Process for producing a Fischer-Tropsch synthesis catalyst

Patent metadata

Field	Value
Publication number	US-11517883-B2
Application number	US-201816485371-A
Country	US
Kind code	B2
Filing date	Feb 9, 2018
Priority date	Feb 10, 2017
Publication date	Dec 6, 2022
Grant date	Dec 6, 2022

Abstract

The present invention relates to a process for conveniently preparing a supported cobalt-containing Fischer-Tropsch synthesis catalyst having improved activity and selectivity for C5+ hydrocarbons. In one aspect, the present invention provides a process for preparing a supported cobalt-containing Fischer-Tropsch synthesis catalyst, said process comprising the steps of: (a) impregnating a support material with: i) a cobalt-containing compound and ii) acetic acid, or a manganese salt of acetic acid, in a single impregnation step to form an impregnated support material; and (b) drying and calcining the impregnated support material; wherein the support material impregnated in step (a) has not previously been modified with a source of metal other than cobalt; and wherein when the cobalt-containing compound is cobalt hydroxide, a manganese salt of acetic acid is not used in step (a) of the process.

First claim

The invention claimed is:

1. A process for preparing a supported cobalt-containing Fischer-Tropsch synthesis catalyst, said process comprising the steps of:
(a) impregnating a support material, wherein the support material is in the form of a powder or granulate, with: i) a cobalt-containing compound and ii) acetic acid, or a manganese salt of acetic acid, in a single impregnation step to form an impregnated support material then extruding the impregnated support material to form an extrudate; and then
(b) drying and calcining the extrudate to provide the supported cobalt-containing Fischer Tropsch synthesis catalyst;
wherein the support material impregnated in step (a) comprises a material selected from the group consisting of silica, alumina, silica/alumina, ceria, gallia, zirconia, titania, magnesia, zinc oxide, and mixtures thereof, and has not previously been modified with a source of metal other than cobalt;
wherein when the cobalt containing-compound is cobalt hydroxide, a manganese salt of acetic acid is not used in step (a) of the process, and
wherein the supported cobalt-containing Fischer Tropsch synthesis catalyst comprises cobalt oxide crystallites below 10 nm in particle size.

2. A process according to claim 1 , wherein the support material is in the form of a powder having a median particle size diameter (d50) of less than 50 μm, or wherein the support material is in the form of a granulate having a median particle size diameter (d50) of from 300 to 600 μm.

3. A process according to claim 1 , wherein the support material is impregnated with a solution or suspension comprising i) the cobalt-containing compound and ii) acetic acid or a manganese salt of acetic acid.

4. A process according to claim 3 , wherein the solution or suspension is an aqueous solution or suspension.

5. A process according to claim 1 , wherein the cobalt-containing compound is the nitrate, acetate, hydroxide or acetylacetonate of cobalt.

6. A process according to claim 1 , wherein the support material is impregnated with acetic acid in step (a) in an amount from 0.1 to 5 wt. %, based on the dry weight of the impregnated support material; or wherein the support material is impregnated with a manganese salt of acetic acid in step (a) in an amount from 0.1 to 5 wt. %.

7. A process according to claim 1 , wherein impregnation step (a) affords a synthesis catalyst containing from 5 wt. % to 20 wt. % of cobalt, on an elemental basis, based on the total weight of the supported synthesis catalyst.

8. A process according to claim 1 , wherein the support material impregnated in step (a) comprises alumina, silica/alumina, zirconia, titania, or zinc oxide.

9. A process according to claim 1 , wherein the cobalt-containing Fischer-Tropsch synthesis catalyst obtained comprises one or more promoters, dispersion aids, strength aids and/or binders.

10. A process according to claim 9 , wherein the one or more promoters, dispersion aids and/or binders, or precursors thereof, is/are introduced during impregnation step (a).

11. A process according to claim 9 , wherein the cobalt-containing Fischer-Tropsch synthesis catalyst obtained comprises one or more promoters selected from the group consisting of ruthenium, palladium, platinum, rhodium, rhenium, manganese, chromium, nickel, iron, molybdenum, tungsten, zirconium, gallium, thorium, lanthanum, cerium and mixtures thereof.

12. A process according to claim 11 , wherein the one or more promoters are present in the cobalt-containing Fischer-Tropsch synthesis catalyst obtained in an amount from 0.1 wt. % to 3 wt. %, on an elemental basis, based on the total weight of the supported synthesis catalyst.

13. A process according to claim 1 , wherein calcining in step (b) is conducted at a temperature of at least 250° C.

14. A process according to claim 1 , further comprising reducing the cobalt-containing Fischer-Tropsch synthesis catalyst obtained to form a reduced Fischer-Tropsch synthesis catalyst.

15. A process for preparing a titania supported cobalt-containing Fischer-Tropsch synthesis catalyst, said process comprising the steps of:
(a) impregnating a titania support material, wherein the titania support material is in the form of a powder or granulate, with: i) a cobalt-containing compound and ii) acetic acid, or a manganese salt of acetic acid, in a single impregnation step to form an impregnated support material, then extruding the impregnated support material to form an extrudate; and then
(b) drying and calcining the extrudate;
wherein the titania support material impregnated in step (a) has not previously been modified with a source of metal other than cobalt;
wherein when the cobalt containing-compound is cobalt hydroxide, a manganese salt of acetic acid is not used in step (a) of the process; and
wherein the supported cobalt-containing Fischer Tropsch synthesis catalyst comprises cobalt oxide crystallites below 10 nm in particle size.

16. A process according to claim 15 , wherein the cobalt-containing compound is the nitrate, acetate, hydroxide or acetylacetonate of cobalt.

17. A process according to claim 15 , wherein the titania support material is impregnated with acetic acid in step (a) in an amount from 0.1 to 5 wt. %, based on the dry weight of the impregnated support material; or wherein the titania support material is impregnated with a manganese salt of acetic acid in step (a) in an amount from 0.1 to 5 wt. %.

18. A process according to claim 15 , wherein impregnation step (a) affords a synthesis catalyst containing from 5 wt. % to 20 wt. % of cobalt, on an elemental basis, based on the total weight of the supported synthesis catalyst.

19. A process according to claim 15 , wherein calcining in step (b) is conducted at a temperature of at least 250° C.

20. A process according to claim 15 , further comprising reducing the cobalt-containing Fischer-Tropsch synthesis catalyst obtained to form a reduced Fischer-Tropsch synthesis catalyst.

21. A process according to claim 15 , wherein the titania support material is impregnated with a manganese salt of acetic acid.

Assignees

• Bp Plc

Inventors

• Ojeda Pineda Manuel
• Paterson Alexander James

Classifications

• B01J23/8892 Primary

  Manganese · CPC title

• B01J37/18

  with gases containing free hydrogen · CPC title

• B01J37/088

  Decomposition of a metal salt · CPC title

• B01J37/0018

  Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat) · CPC title

• B01J37/16

  Reducing · CPC title