IP Library Granted Patent US 7,666,917
Granted Patent B2
US 7,666,917 · App. 12/285,093 · Granted Feb 23, 2010

Modified catalyst and use of this catalyst for the conversion of synthesis gas to hydrocarbons

Assignees: BP Exploration Operating Company Limited; Davy Process Technology Limited
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Quick Facts
Patent No.
US 7,666,917
App. No.
12/285,093
Granted
Feb 23, 2010
Kind
B2
Abstract

Process for conversion of syngas to liquid hydrocarbons using a catalyst composition containing a support and a Fischer-Tropsch metal for the conversion of syngas to liquid hydrocarbons, in which a silylating compound modifier is added to the catalyst composition during catalyst preparation or during a post-treatment stage.

Claims (24)

1. Process for the conversion of syngas to liquid hydrocarbons using a catalyst composition containing a support and a Fischer-Tropsch metal for the conversion of syngas to liquid hydrocarbons, comprising adding a silylating compound modifier to said catalyst composition during catalyst preparation or during a post-treatment stage.

2. Process according to claim 1 wherein the silylating compound is added during a post-treatment stage.

3. Process according to claim 1 wherein the silylating compound is chosen amongst organosilicon compounds.

4. Process according to claim 3 wherein the silylating compound is chosen amongst trimethyl silicon compounds.

5. Process according to claim 4 wherein the silylating compound is bis(trimethylsilyl)trifluoroacetamide.

6. Process according to claim 1 wherein the Fischer-Tropsch metal is a Group VIII metal.

7. Process according to claim 6 wherein the Fischer-Tropsch metal is selected from the group consisting of iron and cobalt.

8. Process according to claim 1 wherein the support is selected from the group consisting of alumina, silica, titania, zinc oxide and mixtures thereof.

9. Process according to claim 1 wherein the catalyst composition contains from 0.1 to 20 wt % cobalt (wrt support) supported on an inorganic oxide having a surface area of less than 100 m 2 /g, and a promoter chosen from ruthenium, platinum or palladium (when not the primary catalyst metal), aluminium, rhenium, hafnium, cerium, lanthanum and zirconium, the said promoter being present in amounts less than the cobalt and with a promoter:metal ratio by weight of at least 1:10.

10. Process for preparing a Fischer-Tropsch catalyst comprising a Fischer Tropsch metal on a support, comprising modifying the Fischer Tropsch catalyst with a silylating compound that is added during the catalyst preparation or during a post-treatment stage.

11. Process according to claim 10 , wherein silylating compound is added during a post-treatment stage.

12. Process according to claim 10 , wherein the silylating compound is chosen amongst organosilicon compounds.

13. Process according to claim 12 wherein the silylating compound is chosen amongst trimethyl silicon compounds.

14. Process according to claim 13 wherein the silylating compound is bis(trimethylsilyl)trifluoroacctamide.

15. Process according to claim 10 , wherein the Fischer-Tropsch metal is a Group VIII metal.

16. Process according to claim 15 wherein the Fischer-Tropsch metal is selected from the group consisting of iron and cobalt.

17. Process according to claim 10 , wherein the support is selected from the group consisting of alumina, silica, titania, zinc oxide and mixtures thereof.

18. Process for the conversion of syngas to liquid hydrocarbons in the presence of a modified supported Fischer-Tropsch catalyst comprising using a catalyst composition containing a support and a Fischer-Tropsch metal for the conversion of syngas to liguid hydrocarbons wherein said catalyst composition is prepared according to claim 10 .

19. Process according to claim 4 wherein the silylating compound is selected from the group consisting of trimethylsilyl chloride, bis(trimethylsilyl)trifluoroacetamide, N-methyl-N-(trimethylsilyl)trifluoroacetamide, and mixtures thereof.

20. Process according to claim 6 wherein the Fischer-Tropsch metal is selected from the group consisting of iron, cobalt, ruthenium, nickel, molybdenum, tungsten and rhenium.

21. Process according to claim 8 wherein the support is zinc oxide.

22. Process according to claim 13 wherein the silylating compound is selected from the group consisting of trimethylsilyl chloride, bis(trimethylsilyl)trifluoroacetamide, N-methyl-N-(trimethylsilyl)trifluoroacetamide, and mixtures thereof.

23. Process according to claim 15 , wherein the Fischer-Tropsch metal is selected from the group consisting of iron, cobalt, ruthenium, nickel, molybdenum, tungsten and rhenium.

24. Process according to claim 17 , wherein the support is zinc oxide.

Assignments (1)
CHANGE OF NAME Recorded Dec 2, 2025
From: DAVY PROCESS TECHNOLOGY LIMITED
To: JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED
Reel/Frame 073804/0494 →
Priority Claims (1)
EP 05250923 · Feb 17, 2005 · regional
Continuity (2)
Division 1188316000
Related Publication 20090036558A1 · Feb 5, 2009