Two-stage hydrocracking process for making heavy lubricating base oil from a heavy coker gas oil blended feedstock

Patent metadata

Field	Value
Publication number	US-9914887-B2
Application number	US-201414483331-A
Country	US
Kind code	B2
Filing date	Sep 11, 2014
Priority date	Sep 12, 2013
Publication date	Mar 13, 2018
Grant date	Mar 13, 2018

Abstract

The present invention is directed to a refining process for producing heavy lubricating base oils (LBO) from a blended hydrocarbonaceous feedstock containing a heavy coker gas oil, a visbroken gas oil, heavy cycle oil, oils from residue hydrocracking, aromatic extract or any other feedstock normally not conducive to lube oil basestock production, using a two-stage hydrocracking process.

First claim

What is claimed is:

1. A process for producing a heavy lubricating base oil, comprising:
hydrocracking a heavy coker gas oil-containing feedstock in a first-stage hydrocracker to produce a hydrocracked heavy coker gas oil-containing feedstock;
distilling the hydrocracked heavy coker gas oil-containing feedstock to form at least one middle distillate fraction and a distillation bottoms fraction;
further distilling the distillation bottoms fraction to form at least one light vacuum gas oil fraction and at least one heavy lubricating base oil feedstock fraction; and
hydrocracking the fraction consisting of the at least one light vacuum gas oil fraction in a second-stage hydrocracker to form a hydrocracked light vacuum gas oil fraction;
wherein the process produces a heavy lubricating base oil product.

2. The process of claim 1 , further comprising the step of combining the hydrocracked light vacuum gas oil fraction with the hydrocracked heavy coker gas oil-containing feedstock.

3. The process of claim 1 , further comprising the step of dewaxing the at least one heavy lubricating base oil feedstock fraction to form at least one dewaxed heavy lubricating base oil feedstock fraction.

4. The process of claim 3 , further comprising the step of distilling the at least one dewaxed heavy lubricating base oil feedstock fraction into at least one finished heavy lubricating base oil product.

5. The process of claim 3 , wherein the first-stage hydrocracker is operated to produce lubricating base oil fractions from the further distillation of the distillation bottoms fraction.

6. The process of claim 1 , wherein the step of further distilling the distillation bottoms fraction comprises forming at least one light vacuum gas oil fraction and a single heavy lubricating base oil fraction.

7. The process of claim 6 , wherein the single heavy lubricating base oil fraction has a boiling range of greater than 500° C.

8. The process of claim 6 , further comprising the step of dewaxing the single heavy lubricating base oil feedstock fraction to form a dewaxed heavy lubricating base oil feedstock fraction.

9. The process of claim 6 , further comprising the step of distilling the dewaxed heavy lubricating base oil feedstock fraction into a finished heavy lubricating base oil product.

10. The process of claim 9 , wherein the finished heavy lubricating base oil product is a 15 to 17 cSt 750N product.

11. The process of claim 1 , wherein the step of further distilling the distillation bottoms fraction to form at least one light vacuum gas oil fraction and at least one heavy lubricating base oil feedstock fraction, is performed using a distillation column.

12. The process of claim 1 , wherein the at least one light vacuum gas oil fraction has a boiling range of 370 to 500° C.

13. The process of claim 1 , wherein the step of further distilling the distillation bottoms fraction comprises forming at least one light vacuum gas oil fraction, a 500 to 570° C. heavy lubricating base oil fraction, and a greater than 570° C. heavy lubricating base oil fraction.

14. The process of claim 1 , wherein the heavy coker gas oil-containing feedstock contains greater than 3,000 ppm nitrogen, greater than 3 wt. % sulfur, and an API gravity of less than 17.

15. The process of claim 2 , further comprising dewaxing the at least one heavy lubricating base oil feedstock fraction to form at least one dewaxed heavy lubricating base oil feedstock fraction.

16. The process of claim 15 , further comprising distilling the at least one dewaxed heavy lubricating base oil feedstock fraction into at least one finished heavy lubricating base oil product.

17. The process of claim 15 , wherein the first-stage hydrocracker is operated to produce lubricating base oil fractions from the further distillation of the distillation bottoms fraction.

18. The process of claim 1 , wherein the heavy lubricating base oil produced is a 600N product, a 750N product, or a 22-32 cSt Group II brightstock product.

Assignees

• Bhattacharya Subhasis
• Chevron Usa Inc

Inventors

• Bhattacharya Subhasis

Classifications

• C10M177/00

  Special methods of preparation of lubricating compositions; Chemical modification by after-treatment of components or of the whole of a lubricating composition, not covered by other classes · CPC title

• C10M2203/1006

  used as base material · CPC title

• C10G69/06

  including at least one step of thermal cracking in the absence of hydrogen · CPC title

• C10G65/10 Primary

  including only cracking steps · CPC title

• C10G7/003

  distillation of lubricating oils · CPC title