US2003119668A1PendingUtilityA1
Catalysts with high cobalt surface area
Est. expiryMay 19, 2020(expired)· nominal 20-yr term from priority
B01J 35/40C07C 209/48B01J 21/04C10G 45/00B01J 23/75C10G 2/332C07C 1/0445B01J 37/031C07C 2523/75C07C 2521/04C07C 209/32C07C 209/36B01J 35/392B01J 35/60B01J 35/635B01J 35/647
45
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Claims
Abstract
A catalyst or precursor thereto comprising cobalt and/or a cobalt compound on a transition alumina support having a total cobalt content of at least 41% by weight and a cobalt surface area, after reduction, greater than 25 m 2 per gram of total cobalt. The catalyst or precursor may be made by slurrying a transition alumina powder having a pore volume of at least 0.7 ml/g with an aqueous cobalt ammine carbonate complex and heating the slurry to decompose the complex.
Claims
exact text as granted — not AI-modified1 . A particulate catalyst precursor comprising cobalt compounds supported on a transition alumina support and having a total cobalt content of 20 to 85% by weight, a pore volume above 0.3 ml/g, and a surface-weighted mean diameter D[3,2] in the range 1 μm to 200 μm and which, upon reduction, has a cobalt surface area of at least 25 m 2 per gram of total cobalt.
2 . A catalyst precursor according to claim 1 having a total cobalt content above 40% by weight.
3 . A catalyst precursor according to claim 1 having a pore volume above 0.5 ml/g.
4 . A catalyst precursor according to claim 1 having a surface-weighted mean diameter D[3,2] below 20 μm.
5 . A catalyst precursor according to claim 1 having an average pore diameter of at least 8 nm.
6 . A catalyst precursor according to claim 1 wherein the cobalt is present as cobalt oxides.
7 . A catalyst precursor according to claim 1 having a total cobalt content above 50% by weight and wherein the alumina is a gamma alumina.
8 . A particulate catalyst comprising cobalt supported on a transition alumina support and having a total cobalt content of 20 to 85% by weight, a pore volume above 0.3 ml/g, a surface-weighted mean diameter D[3,2] in the range 1 μm to 200 μm, and a cobalt surface area of at least 25 m 2 per gram of total cobalt.
9 . A catalyst according to claim 8 having a total cobalt content above 40% by weight.
10 . A catalyst according to claim 8 having a pore volume above 0.5 ml/g.
11 . A catalyst according to claim 8 having a surface-weighted mean diameter D[3,2] below 20 μm.
12 . A catalyst according to claim 8 having an average pore diameter of at least 8 nm.
13 . A catalyst according to claim 8 having a total cobalt content above 50% by weight and wherein the alumina is a gamma alumina.
14 . A catalyst according to claim 8 wherein at least 50% of the cobalt is present as metallic cobalt.
15 . A method of making a catalyst precursor containing 20 to 85% by weight of total cobalt comprising slurrying a transition alumina powder having a pore volume above 0.7 ml/g with an aqueous solution of a cobalt ammine complex, heating the slurry to cause the cobalt ammine complex to decompose with the deposition of an insoluble cobalt compound, filtering the solid residue from the aqueous medium and drying the solid residue.
16 . A method according to claim 15 wherein the slurry is heated for a period of not more than 200 minutes to cause the cobalt ammine complex to decompose.
17 . A method according to claim 15 wherein the alumina powder has a surface-weighted mean diameter D[3,2] in the range 1 μm to 200 μm.
18 . A method according to claim 15 wherein the transition alumina powder has a surface-weighted mean diameter D[3,2] below 20 μm.
19 . A method according to claim 15 , wherein the transition alumina powder has an average pore diameter of at least 10 nm.Join the waitlist — get patent alerts
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