US2014323601A1PendingUtilityA1
Fischer-Tropsch Catalyst
Est. expiryMay 1, 2026(expired)· nominal 20-yr term from priority
C10G 2/332B01J 37/03B01J 23/8953B01J 23/8896B01J 23/83B01J 23/80B01J 21/066B01J 21/06C07C 29/141C07C 1/0435C07C 2523/75B01J 35/40B01J 35/612B01J 35/613B01J 35/633B01J 35/647B01J 35/651B01J 35/615
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Claims
Abstract
The present invention is directed to a catalyst suitable for catalyzing a Fischer-Tropsch reaction, said catalyst comprising cobalt metal supported on zinc-oxide and having the following particle size distribution by volume: <10% having a particle size below 1 micron, 70-99% having a particle size between 1 and 5 micron, and <20% having a particle size above 5 micron.
Claims
exact text as granted — not AI-modified1 . A catalyst suitable for catalyzing a Fischer-Tropsch reaction, said catalyst comprising cobalt metal supported on zinc-oxide and having the following particle size distribution by volume:
<10% having a particle size below 1 micron, 75-85% having a particle size between 1 and 5 micron, and <15% having a particle size above 5 micron.
2 . (canceled)
3 . A catalyst according to claim 1 , wherein the volume average particle size is less than 1.5 to 15 μm.
4 . A catalyst according to claim 3 , wherein the pore volume is mainly formed by pores having a diameter within the range of 5-100 nm.
5 . A catalyst according to claim 1 , wherein the pore volume is less than 0.45 ml/g.
6 . A catalyst according to claim 1 , wherein the surface area is in the range of 5-100 m 2 /g.
7 . A catalyst according to claim 1 , wherein the zinc to cobalt atomic ratio is in the range of 40 to 0.1
8 . A catalyst according to claim 1 , wherein one or more promoters, such as ruthenium, hafnium, platinum, zirconium, palladium, rhenium, cerium, lanthanum or a combination thereof are present in a cobalt to promoter atomic ratio of up to 10:1.
9 . A catalyst according to claim 1 , further comprising at least one group compound of a IIIa element, in a concentration of 0.1-10 wt. %, based upon the total weight of the catalyst.
10 . A method for performing a Fischer-Tropsch process, comprising: contacting the catalyst of claim 1 with syngas; and recovering a product containing 5 or more carbon atoms.
11 . (canceled)
12 . A catalyst suitable for catalyzing a Fischer-Tropsch reaction, said catalyst comprising cobalt metal supported on zinc-oxide and having the following particle size distribution by volume:
<10% having a particle size below 1 micron, 75-85% having a particle size between 1 and 5 micron, and <15% having a particle size above 5 micron.
13 . A catalyst according to claim 12 , wherein the volume average particle size is less than 25 μm.
14 . A catalyst according to claim 12 , wherein the pore volume is mainly formed by pores having a diameter within the range of 5-100 nm.
15 . A catalyst according to claim 12 , wherein the pore volume is less than 0.5 ml/g.
16 . A catalyst according to claim 12 , wherein the surface area is less than 120 m 2 /g.
17 . A catalyst according to claim 12 , wherein the zinc to cobalt atomic ratio is in the range of 75 to 0.1.
18 . A catalyst according to claim 12 , wherein one or more promoters, such as ruthenium, hafnium, platinum, zirconium, palladium, rhenium, cerium, lanthanum or a combination thereof are present in a cobalt to promoter atomic ratio of up to 10:1.
19 . A catalyst according to claim 12 , further comprising at least one group compound of a Ma element in a concentration of 0.1-60 wt. %, based upon the total weight of the catalyst.
20 . A method for performing a Fischer-Tropsch process, comprising:
contacting the catalyst of claim 12 with syngas; and recovering a product containing 5 or more carbon atoms.Join the waitlist — get patent alerts
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