Patent Grant
8869891
The present disclosure relates to systems and methods for producing oil and/or gas.
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 practiced 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
U.S. Pat. No. 5,826,656 discloses a method for recovering waterflood residual oil from a waterflooded oil-bearing subterranean formation penetrated from an earth surface by at least one well by injecting an oil miscible solvent into a waterflood residual oil-bearing lower portion of the oil-bearing subterranean formation through a well completed for injection of the oil miscible solvent into the lower portion of the oil-bearing formation; continuing the injection of the oil miscible solvent into the lower portion of the oil-bearing formation for a period of time equal to at least one week; recompleting the well for production of quantities of the oil miscible solvent and quantities of waterflood residual oil from an upper portion of the oil-bearing formation; and producing quantities of the oil miscible solvent and waterflood residual oil from the upper portion of the oil-bearing formation. The formation may have previously been both waterflooded and oil miscible solvent flooded. The solvent may be injected through a horizontal well and solvent and oil may be recovered through a plurality of wells completed to produce oil and solvent from the upper portion of the oil-bearing formation. U.S. Pat. No. 5,826,656 is herein incorporated by reference in its entirety.
Co-pending U.S. Pat. No. 7,426,959, 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. Pat. No. 7,426,959 is herein incorporated by reference in its entirety.
WO International Publication Number 03/095118 A1 discloses methods of remediating carbon disulfide contaminated soil by contacting the soil with iron. WO International Publication Number 03/095118 A1 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. There is a further need in the art for improved systems and methods for recovering a solvent after miscible flooding. There is a need in the art for remediation of a formation after a miscible solvent flooding operation.
In one aspect, the invention provides a system for producing oil and/or gas from an underground formation comprising a first array of wells dispersed above the formation; a second array of wells dispersed above the formation; wherein the first array of wells comprises a mechanism to inject a miscible enhanced oil recovery formulation into the formation while the second array of wells comprises a mechanism to produce oil and/or gas from the formation for a first time period; and a means to convert at least a portion of the miscible enhanced oil recovery formulation within the formation into another compound during a second time period.
In another aspect, the invention provides a method for producing oil and/or gas comprising injecting a carbon disulfide formulation into a formation for a first time period from a first well; producing oil and/or gas from the formation from a second well for the first time period; and converting at least a portion of the carbon disulfide formulation into another compound in situ at a conclusion of the producing oil and/or gas from the formation.
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 may be miscible with oil in place.
Improved systems and methods for recovering a compound which may be miscible with oil in place.
Improved systems and methods for remediation of a formation which has been flooded with a compound which may be miscible with oil in place
a illustrates a well pattern.
b and 2c illustrate the well pattern of
a-3c illustrate oil and/or gas production systems.
a:
Referring now to
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.
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.
Each well in well group 202 may be surrounded by four wells in well group 204. Each well in well group 204 may be surrounded by four wells in well group 202.
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.
Vertical distance 232 may be 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.
Horizontal distance 236 may be 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.
Vertical distance 238 may be 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.
Distance 234 may be 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.
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.
Array of wells 200 may be seen as a top view with well group 202 and well group 204 being vertical wells spaced on a piece of land. Array of wells 200 may be 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.
b:
Referring now to
In some embodiments, a miscible enhanced oil recovery agent may be injected into well group 204, and oil may be 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.
A miscible enhanced oil recovery agent may be injected into well group 202, and oil may be 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.
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.
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 may be injecting and the other may be producing for a first time period, and then they are switched for a second time period.
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. 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.
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. 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.
c:
Referring now to
A miscible enhanced oil recovery agent may be injected into well group 204, and oil may be 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.
A miscible enhanced oil recovery agent may be injected into well group 202, and oil may be 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 order to recover miscible enhanced oil recovery agent from injection profile 206 back to well group 202, a remediation agent may be injected into well group 204, after the oil recovery from well group 204 has been completed. Suitable remediation agents are discussed below.
In order to clean the formation after a miscible oil flood, the miscible enhanced oil recovery agent may be converted in situ within injection profile 206 into another compound. Suitable methods for the conversion of the miscible enhanced oil recovery agent are discussed below.
a and 3b:
Referring now to
After the soaking period, as shown in
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.
Well 312, as shown in
Well 312, as shown in
In order to recover miscible enhanced oil recovery agent from formation 306 back to well 312, a remediation agent may be injected into another adjacent well (not shown), after the oil recovery from formation 306 has been completed. Suitable remediation agents are discussed below.
In order to clean the formation after a miscible oil flood, the miscible enhanced oil recovery agent may be converted in situ within formation 306 into another compound. Suitable methods for the conversion of the miscible enhanced oil recovery agent are discussed below.
c:
Referring now to
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 may be representative of a well in well group 202, and well 432 which is being used to inject miscible enhanced oil recovery formulation may be representative of a well in well group 204.
In some embodiments, well 412 which is producing oil and/or gas may be representative of a well in well group 204, and well 432 which is being used to inject miscible enhanced oil recovery formulation may be representative of a well in well group 202.
In order to recover miscible enhanced oil recovery agent from formation 406 back to well 432, a remediation agent may be injected into well 412, after the oil recovery from formation 406 and well 412 has been completed. Suitable remediation agents are discussed below.
In order to clean the formation after a miscible oil flood, the miscible enhanced oil recovery agent may be converted in situ within formation 406 into another compound. Suitable methods for the conversion of the miscible enhanced oil recovery agent are discussed below.
Remediation Agents:
Suitable remediation agents include water in liquid or vapor form, foams, aqueous surfactant solutions, aqueous polymer solutions, carbon dioxide, natural gas, and/or other hydrocarbons, and mixtures thereof.
In one embodiment, suitable remediation agents include aqueous surfactant solutions. Suitable aqueous surfactant solutions are disclosed in U.S. Pat. Nos. 3,943,160; 3,946,812; 4,077,471; 4,216,079; 5,318,709; 5,723,423; 6,022,834; 6,269,881; and by Wellington, et al. in “Low Surfactant Concentration Enhanced Waterflooding,” Society of Petroleum Engineers, 1995; all of which are incorporated by reference herein.
As discussed above, a remediation agent may be introduced into the formation after the completion of the miscible solvent flooding process in order to produce as much of the miscible solvent as possible.
In situ Conversion
In some embodiments, any miscible solvent remaining within the formation after the completion of the enhanced oil recovery operation, and after an optional remediation agent flooding operation, may be converted in situ (within the formation) into a different compound.
Iron Sulfide Formation:
In one example, the miscible solvent may include a carbon disulfide formulation. The carbon disulfide may be hydrolyzed within the formation into hydrogen sulfide, for example by the addition of oxygen, water, steam, peroxides, and/or heat. Optionally, one or more catalysts such as alumina and/or titania, for example in a solution, as a powder, or as a suspension in water or other fluids may be introduced into the formation in order to catalyze the reaction from carbon disulfide to hydrogen sulfide.
The hydrogen sulfide may then react with iron, iron oxide, and/or other iron containing compounds within the formation in order to form iron sulfides such as pyrite.
The carbon disulfide can be converted to hydrogen sulfide by any reaction or mechanism. The selection of the reaction or mechanism is not critical. One suitable mechanism by which the carbon disulfide is hydrolyzed to hydrogen sulfide is a known reaction, which has the formula:
CS2+2H2O→2H2S+CO2 (Formula 1)
The hydrogen sulfide can be converted to iron sulfide by any reaction or mechanism. The selection of the reaction or mechanism is not critical. One suitable mechanism by which the hydrogen sulfide is converted to iron sulfides is a known reaction, which has the formula:
4H2S+Fe2O3+½O2→2 FeS2+4H2O (Formula 2)
In order to speed up the conversion of the hydrogen sulfide to iron sulfide, heat may be added, excess oxygen may be added, and suitable catalysts may be introduced to the formation.
Oxidation Reactions:
In one example, the miscible solvent may include an alcohol and/or hydrocarbon such as natural gas, propane, butane, and/or pentane. The miscible solvent may be burned in place within the formation into primarily water and carbon dioxide, for example by the addition of oxygen, steam, peroxides, and/or heat.
In another example, the miscible solvent may include a carbon disulfide formulation. The carbon disulfide may be combusted or oxidized within the formation into sulfur dioxide, for example by the addition of oxygen, peroxides, and/or heat.
The carbon disulfide can be oxidized by any reaction or mechanism. The selection of the reaction or mechanism is not critical. One suitable mechanism by which the carbon disulfide is oxidized to sulfur dioxide is a known reaction, which has the formula:
CS2+3O2→2SO2+CO2 (Formula 3)
The sulfur dioxide may then be stored within the formation, recovered from one or more wells, and/or converted into one or more other compounds.
Sulfur Formation:
In one example, the miscible solvent may include a carbon disulfide formulation. A portion of the carbon disulfide may be combusted or oxidized within the formation into sulfur dioxide, for example by the addition of oxygen, peroxides, and/or heat, as described above. Another portion of the carbon disulfide may be hydrolyzed within the formation, for example by the addition of water, steam, and/or heat, as described above.
The carbon disulfide can be converted to sulfur by any reaction or mechanism. The selection of the reaction or mechanism is not critical. One suitable mechanism by which the sulfur is formed is a known Claus reaction, which has the formula:
SO2+2H2S→2H2O+3S (Formula 4)
The sulfur may then be stored within the formation, recovered from one or more wells, and/or converted into one or more other compounds
The sulfur forming reaction speed may be increased with the addition of heat and one or more catalysts such as alumina, bauxite, cobalt-molybdenum and/or titania.
Alternative Embodiments:
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 U.S. Pat. No. 7,426,959, which is herein incorporated by reference in its entirety.
In some embodiments, suitable miscible enhanced oil recovery agents include carbon disulfide, hydrogen sulfide, carbon dioxide, octane, pentane, LPG, C2-C6 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, 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.
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 Publication No. US2004/0146288, published Jul. 29, 2004, which is herein incorporated by reference in its entirety.
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 produced 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 array of wells dispersed above the formation; a second array of wells dispersed above the formation; wherein the first array of wells comprises a mechanism to inject a miscible enhanced oil recovery formulation into the formation while the second array of wells comprises a mechanism to produce oil and/or gas from the formation for a first time period; and a means to convert at least a portion of the miscible enhanced oil recovery formulation within the formation into another compound during a second time period. In some embodiments, a well in the first array of wells is at a distance of 10 meters to 1 kilometer from one or more adjacent wells in the second array of wells. 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 first array of wells comprises from 5 to 500 wells, and the second array of wells comprises 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 array of wells comprises a miscible enhanced oil recovery formulation profile in the formation, and the second array of wells 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 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 for a first time period from a first well; producing oil and/or gas from the formation from a second well for the first time period; and converting at least a portion of the carbon disulfide formulation into another compound in situ at a conclusion of the producing oil and/or gas from the formation. 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 some embodiments, the method also includes injecting a remediation agent into the formation for a second time period from the second well; and producing the carbon disulfide formulation from the formation from the first well for the second time period. In some embodiments, the remediation agent comprises water and a surfactant. In some embodiments, the remediation agent comprises water and a polymer dissolved in the water. In some embodiments, the method also includes injecting water into the formation for a third time period from the first well; and producing the remediation agent from the formation from the second well for the third time period.
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 for a first time period from a first well; producing oil and/or gas from the formation from a second well for the first time period; and converting at least a portion of the miscible enhanced oil recovery formulation into another compound within the formation after a conclusion of the producing oil and/or gas from the formation. In some embodiments, the method also includes injecting an immiscible enhanced oil recovery formulation into the formation for a time period after the first time period from the first well, to push the miscible enhanced oil recovery formulation through the formation. In some embodiments, the produced oil and/or gas comprises a sulfur compound, further comprising converting at least a portion of the sulfur compound into a miscible enhanced oil recovery formulation. In some embodiments, the miscible enhanced oil recovery formulation comprises a carbon disulfide formulation. In some embodiments, the method also includes heating the miscible enhanced oil recovery formulation. In some embodiments, the method also includes injecting a remediation agent into the formation for a second time period from the second well; and producing the miscible enhanced oil recovery formulation from the formation from the first well for the second time period. In some embodiments, the remediation agent comprises water and a surfactant. In some embodiments, the method also includes injecting water into the formation for a time period after the second time period from the second well, to push the remediation agent through the formation.
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.
The present application claims priority of U.S. Provisional Patent Application No. 60/988,845 filed 19 Nov. 2007.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US2008/083845 | 11/18/2008 | WO | 00 | 7/27/2010 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2009/067420 | 5/28/2009 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 2330934 | Thacker | Oct 1943 | A |
| 2492719 | Thacker | Dec 1949 | A |
| 2636810 | Marisic | Apr 1953 | A |
| 2670801 | Sherborne | Mar 1954 | A |
| 3087788 | Porter | Apr 1963 | A |
| 3250595 | Olsen | May 1966 | A |
| 3345135 | Kerr et al. | Oct 1967 | A |
| 3366452 | Lauer | Jan 1968 | A |
| 3393733 | Kuo et al. | Jul 1968 | A |
| 3402768 | Felsenthal et al. | Sep 1968 | A |
| 3498378 | Stone et al. | Mar 1970 | A |
| 3581821 | Ross | Jun 1971 | A |
| 3647906 | Farley | Mar 1972 | A |
| 3672448 | Hoyt | Jun 1972 | A |
| 3724552 | Snavely | Apr 1973 | A |
| 3724553 | Snavely, Jr. et al. | Apr 1973 | A |
| 3729053 | Froning | Apr 1973 | A |
| 3732166 | Lissant | May 1973 | A |
| 3754598 | Holloway, Jr. | Aug 1973 | A |
| 3794114 | Brandon | Feb 1974 | A |
| 3805892 | Haynes, Jr. | Apr 1974 | A |
| 3822748 | Allen et al. | Jul 1974 | A |
| 3823777 | Allen et al. | Jul 1974 | A |
| 3838738 | Redford et al. | Oct 1974 | A |
| 3840073 | Allen et al. | Oct 1974 | A |
| 3847221 | Allen et al. | Nov 1974 | A |
| 3850245 | Allen et al. | Nov 1974 | A |
| 3878892 | Allen et al. | Apr 1975 | A |
| 3927185 | Meadow et al. | Dec 1975 | A |
| 3943160 | Farmer, III et al. | Mar 1976 | A |
| 3946812 | Gale et al. | Mar 1976 | A |
| 4008764 | Allen | Feb 1977 | A |
| 4057613 | Meadow et al. | Nov 1977 | A |
| 4077471 | Shupe et al. | Mar 1978 | A |
| 4122156 | Kittrell et al. | Oct 1978 | A |
| 4166501 | Korstad et al. | Sep 1979 | A |
| 4182416 | Trantham et al. | Jan 1980 | A |
| 4216079 | Newcombe | Aug 1980 | A |
| 4305463 | Zakiewicz | Dec 1981 | A |
| 4330038 | Soukup et al. | May 1982 | A |
| 4375238 | Parsons | Mar 1983 | A |
| 4393937 | Dilgren et al. | Jul 1983 | A |
| 4465138 | Hunt, III | Aug 1984 | A |
| 4476113 | Young et al. | Oct 1984 | A |
| 4488976 | Dilgren et al. | Dec 1984 | A |
| 4543434 | Chang | Sep 1985 | A |
| 4550779 | Zakiewicz | Nov 1985 | A |
| 4558740 | Yellig, Jr. | Dec 1985 | A |
| 4727937 | Shum et al. | Mar 1988 | A |
| 4822938 | Audeh et al. | Apr 1989 | A |
| 4963340 | Audeh et al. | Oct 1990 | A |
| 4974677 | Shu | Dec 1990 | A |
| 5014784 | Shen | May 1991 | A |
| 5062970 | Muijs et al. | Nov 1991 | A |
| 5065821 | Huang et al. | Nov 1991 | A |
| 5076358 | Kissel | Dec 1991 | A |
| 5120935 | Nenniger | Jun 1992 | A |
| 5167280 | Sanchez et al. | Dec 1992 | A |
| 5318709 | Wuest et al. | Jun 1994 | A |
| 5325920 | Djabbarah | Jul 1994 | A |
| 5358565 | Shu | Oct 1994 | A |
| 5363915 | Marquis et al. | Nov 1994 | A |
| 5607016 | Butler | Mar 1997 | A |
| 5609845 | Cimini et al. | Mar 1997 | A |
| 5723423 | Van Slyke | Mar 1998 | A |
| 5803171 | McCaffery et al. | Sep 1998 | A |
| 5826656 | McGuire et al. | Oct 1998 | A |
| 6022834 | Hsu et al. | Feb 2000 | A |
| 6136282 | Fisher | Oct 2000 | A |
| 6149344 | Eaton | Nov 2000 | A |
| 6241019 | Davidson et al. | Jun 2001 | B1 |
| 6269881 | Chou et al. | Aug 2001 | B1 |
| 6405797 | Davidson et al. | Jun 2002 | B2 |
| 6497855 | Wachs | Dec 2002 | B1 |
| 6506349 | Khanmamedov | Jan 2003 | B1 |
| 6706108 | Polston | Mar 2004 | B2 |
| 6851473 | Davidson | Feb 2005 | B2 |
| 6893620 | Watson et al. | May 2005 | B2 |
| 6918442 | Wellington et al. | Jul 2005 | B2 |
| 6919059 | Watson et al. | Jul 2005 | B2 |
| 6919296 | Geus et al. | Jul 2005 | B2 |
| 6946111 | Keller et al. | Sep 2005 | B2 |
| 7025134 | Byrd et al. | Apr 2006 | B2 |
| 7090818 | Stauffer | Aug 2006 | B2 |
| 7128150 | Thomas et al. | Oct 2006 | B2 |
| 7426959 | Wang et al. | Sep 2008 | B2 |
| 7601320 | Van Dorp et al. | Oct 2009 | B2 |
| 7654322 | Wang et al. | Feb 2010 | B2 |
| 7717171 | Stegemeier et al. | May 2010 | B2 |
| 7730947 | Stegemeier et al. | Jun 2010 | B2 |
| 7866385 | Lambirth | Jan 2011 | B2 |
| 7866386 | Beer et al. | Jan 2011 | B2 |
| 20020195250 | Underdown et al. | Dec 2002 | A1 |
| 20030194366 | Srinivas et al. | Oct 2003 | A1 |
| 20040146288 | Vinegar et al. | Jul 2004 | A1 |
| 20040159583 | Mesters et al. | Aug 2004 | A1 |
| 20050189108 | Davidson | Sep 2005 | A1 |
| 20060254769 | Wang et al. | Nov 2006 | A1 |
| 20070251686 | Sivrikoz et al. | Nov 2007 | A1 |
| 20080023198 | Hsu | Jan 2008 | A1 |
| 20080087425 | Hsu et al. | Apr 2008 | A1 |
| 20080142216 | Vinegar et al. | Jun 2008 | A1 |
| 20080217003 | Kuhlman et al. | Sep 2008 | A1 |
| 20090200022 | Bravo et al. | Aug 2009 | A1 |
| 20090200023 | Costello et al. | Aug 2009 | A1 |
| 20100258265 | Karanikas et al. | Oct 2010 | A1 |
| Number | Date | Country |
|---|---|---|
| 738784 | Jul 1966 | CA |
| 581026 | Feb 1994 | EP |
| 1007674 | Oct 1965 | GB |
| 2379685 | Mar 2003 | GB |
| WO9619638 | Jun 1996 | WO |
| WO9850679 | Nov 1998 | WO |
| WO03095118 | Nov 2003 | WO |
| WO2007013177 | Nov 2007 | WO |
| WO2007127766 | Nov 2007 | WO |
| WO2007131976 | Nov 2007 | WO |
| WO2007131977 | Nov 2007 | WO |
| WO2008003732 | Jan 2008 | WO |
| WO2008034777 | Mar 2008 | WO |
| Entry |
|---|
| Carbon Disulfide, “4.Production, Import, Use, and Disposal”, XP007908050, pp. 119-125, Jun. 29, 2001. |
| Wellington, et al.: Low Surfactant Concentration Enhanced Waterflooding, Society of Petroleum Engineers, SPE Annual Technical Conference & Exhibition, Dallas, Oct. 22-25, 1995, published SPE 30748, SPE Jrnl., vol. 2, Dec. 1997. |
| Number | Date | Country | |
|---|---|---|---|
| 20100307759 A1 | Dec 2010 | US |
| Number | Date | Country | |
|---|---|---|---|
| 60988845 | Nov 2007 | US |
