US2015306583A1PendingUtilityA1

Middle distillate hydrocracking catalyst with a base extrudate having a high nanopore volume

Assignee: ZHANG YIHUAPriority: Apr 24, 2014Filed: Apr 24, 2014Published: Oct 29, 2015
Est. expiryApr 24, 2034(~7.7 yrs left)· nominal 20-yr term from priority
B01J 35/80B01J 2235/00B01J 35/30B01J 35/40B01J 35/31C10G 2300/1048C10G 47/20B01J 29/166C10G 2300/1044B01J 29/064B01J 29/076B01J 2229/20B01J 2229/42C10G 2300/70B01J 35/617B01J 35/638B01J 35/635B01J 35/66B01J 35/647B01J 35/615B01J 21/12B01J 23/888B01J 29/084B01J 37/0009B01J 37/0201
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Claims

Abstract

The present invention is directed to an improved hydrocracking catalyst containing a amorphous silica-alumina (ASA) base and alumina support. The ASA base is characterized as having a high nanopore volume and low particle density. The alumina support is characterized as having a high nanopore volume. Hydrocracking catalysts employing the combination high nanopore volume ASA base and alumina support exhibit improved hydrogen efficiency, and greater product yield and quality, as compared to hydrocracking catalysts containing conventional ASA base and alumina components.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A hydrocracking catalyst, comprising:
 a base extrudate comprising at least one molecular sieve, an alumina and an amorphous silica alumina support, wherein the base extrudate has a nanopore volume in the 6 nm to 11 nm range of 0.5 to 0.9 cc/g; and   at least one metal selected from the group consisting of elements from Group 6 and Groups 8 through 10 of the Periodic Table.   
     
     
         2 . The hydrocracking catalyst of  claim 1 , wherein the base extrudate is formed using an alumina having a nanopore volume in the 6 nm to 11 nm range of 0.1 to 0.3 cc/g. 
     
     
         3 . The hydrocracking catalyst of  claim 2 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g. 
     
     
         4 . The hydrocracking catalyst of  claim 1 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g. 
     
     
         5 . The hydrocracking catalyst of  claim 1 , wherein the base extrudate has a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g. 
     
     
         6 . The hydrocracking catalyst of  claim 1 , wherein the base extrudate has a particle density of 0.7 to 0.9 cc/g. 
     
     
         7 . A method for making a hydrocracking catalyst, comprising the steps of:
 forming a base extrudate comprising at least one molecular sieve, an alumina and an amorphous silica alumina support, wherein the base extrudate has a nanopore volume in the 6 nm to 11 nm range of 0.5 to 0.9 cc/g; and   impregnating the base extrude with at least one metal selected from the group consisting of elements from Group 6 and Groups 8 through 10 of the Periodic Table.   
     
     
         8 . The method of  claim 7 , wherein the base extrudate is formed using an alumina having a nanopore volume in the 6 nm to 11 nm range of 0.1 to 0.3 cc/g. 
     
     
         9 . The method of  claim 8 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g. 
     
     
         10 . The method of  claim 7 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g. 
     
     
         11 . The method of  claim 7 , wherein the base extrudate has a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g. 
     
     
         12 . The method of  claim 7 , wherein the base extrudate has a particle density of 0.7 to 0.9 cc/g. 
     
     
         13 . A process for hydrocracking a hydrocarbonaceous feedstock, comprising contacting the feedstock with a hydrocracking catalyst under hydrocracking conditions to produce a hydrocracked effluent;
 the hydrocracking catalyst comprising
 a base extrudate comprising at least one molecular sieve, an alumina and an amorphous silica alumina support, wherein the base extrudate has a nanopore volume in the 6 nm to 11 nm range of 0.5 to 0.9 cc/g; and 
 at least one metal selected from the group consisting of elements from Group 6 and Groups 8 through 10 of the Periodic Table. 
   
     
     
         14 . The process of  claim 13 , wherein the base extrudate is formed using an alumina having a nanopore volume in the 6 nm to 11 nm range of 0.1 to 0.3 cc/g. 
     
     
         15 . The process of  claim 14 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g. 
     
     
         16 . The process of  claim 13 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g. 
     
     
         17 . The process of  claim 13 , wherein the base extrudate has a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g. 
     
     
         18 . The process of  claim 13 , wherein the base extrudate has a particle density of 0.7 to 0.9 cc/g.

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