초록 ▼

A method and catalysts for producing a hydrogen-rich syngas are disclosed. According to the method a CO-containing gas contacts a water gas shift (WGS) catalyst, optionally in the presence of water, preferably at a temperature of less than about 450° C. to produce a hydrogen-rich gas, such as a hydr

A method and catalysts for producing a hydrogen-rich syngas are disclosed. According to the method a CO-containing gas contacts a water gas shift (WGS) catalyst, optionally in the presence of water, preferably at a temperature of less than about 450° C. to produce a hydrogen-rich gas, such as a hydrogen-rich syngas. Also disclosed is a water gas shift catalyst formulated from: a) Pt, its oxides or mixtures thereof; b) Ru, its oxides or mixtures thereof; and c) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, Sc, Y, Ti, Zr, V, Mo, Mn, Fe, Co, Rh, Ir, Ge, Sn, Sb, La, Ce, Pr, Sm, and Eu. Another disclosed catalyst formulation comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; Co, its oxides or mixtures thereof; and at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, Sc, Y, Ti, Zr, V, Mo, Mn, Fe, Rh, Ir, Ge, Sn, Sb, La, Ce, Pr, Sm, and Eu, their oxides and mixtures thereof. The WGS catalyst may be supported on a carrier, such as any one member or a combination of alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, zeolite, perovskite, silica clay, yttria and iron oxide. Fuel processors containing such water gas shift catalysts are also disclosed.

대표청구항 ▼

What we claim is: 1. A method for producing a hydrogen-rich gas which comprises: contacting a CO-containing gas with a water gas shift catalyst in the presence of water at a temperature of not more than about 450° C., wherein the water gas shift catalyst comprises: a) Pt, its oxides or mixtures the

What we claim is: 1. A method for producing a hydrogen-rich gas which comprises: contacting a CO-containing gas with a water gas shift catalyst in the presence of water at a temperature of not more than about 450° C., wherein the water gas shift catalyst comprises: a) Pt, its oxides or mixtures thereof; b) Ru, its oxides or mixtures thereof; and c) at least one member selected from the group consisting of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, Sc, Y, Ti, Zr, V, Mo, Mn, Fe, Co, Rh, Ir, Ge, Sn, Sb, La, Ce, Pr, Sm, and Eu, their oxides and mixtures thereof. 2. A method according to claim 1, wherein the CO-containing gas is a syngas. 3. A method according to claim 1, wherein the water gas shift catalyst comprises: a) Pt, its oxides or mixtures thereof; b) Ru, its oxides or mixtures thereof; and c) at least one member selected from the group consisting of Sc, Y, and La, their oxides and mixtures thereof. 4. A method according to claim 1, wherein the water gas shift catalyst comprises: a) Pt, its oxides or mixtures thereof; b) Ru, its oxides or mixtures thereof; and c) at least one member selected from the group consisting of Co, Mo, their oxides and mixtures thereof. 5. A method according to claim 4, wherein the water gas shift catalyst comprises: one or more members selected from the group consisting of Na, K, Rb, La, and Ce, their oxides and mixtures thereof. 6. A method according to claim 5, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; Co, its oxides or mixtures thereof; and K, its oxides or mixtures thereof. 7. A method according to claim 5, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; Co, its oxides or mixtures thereof; and Na, its oxides or mixtures thereof. 8. A method according to claim 1, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; and Ti, its oxides or mixtures thereof. 9. A method according to claim 8, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; Ti, its oxides or mixtures thereof; and one or more members selected from the group consisting of V, Mo, Fe, and Ce, their oxides and mixtures thereof. 10. A method according to claim 1, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; Co, its oxides or mixtures thereof; and Fe, its oxides or mixtures thereof. 11. A method according to claim 1, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; and Fe, its oxides or mixtures thereof. 12. A method according to claim 11, wherein the water gas shift catalyst further comprises Ce, its oxides or mixtures thereof. 13. A method according to claim 1, wherein the water gas shift catalyst is supported on a carrier comprising at least one member selected from the group consisting of alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, zeolite, perovskite, silica clay, yttria and iron oxide and mixtures thereof. 14. A method according to claim 13, wherein the carrier comprises at least one member selected from the group consisting of zirconia, titania and ceria. 15. A method according to claim 14, wherein the carrier comprises zirconia. 16. A method according to claim 1, wherein the CO-containing gas is contacted with the water gas shift catalyst at a temperature ranging from about 150° C. to about 450° C. 17. A method according to claim 16, wherein the CO-containing gas is contacted with a water gas shift catalyst at a temperature ranging from more than about 350° C. to up to about 450° C. 18. A method according to claim 16, wherein the CO-containing gas is contacted with a water gas shift catalyst at a temperature ranging from about 250° C. to up to about 350° C. 19. A method according to claim 16, wherein the CO-containing gas is contacted with a water gas shift catalyst at a temperature ranging from about 150° C. to up to about 250° C. 20. A method according to claim 1, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 75 bar. 21. A method according to claim 20, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 50 bar. 22. A method according to claim 20, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 25 bar. 23. A method according to claim 20, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 15 bar. 24. A method according to claim 20, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 1 bar. 25. A method according to claim 1, wherein the water gas shift catalyst comprises between about 0.01 wt. % to about 10 wt. %, with respect to the total weight of all catalyst components plus the support material, of each Group 8, 9, or 10 element present in the water gas shift catalyst. 26. A method according to claim 25, wherein the water gas shift catalyst comprises between about 0.01 wt. % to about 2 wt. % of each Group 8, 9, or 10 element present in the water gas shift catalyst. 27. A method according to claim 26, wherein the water gas shift catalyst comprises between about 0.05 wt. % to about 0.5 wt. % of each Group 8, 9, or 10 element present in the water gas shift catalyst. 28. A method according to claim 1, wherein the water gas shift catalyst comprises between about 0.05 wt. % to about 20 wt. %, with respect to the total weight of all catalyst components plus the support material, of each Group 1 element present in the water gas shift catalyst. 29. A method for producing a hydrogen-rich gas which comprises: contacting a CO-containing gas with a water gas shift catalyst in the presence of water at a temperature of not more than about 450° C., wherein the water gas shift catalyst comprises: a) Pt, its oxides or mixtures thereof; b) Ru, its oxides or mixtures thereof; c) Co, its oxides or mixtures thereof; and d) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, Sc, Y, Ti, Zr, V, Mo, Mn, Fe, Co, Rh, Ir, Ge, Sn, Sb, La, Ce, Pr, Sm, and Eu, their oxides and mixtures thereof. 30. A method according to claim 29, wherein the CO-containing gas is a syngas. 31. A method according to claim 29, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; Co, its oxides or mixtures thereof; and one or more member selected from the group consisting of K, La and Ce, their oxides and mixtures thereof. 32. A method according to claim 31, wherein the water gas shift catalyst further comprises Rh, its oxides or mixtures thereof. 33. A method according to claim 31, wherein the water gas shift catalyst comprises Pt, its oxides or mixtures thereof; Ru, its oxides or mixtures thereof; Co, its oxides or mixtures thereof; and K, its oxides or mixtures thereof. 34. A method according to claim 29, wherein the water gas shift catalyst is supported on a carrier comprising at least one member selected from the group consisting of alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, zeolite, perovskite, silica clay, yttria and iron oxide and mixtures thereof. 35. A method according to claim 34, wherein the carrier comprises at least one member selected from the group consisting of zirconia, titania and ceria. 36. A method according to claim 35, wherein the carrier comprises zirconia. 37. A method according to claim 29, wherein the CO-containing gas is contacted with the water gas shift catalyst in the presence of water at a temperature ranging from about 150° C. to about 450° C. 38. A method according to claim 37, wherein the CO-containing gas is contacted with a water gas shift catalyst in the presence of water at a temperature ranging from more than about 350° C. to up to about 450° C. 39. A method according to claim 37, wherein the CO-containing gas is contacted with a water gas shift catalyst in the presence of water at a temperature ranging from about 250° C. to up to about 350° C. 40. A method according to claim 37, wherein the CO-containing gas is contacted with a water gas shift catalyst in the presence of water at a temperature ranging from about 150° C. to up to about 250° C. 41. A method according to claim 37, wherein the CO-containing gas is contacted with the water gas shift catalyst in the presence of water at a pressure of no more than about 75 bar. 42. A method according to claim 41, wherein the CO-containing gas is contacted with the water gas shift catalyst in the presence of water at a pressure of no more than about 50 bar. 43. A method according to claim 41, wherein the CO-containing gas is contacted with the water gas shift catalyst in the presence of water at a pressure of no more than about 25 bar. 44. A method according to claim 41, wherein the CO-containing gas is contacted with the water gas shift catalyst in the presence of water at a pressure of no more than about 15 bar. 45. A method according to claim 41, wherein the CO-containing gas is contacted with the water gas shift catalyst in the presence of water at a pressure of no more than about 1 bar. 46. A method according to claim 29, wherein the water gas shift catalyst comprises between about 0.01 wt. % to about 10 wt. %, with respect to the total weight of all catalyst components plus the support material, of each Group 8, 9, or 10 element present in the water gas shift catalyst. 47. A method according to claim 46, wherein the water gas shift catalyst comprises between about 0.01 wt. % to about 2 wt. % of each Group 8, 9, or 10 element present in the water gas shift catalyst. 48. A method according to claim 47, wherein the water gas shift catalyst comprises between about 0.05 wt. % to about 0.5 wt. % of each Group 8, 9, or 10 element present in the water gas shift catalyst. 49. A method according to claim 29, wherein the water gas shift catalyst comprises about 0.05 wt. % to about 20 wt. %, with respect to the total weight of all catalyst components plus the support material, of each Group 1 element present in the water gas shift catalyst.