Nickel on strontium-doped calcium aluminate catalyst for reforming
View Patent ↗A strontium-doped, calcium-alumina nickel supported reforming catalyst is useful for reforming reactions when it is desired to generate a low H 2 /CO ratio synthesis gas and to reduce coking. The catalyst can generate a synthesis gas having a H 2 /CO ratio of less than about 2.3. The catalyst includes alumina, from about 0.3 wt. % to about 35 wt. % of calcium oxide, from about 0.1 wl % to about 35 wt. % of a strontium promoter, and about 0.5 wt. % to about 30 wt. % nickel. The support is prepared by a method wherein the calcium oxide is combined with the alumina to form aluminum-rich calcium aluminates.
1. A reforming catalyst for use in a syngas producing process that generates a low H 2 /CO ratio synthesis gas, the catalyst comprising:
a precursor comprising about 0.3 wt. % to about 35 wt. % of a calcium compound, about 1 wt. % to about 35 wt. % of a strontium compound, and up to about 98 wt. % of an aluminum compound that together have been calcined to form a calcined, strontium-doped, calcium-aluminate precursor; and
about 0.5 wt. % to about 30 wt. % of a nickel compound on the calcined, strontium-doped, calcium aluminate precursor, wherein the weight percentages are based on the total weight of the reforming catalyst.
2. The catalyst of claim 1 wherein the calcium compound comprises from about 2 wt. % to about 20 wt. % of the catalyst.
3. The catalyst of claim 2 wherein the nickel compound comprises from about 10 wt. % to about 15 wt. % of the catalyst.
4. The catalyst of claim 3 wherein the strontium compound comprises from about 1.0 wt. % to about 5.0 wt. % of the catalyst.
5. The catalyst of claim 3 wherein the strontium compound comprises from about 1.5 wt. % to about 3.0 wt. % of the catalyst.
6. The catalyst of claim 1 wherein the nickel compound comprises from about 5 wt. % to about 20 wt. % of the catalyst.
7. The catalyst of claim 1 wherein the catalyst produces a synthesis gas having a H 2 /CO ratio less than about 2.3.
8. The catalyst of claim 1 wherein the strontium compound comprises from about 1.5 wt. % to about 3.0 wt. % of the catalyst.
9. The catalyst of claim 1 wherein the strontium compound is selected from the group consisting of strontium nitrate, strontium acetate and a combination thereof.
10. The catalyst of claim 1 wherein the nickel compound is selected from the group consisting of nickel nitrate, nickel acetate and a combination thereof.
11. The catalyst of claim 1 further being highly resistant to carbon/coke formation.
12. The catalyst of claim 1 further having a BET surface area of at least about 10 m 2 /g.
13. The catalyst of claim 1 further having a pore volume greater than about 0.2 cc/g.
14. A method of making the reforming catalyst of claim 1 comprising:
(a) blending the aluminum compound with the calcium compound to form an aluminum/calcium mixture;
(b) forming the aluminum/calcium mixture into a predetermined shape to form a calcium-aluminate carrier precursor;
(c) calcining the calcium-aluminate carrier precursor to form a calcined, calcium-aluminate carrier precursor;
(d) impregnating the calcined, calcium-aluminate carrier precursor with the strontium compound to form a calcined, strontium-doped, calcium-aluminate precursor;
(e) impregnating the calcined, strontium-doped, calcium-aluminate precursor with the nickel compound to form a calcined, strontium-doped, nickel-impregnated, calcium-aluminate precursor; and
(f) calcining the calcined, strontium-doped, nickel-impregnated, calcium-aluminate precursor to make the reforming catalyst.
15. The method of claim 14 wherein the calcining of the calcium-aluminate carrier precursor in step (c) is performed at about 120° C. to about 1700° C.
16. The method of claim 14 further including calcining the calcined, strontium-doped, calcium-aluminate precursor of step (d) at about 900° C. to about 1700° C. prior to the nickel-impregnating step (e).
17. The method of claim 14 wherein the calcining of the calcined, strontium-doped, nickel-impregnated, calcium-aluminate precursor in step (f) is performed at about 500° C.
18. A method of reforming light hydrocarbons comprising contacting the catalyst of claim 1 with a feed stream containing a mixture of steam, carbon dioxide and the light hydrocarbon.
19. A method of autothermal reforming light hydrocarbons comprising contacting the catalyst of claim 1 with a feed stream containing a mixture of steam, air and the light hydrocarbon.
20. A reforming catalyst for use in a syngas producing process that generates a low H 2 /CO ratio synthesis gas, the catalyst comprising
a precursor comprising about 0.3 wt. % to about 35 wt. % of a calcium compound, about 0.5 wt. % to about 35 wt. % of a strontium compound, and up to about 98 wt. % of an aluminum compound that have been calcined to form a calcined, strontium-doped, calcium-aluminate precursor; and
about 0.5 wt. % to about 30 wt. % of a nickel compound on the calcined, strontium-doped, calcium aluminate precursor, wherein the weight percentages are based on the total weight of the reforming catalyst.