Downhole burner systems and methods for heating subsurface formations

• US 7,950,453 B2
• Filed: 04/18/2008
• Issued: 05/31/2011
• Est. Priority Date: 04/20/2007
• Status: Expired due to Fees

• Current Assignee: Shell Oil Company (Shell Plc)
• Original Assignee: Shell Oil Company (Shell Plc)
• Inventors: Brignac, Joseph Phillip Jr., Tsai, Kuochen, Munshi, Abdul Wahid, Farmayan, Walter Farman, Abbasi, Faraz, Clomburg, Lloyd Anthony, Siddoway, Mark Alan, Anderson, Karl Gregory, Giles, Steven Paul
• Primary Examiner(s): Bates; Zakiya W
• Assistant Examiner(s): Ditrani; Angela M
• Application Number:
  US12/106,134
• Publication Number:
  US 20090084547A1
• Time in Patent Office: 1,138 Days
• Field of Search: None
• US Class Current: 166/272.1
• CPC Class Codes: C09K 8/845 containing inorganic compounds
• CPC Class Codes: C09K 8/86 containing organic compounds
• CPC Class Codes: C10G 1/008 Controlling or regulating of liquefaction processes
• CPC Class Codes: C10G 1/02 by distillation
• CPC Class Codes: C10G 1/04 by extraction
• CPC Class Codes: C10G 1/042 by the use of hydrogen-donor solvents
• CPC Class Codes: E21B 36/04 using electrical heaters
• CPC Class Codes: E21B 43/16 Enhanced recovery methods for obtaining hydrocarbons
• CPC Class Codes: E21B 43/24 using heat, e.g. steam injection
• CPC Class Codes: E21B 43/2401 by means of electricity
• CPC Class Codes: Y10T 29/49083 Heater type

Abstract

A gas burner assembly for heating a subsurface formation includes an oxidant conduit, a fuel conduit, and a plurality of oxidizers coupled to the oxidant conduit. At least one of the oxidizers includes a mix chamber for mixing fuel from the fuel conduit with oxidant from the oxidant conduit, an igniter, and a shield. The shield includes a plurality of openings in communication with the oxidant conduit. At least one flame stabilizer is coupled to the shield.

Claims

1. A method of heating a formation, comprising:

providing fuel to a plurality of oxidizers located in an opening in the formation;

providing oxidant to the plurality of oxidizers via an oxidant conduit, wherein an oxidizer that first receives the oxidant is a first oxidizer;

reacting the oxidant and fuel in the oxidizers to produce heat to heat a portion of the formation; and

reducing the amount of excess oxidant supplied to the first oxidizer to less than about 50% excess oxidant by weight, wherein excess oxidant comprises an oxidant amount in excess of the oxidant amount needed for complete oxidation of the fuel by the plurality of oxidizers.

2. The method of claim 1, further comprising reducing the amount of excess oxidant to less than about 25% by weight.

3. The method of claim 1, further comprising reducing the amount of excess oxidant to less than about 10% by weight.

13. The method of claim 1, wherein reducing the amount of excess oxidant occurs after a temperature in the oxidant conduit between the oxidizer and a subsequent oxidizer is over 650°

C.

14. The method of claim 1, wherein reducing the amount of excess oxidant occurs after a temperature in the oxidant conduit between the oxidizer and a subsequent oxidizer is over 700°

C.

15. The method of claim 1, further comprising controlling the flow rate of fuel and oxidant to limit the temperature of the oxidizers below 1500°

C. to inhibit production of NO_x compounds.

16. The method of claim 1, wherein a last oxidizer of the plurality of oxidizers is a catalytic oxidizer.

4. A method of heating a formation, comprising:

providing fuel, via a fuel conduit, to a plurality of oxidizers coupled in series in an opening in the formation, wherein an oxidizer that first receives fuel from the fuel conduit is a first oxidizer;

providing oxidant to the plurality of oxidizers via an oxidant conduit;

reacting the oxidant and fuel in the oxidizers to produce heat to heat a portion of the formation; and

reducing the amount of oxidant supplied via the oxidant conduit when a temperature in the fuel conduit reaches a specified temperature.

5. The method of claim 4, wherein fuel and oxidant supplied to the first oxidizer that was unburned in the first oxidizer pass downstream through the oxidant conduit, and further comprising oxidizing unburned fuel and oxidant in the oxidant conduit between oxidizers.

6. The method of claim 4, wherein the specified temperature is about 1200°

F.

7. The method of claim 4, wherein the specified temperature is about 1400°

F.

8. The method of claim 4, wherein the specified temperature is about 1600°

F.

17. The method of claim 4, further comprising passing fuel supplied to the first oxidizer by the first oxidizer to heat the fuel before the fuel is supplied to the first oxidizer.

18. The method of claim 4, wherein reducing the amount of oxidant supplied via the oxidant conduit comprises reducing the oxidant supplied to the first oxidizer from above 50% excess oxidant by weight to less than 50% excess oxidant by weight, wherein excess oxidant comprises an oxidant amount in excess of the oxidant amount needed for complete oxidation of the fuel by the plurality of oxidizers.

19. The method of claim 4, further comprising controlling the flow rate of fuel and oxidant to limit the temperature of the oxidizers below 1500°

C. to inhibit production of NO_x compounds.

20. The method of claim 4, wherein a last oxidizer of the series of oxidizers is a catalytic oxidizer.

9. A method of heating a formation, comprising:

providing fuel, via a fuel conduit, to a plurality of oxidizers in an opening in the formation, wherein the plurality of oxidizers comprises a first oxidizer, one or more intermediate oxidizers connected in series, and a last oxidizer;

providing oxidant to the plurality of oxidizers via an oxidant conduit;

reacting the oxidant and fuel in the oxidizers to produce heat to heat a portion of the formation; and

reducing the oxidant supplied via the oxidant conduit such that the amount of oxygen in the oxidant supplied to the last oxidizer is minimized.

10. The method of claim 9, further comprising initially reacting the fuel and oxidant in the oxidizers and subsequently reacting fuel and oxidant along a length of the oxidant conduit when the temperature along the length of the oxidant conduit is sufficient to support reaction of oxidant and fuel outside of the oxidizers.

11. The method of claim 10, wherein reducing the amount of oxidant supplied via the conduit occurs after a time when fuel and oxidant are reacted along the length of the oxidant conduit.

12. The method of claim 9, wherein the last oxidizer is a catalytic oxidizer.