CA2730284A1 - Systems and methods for producing oil and/or gas - Google Patents
Systems and methods for producing oil and/or gas Download PDFInfo
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- CA2730284A1 CA2730284A1 CA2730284A CA2730284A CA2730284A1 CA 2730284 A1 CA2730284 A1 CA 2730284A1 CA 2730284 A CA2730284 A CA 2730284A CA 2730284 A CA2730284 A CA 2730284A CA 2730284 A1 CA2730284 A1 CA 2730284A1
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- 238000011084 recovery Methods 0.000 claims abstract description 127
- 238000009472 formulation Methods 0.000 claims abstract description 109
- 230000007246 mechanism Effects 0.000 claims abstract description 25
- 239000003921 oil Substances 0.000 claims description 200
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 claims description 139
- 239000007789 gas Substances 0.000 claims description 85
- 239000003795 chemical substances by application Substances 0.000 claims description 78
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 28
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- 238000002347 injection Methods 0.000 claims description 24
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- 239000001569 carbon dioxide Substances 0.000 claims description 14
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 14
- 229930195733 hydrocarbon Natural products 0.000 claims description 12
- 150000002430 hydrocarbons Chemical class 0.000 claims description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- 150000003464 sulfur compounds Chemical class 0.000 claims description 10
- 239000003570 air Substances 0.000 claims description 9
- 150000002978 peroxides Chemical class 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 239000002904 solvent Substances 0.000 claims description 8
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 7
- 229920000642 polymer Polymers 0.000 claims description 7
- 239000011593 sulfur Substances 0.000 claims description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 6
- 239000000446 fuel Substances 0.000 claims description 6
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 229910052717 sulfur Inorganic materials 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000003345 natural gas Substances 0.000 claims description 5
- 239000000243 solution Substances 0.000 claims description 5
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- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 claims description 3
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- 239000012267 brine Substances 0.000 claims description 3
- -1 diesel Substances 0.000 claims description 3
- 239000003502 gasoline Substances 0.000 claims description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 3
- 239000003350 kerosene Substances 0.000 claims description 3
- 239000000314 lubricant Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 239000011707 mineral Substances 0.000 claims description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 3
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 3
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- 239000008096 xylene Substances 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 2
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 claims description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 2
- 238000005755 formation reaction Methods 0.000 description 105
- 238000003860 storage Methods 0.000 description 8
- 239000012530 fluid Substances 0.000 description 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical class O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 2
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- 235000010269 sulphur dioxide Nutrition 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- FCEHBMOGCRZNNI-UHFFFAOYSA-N 1-benzothiophene Chemical class C1=CC=C2SC=CC2=C1 FCEHBMOGCRZNNI-UHFFFAOYSA-N 0.000 description 1
- BWGNESOTFCXPMA-UHFFFAOYSA-N Dihydrogen disulfide Chemical compound SS BWGNESOTFCXPMA-UHFFFAOYSA-N 0.000 description 1
- 238000010795 Steam Flooding Methods 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 238000003491 array Methods 0.000 description 1
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
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- 238000004939 coking Methods 0.000 description 1
- IYYZUPMFVPLQIF-UHFFFAOYSA-N dibenzothiophene Chemical class C1=CC=C2C3=CC=CC=C3SC2=C1 IYYZUPMFVPLQIF-UHFFFAOYSA-N 0.000 description 1
- 150000002019 disulfides Chemical class 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000004058 oil shale Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
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- 150000004763 sulfides Chemical class 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 229930192474 thiophene Natural products 0.000 description 1
- 150000003577 thiophenes Chemical class 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/30—Specific pattern of wells, e.g. optimising the spacing of wells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
A system for producing oil and/or gas from an underground formation comprising a first well in the formation; a mechanism to inject a miscible enhanced oil recovery formulation into the first well; a second well in the formation; a mechanism to produce oil and/or gas from the second well; wherein the first well and the sec-ond well comprise an interior of the system; a plurality of containment wells exterior to the first well and the second well; and a mechanism to inject a containment agent into the containment wells.
Description
SYSTEMS AND METHODS FOR PRODUCING OIL AND/OR GAS
Field of the Invention The present disclosure relates to systems and methods for producing oil and/or gas.
Background of the Invention Enhanced Oil Recovery (EOR) may be used to increase oil recovery in fields worldwide. There are three main types of EOR, thermal, chemical/polymer and gas injection, which may be used to increase oil recovery from a reservoir, beyond what can be achieved by conventional means - possibly extending the life of a field and boosting the oil recovery factor.
Thermal enhanced recovery works by adding heat to the reservoir. The most widely practised form is a steamdrive, which reduces oil viscosity so that it can flow to the producing wells. Chemical flooding increases recovery by reducing the capillary forces that trap residual oil. Polymer flooding improves the sweep efficiency of injected water. Miscible injection works in a similar way to chemical flooding. By injecting a fluid that is miscible with the oil, trapped residual oil can be recovered.
Referring to Figure 1, there is illustrated prior art system 100. System 100 includes underground formation 102, underground formation 104, underground formation 106, and underground formation 108. Production facility 110 is provided at the surface. Well 112 traverses formations 102 and 104, and terminates in formation 106. The portion of formation 106 is shown at 114. Oil and gas are produced from formation 106 through well 112, to production facility 110. Gas and liquid are separated from each other, gas is stored in gas storage 116 and liquid is stored in liquid storage 118.
U.S. Patent Number 7,225,866 discloses that an oil shale formation may be treated using an in situ thermal process. A mixture of hydrocarbons, H2, and/or other formation fluids may be produced from the formation. Heat may be applied to the formation to raise a temperature of a portion of the formation to a pyrolysis temperature. Heat sources may be used to heat the formation. The heat sources may be positioned within the formation in a selected pattern. U.S. Patent Number 7,225,866 is herein incorporated by reference in its entirety.
Co-pending U.S. Patent Application Publication Number 2006/0254769, published November 16, 2006, and having attorney docket number TH2616, discloses a system including a mechanism for recovering oil and/or gas from an underground formation, the oil and/or gas comprising one or more sulfur compounds;
a mechanism for converting at least a portion of the sulfur compounds from the recovered oil and/or gas into a carbon disulfide formulation; and a mechanism for releasing at least a portion of the carbon disulfide formulation into a formation. U.S.
Patent Application Publication Number 2006/0254769 is herein incorporated by reference in its entirety.
There is a need in the art for improved systems and methods for enhanced oil recovery. There is a further need in the art for improved systems and methods for enhanced oil recovery using a solvent, for example through viscosity reduction, chemical effects, and miscible flooding. There is a further need in the art for improved systems and methods for solvent miscible flooding.
Summary of the Invention In one aspect, the invention provides a system for producing oil and/or gas from an underground formation comprising a first well in the formation; a mechanism to inject a miscible enhanced oil recovery formulation into the first well; a second well in the formation; a mechanism to produce oil and/or gas from the second well;
wherein the first well and the second well comprise an interior of the system;
a plurality of containment wells exterior to the first well and the second well;
and a mechanism to inject a containment agent into the containment wells.
In another aspect, the invention provides a method for producing oil and/or gas comprising injecting a carbon disulfide formulation into a formation from a first well;
producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from a plurality of containment wells. In some embodiments, the method also includes recovering carbon disulfide formulation from the oil and/or gas, if present, and then injecting at least a portion of the recovered carbon disulfide formulation into the formation.
Field of the Invention The present disclosure relates to systems and methods for producing oil and/or gas.
Background of the Invention Enhanced Oil Recovery (EOR) may be used to increase oil recovery in fields worldwide. There are three main types of EOR, thermal, chemical/polymer and gas injection, which may be used to increase oil recovery from a reservoir, beyond what can be achieved by conventional means - possibly extending the life of a field and boosting the oil recovery factor.
Thermal enhanced recovery works by adding heat to the reservoir. The most widely practised form is a steamdrive, which reduces oil viscosity so that it can flow to the producing wells. Chemical flooding increases recovery by reducing the capillary forces that trap residual oil. Polymer flooding improves the sweep efficiency of injected water. Miscible injection works in a similar way to chemical flooding. By injecting a fluid that is miscible with the oil, trapped residual oil can be recovered.
Referring to Figure 1, there is illustrated prior art system 100. System 100 includes underground formation 102, underground formation 104, underground formation 106, and underground formation 108. Production facility 110 is provided at the surface. Well 112 traverses formations 102 and 104, and terminates in formation 106. The portion of formation 106 is shown at 114. Oil and gas are produced from formation 106 through well 112, to production facility 110. Gas and liquid are separated from each other, gas is stored in gas storage 116 and liquid is stored in liquid storage 118.
U.S. Patent Number 7,225,866 discloses that an oil shale formation may be treated using an in situ thermal process. A mixture of hydrocarbons, H2, and/or other formation fluids may be produced from the formation. Heat may be applied to the formation to raise a temperature of a portion of the formation to a pyrolysis temperature. Heat sources may be used to heat the formation. The heat sources may be positioned within the formation in a selected pattern. U.S. Patent Number 7,225,866 is herein incorporated by reference in its entirety.
Co-pending U.S. Patent Application Publication Number 2006/0254769, published November 16, 2006, and having attorney docket number TH2616, discloses a system including a mechanism for recovering oil and/or gas from an underground formation, the oil and/or gas comprising one or more sulfur compounds;
a mechanism for converting at least a portion of the sulfur compounds from the recovered oil and/or gas into a carbon disulfide formulation; and a mechanism for releasing at least a portion of the carbon disulfide formulation into a formation. U.S.
Patent Application Publication Number 2006/0254769 is herein incorporated by reference in its entirety.
There is a need in the art for improved systems and methods for enhanced oil recovery. There is a further need in the art for improved systems and methods for enhanced oil recovery using a solvent, for example through viscosity reduction, chemical effects, and miscible flooding. There is a further need in the art for improved systems and methods for solvent miscible flooding.
Summary of the Invention In one aspect, the invention provides a system for producing oil and/or gas from an underground formation comprising a first well in the formation; a mechanism to inject a miscible enhanced oil recovery formulation into the first well; a second well in the formation; a mechanism to produce oil and/or gas from the second well;
wherein the first well and the second well comprise an interior of the system;
a plurality of containment wells exterior to the first well and the second well;
and a mechanism to inject a containment agent into the containment wells.
In another aspect, the invention provides a method for producing oil and/or gas comprising injecting a carbon disulfide formulation into a formation from a first well;
producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from a plurality of containment wells. In some embodiments, the method also includes recovering carbon disulfide formulation from the oil and/or gas, if present, and then injecting at least a portion of the recovered carbon disulfide formulation into the formation.
In another aspect, the invention provides a method for producing oil and/or gas comprising injecting a miscible enhanced oil recovery formulation into a formation from a first well; producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from plurality of containment wells.
Advantages of the invention include one or more of the following:
Improved systems and methods for enhanced recovery of hydrocarbons from a formation with a solvent.
Improved systems and methods for enhanced recovery of hydrocarbons from a formation with a fluid containing a miscible solvent.
Improved compositions and/or techniques for secondary recovery of hydrocarbons.
Improved systems and methods for enhanced oil recovery.
Improved systems and methods for enhanced oil recovery using a miscible solvent.
Improved systems and methods for enhanced oil recovery using a compound which is miscible with oil in place.
Brief Description of the Drawings Figure 1 illustrates an oil and/or gas production system.
Figure 2a illustrates a well pattern.
Figures 2b and 2c illustrate the well pattern of Figure 2a during enhanced oil recovery processes.
Figures 3a-3c illustrate oil and/or gas production systems.
Figure 4 illustrates a well pattern.
Detailed Description of the Invention Figure 2a:
Referring now to Figure 2a, in some embodiments, an array of wells 200 is illustrated. Array 200 includes well group 202 (denoted by horizontal lines) and well group 204 (denoted by diagonal lines).
Array 200 defines a production area, enclosed by the rectangle. Array 200 defines an interior of the system. Exterior to array 200 are located a plurality of containment wells 250.
Advantages of the invention include one or more of the following:
Improved systems and methods for enhanced recovery of hydrocarbons from a formation with a solvent.
Improved systems and methods for enhanced recovery of hydrocarbons from a formation with a fluid containing a miscible solvent.
Improved compositions and/or techniques for secondary recovery of hydrocarbons.
Improved systems and methods for enhanced oil recovery.
Improved systems and methods for enhanced oil recovery using a miscible solvent.
Improved systems and methods for enhanced oil recovery using a compound which is miscible with oil in place.
Brief Description of the Drawings Figure 1 illustrates an oil and/or gas production system.
Figure 2a illustrates a well pattern.
Figures 2b and 2c illustrate the well pattern of Figure 2a during enhanced oil recovery processes.
Figures 3a-3c illustrate oil and/or gas production systems.
Figure 4 illustrates a well pattern.
Detailed Description of the Invention Figure 2a:
Referring now to Figure 2a, in some embodiments, an array of wells 200 is illustrated. Array 200 includes well group 202 (denoted by horizontal lines) and well group 204 (denoted by diagonal lines).
Array 200 defines a production area, enclosed by the rectangle. Array 200 defines an interior of the system. Exterior to array 200 are located a plurality of containment wells 250.
Each well in well group 202 has horizontal distance 230 from the adjacent well in well group 202. Each well in well group 202 has vertical distance 232 from the adjacent well in well group 202.
Each well in well group 204 has horizontal distance 236 from the adjacent well in well group 204. Each well in well group 204 has vertical distance 238 from the adjacent well in well group 204.
As shown in Figure 2a, horizontal distance 230 and horizontal distance 236 refer to a distance from left to right of the paper, and vertical distance 232 and vertical distance 238 refer to a distance from up to down of the paper. In practice, array may be composed of vertical wells that are perpendicular to the earth's surface, horizontal wells that are parallel to the earth's surface, or wells that are inclined at some other angle, for example 30 to 60 degrees with respect to the earth's surface.
Each well in well group 202 is distance 234 from the adjacent wells in well group 204. Each well in well group 204 is distance 234 from the adjacent wells in well group 202.
In some embodiments, each well in well group 202 is surrounded by four wells in well group 204. In some embodiments, each well in well group 204 is surrounded by four wells in well group 202.
In some embodiments, horizontal distance 230 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, vertical distance 232 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, horizontal distance 236 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
Each well in well group 204 has horizontal distance 236 from the adjacent well in well group 204. Each well in well group 204 has vertical distance 238 from the adjacent well in well group 204.
As shown in Figure 2a, horizontal distance 230 and horizontal distance 236 refer to a distance from left to right of the paper, and vertical distance 232 and vertical distance 238 refer to a distance from up to down of the paper. In practice, array may be composed of vertical wells that are perpendicular to the earth's surface, horizontal wells that are parallel to the earth's surface, or wells that are inclined at some other angle, for example 30 to 60 degrees with respect to the earth's surface.
Each well in well group 202 is distance 234 from the adjacent wells in well group 204. Each well in well group 204 is distance 234 from the adjacent wells in well group 202.
In some embodiments, each well in well group 202 is surrounded by four wells in well group 204. In some embodiments, each well in well group 204 is surrounded by four wells in well group 202.
In some embodiments, horizontal distance 230 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, vertical distance 232 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, horizontal distance 236 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, vertical distance 238 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, distance 234 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, array of wells 200 may have from about 10 to about 1000 wells, for example from about 5 to about 500 wells in well group 202, and from about 5 to about 500 wells in well group 204. There may be provided from about 2 to about 1000 containment wells 250, for example from about 5 to about 500, or from about 10 to about 200.
In some embodiments, array of wells 200 is seen as a top view with well group 202 and well group 204 being vertical wells spaced on a piece of land. In some embodiments, array of wells 200 is seen as a cross-sectional side view with well group 202 and well group 204 being horizontal wells spaced within a formation.
The recovery of oil and/or gas with array of wells 200 from an underground formation may be accomplished by any known method. Suitable methods include subsea production, surface production, primary, secondary, or tertiary production.
The selection of the method used to recover the oil and/or gas from the underground formation is not critical.
The containment of oil and/or gas and/or an enhanced oil recovery agent with containment wells 250 may be accomplished by any known method. Suitable methods include pumping water, a peroxide such as hydrogen peroxide or a solution of hydrogen peroxide in water, carbon dioxide, natural gas or other gaseous or liquid hydrocarbons, nitrogen, air, brine, or other liquids or gases into containment wells 250. In another embodiment, containment wells 250 may be used to create a freeze wall barrier. One suitable freeze wall barrier is disclosed in U.S. Patent Number 7,225,866 is herein incorporated by reference in its entirety. The selection of the method used to contain oil and/or gas and/or an enhanced oil recovery agent with containment wells 250 is not critical.
In some embodiments, oil and/or gas may be recovered from a formation into a well, and flow through the well and flowline to a facility. In some embodiments, enhanced oil recovery, with the use of an agent for example steam, water, a surfactant, a polymer flood, and/or a miscible agent such as a carbon disulfide formulation or carbon dioxide, may be used to increase the flow of oil and/or gas from the formation.
In some embodiments, oil and/or gas recovered from a formation may include a sulfur compound. The sulfur compound may include hydrogen sulfide, mercaptans, sulfides and disulfides other than hydrogen disulfide, or heterocyclic sulfur compounds for example thiophenes, benzothiophenes, or substituted and condensed ring dibenzothiophenes, or mixtures thereof.
In some embodiments, a sulfur compound from the formation may be converted into a carbon disulfide formulation. The conversion of at least a portion of the sulfur compound into a carbon disulfide formulation may be accomplished by any known method. Suitable methods may include oxidation reaction of the sulfur compound to sulfur and/or sulfur dioxides, and by reaction of sulfur and/or sulfur dioxide with carbon and/or a carbon containing compound to form the carbon disulfide formulation. The selection of the method used to convert at least a portion of the sulfur compound into a carbon disulfide formulation is not critical.
In some embodiments, a suitable miscible enhanced oil recovery agent may be a carbon disulfide formulation. The carbon disulfide formulation may include carbon disulfide and/or carbon disulfide derivatives for example, thiocarbonates, xanthates and mixtures thereof; and optionally one or more of the following: hydrogen sulfide, sulfur, carbon dioxide, hydrocarbons, and mixtures thereof.
In some embodiments, a suitable method of producing a carbon disulfide formulation is disclosed in copending U.S. Patent Application having serial number 11/409,436, filed on April 19, 2006, having attorney docket number TH2616.
U.S.
Patent Application having serial number 11/409,436 is herein incorporated by reference in its entirety.
In some embodiments, distance 234 is from about 5 to about 1000 meters, or from about 10 to about 500 meters, or from about 20 to about 250 meters, or from about 30 to about 200 meters, or from about 50 to about 150 meters, or from about 90 to about 120 meters, or about 100 meters.
In some embodiments, array of wells 200 may have from about 10 to about 1000 wells, for example from about 5 to about 500 wells in well group 202, and from about 5 to about 500 wells in well group 204. There may be provided from about 2 to about 1000 containment wells 250, for example from about 5 to about 500, or from about 10 to about 200.
In some embodiments, array of wells 200 is seen as a top view with well group 202 and well group 204 being vertical wells spaced on a piece of land. In some embodiments, array of wells 200 is seen as a cross-sectional side view with well group 202 and well group 204 being horizontal wells spaced within a formation.
The recovery of oil and/or gas with array of wells 200 from an underground formation may be accomplished by any known method. Suitable methods include subsea production, surface production, primary, secondary, or tertiary production.
The selection of the method used to recover the oil and/or gas from the underground formation is not critical.
The containment of oil and/or gas and/or an enhanced oil recovery agent with containment wells 250 may be accomplished by any known method. Suitable methods include pumping water, a peroxide such as hydrogen peroxide or a solution of hydrogen peroxide in water, carbon dioxide, natural gas or other gaseous or liquid hydrocarbons, nitrogen, air, brine, or other liquids or gases into containment wells 250. In another embodiment, containment wells 250 may be used to create a freeze wall barrier. One suitable freeze wall barrier is disclosed in U.S. Patent Number 7,225,866 is herein incorporated by reference in its entirety. The selection of the method used to contain oil and/or gas and/or an enhanced oil recovery agent with containment wells 250 is not critical.
In some embodiments, oil and/or gas may be recovered from a formation into a well, and flow through the well and flowline to a facility. In some embodiments, enhanced oil recovery, with the use of an agent for example steam, water, a surfactant, a polymer flood, and/or a miscible agent such as a carbon disulfide formulation or carbon dioxide, may be used to increase the flow of oil and/or gas from the formation.
In some embodiments, oil and/or gas recovered from a formation may include a sulfur compound. The sulfur compound may include hydrogen sulfide, mercaptans, sulfides and disulfides other than hydrogen disulfide, or heterocyclic sulfur compounds for example thiophenes, benzothiophenes, or substituted and condensed ring dibenzothiophenes, or mixtures thereof.
In some embodiments, a sulfur compound from the formation may be converted into a carbon disulfide formulation. The conversion of at least a portion of the sulfur compound into a carbon disulfide formulation may be accomplished by any known method. Suitable methods may include oxidation reaction of the sulfur compound to sulfur and/or sulfur dioxides, and by reaction of sulfur and/or sulfur dioxide with carbon and/or a carbon containing compound to form the carbon disulfide formulation. The selection of the method used to convert at least a portion of the sulfur compound into a carbon disulfide formulation is not critical.
In some embodiments, a suitable miscible enhanced oil recovery agent may be a carbon disulfide formulation. The carbon disulfide formulation may include carbon disulfide and/or carbon disulfide derivatives for example, thiocarbonates, xanthates and mixtures thereof; and optionally one or more of the following: hydrogen sulfide, sulfur, carbon dioxide, hydrocarbons, and mixtures thereof.
In some embodiments, a suitable method of producing a carbon disulfide formulation is disclosed in copending U.S. Patent Application having serial number 11/409,436, filed on April 19, 2006, having attorney docket number TH2616.
U.S.
Patent Application having serial number 11/409,436 is herein incorporated by reference in its entirety.
Figure 2b:
Referring now to Figure 2b, in some embodiments, array of wells 200 is illustrated. Array 200 includes well group 202 (denoted by horizontal lines) and well group 204 (denoted by diagonal lines). Containment wells 250 are provided about array of wells 200.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 204, and oil is recovered from well group 202. As illustrated, the miscible enhanced oil recovery agent has injection profile 208, and oil recovery profile 206 is being produced to well group 202. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 202.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 202, and oil is recovered from well group 204. As illustrated, the miscible enhanced oil recovery agent has injection profile 206, and oil recovery profile 208 is being produced to well group 204. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 204.
In some embodiments, well group 202 may be used for injecting a miscible enhanced oil recovery agent, and well group 204 may be used for producing oil and/or gas from the formation for a first time period; then well group 204 may be used for injecting a miscible enhanced oil recovery agent, and well group 202 may be used for producing oil and/or gas from the formation for a second time period, where the first and second time periods comprise a cycle.
In some embodiments, multiple cycles may be conducted which include alternating well groups 202 and 204 between injecting a miscible enhanced oil recovery agent, and producing oil and/or gas from the formation, where one well group is injecting and the other is producing for a first time period, and then they are switched for a second time period.
In some embodiments, a cycle may be from about 12 hours to about 1 year, or from about 3 days to about 6 months, or from about 5 days to about 3 months.
In some embodiments, each cycle may increase in time, for example each cycle may be from about 5% to about 10% longer than the previous cycle, for example about 8%
longer.
In some embodiments, a miscible enhanced oil recovery agent or a mixture including a miscible enhanced oil recovery agent may be injected at the beginning of a cycle, and an immiscible enhanced oil recovery agent or a mixture including an immiscible enhanced oil recovery agent may be injected at the end of the cycle. In some embodiments, the beginning of a cycle may be the first 10% to about 80%
of a cycle, or the first 20% to about 60% of a cycle, the first 25% to about 40% of a cycle, and the end may be the remainder of the cycle.
In some embodiments, suitable miscible enhanced oil recovery agents include carbon disulfide, hydrogen sulfide, carbon dioxide, octane, pentane, LPG, C2-aliphatic hydrocarbons, nitrogen, diesel, mineral spirits, naptha solvent, asphalt solvent, kerosene, acetone, xylene, trichloroethane, or mixtures of two or more of the preceding, or other miscible enhanced oil recovery agents as are known in the art. In some embodiments, suitable miscible enhanced oil recovery agents are first contact miscible or multiple contact miscible with oil in the formation.
In some embodiments, suitable immiscible enhanced oil recovery agents include water in gas or liquid form, air, mixtures of two or more of the preceding, or other immiscible enhanced oil recovery agents as are known in the art. In some embodiments, suitable immiscible enhanced oil recovery agents are not first contact miscible or multiple contact miscible with oil in the formation.
In some embodiments, an immiscible enhanced oil recovery agent and/or a miscible enhanced oil recovery agent may be used as a containment agent and injected into containment wells 250.
In some embodiments, immiscible and/or miscible enhanced oil recovery agents injected into the formation may be recovered from the produced oil and/or gas and re-injected into the formation.
In some embodiments, oil as present in the formation prior to the injection of any enhanced oil recovery agents has a viscosity of at least about 100 centipoise, or at least about 500 centipoise, or at least about 1000 centipoise, or at least about 2000 centipoise, or at least about 5000 centipoise, or at least about 10,000 centipoise. In some embodiments, oil as present in the formation prior to the injection of any enhanced oil recovery agents has a viscosity of up to about 5,000,000 centipoise, or up to about 2,000,000 centipoise, or up to about 1,000,000 centipoise, or up to about 500,000 centipoise.
Figure 2c:
Referring now to Figure 2c, in some embodiments, array of wells 200 is illustrated. Array 200 includes well group 202 (denoted by horizontal lines) and well group 204 (denoted by diagonal lines). Containment wells 250 are located exterior to array 200 to form a perimeter about array 200.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 204, and oil is recovered from well group 202. As illustrated, the miscible enhanced oil recovery agent has injection profile 208 with overlap 210 with oil recovery profile 206, which is being produced to well group 202. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 202.
After a sufficient period of time containment agent injection profile may overlap with one or more of injection profile 208 and oil recovery profile 206 so that enhanced oil recovery agent is contained within array 200; and/or so that oil and/or gas is contained within array 200; and/or so that containment agent is produced to well group 202.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 202, and oil is recovered from well group 204. As illustrated, the miscible enhanced oil recovery agent has injection profile 206 with overlap 210 with oil recovery profile 208, which is being produced to well group 204. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 204.
After a sufficient period of time containment agent injection profile may overlap with one or more of injection profile 208 and oil recovery profile 206 so that enhanced oil recovery agent is contained within array 200; and/or so that oil and/or gas is contained within array 200; and/or so that containment agent is produced to well group 204.
Releasing at least a portion of the miscible enhanced oil recovery agent and/or other liquids and/or gases may be accomplished by any known method. One suitable method is injecting the miscible enhanced oil recovery formulation into a single conduit in a single well, allowing carbon disulfide formulation to soak, and then pumping out at least a portion of the carbon disulfide formulation with gas and/or liquids. Another suitable method is injecting the miscible enhanced oil recovery formulation into a first well, and pumping out at least a portion of the miscible enhanced oil recovery formulation with gas and/or liquids through a second well. The selection of the method used to inject at least a portion of the miscible enhanced oil recovery formulation and/or other liquids and/or gases is not critical.
In some embodiments, the miscible enhanced oil recovery formulation and/or other liquids and/or gases may be pumped into a formation at a pressure up to the fracture pressure of the formation.
In some embodiments, the miscible enhanced oil recovery formulation may be mixed in with oil and/or gas in a formation to form a mixture which may be recovered from a well. In some embodiments, a quantity of the miscible enhanced oil recovery formulation may be injected into a well, followed by another component to force carbon the formulation across the formation. For example air, water in liquid or vapor form, carbon dioxide, other gases, other liquids, and/or mixtures thereof may be used to force the miscible enhanced oil recovery formulation across the formation.
In some embodiments, the miscible enhanced oil recovery formulation may be heated prior to being injected into the formation to lower the viscosity of fluids in the formation, for example heavy oils, paraffins, asphaltenes, etc.
In some embodiments, the miscible enhanced oil recovery formulation may be heated and/or boiled while within the formation, with the use of a heated fluid or a heater, to lower the viscosity of fluids in the formation. In some embodiments, heated water and/or steam may be used to heat and/or vaporize the miscible enhanced oil recovery formulation in the formation.
In some embodiments, the miscible enhanced oil recovery formulation may be heated and/or boiled while within the formation, with the use of a heater. One suitable heater is disclosed in copending United States Patent Application having serial number 10/693,816, filed on October 24, 2003, and having attorney docket number TH2557. United States Patent Application having serial number 10/693,816 is herein incorporated by reference in its entirety.
Figures 3a & 3b:
Referring now to Figures 3a and 3b, in some embodiments of the invention, system 300 is illustrated. System 300 includes underground formation 302, underground formation 304, underground formation 306, and underground formation 308. Facility 310 is provided at the surface. Well 312 traverses formations 302 and 304, and has openings in formation 306. Portions 314 of formation 306 may be optionally fractured and/or perforated. During primary production, oil and gas from formation 306 is produced into portions 314, into well 312, and travels up to facility 310. Facility 310 then separates gas, which is sent to gas processing 316, and liquid, which is sent to liquid storage 318. Facility 310 also includes miscible enhanced oil recovery formulation storage 330. As shown in Figure 3a, miscible enhanced oil recovery formulation may be pumped down well 312 that is shown by the down arrow and pumped into formation 306. Miscible enhanced oil recovery formulation may be left to soak in formation for a period of time from about 1 hour to about 15 days, for example from about 5 to about 50 hours.
Containment well 350 with injection mechanism 352 and containment well 360 with injection mechanism 362 may be provided to contain miscible enhanced oil recovery formulation between containment well 350 and containment well 360.
Injection mechanisms 352 and 362 may be used to inject a containment agent, for example a refrigerant to create a freeze wall, cement, liquid sulfur, or a liquid or gas such as water, peroxide, a peroxide solution, carbon dioxide, natural gas, other C, -C15 hydrocarbons, nitrogen, or air.
After the soaking period, as shown in Figure 3b, miscible enhanced oil recovery formulation and oil and/or gas is then produced back up well 312 to facility 310. Facility 310 is adapted to separate and/or recycle miscible enhanced oil recovery formulation, for example by boiling the formulation, condensing it or filtering or reacting it, then re-injecting the formulation into well 312, for example by repeating the soaking cycle shown in Figures 3a and 3b from about 2 to about 5 times.
In some embodiments, miscible enhanced oil recovery formulation may be pumped into formation 306 below the fracture pressure of the formation, for example from about 40% to about 90% of the fracture pressure.
In some embodiments, well 312 as shown in Figure 3a injecting into formation 306 may be representative of a well in well group 202, and well 312 as shown in Figure 3b producing from formation 306 may be representative of a well in well group 204.
In some embodiments, well 312 as shown in Figure 3a injecting into formation 306 may be representative of a well in well group 204, and well 312 as shown in Figure 3b producing from formation 306 may be representative of a well in well group 202.
Figure 3c:
Referring now to Figure 3c, in some embodiments of the invention, system 400 is illustrated. System 400 includes underground formation 402, formation 404, formation 406, and formation 408. Production facility 410 is provided at the surface.
Well 412 traverses formation 402 and 404 has openings at formation 406.
Portions of formation 414 may be optionally fractured and/or perforated. As oil and gas is produced from formation 406 it enters portions 414, and travels up well 412 to production facility 410. Gas and liquid may be separated, and gas may be sent to gas storage 416, and liquid may be sent to liquid storage 418. Production facility 410 is able to produce and/or store miscible enhanced oil recovery formulation, which may be produced and stored in production / storage 430. Hydrogen sulfide and/or other sulfur containing compounds from well 412 may be sent to miscible enhanced oil recovery formulation production / storage 430. Miscible enhanced oil recovery formulation is pumped down well 432, to portions 434 of formation 406.
Miscible enhanced oil recovery formulation traverses formation 406 to aid in the production of oil and gas, and then the miscible enhanced oil recovery formulation, oil and/or gas may all be produced to well 412, to production facility 410. Miscible enhanced oil recovery formulation may then be recycled, for example by boiling the formulation, condensing it or filtering or reacting it, then re-injecting the formulation into well 432.
Containment well 450 with injection mechanism 452 and containment well 460 with injection mechanism 462 may be provided to contain miscible enhanced oil recovery formulation between containment well 450 and containment well 460.
Injection mechanisms 452 and 462 may be used to inject a containment agent, for example a refrigerant to create a freeze wall, or a liquid or gas such as water, peroxide, a peroxide solution, carbon dioxide, natural gas, other C1 - C15 hydrocarbons, nitrogen, or air, or mixtures thereof.
In some embodiments, a quantity of miscible enhanced oil recovery formulation or miscible enhanced oil recovery formulation mixed with other components may be injected into well 432, followed by another component to force miscible enhanced oil recovery formulation or miscible enhanced oil recovery formulation mixed with other components across formation 406, for example air; water in gas or liquid form;
water mixed with one or more salts, polymers, and/or surfactants; carbon dioxide;
other gases; other liquids; and/or mixtures thereof.
In some embodiments, well 412 which is producing oil and/or gas is representative of a well in well group 202, and well 432 which is being used to inject miscible enhanced oil recovery formulation is representative of a well in well group 204.
In some embodiments, well 412 which is producing oil and/or gas is representative of a well in well group 204, and well 432 which is being used to inject miscible enhanced oil recovery formulation is representative of a well in well group 202.
Figure 4:
Referring now to Figure 4, in some embodiments of the invention, an array of wells 500 is illustrated. Array 500 includes well group 502 (denoted by horizontal lines) and well group 504 (denoted by diagonal lines).
Array 500 defines a production area, enclosed by the rectangle. Array 500 defines an interior of the system. Exterior to array 500 are located internal containment wells 550, and external containment wells 552. Other arrays of containment wells may also be provided (not shown).
In some embodiments, a containment agent may be injected into internal containment wells 550 and external containment wells 552. In another embodiment, a containment agent may be injected into external containment wells 552, and the containment agent, oil and/or gas, and/or an enhanced oil recovery agent may be produced from internal containment wells 550.
Each well in well group 502 has horizontal distance 530 from the adjacent well in well group 502. Each well in well group 502 has vertical distance 532 from the adjacent well in well group 502.
Each well in well group 504 has horizontal distance 536 from the adjacent well in well group 504. Each well in well group 504 has vertical distance 538 from the adjacent well in well group 504.
Each well in well group 502 is distance 534 from the adjacent wells in well group 504. Each well in well group 504 is distance 534 from the adjacent wells in well group 502.
In some embodiments, each well in well group 502 is surrounded by four wells in well group 504. In some embodiments, each well in well group 504 is surrounded by four wells in well group 502.
Alternatives:
In some embodiments, oil and/or gas produced may be transported to a refinery and/or a treatment facility. The oil and/or gas may be processed to produce commercial products such as transportation fuels such as gasoline and diesel, heating fuel, lubricants, chemicals, and/or polymers. Processing may include distilling and/or fractionally distilling the oil and/or gas to produce one or more distillate fractions. In some embodiments, the oil and/or gas, and/or the one or more distillate fractions may be subjected to a process of one or more of the following:
catalytic cracking, hydrocracking, hydrotreating, coking, thermal cracking, distilling, reforming, polymerization, isomerization, alkylation, blending, and dewaxing.
Illustrative Embodiments:
In one embodiment of the invention, there is disclosed a system for producing oil and/or gas from an underground formation comprising a first well in the formation;
a mechanism to inject a miscible enhanced oil recovery formulation into the first well;
a second well in the formation; a mechanism to produce oil and/or gas from the second well; wherein the first well and the second well comprise an interior of the system; a plurality of containment wells exterior to the first well and the second well;
and a mechanism to inject a containment agent into the containment wells. In some embodiments, the first well is at a distance of 10 meters to 1 kilometer from the second well. In some embodiments, the underground formation is beneath a body of water. In some embodiments, the system also includes a mechanism for injecting an immiscible enhanced oil recovery formulation into the formation, after the miscible enhanced oil recovery formulation has been released into the formation. In some embodiments, the system also includes a miscible enhanced oil recovery formulation selected from the group consisting of a carbon disulfide formulation, hydrogen sulfide, carbon dioxide, octane, pentane, LPG, C2-C6 aliphatic hydrocarbons, nitrogen, diesel, mineral spirits, naptha solvent, asphalt solvent, kerosene, acetone, xylene, trichloroethane, and mixtures thereof. In some embodiments, the system also includes an immiscible enhanced oil recovery formulation selected from the group consisting of water in gas or liquid form, air, and mixtures thereof. In some embodiments, the system also includes a first array of wells comprising from 5 to 500 wells, and a second array of wells comprising from 5 to 500 wells. In some embodiments, the system also includes a miscible enhanced oil recovery formulation comprising a carbon disulfide formulation. In some embodiments, the system also includes a mechanism for producing a carbon disulfide formulation. In some embodiments, the underground formation comprises an oil having a viscosity from 100 to 5,000,000 centipoise. In some embodiments, the first well comprises a miscible enhanced oil recovery formulation profile in the formation, and the second well comprises an oil recovery profile in the formation, the system further comprising an overlap between the miscible enhanced oil recovery formulation profile and the oil recovery profile. In some embodiments, the containment agent is selected from the group consisting of a refrigerant, water, brine, peroxide, peroxide solutions, nitrogen, air, carbon dioxide, natural gas, other C1 - C15 hydrocarbons, and mixtures thereof.
In some embodiments, the containment agent comprises water. In some embodiments, the second well produces the containment agent. In some embodiments, the second well produces the containment agent, the miscible enhanced oil recovery formulation, and oil and/or gas.
In one embodiment of the invention, there is disclosed a method for producing oil and/or gas comprising injecting a carbon disulfide formulation into a formation from a first well; producing oil and/or gas from the formation from a second well;
and injecting a containment agent into the formation from a plurality of containment wells.
In some embodiments, the method also includes recovering carbon disulfide formulation from the oil and/or gas, if present, and then injecting at least a portion of the recovered carbon disulfide formulation into the formation. In some embodiments, injecting the carbon disulfide formulation comprises injecting at least a portion of the carbon disulfide formulation into the formation in a mixture with one or more of hydrocarbons; sulfur compounds other than carbon disulfide; carbon dioxide;
carbon monoxide; or mixtures thereof. In some embodiments, the method also includes heating the carbon disulfide formulation prior to injecting the carbon disulfide formulation into the formation, or while within the formation. In some embodiments, the carbon disulfide formulation is injected at a pressure from 0 to 37,000 kilopascals above the initial reservoir pressure, measured prior to when carbon disulfide injection begins. In some embodiments, the underground formation comprises a permeability from 0.0001 to 15 Darcies, for example a permeability from 0.001 to 1 Darcy.
In some embodiments, any oil, as present in the underground formation prior to the injecting the carbon disulfide formulation, has a sulfur content from 0.5% to 5%, for example from 1 % to 3%. In some embodiments, the method also includes converting at least a portion of the recovered oil and/or gas into a material selected from the group consisting of transportation fuels such as gasoline and diesel, heating fuel, lubricants, chemicals, and/or polymers.
In one embodiment of the invention, there is disclosed a method for producing oil and/or gas comprising injecting a miscible enhanced oil recovery formulation into a formation from a first well; producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from plurality of containment wells. In some embodiments, the method also includes injecting an immiscible enhanced oil recovery formulation after injecting the miscible enhanced oil recovery formulation, to push the miscible enhanced oil recovery formulation through the formation. In some embodiments, the miscible enhanced oil recovery formulation comprises a carbon disulfide formulation.
Those of skill in the art will appreciate that many modifications and variations are possible in terms of the disclosed embodiments of the invention, configurations, materials and methods without departing from their spirit and scope.
Accordingly, the scope of the claims appended hereafter and their functional equivalents should not be limited by particular embodiments described and illustrated herein, as these are merely exemplary in nature.
Referring now to Figure 2b, in some embodiments, array of wells 200 is illustrated. Array 200 includes well group 202 (denoted by horizontal lines) and well group 204 (denoted by diagonal lines). Containment wells 250 are provided about array of wells 200.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 204, and oil is recovered from well group 202. As illustrated, the miscible enhanced oil recovery agent has injection profile 208, and oil recovery profile 206 is being produced to well group 202. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 202.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 202, and oil is recovered from well group 204. As illustrated, the miscible enhanced oil recovery agent has injection profile 206, and oil recovery profile 208 is being produced to well group 204. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 204.
In some embodiments, well group 202 may be used for injecting a miscible enhanced oil recovery agent, and well group 204 may be used for producing oil and/or gas from the formation for a first time period; then well group 204 may be used for injecting a miscible enhanced oil recovery agent, and well group 202 may be used for producing oil and/or gas from the formation for a second time period, where the first and second time periods comprise a cycle.
In some embodiments, multiple cycles may be conducted which include alternating well groups 202 and 204 between injecting a miscible enhanced oil recovery agent, and producing oil and/or gas from the formation, where one well group is injecting and the other is producing for a first time period, and then they are switched for a second time period.
In some embodiments, a cycle may be from about 12 hours to about 1 year, or from about 3 days to about 6 months, or from about 5 days to about 3 months.
In some embodiments, each cycle may increase in time, for example each cycle may be from about 5% to about 10% longer than the previous cycle, for example about 8%
longer.
In some embodiments, a miscible enhanced oil recovery agent or a mixture including a miscible enhanced oil recovery agent may be injected at the beginning of a cycle, and an immiscible enhanced oil recovery agent or a mixture including an immiscible enhanced oil recovery agent may be injected at the end of the cycle. In some embodiments, the beginning of a cycle may be the first 10% to about 80%
of a cycle, or the first 20% to about 60% of a cycle, the first 25% to about 40% of a cycle, and the end may be the remainder of the cycle.
In some embodiments, suitable miscible enhanced oil recovery agents include carbon disulfide, hydrogen sulfide, carbon dioxide, octane, pentane, LPG, C2-aliphatic hydrocarbons, nitrogen, diesel, mineral spirits, naptha solvent, asphalt solvent, kerosene, acetone, xylene, trichloroethane, or mixtures of two or more of the preceding, or other miscible enhanced oil recovery agents as are known in the art. In some embodiments, suitable miscible enhanced oil recovery agents are first contact miscible or multiple contact miscible with oil in the formation.
In some embodiments, suitable immiscible enhanced oil recovery agents include water in gas or liquid form, air, mixtures of two or more of the preceding, or other immiscible enhanced oil recovery agents as are known in the art. In some embodiments, suitable immiscible enhanced oil recovery agents are not first contact miscible or multiple contact miscible with oil in the formation.
In some embodiments, an immiscible enhanced oil recovery agent and/or a miscible enhanced oil recovery agent may be used as a containment agent and injected into containment wells 250.
In some embodiments, immiscible and/or miscible enhanced oil recovery agents injected into the formation may be recovered from the produced oil and/or gas and re-injected into the formation.
In some embodiments, oil as present in the formation prior to the injection of any enhanced oil recovery agents has a viscosity of at least about 100 centipoise, or at least about 500 centipoise, or at least about 1000 centipoise, or at least about 2000 centipoise, or at least about 5000 centipoise, or at least about 10,000 centipoise. In some embodiments, oil as present in the formation prior to the injection of any enhanced oil recovery agents has a viscosity of up to about 5,000,000 centipoise, or up to about 2,000,000 centipoise, or up to about 1,000,000 centipoise, or up to about 500,000 centipoise.
Figure 2c:
Referring now to Figure 2c, in some embodiments, array of wells 200 is illustrated. Array 200 includes well group 202 (denoted by horizontal lines) and well group 204 (denoted by diagonal lines). Containment wells 250 are located exterior to array 200 to form a perimeter about array 200.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 204, and oil is recovered from well group 202. As illustrated, the miscible enhanced oil recovery agent has injection profile 208 with overlap 210 with oil recovery profile 206, which is being produced to well group 202. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 202.
After a sufficient period of time containment agent injection profile may overlap with one or more of injection profile 208 and oil recovery profile 206 so that enhanced oil recovery agent is contained within array 200; and/or so that oil and/or gas is contained within array 200; and/or so that containment agent is produced to well group 202.
In some embodiments, a miscible enhanced oil recovery agent is injected into well group 202, and oil is recovered from well group 204. As illustrated, the miscible enhanced oil recovery agent has injection profile 206 with overlap 210 with oil recovery profile 208, which is being produced to well group 204. In some embodiments, a containment agent is injected into containment wells 250. As illustrated, the containment agent has an injection profile about each of the containment wells 250. Containment agent may be used to force miscible enhanced oil recovery agent and/or oil and/or gas towards producing well group 204.
After a sufficient period of time containment agent injection profile may overlap with one or more of injection profile 208 and oil recovery profile 206 so that enhanced oil recovery agent is contained within array 200; and/or so that oil and/or gas is contained within array 200; and/or so that containment agent is produced to well group 204.
Releasing at least a portion of the miscible enhanced oil recovery agent and/or other liquids and/or gases may be accomplished by any known method. One suitable method is injecting the miscible enhanced oil recovery formulation into a single conduit in a single well, allowing carbon disulfide formulation to soak, and then pumping out at least a portion of the carbon disulfide formulation with gas and/or liquids. Another suitable method is injecting the miscible enhanced oil recovery formulation into a first well, and pumping out at least a portion of the miscible enhanced oil recovery formulation with gas and/or liquids through a second well. The selection of the method used to inject at least a portion of the miscible enhanced oil recovery formulation and/or other liquids and/or gases is not critical.
In some embodiments, the miscible enhanced oil recovery formulation and/or other liquids and/or gases may be pumped into a formation at a pressure up to the fracture pressure of the formation.
In some embodiments, the miscible enhanced oil recovery formulation may be mixed in with oil and/or gas in a formation to form a mixture which may be recovered from a well. In some embodiments, a quantity of the miscible enhanced oil recovery formulation may be injected into a well, followed by another component to force carbon the formulation across the formation. For example air, water in liquid or vapor form, carbon dioxide, other gases, other liquids, and/or mixtures thereof may be used to force the miscible enhanced oil recovery formulation across the formation.
In some embodiments, the miscible enhanced oil recovery formulation may be heated prior to being injected into the formation to lower the viscosity of fluids in the formation, for example heavy oils, paraffins, asphaltenes, etc.
In some embodiments, the miscible enhanced oil recovery formulation may be heated and/or boiled while within the formation, with the use of a heated fluid or a heater, to lower the viscosity of fluids in the formation. In some embodiments, heated water and/or steam may be used to heat and/or vaporize the miscible enhanced oil recovery formulation in the formation.
In some embodiments, the miscible enhanced oil recovery formulation may be heated and/or boiled while within the formation, with the use of a heater. One suitable heater is disclosed in copending United States Patent Application having serial number 10/693,816, filed on October 24, 2003, and having attorney docket number TH2557. United States Patent Application having serial number 10/693,816 is herein incorporated by reference in its entirety.
Figures 3a & 3b:
Referring now to Figures 3a and 3b, in some embodiments of the invention, system 300 is illustrated. System 300 includes underground formation 302, underground formation 304, underground formation 306, and underground formation 308. Facility 310 is provided at the surface. Well 312 traverses formations 302 and 304, and has openings in formation 306. Portions 314 of formation 306 may be optionally fractured and/or perforated. During primary production, oil and gas from formation 306 is produced into portions 314, into well 312, and travels up to facility 310. Facility 310 then separates gas, which is sent to gas processing 316, and liquid, which is sent to liquid storage 318. Facility 310 also includes miscible enhanced oil recovery formulation storage 330. As shown in Figure 3a, miscible enhanced oil recovery formulation may be pumped down well 312 that is shown by the down arrow and pumped into formation 306. Miscible enhanced oil recovery formulation may be left to soak in formation for a period of time from about 1 hour to about 15 days, for example from about 5 to about 50 hours.
Containment well 350 with injection mechanism 352 and containment well 360 with injection mechanism 362 may be provided to contain miscible enhanced oil recovery formulation between containment well 350 and containment well 360.
Injection mechanisms 352 and 362 may be used to inject a containment agent, for example a refrigerant to create a freeze wall, cement, liquid sulfur, or a liquid or gas such as water, peroxide, a peroxide solution, carbon dioxide, natural gas, other C, -C15 hydrocarbons, nitrogen, or air.
After the soaking period, as shown in Figure 3b, miscible enhanced oil recovery formulation and oil and/or gas is then produced back up well 312 to facility 310. Facility 310 is adapted to separate and/or recycle miscible enhanced oil recovery formulation, for example by boiling the formulation, condensing it or filtering or reacting it, then re-injecting the formulation into well 312, for example by repeating the soaking cycle shown in Figures 3a and 3b from about 2 to about 5 times.
In some embodiments, miscible enhanced oil recovery formulation may be pumped into formation 306 below the fracture pressure of the formation, for example from about 40% to about 90% of the fracture pressure.
In some embodiments, well 312 as shown in Figure 3a injecting into formation 306 may be representative of a well in well group 202, and well 312 as shown in Figure 3b producing from formation 306 may be representative of a well in well group 204.
In some embodiments, well 312 as shown in Figure 3a injecting into formation 306 may be representative of a well in well group 204, and well 312 as shown in Figure 3b producing from formation 306 may be representative of a well in well group 202.
Figure 3c:
Referring now to Figure 3c, in some embodiments of the invention, system 400 is illustrated. System 400 includes underground formation 402, formation 404, formation 406, and formation 408. Production facility 410 is provided at the surface.
Well 412 traverses formation 402 and 404 has openings at formation 406.
Portions of formation 414 may be optionally fractured and/or perforated. As oil and gas is produced from formation 406 it enters portions 414, and travels up well 412 to production facility 410. Gas and liquid may be separated, and gas may be sent to gas storage 416, and liquid may be sent to liquid storage 418. Production facility 410 is able to produce and/or store miscible enhanced oil recovery formulation, which may be produced and stored in production / storage 430. Hydrogen sulfide and/or other sulfur containing compounds from well 412 may be sent to miscible enhanced oil recovery formulation production / storage 430. Miscible enhanced oil recovery formulation is pumped down well 432, to portions 434 of formation 406.
Miscible enhanced oil recovery formulation traverses formation 406 to aid in the production of oil and gas, and then the miscible enhanced oil recovery formulation, oil and/or gas may all be produced to well 412, to production facility 410. Miscible enhanced oil recovery formulation may then be recycled, for example by boiling the formulation, condensing it or filtering or reacting it, then re-injecting the formulation into well 432.
Containment well 450 with injection mechanism 452 and containment well 460 with injection mechanism 462 may be provided to contain miscible enhanced oil recovery formulation between containment well 450 and containment well 460.
Injection mechanisms 452 and 462 may be used to inject a containment agent, for example a refrigerant to create a freeze wall, or a liquid or gas such as water, peroxide, a peroxide solution, carbon dioxide, natural gas, other C1 - C15 hydrocarbons, nitrogen, or air, or mixtures thereof.
In some embodiments, a quantity of miscible enhanced oil recovery formulation or miscible enhanced oil recovery formulation mixed with other components may be injected into well 432, followed by another component to force miscible enhanced oil recovery formulation or miscible enhanced oil recovery formulation mixed with other components across formation 406, for example air; water in gas or liquid form;
water mixed with one or more salts, polymers, and/or surfactants; carbon dioxide;
other gases; other liquids; and/or mixtures thereof.
In some embodiments, well 412 which is producing oil and/or gas is representative of a well in well group 202, and well 432 which is being used to inject miscible enhanced oil recovery formulation is representative of a well in well group 204.
In some embodiments, well 412 which is producing oil and/or gas is representative of a well in well group 204, and well 432 which is being used to inject miscible enhanced oil recovery formulation is representative of a well in well group 202.
Figure 4:
Referring now to Figure 4, in some embodiments of the invention, an array of wells 500 is illustrated. Array 500 includes well group 502 (denoted by horizontal lines) and well group 504 (denoted by diagonal lines).
Array 500 defines a production area, enclosed by the rectangle. Array 500 defines an interior of the system. Exterior to array 500 are located internal containment wells 550, and external containment wells 552. Other arrays of containment wells may also be provided (not shown).
In some embodiments, a containment agent may be injected into internal containment wells 550 and external containment wells 552. In another embodiment, a containment agent may be injected into external containment wells 552, and the containment agent, oil and/or gas, and/or an enhanced oil recovery agent may be produced from internal containment wells 550.
Each well in well group 502 has horizontal distance 530 from the adjacent well in well group 502. Each well in well group 502 has vertical distance 532 from the adjacent well in well group 502.
Each well in well group 504 has horizontal distance 536 from the adjacent well in well group 504. Each well in well group 504 has vertical distance 538 from the adjacent well in well group 504.
Each well in well group 502 is distance 534 from the adjacent wells in well group 504. Each well in well group 504 is distance 534 from the adjacent wells in well group 502.
In some embodiments, each well in well group 502 is surrounded by four wells in well group 504. In some embodiments, each well in well group 504 is surrounded by four wells in well group 502.
Alternatives:
In some embodiments, oil and/or gas produced may be transported to a refinery and/or a treatment facility. The oil and/or gas may be processed to produce commercial products such as transportation fuels such as gasoline and diesel, heating fuel, lubricants, chemicals, and/or polymers. Processing may include distilling and/or fractionally distilling the oil and/or gas to produce one or more distillate fractions. In some embodiments, the oil and/or gas, and/or the one or more distillate fractions may be subjected to a process of one or more of the following:
catalytic cracking, hydrocracking, hydrotreating, coking, thermal cracking, distilling, reforming, polymerization, isomerization, alkylation, blending, and dewaxing.
Illustrative Embodiments:
In one embodiment of the invention, there is disclosed a system for producing oil and/or gas from an underground formation comprising a first well in the formation;
a mechanism to inject a miscible enhanced oil recovery formulation into the first well;
a second well in the formation; a mechanism to produce oil and/or gas from the second well; wherein the first well and the second well comprise an interior of the system; a plurality of containment wells exterior to the first well and the second well;
and a mechanism to inject a containment agent into the containment wells. In some embodiments, the first well is at a distance of 10 meters to 1 kilometer from the second well. In some embodiments, the underground formation is beneath a body of water. In some embodiments, the system also includes a mechanism for injecting an immiscible enhanced oil recovery formulation into the formation, after the miscible enhanced oil recovery formulation has been released into the formation. In some embodiments, the system also includes a miscible enhanced oil recovery formulation selected from the group consisting of a carbon disulfide formulation, hydrogen sulfide, carbon dioxide, octane, pentane, LPG, C2-C6 aliphatic hydrocarbons, nitrogen, diesel, mineral spirits, naptha solvent, asphalt solvent, kerosene, acetone, xylene, trichloroethane, and mixtures thereof. In some embodiments, the system also includes an immiscible enhanced oil recovery formulation selected from the group consisting of water in gas or liquid form, air, and mixtures thereof. In some embodiments, the system also includes a first array of wells comprising from 5 to 500 wells, and a second array of wells comprising from 5 to 500 wells. In some embodiments, the system also includes a miscible enhanced oil recovery formulation comprising a carbon disulfide formulation. In some embodiments, the system also includes a mechanism for producing a carbon disulfide formulation. In some embodiments, the underground formation comprises an oil having a viscosity from 100 to 5,000,000 centipoise. In some embodiments, the first well comprises a miscible enhanced oil recovery formulation profile in the formation, and the second well comprises an oil recovery profile in the formation, the system further comprising an overlap between the miscible enhanced oil recovery formulation profile and the oil recovery profile. In some embodiments, the containment agent is selected from the group consisting of a refrigerant, water, brine, peroxide, peroxide solutions, nitrogen, air, carbon dioxide, natural gas, other C1 - C15 hydrocarbons, and mixtures thereof.
In some embodiments, the containment agent comprises water. In some embodiments, the second well produces the containment agent. In some embodiments, the second well produces the containment agent, the miscible enhanced oil recovery formulation, and oil and/or gas.
In one embodiment of the invention, there is disclosed a method for producing oil and/or gas comprising injecting a carbon disulfide formulation into a formation from a first well; producing oil and/or gas from the formation from a second well;
and injecting a containment agent into the formation from a plurality of containment wells.
In some embodiments, the method also includes recovering carbon disulfide formulation from the oil and/or gas, if present, and then injecting at least a portion of the recovered carbon disulfide formulation into the formation. In some embodiments, injecting the carbon disulfide formulation comprises injecting at least a portion of the carbon disulfide formulation into the formation in a mixture with one or more of hydrocarbons; sulfur compounds other than carbon disulfide; carbon dioxide;
carbon monoxide; or mixtures thereof. In some embodiments, the method also includes heating the carbon disulfide formulation prior to injecting the carbon disulfide formulation into the formation, or while within the formation. In some embodiments, the carbon disulfide formulation is injected at a pressure from 0 to 37,000 kilopascals above the initial reservoir pressure, measured prior to when carbon disulfide injection begins. In some embodiments, the underground formation comprises a permeability from 0.0001 to 15 Darcies, for example a permeability from 0.001 to 1 Darcy.
In some embodiments, any oil, as present in the underground formation prior to the injecting the carbon disulfide formulation, has a sulfur content from 0.5% to 5%, for example from 1 % to 3%. In some embodiments, the method also includes converting at least a portion of the recovered oil and/or gas into a material selected from the group consisting of transportation fuels such as gasoline and diesel, heating fuel, lubricants, chemicals, and/or polymers.
In one embodiment of the invention, there is disclosed a method for producing oil and/or gas comprising injecting a miscible enhanced oil recovery formulation into a formation from a first well; producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from plurality of containment wells. In some embodiments, the method also includes injecting an immiscible enhanced oil recovery formulation after injecting the miscible enhanced oil recovery formulation, to push the miscible enhanced oil recovery formulation through the formation. In some embodiments, the miscible enhanced oil recovery formulation comprises a carbon disulfide formulation.
Those of skill in the art will appreciate that many modifications and variations are possible in terms of the disclosed embodiments of the invention, configurations, materials and methods without departing from their spirit and scope.
Accordingly, the scope of the claims appended hereafter and their functional equivalents should not be limited by particular embodiments described and illustrated herein, as these are merely exemplary in nature.
Claims (26)
1. A system for producing oil and/or gas from an underground formation comprising:
a first well in the formation;
a mechanism to inject a miscible enhanced oil recovery formulation into the first well;
a second well in the formation;
a mechanism to produce oil and/or gas from the second well;
wherein the first well and the second well comprise an interior of the system;
a plurality of containment wells exterior to the first well and the second well;
and a mechanism to inject a containment agent into the containment wells.
a first well in the formation;
a mechanism to inject a miscible enhanced oil recovery formulation into the first well;
a second well in the formation;
a mechanism to produce oil and/or gas from the second well;
wherein the first well and the second well comprise an interior of the system;
a plurality of containment wells exterior to the first well and the second well;
and a mechanism to inject a containment agent into the containment wells.
2. The system of claim 1, wherein the first well is at a distance of 10 meters to 1 kilometer from the second well.
3. The system of one or more of claims 1-2, wherein the underground formation is beneath a body of water.
4. The system of one or more of claims 1-3, further comprising a mechanism for injecting an immiscible enhanced oil recovery formulation into the formation, after the miscible enhanced oil recovery formulation has been released into the formation.
5. The system of one or more of claims 1-4, further comprising a miscible enhanced oil recovery formulation selected from the group consisting of a carbon disulfide formulation, hydrogen sulfide, carbon dioxide, octane, pentane, LPG, aliphatic hydrocarbons, nitrogen, diesel, mineral spirits, naptha solvent, asphalt solvent, kerosene, acetone, xylene, trichloroethane, and mixtures thereof.
6. The system of one or more of claims 1-5, further comprising an immiscible enhanced oil recovery formulation selected from the group consisting of water in gas or liquid form, air, and mixtures thereof.
7. The system of one or more of claims 1-6, further comprising a first array of wells comprising from 5 to 500 wells, and a second array of wells comprising from 5 to 500 wells.
8. The system of one or more of claims 1-7, further comprising a miscible enhanced oil recovery formulation comprising a carbon disulfide formulation.
9. The system of one or more of claims 1-8, further comprising a mechanism for producing a carbon disulfide formulation.
10. The system of one or more of claims 1-9, wherein the underground formation comprises an oil having a viscosity from 100 to 5,000,000 centipoise.
11. The system of one or more of claims 1-10, wherein the first well comprises a miscible enhanced oil recovery formulation profile in the formation, and the second well comprises an oil recovery profile in the formation, the system further comprising an overlap between the miscible enhanced oil recovery formulation profile and the oil recovery profile.
12. The system of one or more of claims 1-11, wherein the containment agent is selected from the group consisting of a refrigerant, water, brine, peroxide, peroxide solutions, nitrogen, air, carbon dioxide, natural gas, other C1-C15 hydrocarbons, and mixtures thereof.
13. The system of claim 12, wherein the containment agent comprises water.
14. The system of one or more of claims 1-13, wherein the second well produces the containment agent.
15. The system of one or more of claims 1-14, wherein the second well produces the containment agent, the miscible enhanced oil recovery formulation, and oil and/or gas.
16. A method for producing oil and/or gas comprising:
injecting a carbon disulfide formulation into a formation from a first well;
producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from a plurality of containment wells.
injecting a carbon disulfide formulation into a formation from a first well;
producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from a plurality of containment wells.
17. The method of claim 16, further comprising recovering carbon disulfide formulation from the oil and/or gas, if present, and then injecting at least a portion of the recovered carbon disulfide formulation into the formation.
18. The method of one or more of claims 16-17, wherein injecting the carbon disulfide formulation comprises injecting at least a portion of the carbon disulfide formulation into the formation in a mixture with one or more of hydrocarbons;
sulfur compounds other than carbon disulfide; carbon dioxide; carbon monoxide; or mixtures thereof.
sulfur compounds other than carbon disulfide; carbon dioxide; carbon monoxide; or mixtures thereof.
19. The methods of one or more of claims 16-18, further comprising heating the carbon disulfide formulation prior to injecting the carbon disulfide formulation into the formation, or while within the formation.
20. The method of one or more of claims 16-19, wherein the carbon disulfide formulation is injected at a pressure from 0 to 37,000 kilopascals above the initial reservoir pressure, measured prior to when carbon disulfide injection begins.
21. The method of one or more of claims 16-20, wherein the underground formation comprises a permeability from 0.0001 to 15 Darcies, for example a permeability from 0.001 to 1 Darcy.
22. The method of one or more of claims 16-21, wherein any oil, as present in the underground formation prior to the injecting the carbon disulfide formulation, has a sulfur content from 0.5% to 5%, for example from 1% to 3%.
23. The method of one or more of claims 16-22, further comprising converting at least a portion of the recovered oil and/or gas into a material selected from the group consisting of transportation fuels such as gasoline and diesel, heating fuel, lubricants, chemicals, and/or polymers.
24. A method for producing oil and/or gas comprising:
injecting a miscible enhanced oil recovery formulation into a formation from a first well;
producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from plurality of containment wells.
injecting a miscible enhanced oil recovery formulation into a formation from a first well;
producing oil and/or gas from the formation from a second well; and injecting a containment agent into the formation from plurality of containment wells.
25. The method of claim 24, further comprising:
injecting an immiscible enhanced oil recovery formulation after injecting the miscible enhanced oil recovery formulation, to push the miscible enhanced oil recovery formulation through the formation.
injecting an immiscible enhanced oil recovery formulation after injecting the miscible enhanced oil recovery formulation, to push the miscible enhanced oil recovery formulation through the formation.
26. The method of one or more of claims 24-25, wherein the miscible enhanced oil recovery formulation comprises a carbon disulfide formulation.
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| US61/080,405 | 2008-07-14 | ||
| PCT/US2009/050530 WO2010009118A1 (en) | 2008-07-14 | 2009-07-14 | Systems and methods for producing oil and/or gas |
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| CA2730284A1 true CA2730284A1 (en) | 2010-01-21 |
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| CA2761321C (en) * | 2011-02-11 | 2014-08-12 | Cenovus Energy, Inc. | Selective displacement of water in pressure communication with a hydrocarbon reservoir |
| CA2739953A1 (en) * | 2011-02-11 | 2012-08-11 | Cenovus Energy Inc. | Method for displacement of water from a porous and permeable formation |
| CN106545321B (en) * | 2015-09-18 | 2019-06-07 | 中国石油化工股份有限公司 | A kind of method and its application of the gravity auxiliary displacement of reservoir oil |
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- 2009-07-14 EP EP09798649A patent/EP2318651A1/en not_active Withdrawn
- 2009-07-14 US US13/054,416 patent/US20110180254A1/en not_active Abandoned
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- 2009-07-14 AU AU2009271072A patent/AU2009271072B2/en not_active Ceased
- 2009-07-14 WO PCT/US2009/050530 patent/WO2010009118A1/en active Application Filing
- 2009-07-14 MX MX2011000563A patent/MX2011000563A/en unknown
- 2009-07-14 RU RU2011105154/03A patent/RU2510454C2/en not_active IP Right Cessation
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| WO2010009118A1 (en) | 2010-01-21 |
| AU2009271072B2 (en) | 2012-10-11 |
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| AU2009271072A1 (en) | 2010-01-21 |
| CN102119258A (en) | 2011-07-06 |
| US20110180254A1 (en) | 2011-07-28 |
| RU2510454C2 (en) | 2014-03-27 |
| EP2318651A1 (en) | 2011-05-11 |
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