Strengthened iron catalyst for slurry reactors
View Patent ↗A method of strengthening a precipitated unsupported iron catalyst by: preparing a precipitated unsupported iron catalyst containing copper and potassium; adding a solution comprising a structural promoter to the previously prepared catalyst; drying the mixture; and calcining the dried catalyst. A method for preparing an iron catalyst, the method comprising: precipitating a catalyst precursor comprising iron phases selected from hydroxides, oxides, and carbonates; adding a promoter to the catalyst precursor to yield a promoted precursor; drying the promoted precursor to yield dried catalyst; and calcining the dried catalyst, wherein the catalyst further comprises copper and potassium. A method of preparing a strengthened precipitated iron catalyst comprising: co-precipitating iron, copper, magnesium, and aluminum; washing the precipitate; alkalizing the precipitate; and drying the precipitate to yield a dried catalyst precursor. The dried catalyst precursor may be calcined and treated with a gas comprising carbon monoxide.
1. A method for preparing an iron catalyst to be used in a Fischer-Tropsch slurry reactor, the method comprising:
preparing a solution comprising ferrous and ferric nitrates, copper nitrate, and at least one of aluminum nitrates and magnesium nitrate by dissolving iron, copper, and at least one of magnesium and aluminum in nitric acid,
precipitating a catalyst precursor comprising at least one of iron hydroxides and iron carbonates, by combining the solution with a base;
contacting the catalyst precursor with a promoter comprising potassium and a structural promoter selected from the group consisting of potassium silicate, colloidal silica, TEOS, and polysilicic acid, to yield a promoted precursor, wherein the catalyst precursor is contacted with the promoter and the structural promoter by adding the promoter and the structural promoter to a slurry comprising the catalyst precursor;
drying the promoted precursor to yield dried catalyst, wherein the dried catalyst comprises from about 1 wt % SiO 2 to about 2.2 wt % SiO 2 ; and
calcining the dried catalyst.
2. The method of claim 1 wherein contacting the catalyst precursor with a promoter comprises contacting the catalyst precursor with an amount of potassium carbonate sufficient to promote the catalyst with potassium.
3. The method of claim 1 wherein the catalyst precursor further comprises copper oxide.
4. The method of claim 1 wherein contacting the catalyst precursor with a promoter comprises contacting the catalyst precursor with copper nitrate.
5. The method of claim 1 wherein the structural promoter comprises potassium silicate.
6. The method of claim 5 wherein the potassium silicate is an aqueous solution.
7. The method of claim 1 wherein the catalyst comprises about 1 wt % copper and about 1 wt % potassium.
8. The method of claim 1 wherein the structural promoter comprises TEOS.
9. The method of claim 1 wherein the structural promoter is colloidal silica.
10. The method of claim 9 wherein the silica is silica sol.
11. The method of claim 10 wherein the catalyst has an Fe: SiO 2 mass ratio of between about 100:1 and about 100:8.
12. The method of claim 11 wherein the Fe: SiO 2 mass ratio is about 100:5.
13. The method of claim 11 wherein the catalyst has an Fe:Cu:K:SiO 2 mass ratio of about 100:4:3:5.
14. The method of claim 11 wherein the Fe:Cu:K:SiO 2 mass ratio is about 100:3:3:5.
15. The method of claim 1 wherein the Fe:Cu mass ratio is between about 100:1 and 100:7.
16. The method of claim 15 wherein the Fe:Cu mass ratio is about 100:4.
17. The method of claim 1 wherein the promoter comprises potassium and wherein the Fe:K mass ratio of the iron catalyst is in the range of from about 100:1 to about 100:5.
18. The method of claim 17 wherein the Fe:K mass ratio is about 100:3.
19. The method of claim 1 wherein precipitating is performed at a pH in the range of from about 7.2 to about 7.4.
20. The method of claim 1 wherein the base is selected from the group consisting of ammonium hydroxide and sodium carbonate.
21. The method of claim 20 wherein the base comprises about 14.5 wt % aqueous ammonium hydroxide.
22. The method of claim 1 further comprising spray drying the catalyst prior to, subsequent to, or both prior to and subsequent to combining the promoted precursor with the structural promoter.
23. The method of claim 22 further comprising calcining the iron catalyst.
24. A method for preparing an iron catalyst to be used in a Fischer-Tropsch slurry reactor, the method comprising:
precipitating a catalyst precursor from a solution comprising an iron salt, and a copper salt, and at least one of aluminum salts and magnesium salts;
promoting the catalyst precursor by adding potassium carbonate and a structural promoter to a slurry comprising the catalyst precursor, wherein the structural promoter is selected from the group consisting of potassium silicate, colloidal silica, TEOS, and polysilicic acid;
drying to yield dried catalyst, wherein the dried catalyst comprises from about 1 wt % SiO 2 to about 2.2 wt % SiO 2 ; and
calcining the dried catalyst.
25. The method of claim 24 wherein precipitating the catalyst precursor comprises adding a base solution to the solution consisting essentially of the iron salt and the copper salt and the at least one of aluminum salts and magnesium salts.
26. The method of claim 24 wherein precipitating the catalyst precursor comprises adding the solution consisting essentially of the iron salt and the copper salt and the at least one of aluminum salts and magnesium salts to a base solution.
27. The method of claim 24 wherein precipitating the catalyst precursor comprises cofeeding a base solution and the solution consisting essentially of the iron salt and the copper salt and the at least one of aluminum salts and magnesium salts.
28. The method of claim 24 wherein the precipitation solution consists essentially of an iron salt and a copper salt and at least one salt selected from the group consisting of aluminum salts and magnesium salts.
29. A method for preparing an iron catalyst to be used in a Fischer-Tropsch slurry reactor, the method comprising:
forming a catalyst precursor from an iron salt, and a copper salt, and at least one of aluminum salts and magnesium salts;
precipitating a promoted precursor from the catalyst precursor by adding a solution comprising potassium and a structural promoter to a slurry comprising the catalyst precursor, wherein the structural promoter is selected from the group consisting of potassium silicate, colloidal silica, TEOS, and polysilicic acid;
drying the promoted precursor to yield dried catalyst, wherein the dried catalyst comprises from about 1 wt % SiO 2 to about 2.2 wt % SiO 2 ; and
calcining the dried catalyst.
30. The method of claim 29 wherein precipitating further comprises mixing a solution comprising TEOS with a solution comprising the iron salt and the copper salt and the at least one of aluminum salts and magnesium salts prior to precipitating the catalyst precursor.