System and method to treat a multiphase stream

Patent metadata

Field	Value
Publication number	US-9764252-B2
Application number	US-201314380589-A
Country	US
Kind code	B2
Filing date	Feb 25, 2013
Priority date	Mar 29, 2012
Publication date	Sep 19, 2017
Grant date	Sep 19, 2017

Abstract

A system and method for enhancing separation of a denser phase liquid from a lighter phase liquid within a multiphase stream. In one example, a cyclonic coalescer has a tubular housing and a plurality of coaxial flow chambers extending in the axial direction of the housing. A swirling element is associated with each of the plurality of coaxial flow chambers. The swirling elements are constructed and arranged to impart a tangential velocity of the stream flowing through the associated flow chamber.

First claim

What is claimed is:

1. A cyclonic coalescer for enhancing separation of a denser phase liquid from a lighter phase liquid within a multiphase stream, the coalescer comprising:
an inlet for receiving the stream;
a tubular housing having a first length;
a plurality of coaxial flow chambers extending in the axial direction of the housing;
a swirling element associated with each of the plurality of coaxial flow chambers, the swirling elements extend a second length and are constructed and arranged to impart a tangential velocity of the stream flowing through the associated flow chamber; and
an outlet providing the stream including the denser phase liquid and the lighter phase liquid of the stream, wherein an average droplet size or a median droplet size of the denser phase liquid of the stream is increased.

2. The coalescer of claim 1 , wherein the first length is greater than the second length.

3. The coalescer of claim 1 , wherein the first length is equal to the second length.

4. The coalescer of claim 1 , wherein the swirling element is a vane.

5. The coalescer of claim 4 , wherein the vane is fixed at an angle between 40° and 50° with respect to the axial direction of the associated flow chamber.

6. The coalescer of claim 1 further comprising an anti-swirl element associated with each of the plurality of coaxial flow chambers.

7. The coalescer of claim 6 , wherein the anti-swirl elements are positioned downstream of the swirling elements.

8. The coalescer of claim 1 , wherein the housing has an internal diameter of 16 inches.

9. A system for treating a multiphase fluid stream comprising a denser phase liquid and a lighter phase liquid, the system comprising:
an electrostatic coalescer; and
a cyclonic coalescer comprising:
an inlet to receive the stream from the electrostatic coalescer,
a tubular housing having a first length and in fluid communication with the electrostatic coalescer,
a plurality of coaxial flow chambers extending in the axial direction of the housing,
a swirling element associated with each of the plurality of coaxial flow chambers, the swirling elements extend a second length and are constructed and arranged to impart a tangential velocity of the stream flowing through the associated flow chamber, and
an outlet providing the stream including the denser phase liquid and the lighter phase liquid of the stream, wherein an average droplet size or a median droplet size of the denser phase liquid of the stream is increased compared to the stream received into the inlet.

10. The system of claim 9 , wherein the first length is greater than the second length.

11. The system of claim 9 , wherein the swirling element is a vane.

12. The system of claim 11 , wherein the vane is fixed at an angle between 40° and 50° with respect to the axial direction of the associated flow chamber.

13. The system of claim 9 further comprising an anti-swirl element associated with each of the plurality of coaxial flow chambers.

14. The system of claim 13 , wherein the anti-swirl elements are positioned downstream of the swirling elements.

15. The system of claim 9 , wherein the cyclonic coalescer is downstream of the electrostatic coalescer.

16. The system of claim 9 further comprising a gravity separation vessel in fluid communication with the cyclonic coalescer.

17. The system of claim 16 , wherein the gravity separation vessel is downstream of the cyclonic coalescer.

18. A method for treating a multiphase fluid stream to enhance separation of a denser phase liquid from a lighter phase liquid within the multiphase fluid stream, the method comprising:
flowing the stream into a plurality of coaxially extending flow chambers;
imparting a tangential velocity component on the stream flowing through each flow chamber, the tangential velocity is imparted using a swirl element;
controlling the tangential velocity imparted on the stream to increase an average denser phase liquid droplet size of the stream; and
flowing the stream to an outlet.

19. The method of claim 18 , wherein controlling the tangential velocity comprises limiting the total velocity of the flow stream flowing into the flow chambers.

20. The method of claim 19 , wherein the total velocity of the flow stream flowing into the flow chambers is less than 3 m/s.

21. The method of claim 18 , wherein the swirl element is a vane, wherein controlling the tangential velocity comprises selecting a vane angle with respect to the axial direction of the flow chambers.

22. The method of claim 21 , wherein the vane angle is between 40° and 50°.

23. The method of claim 18 , wherein the denser phase liquid has a cut diameter of 1000-1350 microns after the tangential velocity has been imparted on the stream.

24. The method of claim 18 further comprising straightening the flow downstream of the swirl element to reduce the tangential velocity component of the stream.

25. The method of claim 18 , wherein the tangential velocity imparted on the stream causes an average lighter phase droplet size to increase.

26. A method of producing hydrocarbons from a subsurface reservoir, comprising:
producing hydrocarbons through a wellbore, the produced hydrocarbons exist in a liquid-dominated-by-volume multiphase stream having a denser phase liquid and a lighter phase liquid;
flowing the hydrocarbon stream into a plurality of longitudinally extending coaxial flow chambers;
imparting a tangential velocity component on the hydrocarbon stream flowing through each flow chamber, the tangential velocity is imparted using a swirl element;
controlling the tangential velocity imparted on the hydrocarbon stream to increase an average denser phase liquid droplet size of the hydrocarbon stream; and
flowing the hydrocarbon stream to an outlet.

Assignees

• Whitney Scott M
• Grave Edward J
• Fowler Tracy A
• Exxonmobil Upstream Res Co

Inventors

• Whitney Scott M
• Grave Edward J
• Fowler Tracy A

Classifications

• E21B43/34

  Arrangements for separating materials produced by the well · CPC title

• B03C11/00

  Separation by high-voltage electrical fields, not provided for in other groups of this subclass · CPC title

• B01D17/0217 Primary

  by centrifugal force · CPC title

• B04C2003/003

  Shapes or dimensions of vortex chambers · CPC title

• B04C3/04

  Multiple arrangement thereof {(combined with types according to other groups, B04C7/00)} · CPC title