Method for purification of a hydrocarbon stream containing olefin and amine

Patent metadata

Field	Value
Publication number	US-9284238-B2
Application number	US-201113988776-A
Country	US
Kind code	B2
Filing date	Sep 27, 2011
Priority date	Nov 23, 2010
Publication date	Mar 15, 2016
Grant date	Mar 15, 2016

Abstract

The present invention relates to a method for purification of a hydrocarbon stream containing linear alpha olefins, isomers thereof and at least one organic amine, the linear alpha olefins, isomers and the amine having boiling points under atmospheric pressure which differ by at most 5° C., comprising the step of removing a major amount of the organic amine from the hydrocarbon stream by distillation, wherein the distillation is carried out to that, together with the amine, between 5% and 95 wt % of the isomers, based on the total amount of the isomers in the hydrocarbon stream, are removed from the hydrocarbon stream in an amine/isomer-rich fraction.

First claim

The invention claimed is:

1. A method for purification of a hydrocarbon stream containing linear alpha olefins, isomers thereof and at least one organic amine, comprising:
removing a major amount of the organic amine from the hydrocarbon stream by distillation;
wherein the distillation is carried out so that, together with the amine, between 5% and 95 wt % of the isomers, based on the total amount of the isomers in the hydrocarbon stream, are removed from the hydrocarbon stream in an amine/isomer-rich fraction of the distillation; and
wherein the linear alpha olefins, isomers and the amine have boiling points under atmospheric pressure which differ by at most 5° C.

2. The method according to claim 1 , wherein the boiling points under atmospheric pressure of the linear alpha olefins, isomers thereof and the organic amine differ by at most 3° C.

3. The method according to claim 1 , wherein the distillation is carried out under atmospheric pressure.

4. The method of claim 1 , wherein a distillation column is utilized for removing the major amount of the organic amine.

5. The method of claim 1 , wherein the hydrocarbon stream contains as a major constituent linear C 10 alpha olefins and its isomers and/or linear C 14 alpha olefins and its isomers.

6. The method of claim 1 , wherein the amine/isomer-rich fraction is further separated by removing the organic amine contained therein by converting with an acid, forming an amine salt, and extracting the amine-salt formed into an aqueous phase.

7. The method of claim 6 , wherein further separation of the organic amine is in a batch or continuous operation.

8. The method of claim 1 , wherein the amine/isomer-rich fraction is recycled to a reaction section of an oligomerization plant without prior separation.

9. The method of claim 6 , further comprising isolating the organic amine.

10. The method of claim 9 , wherein the isolated organic amine is recycled to a reaction section of an oligomerization plant.

11. The method of claim 2 , wherein the boiling points differ by 0.5° C. to 3° C.

12. The method according to claim 2 , wherein the distillation is carried out under atmospheric pressure.

13. The method of claim 4 , wherein the distillation column has 50 to 100 theoretical trays.

14. The method of claim 1 , wherein the amine is n-dodecyl amine.

15. The method of claim 1 , wherein the amine is 2-ethyl-hexyl-amine.

16. The method of claim 1 , wherein the purity of the linear alpha olefin after distillation is increased by greater than or equal to 5%.

17. A method for purification of a hydrocarbon stream containing linear alpha olefins, isomers thereof and at least one organic amine, comprising:
removing a major amount of the organic amine from the hydrocarbon stream by distillation, wherein the distillation is carried out so that, together with the amine, between 5% and 95 wt % of the isomers, based on the total amount of the isomers in the hydrocarbon stream, are removed from the hydrocarbon stream in an amine/isomer-rich fraction of the distillation;
removing the organic amine from the amine/isomer-rich fraction by converting with an acid, forming an amine salt, and extracting the amine-salt formed into an aqueous phase;
isolating the organic amine; and
recycling the organic amine to a reaction section of an oligomerization plant;
wherein the linear alpha olefins, isomers and the amine have boiling points under atmospheric pressure which differ by at most 3° C.

18. The method of claim 11 , wherein the purity of the linear alpha olefin after distillation is increased by greater than or equal to 5%.

19. A method for purification of a hydrocarbon stream containing linear alpha olefins, isomers thereof and at least one organic amine, comprising:
removing a major amount of the organic amine from the hydrocarbon stream by distillation, wherein the distillation is carried out so that, together with the amine, between 5% and 95 wt % of the isomers, based on the total amount of the isomers in the hydrocarbon stream, are removed from the hydrocarbon stream in an amine/isomer-rich fraction of the distillation; and
recycling the amine/isomer-rich fraction to a reaction section of an oligomerization plant, without prior separation;
wherein the linear alpha olefins, isomers and the amine have boiling points under atmospheric pressure which differ by at most 3° C.

20. The method of claim 15 , wherein the purity of the linear alpha olefin after distillation is increased by greater than or equal to 5%.

Assignees

• Müller Wolfgang
• Harff Marco
• Wellenhofer Anton
• Wöhl Anina
• Bölt Heinz
• Meiswinkel Andreas
• Saudi Basic Ind Corp
• Linde Ag

Inventors

• Müller Wolfgang
• Harff Marco
• Wellenhofer Anton
• Wöhl Anina
• Bölt Heinz
• Meiswinkel Andreas

Classifications

• C07C7/04 Primary

  by distillation · CPC title

• C07C11/02

  Alkenes · CPC title

• C07C9/00

  Aliphatic saturated hydrocarbons · CPC title