|Número de publicación||US3759328 A|
|Tipo de publicación||Concesión|
|Fecha de publicación||18 Sep 1973|
|Fecha de presentación||11 May 1972|
|Fecha de prioridad||11 May 1972|
|Número de publicación||US 3759328 A, US 3759328A, US-A-3759328, US3759328 A, US3759328A|
|Inventores||Brew J, Ueber R, Van Meurs P|
|Cesionario original||Shell Oil Co|
|Exportar cita||BiBTeX, EndNote, RefMan|
|Citas de patentes (9), Citada por (189), Clasificaciones (14)|
|Enlaces externos: USPTO, Cesión de USPTO, Espacenet|
United States Patent [1 1 Ueber et al.
[111 3,759,328 [4 1 Sept. 18, 1973 LATERALLY EXPANDING OIL SHALE PERMEABILIZATION  Inventors: Russell C. Ueber; Peter Van Meurs;
. Jerke R. Brew, all of Houston, Tex.
 Assignee: Shell Oil Company, Houston, Tex.
 Filed: May 11, 1972  Appl. No.: 252,448
Related US. Application Data  Continuatiomin-part of Ser. No. 57,209, July 22,
Primary Examiner-Stephen J. Novosad Attorney-H. L. Denkler et al.
[5 7] ABSTRACT An improved process of permeabilizing and recovering water soluble and/or heat sensitive minerals and hydrocarbons from an oil shale formation containing said minerals by forming a cavern and vertically expanding it by contacting the cavern roof with a hot aqueous fluid while also causing horizontal expansion of the cavern by contacting the oil shale therein with the same or different hot aqueous fluid at a relatively shallow depth and flowing down along a vertical section while dissolving said minerals and rubbling the oil' shale and producing from a relatively deep location in the cavern an aqueous liquid containing dissolved minerals therein and subsequently or simultaneously injecting a pyrolyzing fluid into the rubbled oil shale cavern to effect pyrolysis of the oil shale and recovery of hydrocarbons therefrom.
6 Claims, 3 Drawing Figures INFLOWING HOT '4 FLUID HORIZONTAL EXPANSION VERTICAL FLUID Patented Sept. 18, 1973 3,759,328
OUTFLOWING INFLOWING HOT COOL FLUID I INFLOWING I INERT LIGHT FLUID FLU'D HOT FLUID FLUID OUTFLOWING COOL I I5 I I I I I VERTICAL l EXPANSION INFLOWING OUT- OUTFLOWING STEAM FLOWING LIQUID INVENTORS:
RUSSELL C. UEBER PETER VAN MEURS JERE R. BREW LATERALLY EXPANDING OIL SHALE PERMEABILIZATION CROSS REFERENCES TO RELATED APPLICATIONS This application is a continuation-in-part of copending patent application Ser. No. 57,209 filed July 22, 1970, now abandoned.
BACKGROUND OF THE INVENTION The present invention relates to production of hydrocarbons and/or water soluble and/or heat sensitive minerals from underground oil shale formations by controlled circulation of a hot aqueous fluid through said oil shale formation so as to vertically and horizontally expand a permeable zone of rubbled oil shale within said formation by leaching and recovering said miner als from a relatively deep location within the treated area of the formation and thereafter injecting a pyrolyzing fluid into the rubbled oil shale to effect pyrolysis and recovery of hydrocarbons therefrom.
Various methods have been proposed for imparting permeability to underground oil shale formations such as fracturing by hydraulic or explosive means and/or acidization but they have proven to be ineffective and- /or too expensive to use. Thus, oil shale formations which have been fractured on subsequent pyrolysis with pyrolyzing fluid to effect oil recovery, such fractures tend to close unless high pyrolyzing fluid circulation pressures at least equal to the overburden pressure, are maintained and this is difficult to do. Acidizato control.
SUMMARY OF THE INVENTION The present invention is directed to an improved method of recovering hydrocarbons and water-soluble carbonates and/or heat sensitive materials from underground oil shale formations containing substantial amounts of said carbonate and/or minerals by forming a cavern therein by leaching with an aqueous fluid said carbonates and/or minerals and imparting permeability while effecting rubbling of the oil shale in said treated area by contacting and flowing a hot aqueous fluid downward from a relatively shallow depth along a vertical interval of said treated oil shale to cause horizontal expansion and-recovering from a relatively deep depth an aqueous liquid containing dissolved therein watersoluble'carbonates and/or heat sensitive minerals and subsequently injecting a pyrolyzing fluid or solvent to effect recovery of hydrocarbons from the rubbled oil shale.
DESCRIPTION OF THE DRAWING FIG. 1 is a vertical section showing a subterranean oil shale and downhole equipment for practicing the present invention.
FIG. 2 is a schematic illustration of a flow path for circulating fluid in accordance with the present invention.
FIG. 3 is a vertical section showing an alternative arrangement of downhole equipment of the type shown in FIG. 1.
DESCRIPTION OF THE INVENTION The present invention is in part premised on a discovery that, in a cavern in an oil shale that contains a significant amount of heat sensitive minerals and/or water soluble carbonates a hot aqueous fluid can be caused to flow along a path that causes a horizontal expansion of the cavern. In a cavern within such an oil shale, the rate at which a hot aqueous fluid is segregated into layers having increasing densities, has been found to be related to the rate at which heat can be transferred into the walls of the cavern in a manner conducive to the establishing and maintaining of the flow path described above, and the resultant heating and leaching along substantially vertical portions of the walls of such a cavern has been found to cause a horizontal expansionof the cavern.
The term cavern is used to refer to any relatively solids free opening, such asa cave, void, tunnel, borehole, or interconnected fractures, etc., in which the rate of gravity segregation of fluids is not significantly impeded by a lack of permeability.
In the present process, the fluid circulation and cavern expansion operations can be initiated by opening at least a single well into an interval of oil shale that contains heat sensitive minerals and/or water soluble carbonates, inflowing hot fluid into contact with an upper portion of the borehole wall, flowing the hot fluid down along the borehole wall, and removing liquid containing dissolved minerals and/or water-soluble carbonates from a lower portion of the borehole. Alternatively, a plurality of wells can be used to provide flow paths into a horizontally extensive cavern in or adjacent to oil shale that contains heat sensitive minerals and/or water-soluble carbonates and the wells and the cavern can be utilized to cause a concurrent horizontal and vertical expansion of a permeable zone by inflowing hot aqueous fluid into contact with a upper portion of such oil shale, flowing fluid downward along a vertical interval of such oil shale, flowing fluid horizontally along the roof of the cavern, and removing liquid containing dissolved minerals and/or water-soluble carbonates from within the cavern.
As used herein, the term heat sensitive and/or water-soluble carbonate refers to materials that decompose relatively rapidly at a relatively low temperature, such as one between about 250 F to about 700 F to yield carbon dioxide and water. Examples of heat sensitive carbonate minerals include nahcolite, dawsonite, trona, and the like minerals, which are usually inclusive of saline carbonate and/or bicarbonate molecular structures or moities.
In a preferred embodiment of the present invention, a borehole is drilled into a relatively low-lying portion of oil shale which contains or is adjacent to a layer or region that is relatively rich in water soluble mineral.
Such water soluble minerals (generally saline minerals) are frequently encountered in oil shale formations in the United States, such as the Green River formation in Colorado, in the form of beds, lenses, nodules, nodes, veins or the like. Examples of such water soluble minerals include the alkali metal chloride salts such as halite minerals and/or water soluble heat sensitive carbonate minerals such as nahcolite, trona, or the like.
The locations of portions of subterranean oil shales which contain specific mineral components, such as heat sensitive carbonate minerals and/or water soluble minerals, can be determined by means of known geological investigation procedures and equipment. In a preferred embodiment of the present invention, geological investigation procedures are utilized to locate a portion of oil shale that contains heat sensitive carbonate mineral and is underlain by a portion or layer that contains water soluble mineral. The water soluble mineral is solution mined or leached for example, by means of a process of the type described in copending patent application Ser. No. 770,964; filed Oct. 28, 1968, now abandoned, and Ser. No. 860,349; filed Sept. 23, 1969, now abandoned. Those applications describe procedures for utilizing a water soluble mineral-rich portion of an oil shale to form a cavern that can be expanded before or during the recovery of shale oil from the oil shale exposed in and around the cavern. Such a solution mined cavern in or adjacent to an oil shale that contains heat sensitive carbonate mineral can advantageously be utilized as a horizontally extensive cavern that is expanded vertically during the horizontal expansion of a vertically extensive cavernous zone, such as a section of a borehole.
Referring to the drawing, FIG. 1 shows a portion of a well borehole 1 which has been drilled through an overburden 2, comprising successively shallower earth formations, and opened into an oil shale formation 3 that contains a heat sensitive carbonate mineral. The oil shale formation that is placed in fluid communication with a portion of the borehole to be used in practicing the present invention, should be a formation containing a significant proportion, e.g., greater than 5 percent by weight, of heat sensitive carbonate mineral. Borehole 1 is equipped with a string of casing 4, which is bonded to the surrounding earth formations by cement 5.
Separate conduits for conveying fluids between a surface location and, respectively, relatively shallow and relatively deep depths within the oil shale are provided by tubing strings 7 and 8. Alternatively, such conduits may comprise two or more parallel strings of tubing and may be located in two or more well boreholes that intersect or extend into a common cavern within the oilshale. Such conduits can be installed and equipped by means of known procedures and devices and heat insulation (not shown) is preferably installed around at least those of such conduits that are used for the inflowing of hot fluid.
As indicated by FIG. 1, the vertically extensive cavern or opening that is expanded by the present process can comprise the borehole of a well that extends into an interval of oil shale that contains heat sensitive carbonatematerial. Such an interval preferably has a vertical thickness of at least about 100 feet. In the initial stages, such a borehole may have a generally cylindrical form, such as indicated by the dotted line 1a, and may comprise a relatively slender, generally vertical cavern within the oil shale. In operating the process with the equipment shown in FIG. 1, a hot aqueous fluid is flowed into contact with the wall of the cavern by inflowing hot aqueous gas and/or liquid through the annulus within pipe 8 (i.e., the space between pipes 7 and 8) and through adjacent perforations 6 at a relatively shallow depth within the carbonate mineralcontaining portion of the oil shale. The inflowing fluid such as hot water and/or steam flows downward along the face of the vertical interval of oil shale (along the wall of the borehole) and decomposes and dissolves the heat sensitive carbonate mineral material. The dissolving of water soluble material forms a liquid solution 9. This solution, which is usually mixed with at least some gas, such as carbon dioxide and gaseous hydrocarbon,
is out-flowed through pipe 7, which extends to a relatively low level within the borehole. The decomposing and dissolving of carbonate mineral components of the oil shale causes the spalling and caving in of particles 10 of the oil shale and causes a generally horizontal expansion of a rubble-containing cavernous zone of permeability within the oil shale.
Where the oil shale being treated contains a significant proportion of a mineral, such as a halite, which is water soluble in its natural form, the inflowing of hot aqueous fluid can advantageously be preceded by a circulation of aqueous liquid at a relatively low temperature, such as the wellhead temperature, the temperature of the source of the liquid or the like. In such a pretreatment, the circulating liquid may leach out significant portions of distributed layers or particles of the soluble mineral. This increases the surface area of exposed oil shale and/or weakens the support for layers or chunks of the oil shale. such a pretreatment circulation can advantageously be continued while the rate of dissolution is high, e.g., as indicated by the proportion of solute in the outflowing liquid. The so-circulated aqueous liquid can then be gradually or rapidly heated to the temperature selected for the inflowing hot aqueous liquid used to decompose heat sensitive carbonate material, with or without an interruption of the flow through the cavern.
When necessary or desirable the vertical expansion of the cavern can be inhibited by spotting and maintaining a relatively light and cool fluid 13 along the roof of the cavern. Such a fluid is preferably a gas and can in inflowed, or maintained substantially stationary, in and around the annulus within casing 4 (i.e., the space between pipe 8 and casing 4) and the upper portion of borehole 1 (below cement 5) to extend along the roof of the horizontally expanding cavern as the walls of the cavern more radially outward to and beyond the location shown at 1b.
The hot aqueous fluid used in the present cavernenlarging procedure is preferably steam, hot aqueous liquid (hot water) or a mixture of such fluids. The hot fluid is preferably inflowed at a temperature, e.g., at least about 250 F, that is significantly higher than the normal temperature of the subterranean oil shale formation. The heat transported by such a hot fluid converts the heat sensitive carbonate material to carbon dioxide and water vapor within portions of the normally impermeable oil shale matrix. Such a generation of gas causes localized fracturing and/or spalling of the oil shale.
The aqueous liquid component of the inflowing hot fluid dissolves water soluble mineral material and creates additional solid-free void space. This occurs along most, if not all, of the vertical extent of the flow path used in the present process. The spalling and dissolution causes a horizontal expansion of a rubblecontaining cavern. The inflowing hot aqueous fluid can comprise super heated, dry, or wet steam, or a mixture of such a steam with substantially any gas vapor or liquid, such as carbon dioxide, phenols, hydrocarbons, alcohols, halogenated hydrocarbons, acids, or the like, or with substantially any aqueous solution, such as an aqueous acid or base or solution or neutral salt. Where the inflowing fluid is substantially completely gaseous it should contain sufficient steam to provide a significant amount of aqueous liquid as it condenses within.
The inflowing hot aqueous fluid can be heated by means of surface located and/or downhole located, steam generators, water heaters, or the like. Alternatively, or additionally, such heating can be effected or supplemented in an insitu combustion within the oil shale formation. The temperature of the inflowing hot aqueous fluid can range from about 250? F to one sufficient to cause a relatively rapid oil shale pyrolysis, e.g., a temperature of from about 600 to 1000F.
The inflowing aqueous liquid phase of the hot aqueous fluid dissolves naturally water soluble minerals such as nahcolite, trona, halite, or the like, and/or water soluble decomposition products from a heat sensitive carbonate material, such as nahcolite, etc., to create solid-free space within the oil shale. Various water soluble minerals, such as nahocolite (NaI-ICO may dissolve prior to any thermal decomposition, if the pressure is sufficiently high at the temperature of the inflowing fluid. Alternatively, such minerals may be partially or wholly decomposed to gaseous fluids and sodium carbonate before dissolution.
Although the portion of oil shale formation which is treated in accordance with the present invention must contain a significant amount of heat sensitive carbonate material, it may contain sections, or vertical intervals of as much as several tens of feet thick, which are substantially devoid of heat sensitive and/or water soluble minerals. In such heterogeneous regions, the heat sensitive or soluble minerals are converted or dissolved and removed. Portions of the so-converted oil shale materials become incompetent and break into pieces under the existing local stress field. Such pieces, or chunks, of oil shale mineral materials tend to accumulate on top of ledges of oil shale that contains little or no heat sensitive or soluble material. The accumulation of weight from such chunks, together with the existing stress field, cause such ledges to break into pieces and fall to a lower level. The action of converting kerogen into shale oil materials such as gaseous and liquid hydrocarbons enhances such an operation and, where the oil shale is relatively lean with respect to heat sensitive and soluble materials, the use of hot aqueous fluid heat to a kerogen-pyrolyzing temperature is desirable. Also hydrocarbons can be extracted from the rubbled oil shale by solvent means such as by use of phenols, aromatic solvents, e.g., benzene, xylene, etc.
Due to mechanisms such as those mentioned above, the application of the present process causes a generally vertical cavernous zone to grow in a horizontal direction. The rate of growth will vary depending upon the heat sensitive and water soluble mineral content of the particular zone. The outer boundary of the zone will generally be very irregular with portions extending several tens of feet further than others. In order to enhance horizontal growth while injecting a hot aqueous fluid that is predominantly liquid, it is generally desirable to maintain most or all of the rubble-containing cavern full of liquid. Alternatively, when the injected hot aqueous fluid is steam, it is generally preferably to keep much of the rubble-containing kerogen filled with steam and/or gas.
A particularly suitable arrangement of flow paths to be used in the present process is shown in FIG. 2. At least two horizontally separated wells are opened into a region of oil shale that contains heat sensitive carbonate mineral and is located immediately above a layer or zone of oil shale or other earth formation material that is rich in water soluble mineral and/or heat sensitive carbonate mineral. Such wells are used to form an inflow path 14 and an outflow path 15 that are interconnected by a path extending through an areally extensive cavern 6. As indicated by the arrows, hot aqueous fluid is inflowed into contact with oil shale containing heat sensitive carbonate material at a relatively shallow depth, flowed down along a vertical section of such oil shale, flowed along the roof of a horizontally extensive cavern within such oil shale, and, liquid containing dissolved mineral material is removed from within the horizontally extensive cavern. Such a horizontally extensive cavern can advantageously be formed by means of mechanical fracturing, and/or solution mining techniques, for example, by one or more of such techniques described in the above mentioned copending patent applications.
A principle advantage of a flow path of the type shown in FIG. 2 is the heat economy and the fact that much larger volumes of oil shale can be rubbled per unit time than could be achieved by either a horizontal or vertical rubbling by itself. Relative to horizontal rubbling from a single well, the concurrent vertical and horizontal rubbling is capable of providing much higher oil production rates, particularly in the early stages of the process. Such a flow path can be utilized to produce a relatively cool fluid with much of the produced hydrocarbon and injected fluid being outflowed in the liquid phase. I I
A flow path of the type shown in FIG. 2 can be initiated between one or more pairs of wells. Initial communication is preferably achieved by fracturing or dissolving within the layer of water soluble material until fluid injected in one well can be produced from another. Hot aqueous fluid is then injected at the top of an injected well and fluid is produced from within a generally horizontal cavern or flow path through a production well. The upper portion of the injection well will enlarge laterally and the lower portion or rubble-containing cavern will enlarge vertically so that the permeable zone is expanded both laterally and vertically. It is in the lower region of the rubble-containing cavern that heat improvements are made. With such a flow path, the inflowing fluid preferably has a temperature below one at which the pyrolysis of kerogen is rapid. Where it is desired to rubble large volumes of oil shale while removing solid materials and preheating the shale for later pyrolysis, such a use of a relatively low temperature results in significant heat economy. If communication between different patterns of injection and production wells is desired the depth of the location from which liquid is produced can be kept relatively deep within the soluble layer so that the circulating fluid will containue to enlarge the areal extent of the dissolved zone.
Where communication between different well patterns is not desired, the production point and production rate can be adjusted to leave a substantially saturated liquid solution in the soluble layer in order to prevent its further growth.
Such a versatility with respect to the size and shape of the cavernous zones that are formed before and/or during a recovery of shale oil is a unique advantage of the present process. For example, where the oil shale is thick, large amounts of shale oil can be recovered from a series of zones that are vertically extensive but are horizontally spaced so that problems due to subsidence are avoided. For example, wells in a plurality of horizontally separated patterns that each contain one or more wells opening into a layer rich in water soluble minerals can be operated as described in connection with FIG. 2 to form horizontally expanding permeable zones and produce shale oil. The sizes of the permeable zones can be monitored by means of acoustic, electromagnetic the like measurements of the extents of the substantially void space and/or measurements of the volume of fluids that are contained into caverns. The horizontal expansion of the caverns can be controlled to provide an efficient recovery of oil from nonintersecting, generally vertically extensive zones that are spaced so that undisturbed columns capable of supporting the overburden are left between the depleted zones.
During the initial stages of expanding a rubblecontaining cavern in accordance with the present process, it is not necessary and is generally undesirable to use a temperature high enough to decompose a predominant proportion of the fluid-contacted heat sensitive carbonate material. It is preferable to keep the cavern substantially full of aqueous liquid in which the carbonate material is soluble. This tends to provide the best heat economy since it minimizes the decomposition reaction (which is an endothermic reaction that comsumes heat). In order to keep the cavern substantially filled with aqueous liquid it is preferable to maintain the pressure within the cavern above the decomposition pressure of the heat sensitive carbonate material at the temperature within the cavern. In general the pressure within the cavern cannot be kept high enough to prevent such a decomposition during an oil recovering stage. The retorting and hydrocarbon recovery is preferably conducted at a temperature above about 500 F, and at the depths at which oil shale is usually encountered, the pressure in the cavern cannot be high enough to prevent decomposition of heat sensitive carbonate material at such a temperature, without a danger of creating large scale fractures which are extended into locations in which fractures are undesirable.
When one or a plurality of generally vertically extensive permeable zones have been expanded horizontally to substantially the extent desired, the circulation of fluid within throne zones or caverns is preferably adjusted to minimize the rate of horizontal growth and/or maximize the rate of oil recovery. Such an adjustment can be effected by increasing the temperature and/or decreasing the aqueous liquid content of the fluid within the cavern. A higher temperature tends to increase the rate of oil recovery (particularly with respect to the gaseous components of shale oil). Altematively, a decrease in the aqueous liquid content tends to reduce the rate of dissolution of soluble mineral. Where the removal of solid material from the oil shale is confined to a removal of the fluid products of the pyrolysis reaction and/or the CO and water vapor produced by the decomposition of heat sensitive carbonates, the volume of the depleted oil shale tends to be sufficient, relative to the volume of solids that are removed, to terminate the growth of the permeable zone (unless the oil shale is one that contains an exceptionally large proportion of heat sensitive carbonate mineral). The aqueous liquid content of the fluid within the cavern can be reduced by, for example, circulating substantially dry steam, or a mixture of a dry steam and e. g., carbon dioxide, at a rate and temperature at which the outflowing fluid is predominately gaseous and the aqueous liquid lift within the cavern contains a relatively high proportion of inert inorganic solute.
FIG. 3 shows downhole equipment of the type shown in FIG. 1 arranged to effect a downhole separation of the gaseous and liquid phases of the fluid being produced. Particularly when the concentration of heat sensitive carbonate material is relatively high, and/or the temperature of the inflowing hot aqueous fluid is relatively high, a significant amount of gaseous carbon dioxide and water will be formed. However, to the extent that it is feasible, it is desirable to produce a relatively cool liquid phase fluid that contains a significant proportion of produced shale oil hydrocarbon. In the arrangement shown in FIG. 3, borehole 20 is equipped with pipe strings 21, 22 and 23. Some or all of such pipes are preferably thermally insulated, as indicated by coatings 24 on pipes 21 and 22. Pipe 21, through which the hot aqueous fluid is inflowed, opens into the borehole at a relatively shallow depth. Pipe 22 extends to an intermediate depth and is used to outflow fluid that is relatively cool but is predominately gaseous. Pipe 23 extends to a relatively deep depth, is preferably equipped with downhole pumping means (not shown), and is used to outflow fluid that is predominately liquid. The vertical section of borehole between the ends of pipes 22 and 23 serves as a downhole gravity of separation chamber.
Steam or a mixture of steam and hot aqueous liquid (hot water) is inflowed through pipe 21. The inflowing hottest and lightest gas tends to remain above the cooler and heavier gas and in situ generated carbon dioxide. The cooler gases outflow through pipe 22 while the hotter and lighter inflowing gases tend to flow along the walls of the cavern. Where desirable a relatively light and cool gas, such as methane, hydrogen, etc., can be maintained substantially static, or slowly injected, through and around the upper portion of the borehole and cavern.
Once the rubbled oil shale cavern has been established and the heat sensitive minerals and water-soluble carbonates removed as an aqueous solution, the hydrocarbons (oil) can be recovered by suitable means such as by contacting the rubbled oil shale within the cavern with a pyrolyzing fluid to effect decomposition of the kerogens to hydrocarbon which is removed from the formation. .In recovering the hydrocarbons, the pyrolyzing fluid can be injected (FIG. 1) via 7 and recovered via tubing 8 visa versa and in a dual sytem as shown in FIG. 3 the pyrolyzing fluid such as steam can be injected via tubing string 21 and the hydrocarbons recovered via 22 or the process can be reversed.
It is understood that various changes in the detailed described to explain the invention can be made by per sons skilled in the art within the scope of the invention as expressed in the appended claims.
I claim as my invention: 7 1. In a process for expanding a zone of permeability within a subterranean oil shale by forming a permeable zone within a portion that contains heat sensitive carbonate mineral and circulating hot aqueous fluid within the permeable zone, the improvement which comprises:
inflowing hot aqueous fluid into contact with a subterranean portion of oil shale that contains heat sensitive carbonate mineral at a relatively shallow depth, the temperature of said inflowing fluid being high enough to pyrolyze oil shale;
flowing hot aqueous fluid downward along a vertically extensive portion of oil shale that contains heat sensitive carbonate mineral, from said relatively shallow depth to a deeper depth;
outflowing an aqueous solution of mineral material from a relatively deep depth, in order to cause a horizontal expansion of rubble-containing cavemous zone within said oil shale;
adjusting the rate of said fluid inflows and outflows so as to keep a substantial proportion of the rubble containing cavern filled with fluid; and recovering shale oil with said outflowing fluid.
2. In a process for expanding a zone of permeability within a subterranean oil shale by forming a cavern within a portion-that contains heat sensitive carbonate mineral and circulating hot aqueous fluid within the cavern, the improvement which comprises:
inflowing hot aqueous fluid into contact with a subterranean portion of oil shale that contains heat sensitive carbonate mineral at a relatively shallow depth, the temperature of said inflowing fluid being high enough to pyrolyze oil shale; flowing hot aqueous fluid downward along a vertically extensive portion of oil shale that contains heat sensitive carbonate mineral, from said relatively shallow depth to a deeper depth;
outflowing an aqueous solution of mineral material from a relatively deep depth, in order to cause a horizontal expansion of a rubble-containing cavernous zone within said oil shale;
outflowing a substantially gaseous fluid from the rubble-containing cavern at an intermediate depth between the depth of said inflow of hot aqueous fluid and said outflow of aqueous liquid solution; and recovering shale oil with said outflowing fluid.
3. In a process for expanding a zone of permeability within a subterranean oil shale by forming a cavern within a portion that contains heat sensitive carbonate mineral and circulating hot aqueous fluid within the cavern, the improvement which comprises:
inflowing hot aqueous fluid into contact with a subterranean portion of oil shale that contains heat sensitive carbonate mineral at a relatively shallow depth, the temperature of said inflowing fluid being high enough to pyrolyze oil shale;
flowing a mixture of a hot aqueous fluid, gaseous carbon dioxide and hydrocarbon downward along a vertically extensive portion of oil shale that contains heat sensitive carbonate mineral, from said relatively shallow depth to a deeper depth;
outflowing an aqueous solution of mineral material from a relatively deep depth, in order to cause a horizontal expansion of a rubble-containing cavernous zone within said oil shale; and
recovering shale oil with said outflowing fluid.
4. A process of expanding a fluid permeable opening within a subterranean oil shale formation, comprising:
establishing separate paths of fluid communication between a surface location and upper and lower portions of a relatively solids-free opening within a subterranean oil shale formation that contains heat sensitive carbonate material;
inflowing relatively hot and relatively low density aqueous fluid into contact with the oil shale around the upper portion of said opening at a temperature sufiicient to cause a localized removal of solid material from the oil shale;
removing cooler and heavier fluid from the lower portion of the opening within said oil shale formation at a rate correlated with the rate of fluid inflow to maintain a layer of relatively hot and low density aqueous fluid above a layer of relatively cooler and higher density aqueous solution of mineral material; and
continuing said fluid circulation to cause a generally horizontal expansion of the opening within said oil shale formation due to a decomposition dissolution of solid components of the oil shale.
5. The process of claim 4 in which said subterranean oil shale formation contains at least about 5 percent by weight of heat sensitive carbonate material.
6. The process of claim 4 in which:
said solids-free opening and at least one of said paths of fluid communication is extended into an areally extensive opening within an adjacent underlying zone that is rich in water soluble mineral; and said fluid circulation is adjusted to cause a generally vertical expansion of said underlying opening concurrent with said generally horizontal expansion.
|Patente citada||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US2969226 *||19 Ene 1959||24 Ene 1961||Pyrochem Corp||Pendant parting petro pyrolysis process|
|US2979317 *||12 Ago 1959||11 Abr 1961||Fmc Corp||Solution mining of trona|
|US3050290 *||30 Oct 1959||21 Ago 1962||Fmc Corp||Method of recovering sodium values by solution mining of trona|
|US3309140 *||28 Nov 1962||14 Mar 1967||Utah Construction & Mining Co||Leaching of uranium ore in situ|
|US3405974 *||21 Feb 1966||15 Oct 1968||Intermountain Res & Dev Corp||Process of underground salt recovery|
|US3455383 *||24 Abr 1968||15 Jul 1969||Shell Oil Co||Method of producing fluidized material from a subterranean formation|
|US3501201 *||30 Oct 1968||17 Mar 1970||Shell Oil Co||Method of producing shale oil from a subterranean oil shale formation|
|US3516495 *||29 Nov 1967||23 Jun 1970||Exxon Research Engineering Co||Recovery of shale oil|
|US3572838 *||7 Jul 1969||30 Mar 1971||Shell Oil Co||Recovery of aluminum compounds and oil from oil shale formations|
|Patente citante||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US3880238 *||18 Jul 1974||29 Abr 1975||Shell Oil Co||Solvent/non-solvent pyrolysis of subterranean oil shale|
|US3888307 *||29 Ago 1974||10 Jun 1975||Shell Oil Co||Heating through fractures to expand a shale oil pyrolyzing cavern|
|US4026360 *||12 Ago 1976||31 May 1977||Shell Oil Company||Hydrothermally forming a flow barrier in a leached subterranean oil shale formation|
|US4059308 *||15 Nov 1976||22 Nov 1977||Trw Inc.||Pressure swing recovery system for oil shale deposits|
|US4065183 *||15 Nov 1976||27 Dic 1977||Trw Inc.||Recovery system for oil shale deposits|
|US4083604 *||15 Nov 1976||11 Abr 1978||Trw Inc.||Thermomechanical fracture for recovery system in oil shale deposits|
|US4545891 *||30 Mar 1982||8 Oct 1985||Trw Inc.||Extraction and upgrading of fossil fuels using fused caustic and acid solutions|
|US4688637 *||27 Feb 1987||25 Ago 1987||Theis Ralph W||Method for induced flow recovery of shallow crude oil deposits|
|US4815790 *||13 May 1988||28 Mar 1989||Natec, Ltd.||Nahcolite solution mining process|
|US5059307 *||11 Oct 1989||22 Oct 1991||Trw Inc.||Process for upgrading coal|
|US5085764 *||19 Dic 1989||4 Feb 1992||Trw Inc.||Process for upgrading coal|
|US5588713 *||20 Dic 1995||31 Dic 1996||Stevenson; Tom D.||Process for making sodium bicarbonate from Nahcolite-rich solutions|
|US7040397||24 Abr 2002||9 May 2006||Shell Oil Company||Thermal processing of an oil shale formation to increase permeability of the formation|
|US7100994 *||24 Oct 2002||5 Sep 2006||Shell Oil Company||Producing hydrocarbons and non-hydrocarbon containing materials when treating a hydrocarbon containing formation|
|US7207395||30 Ene 2004||24 Abr 2007||Cdx Gas, Llc||Method and system for testing a partially formed hydrocarbon well for evaluation and well planning refinement|
|US7222670||27 Feb 2004||29 May 2007||Cdx Gas, Llc||System and method for multiple wells from a common surface location|
|US7264048||21 Abr 2003||4 Sep 2007||Cdx Gas, Llc||Slot cavity|
|US7360595 *||8 May 2002||22 Abr 2008||Cdx Gas, Llc||Method and system for underground treatment of materials|
|US7571771||31 May 2005||11 Ago 2009||Cdx Gas, Llc||Cavity well system|
|US7640987||17 Ago 2005||5 Ene 2010||Halliburton Energy Services, Inc.||Communicating fluids with a heated-fluid generation system|
|US7644765||19 Oct 2007||12 Ene 2010||Shell Oil Company||Heating tar sands formations while controlling pressure|
|US7644993||22 Mar 2007||12 Ene 2010||Exxonmobil Upstream Research Company||In situ co-development of oil shale with mineral recovery|
|US7673681||19 Oct 2007||9 Mar 2010||Shell Oil Company||Treating tar sands formations with karsted zones|
|US7673786||20 Abr 2007||9 Mar 2010||Shell Oil Company||Welding shield for coupling heaters|
|US7677310||19 Oct 2007||16 Mar 2010||Shell Oil Company||Creating and maintaining a gas cap in tar sands formations|
|US7677314||19 Oct 2007||16 Mar 2010||Shell Oil Company||Method of condensing vaporized water in situ to treat tar sands formations|
|US7681647||19 Oct 2007||23 Mar 2010||Shell Oil Company||Method of producing drive fluid in situ in tar sands formations|
|US7683296||20 Abr 2007||23 Mar 2010||Shell Oil Company||Adjusting alloy compositions for selected properties in temperature limited heaters|
|US7703513||19 Oct 2007||27 Abr 2010||Shell Oil Company||Wax barrier for use with in situ processes for treating formations|
|US7717171||19 Oct 2007||18 May 2010||Shell Oil Company||Moving hydrocarbons through portions of tar sands formations with a fluid|
|US7730945||19 Oct 2007||8 Jun 2010||Shell Oil Company||Using geothermal energy to heat a portion of a formation for an in situ heat treatment process|
|US7730946||19 Oct 2007||8 Jun 2010||Shell Oil Company||Treating tar sands formations with dolomite|
|US7730947||19 Oct 2007||8 Jun 2010||Shell Oil Company||Creating fluid injectivity in tar sands formations|
|US7735935||1 Jun 2007||15 Jun 2010||Shell Oil Company||In situ thermal processing of an oil shale formation containing carbonate minerals|
|US7770643||10 Oct 2006||10 Ago 2010||Halliburton Energy Services, Inc.||Hydrocarbon recovery using fluids|
|US7785427||20 Abr 2007||31 Ago 2010||Shell Oil Company||High strength alloys|
|US7793722||20 Abr 2007||14 Sep 2010||Shell Oil Company||Non-ferromagnetic overburden casing|
|US7798220||18 Abr 2008||21 Sep 2010||Shell Oil Company||In situ heat treatment of a tar sands formation after drive process treatment|
|US7798221||31 May 2007||21 Sep 2010||Shell Oil Company||In situ recovery from a hydrocarbon containing formation|
|US7809538||13 Ene 2006||5 Oct 2010||Halliburton Energy Services, Inc.||Real time monitoring and control of thermal recovery operations for heavy oil reservoirs|
|US7831134||21 Abr 2006||9 Nov 2010||Shell Oil Company||Grouped exposed metal heaters|
|US7832482||10 Oct 2006||16 Nov 2010||Halliburton Energy Services, Inc.||Producing resources using steam injection|
|US7832484||18 Abr 2008||16 Nov 2010||Shell Oil Company||Molten salt as a heat transfer fluid for heating a subsurface formation|
|US7841401||19 Oct 2007||30 Nov 2010||Shell Oil Company||Gas injection to inhibit migration during an in situ heat treatment process|
|US7841408||18 Abr 2008||30 Nov 2010||Shell Oil Company||In situ heat treatment from multiple layers of a tar sands formation|
|US7841425||18 Abr 2008||30 Nov 2010||Shell Oil Company||Drilling subsurface wellbores with cutting structures|
|US7845411||19 Oct 2007||7 Dic 2010||Shell Oil Company||In situ heat treatment process utilizing a closed loop heating system|
|US7849922||18 Abr 2008||14 Dic 2010||Shell Oil Company||In situ recovery from residually heated sections in a hydrocarbon containing formation|
|US7860377||21 Abr 2006||28 Dic 2010||Shell Oil Company||Subsurface connection methods for subsurface heaters|
|US7866385||20 Abr 2007||11 Ene 2011||Shell Oil Company||Power systems utilizing the heat of produced formation fluid|
|US7866386||13 Oct 2008||11 Ene 2011||Shell Oil Company||In situ oxidation of subsurface formations|
|US7866388||13 Oct 2008||11 Ene 2011||Shell Oil Company||High temperature methods for forming oxidizer fuel|
|US7912358||20 Abr 2007||22 Mar 2011||Shell Oil Company||Alternate energy source usage for in situ heat treatment processes|
|US7931086||18 Abr 2008||26 Abr 2011||Shell Oil Company||Heating systems for heating subsurface formations|
|US7942197||21 Abr 2006||17 May 2011||Shell Oil Company||Methods and systems for producing fluid from an in situ conversion process|
|US7942203||4 Ene 2010||17 May 2011||Shell Oil Company||Thermal processes for subsurface formations|
|US7950453||18 Abr 2008||31 May 2011||Shell Oil Company||Downhole burner systems and methods for heating subsurface formations|
|US7986869||21 Abr 2006||26 Jul 2011||Shell Oil Company||Varying properties along lengths of temperature limited heaters|
|US8011451||13 Oct 2008||6 Sep 2011||Shell Oil Company||Ranging methods for developing wellbores in subsurface formations|
|US8027571||21 Abr 2006||27 Sep 2011||Shell Oil Company||In situ conversion process systems utilizing wellbores in at least two regions of a formation|
|US8042610||18 Abr 2008||25 Oct 2011||Shell Oil Company||Parallel heater system for subsurface formations|
|US8070840||21 Abr 2006||6 Dic 2011||Shell Oil Company||Treatment of gas from an in situ conversion process|
|US8082995||14 Nov 2008||27 Dic 2011||Exxonmobil Upstream Research Company||Optimization of untreated oil shale geometry to control subsidence|
|US8083813||20 Abr 2007||27 Dic 2011||Shell Oil Company||Methods of producing transportation fuel|
|US8087460||7 Mar 2008||3 Ene 2012||Exxonmobil Upstream Research Company||Granular electrical connections for in situ formation heating|
|US8104537||15 Dic 2009||31 Ene 2012||Exxonmobil Upstream Research Company||Method of developing subsurface freeze zone|
|US8113272||13 Oct 2008||14 Feb 2012||Shell Oil Company||Three-phase heaters with common overburden sections for heating subsurface formations|
|US8122955||18 Abr 2008||28 Feb 2012||Exxonmobil Upstream Research Company||Downhole burners for in situ conversion of organic-rich rock formations|
|US8146661||13 Oct 2008||3 Abr 2012||Shell Oil Company||Cryogenic treatment of gas|
|US8146664||21 May 2008||3 Abr 2012||Exxonmobil Upstream Research Company||Utilization of low BTU gas generated during in situ heating of organic-rich rock|
|US8146669||13 Oct 2008||3 Abr 2012||Shell Oil Company||Multi-step heater deployment in a subsurface formation|
|US8151877||18 Abr 2008||10 Abr 2012||Exxonmobil Upstream Research Company||Downhole burner wells for in situ conversion of organic-rich rock formations|
|US8151880||9 Dic 2010||10 Abr 2012||Shell Oil Company||Methods of making transportation fuel|
|US8151884||10 Oct 2007||10 Abr 2012||Exxonmobil Upstream Research Company||Combined development of oil shale by in situ heating with a deeper hydrocarbon resource|
|US8151907||10 Abr 2009||10 Abr 2012||Shell Oil Company||Dual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations|
|US8162059||13 Oct 2008||24 Abr 2012||Shell Oil Company||Induction heaters used to heat subsurface formations|
|US8162405||10 Abr 2009||24 Abr 2012||Shell Oil Company||Using tunnels for treating subsurface hydrocarbon containing formations|
|US8172335||10 Abr 2009||8 May 2012||Shell Oil Company||Electrical current flow between tunnels for use in heating subsurface hydrocarbon containing formations|
|US8177305||10 Abr 2009||15 May 2012||Shell Oil Company||Heater connections in mines and tunnels for use in treating subsurface hydrocarbon containing formations|
|US8191630||28 Abr 2010||5 Jun 2012||Shell Oil Company||Creating fluid injectivity in tar sands formations|
|US8192682||26 Abr 2010||5 Jun 2012||Shell Oil Company||High strength alloys|
|US8196658||13 Oct 2008||12 Jun 2012||Shell Oil Company||Irregular spacing of heat sources for treating hydrocarbon containing formations|
|US8200072||24 Oct 2003||12 Jun 2012||Shell Oil Company||Temperature limited heaters for heating subsurface formations or wellbores|
|US8220539||9 Oct 2009||17 Jul 2012||Shell Oil Company||Controlling hydrogen pressure in self-regulating nuclear reactors used to treat a subsurface formation|
|US8224163||24 Oct 2003||17 Jul 2012||Shell Oil Company||Variable frequency temperature limited heaters|
|US8224164||24 Oct 2003||17 Jul 2012||Shell Oil Company||Insulated conductor temperature limited heaters|
|US8224165||21 Abr 2006||17 Jul 2012||Shell Oil Company||Temperature limited heater utilizing non-ferromagnetic conductor|
|US8225866||21 Jul 2010||24 Jul 2012||Shell Oil Company||In situ recovery from a hydrocarbon containing formation|
|US8230927||16 May 2011||31 Jul 2012||Shell Oil Company||Methods and systems for producing fluid from an in situ conversion process|
|US8230929||17 Mar 2009||31 Jul 2012||Exxonmobil Upstream Research Company||Methods of producing hydrocarbons for substantially constant composition gas generation|
|US8233782||29 Sep 2010||31 Jul 2012||Shell Oil Company||Grouped exposed metal heaters|
|US8238730||24 Oct 2003||7 Ago 2012||Shell Oil Company||High voltage temperature limited heaters|
|US8240774||13 Oct 2008||14 Ago 2012||Shell Oil Company||Solution mining and in situ treatment of nahcolite beds|
|US8256512||9 Oct 2009||4 Sep 2012||Shell Oil Company||Movable heaters for treating subsurface hydrocarbon containing formations|
|US8261832||9 Oct 2009||11 Sep 2012||Shell Oil Company||Heating subsurface formations with fluids|
|US8267170||9 Oct 2009||18 Sep 2012||Shell Oil Company||Offset barrier wells in subsurface formations|
|US8267185||9 Oct 2009||18 Sep 2012||Shell Oil Company||Circulated heated transfer fluid systems used to treat a subsurface formation|
|US8272455||13 Oct 2008||25 Sep 2012||Shell Oil Company||Methods for forming wellbores in heated formations|
|US8276661||13 Oct 2008||2 Oct 2012||Shell Oil Company||Heating subsurface formations by oxidizing fuel on a fuel carrier|
|US8281861||9 Oct 2009||9 Oct 2012||Shell Oil Company||Circulated heated transfer fluid heating of subsurface hydrocarbon formations|
|US8291974||31 Oct 2007||23 Oct 2012||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8297350||31 Oct 2007||30 Oct 2012||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface|
|US8297377||29 Jul 2003||30 Oct 2012||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8316966||31 Oct 2007||27 Nov 2012||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8327681||18 Abr 2008||11 Dic 2012||Shell Oil Company||Wellbore manufacturing processes for in situ heat treatment processes|
|US8327932||9 Abr 2010||11 Dic 2012||Shell Oil Company||Recovering energy from a subsurface formation|
|US8333245||17 Sep 2002||18 Dic 2012||Vitruvian Exploration, Llc||Accelerated production of gas from a subterranean zone|
|US8353347||9 Oct 2009||15 Ene 2013||Shell Oil Company||Deployment of insulated conductors for treating subsurface formations|
|US8355623||22 Abr 2005||15 Ene 2013||Shell Oil Company||Temperature limited heaters with high power factors|
|US8371399||31 Oct 2007||12 Feb 2013||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8376039||21 Nov 2008||19 Feb 2013||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8376052||1 Nov 2001||19 Feb 2013||Vitruvian Exploration, Llc||Method and system for surface production of gas from a subterranean zone|
|US8381815||18 Abr 2008||26 Feb 2013||Shell Oil Company||Production from multiple zones of a tar sands formation|
|US8434555||9 Abr 2010||7 May 2013||Shell Oil Company||Irregular pattern treatment of a subsurface formation|
|US8434568||22 Jul 2005||7 May 2013||Vitruvian Exploration, Llc||Method and system for circulating fluid in a well system|
|US8448707||9 Abr 2010||28 May 2013||Shell Oil Company||Non-conducting heater casings|
|US8459359||18 Abr 2008||11 Jun 2013||Shell Oil Company||Treating nahcolite containing formations and saline zones|
|US8464784||31 Oct 2007||18 Jun 2013||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8469119||31 Oct 2007||25 Jun 2013||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8479812||31 Oct 2007||9 Jul 2013||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8485252||11 Jul 2012||16 Jul 2013||Shell Oil Company||In situ recovery from a hydrocarbon containing formation|
|US8505620||31 Oct 2007||13 Ago 2013||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8511372||31 Oct 2007||20 Ago 2013||Vitruvian Exploration, Llc||Method and system for accessing subterranean deposits from the surface|
|US8536497||13 Oct 2008||17 Sep 2013||Shell Oil Company||Methods for forming long subsurface heaters|
|US8540020||21 Abr 2010||24 Sep 2013||Exxonmobil Upstream Research Company||Converting organic matter from a subterranean formation into producible hydrocarbons by controlling production operations based on availability of one or more production resources|
|US8555971||31 May 2012||15 Oct 2013||Shell Oil Company||Treating tar sands formations with dolomite|
|US8562078||25 Nov 2009||22 Oct 2013||Shell Oil Company||Hydrocarbon production from mines and tunnels used in treating subsurface hydrocarbon containing formations|
|US8579031||17 May 2011||12 Nov 2013||Shell Oil Company||Thermal processes for subsurface formations|
|US8596355||10 Dic 2010||3 Dic 2013||Exxonmobil Upstream Research Company||Optimized well spacing for in situ shale oil development|
|US8606091||20 Oct 2006||10 Dic 2013||Shell Oil Company||Subsurface heaters with low sulfidation rates|
|US8608249||26 Abr 2010||17 Dic 2013||Shell Oil Company||In situ thermal processing of an oil shale formation|
|US8616279||7 Ene 2010||31 Dic 2013||Exxonmobil Upstream Research Company||Water treatment following shale oil production by in situ heating|
|US8616280||17 Jun 2011||31 Dic 2013||Exxonmobil Upstream Research Company||Wellbore mechanical integrity for in situ pyrolysis|
|US8622127||17 Jun 2011||7 Ene 2014||Exxonmobil Upstream Research Company||Olefin reduction for in situ pyrolysis oil generation|
|US8622133||7 Mar 2008||7 Ene 2014||Exxonmobil Upstream Research Company||Resistive heater for in situ formation heating|
|US8627887||8 Dic 2008||14 Ene 2014||Shell Oil Company||In situ recovery from a hydrocarbon containing formation|
|US8631866||8 Abr 2011||21 Ene 2014||Shell Oil Company||Leak detection in circulated fluid systems for heating subsurface formations|
|US8636323||25 Nov 2009||28 Ene 2014||Shell Oil Company||Mines and tunnels for use in treating subsurface hydrocarbon containing formations|
|US8641150||11 Dic 2009||4 Feb 2014||Exxonmobil Upstream Research Company||In situ co-development of oil shale with mineral recovery|
|US8662175||18 Abr 2008||4 Mar 2014||Shell Oil Company||Varying properties of in situ heat treatment of a tar sands formation based on assessed viscosities|
|US8701768||8 Abr 2011||22 Abr 2014||Shell Oil Company||Methods for treating hydrocarbon formations|
|US8701769||8 Abr 2011||22 Abr 2014||Shell Oil Company||Methods for treating hydrocarbon formations based on geology|
|US8739874||8 Abr 2011||3 Jun 2014||Shell Oil Company||Methods for heating with slots in hydrocarbon formations|
|US8752904||10 Abr 2009||17 Jun 2014||Shell Oil Company||Heated fluid flow in mines and tunnels used in heating subsurface hydrocarbon containing formations|
|US8770284||19 Abr 2013||8 Jul 2014||Exxonmobil Upstream Research Company||Systems and methods of detecting an intersection between a wellbore and a subterranean structure that includes a marker material|
|US8789586||12 Jul 2013||29 Jul 2014||Shell Oil Company||In situ recovery from a hydrocarbon containing formation|
|US8791396||18 Abr 2008||29 Jul 2014||Shell Oil Company||Floating insulated conductors for heating subsurface formations|
|US8813840||12 Ago 2013||26 Ago 2014||Efective Exploration, LLC||Method and system for accessing subterranean deposits from the surface and tools therefor|
|US8820406||8 Abr 2011||2 Sep 2014||Shell Oil Company||Electrodes for electrical current flow heating of subsurface formations with conductive material in wellbore|
|US8833453||8 Abr 2011||16 Sep 2014||Shell Oil Company||Electrodes for electrical current flow heating of subsurface formations with tapered copper thickness|
|US8851170||9 Abr 2010||7 Oct 2014||Shell Oil Company||Heater assisted fluid treatment of a subsurface formation|
|US8857506||24 May 2013||14 Oct 2014||Shell Oil Company||Alternate energy source usage methods for in situ heat treatment processes|
|US8863839||15 Nov 2010||21 Oct 2014||Exxonmobil Upstream Research Company||Enhanced convection for in situ pyrolysis of organic-rich rock formations|
|US8875789||8 Ago 2011||4 Nov 2014||Exxonmobil Upstream Research Company||Process for producing hydrocarbon fluids combining in situ heating, a power plant and a gas plant|
|US8881806||9 Oct 2009||11 Nov 2014||Shell Oil Company||Systems and methods for treating a subsurface formation with electrical conductors|
|US9016370||6 Abr 2012||28 Abr 2015||Shell Oil Company||Partial solution mining of hydrocarbon containing layers prior to in situ heat treatment|
|US9022109||21 Ene 2014||5 May 2015||Shell Oil Company||Leak detection in circulated fluid systems for heating subsurface formations|
|US9022118||9 Oct 2009||5 May 2015||Shell Oil Company||Double insulated heaters for treating subsurface formations|
|US9033042||8 Abr 2011||19 May 2015||Shell Oil Company||Forming bitumen barriers in subsurface hydrocarbon formations|
|US9051829||9 Oct 2009||9 Jun 2015||Shell Oil Company||Perforated electrical conductors for treating subsurface formations|
|US9080441||26 Oct 2012||14 Jul 2015||Exxonmobil Upstream Research Company||Multiple electrical connections to optimize heating for in situ pyrolysis|
|US9127523||8 Abr 2011||8 Sep 2015||Shell Oil Company||Barrier methods for use in subsurface hydrocarbon formations|
|US9127538||8 Abr 2011||8 Sep 2015||Shell Oil Company||Methodologies for treatment of hydrocarbon formations using staged pyrolyzation|
|US9129728||9 Oct 2009||8 Sep 2015||Shell Oil Company||Systems and methods of forming subsurface wellbores|
|US9181780||18 Abr 2008||10 Nov 2015||Shell Oil Company||Controlling and assessing pressure conditions during treatment of tar sands formations|
|US9309755||4 Oct 2012||12 Abr 2016||Shell Oil Company||Thermal expansion accommodation for circulated fluid systems used to heat subsurface formations|
|US9347302||12 Nov 2013||24 May 2016||Exxonmobil Upstream Research Company||Resistive heater for in situ formation heating|
|US9394772||17 Sep 2014||19 Jul 2016||Exxonmobil Upstream Research Company||Systems and methods for in situ resistive heating of organic matter in a subterranean formation|
|US9399905||4 May 2015||26 Jul 2016||Shell Oil Company||Leak detection in circulated fluid systems for heating subsurface formations|
|US20020029885 *||24 Abr 2001||14 Mar 2002||De Rouffignac Eric Pierre||In situ thermal processing of a coal formation using a movable heating element|
|US20020038069 *||24 Abr 2001||28 Mar 2002||Wellington Scott Lee||In situ thermal processing of a coal formation to produce a mixture of olefins, oxygenated hydrocarbons, and aromatic hydrocarbons|
|US20020038711 *||24 Abr 2001||4 Abr 2002||Rouffignac Eric Pierre De||In situ thermal processing of a hydrocarbon containing formation using heat sources positioned within open wellbores|
|US20020040780 *||24 Abr 2001||11 Abr 2002||Wellington Scott Lee||In situ thermal processing of a hydrocarbon containing formation to produce a selected mixture|
|US20020043365 *||24 Abr 2001||18 Abr 2002||Berchenko Ilya Emil||In situ thermal processing of a coal formation with a selected ratio of heat sources to production wells|
|US20020056551 *||24 Abr 2001||16 May 2002||Wellington Scott Lee||In situ thermal processing of a hydrocarbon containing formation in a reducing environment|
|US20020057905 *||24 Abr 2001||16 May 2002||Wellington Scott Lee||In situ thermal processing of a hydrocarbon containing formation to produce oxygen containing formation fluids|
|US20020077515 *||24 Abr 2001||20 Jun 2002||Wellington Scott Lee||In situ thermal processing of a hydrocarbon containing formation to produce hydrocarbons having a selected carbon number range|
|US20020084074 *||24 Sep 2001||4 Jul 2002||De Rouffignac Eric Pierre||In situ thermal processing of a hydrocarbon containing formation to increase a porosity of the formation|
|US20030102124 *||24 Abr 2002||5 Jun 2003||Vinegar Harold J.||In situ thermal processing of a blending agent from a relatively permeable formation|
|US20030102125 *||24 Abr 2002||5 Jun 2003||Wellington Scott Lee||In situ thermal processing of a relatively permeable formation in a reducing environment|
|US20030102130 *||24 Abr 2002||5 Jun 2003||Vinegar Harold J.||In situ thermal recovery from a relatively permeable formation with quality control|
|US20030131994 *||24 Abr 2002||17 Jul 2003||Vinegar Harold J.||In situ thermal processing and solution mining of an oil shale formation|
|US20030155111 *||24 Oct 2002||21 Ago 2003||Shell Oil Co||In situ thermal processing of a tar sands formation|
|US20030205378 *||24 Oct 2002||6 Nov 2003||Wellington Scott Lee||In situ recovery from lean and rich zones in a hydrocarbon containing formation|
|US20030209348 *||24 Abr 2002||13 Nov 2003||Ward John Michael||In situ thermal processing and remediation of an oil shale formation|
|US20050051327 *||23 Abr 2004||10 Mar 2005||Vinegar Harold J.||Thermal processes for subsurface formations|
|US20070137857 *||21 Abr 2006||21 Jun 2007||Vinegar Harold J||Low temperature monitoring system for subsurface barriers|
|US20100147521 *||9 Oct 2009||17 Jun 2010||Xueying Xie||Perforated electrical conductors for treating subsurface formations|
|CN101313126B||20 Oct 2006||16 Ene 2013||国际壳牌研究有限公司||Solution mining systems and methods for treating hydrocarbon containing formations|
|Clasificación de EE.UU.||166/272.1, 299/4, 166/272.6|
|Clasificación internacional||E21B36/00, E21B43/28, E21B43/00, E21B43/16, E21B43/24|
|Clasificación cooperativa||E21B43/24, E21B36/00, E21B43/281|
|Clasificación europea||E21B43/24, E21B43/28B, E21B36/00|