Active coalescer to remove fine liquid droplets

Patent metadata

Field	Value
Publication number	US-10596498-B2
Application number	US-201514700919-A
Country	US
Kind code	B2
Filing date	Apr 30, 2015
Priority date	Apr 30, 2015
Publication date	Mar 24, 2020
Grant date	Mar 24, 2020

Abstract

Separation processes and separation apparatus are described. The process includes introducing a stream of liquid containing dispersed droplets of another liquid into a separation apparatus comprising a vessel having at least one mesh screen covering substantially all of the cross-section of the vessel. The mesh screen is periodically slightly moved so that the wires of the mesh screen contact the dispersed droplets and some of the dispersed droplets coalesce on the wires. The coalesced droplets rise or fall from the wires through the stream of the second liquid. The coalesced droplets are collected in a portion of the vessel. A stream of the second liquid having a reduced level of dispersed droplets is recovered.

First claim

What is claimed is:

1. A process for the separation of a first liquid from a continuous phase of a second liquid containing dispersed droplets of the first liquid comprising:
introducing a stream of the continuous phase of the second liquid containing the dispersed droplets of the first liquid into a separation apparatus comprising a vessel containing at least one mesh screen covering substantially all of a cross-section of the vessel, the mesh screen made of wires;
periodically slightly moving the mesh screen a distance larger than the maximum spacing between the wires and less than about twice the maximum spacing between adjacent wires in the direction of movement so that the wires of the mesh screen contact the dispersed droplets of the first liquid and at least a portion of the dispersed droplets of the first liquid coalesce on the wires;
forming coalesced droplets of the first liquid on the wires;
allowing the coalesced droplets to move from the wires through the stream of the second liquid;
collecting the coalesced droplets in a portion of the vessel to form a layer of the first liquid and a stream of the continuous phase of the second liquid having a reduced level of dispersed droplets of the first liquid;
and
recovering the stream of the continuous phase of the second liquid having the reduced level of dispersed droplets of the first liquid.

2. The process of claim 1 further comprising recovering the layer of the first liquid.

3. The process of claim 1 wherein there are at least two mesh screens separated by less than 5.0 cm.

4. The process of claim 1 wherein the maximum distance between adjacent wires is in a range of about 0.25 cm to about 2.5 cm.

5. The process of claim 1 wherein a distance between adjacent wires at an outer edge of the at least one mesh screen is greater than a distance between adjacent wires in the middle of the at least one mesh screen.

6. The process of claim 1 wherein periodically slightly moving the at least one mesh screen comprises periodically rotating the mesh screen less than 10°.

7. The process of claim 1 wherein a horizontal axis of the vessel is greater than a vertical axis, and wherein the at least one mesh screen is perpendicular to a bulk flow of the stream of the continuous phase of the second liquid containing the dispersed droplets of the first liquid.

8. The process of claim 1 wherein a vertical axis of the vessel is greater than a horizontal axis, and wherein the mesh screen is perpendicular to a bulk flow of the stream of the continuous phase of the second liquid containing the dispersed droplets of the first liquid.

9. The process of claim 1 wherein the mesh screen moves at a frequency so that the dispersed droplets of the first liquid contact at least one wire when passing through the screen.

10. The process of claim 1 wherein the first liquid is an ionic liquid and the second liquid is a hydrocarbon.

11. The process of claim 10 wherein the ionic liquid comprises a phosphonium based ionic liquid, an imidazolium based ionic liquid, a pyridinium based ionic liquid, a trialkyl or tetraalkyl ammonium based ionic liquid, a pyrrolidinium based ionic liquid, a lactamium based ionic liquid, and combinations thereof.

12. The process of claim 1 wherein the dispersed droplets of the first liquid have a diameter of less than about 100 μm.

13. The process of claim 1 wherein the wires are made of a material having a stronger affinity for the first liquid than the second liquid.

14. A process for the separation of a first liquid from a continuous phase of a second liquid containing dispersed droplets of the first liquid comprising:
introducing a stream of the continuous phase of the second liquid containing the dispersed droplets of the first liquid into a separation apparatus comprising a vessel containing at least one mesh screen covering substantially all of a cross-section of the vessel, the mesh screen made of wires;
periodically slightly moving the at least one mesh screen from a first side of the vessel to a second side of the vessel a distance larger than the maximum spacing between the wires and less than about twice the maximum spacing between adjacent wires in the direction of movement so that the wires of the mesh screen contact the dispersed droplets of the first liquid and at least a portion of the dispersed droplets of the first liquid coalesce on the wires;
forming coalesced droplets of the first liquid on the wires;
allowing the coalesced droplets to move from the wires through the stream of the second liquid;
collecting the coalesced droplets in a portion of the vessel to form a layer of the first liquid and a stream of the continuous phase of the second liquid having a reduced level of dispersed droplets of the first liquid;
and
recovering the stream of the continuous phase of the second liquid having the reduced level of dispersed droplets of the first liquid.

15. The process of claim 14 further comprising recovering the layer of the first liquid.

16. The process of claim 14 wherein there are at least two mesh screens separated by less than 5.0 cm.

17. The process of claim 14 wherein the maximum distance between adjacent wires is in a range of about 0.25 cm to about 2.5 cm.

18. The process of claim 14 wherein a distance between adjacent wires at an outer edge of the at least one mesh screen is greater than a distance between adjacent wires in the middle of the at least one mesh screen.

19. The process of claim 14 wherein periodically slightly moving the at least one mesh screen comprises periodically rotating the mesh screen less than 10°.

20. The process of claim 14 wherein the dispersed droplets of the first liquid have a diameter of less than about 100 μm.

Assignees

• Uop Llc

Inventors

• Chen Pengfei
• Xu Zhanping
• Wen Xiaoming

Classifications

• B01D17/045

  with coalescers · CPC title

• B01D39/12 Primary

  of wire gauze; of knitted wire; of expanded metal · CPC title