US2016214093A1PendingUtilityA1

Catalyst structure and method of fischer-tropsch synthesis

Assignee: BATTELLE MEMORIAL INSTITUTEPriority: Aug 17, 1999Filed: Dec 21, 2015Published: Jul 28, 2016
Est. expiryAug 17, 2019(expired)· nominal 20-yr term from priority
B01J 35/395B01J 2235/30B01J 35/56B01J 23/8913B01J 23/462B01J 23/75B01J 35/1009B01J 8/0285B01J 12/007B01J 19/248B01J 37/0221B01J 37/0238B01J 37/0244B01J 2219/32293B01J 2219/32296B01J 2219/32408B01J 2219/32466B01J 2219/32475C07C 1/041C07C 1/0425C07C 1/0455C07C 2523/46C07C 2523/745C07C 2523/75C10G 2/33C10G 2/332B01J 35/19B01J 35/60B01J 35/612
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Claims

Abstract

The present invention includes Fischer-Tropsch catalysts, reactions using Fischer-Tropsch catalysts, methods of making Fischer-Tropsch catalysts, processes of hydrogenating carbon monoxide, and fuels made using these processes. The invention provides the ability to hydrogenate carbon monoxide with low contact times, good conversion rates and low methane selectivities. In a preferred method, the catalyst is made using a metal foam support.

Claims

exact text as granted — not AI-modified
1 - 12 . (canceled) 
     
     
         13 . A catalyst, comprising:
 a porous stainless steel support;   a titania layer disposed over the porous stainless steel support;   an alumina interfacial layer disposed over the titania layer; and   a Fischer-Tropsch catalytic metal selected from iron, cobalt, nickel, ruthenium, rhenium, osmium and combinations thereof disposed on the alumina interfacial layer.   
     
     
         14 . The catalyst of  claim 13  wherein the interfacial layer has a surface area, as measured by BET, of at least 1.0 m 2 /g. 
     
     
         15 . The catalyst of  claim 13  wherein the porous stainless steel support has a porosity of 30% to 99%. 
     
     
         16 . The catalyst of  claim 13  wherein the catalyst does not show spalling after 3 thermal cycles from room temperature to 600° C. in air. 
     
     
         17 . A catalyst, comprising:
 a porous nickel support;   a titania layer disposed over the porous stainless steel support;   an alumina interfacial layer disposed over the titania layer; and   a Fischer-Tropsch catalytic metal selected from iron, cobalt, nickel, ruthenium, rhenium, osmium and combinations thereof disposed on the alumina interfacial layer.

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