High activity and high distillate yield hydrocracking catalysts with intimate interaction between unsupported metal oxide and zeolite

Patent metadata

Field	Value
Publication number	US-2022023846-A1
Application number	US-202117380667-A
Country	US
Kind code	A1
Filing date	Jul 20, 2021
Priority date	Jul 27, 2020
Publication date	Jan 27, 2022
Grant date	—

Abstract

A hydroprocessing catalyst with improved performance has been produced that involves an intimately mixed unsupported metal oxide with a zeolite or other acid function. The intimate mixing allows an intimate interaction between the unsupported metal oxide and the acid function. The hydroprocessing catalyst may be used alone or may be incorporated with a portion of a conventional hydrocracking catalyst.

First claim

1 . A catalyst comprising an acid function and a metal function wherein said acid function and said metal function are less than 300 um apart wherein said acid function and said metal function are intimately mixed prior to catalyst forming.

2 . The catalyst of claim 1 wherein said acid function and said metal function are between about ≤1 to 180 um apart.

3 . The catalyst of claim 1 comprising 0 (binderless) to 30 wt % binder.

4 . The catalyst of claim 1 wherein said metal function comprises a Group JIB, a Group VIII, a Group VIB metal or a mixture thereof.

5 . The catalyst of claim 1 wherein said acid function is contributed by a zeolite, a non-zeolite molecular sieve or an amorphous silica alumina in a concentration range from about 0.5 to 35 wt %.

6 . The catalyst of claim 5 wherein said zeolite is a Y zeolite, a beta zeolite, a modified zeolite, or mixtures thereof.

7 . A process comprising introducing a feedstock to a hydroprocessing reaction zone at hydroprocessing reaction conditions in the presence of a hydroprocessing catalyst, wherein said hydroprocessing catalyst is consisting of a metal selected from Group VIII metals, Group VIB metals, and Group JIB metals or mixtures thereof and an acid function wherein said metal and said acid function are intimately mixed, to produce a hydroprocessed product.

8 . The process of claim 7 wherein the hydroprocessed feedstock is selected from vacuum gas oil, kerosene, jet fuel, distillate, light cycle oil, naphtha, deasphalted oil, atmospheric gas oil, coker gas oil and mixtures thereof.

9 . The process of claim 7 wherein said hydroprocessing catalyst further comprises an additional refractory oxide.

10 . The process of claim 7 wherein said acid function is provided by a zeolite, a non-zeolite molecular sieve, an amorphous silica alumina or mixtures thereof in concentrations from about 0.5 to 35 wt % of said hydroprocessing catalyst.

11 . The process of claim 10 wherein said zeolite is selected from a Y zeolite, a beta zeolite, a modified zeolite, or mixtures thereof.

12 . The process of claim 7 wherein said Group VIII metal ranges from about 2 to 25 wt % of said hydroprocessing catalyst and said Group VIB metal ranges from about 5 to 55 wt % of said hydroprocessing catalyst.

13 . The process of claim 7 wherein said hydroprocessing catalyst comprises a layer within said hydroprocessing reaction zone which further comprises a second layer comprising a second hydroprocessing catalyst that is different from said hydroprocessing catalyst.

14 . The process of claim 13 wherein said hydroprocessing catalyst comprises about 5-100% of a total volume of catalyst in said hydroprocessing reaction zone.

15 . A method of preparing a catalyst composition comprising intimately mixing an unsupported metal oxide with an acid function.

16 . The method of claim 15 wherein said unsupported metal oxide comprises Group VIII metals, and Group VIB metals, from 0-5 wt % Group IIB metals and said acid function comprises a zeolite, a non-zeolite molecular sieve, an amorphous silica alumina or mixtures thereof.

17 . The method of claim 16 wherein said zeolite is a Y zeolite, a Beta zeolite, a modified zeolite, or combinations thereof.

18 . The method of claim 16 wherein when a zeolite is used for the acid function, less than 4% of metal is incorporated in the zeolite.

19 . The method of claim 15 wherein said intimate mixing comprises co-mulling.

20 . The method of claim 16 wherein said zeolite is first heat treated at less than about 650° C. prior to being added to said unsupported metal oxide.

Assignees

• Uop Llc

Inventors

• Bogdan Paula
• Schaal Melanie Timmons
• Martins Susie C
• Knight Lisa
• Sinkler Wharton
• Kuzmanich Gregory
• Bricker Maureen
• Abdo Suheil F
• Miller Stuart
• Pan Wei
• Willis Richard R

Classifications

• B01J29/084 Primary

  Y-type faujasite · CPC title

• B01J37/04

  Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• C10G47/16

  Crystalline alumino-silicate carriers · CPC title

• B01J29/7007 Primary

  Zeolite Beta · CPC title

• B01J29/80

  Mixtures of different zeolites · CPC title