WO1997012119A1 - Procede modifie de drainage a commande continue - Google Patents
Procede modifie de drainage a commande continue Download PDFInfo
- Publication number
- WO1997012119A1 WO1997012119A1 PCT/US1995/012578 US9512578W WO9712119A1 WO 1997012119 A1 WO1997012119 A1 WO 1997012119A1 US 9512578 W US9512578 W US 9512578W WO 9712119 A1 WO9712119 A1 WO 9712119A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- wells
- array
- hydrocarbons
- formation
- fluid
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 73
- 230000008569 process Effects 0.000 title description 20
- 239000012530 fluid Substances 0.000 claims abstract description 85
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 71
- 238000004519 manufacturing process Methods 0.000 claims abstract description 65
- 238000002347 injection Methods 0.000 claims abstract description 59
- 239000007924 injection Substances 0.000 claims abstract description 59
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 47
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 46
- 238000004891 communication Methods 0.000 claims abstract description 36
- 230000001186 cumulative effect Effects 0.000 claims abstract description 21
- 230000005484 gravity Effects 0.000 claims description 8
- 230000001965 increasing effect Effects 0.000 claims description 5
- 238000005553 drilling Methods 0.000 claims description 4
- 230000004044 response Effects 0.000 claims description 4
- 230000024042 response to gravity Effects 0.000 claims 5
- 238000010438 heat treatment Methods 0.000 claims 3
- 230000001360 synchronised effect Effects 0.000 claims 1
- 238000010794 Cyclic Steam Stimulation Methods 0.000 description 39
- 238000005755 formation reaction Methods 0.000 description 36
- 239000010779 crude oil Substances 0.000 description 33
- 239000003921 oil Substances 0.000 description 18
- 238000010924 continuous production Methods 0.000 description 17
- 230000008901 benefit Effects 0.000 description 11
- 238000010793 Steam injection (oil industry) Methods 0.000 description 8
- 238000011084 recovery Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 241000245063 Primula Species 0.000 description 3
- 235000016311 Primula vulgaris Nutrition 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000010796 Steam-assisted gravity drainage Methods 0.000 description 2
- 239000008186 active pharmaceutical agent Substances 0.000 description 2
- 238000003491 array Methods 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000010408 sweeping Methods 0.000 description 2
- 229910021532 Calcite Inorganic materials 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 125000001183 hydrocarbyl group Chemical group 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000008450 motivation Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000013589 supplement 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
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
- E21B43/2406—Steam assisted gravity drainage [SAGD]
-
- 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
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
-
- 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
- E21B43/305—Specific pattern of wells, e.g. optimising the spacing of wells comprising at least one inclined or horizontal well
Definitions
- This invention relates to the general subject of methods for recovering hydrocarbons from subterranean formations, and in particular, to methods and processes for recovering heavy oil by means of injecting fluids into the formation.
- liquid hydrocarbons commonly known as crude oils
- Crude oils with an API gravity of 22 degrees or less are generally considered to be heavy crude oils.
- the market value of heavy crude oils has been traditionally lower than the value of lighter crude oils.
- hydrocarbon bearing formations can varying in physical composition from consolidated rock to unconsolidated sands, which may affect permeability and porosity.
- Natural layering and mixing of a variety of natural impermeable materials within a subterranean formation can also occur.
- the presence of diagenetic clay, or impermeable partial barriers such as mud or mud stone laminations, or calcite lenses within a subterranean formation may affect the ability of hydrocarbons to flow within the formation.
- the current state of the art reflects both an evolution of technology through general innovative improvement as well as innovation to meet conditions encountered in specific heavy crude, oil bearing subterranean formations.
- Keplinger, C.H. "Economic Considerations Affecting Steam Flood Prospects", Producers Monthly. Vol. 29, No. 5, May 1965, pp. 14- 20,
- the Ong Patent teaches either a gravity drainage effect, or a vertical or horizontal sweep of the oil within the reservoir.
- the Ong Patent teaches the injection of steam through horizontal injection wells located above horizontal production wells, at different pressures with the intention of creating a mild pressure drive to supplement gravity drainage of oil within the reservoir to lower production wells.
- the Brannan Patent teaches a method combining steam assisted gravity drainage and a significant vertical and horizontal sweeping of oil within the reservoir.
- the process and invention taught to the Ong Patent is intended to be applied to the production of oil from a reservoir where the oil is sufficiently immobile such that the reservoir is considered impermeable.
- the process and invention taught by the Brannan Patent is intended to be applied to the production of oil from a reservoir containing oil which is mobile to some extent within the reservoir prior to the application of such process and invention.
- the Brannan Patent teaches that the use of horizontal injection and production wells in a pattern where the horizontal sections of the wells are parallel but offset from one another in the vertical plane, with the horizontal section of the injection wells being placed in the reservoir above the horizontal sections of the production wells, with the horizontal sections of the production wells being drilled in the reservoir at a point between the base of the reservoir and the midpoint of the reservoir. Steam is injected on a continuous basis through the upper injection wells, while oil is produced through the lower production wells, at a rate which greater than the cumulative rate at which steam is injected into the upper horizontal wells.
- the Ong Patent teaches the initial and continuous injection of steam through the injection wells in the array, with the application of out of sync CSS to only the production wells in the array for the purpose of creating a permeable path between the injection wells and the production wells. Furthermore, the Ong Patent teaches that CSS may be applied to the production wells either out of sync or in sync, with no stated preferred method or any appreciation of any benefit of such an application.
- a method for producing hydrocarbons from a subterranean formation.
- the method comprises the steps of: (i) building an array of at least three horizontal wells, wherein the ho ⁇ zontal sections of all wells in the array are generally located in the bottom-half of the formation, are relatively parallel to one another, and are essentially horizontally co-planar with each other; (ii) establishing injectivity in the formation; (iii) creating thermal and pressure communication between adjacent wells in the array without inducing fractures in the formation; (iv) continuously injecting a fluid through the first outer well in the array; continuously producing hydrocarbons and associated fluids through the well immediately adjacent to such outer well; and (vi) simultaneously applying the steps of continuously injecting and continuously producing to adjacent remaining pairs of wells in the array so that each well in the array subject to continuous injection is offset only by wells subject to continuous production, wherein the hydrocarbons and associated fluids are produced at a cumulative rate of production such that a pressure differential is established between the wells in the array
- the present invention teaches the application of CSS to groups or arrays of three or more substantially coplanar and parallel horizontal wells, by conducting the injection phase, soak period and production phase of each well, "out of sync" with the wells located immediately adjacent to it in the array.
- the invention maximizes the benefits of using a heated fluid for injection purposes.
- the present invention also facilitates recovery of oil from the reservoir through the gravity drainage of oil within the reservoir in combination with the vertical and horizontal sweeping of such oil, as taught by the Brannan Patent, without the need to drill upper injection wells.
- a fluid such as steam, a solvent or a gas
- a fluid can be injected on a continuous basis while fluid is produced on a continuous basis from the formation following the method described in the first paragraph of this summary.
- the present invention teaches that, where the initial application of CSS is required to create thermal and pressure communication between injection and production wells in the array, it is preferable to apply CSS out of sync to both the injection and production wells in the array.
- a key advantage of the application of out of sync CSS to all wells in the array is that thermal and pressure communication between adjacent wells is established faster at a lower capital cost than if all wells were subject to each phase of the CSS process (i.e., injection, soak period and production) at the same time.
- the reservoir may be pressured-up and such pressurization maintained over the whole period of time that CSS is being applied.
- each well undergoing the fluid production phase of the CSS cycle can benefit from increased fluid production as a result of the pressure drive created by the injection of fluids from wells that are adjacent to it and that are undergoing the fluid injection phase of the cycle.
- the use of out of sync CSS as taught by the invention facilitates the use smaller capacity steam generation equipment, providing immediate economic benefits through reduction of capital costs.
- the present invention may be practiced as an alternative to the process and invention taught by the Brannan Patent. This would occur, for example, where the reservoir is characterized as having partial, non-continuous impermeable barriers which would hinder the vertical flow of fluids, or where the viscosity of the heavy crude oil within the reservoir may vary considerably over a large range.
- the preferred method of the present invention is to conduct CSS only in respect of horizontal wells where the horizontal section of each well is located in the lower half of the reservoir. This maximizes the efficiencies of using CSS by preventing the formation of a steam chamber that prematurely contacts the top of the reservoir. It also exposes a greater portion of the vertical cross section of the reservoir at the point of injection to the thermal effects of steam injection.
- Yet another advantage of the present invention is the savings of electrical power.
- the surface pumping equipment i.e., pumpjacks used to produce fluids from the wells
- a significant savings can be realized through the reduction in power usage resulting from not starting up and running the pumpjacks for all of the wells in the array at the same time.
- FIG. 1 shows by cross section the approximate geometry of the horizontal sections wells drilled as taught by U.S. 5,273,11 1 ;
- FIG. 2 shows by cross section the approximate geometry of the horizontal sections of the wells drilled as taught by the present invention
- FIG's. 3 and 4 show by cross section the development of a steam chamber around each horizontal well by the application of CSS in the case of the wells drilled as taught by U.S. 5,273,11 1 (FIG. 3) and as thought by the present invention (FIG. 4);
- FIG's. 5 and 6 show by cross section the application of CSI to the injection wells as taught by U.S. 5,273,11 1 (FIG. 5) and as thought by the present invention (FIG. 6), with continuous production from the production wells in both cases; and
- FIG's. 7 and 8 show by cross section the application of CSS to wells drilled in an array as taught by the present invention, with the injection/production phase for each well being out of sync with the wells adjacent to and offsetting such well.
- FIG. 2 illustrates an array consisting of at least three horizontal wells 10a, 10b and 10c is drilled into a formation 12 having a reservoir containing heavy crude oil.
- the formation 12 has a top 12t and a bottom 12b.
- These wells are drilled using means known in the art.
- the wells are drilled so that the horizontal section of each well is located between the bottom and midpoint of the reservoir.
- the wells are drilled so that the horizontal sections of all wells in the array are approximately equidistant, relatively parallel to one another, and horizontally coplanar with each other.
- the present invention allows for the horizontal section of the wells comprising the array to deviate from true parallel and true co-planar by as much as 5 meters.
- FIG. 1 of the present application corresponds to FIG. 1 of U.S. 5,273,11 1.
- the wells of FIG. 1 resemble the end points of the letter "W”. Spacing between the horizontal wells in the array of Brannan et al. is not specified and may be varied depending on the nature of the reservoir and the heavy crude oil contained therein.
- Continuous Steam Injection can begin with the outer wells 10a and 10c in the array being used as injectors and the inner or center well 10b being used to continuously produce heavy crude oil (See FIG. 6).
- the outer wells may be used for continuous production and the inner well may be used for CSI.
- the present invention facilitates both methods, with the choice of method being determined by the nature of the particular reservoir in which the process is applied, and the characteristics of the heavy crude oil contained therein.
- the main rule to follow in practicing the invention is that: while any well is adjacent to a particular well and is on continuous production of fluids, then the particular well in question must be used for continuous injection of fluids; and while any well is adjacent to a particular well and is being used for continuous fluid injection, the particular well in question must be used for continuous fluid production.
- steam is injected at pressures below the fracture pressure of the formation.
- the method also comprises Continuous Production (CP) occurring at a rate greater than the cumulative rate of CSI.
- CP Continuous Production
- every second well (i.e., the even-numbered wells) in the array is used as an injector during CSI, and the remaining wells (i.e., the odd-numbered wells or the wells "off-setting" the injectors) are used to continuously produce heavy crude oil.
- the remaining wells i.e., the odd-numbered wells or the wells "off-setting" the injectors.
- the present invention teaches the application of CSS to all wells in the array in the following described manner until such communication is established:
- CSS is applied simultaneously to all wells in the array using means that are known in the art, for at least one steam/production cycle to create voidage within the reservoir and provide sufficient injectivity. This causes the formation of steam chambers 14a, 14b and 14c (See FIG. 4) within the reservoir formation 12. Injection pressures are below reservoir fracture pressure. Depending on reservoir conditions and the nature of the heavy crude oil contained therein, further cycles of CSS may be required.
- CSS of all wells in the array continues with the steam injection and production cycle being applied to each well, "out of sync" with the well or wells adjacent to such well, so that while steam is being injected through a particular well, production is being taken from adjacent wells (See FIG's. 7 and 8).
- the vertical arrows denote the direction of fluid flow to and from the wells 10a, 10b and 10c.
- FIG. 7 the center well 10b is in the injection phase (steam being injected through such well).
- the wells 10a and 10c beside it are in the production phase (fluids being produced through such wells).
- FIG. 8 the situation is reversed.
- the reservoir may be pressured-up and pressurization maintained over the whole period of time that CSS is being applied.
- the wells in the array were cycled simultaneously (i.e., "in sync") between the injection and production phases, then, by the end of the production phase, the drop in reservoir pressure, from the level achieved at the end of the injection phase, would occur sooner and would be larger.
- all wells in the array were placed on the sar ⁇ e phase of CSS and cycled at the same time, clearly a much larger steam generator would be required. More importantly, one would not be able to build and maintain pressure in the reservoir.
- CSI and CP may be commenced with the wells in the array, in the manner described above (See FIG. 6).
- steam is injected into the two outer wells 10a and 10c at a pressure below the fracture pressure of the reservoir using conventional means known in the art.
- CP from the production well 10b is conducted at a rate greater than the cumulative rate of steam injection into the injection wells.
- One recommended minimum ratio for rate of injection to rate production is 1 to 1.5. However, the ratio can vary significantly depending on the nature of the reservoir, the native viscosity of the heavy crude oil and the type of fluid injected, as long as the rate of fluid production exceeds the rate of injection.
- additional horizontal wells may be drilled with the horizontal sections thereof being formed between, parallel to and co-planar with the horizontal sections of the existing wells in the array. Such additional wells would be utilized as either injectors for CSI or producers for CP as reservoir conditions require.
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- 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)
Abstract
La présente invention concerne un procédé de production d'hydrocarbures provenant d'une formation souterraine. Ce procédé comprend les étapes suivantes: constitution d'un ensemble d'au moins trois puits horizontaux (10a, 10b et 10c); établissement de l'injectivité dans la formation; établissement d'une communication entre des sections horizontales voisines de puits (10a, 10b et 10c) dans l'ensemble en question; injection d'un liquide par la partie horizontale d'un puits extérieur (10a) pendant la production d'hydrocarbures et de liquides associés par la section horizontale d'un puits (10b) immédiatement voisin du puits extérieur, avec exécution simultanée des opérations d'injection et de production pour des couples de puits (10b et 10c) restants voisins, dans l'ensemble précité, de telle sorte que, par rapport à tout puits particulier (10b) qu'on est en train d'utiliser pour l'injection de liquide, tout puits (10a et 10c) de cet ensemble qui en est immédiatement voisin est utilisé à ce moment pour la production de liquide. Avec ce procédé, les hydrocarbures et les liquides associés sont produits avec un débit cumulé, pour tout l'ensemble, qui établit une différence de pression entre les puits (10a, 10b et 10c) de l'ensemble.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
MX9603323A MX9603323A (es) | 1995-09-29 | 1995-09-29 | Proceso de drenaje por arrastre continuo modificado. |
PCT/US1995/012578 WO1997012119A1 (fr) | 1995-09-29 | 1995-09-29 | Procede modifie de drainage a commande continue |
US08/682,644 US5803171A (en) | 1995-09-29 | 1995-09-29 | Modified continuous drive drainage process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/US1995/012578 WO1997012119A1 (fr) | 1995-09-29 | 1995-09-29 | Procede modifie de drainage a commande continue |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1997012119A1 true WO1997012119A1 (fr) | 1997-04-03 |
Family
ID=22249876
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1995/012578 WO1997012119A1 (fr) | 1995-09-29 | 1995-09-29 | Procede modifie de drainage a commande continue |
Country Status (2)
Country | Link |
---|---|
MX (1) | MX9603323A (fr) |
WO (1) | WO1997012119A1 (fr) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2025862A1 (fr) * | 2007-08-17 | 2009-02-18 | Shell Internationale Research Maatschappij B.V. | Procédé pour l'amélioration de la récupération de pétrole brut lourd par la combustion in situ en présence d'aquifères forts |
WO2013075206A1 (fr) * | 2011-11-25 | 2013-05-30 | Archon Technologies Ltd. | Procédé de récupération de pétrole par balayage en ligne dans un puits horizontal |
US10012064B2 (en) | 2015-04-09 | 2018-07-03 | Highlands Natural Resources, Plc | Gas diverter for well and reservoir stimulation |
US10344204B2 (en) | 2015-04-09 | 2019-07-09 | Diversion Technologies, LLC | Gas diverter for well and reservoir stimulation |
US10982520B2 (en) | 2016-04-27 | 2021-04-20 | Highland Natural Resources, PLC | Gas diverter for well and reservoir stimulation |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4249777A (en) * | 1979-07-24 | 1981-02-10 | The United States Of America As Represented By The Secretary Of The Interior | Method of in situ mining |
US4598770A (en) * | 1984-10-25 | 1986-07-08 | Mobil Oil Corporation | Thermal recovery method for viscous oil |
US4850429A (en) * | 1987-12-21 | 1989-07-25 | Texaco Inc. | Recovering hydrocarbons with a triangular horizontal well pattern |
US5033546A (en) * | 1988-12-30 | 1991-07-23 | Institut Francais Du Petrole | Production simulation process by pilot test in a hydrocarbon deposit |
US5273111A (en) * | 1991-07-03 | 1993-12-28 | Amoco Corporation | Laterally and vertically staggered horizontal well hydrocarbon recovery method |
US5318124A (en) * | 1991-11-14 | 1994-06-07 | Pecten International Company | Recovering hydrocarbons from tar sand or heavy oil reservoirs |
-
1995
- 1995-09-29 WO PCT/US1995/012578 patent/WO1997012119A1/fr active Application Filing
- 1995-09-29 MX MX9603323A patent/MX9603323A/es not_active Application Discontinuation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4249777A (en) * | 1979-07-24 | 1981-02-10 | The United States Of America As Represented By The Secretary Of The Interior | Method of in situ mining |
US4598770A (en) * | 1984-10-25 | 1986-07-08 | Mobil Oil Corporation | Thermal recovery method for viscous oil |
US4850429A (en) * | 1987-12-21 | 1989-07-25 | Texaco Inc. | Recovering hydrocarbons with a triangular horizontal well pattern |
US5033546A (en) * | 1988-12-30 | 1991-07-23 | Institut Francais Du Petrole | Production simulation process by pilot test in a hydrocarbon deposit |
US5273111A (en) * | 1991-07-03 | 1993-12-28 | Amoco Corporation | Laterally and vertically staggered horizontal well hydrocarbon recovery method |
US5318124A (en) * | 1991-11-14 | 1994-06-07 | Pecten International Company | Recovering hydrocarbons from tar sand or heavy oil reservoirs |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2025862A1 (fr) * | 2007-08-17 | 2009-02-18 | Shell Internationale Research Maatschappij B.V. | Procédé pour l'amélioration de la récupération de pétrole brut lourd par la combustion in situ en présence d'aquifères forts |
WO2013075206A1 (fr) * | 2011-11-25 | 2013-05-30 | Archon Technologies Ltd. | Procédé de récupération de pétrole par balayage en ligne dans un puits horizontal |
US10012064B2 (en) | 2015-04-09 | 2018-07-03 | Highlands Natural Resources, Plc | Gas diverter for well and reservoir stimulation |
US10344204B2 (en) | 2015-04-09 | 2019-07-09 | Diversion Technologies, LLC | Gas diverter for well and reservoir stimulation |
US10385258B2 (en) | 2015-04-09 | 2019-08-20 | Highlands Natural Resources, Plc | Gas diverter for well and reservoir stimulation |
US10385257B2 (en) | 2015-04-09 | 2019-08-20 | Highands Natural Resources, PLC | Gas diverter for well and reservoir stimulation |
US10982520B2 (en) | 2016-04-27 | 2021-04-20 | Highland Natural Resources, PLC | Gas diverter for well and reservoir stimulation |
Also Published As
Publication number | Publication date |
---|---|
MX9603323A (es) | 1997-03-29 |
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