Mesoporous cobalt-metal oxide catalyst for Fischer-Tropsch synthesis reactions and a preparing method thereof

Patent metadata

Field	Value
Publication number	US-10066169-B2
Application number	US-201615210062-A
Country	US
Kind code	B2
Filing date	Jul 14, 2016
Priority date	Jul 14, 2015
Publication date	Sep 4, 2018
Grant date	Sep 4, 2018

Abstract

The present invention relates to a mesoporous cobalt-metal oxide catalyst for the Fischer-Tropsch synthesis and a method of preparing the same. The mesoporous cobalt-metal oxide catalyst for the Fischer-Tropsch synthesis of the present invention can very stably maintain the mesoporous structure even under a H 2 -rich high-temperature reduction condition and under a reaction condition of the low-temperature Fischer-Tropsch synthesis, easily transport reactants to the active site of the catalyst due to structural stability, and facilitate the release of heavier hydrocarbon products after production thereof. Additionally, unlike the conventional cobalt-based catalysts which are prepared by adding various co-catalysts for the purpose of improving reducibility, activity, selectivity and increasing thermal stability, etc., the mesoporous cobalt-metal oxide catalyst for the Fischer-Tropsch synthesis can constantly maintain conversion and selectivity at high levels without further requiring co-catalysts and thus it can be very effectively used for the Fischer-Tropsch synthesis.

First claim

The invention claimed is:

1. A mesoporous cobalt-based catalyst for the Fischer-Tropsch synthesis comprising a main framework of a mesoporous structure, wherein the main framework of the mesoporous structure comprises components represented by Formula 1 below uniformly mixed:
CoM a O b   [Formula 1]

wherein M is Zr and/or Al; and
a or b is a molar ratio, wherein a and b are in the range of 0.1≤a≤0.35 and 1≤b≤4, respectively.

2. The mesoporous cobalt-based catalyst of claim 1 , wherein the main framework has a highly-ordered mesoporous structure, wherein an average pore diameter is in the range of 4 nm to 8 nm.

3. The mesoporous cobalt-based catalyst of claim 1 , wherein the specific surface area of the catalyst is in the range of 45 m 2 /g to 200 m 2 /g.

4. The mesoporous cobalt-based catalyst of claim 1 , wherein alumina is further impregnated in the pores as a structural promoter, in the main framework of a mesoporous structure in which cobalt oxide, zirconia and/or alumina are uniformly mixed.

5. The mesoporous cobalt-based catalyst of claim 4 , wherein alumina as a structural promoter is added in an amount of 2 wt % to 12 wt % relative to the total weight of the catalyst.

6. The mesoporous cobalt-based catalyst of claim 4 , wherein platinum is further impregnated in the pores, in the main framework of a mesoporous structure.

7. The mesoporous cobalt-based catalyst of claim 1 , wherein the main framework is made of CoZr a O b , CoAl a O b , Al 2 O 3 —CoZr a O b , Al 2 O 3 —CoAl a O b , Al 2 O 3 —Pt—CoZr a O b , or a mixture thereof (wherein a and b are in the range of 0.1≤a≤0.35 and 1≤b≤4, respectively).

8. A method for preparing a mesoporous cobalt-based catalyst for the Fischer-Tropsch synthesis according to claim 1 , comprising:
(1) preparing a mixed solution in which a cobalt precursor, a zirconium precursor, and/or an aluminum precursor are dissolved;
(2) filling the inside of the pores of a mesoporous template with the mixed solution in step (1) followed by drying and calcination; and
(3) removing the mesoporous template to form the main framework of a mesoporous structure, wherein the main framework of the mesoporous structure comprises components represented by Formula 1 below uniformly mixed:
CoM a O b   [Formula 1]

wherein M is Zr and/or Al; and
a or b is a molar ratio, wherein a and b are in the range of 0.1≤a≤0.35 and 1≤b≤4, respectively.

9. The method of claim 8 , wherein the method further comprises step (4) of further supporting alumina as a structural promoter inside of the pores of the main framework of a mesoporous structure.

10. The method of claim 9 , wherein step (4) comprises impregnating, drying, and calcinating the main framework of a mesoporous structure formed in step (3) in a solution containing the aluminum precursor.

11. The method of claim 9 , wherein the method further comprises step (5) of further supporting a platinum precursor after step (4).

12. The method of claim 11 , wherein the platinum precursor used in step (5) is selected from the group consisting of tetraammineplatinum nitrate, platinum dichloride, platinum acetylacetonate, diammine dinitro platinum, and sodium hexachloroplatinate hexahydrate.

13. The method of claim 8 , wherein the solvent for the mixed solution of step (1) is at least one selected from the group consisting of distilled water, methanol, ethanol, and ethylene glycol.

14. The method of claim 8 , wherein the cobalt precursor is selected from the group consisting of cobalt chloride (CoCl 2 .6H 2 O), cobalt acetate ((CH 3 COO) 2 Co.4H 2 O), and cobalt nitrate (Co(NO 3 ) 2 .6H 2 O); a zirconium precursor is selected from the group consisting of zirconium oxynitrate hydrate (ZrO(NO 3 ) 2 .xH 2 O), zirconium chloride octahydrate (ZrOCl 2 .8H 2 O), and zirconium acetate hydroxide ((CH 3 CO 2 ) x Zr(OH) y ); and an aluminum precursor is selected from the group consisting of aluminum nitrate nonahydrate (Al(NO 3 ) 3 .9H 2 O), aluminum chloride hexahydrate (AlCl 3 .6H 2 O), and aluminum acetate (Al(OH)(C 2 H 3 O 2 ) 2 .

15. The method of claim 8 , wherein the cobalt precursor, and the zirconium precursor and/or the aluminum precursor in step (1) are mixed in a weight ratio of 1:0.1 to 1:0.3.

16. A mesoporous cobalt-based catalyst made by the process of claim 8 , wherein the main framework of the mesoporous structure is formed using a mesoporous template selected from the group consisting of KIT-6, SBA-15, SBA-16, MCM-41, MCM-48, HMS, AMS-8, AMS-10, FDU-1, FDU-2, and FDU-12.

17. A method of preparing middle distillate-based liquid hydrocarbons from syngas by a low-temperature Fischer-Tropsch synthesis, comprising:
i) applying the mesoporous cobalt-based catalyst for the Fischer-Tropsch synthesis according to claim 1 to a fixed-bed reactor for the Fischer-Tropsch synthesis;
ii) activating the catalyst by reducing under a high-temperature hydrogen atmosphere; and
iii) carrying out the Fischer-Tropsch synthesis using the activated catalyst for the low-temperature Fischer-Tropsch synthesis.

18. The method of claim 17 , wherein the low-temperature Fischer-Tropsch synthesis is carried out at a reaction temperature of 200° C. to 350° C. under a reaction pressure of 10 bar to 30 bar and at a space velocity of 8,000 L/kg·cat./h to 64,000 L/kg·cat./h.

Assignees

• Research & Business Found Sungkyunkwan Univ

Inventors

• Bae Jong Wook
• Ahn Chang Il

Classifications

• B01J23/75 Primary

  Cobalt · CPC title

• C10G2/333 Primary

  of the platinum-group · CPC title

• C10G2/332

  of the iron-group · CPC title

• B01J23/002

  Mixed oxides other than spinels, e.g. perovskite · CPC title

• B01J37/08

  Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title