Heating tar sands formations while controlling pressure

• US 7,644,765 B2
• Filed: 10/19/2007
• Issued: 01/12/2010
• Est. Priority Date: 10/20/2006
• Status: Expired due to Fees

• Current Assignee: Shell Oil Company (Shell Plc)
• Original Assignee: Shell Oil Company (Shell Plc)
• Inventors: Beer, Gary Lee, Stegemeier, George Leo, Zhang, Etuan
• Primary Examiner(s): SUCHFIELD, GEORGE A
• Application Number:
  US11/975,713
• Publication Number:
  US 20080277113A1
• Time in Patent Office: 816 Days
• Field of Search: None
• US Class Current: 166/302
• CPC Class Codes: C10G 1/02 by distillation
• CPC Class Codes: C10G 2300/4037 In-situ processes
• CPC Class Codes: E21B 36/04 using electrical heaters
• CPC Class Codes: E21B 43/243 Combustion in situ
• CPC Class Codes: E21B 43/30 Specific pattern of wells, e.g. optimising the spacing of wells
• CPC Class Codes: E21B 47/0228 using electromagnetic energy or detectors therefor

Abstract

Methods for treating a tar sands formation are described herein. Methods may include heating at least a section of a hydrocarbon layer in the formation from a plurality of heaters located in the formation. A pressure in the majority of the section may be maintained below a fracture pressure of the formation. The pressure in the majority of the section may be reduced to a selected pressure after the average temperature reaches a temperature that is above 240° C. and is at or below pyrolysis temperatures of hydrocarbons in the section. At least some hydrocarbon fluids may be produced from the formation.

Claims

1. A method for treating a tar sands formation, comprising:

heating at least a section of a hydrocarbon layer in the formation from a plurality of heaters located in the formation;

maintaining a pressure in the majority of the section below a fracture pressure of the formation while an average temperature in the section is at a temperature below about 24°

C.;

reducing the pressure in the majority of the section to a selected pressure after the average temperature reaches a temperature that is above about 240°

C. and at or below pyrolysis temperatures of hydrocarbons in the section; and

producing at least some hydrocarbon fluids from the formation.

2. The method of claim 1, further comprising operating the heaters at substantially full power until the section of the formation reaches temperatures sufficient to result in visbreaking of hydrocarbons in the section.

3. The method of claim 1, further comprising maintaining the pressure within about 1 MPa of the fracture pressure.

4. The method of claim 1, further comprising maintaining the pressure in the section below the fracture pressure of the formation by removing at least some fluids from the section.

5. The method of claim 1, wherein the fracture pressure of the formation is between about 2000 kPa and about 15000 kPa.

6. The method of claim 1, wherein the selected pressure is between about 300 kPa and about 1000 kPa.

7. The method of claim 1, wherein reducing the pressure to the selected pressure inhibits coking in the formation.

8. The method of claim 1, further comprising increasing the average temperature of the section of the formation to a temperatures above about 270°

C. after reducing the pressure to the selected pressure.

9. The method of claim 1, further comprising producing at least some mobilized hydrocarbons from the formation, at least some visbroken hydrocarbons from the formation, and/or at least some pyrolyzed hydrocarbons from the formation.

10. The method of claim 1, further comprising reducing the pressure in the majority of the section to the selected pressure after the average temperature in the section reaches a temperature between about 275°

C. and about 305°

C.

11. A method for treating a tar sands formation, comprising:

heating at least a section of a hydrocarbon layer in the formation from a plurality of heaters located in the formation;

allowing pressure in the majority of the section to increase into a first pressure range, the first pressure range being from about 1000 kPa below a fracture pressure of the formation to the fracture pressure of the formation;

maintaining the pressure in the majority of the section in the first pressure range while allowing an average temperature in the section to increase up to a temperature of about 24°

C.;

reducing the pressure in the majority of the section into a second pressure range after the average temperature in the section reaches a temperature that is above about 240°

C. but is at or below pyrolysis temperatures of hydrocarbons in the section; and

producing at least some hydrocarbon fluids from the formation in the second pressure range.

12. The method of claim 11, further comprising maintaining the pressure in the section in the first pressure range by removing at least some fluids from the section.

13. The method of claim 11, wherein the fracture pressure of the formation is between about 2000 kPa and about 15000 kPa.

14. The method of claim 11, wherein the second pressure range is from about 300 kPa to about 1000 kPa.

15. The method of claim 11, wherein reducing the pressure into the second pressure range inhibits coking in the formation.

16. The method of claim 11, further comprising increasing the average temperature of the section of the formation to a temperature above about 27°

C. after reducing the pressure into the second pressure range.

17. The method of claim 11, further comprising producing at least some mobilized hydrocarbons from the formation, at least some visbroken hydrocarbons from the formation, and/or at least some pyrolyzed hydrocarbons from the formation.

18. The method of claim 11, further comprising reducing the pressure in the majority of the section into the second pressure range after the average temperature in the section reaches a temperature between about 275°

C. and about 305°

C.