US2020061586A1PendingUtilityA1

Process for preparing porous iron oxide-zirconia composite catalyst, porous iron oxide-zirconia composite catalyst prepared thereby, and method for producing alcohol using the catalyst

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Assignee: UNIV SOGANG RES FOUNDATIONPriority: Aug 22, 2018Filed: Sep 18, 2018Published: Feb 27, 2020
Est. expiryAug 22, 2038(~12.1 yrs left)· nominal 20-yr term from priority
B01J 37/086B01J 23/745B01J 23/002B01J 37/084B01J 37/0234C25B 11/04B01J 37/0018B01J 37/0236C07C 29/48B01J 37/088B01J 21/066B01J 37/0201B01J 35/1066B01J 35/1019B01J 35/1023B01J 35/1014B01J 35/1071B01J 35/1009B01J 35/30B01J 37/08B01J 2235/15B01J 2235/30B01J 35/70B01J 2235/00C25B 3/23B01J 35/653B01J 35/657B01J 35/612B01J 35/613B01J 35/615B01J 35/617B01J 35/651
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Claims

Abstract

The present invention relates to a porous iron oxide-zirconia composite catalyst, a preparation method thereof, and a method for producing alcohol using the same, and the iron oxide-zirconia composite catalyst having a porous structure may produce alcohol at low cost by carrying out an excellent methane reforming reaction even under room temperature and room pressure conditions through an electrochemical reaction.

Claims

exact text as granted — not AI-modified
1 . A method for preparing a porous iron oxide-zirconia composite catalyst, the method including:
 impregnating a polymer template mold with a precursor mixture of iron oxide precursor and a zirconia precursor;   drying the polymer template mold impregnated with the precursor mixture; and   sintering the dried polymer template mold.   
     
     
         2 . The method of  claim 1 ,
 wherein the iron oxide precursor is one or more selected from the group consisting of iron (III) nitrate, iron (III) chlorate, and iron (III) sulfate.   
     
     
         3 . The method of  claim 1 ,
 wherein the zirconia precursor is one or more selected from the group consisting of zirconium oxynitrate, zirconium nitrate, and zirconium sulfate.   
     
     
         4 . The method of  claim 1 ,
 wherein the iron oxide precursor and the zirconia precursor are mixed at a molar ratio of 8:1 to 2:1.   
     
     
         5 . The method of  claim 1 ,
 wherein the polymer template mold includes a spherical polymer arranged in a face centered cubic (fcc) structure.   
     
     
         6 . The method of  claim 1 ,
 wherein the polymer template mold is manufactured by a method including emulsion polymerization of monomers, followed by drying step.   
     
     
         7 . The method of  claim 1 ,
 wherein the polymer template mold includes one or more polymers selected from the group consisting of poly(methyl methacrylate) [PMMA], poly(butyl methacrylate) [PBMA], poly(methyl methacrylate)(butyl methacrylate), poly(hydroxyethyl methacrylate) [PHEMA], and polystyrene.   
     
     
         8 . A porous iron oxide-zirconia composite catalyst manufactured by a method comprising:
 impregnating a polymer template mold with a precursor mixture of iron oxide precursor and a zirconia precursor;   drying the polymer template mold impregnated with the precursor mixture; and   sintering the dried polymer template mold,   wherein the average pore size is 50 to 900 nm.   
     
     
         9 . The porous iron oxide-zirconia composite catalyst of  claim 8 ,
 wherein the porous iron oxide-zirconia composite catalyst has a specific surface area of 1 to 1,000 m 2 /g.   
     
     
         10 . The porous iron oxide-zirconia composite catalyst of  claim 8 ,
 wherein the composite catalyst has a molar ratio of iron oxide to zirconia of 9.9:0.1 to 4.0:6.0.   
     
     
         11 . The porous iron oxide-zirconia composite catalyst of  claim 8 ,
 wherein zirconia in the porous iron oxide-zirconia composite catalyst is in the form of tetragonal phase.   
     
     
         12 . A method for manufacturing alcohols, the method comprising:
 contacting the porous iron oxide-zirconia composite catalyst of  claim 8  with methane.   
     
     
         13 . The method of  claim 12 ,
 wherein the contacting is carried out at a temperature of 5 to 40° C.   
     
     
         14 . The method of  claim 12 ,
 wherein the contacting is carried out at a pressure of 1 to 20 bar.   
     
     
         15 . The method of  claim 12 ,
 wherein the alcohol is methanol, 1-propanol, 2-propanol, or ethanol.

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