US2014357916A1PendingUtilityA1

Rhenium Promoted Catalyst

Assignee: FINA TECHNOLOGYPriority: May 31, 2010Filed: Aug 14, 2014Published: Dec 4, 2014
Est. expiryMay 31, 2030(~3.9 yrs left)· nominal 20-yr term from priority
B01J 29/076B01J 29/16C07C 2529/08B01J 29/26C07C 2529/06C07C 6/06B01J 29/83B01J 29/85Y02P20/584C07C 6/12Y02P20/50C07C 2523/36C07C 2523/20Y02P20/52B01J 38/12B01J 29/90B01J 38/14B01J 2229/20B01J 37/0203B01J 38/10C07C 2529/18
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Claims

Abstract

A group V metal/rhenium-modified molecular sieve catalyst can be used in hydrocarbon conversion reactions. Embodiments can provide a toluene conversion of at least 30 wt % with selectivity to benzene above 40 wt % and to xylenes above 40 wt % and non-aromatics selectivity of less than 2.0 wt %.

Claims

exact text as granted — not AI-modified
1 . A catalyst comprising:
 a molecular sieve catalyst containing a group V metal and rhenium;   wherein the molecular sieve catalyst is a zeolite, a faujasite, a crystalline silicoaluminophosphate (SAPO), or an aluminophosphate (ALPO), and wherein the molecular sieve catalyst contains at least 0.0002 wt % and up to 0.3 wt % of the rhenium based on the total weight of the catalyst.   
     
     
         2 . The catalyst of  claim 1 , wherein the rhenium comes from a rhenium precursor comprising one or more rhenium compounds. 
     
     
         3 . The catalyst of  claim 2 , wherein the rhenium precursor is selected from the group consisting of water-soluble rhenium compounds. 
     
     
         4 . The catalyst of  claim 2 , wherein the rhenium precursor is selected from the group consisting of sodium perrhenate, ammonium perrhenate, and dirhenium decacarbonyl. 
     
     
         5 . The catalyst of  claim 1 , wherein the group V metal is niobium. 
     
     
         6 . The catalyst of  claim 5 , wherein the niobium comes from a niobium precursor comprising one or more niobium compounds. 
     
     
         7 . The catalyst of  claim 6 , wherein the niobium precursor is selected from the group consisting of water-soluble niobium compounds. 
     
     
         8 . The catalyst of  claim 6 , wherein the niobium precursor is selected from the group consisting of niobium oxalate and ammonium niobate(V) oxalate. 
     
     
         9 . The catalyst of  claim 1 , wherein the molecular sieve catalyst is the zeolite. 
     
     
         10 . The catalyst of  claim 1 , wherein the molecular sieve catalyst is the crystalline silicoaluminophosphate (SAPO). 
     
     
         11 . The catalyst of  claim 1 , wherein the molecular sieve catalyst is the aluminophosphate (ALPO). 
     
     
         12 . The catalyst of  claim 1 , wherein the molecular sieve catalyst contains at least 0.005 wt % niobium based on the total weight of the catalyst. 
     
     
         13 . (canceled) 
     
     
         14 . (canceled) 
     
     
         15 . A process for disproportionation of toluene to benzene and xylene, comprising:
 passing a toluene/hydrogen feedstock over a group V metal/rhenium-molecular sieve catalyst at a reaction temperature ranging from 150° C. to 500° C. and a reaction pressure ranging from 200 psig to 800 psig;   wherein the molecular sieve catalyst is a zeolite, a faujasite, a crystalline silicoaluminophosphate (SAPO), or an aluminophosphate (ALPO), and wherein the molecular sieve catalyst contains at least 0.0002 wt % and up to 0.3 wt % of the rhenium based on the total weight of the catalyst.   
     
     
         16 . The process of  claim 15 , wherein the molecular sieve catalyst is the faujasite. 
     
     
         17 . The process of  claim 15 , wherein the group V metal content of the catalyst is from 0.005 wt % to 5.0 wt % based on the total weight of the catalyst. 
     
     
         18 . The process of  claim 15 , wherein the rhenium content of the catalyst is from 0.0002 wt % to 1.0 wt % based on the total weight of the catalyst. 
     
     
         19 . The process of  claim 15 , wherein the reaction temperature ranges from 300° C.-400° C. 
     
     
         20 . The process of  claim 15 , wherein the molecular sieve catalyst is the crystalline silicoaluminophosphate (SAPO). 
     
     
         21 . The process of  claim 15 , wherein the hydrogen:toluene molar ratio is between 0.05:1 to 4:1. 
     
     
         22 . The process of  claim 15 , wherein the reaction pressure range is between 400 psig to 800 psig. 
     
     
         23 . The process of  claim 15 , wherein the molecular sieve catalyst is the aluminophosphate (ALPO). 
     
     
         24 . (canceled) 
     
     
         25 . (canceled)

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