IP Library Granted Patent US 8,480,880
Granted Patent B2
US 8,480,880 · App. 13/008,153 · Granted Jul 9, 2013

Process for making high viscosity index lubricating base oils

Inventor: Stephen J. Miller (San Francisco, CA)
Assignee: Chevron U.S.A. Inc.
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Quick Facts
Patent No.
US 8,480,880
App. No.
13/008,153
Granted
Jul 9, 2013
Kind
B2
Abstract

A process for making a lubricating base oil having a viscosity index of at least 110, comprising the steps of: combining a waxy light neutral base oil and a wax derived from pyrolyzing a plastics feed comprising polyethylene to form a blend; hydroisomerization dewaxing the blend; and recovering the lubricating base oil from an effluent from the hydroisomerization dewaxing step.

Claims (20)

1. A process for making a lubricating base oil having a viscosity index of at least 110, comprising the steps of:

a) combining a waxy light neutral base oil and a wax derived from pyrolyzing a plastics feed comprising polyethylene to form a blend;

b) hydroisomerization dewaxing the blend; and

c) recovering the lubricating base oil from an effluent from the hydroisomerization dewaxing step.

2. The process of claim 1 , wherein the plastics feed comprises at least 95 wt. % polyethylene.

3. The process of claim 1 , wherein the polyethylene is selected from the group consisting of waste polyethylene, virgin polyethylene, and mixtures thereof.

4. The process of claim 1 , wherein the polyethylene is selected from the group consisting of high-density polyethylene, low-density polyethylene, and mixtures thereof.

5. The process of claim 1 , wherein less than 10 wt. % of the wax derived from pyrolyzing a plastics feed boils above 1000° F. (538° C.).

6. The process of claim 1 , wherein less than 5 wt. % of the wax derived from pyrolyzing a plastics feed boils above 1000° F. (538° C.).

7. The process of claim 1 , wherein the blend comprises at least 20 wt. % of the wax derived from pyrolyzing a plastics feed.

8. The process of claim 1 , wherein the blend comprises at least 50 wt. % of the wax derived from pyrolyzing a plastics feed.

9. The process of claim 1 , wherein the hydroisomerization dewaxing is performed using a shape selective intermediate pore size molecular sieve.

10. The process of claim 9 , wherein the molecular sieve is selected from the group consisting of SAPO-11, SAPO-31, SAPO-41, SM-3, SM-7, ZSM-22, ZSM-23, ZSM-35, ZSM-48, ZSM-57, SSZ-32, SSZ-32X, metal modified SSZ-32x, offretite, ferrierite, and combinations thereof.

11. The process of claim 1 , wherein the lubricating base oil is a Group II plus base oil.

12. The process of claim 1 , wherein the lubricating base oil is a Group III base oil.

13. The process of claim 1 , wherein the lubricating base oil has a viscosity index of at least 130.

14. The process of claim 1 , wherein the lubricating base oil has a viscosity index of at least 140.

15. The process of claim 1 , wherein the lubricating base oil has a pour point of less than −10° C.

16. The process of claim 1 , wherein the lubricating base oil has a pour point of less than −20° C.

17. The process of claim 1 , wherein the lubricating base oil has a cloud point of less than 0° C.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 18, 2011
From: MILLER, STEPHEN J.
To: CHEVRON U.S.A. INC.
Reel/Frame 025652/0170 →
Continuity (1)
Related Publication 20120184787A1 · Jul 19, 2012