US2019225890A1PendingUtilityA1

Catalysts

Assignee: JOHNSON MATTHEY PLCPriority: Mar 31, 2015Filed: Apr 3, 2019Published: Jul 25, 2019
Est. expiryMar 31, 2035(~8.7 yrs left)· nominal 20-yr term from priority
C04B 2235/616B01D 39/2093C04B 38/0061C04B 2235/3275B01J 21/063B01J 35/04B01J 35/0053C04B 2111/0081B01J 23/75B01J 35/023C04B 38/00C04B 35/46C10G 2/332B01J 37/0201B01J 35/45B01J 35/40C07C 1/0425C04B 2235/658B01J 35/392
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Claims

Abstract

A catalyst precursor suitable for the Fischer Tropsch reaction is described comprising cobalt oxide supported on a porous support wherein the porous support is a ceramic foam comprising a closed cell structure.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A Fischer Tropsch reaction catalyst precursor, comprising cobalt oxide supported on a porous support that is a ceramic foam comprising a closed cell structure, wherein the ceramic foam has a cell fraction in the range of from 50 to 95 vol % relative to the volume of the ceramic foam. 
     
     
         2 . The catalyst precursor of  claim 1 , wherein the cobalt content, expressed as Co, is in the range of 5-50% by weight of the total precursor. 
     
     
         3 . The catalyst precursor of  claim 1 , wherein up to 20% by volume of the cell volume is interconnected. 
     
     
         4 . The catalyst precursor of  claim 1 , wherein the closed cell structure comprises cells having an average cell diameter in a size range of from 10 to 150 μm. 
     
     
         5 . The catalyst precursor of  claim 1 , wherein the ceramic foam contains cells having cell walls, where the cell wall thicknesses is up to 500 μm with an average cell wall thickness in the range of 10-100 μm. 
     
     
         6 . The catalyst precursor of  claim 1 , wherein the ceramic foam comprises titania. 
     
     
         7 . The catalyst precursor of  claim 1 , that has been subjected to a heating step at a temperature in the range of 500-1600° C. 
     
     
         8 . A catalyst comprising elemental cobalt supported on a porous ceramic foam support having a closed cell structure, wherein the ceramic foam support has a cell fraction in the range of from 50 to 95 vol % relative to the volume of the ceramic foam support. 
     
     
         9 . The catalyst of  claim 8 , wherein the cobalt content, expressed as Co, is in the range of 5-50% by weight of the total precursor. 
     
     
         10 . The catalyst of  claim 8 , wherein up to 20% by volume of the cell volume is interconnected. 
     
     
         11 . The catalyst of  claim 8 , wherein the closed cell structure comprises cells having an average cell diameter in a size range of from 10 to 150 μm. 
     
     
         12 . The catalyst of  claim 8 , wherein the ceramic foam contains cells having cell walls, where the cell wall thicknesses is up to 500 μm with an average cell wall thickness in the range of 10-100 μm. 
     
     
         13 . The catalyst of  claim 8 , wherein the ceramic foam comprises titania. 
     
     
         14 . The catalyst of  claim 8 , prepared by applying a reducing gas stream to a Fisher Tropsch reaction catalyst precursor comprising cobalt oxide supported on a porous support that is a ceramic foam comprising a closed cell structure, wherein the ceramic foam has a cell fraction in the range of from 50 to 95 vol % relative to the volume of the ceramic foam. 
     
     
         15 . A Fisher-Tropsch reaction process for producing hydrocarbons, comprising contacting a synthesis gas comprising carbon monoxide and hydrogen with a catalyst of  claim 8 .

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