Process for producing diesel fuel

Patent metadata

Field	Value
Publication number	US-9783748-B2
Application number	US-201414481461-A
Country	US
Kind code	B2
Filing date	Sep 9, 2014
Priority date	Sep 9, 2014
Publication date	Oct 10, 2017
Grant date	Oct 10, 2017

Abstract

One exemplary embodiment can be a process for producing a diesel fuel. The process can include providing a hydrocarbon feed to a residue processing unit. Generally, the residue processing unit includes a solvent deasphalting zone, a hydroprocessing zone, and a hydroprocessing fractionation zone. The process can further include recycling at least a portion of an unconverted oil stream from the hydroprocessing fractionation zone, and sending one part of the at least a portion of the recycled unconverted oil stream to the unconverted oil fractionation zone providing a light unconverted oil stream downstream of the solvent deasphalting zone and a heavy unconverted oil stream to the solvent deasphalting zone.

First claim

The invention claimed is:

1. A process for producing a diesel fuel, comprising:
A) providing a hydrocarbon feed to a residue processing unit, wherein the residue processing unit comprises:
1) a solvent deasphalting zone;
2) a hydroprocessing zone; and
3) a hydroprocessing fractionation zone;

B) recycling at least a portion of an unconverted oil stream from the hydroprocessing fractionation zone as a recycled unconverted oil stream; and
C) sending one part of the at least a portion of the recycled unconverted oil stream to an unconverted oil fractionation zone operating at a cut point providing a light unconverted oil stream downstream of the solvent deasphalting zone and a heavy unconverted oil stream to the solvent deasphalting zone.

2. The process according to claim 1 , further comprising purging another part of the at least a portion of the unconverted oil stream prior to the solvent deasphalting zone.

3. The process according to claim 1 , further comprising sending yet another part of the at least a portion of the unconverted oil stream to an adsorption zone.

4. The process according to claim 3 , wherein the adsorption zone provides an effluent upstream of the hydroprocessing zone.

5. The process according to claim 1 , wherein some of the light unconverted oil stream is sent to the solvent deasphalting zone and some of the heavy unconverted oil stream is purged.

6. The process according to claim 5 , wherein at least about 90%, by weight, of the light unconverted oil stream is sent downstream of the solvent deasphalting zone and no more than about 5%, by weight, of the heavy unconverted oil stream is purged.

7. The process according to claim 1 , wherein substantially all of the unconverted oil stream is recycled to the solvent deasphalting zone.

8. The process according to claim 1 , wherein the hydroprocessing zone comprises a hydrocracking zone.

9. The process according to claim 8 , further comprising providing a hydrocarbon feed to the hydrocracking zone.

10. The process according to claim 9 , wherein the hydrocarbon feed comprises a vacuum gas oil.

11. A process for producing a diesel fuel, comprising:
A) providing a hydrocarbon feed to a residue processing unit, wherein the residue processing unit comprises:
1) a solvent deasphalting zone;
2) a hydroprocessing zone; and
3) a hydroprocessing fractionation zone;

B) recycling at least a portion of an unconverted oil stream from the hydroprocessing fractionation zone;
C) sending one part of the at least a portion of the recycled unconverted oil stream to an unconverted oil fractionation zone providing a light unconverted oil stream downstream of the solvent deasphalting zone and a heavy unconverted oil stream to the solvent deasphalting zone, and
D) sending yet another part of the at least a portion of the unconverted oil stream to an adsorption zone.

12. The process according to claim 11 , further comprising purging another part of the at least a portion of the unconverted oil stream prior to the solvent deasphalting zone.

13. The process according to claim 11 , wherein the adsorption zone provides an effluent upstream of the hydroprocessing zone.

14. The process according to claim 11 , wherein some of the light unconverted oil stream is sent to the solvent deasphalting zone and some of the heavy unconverted oil stream is purged.

15. The process according to claim 14 , wherein at least about 90%, by weight, of the light unconverted oil stream is sent downstream of the solvent deasphalting zone and no more than about 5%, by weight, of the heavy unconverted oil stream is purged.

16. The process according to claim 11 , wherein the hydroprocessing zone comprises a hydrocracking zone.

17. The process according to claim 16 , further comprising providing a hydrocarbon feed to the hydrocracking zone.

18. The process according to claim 17 , wherein the hydrocarbon feed comprises a vacuum gas oil.

19. A process for producing a diesel fuel, comprising:
A) providing a hydrocarbon feed to a residue processing unit, wherein the residue processing unit comprises:
1) a solvent deasphalting zone;
2) a hydroprocessing zone; and
3) a hydroprocessing fractionation zone;

B) recycling at least a portion of an unconverted oil stream from the hydroprocessing fractionation zone; and
C) sending one part of the at least a portion of the recycled unconverted oil stream to an unconverted oil fractionation zone providing a light unconverted oil stream downstream of the solvent deasphalting zone and a heavy unconverted oil stream to the solvent deasphalting zone, wherein some of the light unconverted oil stream is sent to the solvent deasphalting zone and some of the heavy unconverted oil stream is purged.

20. The process according to claim 19 , wherein at least about 90%, by weight, of the light unconverted oil stream is sent downstream of the solvent deasphalting zone and no more than about 5%, by weight, of the heavy unconverted oil stream is purged.

Assignees

• Uop Llc

Inventors

• Harvey Craig
• Wang Haiyan
• Thomas B Daniel
• Ganyu Brian
• Govindhakannan Jagannathan

Classifications

• C10G67/14

  including at least two different refining steps in the absence of hydrogen · CPC title

• C10G67/049 Primary

  The hydrotreatment being a hydrocracking · CPC title

• C10G2400/04

  Diesel oil · CPC title

• C10G67/0454

  Solvent desasphalting · CPC title

• C10L1/026

  for compression ignition · CPC title