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A catalyst formed of a ziroonia carrier carrying ruthenium and a catalyst formed of an inorganic oxide carrier carrying zirconium and ruthenium provide high conversion in autothermal reforming of a variety of hydrocarbons. The catalysts also provide high yield of carbon monoxide in reforming reactio

A catalyst formed of a ziroonia carrier carrying ruthenium and a catalyst formed of an inorganic oxide carrier carrying zirconium and ruthenium provide high conversion in autothermal reforming of a variety of hydrocarbons. The catalysts also provide high yield of carbon monoxide in reforming reaction making use of carbon dioxide and exhibit long-term stable characteristics with a small amount of coke deposition.

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1. A method for autothermal reforming to produce hydrogen or a synthesis gas, comprising contacting a feedstock as a starting material and a reforming gas comprising oxygen and steam with a catalyst, wherein the catalyst comprises ruthenium supported on a zirconia carrier and an amount of rutheni

1. A method for autothermal reforming to produce hydrogen or a synthesis gas, comprising contacting a feedstock as a starting material and a reforming gas comprising oxygen and steam with a catalyst, wherein the catalyst comprises ruthenium supported on a zirconia carrier and an amount of ruthenium supported on the carrier is from 0.05 to 20 wt. % based on the entirety of the catalyst;a ratio of steam to the feedstock fed to the reaction system is from 0.4 to 4 in terms of the number of water molecules/the number of carbon atoms in the feedstock; anda ratio of oxygen to the feedstock fed to the reaction system is from 0.2 to 0.8 in terms of the number of oxygen molecules/the number of carbon atoms in the feedstock.2. A method for autothermal reforming to produce hydrogen or a synthesis gas, comprising contacting a feedstock as a starting material and a reforming gas comprising oxygen and steam with a catalyst, wherein the catalyst comprises zirconium and ruthenium supported on an inorganic oxide carrier and an amount of zirconium on the carrier is from 0.05 to 20 wt. % as reduced to ZrO2based on the entirety of the catalyst;a ratio of steam to the feedstock fed to the reaction system is from 0.4 to 4 in terms of the number of water molecules/the number of carbon atoms in the feedstock;and a ratio of oxygen to the feedstock fed to the reaction system is from 0.2 to 0.8 in terms of the number of oxygen molecules/the number of carbon atoms in the feedstock.3. The method according to claim 2, wherein the starting material is a hydrocarbon.4. The method according to claim 3, wherein the hydrocarbon is at least one member selected from the group consisting of methane, liquefied petroleum gas, naphtha, kerosene, and gas oil.5. The method according to claim 2, wherein the feedstock is at least one member selected from the group consisting of methanol, ethanol, and dimethyl ether.6. The method according to claim 2, wherein the reforming gas comprises a mixture of oxygen, steam and carbon dioxide.7. A method for reforming hydrocarbon, comprising contacting the hydrocarbon and carbon dioxide gas with a catalyst, wherein the catalyst comprises ruthenium supported on a zirconia carrier and an amount of ruthenium supported on the carrier is from 0.05 to 20 wt. % based on the entirety of the catalyst; anda ratio of feedstock hydrocarbons to carbon dioxide is from 0.1 to 3 in terms of the number of carbon dioxide molecules/the number of carbon atoms in the hydrocarbons.8. The method according to claim 7, wherein the catalyst supported on the zirconia carrier further contains at least one member selected from the group consisting of cobalt and magnesium.9. The method according to claim 8, wherein the cobalt content is from 0.01 to 30 based on the atomic ratio of cobalt to ruthenium.10. The method according to claim 8, wherein the magnesium content is from 0.5 to 20 wt. % as reduced to MgO based on the entirety of the catalyst.11. The method according to claim 7, wherein the hydrocarbon is methane.12. The method for reforming hydrocarbon according to claim 7, wherein the hydrocarbon is a natural gas.13. The method for reforming hydrocarbon according to claim 7, wherein carbon dioxide gas and steam contact the catalyst, a ratio of steam to carbon contained in the hydrocarbon is less than 10, and a ratio of carbon dioxide to carbon contained hydrocarbon is from 20/80 to 70/30.14. A method for reforming hydrocarbon, comprising contacting the hydrocarbon and carbon dioxide gas with a catalyst comprising zirconium and ruthenium supported on an inorganic oxide carrier, wherein the catalyst comprises an amount of zirconium supported on the carrier of from 0.05 to 20 wt. % zirconium as reduced to ZrO2based on the entirety of the catalyst; anda ratio of feedstock hydrocarbons to carbon dioxide is from 0.1 to 3 in terms of the number of carbon dioxide molecules/the number of carbon atoms in the hydrocarbons.15. The method according to claim 1 4, wherein the ruthenium is present in an amount of from 0.05 to 20 wt. %.16. The method according to claim 14, wherein the inorganic oxide carrier comprises alumina.17. The method according to claim 16, wherein the alumina is at least one member selected from the group consisting of α-alumina and &ggr;-alumina.18. The method according to claim 14, wherein the catalyst supported on the inorganic oxide carrier further contains at least one member selected from the group consisting of cobalt and magnesium.19. The method according to claim 18, wherein the cobalt content is from 0.01 to 30 based on the atomic ratio of cobalt to ruthenium.20. The method according to claim 18, wherein the magnesium content is from 0.5 to 20 wt. % as reduced to MgO based on the entirety of the catalyst.21. The method according to claim 14, wherein ruthenium is present in an amount of from 0.05 to 20 wt. % based on the entirety of the catalyst.