Two stage hydrocracking process and apparatus for multiple grade lube oil base feedstock production

Patent metadata

Field	Value
Publication number	US-9388347-B2
Application number	US-201414215220-A
Country	US
Kind code	B2
Filing date	Mar 17, 2014
Priority date	Mar 15, 2013
Publication date	Jul 12, 2016
Grant date	Jul 12, 2016

Abstract

Multiple grades of lube oil base feedstock are produced within a two-stage hydrocracking unit. Effluent from a first hydrocracking zone is sent to a separation zone, which includes multiple separation vessels, and a heavy liquid stream enters one cell of a dual cell fractionator charge heater and is flashed in the distillation zone of a divided wall fractionation column. A portion of the bottom stream from one side of the divided wall column is sent to the second hydrocracking zone. Feed to a second cell of the dual cell fractionation column is derived from the effluent of this second hydrocracking zone. A different lube oil base feedstocks is derived from each of the cells of the dual cell fractionation column.

First claim

The invention claimed is:

1. A method for producing multiple grades of lube oil feedstock comprising:
charging a feedstock and hydrogen to a first hydrocracking zone to produce a first hydrocracking zone effluent that is separated into a hydrogen recycle stream and a first intermediate product effluent;
heating at least a portion of the first intermediate product effluent in a first cell of a multiple cell fractionator charge heater;
passing the heated first intermediate product effluent to a first flash zone of a divided wall fractionation column to produce a first flash zone bottom stream;
recovering a portion of the first flash zone bottom stream as a first type of lube oil feedstock;
passing a second portion of the first flash zone bottom stream to a second hydrocracking zone to produce a second hydrocracking zone effluent that is separated into a hydrogen recycle stream and a second intermediate product effluent;
heating at least a portion of the second intermediate product effluent in a second cell of a multiple cell fractionator charge heater;
passing the heated second intermediate product effluent to a second flash zone of a divided wall fractionation column to produce a second flash zone bottom stream;
recovering a portion of the second flash zone bottom stream as a second type of lube oil feedstock; and
recovering one or more distillate product streams from overhead and/or side cuts of the fractionation column.

2. The method as in claim 1 , wherein the feedstock is subjected to hydrotreating, and the feedstock to the first hydrocracking zone is hydrotreated feedstock.

3. The method as in claim 1 , wherein the first hydrocracking zone includes a hydrocracking reactor having a single catalyst bed.

4. The method as in claim 1 , wherein the first hydrocracking zone includes a hydrocracking reactor having multiple catalyst beds.

5. The method as in claim 4 , wherein a quench hydrogen stream is introduced between catalyst beds.

6. The method as in claim 1 , wherein the second hydrocracking zone includes a hydrocracking reactor having a single catalyst bed.

7. The method as in claim 1 , wherein the second hydrocracking zone includes a hydrocracking reactor having multiple catalyst beds.

8. The method as in claim 7 , wherein a quench hydrogen stream is introduced between catalyst beds.

9. The method as in claim 1 , wherein a second portion of the second flash zone bottoms stream is recycled to the second hydrocracking zone.

10. The method as in claim 1 , further wherein
the first intermediate product effluent is passed through a stripper column,
discharging a vapor stream from the stripper column, and
passing a bottoms stream to the first cell of the multiple cell fractionator charge heater.

11. The method as in claim 1 , wherein the divided wall fractionation column comprises a vertical division wall placed in a stripping zone of a fractionation column that extends up to three trays above the flash zone.

12. The method as in claim 1 , wherein the feedstock is selected from the group consisting of heavy vacuum gas oil, heavy gas oil and de-asphalted oil.

13. The method as in claim 12 , wherein the feedstock is characterized by boiling points in the range of from 170° C. to 700° C.

14. The method as in claim 13 , wherein the first type of lube oil feedstock recovered from the first flash zone bottom stream comprises Group II lube oil based feedstock, and the second type of lube oil feedstock recovered from the second flash zone bottom stream comprises Group III lube oil based feedstock.

15. The method as in claim 1 , further wherein
the first intermediate product effluent is passed through a high-pressure separator,
discharging a vapor stream from the high-pressure separator,
passing a liquid stream from the high-pressure separator to a low-pressure separator;
discharging a vapor stream from the low-pressure separator, and
passing a liquid stream from the low-pressure separator to the second cell of the multiple cell fractionator charge heater.

Assignees

• Saudi Arabian Oil Co

Inventors

• Ramaseshan Vinod
• Al-Abdul Al Ali H

Classifications

• C10G2400/10

  Lubricating oil · CPC title

• B01D3/141

  where at least one distillation column contains at least one dividing wall · CPC title

• C10G65/10 Primary

  including only cracking steps · CPC title

• C10G65/12

  including cracking steps and other hydrotreatment steps · CPC title