Catalyst and process using ssz-91 and zsm-12

Abstract

An improved hydroisomerization catalyst and process for making a base oil product using a catalyst comprising SSZ-91 molecular sieve and ZSM-12 molecular sieve. The catalyst and process generally involves the use of a catalyst comprising an SSZ-91 molecular sieve combined with a ZSM-12 molecular sieve to produce dewaxed base oil products by contacting the catalyst with a hydrocarbon feedstock. The catalyst and process provide improved base oil cold properties, such as pour point and cloud point, along with other beneficial base oil properties.

What is claimed is: 
     
         1 . A hydroisomerization catalyst, useful to make dewaxed products including base oils having improved cloud and pour points, comprising
 a catalyst composition comprising an SSZ-91 molecular sieve and a ZSM-12 molecular sieve;   wherein, the ZSM-12 molecular sieve is present in an amount from about 1.0 to 15.0 wt. %.   
     
     
         2 . The catalyst of  claim 1 , wherein the SSZ-91 molecular sieve and a ZSM-12 molecular sieve are combined with a matrix material to form a base material, and wherein the catalyst further comprises at least one modifier selected from Groups 6 to 10 and Group 14, and optionally further comprising a Group 2 metal, of the Periodic Table. 
     
     
         3 . The catalyst of  claim 1 , wherein the SSZ-91 molecular sieve comprises ZSM-48 type zeolite material, the molecular sieve having:
 at least 70% polytype 6 of the total ZSM-48-type material;   an EUO-type phase in an amount of between 0 and 3.5 percent by weight; and   polycrystalline aggregate morphology comprising crystallites having an average aspect ratio of between 1 and 8.   
     
     
         4 . The catalyst of  claim 1 , wherein the silicon oxide to aluminum oxide mole ratio of the SSZ-91 molecular sieve and/or the ZSM-12 molecular sieve is in the range of 40 to 220 or 50 to 220 or 40 to 200, or 50 to 140. 
     
     
         5 . The catalyst of  claim 3 , wherein the SSZ-91 molecular sieve comprises one of more of:
 at least 80%, or 90%, polytype 6 of the total ZSM-48-type material;   between 0.1 and 2 wt. % EU-1;   crystallites having an average aspect ratio of between 1 and 5, or between 1 and 3;   or a combination thereof.   
     
     
         6 . The catalyst of  claim 2 , wherein the modifier content is 0.01-5.0 wt. % or 0.01-2.0 wt. %, or 0.1-2.0 wt. % (total catalyst weight basis). 
     
     
         7 . The catalyst of  claim 2 , wherein the catalyst comprises Pt, or a combination of Pt and Pd, as the modifier in an amount of 0.01-1.0 wt. %, or 0.3-0.8 wt. % Pt or the combination of Pt and Pd, optionally further comprising Mg. 
     
     
         8 . The catalyst of  claim 2 , wherein the matrix material is selected from alumina, silica, ceria, titania, tungsten oxide, zirconia, or a combination thereof. 
     
     
         9 . The catalyst of  claim 2 , wherein the catalyst comprises 0.01 to 5.0 wt. % of the modifier, 0 to 99 wt. % of the matrix material, and 0.1 to 99 wt. % of the SSZ-91 and ZSM-12 molecular sieves. 
     
     
         10 . The catalyst of  claim 9 , wherein the catalyst comprises 0.1 to 99 wt. % of the SSZ-91 molecular sieve and about 1 to 15 wt. % of the ZSM-12 molecular sieve, or about 1 to 12 wt. % of the ZSM-12 molecular sieve. 
     
     
         11 . The catalyst of  claim 1 , wherein the product is a base oil product, or is used to make a base oil product, having a viscosity index of at least about 109 and/or a pour point or a cloud point of no greater than about −12° C. or −15° C. or −20° C. 
     
     
         12 . A process for producing a base oil product having reduced base oil pour point and/or cloud point, the process comprising contacting a hydrocarbon feedstock with the hydroisomerization catalyst of  claim 1  under hydroisomerization conditions to produce a base oil product. 
     
     
         13 . The process of  claim 12 , wherein the hydrocarbon feedstock comprises gas oil; vacuum gas oil; long residue; vacuum residue; atmospheric distillate; heavy fuel; oil; wax and paraffin; used oil; deasphalted residue or crude; charges resulting from thermal or catalytic conversion processes; shale oil; cycle oil; animal and vegetable derived fats, oils and waxes; petroleum and slack wax; or a combination thereof. 
     
     
         14 . The process of  claim 12 , wherein the base oil pour point and/or the base oil cloud point is reduced using the catalyst of  claim 1  as compared with the same process using a catalyst comprising the same SSZ-91 molecular sieve but excluding the ZSM-12 molecular sieve. 
     
     
         15 . The process of  claim 14 , wherein the base oil pour point and/or the base oil cloud point is reduced by at least about 1° C. or 3° C. or 5° C. or 10° C. using the catalyst of  claim 1  as compared with the same process using a catalyst comprising the same SSZ-91 molecular sieve but excluding the ZSM-12 molecular sieve. 
     
     
         16 . The process of  claim 12 , wherein the product is a base oil product, or is used to make a base oil product, having a viscosity index of at least about 109 and/or a pour point or a cloud point of no greater than about −12° C. or −15° C. or −20° C. 
     
     
         17 . A process for making the hydroisomerization catalyst of  claim 1 , comprising mixing together the SSZ-91 molecular sieve, the ZSM-12 molecular sieve, any added matrix material and sufficient liquid to form an extrudable paste; extruding the paste to form an extrudate base; impregnating the extrudate base with a metal impregnation solution containing at least one modifier selected from Groups 6 to 10 and Group 14, and optionally further comprising a Group 2 metal, of the Periodic Table, to form a metal loaded extrudate; and subjecting the metal loaded extrudate to drying and calcination post-treatment conditions. 
     
     
         18 . The process of  claim 17 , wherein
 the SSZ-91 molecular sieve, the ZSM-12 molecular sieve, any added matrix material and the liquid are mixed together at about 20 to 80° C. for about 0.5 to 30 min.;   the extrudate is formed at about 20 to 80° C. and dried at about 90-150° C. for 0.5-8 hrs;   the extrudate is calcined at 260-649° C. (500-1200° F.), in the presence of sufficient air flow, for 0.1-10 hours;   the extrudate is impregnated with a modifier by contacting the extrudate with the metal impregnation solution containing at least one modifier for 0.1-10 hrs at a temperature in the range of about 20 to 80° C.; and   the metal loaded extrudate is dried at about 90-150° C. for 0.1-10 hrs and calcined at 260-649° C. (500-1200° F.), in the presence of sufficient air flow, for 0.1-10 hours.