Multi-Metallic Catalysts For Pre-Reforming Reactions

• US 20100147749A1
• Filed: 12/10/2009
• Published: 06/17/2010
• Est. Priority Date: 12/11/2008
• Status: Abandoned Application

• Current Assignee: L'Air Liquide Societe Anonyme Pour L'Etude et L'Exploitation Des Procedes Georges Claude (L'Air Liquide SA)
• Original Assignee: American Air Liquide Incorporated (L'Air Liquide SA)
• Inventors: Huang, Wei, Tromeur, Pascal, Chen, Jingguang G., Pranda, Pavol
• Application Number:
  US12/635,145
• Publication Number:
  US 20100147749A1
• Time in Patent Office: Days
• US Class Current: 208/244
• CPC Class Codes: B01J 23/755 Nickel
• CPC Class Codes: B01J 23/80 with zinc, cadmium or mercury
• CPC Class Codes: B01J 23/892 Nickel and noble metals
• CPC Class Codes: B01J 37/0201 Impregnation
• CPC Class Codes: C10G 25/003 Specific sorbent material, not covered by C10G25/02 or C10G25/03
• CPC Class Codes: C10G 29/04 Metals, or metals deposited on a carrier
• CPC Class Codes: C10G 29/06 Metal salts, or metal salts deposited on a carrier

Abstract

The present invention relates to multi-metallic catalyst compositions for improved coke resistance in a hydrocarbon feed pre-reformer unit that comprises nickel and an enhancing component selected from at least one member of the group consisting of ruthenium, palladium, platinum, rhodium, cobalt, gold and silver on a support. The present invention further relates to a catalyst system for improved coke and sulfur resistance in a hydrocarbon feed pre-reformer unit that comprises at least one multi-metallic catalyst composition comprising nickel and an enhancing component selected from at least one member of the group consisting of ruthenium, palladium, platinum, rhodium, cobalt, gold and silver on a support used in conjunction with at least one sulfur capturing component selected from the group comprising copper oxide and zinc oxide. Finally the present invention relates to the use of this catalyst system in a process for pre-reforming a hydrocarbon feed stream.

Claims

1. A multi-metallic catalyst composition for improved coke resistance in a hydrocarbon feed pre-reformer, the composition comprising nickel and an enhancing component selected from at least one member of the group consisting of ruthenium, palladium, platinum, rhodium, cobalt, gold and silver on a support, the nickel being present in an amount from 0.10 to 2.35 weight percent of the coke resistant catalyst composition.

2. The catalyst composition of claim 1, wherein the enhancing component is silver.

3. The catalyst composition of claim 2, wherein the nickel is present in an amount from 2.00 to 2.35 weight percent of the coke resistant catalyst composition.

4. The catalyst composition of claim 3, wherein the silver is present in a molar ratio of silver to nickel from 1:

3 to 1;

9.

5. A catalyst system for improved coke and sulfur resistance in a hydrocarbon feed pre-reformer unit, the catalyst system comprising at least one multi-metallic catalyst composition comprising nickel and an enhancing component selected from at least one member of the group consisting of ruthenium, palladium, platinum, rhodium, cobalt, gold and silver on a support, the nickel being present in the catalyst composition in an amount from 0.1 to 50 weight percent;

used in conjunction with at least one sulfur capturing component selected from the group comprising copper oxide and zinc oxide, with the proviso that when the sulfur capturing component is copper oxide, the copper oxide is activated copper oxide.

6. The catalyst system of claim 5, wherein the nickel is present in the catalyst composition in an amount from 15 to 45 weight percent.

7. The catalyst system of claim 6, wherein the nickel is present in the coke resistant catalyst composition in an amount from 25 to 40 weight percent.

8. The catalyst system of claim 5, wherein the catalyst system is in the form of a fixed catalyst bed comprising one or more layers of the multi-metallic catalyst composition and one or more layers of the sulfur capturing component.

9. The catalyst system of claim 8, wherein the ratio of catalyst composition to sulfur capturing component in the catalyst system ranges from 10:

1 to 1;

10.

10. The catalyst system of claim 9, wherein the enhancing metal component in present in the catalyst composition in a molar ratio of enhancing metal component to nickel of from 1:

10 to 10;

1.

11. The catalyst system of claim 10, wherein the catalyst composition comprises nickel and silver.

12. The catalyst system of claim 11, wherein the sulfur capturing component is activated copper oxide.

13. The catalyst system of claim 11, wherein the sulfur capturing component is zinc oxide.

14. The catalyst system of claim 12, wherein the nickel is present in the catalyst composition in an amount from 25 to 40 weight percent.

15. The catalyst system of claim 13, wherein the nickel is present in the catalyst composition in an amount from 25 to 40 weight percent.

16. The catalyst system of claim 5, wherein the catalyst system is in the form of a physical mixture of pellets of multi-metallic catalyst composition and pellets of the sulfur capturing component.

17. The catalyst system of claim 16, wherein the molar ratio of catalyst composition to sulfur capturing component in the catalyst system ranges from 10:

1 to 1;

10.

18. The catalyst system of claim 17, wherein the enhancing metal component is present in the catalyst composition in a molar ratio of one or more enhancing components to nickel of from 1:

10 to 10;

1.

19. The catalyst system of claim 18, wherein the catalyst composition comprises nickel and silver.

20. The catalyst system of claim 19, wherein the sulfur capturing component is activated copper oxide.

21. The catalyst system of claim 19, wherein the sulfur capturing component is zinc oxide.

22. The catalyst system of claim 20, wherein the nickel is present in the catalyst composition in an amount from 25 to 40 weight percent.

23. The catalyst system of claim 21, wherein the nickel is present in the catalyst composition in an amount from 25 to 40 weight percent.

24. A process for pre-reforming a hydrocarbon feed stream prior to the hydrocarbon feed stream being injected into a steam hydrocarbon reforming unit, the process comprising the steps of:

(a) providing a hydrocarbon feed stream source, a heat exchanger to heat the hydrocarbon feed stream source and a pre-reformer unit comprising a pre-reformer vessel, a gas inlet, a gas outlet and a catalyst system disposed within the pre-reformer vessel, the catalyst system comprising;

(i) at least one multi-metallic coke resistant catalyst composition comprising nickel and an enhancing component selected from at least one member of the group consisting of ruthenium, palladium, platinum, rhodium, cobalt, gold and silver on a support, the nickel being present in the coke resistant catalyst composition in an amount from 0.1 to 50 weight percent; and

(ii) at least one sulfur capturing component selected from the group comprising copper oxide and zinc oxide;

(b) injecting the hydrocarbon feed stream into the heat exchanger and heating the hydrocarbon feed stream to a temperature that ranges from 300 to 700 C;

(c) withdrawing the heated hydrocarbon feed stream from the heat exchanger and injecting the heated hydrocarbon feed stream into the pre-reformer vessel; and

(d) bringing the heated hydrocarbon feed stream into contact with the catalyst system of the pre-reformer vessel in order to decrease the amount of sulfur in the hydrocarbon feed stream and decrease the amount of coke typically caused by the pre-reforming step thereby producing a sulfur free hydrocarbon feed stream; and

(e) withdrawing the sulfur free hydrocarbon feed stream and passing it on for further treatment in a steam hydrocarbon reforming unit.