US2014058182A1PendingUtilityA1

Catalyst with Supplement Component for Hydroprocessing of Bio-feedstock

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Assignee: AGGREGATE ENERGY LLCPriority: Jun 12, 2009Filed: Feb 13, 2013Published: Feb 27, 2014
Est. expiryJun 12, 2029(~2.9 yrs left)· nominal 20-yr term from priority
B01J 35/45B01J 35/40B01J 31/06B82Y 30/00B01J 23/883C10G 2300/1014B01J 25/02C10G 2300/1018C10G 3/46C10G 3/45B01J 23/755B01J 37/06B01J 23/882B01J 37/0018B01J 37/20B01J 25/00B01J 37/0036C10G 3/50C10G 3/00Y02P30/20B01J 2231/643B01J 23/88B01J 21/18B01J 27/055B01J 23/888C10G 2300/70B01J 37/04C10G 3/47B01J 21/185B01J 35/33
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Claims

Abstract

A process for hydrogenation of oxygen-containing organic products, oil refinery products or mixtures thereof, wherein the process comprises bringing the organic products, oil refinery products, or mixtures thereof into contact with a catalyst according to claim 1 in the presence of hydrogen gas at a temperature in the range of 200 to 500° C. and at a pressure in the range of 10 to 1000 bar.

Claims

exact text as granted — not AI-modified
We claim: 
     
         1 . A catalyst, comprising at least one metal component selected from the group consisting of cobalt, nickel, molybdenum, and tungsten, and
 at least one non-metallic supplement component that is electrically conducting;   wherein the catalyst includes a mixture of particles of the at least one metal component and the at least one non-metallic supplement component.   
     
     
         2 . The catalyst of  claim 1 , wherein the metal component is molybdenum. 
     
     
         3 . The catalyst of  claim 1 , wherein the supplement component is hydrophobic or is made hydrophobic. 
     
     
         4 . The catalyst of  claim 1 , wherein the supplement component comprises one or more constituents selected of the group of materials that are graphite, graphite-containing material, graphite-like material, made graphitic material, carbon black, carbon fibers, single-walled carbon nanotubes, multi-walled carbon nanotubes, carbon nanofibers, mesoporous carbon, fullerene, doped diamond, conducting polymers, ion-conducting polymers, polyaniline, polythiophene, polypyrrol, polyacetylene, poly(para-phenylene), poly(para-phenylenvinylene), polyethylendioxythiophene, polybenzimidazole, polyphthalocyanin, ion-exchanging material, ion-exchanging resin, sulfonated polymers, sulfonated high performance polymers, sulfonated PTFE, sulfonated PPS, sulfonated PEEK, polyphosphazene, fullerene hydride, C 60 H x  with x=1-60, C 70 H x  with x=1-70, conducting metal oxide or mixed metal oxide, doped metal oxide, tin oxide/indium tin oxide, titanium oxide, zirconium oxide, cerium oxide, tungsten oxides, Na +  super ionic conductor NASICON, ceramic ion-conductor, tungsten carbide, metallate containing cobalt, vanadium, iron, nickel, manganese or tungsten; amorphous or nanocrystalline transition metal oxide materials, amorphous or nanocrystalline VO 2 , CrO 2 , MoO 2  or LiMn 2 O 4 ; perovskite-based metal oxide, perovskite or a conducting ceramic material. 
     
     
         5 . The catalyst of  claim 1 , wherein the metal component comprises a Raney alloy. 
     
     
         6 . The catalyst of  claim 1 , wherein the catalyst or the metal component are sulfided. 
     
     
         7 . The catalyst of  claim 1 , wherein the catalyst further comprises a support material or carrier. 
     
     
         8 . The catalyst of  claim 1 , wherein the catalyst is in the form of a powder. 
     
     
         9 . The catalyst of  claim 1 , wherein the catalyst is in the form of a sintered body. 
     
     
         10 . The catalyst of  claim 1 , wherein the catalyst is in the form of a porous pellet. 
     
     
         11 . The catalyst of  claim 1 , wherein the catalyst further comprises a binding material. 
     
     
         12 . The catalyst of  claim 1 , wherein the catalyst further comprises a pore forming material. 
     
     
         13 . A process for hydrogenation of oxygen-containing organic products, oil refinery products or mixtures thereof, wherein the process comprises bringing the organic products, oil refinery products, or mixtures thereof into contact with a catalyst according to  claim 1  in the presence of hydrogen gas at a temperature in the range of 200 to 500° C. and at a pressure in the range of 10 to 1000 bar. 
     
     
         14 . The process of  claim 13 , where the hydrogenation is carried out in a batch reactor, a continuous reactor or a micro reactor. 
     
     
         15 . The process of  claim 13 , wherein the oxygen-containing organic products are selected from the group consisting of rape seed oil, sun flower oil, palm oil, nuts oil, olive oil, coliza oil, canola oil, tall oil, hemp seed oil, linseed oil, mustard oil, peanut oil, castor oil, coconut oil, train lard, lard, tallow, jatropha oil, oils from algae, the pyrolysate from plan-biomass, animal fats, fatty acids, fish oils, and mixtures thereof.

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