US2016244680A1PendingUtilityA1

Method for optimizing catalyst loading for hydrocracking process

Assignee: SAUDI ARABIAN OIL COPriority: Jan 8, 2013Filed: May 3, 2016Published: Aug 25, 2016
Est. expiryJan 8, 2033(~6.5 yrs left)· nominal 20-yr term from priority
C10G 65/12B01J 23/883B01J 29/166B01J 23/882C10G 2300/1074C10G 2300/202C10G 45/12C10G 45/04C10G 45/44C10G 49/04C10G 49/06C10G 45/06C10G 49/002B01J 29/084C10G 45/10C10G 49/08C10G 47/02C10G 45/32C10G 49/02B01J 35/19
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Claims

Abstract

The invention relates to a method for optimizing layered catalytic processes. This is accomplished by testing various catalysts with a compound found in a feedstock to be tested, to determine the facility of the catalyst in hydrogenating, hydrosulfurizing, or hydrodenitrogenating the molecule, and hence the feedstock. in a preferred embodiment, the Double Bond Equivalence of the feedstock and molecule are determined, and catalysts are pre-selected based upon their known ability to work with materials of this DBE value.

Claims

exact text as granted — not AI-modified
1 . A method for optimizing a layered hydrocracking catalytic process, comprising (i) contacting a model compound capable of (a) being hydrocracked as well as at least one of (ii) hydrogenation, hydrosulfurization and hydrodenitrogenation to a plurality of catalysts to determine an optimal catalyst for each of (i) and (ii), (b) followed by layering the optimal catalysts for each of (i) and (ii) in a reaction chamber based on their activity reacting with said model compound, and (c) contacting a feedstock to the layered catalysts under condition favoring formation of lower weight hydrocarbon from said hydrocarbon containing feedstock, wherein said model compound boils in the range of 180° C.-520° C. and is selected from the group consisting of methylnaphthalene, dibenzothiophene, an alkylated or naphthalated derivative thereof, a basic nitrogen compound and a carbazole molecule. 
     
     
         2 . (canceled) 
     
     
         3 . (canceled) 
     
     
         4 . The method of  claim 1 , further comprising determining double bond equivalence (DBE) of said feedstock, and contacting said model compound to a plurality of catalysts suitable for hydrocracking a substance with a DBE of said feedstock, to determine an optimum hydrocracking catalyst for said feedstock. 
     
     
         5 . The method of  claim 4 , further comprising contacting said model compound to a second plurality of catalysts suitable for hydrogenating, hydrodesulfurizing, or hydrodenitrogenating a substance with a DBE value less than said feedstock to determine an optimal, second catalyst. 
     
     
         6 . The method of  claim 4 , wherein said hydrocarbons contained in said feedstock have a double bond equivalency of 24 or less. 
     
     
         7 . The method of  claim 4 , wherein said feedstock has a double bond equivalency of 24 or less, and at least one of said catalysts for VGO hydrocracking catalyst. 
     
     
         8 . The method of  claim 4 , wherein said feedstock has a double bond equivalency of 25 or more, and at least one of said catalysts is a catalyst designed for heavy feedstock. 
     
     
         9 . The method of  claim 1 , comprising contacting said hydrocarbon containing feedstock to said reaction chamber at a temperature of from 350° C. to 450° C. 
     
     
         10 . The method of  claim 1 , comprising contacting said hydrocarbon containing feedstock to said reaction chamber at a hydrogen feed rate less than 2500 liters per liter of feedstock. 
     
     
         11 . The method of  claim 1 , comprising contacting said hydrocarbon containing feedstock to said reaction vessel at a pressure of from 100 bars to 200 bars. 
     
     
         12 . The method of  claim 1 , wherein at least one of said catalysts contains a metal from Group VI, VII or VIIIB of the periodic table, or is a noble metal. 
     
     
         13 . The method of  claim 12 , wherein said metal is Co, Ni, W, Mo, Pt, or Pd. 
     
     
         14 . The method of  claim 1 , wherein at least one of said catalysts contains amorphous alumina, silica-alumina, titanium, Y zeolite, or at least one a transition metal inserted Y zeolite. 
     
     
         15 . The method of  claim 14 , wherein said transition metal is Zr, Ti, Hf and combination thereof. 
     
     
         16 . The method of  claim 1 , wherein said molecule is capable of being at least two of hydrogenated, hydrodesulfurized, and hydrodenitrogenated. 
     
     
         17 . The method of  claim 1 , wherein said molecule is capable of being hydrogenated, hydrodesulfurized, and hydrodenitrogenated.

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