Downhole flow control device and method

• US 8,171,999 B2
• Filed: 06/10/2008
• Issued: 05/08/2012
• Est. Priority Date: 05/13/2008
• Status: Expired due to Fees

• Current Assignee: Baker Hughes Incorporated (Baker Hughes Company)
• Original Assignee: Baker Hughes, a GE Company, LLC (Baker Hughes Company)
• Inventors: Langeslag, René
• Primary Examiner(s): Bomar, Shane
• Assistant Examiner(s): FULLER, ROBERT EDWARD
• Application Number:
  US12/136,377
• Publication Number:
  US 20090283262A1
• Time in Patent Office: 1,428 Days
• Field of Search: 166/51, 166/227, 166/278, 166/373, 166/386, 166/316, 166/320, 166/332.1, 166/8
• US Class Current: 166/373
• CPC Class Codes: E21B 34/06 in wells
• CPC Class Codes: E21B 43/10 Setting of casings, screens, liners or the like in wells

Abstract

A downhole flow control device includes, a first member defining a first portion of a flow path, and a second member defining a second portion of the flow path, the flow path has a cross sectional flow area defined at least partially by the first member and the second member, a length of the flow path is greater than a largest dimension of the cross sectional flow area, and the cross sectional flow area is adjustable by movement of at least a portion of the first member relative to the second member.

Claims

1. A downhole flow control device, comprising:

a first member defining a first portion of a flow path; and

a second member defining a second portion of the flow path, the flow path having a cross sectional flow area defined at least partially by the first member and the second member, a length of the flow path being greater than a largest dimension of the cross sectional flow area, and the cross sectional flow area being adjustable by movement of at least a portion of the first member relative to the second member, wherein the first member has a first coefficient of thermal expansion and the second member has a second coefficient of thermal expansion and the first coefficient of thermal expansion is different than the second coefficient of thermal expansion.

2. The downhole flow control device of claim 1, wherein the first member is tubular with a radially inwardly protruding thread and the second member is tubular with a radially outwardly protruding thread and the radially outwardly protruding thread extends radially outwardly a dimension greater than a minimum dimension of the radially inwardly protruding thread.

3. The downhole flow control device of claim 2, wherein clearance between the radially inwardly protruding thread and the radially outwardly protruding thread defines the flow path.

4. The downhole flow control device of claim 1, wherein a plurality of the downhole flow control devices are incorporated in a well to equalize at least one of injection of steam and production of hydrocarbons along the well.

5. The downhole flow control device of claim 1, wherein the difference between the first coefficient of thermal expansion and the second coefficient of thermal expansion causes the at least a portion of the first member to move relative to the second member in response to a temperature change of the downhole flow control device.

6. The downhole flow control device of claim 1, wherein the movement of at least a portion of the first member is axial movement.

7. The downhole flow control device of claim 6, wherein the cross sectional flow area is altered at every point along the flow path in response to the movement.

8. The downhole flow control device of claim 7, wherein the alteration of the cross sectional flow area varies over the length of the flow path.

9. The downhole flow control device of claim 1, wherein the flow path has a helical shape.

10. A method of adjusting restriction of a downhole flow path, comprising:

porting fluid through the downhole flow path, the downhole flow path having a length greater than a largest dimension of a cross sectional area of the downhole flow path;

axially moving without rotating at least a portion of one of a first member defining a first portion of the downhole flow path and a second member defining a second portion of the downhole flow path relative to the other of the first member and the second member such that the cross sectional area is altered; and

expanding the first member a different amount than the second member in response to a temperature change of the first member and a temperature change of the second member.

11. The method of adjusting restriction of a downhole flow path of claim 10 wherein the temperature change of the first member and the temperature change of the second member are the same temperature change.

12. The method of adjusting restriction of a downhole flow path of claim 10, further comprising varying the alteration of the cross sectional area over the length of the downhole flow path.

13. The method of adjusting restriction of a downhole flow path of claim 10, further comprising automatically altering the cross sectional area in response to temperature changes in the first member and the second member.

14. The method of adjusting restriction of a downhole flow path of claim 13, further comprising automatically reducing the cross sectional area.

15. A downhole flow control device, comprising:

a first member defining a first portion of a flow path; and

a second member defining a second portion of the flow path, the flow path having a cross sectional flow area defined at least partially by the first member and the second member, a length of the flow path being greater than a largest dimension of the cross sectional flow area, the downhole flow control device being configured to adjust the cross sectional flow area in response to axial movement alone of at least a portion of the first member relative to the second member, the first member having a first coefficient of thermal expansion and the second member having a second coefficient of thermal expansion and the first coefficient of thermal expansion is different than the second coefficient of thermal expansion.