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In situ combustion following sagd

a technology of in situ combustion and petroleum, which is applied in the direction of fluid removal, earth drilling and mining, borehole/well accessories, etc., can solve the problems of difficult production of heavy oil and bitumen from subsurface reservoirs, inability to pump high viscosity oil out of the ground, and inability to reach greater depths

Inactive Publication Date: 2013-03-14
CONOCOPHILLIPS CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent describes a method called steam-assisted gravity drainage (SAGD) that can be used to recover oil from a reservoir using steam. This method can also be used to repressurize the reservoir before it is ready to be produced. The technical effect of this patent is that it provides an effective way to recover more oil from a reservoir and to prepare it for further production.

Problems solved by technology

Production of heavy oil and bitumen from a subsurface reservoir can be quite challenging, especially when the viscosity of the oil at reservoir temperature is often greater than a million centipoise (cP).
High viscosity oil cannot be pumped out of the ground using typical methods, but must be mined or processed in situ.
Greater depths are not economical to access and most reserves are not accessible by mining.
Heating rods and other approaches can achieve this outcome, but they are not as yet economical.
These applications fail to teach or suggest use of in situ combustion after a formation is developed with a steam-assisted process, and describe recovery only at steam chamber walls rather than from the formation as a whole, such as edges of the formation and residual oil within the steam chamber.

Method used

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  • In situ combustion following sagd
  • In situ combustion following sagd
  • In situ combustion following sagd

Examples

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example 1

In Situ Combustion after SAGD

[0044]In a typical oil saturation of a SAGD well pattern at the end of its economic life, about 10% of the original oil still remains in the steam chamber, with very high saturation on the edges of the SAGD pattern (FIG. 2). Please note that in this figure and in others like it (FIGS. 3, 4, &5), the producer and injector and / or their labels are superimposed on one another.

[0045]The residual oil can be removed from the steam chamber by in situ combustion following the SAGD process. Oxidant injection wells are placed at the top of the reservoir at the edge of the SAGD pattern or, if the reservoir contains multiple SAGD wellpairs, between SAGD wellpairs. This placement allows the oxidant injection wells to supply an oxidizing agent to two steam chambers simultaneously.

[0046]After combustion initiates, the combustion front proceeds from the oxidant injectors to the SAGD wellpair, having maximum temperatures of about 500° C. (FIG. 4). Temperature of the combu...

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Abstract

There is provided herein a method for recovering petroleum from a formation, wherein said formation is intersected by at least one wellpair consisting of a horizontal production well and a horizontal injection well, and wherein said formation comprises at least one steam chamber developed by a steam-assisted process, said method comprising: providing an oxidizing agent near the top of said formation; initiating in situ combustion (ISC); and recovering petroleum from said at least one production well.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS[0001]This application is a non-provisional application which claims the benefit of and priority to U.S. Provisional Application Ser. No. 61 / 448,868 filed Mar. 3, 2011, entitled “In Situ Combustion Following SAGD,” which is hereby incorporated by reference in its entirety.FEDERALLY SPONSORED RESEARCH STATEMENT[0002]Not applicable.FIELD OF THE INVENTION[0003]The invention relates to recovery of petroleum from a petroliferous formation, in particular to in situ processing of a reservoir containing heavy oil and / or bitumen.BACKGROUND OF THE INVENTION[0004]Production of heavy oil and bitumen from a subsurface reservoir can be quite challenging, especially when the viscosity of the oil at reservoir temperature is often greater than a million centipoise (cP). High viscosity oil cannot be pumped out of the ground using typical methods, but must be mined or processed in situ. Surface mining is limited to reservoirs to a depth of about 70 meters. Greate...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): E21B43/24
CPCE21B43/2408E21B43/2406E21B43/243
Inventor SULTENFUSS, DANIEL RAYDREHER, JR., WAYNE REID
Owner CONOCOPHILLIPS CO