrogen-enriched gas that is enriched in hydrogen;a high-pressure desorption step of desorbing the components adsorbed on the adsorbent under a relatively high pressure;a low-pressure desorption step of desorbing the components adsorbed on the adsorbent under a relatively low pressure;a carbon dioxide membrane-separating step of separating the gas obtained from the low-pressure desorption step with the use of a carbon dioxide separation membrane into a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide and a carbon dioxide separation membrane offgas that is a gas enriched in the components other than carbon dioxide; anda cleaning step of cleaning the interior of the adsorption tower having completed the low-pressure desorption step with the use of the hydrogen-enriched gas obtained from the adsorption step. 16. The method of claim 15, comprising a mixing step of mixing together the gas obtained from the high-pressure desorption step and the gas obtained from the cleaning step to yield a mixed gas. 17. The method of claim 15, wherein combustion heat generated by combusting the gas obtained from the high-pressure desorption step is utilized for the reforming in the hydrogen-containing gas producing step. 18. The method of claim 15, wherein combustion heat generated by combusting the gas obtained from the cleaning step is utilized for the reforming in the hydrogen-containing gas producing step. 19. The method of claim 16, wherein combustion heat generated by combusting the mixed gas is utilized for the reforming in the hydrogen-containing gas producing step. 20. The method of claim 15, comprising a recycling step of recycling the gas obtained from the high-pressure desorption step to the adsorption step. 21. The method of claim 20, wherein in the recycling step, the gas obtained from the high-pressure desorption step is increased in the hydrogen concentration with the use of a hydrogen separation membrane, and thereafter recycled to the adsorption step. 22. The method of claim 15, wherein the ratio α of the carbon dioxide permeability coefficient to the hydrogen permeability coefficient of the carbon dioxide separation membrane is 5 or more.