Methods for recovering ionic liquid fines from a process stream

Patent metadata

Field	Value
Publication number	US-9522859-B2
Application number	US-201414567877-A
Country	US
Kind code	B2
Filing date	Dec 11, 2014
Priority date	Dec 11, 2014
Publication date	Dec 20, 2016
Grant date	Dec 20, 2016

Abstract

Methods of recovering droplets of ionic liquid catalyst from a process stream are described. The volume fraction of ionic liquid in the hydrocarbon is increased to cause the ionic liquid droplets to coalesce. One method incorporates various combinations of gravity separation zone(s) and fractionation zones. Another method involves using a combination of a flash vessel and a fractionation zone, as well as an optional gravity separation zone.

First claim

What is claimed is:

1. A method of recovering ionic liquid from a process stream comprising:
separating the process stream comprising a mixture of hydrocarbons and ionic liquid into an ionic liquid phase and a hydrocarbon phase in a gravity separation zone, the hydrocarbon phase containing droplets of ionic liquid, and the hydrocarbon phase having a first volume fraction of ionic liquid;
fractionating the hydrocarbon phase into at least two hydrocarbon fractions, at least one of the hydrocarbon fractions containing the droplets of ionic liquid, the fraction containing the droplets of ionic liquid having a second volume fraction of ionic liquid, the second volume fraction being greater than the first volume fraction; and
separating at least a portion of the hydrocarbon fraction containing the droplets of ionic liquid in a second separation zone into an ionic liquid stream and at least one hydrocarbon stream.

2. The method of claim 1 :
wherein fractionating the hydrocarbon phase into the at least two hydrocarbon fractions comprises fractionating the hydrocarbon phase into at least a first hydrocarbon fraction, a second hydrocarbon fraction, and a third hydrocarbon fraction containing the droplets of ionic liquid; and
wherein separating the at least the portion of the hydrocarbon fraction containing the droplets of ionic liquid in the second separation zone comprises separating the third hydrocarbon fraction into the ionic liquid stream and a second stream.

3. The method of claim 2 wherein at least a portion of the first hydrocarbon fraction is recycled to a reaction zone.

4. The method of claim 2 wherein the first hydrocarbon fraction comprises isobutane, the second hydrocarbon fraction comprises n-butane, and wherein the third hydrocarbon fraction comprises alkylate.

5. The method of claim 1 :
wherein fractionating the hydrocarbon phase into the at least two hydrocarbon fractions comprises fractionating the hydrocarbon phase into at least a first hydrocarbon fraction, and a second hydrocarbon fraction containing the droplets of ionic liquid in a first fractionation zone;
wherein separating the at least the portion of the hydrocarbon fraction containing the droplets of ionic liquid in the second separation zone comprises separating the second hydrocarbon fraction into the ionic liquid stream and a stream comprising at least two hydrocarbons; and further comprising:
fractionating the stream comprising the at least two hydrocarbons into a third fraction and a fourth fraction in a second fractionation zone.

6. The method of claim 5 wherein the first fractionation zone is operated at a pressure higher than a pressure of the second fractionation zone.

7. The method of claim 6 wherein the first fractionation zone is operated at a pressure in a range of about 965 kPa (g) (140 psig) to about 1310 kPa (g) (190 psig), and the second fractionation zone is operated at a pressure in a range of about 620 kPa (g) (90 psig) to about 965 kPa (g) (140 psig).

8. The method of claim 5 wherein the first hydrocarbon fraction comprises isobutane, the second hydrocarbon fraction comprises n-butane and alkylate, and wherein the third fraction comprises n-butane and the fourth fraction comprises alkylate.

9. The method of claim 5 wherein at least a portion of the first hydrocarbon fraction is recycled to a reaction zone.

10. The method of claim 1 :
wherein fractionating the hydrocarbon phase into the at least two hydrocarbon fractions comprises:
fractionating the hydrocarbon phase into at least a first hydrocarbon fraction and a second hydrocarbon fraction containing the droplets of ionic liquid in a first fractionation zone; and
fractionating the second hydrocarbon fraction containing the droplets of ionic liquid into at least a third fraction and a fourth fraction containing the droplets of ionic liquid in a second fractionation zone; and
wherein separating the at least the portion of the hydrocarbon fraction containing the droplets of ionic liquid in the second separation zone comprises separating the fourth fraction into the ionic liquid stream and the at least one hydrocarbon stream.

11. The method of claim 10 wherein the first fractionation zone is operated at a pressure higher than the second fractionation zone.

12. The method of claim 11 wherein the first fractionation zone is operated at a pressure in a range of about 965 kPa (g) (140 psig) to about 1310 kPa (g) (190 psig), and the second fractionation zone is operated at a pressure in a range of about 620 kPa (g) (90 psig) to about 965 kPa (g) (140 psig).

13. The method of claim 10 wherein at least a portion of the first hydrocarbon fraction is recycled to a reaction zone.

14. The method of claim 1 further comprising:
treating the at least one hydrocarbon stream to remove residual ionic liquid.

15. The method of claim 1 further comprising:
recycling at least one of the ionic liquid phase and the ionic liquid stream to a process zone.

16. A method of recovering ionic liquid from a process stream comprising:
flashing at least a portion of the process stream comprising a mixture of hydrocarbons and ionic liquid into a vapor phase comprising a first portion of at least one first hydrocarbon and a liquid phase comprising a second portion of the at least one first hydrocarbon, at least one second hydrocarbon, and the ionic liquid, and separating the liquid phase into an ionic liquid phase and a hydrocarbon phase in a flash vessel, wherein the flash vessel is at a pressure between a bubble point of the at least one first hydrocarbon and a bubble point of the at least one second hydrocarbon; and
fractionating the hydrocarbon phase into at least two fractions.

17. The method of claim 16 wherein the process stream is separated into an ionic liquid stream and a hydrocarbon stream in a gravity separation zone before flashing the at least the portion of the process stream in the flash vessel, and wherein flashing the at least the portion of the process stream comprises flashing the at least a portion of the hydrocarbon stream.

18. The method of claim 16 further comprising:
treating the at least a portion of the hydrocarbon phase to remove residual ionic liquid before fractionating the hydrocarbon phase.

19. The method of claim 16 further comprising:
recycling at least a portion of the ionic liquid phase to a process zone.

20. The method of claim 16 further comprising:
condensing at least one of a portion of the vapor phase and a portion of the first fraction; and
recycling at least one of the portion of the condensed vapor phase and the portion of the condensed first fraction to a process zone.

Assignees

• Uop Llc

Inventors

• Buchbinder Avram M
• Detrick Kurt
• Pham Trung

Classifications

• B01D17/0208

  by sedimentation · CPC title

• C07C7/04

  by distillation · CPC title

• B01D3/143

  by two or more of a fractionation, separation or rectification step · CPC title

• C07C7/005 Primary

  Processes comprising at least two steps in series · CPC title

• C10G29/205

  by reaction with hydrocarbons added to the hydrocarbon oil · CPC title