US2017175003A1PendingUtilityA1

Catalyst composition for producing hydrocarbons and method for producing hydrocarbons

Assignee: COSMO OIL CO LTDPriority: Dec 18, 2009Filed: Mar 2, 2017Published: Jun 22, 2017
Est. expiryDec 18, 2029(~3.4 yrs left)· nominal 20-yr term from priority
C10G 2/334C10G 2400/02B01J 27/232B01J 29/48B01J 23/8892B01J 29/076B01J 23/6562
56
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Claims

Abstract

There are provided a catalyst composition for producing hydrocarbons and a method for producing hydrocarbons which exhibit a high CO conversion rate, generates minimal amount of gaseous components, and is also capable of efficiently obtaining, from a syngas, a gasoline fraction which is selective for and rich in the components having a high octane number, such as aromatic, naphthenic, olefinic and branched paraffinic hydrocarbons, by using a Fischer-Tropsch synthesis catalyst that contains at least one type of metal exhibiting activity in Fischer-Tropsch reaction and manganese carbonate and a zeolite serving as a solid acid.

Claims

exact text as granted — not AI-modified
1 - 3 . (canceled) 
     
     
         4 . A method for producing hydrocarbons comprising:
 a FT reaction for synthesizing hydrocarbons from a gas composed mainly of hydrogen and carbon monoxide using a Fischer-Tropsch synthesis catalyst that contains at least one type of metal exhibiting activity in Fischer-Tropsch reaction and manganese carbonate; and   a conversion reaction in which hydrocarbons obtained by the FT reaction are brought into contact with a zeolite serving as a solid acid.   
     
     
         5 . The method for producing hydrocarbons according to  claim 4 ,
 wherein the FT reaction and the conversion reaction are carried out at the same time in the same reaction vessel.   
     
     
         6 . The method for producing hydrocarbons according to  claim 5 ,
 wherein the FT reaction and the conversion reaction are carried out using a catalyst composition containing the Fischer-Tropsch synthesis catalyst and a zeolite serving as a solid acid.   
     
     
         7 . The method for producing hydrocarbons according to  claim 4 , wherein the FT reaction and the conversion reaction are carried out at 230 to 350° C. 
     
     
         8 - 9 . (canceled)

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