IP Library Granted Patent US 9,713,807
Granted Patent B2
US 9,713,807 · App. 14/388,945 · Granted Jul 25, 2017

Method for producing hydroisomerization catalyst and method for producing lubricant base oil

Inventors: Yoshiyuki Nagayasu (Tokyo, JP); Kazuaki Hayasaka (Tokyo, JP); Marie Iwama (Tokyo, JP)
Assignee: JX NIPPON OIL & ENERGY CORPORATION
B01J29/7484B01J29/076B01J29/703B01J29/74B01J29/7461B01J29/78B01J29/7861B01J29/7884B01J29/7892C07C5/2791C10G45/62C10G45/64B01J2229/186
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Quick Facts
Patent No.
US 9,713,807
App. No.
14/388,945
Granted
Jul 25, 2017
Kind
B2
Abstract

A method for producing a hydroisomerization catalyst according to the present invention includes: a first step of preparing a catalyst to be treated, which contains a support having a one-dimensional porous structure including a 10-membered ring and at least one metal selected from the group consisting of: group 8 to 10 metals of the periodic table, Mo, and W supported on the hydroisomerization catalyst; and a second step of producing a hydroisomerization catalyst having a carbon content of 0.4 to 2.5% by mass by subjecting the catalyst to be treated to a coking treatment by means of a carbon-containing compound.

Claims (12)

1. A method for producing lubricant base oil, wherein the method comprises:

subjecting a catalyst to a coking treatment with a carbon containing compound, the coking treatment being at a temperature of 300° C. to 350° C. to obtain a hydroisomerization catalyst having a carbon content of 0.4% to 2.5% by mass, wherein the catalyst comprises a support having a one-dimensional porous structure including a 10-membered ring and at least one metal selected from the group consisting of group 8 to 10 metals of the periodic table, Mo, and W, supported on the catalyst; and

contacting a hydrocarbon feedstock containing normal paraffins having 10 or more carbon atoms with the hydroisomerization catalyst in the presence of hydrogen at a hydroisomerization temperature of 370° C. to 450° C.

2. The method for producing lubricant base oil according to claim 1 , wherein the catalyst is subjected to a coking treatment by using the hydrocarbon feedstock as the carbon-containing compound.

3. The method for producing lubricant base oil according to claim 1 , wherein the hydrocarbon feedstock is further hydrofinished and vacuum-distilled after the hydrocarbon feedstock is contacted with the hydroisomerization catalyst.

4. The method for producing lubricant base oil according to claim 1 , wherein the hydrocarbon feedstock is at least one selected from the group consisting of: atmospheric residues; vacuum residues; a vacuum gas oil; a slack wax; and a Fischer Tropsch synthetic wax.

5. The method for producing lubricant base oil according to claim 1 , wherein the hydrocarbon feedstock includes a fraction with a boiling point at atmospheric pressure of more than 360° C.

6. The method for producing lubricant base oil according to claim 1 , wherein the hydroisomerization catalyst has a volume of micropores per unit mass of the catalyst of 0.02 to 0.11 cc/g and a volume of micropores per unit mass of a zeolite contained in the catalyst of 0.04 to 0.12 cc/g.

7. The method for producing lubricant base oil according to claim 1 , wherein the hydroisomerization catalyst comprises at least one zeolite selected from the group consisting of: a ZSM-22 zeolite; a ZSM-23 zeolite; an SSZ-32 zeolite; and a ZSM-48 zeolite.

8. A method for producing lubricant base oil, wherein the method comprises:

subjecting a catalyst to a coking treatment with a carbon containing compound, the coking treatment being at a temperature of 300° C. to 350° C. to obtain a hydroisomerization catalyst having a carbon content of 0.4% to 2.5% by mass, wherein the catalyst comprises a support having a one-dimensional porous structure including a 10-membered ring and at least one metal selected from the group consisting of group 8 to 10 metals of the periodic table, Mo, and W, supported on the catalyst; and

contacting a hydrocarbon feedstock containing normal paraffins having 10 or more carbon atoms with the hydroisomerization catalyst in the presence of hydrogen at a hydroisomerization temperature of 370° C. to 450° C., wherein the hydrocarbon feedstock includes a fraction with a boiling point at atmospheric pressure of more than 360° C.

Assignments (3)
CHANGE OF NAME Recorded Aug 25, 2020
From: JXTG NIPPON OIL ENERGY CORPORATION
To: ENEOS CORPORATION
Reel/Frame 053596/0282 →
CHANGE OF NAME Recorded Jun 15, 2018
From: JX NIPPON OIL & ENERGY CORPORATION
To: JXTG NIPPON OIL & ENERGY CORPORATION
Reel/Frame 046634/0132 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 5, 2014
From: NAGAYASU, YOSHIYUKI; HAYASAKA, KAZUAKI; IWAMA, MARIE
To: JX NIPPON OIL & ENERGY CORPORATION
Reel/Frame 034391/0911 →
Priority Claims (1)
JP 2012-082501 · Mar 30, 2012 · national
Continuity (1)
Related Publication 20150051432A1 · Feb 19, 2015