US2014315710A1PendingUtilityA1

Process for the conversion of lower alkanes to aromatic hydrocarbons

Assignee: SHELL OIL COPriority: Feb 18, 2008Filed: Jul 2, 2014Published: Oct 23, 2014
Est. expiryFeb 18, 2028(~1.6 yrs left)· nominal 20-yr term from priority
B01J 29/44B01J 29/7492C10G 11/05C07C 2529/44B01J 37/0201B01J 29/67C07C 2529/67C10G 45/68B01J 2229/42Y02P20/52B01J 29/068C07C 2529/74C07C 2/76B01J 37/0009
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Claims

Abstract

A process for producing aromatic hydrocarbons which comprises (a) contacting one or more lower alkanes with a dehyroaromatization aromatic catalyst which is comprised of 0.005 to 0.1% wt platinum, not more than 0.2% wt of an amount of an attenuating metal wherein the amount of platinum is not more than about 0.02% wt more than the amount of the attenuating metal, from about 10 to about 99.9% wt of an aluminosilicate, and a binder, and (b) separating methane, hydrogen, and C 2-5 hydrocarbons from the reaction products of step (a) to produce aromatic reaction products including benzene.

Claims

exact text as granted — not AI-modified
1 . A catalyst comprising:
 (a) about 0.005 to about 0.1% wt platinum, basis the metal,   (b) an amount of an attenuating metal selected from the group consisting of tin, lead, and germanium which is not more than about 0.2% wt of the catalyst, basis the metal, and wherein the amount of platinum is not more than about 0.02% wt more than the amount of the attenuating metal,   (c) about 10 to about 99.9% wt of an aluminosilicate, and   (d) a binder.   
     
     
         2 . The catalyst of  claim 1  wherein the amount of platinum is from about 0.01 to about 0.05% wt. 
     
     
         3 . The catalyst of  claim 1  wherein the catalyst comprises not more than about 0.15% wt of the attenuating metal. 
     
     
         4 . The catalyst of  claim 1  wherein the amount of the aluminosilicate is from about 30 to about 99.9% wt. 
     
     
         5 . The catalyst of  claim 1  wherein the aluminosilicate has a silicon dioxide:aluminum trioxide molar ratio of from about 20 to about 80. 
     
     
         6 . The catalyst of  claim 1  wherein the aluminosilicate is a zeolite.

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