Processes and systems for separating carbon dioxide in the production of alkanes

Patent metadata

Field	Value
Publication number	US-11377403-B2
Application number	US-201816607780-A
Country	US
Kind code	B2
Filing date	Apr 25, 2018
Priority date	Apr 28, 2017
Publication date	Jul 5, 2022
Grant date	Jul 5, 2022

Abstract

A method for separating CO2 from C2 to C5 alkanes includes introducing a first stream including C2 to C5 alkanes and CO2 into a first separation zone, the first separation zone including a hydrocarbon solvent, and separating the first stream into a recycle stream and a second stream in the first separation zone. The recycle stream including CO2 and one or more of CO, H2, and CH4, and the second stream including C2 to C5 alkanes. The method further includes introducing the second stream into a second separation zone, and separating the second stream into a third stream and a fourth stream, wherein the third stream includes C2 alkanes and the fourth stream includes C3 to C5 alkanes.

First claim

The invention claimed is:

1. A method for separating CO 2 from C 2 to C 5 alkanes, comprising:
introducing a first stream comprising C 2 to C 5 alkanes and CO 2 into a first separation zone, the first separation zone comprising a hydrocarbon solvent;
separating the first stream into a recycle stream and a second stream in the first separation zone, wherein the recycle stream comprises CO 2 and one or more of CO, H 2 , and CH 4 , and the second stream comprises C 2 to C 5 alkanes;
introducing the recycle stream into a reaction zone;
introducing the second stream into a second separation zone; and
separating the second stream into a third stream and a fourth stream, wherein the third stream comprises C 2 alkanes and the fourth stream comprises C 3 to C 5 alkanes.

2. The method of claim 1 , wherein the method further comprises introducing at least a portion of the fourth stream into the first separation zone as the hydrocarbon solvent.

3. The method of claim 1 , wherein a portion of the recycle stream is purged before the recycle stream is introduced into the reaction zone.

4. The method of claim 1 , wherein a ratio of the hydrocarbon solvent to C 2 to C 5 alkanes in the first separation zone is from 1:1 to 5:1.

5. The method of claim 1 , wherein the first stream is a feed stream that is introduced from a reaction zone into the first separation zone.

6. The method of claim 1 , wherein the third stream further comprises CO 2 , and the method further comprises introducing the third stream to a CO 2 separator where a purge amount of CO 2 separated from the third stream.

7. The method of claim 1 , wherein the method further comprises removing a purge amount of CO 2 from the first stream before it is introduced into the first separation zone.

8. The method of claim 6 , wherein removing the purge amount of CO 2 comprises introducing a stream comprising CO 2 into a CO 2 separator that comprises an amine solvent, and isolating the purge amount of CO 2 in the amine solvent.

9. The method of claim 8 , wherein the method further comprises:
introducing the amine solvent and the purge amount of CO 2 into a CO 2 stripper that strips the purge amount CO 2 from the amine solvent thereby forming a stripped amine solvent, and
introducing the stripped amine solvent into the CO 2 separator.

10. The method of claim 1 , wherein the fourth stream comprises C 3 alkanes and C 4 to C 5 alkanes.

11. The method of claim 1 , wherein the recycle stream comprises CH 4 .

Assignees

• Dow Global Technologies Llc

Inventors

• Fish Barry Brent
• Groenendijk Peter E
• Malek Andrzej
• Nieskens Davy L S
• Stears Brien A

Classifications

• B01D53/1418

  Recovery of products · CPC title

• C07C7/08 Primary

  by extractive distillation · CPC title

• B01D3/14

  Fractional distillation {or use of a fractionation or rectification column} · CPC title

• B01D53/1475

  Removing carbon dioxide · CPC title

• B01D3/146

  Multiple effect distillation · CPC title