CA2695246C - Device for in situ extraction of a substance comprising hydrocarbons - Google Patents
Device for in situ extraction of a substance comprising hydrocarbons Download PDFInfo
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- CA2695246C CA2695246C CA2695246A CA2695246A CA2695246C CA 2695246 C CA2695246 C CA 2695246C CA 2695246 A CA2695246 A CA 2695246A CA 2695246 A CA2695246 A CA 2695246A CA 2695246 C CA2695246 C CA 2695246C
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- 239000000126 substance Substances 0.000 title claims abstract description 33
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 32
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 32
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 17
- 238000000605 extraction Methods 0.000 title abstract description 21
- 238000004519 manufacturing process Methods 0.000 claims abstract description 39
- 238000002347 injection Methods 0.000 claims description 37
- 239000007924 injection Substances 0.000 claims description 37
- 239000007788 liquid Substances 0.000 claims description 14
- 239000004020 conductor Substances 0.000 claims description 8
- 230000001965 increasing effect Effects 0.000 claims description 8
- 150000003839 salts Chemical class 0.000 claims description 7
- 230000007423 decrease Effects 0.000 claims description 6
- 239000003792 electrolyte Substances 0.000 claims description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 2
- 230000008021 deposition Effects 0.000 claims description 2
- 238000011084 recovery Methods 0.000 claims description 2
- 238000003860 storage Methods 0.000 abstract description 119
- 239000010426 asphalt Substances 0.000 description 23
- 238000000034 method Methods 0.000 description 18
- 238000010438 heat treatment Methods 0.000 description 12
- 230000001939 inductive effect Effects 0.000 description 9
- 239000003921 oil Substances 0.000 description 8
- 238000010796 Steam-assisted gravity drainage Methods 0.000 description 7
- 239000000295 fuel oil Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000002689 soil Substances 0.000 description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 239000003027 oil sand Substances 0.000 description 4
- 238000005485 electric heating Methods 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 239000011435 rock Substances 0.000 description 3
- 238000010793 Steam injection (oil industry) Methods 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 239000000615 nonconductor Substances 0.000 description 1
- 239000004058 oil shale Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000002195 synergetic effect Effects 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
- E21B43/2401—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection by means of electricity
-
- 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]
- E21B43/2408—SAGD in combination with other methods
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention relates to a device for in situ extraction of a substance comprising hydrocarbons while reducing the viscosity thereof from an underground storage site (100). The device comprises at least one production pipeline (102, 102') leading out of the storage site (100). The device further comprises at least two electrodes (301, 301') that are inductively and resistively effective relative to at least parts of the storage site (100).
Description
Description Device for in situ extraction of a substance comprising hydrocarbons The invention relates to a device for in situ extraction of a substance comprising hydrocarbons. The substance comprising hydrocarbons is conveyed from an underground storage site while reducing the viscosity thereof. The device comprises at least one production pipeline leading out of the storage site.
Such devices for conveying substances comprising hydrocarbons are for example known from "Steam-Injection Strategy and Energetics of Steam-Assisted Gravity Drainage" by I.D. Gates, 2005, SPE International Thermal Operations and Heavy Oil Symposium, Calgary, Canada, November 1 - 3, 2005.
Large parts of the world's oil reserves are in the form of oil sands. Oil sand is a mixture of rock, clay, sand, water and bitumen or other heavy oils. In the following, references to bitumen, which occurs with a typical viscosity of API 5 to 15 depending on the storage site, also include heavy and very heavy oils or long-chain hydrocarbons generally. The bitumen can be converted into synthetic crude oil by means of further process steps. Oil sands in some cases are found in geological strata at low depth, which are accessible to open-cast mining.
However, large deposits of oil sands also exist which cannot be accessed by open-cast mining. Typically in situ extraction takes place at depths of 60 m or more, since in this situation it no longer seems profitable to remove the overburden.
A method typically used to extract such deposits is "Steam Assisted Gravity Drainage" (SAGD), in which the bitumen occurring in a storage site is heated by hot steam and the Pc:T/EP2008/060074 / 2007P16206WOUS
Such devices for conveying substances comprising hydrocarbons are for example known from "Steam-Injection Strategy and Energetics of Steam-Assisted Gravity Drainage" by I.D. Gates, 2005, SPE International Thermal Operations and Heavy Oil Symposium, Calgary, Canada, November 1 - 3, 2005.
Large parts of the world's oil reserves are in the form of oil sands. Oil sand is a mixture of rock, clay, sand, water and bitumen or other heavy oils. In the following, references to bitumen, which occurs with a typical viscosity of API 5 to 15 depending on the storage site, also include heavy and very heavy oils or long-chain hydrocarbons generally. The bitumen can be converted into synthetic crude oil by means of further process steps. Oil sands in some cases are found in geological strata at low depth, which are accessible to open-cast mining.
However, large deposits of oil sands also exist which cannot be accessed by open-cast mining. Typically in situ extraction takes place at depths of 60 m or more, since in this situation it no longer seems profitable to remove the overburden.
A method typically used to extract such deposits is "Steam Assisted Gravity Drainage" (SAGD), in which the bitumen occurring in a storage site is heated by hot steam and the Pc:T/EP2008/060074 / 2007P16206WOUS
storage site is rendered more permeable by the steam pressure.
In this way the viscosity of the bitumen is reduced, so that it can be conveyed in liquid form, as well as more quickly, from the storage site. The change in the viscosity of the bitumen is caused by an increase in temperature. For this purpose hot steam is compressed through pipelines into the underground storage site, so that the storage site is heated, and at the same time an overpressure builds up in the storage site. Liquid bitumen is conveyed through a further pipe to the surface by the overpressure prevailing in the storage site (cf. also undergraduate seminar on topics relating to "Unconventional hydrocarbons" on the subject of "Heavy oils and ultra-heavy oils" by J. Seim, Freiberg, Germany, January 2001).
To improve the fluidity of the bitumen the hot steam can be mixed with a solvent. The pipelines for the injection of the hot steam, or of the mixture of hot steam and solvent, are essentially laid in parallel to one another, running horizontally within the storage site. The injection pipeline and production pipeline are typically about 5 m to 10 m apart from one another in the vertical direction. However, the distance between the injection and the production pipeline depends on the thickness of the storage site. In the horizontal direction the pipes extend for a length of between several hundred meters and a few kilometers within the storage site.
Before bitumen actually starts being conveyed out of the storage site, it first has to be heated, in order to reduce the viscosity of the bitumen present in the sand or rock.
During the heating phase, to ensure rapid heating of the storage site, hot steam is applied to both the injection pipeline and the production pipeline for a period of approximately 3 months. At the end of the heating phase, the viscosity of the bitumen in the storage site is such that when further hot steam is applied to the injection pipeline, resulting in overpressure in the storage site, liquid bitumen can be conveyed out of the production pipeline to the surface.
When sufficient pressure builds up the installation of jacking oil pumps to bring the bitumen/water emulsion up can be dispensed with.
The SAGD procedure currently practiced, as has been roughly outlined, exhibits various technical problems. Firstly, hot steam can escape from the storage site via channels or porous rock strata present in the storage site, thereby reducing the thermal energy introduced into the storage site. Excessive pressures in the storage site can result in soil distortions on the surface (blow-out), especially if the overburden is not very thick. A further problem is "fingering" within the reservoir, whereby steam breakout (steam short-circuit) occurs generally at the start or end of the horizontal part of the parallel steam injection or production pipeline, when the steam seeks out a preferred communicating path between both pipelines and undesired pressure is dissipated, with the injected steam condensing and being conveyed through the production pipeline as water, so that less steam and thus thermal energy is supplied to the storage site and the effectiveness of the process is dramatically reduced. Pressure and temperature within the storage site, for the rapid heating thereof, cannot therefore be increased arbitrarily, depending on the storage site conditions. Large quantities of fresh water are required for the SAGD procedure. The quantity of water required is measured on the basis of the "steam to oil ratio" (SOR). Strict environmental regulations in the production areas call for a reduction in the "steam to oil ratio", in order to protect the above-ground and underground stores of water.
According to one aspect of the present invention, there is provided a device for in situ recovery of a hydrocarbon-containing substance from an underground deposit, the device having means for reducing the viscosity of the substance and at least one production pipe leading out of the deposit; the device comprising: at least two electrodes of an electric heater that is inductively and resistively effective with respect to at least a part of the deposit, the at least two electrodes connected to a power source; and wherein means to improve electrical conductivity are introduced in the deposit between the at least two electrodes.
Some embodiments may provide a device for in situ extraction of a substance comprising hydrocarbons, in particular a device for conveying heavy oils or bitumen out of an oil sand storage site, which is an improvement over the prior art at least in that a reduced heating phase prior to the start of the production phase can be achieved.
Some embodiments of the invention are based on the consideration of using an electric heater, which works both inductively and resistively relative to at least parts of the storage site, for the rapid heating thereof. The storage site itself works as a resistive (non-inductive) resistor relative to the heater's at least two electrodes. At the same time the storage site is also heated inductively by the electric heater.
According to some embodiments of the invention, a device is specified for in situ extraction of a substance comprising hydrocarbons while reducing the viscosity thereof from an underground storage site, said device containing at least one production pipeline leading out of the storage site. The device further has at least two electrodes, which work inductively and resistively relative to at least parts of the storage site as an electric heater. Advantageously the heating time for the reservoir containing the substance comprising hydrocarbons may be reduced with the device.
Compared to devices as known from the prior art, the "steam to oil ratio" may be reduced.
Some embodiments of the device for extraction of a substance comprising hydrocarbons can additionally have the following features:
In this way the viscosity of the bitumen is reduced, so that it can be conveyed in liquid form, as well as more quickly, from the storage site. The change in the viscosity of the bitumen is caused by an increase in temperature. For this purpose hot steam is compressed through pipelines into the underground storage site, so that the storage site is heated, and at the same time an overpressure builds up in the storage site. Liquid bitumen is conveyed through a further pipe to the surface by the overpressure prevailing in the storage site (cf. also undergraduate seminar on topics relating to "Unconventional hydrocarbons" on the subject of "Heavy oils and ultra-heavy oils" by J. Seim, Freiberg, Germany, January 2001).
To improve the fluidity of the bitumen the hot steam can be mixed with a solvent. The pipelines for the injection of the hot steam, or of the mixture of hot steam and solvent, are essentially laid in parallel to one another, running horizontally within the storage site. The injection pipeline and production pipeline are typically about 5 m to 10 m apart from one another in the vertical direction. However, the distance between the injection and the production pipeline depends on the thickness of the storage site. In the horizontal direction the pipes extend for a length of between several hundred meters and a few kilometers within the storage site.
Before bitumen actually starts being conveyed out of the storage site, it first has to be heated, in order to reduce the viscosity of the bitumen present in the sand or rock.
During the heating phase, to ensure rapid heating of the storage site, hot steam is applied to both the injection pipeline and the production pipeline for a period of approximately 3 months. At the end of the heating phase, the viscosity of the bitumen in the storage site is such that when further hot steam is applied to the injection pipeline, resulting in overpressure in the storage site, liquid bitumen can be conveyed out of the production pipeline to the surface.
When sufficient pressure builds up the installation of jacking oil pumps to bring the bitumen/water emulsion up can be dispensed with.
The SAGD procedure currently practiced, as has been roughly outlined, exhibits various technical problems. Firstly, hot steam can escape from the storage site via channels or porous rock strata present in the storage site, thereby reducing the thermal energy introduced into the storage site. Excessive pressures in the storage site can result in soil distortions on the surface (blow-out), especially if the overburden is not very thick. A further problem is "fingering" within the reservoir, whereby steam breakout (steam short-circuit) occurs generally at the start or end of the horizontal part of the parallel steam injection or production pipeline, when the steam seeks out a preferred communicating path between both pipelines and undesired pressure is dissipated, with the injected steam condensing and being conveyed through the production pipeline as water, so that less steam and thus thermal energy is supplied to the storage site and the effectiveness of the process is dramatically reduced. Pressure and temperature within the storage site, for the rapid heating thereof, cannot therefore be increased arbitrarily, depending on the storage site conditions. Large quantities of fresh water are required for the SAGD procedure. The quantity of water required is measured on the basis of the "steam to oil ratio" (SOR). Strict environmental regulations in the production areas call for a reduction in the "steam to oil ratio", in order to protect the above-ground and underground stores of water.
According to one aspect of the present invention, there is provided a device for in situ recovery of a hydrocarbon-containing substance from an underground deposit, the device having means for reducing the viscosity of the substance and at least one production pipe leading out of the deposit; the device comprising: at least two electrodes of an electric heater that is inductively and resistively effective with respect to at least a part of the deposit, the at least two electrodes connected to a power source; and wherein means to improve electrical conductivity are introduced in the deposit between the at least two electrodes.
Some embodiments may provide a device for in situ extraction of a substance comprising hydrocarbons, in particular a device for conveying heavy oils or bitumen out of an oil sand storage site, which is an improvement over the prior art at least in that a reduced heating phase prior to the start of the production phase can be achieved.
Some embodiments of the invention are based on the consideration of using an electric heater, which works both inductively and resistively relative to at least parts of the storage site, for the rapid heating thereof. The storage site itself works as a resistive (non-inductive) resistor relative to the heater's at least two electrodes. At the same time the storage site is also heated inductively by the electric heater.
According to some embodiments of the invention, a device is specified for in situ extraction of a substance comprising hydrocarbons while reducing the viscosity thereof from an underground storage site, said device containing at least one production pipeline leading out of the storage site. The device further has at least two electrodes, which work inductively and resistively relative to at least parts of the storage site as an electric heater. Advantageously the heating time for the reservoir containing the substance comprising hydrocarbons may be reduced with the device.
Compared to devices as known from the prior art, the "steam to oil ratio" may be reduced.
Some embodiments of the device for extraction of a substance comprising hydrocarbons can additionally have the following features:
5 - The two electrodes of the electric heater can be formed by essentially perpendicularly oriented electric conductors running at least in part in the storage site. A perpendicular borehole does not require a great deal of drilling. Thus electric conductors which work inductively and resistively relative to at least parts of the storage site can be introduced into the storage site simply and effectively.
This device is especially advantageous if it has to be assumed that the permeability diminishes at increasing depth, or the permeability is non-homogeneous in a horizontal direction, in other words that a non-homogeneous and if appropriate anisotropic storage site is present in respect of permeability and/or porosity.
- The at least two electrodes of the electric heater can be formed by essentially horizontally oriented electric conductors running at least in part within the storage site. With electric conductors which run horizontally within the storage site, a large part of the storage site can be heated both resistively and inductively by electricity.
This device is especially advantageous if it has to be assumed that the permeability diminishes at increasing depth, or the permeability is non-homogeneous in a horizontal direction, in other words that a non-homogeneous and if appropriate anisotropic storage site is present in respect of permeability and/or porosity.
- The at least two electrodes of the electric heater can be formed by essentially horizontally oriented electric conductors running at least in part within the storage site. With electric conductors which run horizontally within the storage site, a large part of the storage site can be heated both resistively and inductively by electricity.
- The electrodes can be rod-shaped metal conductors. Rod-shaped metal conductors are especially simple and cheap.
- The space between at least segments of the electrodes can decrease as the length of the electrodes increases, from the perspective of a power source. The reduction in distance can in particular be stepless. In particular the distance between the segments of the electrodes can decrease linearly. By changing the distance between the electrodes it is possible to keep the voltage drop constant over the length of the electrodes. This voltage drop is determined by the electrical resistance of the electrodes themselves, plus the electrical resistance of the soil correspondingly present between the electrodes. In this way it is advantageously possible to prevent the entire heat output of the electrodes dropping away at an area in the soil close to the power source.
- The electrodes can run coaxially in a guide pipe, said guide pipe being permeable to liquid for the selective deposition of a liquid in parts of the storage site at the corresponding subareas running in the storage site. Thanks to the guide pipe the storage site can be supplied with liquid in selective areas, as a result of which the electrical conductivity of the storage site can be affected.
In this way the conductivity of the storage site can be ensured, so that the electric heater will operate fault-free.
- The device can have an injection pipeline projecting into the storage site. In that the device has both an injection pipeline and a production pipeline, the storage site can be heated on the one hand by means of the electric heater and on the other hand by for example a steam-assisted heating procedure. Both procedures can interwork in synergy.
- The electrodes can be connected to one another electrically at their end regions remote from the power source by a connecting post. Thanks to such an electrical connection the operational reliability of the electric heater can be improved.
- The injection pipeline and the production pipeline can have pipe sections running in the storage site essentially parallel to one another, oriented essentially horizontally.
Seen in cross-section perpendicular to the injection and production pipeline, the electrodes of the electric heater are disposed on both sides of the injection and production pipeline. Thanks to an arrangement of the electrodes of the electric heater on both sides of the injection and production pipeline, the volume of the storage site, which extends in a horizontal direction between the injection and production pipelines, can in particular be heated by the electric heater. Particularly advantageously, a larger volume of the storage site can be extracted in this way.
SAGD procedures known from the prior art achieve an extraction of between 40 and 60% of the bitumen present in the storage site. According to the embodiment described above, extraction levels of over 70% appear possible.
- At least two of the electrodes of the electric heater can be formed by at least parts of the injection pipeline or the production pipeline. In that the electric heater is formed by at least parts of the injection or production pipeline, it is possible to cut down on additional material for the electric heater; another borehole is thus likewise dispensed with. Such a design of the electric heater is hence especially advantageous.
- Hot steam can be applied to the injection pipeline and the production pipeline. If an underground storage site is exploited in accordance with an SAGD procedure or a similar or related procedure, hot steam is applied to pipelines typically present in the storage site. The combination of such a hot-steam-based procedure with an electric heating procedure is especially advantageous, since as a result of the hot steam additional water is introduced into the storage site, which increases the electrical conductivity of the storage site. A particular electrical conductivity is necessary in order to implement an inductive and resistive electric heating procedure. Thanks to the synergetic combination of a hot steam procedure and an electric heating procedure the efficiency of the combined procedure can be increased over and above that of both individual procedures.
- The hot steam can be enriched with an electrolyte, preferably with salt. The electrical conductivity of the steam is increased in this way. The effectiveness of an inductive and resistive electric heater relative to at least parts of a storage site essentially depends on the electrical conductivity of the storage site. In that the hot steam introduced into the storage site by the injection and/or production pipeline is additionally provided with minerals, preferably with salt, the electrical conductivity of the storage site can be selectively adjusted and if appropriate increased.
- The electric heater can be an alternating current heater. An alternating current heater prevents ions from migrating within the storage site. Advantageously carbonization or salt encrustation of the injection and/or production pipeline can be prevented in this way.
Further advantageous embodiments of the inventive device emerge from the claims not addressed above and in particular from the drawing explained below. The drawing shows preferred embodiments of the inventive device in a highly diagrammatic illustration. It shows:
Figure 1 an outline sketch of a device for in situ extraction of a substance comprising hydrocarbons from an underground storage site, Figure 2 a cross-section through the extraction area of such a storage site, Figures 3 and 4 a device for in situ extraction of a substance comprising hydrocarbons with an electric heater and Figure 5 a further possible embodiment of such a device.
Corresponding parts in the figures are in each case provided with the same reference characters. Parts not explained in greater detail are generally known prior art.
Figure 1 shows a diagrammatic illustration of a device for in situ extraction of a substance comprising hydrocarbons from an underground storage site 100 while reducing the viscosity thereof. Such a device can for example be a device for extraction of bitumen from an oil sand deposit. An injection pipeline 101 runs from the earth's surface into the storage site 100. A production pipeline 102 leads out of the storage site 100 to the earth's surface. Devices are conceivable in which a plurality of injection pipelines 101 and a plurality of production pipelines 102 are used to convey the substance comprising hydrocarbons from the underground storage site 100.
The storage site 100 can in particular be an oil sand deposit or an oil shale deposit, from which bitumen or other heavy oils can be extracted.
To be able to extract the substance comprising hydrocarbons from the storage site 100, the viscosity of the substance comprising hydrocarbons present in the storage site 100 must be reduced. For this purpose at least parts of the storage site 100 must be heated. To heat the storage site 100 hot steam is applied to the injection pipeline and the production pipeline 102. After being heated for a period of typically 3 months the viscosity of the substance comprising hydrocarbons present in the storage site 100 has decreased so much as a result of the increased temperature that the substance has become free-flowing. If water steam is now further applied to the injection pipeline 101, then as a result of the overpressure present in the storage site or at least parts of the storage site 100 a substance comprising hydrocarbons can be conveyed through the production pipeline 102 to the surface. To maintain the temperature needed for the substance comprising hydrocarbons to flow freely, hot steam is again applied to the injection pipeline 101. Once the extracted substance comprising hydrocarbons arrives at the surface it can be subjected to further processing steps, so that synthetic crude oil can be obtained.
Figure 2 shows a cross-section through the storage site 100, in which two injection pipelines 101, 101' and two production pipelines 102, 102' run. The hot steam exiting from the injection pipelines 101, 101' is shown diagrammatically by arrows. The hot steam forms steam chambers 201, 201' within the storage site 100, from which the substance comprising hydrocarbons which has become free-flowing can be conveyed. A
dead volume 202, in which the viscosity of the substance comprising hydrocarbons present in the storage site 100 is too high to enable it to be conveyed, extends in a horizontal direction between the steam chambers 201, 201'. The dead volume 202 of the storage site 100 cannot be extracted.
Figure 3 shows a device for in situ extraction of a substance comprising hydrocarbons from a storage site 100, which in addition to two injection pipelines 101, 101', which have pipeline sections running horizontally in the storage site 100, has two production pipelines 102, 102'. The device for in situ extraction of a substance comprising hydrocarbons furthermore has two electrodes 301, 301', which run in perpendicular boreholes within the storage site 100. The electrodes 301, 301' work as an inductive and resistive electric heater relative to at least parts of the storage site 100. Determined by the conductivity of at least parts of the storage site 100, especially of the dead volume 202, this can be heated resistively by current flowing between the two electrodes 301, 301'. The resistive heating effect is indicated by arrows and/or lines within the storage site 100.
At the same time the electrodes 301, 301' work in the volumes 303, 303' as inductive heaters. The electrodes 301, 301' can be insulated in respect of the soil by means of electrical insulators 304, 304' in areas in which these run outside the actual storage site 100. In this way the resistive heat output can be introduced in defined areas of the storage site 100.
The electrodes 301, 301' can in particular be rod-shaped metal conductors made of an especially highly conductive metal.
The device shown in Figure 3 for in situ extraction of a substance comprising hydrocarbons can in particular be operated such that the storage site 100 is heated both by means of hot steam and also by means of the electric heater.
In the heating phase of the storage site 100 hot steam can thus be applied both to the injection pipelines 101, 101' and to the production pipelines 102, 102', and in addition the volume to be conveyed out of the substance comprising hydrocarbons, especially the dead volume 202, can be heated by means of the electric heater via the electrodes 301, 301'. In this way a shorter heating time can be achieved than if the storage site 100 is merely heated by means of the electric heater or by means of steam being applied. The electric heater can in particular be an alternating current heater, as a result of which no migration of ions occurs within the storage site 100.
By heating the storage site 100 or at least parts of the storage site 100 it is possible to reduce the liquid content of the storage site 100 and thus to reduce the electrical conductivity of the storage site 100. A decreasing conductivity of the storage site 100 means that the electric heater, in particular the resistive method of operation, becomes less efficient. To counter this loss of conductivity, hot steam forced into the storage site 100 can be enriched with minerals, in particular with salts. Furthermore, by controlling the enrichment of the hot steam with minerals, in particular with salts, the conductivity of the storage site 100 can be selectively adjusted. The minerals or salts are thereby added to the hot steam after it exits from the steam generator. On the other hand, when the bitumen is extracted at a location, no conductivity is required at this location either. In particular the inductive mode of working means that losses only occur where conductivity exists, in other words the depth of penetration expands accordingly and the bitumen present in the case of natural conductivity is heated and flows down by force of gravity with the naturally occurring reservoir electrolyte. Naturally initially the loss mechanism at the electrode will be at its most effective as a result of resistive as well as inductive working; in other words at the start of extraction the bitumen is made more free-flowing there. If the conductivity at the electrode is low, there is no contact between electrode and reservoir; the inductive mechanism now comes into its own, as it does not rely on the electrical contact between electrode and reservoir.
Figure 4 shows a device for in situ extraction of a substance comprising hydrocarbons from a storage site 100. According to the exemplary embodiment illustrated in Figure 4 at least parts of the injection pipelines 100, 101' are used as electrodes of the electric heater. In particular those parts of the injection pipelines 100, 101' can be used as electrodes 301, 301' of the electric heater which run essentially horizontally within the storage site 100. The parts of the injection pipelines 100, 101' acting as electrodes 301, 301' heat at least parts of the storage site 100 both resistively and inductively. In particular the electrodes 301, 301' heat areas 303, 303' which extend in cylindrical fashion around the injection pipelines 101, 101'. In addition to these inductively heated areas 303, 303' the dead volume 202 is in particular heated in resistive fashion. For the purpose of the electric heater the injection pipelines 101, 101' are connected to an alternating current source 302.
Figure 5 shows a device for in situ extraction of a substance comprising hydrocarbons from a storage site 100. The exemplary embodiment shown in Figure 5 comprises two production pipelines 102, 102' which lead out of the storage site 100.
Two electrodes 301, 301', each of which is disposed in a guide pipe 501, 501', project into the storage site 100. The guide pipes 501, 501' can be accessed from the surface and the parts running outside the storage site or the areas of the storage site 100 to be heated are additionally electrically insulated against the soil by electrical insulations 304, 304'. The guide pipes 501, 501' can be accessed from the earth's surface for a liquid and in certain areas within the storage site 100 have areas permeable to liquid. This can for example entail porous designs of the pipe walls or openings or holes.
In that liquid, preferably a liquid which is enriched with an electrolyte to improve the conductivity, is selectively introduced into the storage site 100 or parts of the storage site 100, the electrical conductivity of the storage site 100 can be selectively adjusted. In this way the functional capability of the electric heater can be ensured. As a further measure to ensure the functional capability of the electric heater the ends of the electrodes 301, 301' which face away from the power source 302 can be short-circuited using an electrical bridge 502.
With the exemplary embodiment illustrated in Figure 5 it is possible to exploit a bitumen storage site without using hot steam. The storage site can be heated merely by means of the electric heater in inductive and resistive fashion, and the liquid bitumen present in the production pipeline 102, 102' can be recovered by means of a lifting pump or is conveyed to the surface by natural geological overpressure. As an option, hot steam can be applied to the storage site 100 at intervals over the production pipelines 102, 102', so that the pressure within the storage site 100 rises. The overpressure created in this way can likewise be used to convey bitumen from the storage site 100.
The electrodes 301, 301' can continue to run within the storage site 100 such that the distance between them decreases with the increasing length of the electrodes 301, from the perspective of the power source 302. In particular the distance between the electrodes 301, 301' can decrease linearly. In this way it is possible to prevent the electric heat output, in particular the resistive electric heat output from the perspective of the power source 302, from being introduced into the storage site 100 at the start of the electrodes 301, 301' or dropping away into this area. The distance between the electrodes 301, 301' can in particular be selected such that a continuous heat output over the length of the electrodes 301, 301', in particular over the length of the subareas of the electrodes 301, 301' which run within the storage site 100, can be achieved by taking account of the electrical conductivity of the storage site 100.
The distance between the boreholes can in this case be controlled using generally known measures; for example a transmitter can be operated in the first borehole, with the drill head of the second borehole being able to determine the distance from the first borehole on the basis of this transmitted signal.
- The space between at least segments of the electrodes can decrease as the length of the electrodes increases, from the perspective of a power source. The reduction in distance can in particular be stepless. In particular the distance between the segments of the electrodes can decrease linearly. By changing the distance between the electrodes it is possible to keep the voltage drop constant over the length of the electrodes. This voltage drop is determined by the electrical resistance of the electrodes themselves, plus the electrical resistance of the soil correspondingly present between the electrodes. In this way it is advantageously possible to prevent the entire heat output of the electrodes dropping away at an area in the soil close to the power source.
- The electrodes can run coaxially in a guide pipe, said guide pipe being permeable to liquid for the selective deposition of a liquid in parts of the storage site at the corresponding subareas running in the storage site. Thanks to the guide pipe the storage site can be supplied with liquid in selective areas, as a result of which the electrical conductivity of the storage site can be affected.
In this way the conductivity of the storage site can be ensured, so that the electric heater will operate fault-free.
- The device can have an injection pipeline projecting into the storage site. In that the device has both an injection pipeline and a production pipeline, the storage site can be heated on the one hand by means of the electric heater and on the other hand by for example a steam-assisted heating procedure. Both procedures can interwork in synergy.
- The electrodes can be connected to one another electrically at their end regions remote from the power source by a connecting post. Thanks to such an electrical connection the operational reliability of the electric heater can be improved.
- The injection pipeline and the production pipeline can have pipe sections running in the storage site essentially parallel to one another, oriented essentially horizontally.
Seen in cross-section perpendicular to the injection and production pipeline, the electrodes of the electric heater are disposed on both sides of the injection and production pipeline. Thanks to an arrangement of the electrodes of the electric heater on both sides of the injection and production pipeline, the volume of the storage site, which extends in a horizontal direction between the injection and production pipelines, can in particular be heated by the electric heater. Particularly advantageously, a larger volume of the storage site can be extracted in this way.
SAGD procedures known from the prior art achieve an extraction of between 40 and 60% of the bitumen present in the storage site. According to the embodiment described above, extraction levels of over 70% appear possible.
- At least two of the electrodes of the electric heater can be formed by at least parts of the injection pipeline or the production pipeline. In that the electric heater is formed by at least parts of the injection or production pipeline, it is possible to cut down on additional material for the electric heater; another borehole is thus likewise dispensed with. Such a design of the electric heater is hence especially advantageous.
- Hot steam can be applied to the injection pipeline and the production pipeline. If an underground storage site is exploited in accordance with an SAGD procedure or a similar or related procedure, hot steam is applied to pipelines typically present in the storage site. The combination of such a hot-steam-based procedure with an electric heating procedure is especially advantageous, since as a result of the hot steam additional water is introduced into the storage site, which increases the electrical conductivity of the storage site. A particular electrical conductivity is necessary in order to implement an inductive and resistive electric heating procedure. Thanks to the synergetic combination of a hot steam procedure and an electric heating procedure the efficiency of the combined procedure can be increased over and above that of both individual procedures.
- The hot steam can be enriched with an electrolyte, preferably with salt. The electrical conductivity of the steam is increased in this way. The effectiveness of an inductive and resistive electric heater relative to at least parts of a storage site essentially depends on the electrical conductivity of the storage site. In that the hot steam introduced into the storage site by the injection and/or production pipeline is additionally provided with minerals, preferably with salt, the electrical conductivity of the storage site can be selectively adjusted and if appropriate increased.
- The electric heater can be an alternating current heater. An alternating current heater prevents ions from migrating within the storage site. Advantageously carbonization or salt encrustation of the injection and/or production pipeline can be prevented in this way.
Further advantageous embodiments of the inventive device emerge from the claims not addressed above and in particular from the drawing explained below. The drawing shows preferred embodiments of the inventive device in a highly diagrammatic illustration. It shows:
Figure 1 an outline sketch of a device for in situ extraction of a substance comprising hydrocarbons from an underground storage site, Figure 2 a cross-section through the extraction area of such a storage site, Figures 3 and 4 a device for in situ extraction of a substance comprising hydrocarbons with an electric heater and Figure 5 a further possible embodiment of such a device.
Corresponding parts in the figures are in each case provided with the same reference characters. Parts not explained in greater detail are generally known prior art.
Figure 1 shows a diagrammatic illustration of a device for in situ extraction of a substance comprising hydrocarbons from an underground storage site 100 while reducing the viscosity thereof. Such a device can for example be a device for extraction of bitumen from an oil sand deposit. An injection pipeline 101 runs from the earth's surface into the storage site 100. A production pipeline 102 leads out of the storage site 100 to the earth's surface. Devices are conceivable in which a plurality of injection pipelines 101 and a plurality of production pipelines 102 are used to convey the substance comprising hydrocarbons from the underground storage site 100.
The storage site 100 can in particular be an oil sand deposit or an oil shale deposit, from which bitumen or other heavy oils can be extracted.
To be able to extract the substance comprising hydrocarbons from the storage site 100, the viscosity of the substance comprising hydrocarbons present in the storage site 100 must be reduced. For this purpose at least parts of the storage site 100 must be heated. To heat the storage site 100 hot steam is applied to the injection pipeline and the production pipeline 102. After being heated for a period of typically 3 months the viscosity of the substance comprising hydrocarbons present in the storage site 100 has decreased so much as a result of the increased temperature that the substance has become free-flowing. If water steam is now further applied to the injection pipeline 101, then as a result of the overpressure present in the storage site or at least parts of the storage site 100 a substance comprising hydrocarbons can be conveyed through the production pipeline 102 to the surface. To maintain the temperature needed for the substance comprising hydrocarbons to flow freely, hot steam is again applied to the injection pipeline 101. Once the extracted substance comprising hydrocarbons arrives at the surface it can be subjected to further processing steps, so that synthetic crude oil can be obtained.
Figure 2 shows a cross-section through the storage site 100, in which two injection pipelines 101, 101' and two production pipelines 102, 102' run. The hot steam exiting from the injection pipelines 101, 101' is shown diagrammatically by arrows. The hot steam forms steam chambers 201, 201' within the storage site 100, from which the substance comprising hydrocarbons which has become free-flowing can be conveyed. A
dead volume 202, in which the viscosity of the substance comprising hydrocarbons present in the storage site 100 is too high to enable it to be conveyed, extends in a horizontal direction between the steam chambers 201, 201'. The dead volume 202 of the storage site 100 cannot be extracted.
Figure 3 shows a device for in situ extraction of a substance comprising hydrocarbons from a storage site 100, which in addition to two injection pipelines 101, 101', which have pipeline sections running horizontally in the storage site 100, has two production pipelines 102, 102'. The device for in situ extraction of a substance comprising hydrocarbons furthermore has two electrodes 301, 301', which run in perpendicular boreholes within the storage site 100. The electrodes 301, 301' work as an inductive and resistive electric heater relative to at least parts of the storage site 100. Determined by the conductivity of at least parts of the storage site 100, especially of the dead volume 202, this can be heated resistively by current flowing between the two electrodes 301, 301'. The resistive heating effect is indicated by arrows and/or lines within the storage site 100.
At the same time the electrodes 301, 301' work in the volumes 303, 303' as inductive heaters. The electrodes 301, 301' can be insulated in respect of the soil by means of electrical insulators 304, 304' in areas in which these run outside the actual storage site 100. In this way the resistive heat output can be introduced in defined areas of the storage site 100.
The electrodes 301, 301' can in particular be rod-shaped metal conductors made of an especially highly conductive metal.
The device shown in Figure 3 for in situ extraction of a substance comprising hydrocarbons can in particular be operated such that the storage site 100 is heated both by means of hot steam and also by means of the electric heater.
In the heating phase of the storage site 100 hot steam can thus be applied both to the injection pipelines 101, 101' and to the production pipelines 102, 102', and in addition the volume to be conveyed out of the substance comprising hydrocarbons, especially the dead volume 202, can be heated by means of the electric heater via the electrodes 301, 301'. In this way a shorter heating time can be achieved than if the storage site 100 is merely heated by means of the electric heater or by means of steam being applied. The electric heater can in particular be an alternating current heater, as a result of which no migration of ions occurs within the storage site 100.
By heating the storage site 100 or at least parts of the storage site 100 it is possible to reduce the liquid content of the storage site 100 and thus to reduce the electrical conductivity of the storage site 100. A decreasing conductivity of the storage site 100 means that the electric heater, in particular the resistive method of operation, becomes less efficient. To counter this loss of conductivity, hot steam forced into the storage site 100 can be enriched with minerals, in particular with salts. Furthermore, by controlling the enrichment of the hot steam with minerals, in particular with salts, the conductivity of the storage site 100 can be selectively adjusted. The minerals or salts are thereby added to the hot steam after it exits from the steam generator. On the other hand, when the bitumen is extracted at a location, no conductivity is required at this location either. In particular the inductive mode of working means that losses only occur where conductivity exists, in other words the depth of penetration expands accordingly and the bitumen present in the case of natural conductivity is heated and flows down by force of gravity with the naturally occurring reservoir electrolyte. Naturally initially the loss mechanism at the electrode will be at its most effective as a result of resistive as well as inductive working; in other words at the start of extraction the bitumen is made more free-flowing there. If the conductivity at the electrode is low, there is no contact between electrode and reservoir; the inductive mechanism now comes into its own, as it does not rely on the electrical contact between electrode and reservoir.
Figure 4 shows a device for in situ extraction of a substance comprising hydrocarbons from a storage site 100. According to the exemplary embodiment illustrated in Figure 4 at least parts of the injection pipelines 100, 101' are used as electrodes of the electric heater. In particular those parts of the injection pipelines 100, 101' can be used as electrodes 301, 301' of the electric heater which run essentially horizontally within the storage site 100. The parts of the injection pipelines 100, 101' acting as electrodes 301, 301' heat at least parts of the storage site 100 both resistively and inductively. In particular the electrodes 301, 301' heat areas 303, 303' which extend in cylindrical fashion around the injection pipelines 101, 101'. In addition to these inductively heated areas 303, 303' the dead volume 202 is in particular heated in resistive fashion. For the purpose of the electric heater the injection pipelines 101, 101' are connected to an alternating current source 302.
Figure 5 shows a device for in situ extraction of a substance comprising hydrocarbons from a storage site 100. The exemplary embodiment shown in Figure 5 comprises two production pipelines 102, 102' which lead out of the storage site 100.
Two electrodes 301, 301', each of which is disposed in a guide pipe 501, 501', project into the storage site 100. The guide pipes 501, 501' can be accessed from the surface and the parts running outside the storage site or the areas of the storage site 100 to be heated are additionally electrically insulated against the soil by electrical insulations 304, 304'. The guide pipes 501, 501' can be accessed from the earth's surface for a liquid and in certain areas within the storage site 100 have areas permeable to liquid. This can for example entail porous designs of the pipe walls or openings or holes.
In that liquid, preferably a liquid which is enriched with an electrolyte to improve the conductivity, is selectively introduced into the storage site 100 or parts of the storage site 100, the electrical conductivity of the storage site 100 can be selectively adjusted. In this way the functional capability of the electric heater can be ensured. As a further measure to ensure the functional capability of the electric heater the ends of the electrodes 301, 301' which face away from the power source 302 can be short-circuited using an electrical bridge 502.
With the exemplary embodiment illustrated in Figure 5 it is possible to exploit a bitumen storage site without using hot steam. The storage site can be heated merely by means of the electric heater in inductive and resistive fashion, and the liquid bitumen present in the production pipeline 102, 102' can be recovered by means of a lifting pump or is conveyed to the surface by natural geological overpressure. As an option, hot steam can be applied to the storage site 100 at intervals over the production pipelines 102, 102', so that the pressure within the storage site 100 rises. The overpressure created in this way can likewise be used to convey bitumen from the storage site 100.
The electrodes 301, 301' can continue to run within the storage site 100 such that the distance between them decreases with the increasing length of the electrodes 301, from the perspective of the power source 302. In particular the distance between the electrodes 301, 301' can decrease linearly. In this way it is possible to prevent the electric heat output, in particular the resistive electric heat output from the perspective of the power source 302, from being introduced into the storage site 100 at the start of the electrodes 301, 301' or dropping away into this area. The distance between the electrodes 301, 301' can in particular be selected such that a continuous heat output over the length of the electrodes 301, 301', in particular over the length of the subareas of the electrodes 301, 301' which run within the storage site 100, can be achieved by taking account of the electrical conductivity of the storage site 100.
The distance between the boreholes can in this case be controlled using generally known measures; for example a transmitter can be operated in the first borehole, with the drill head of the second borehole being able to determine the distance from the first borehole on the basis of this transmitted signal.
Claims (17)
1. A device for in situ recovery of a hydrocarbon-containing substance from an underground deposit, the device having means for reducing the viscosity of the substance and at least one production pipe leading out of the deposit; the device comprising: at least two electrodes of an electric heater that is inductively and resistively effective with respect to at least a part of the deposit, the at least two electrodes connected to a power source; and wherein means to improve electrical conductivity are introduced in the deposit between the at least two electrodes.
2. A device according to claim 1, wherein the means for improving the electrical conductivity between the at least two electrodes is a liquid containing an electrolyte.
3. A device according to claim 1, wherein the means for improving the electrical conductivity between the at least two electrodes is an electrical bridge shorting the at least two electrodes at end portions distant to the power source.
4. A device according to claim 1, wherein the at least two electrodes of the electric heater are oriented substantially vertically at least partially in the deposit.
5. A device according to claim 1, wherein the at least two electrodes of the electric heater are oriented substantially horizontally at least partially in the deposit.
6. A device according to any one of claims 1 to 5, wherein sections of the electrodes are at a spatial distance from one another which, with increasing length of the electrodes, viewed from the power source, continuously decreases.
7. A device according to claim 6, wherein the spatial distance between the sections of the electrodes decreases linearly.
8. A device according to any one of claims 1 to 7, wherein the electrodes are rod-shaped, metallic, electrical conductors.
9. A device according to claim 2, wherein the electrodes run coaxially in a guide pipe, wherein the guide pipe, at the appropriate sections extending into the deposit, is permeable for targeted deposition of the liquid in parts of the deposit.
10. A device according to any one of claims 1 to 9, further comprising at least one injection pipe for protrusion into the deposit.
11. A device according to claim 10, wherein the injection pipe and the production pipe in the deposit comprise pipe sections that are running substantially parallel to each other and are horizontally oriented, and, in a section perpendicular to the injection pipe and the production pipe, the electrodes are arranged at both sides of the injection pipe and the production pipe.
12. A device according to claim 10 or claim 11, wherein one of the at least two electrodes of the electric heater is formed by at least parts of the injection pipe, and another of the at least two electrodes is formed by the at least parts of the production pipe.
13. A device according to any one of claims 10 to 12, wherein the injection pipe and the production pipe may be pressurized with hot steam.
14. A device according to claim 13, wherein the hot steam is mixed with an electrolyte to increase its electrical conductivity.
15. A device according to claim 14 wherein the electrolyte is a salt.
16. A device according to any one of claims 1 to 15, wherein the electric heater is an alternating current heater.
17. A device according to claim 16, wherein the alternating current electric heater has a frequency ranging from 1 Hz to 200 kHz and a voltage ranging from 100 V to 10 kV.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102007036832.3 | 2007-08-03 | ||
| DE102007036832A DE102007036832B4 (en) | 2007-08-03 | 2007-08-03 | Apparatus for the in situ recovery of a hydrocarbonaceous substance |
| PCT/EP2008/060074 WO2009019197A2 (en) | 2007-08-03 | 2008-07-31 | Device for in situ extraction of a substance comprising hydrocarbons |
Publications (2)
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| CA2695246A1 CA2695246A1 (en) | 2009-02-12 |
| CA2695246C true CA2695246C (en) | 2013-02-12 |
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| CA2695246A Expired - Fee Related CA2695246C (en) | 2007-08-03 | 2008-07-31 | Device for in situ extraction of a substance comprising hydrocarbons |
Country Status (5)
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| US (1) | US20100252249A1 (en) |
| CA (1) | CA2695246C (en) |
| DE (1) | DE102007036832B4 (en) |
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| WO (1) | WO2009019197A2 (en) |
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| DE102008022176A1 (en) | 2007-08-27 | 2009-11-12 | Siemens Aktiengesellschaft | Device for "in situ" production of bitumen or heavy oil |
| DE102008062326A1 (en) | 2008-03-06 | 2009-09-17 | Siemens Aktiengesellschaft | Arrangement for inductive heating of oil sands and heavy oil deposits by means of live conductors |
| RU2461703C2 (en) | 2008-05-05 | 2012-09-20 | Сименс Акциенгезелльшафт | Method and device for transportation bitumen or heavy oil in situ |
| DE102008044953A1 (en) | 2008-08-29 | 2010-03-04 | Siemens Aktiengesellschaft | Plant for the in situ recovery of a carbonaceous substance |
| DE102008044955A1 (en) | 2008-08-29 | 2010-03-04 | Siemens Aktiengesellschaft | Method and apparatus for "in situ" production of bitumen or heavy oil |
| DE102008047219A1 (en) | 2008-09-15 | 2010-03-25 | Siemens Aktiengesellschaft | Process for the extraction of bitumen and / or heavy oil from an underground deposit, associated plant and operating procedures of this plant |
| DE102009010289A1 (en) | 2009-02-24 | 2010-09-02 | Siemens Aktiengesellschaft | Device for measuring temperature in electromagnetic fields, use of this device and associated measuring arrangement |
| DE102010008779B4 (en) | 2010-02-22 | 2012-10-04 | Siemens Aktiengesellschaft | Apparatus and method for recovering, in particular recovering, a carbonaceous substance from a subterranean deposit |
| DE102010008776A1 (en) | 2010-02-22 | 2011-08-25 | Siemens Aktiengesellschaft, 80333 | Apparatus and method for recovering, in particular recovering, a carbonaceous substance from a subterranean deposit |
| DE102010023542B4 (en) | 2010-02-22 | 2012-05-24 | Siemens Aktiengesellschaft | Apparatus and method for recovering, in particular recovering, a carbonaceous substance from a subterranean deposit |
| DE102010020154B4 (en) | 2010-03-03 | 2014-08-21 | Siemens Aktiengesellschaft | Method and apparatus for "in situ" production of bitumen or heavy oil |
| US20110277992A1 (en) * | 2010-05-14 | 2011-11-17 | Paul Grimes | Systems and methods for enhanced recovery of hydrocarbonaceous fluids |
| DE102010041329A1 (en) | 2010-09-24 | 2012-03-29 | Siemens Aktiengesellschaft | Device for heating soil |
| RU2518581C2 (en) * | 2012-07-17 | 2014-06-10 | Александр Петрович Линецкий | Oil and gas, shale and coal deposit development method |
| CA2783439A1 (en) * | 2012-07-20 | 2014-01-20 | Sunrise Oil Sands Partnership | Water injection method for assisting in collection of oil in a sagd oil recovery application |
| EP2734009A1 (en) * | 2012-11-15 | 2014-05-21 | Siemens Aktiengesellschaft | Induction device for the heating of an oil reservoir, in particular a heavy oil reservoir |
| CA2893876A1 (en) | 2012-12-06 | 2014-06-12 | Wintershall Holding GmbH | Arrangement and method for introducing heat into a geological formation by means of electromagnetic induction |
| AU2014347209B8 (en) * | 2013-11-07 | 2017-02-16 | Exxonmobil Upstream Research Company | Systems and methods of controlling in situ resistive heating elements |
| EP2886793A1 (en) * | 2013-12-18 | 2015-06-24 | Siemens Aktiengesellschaft | Method for introducing an inductor loop into a rock formation |
| EP2886792A1 (en) * | 2013-12-18 | 2015-06-24 | Siemens Aktiengesellschaft | Method for introducing an inductor loop into a rock formation |
| DE102014223621A1 (en) * | 2014-11-19 | 2016-05-19 | Siemens Aktiengesellschaft | deposit Heating |
| RU2710057C1 (en) * | 2018-09-05 | 2019-12-24 | Артём Сергеевич Голубов | Oil well viscous production method |
| CN111537434B (en) * | 2020-05-11 | 2022-05-31 | 西南石油大学 | Stride earthquake fault buried pipeline test device |
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| US3133591A (en) * | 1954-05-20 | 1964-05-19 | Orpha B Brandon | Method and apparatus for forming and/or augmenting an energy wave |
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| USRE30738E (en) * | 1980-02-06 | 1981-09-08 | Iit Research Institute | Apparatus and method for in situ heat processing of hydrocarbonaceous formations |
| US4545435A (en) * | 1983-04-29 | 1985-10-08 | Iit Research Institute | Conduction heating of hydrocarbonaceous formations |
| US4821798A (en) * | 1987-06-09 | 1989-04-18 | Ors Development Corporation | Heating system for rathole oil well |
| US4957646A (en) * | 1987-08-26 | 1990-09-18 | Shell Oil Company | Steam foam surfactants enriched in alpha olefin disulfonates for enhanced oil recovery |
| US5167280A (en) * | 1990-06-24 | 1992-12-01 | Mobil Oil Corporation | Single horizontal well process for solvent/solute stimulation |
| US5586213A (en) * | 1992-02-05 | 1996-12-17 | Iit Research Institute | Ionic contact media for electrodes and soil in conduction heating |
| US5449251A (en) * | 1993-05-04 | 1995-09-12 | The Regents Of The University Of California | Dynamic underground stripping: steam and electric heating for in situ decontamination of soils and groundwater |
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| DE102007008292B4 (en) * | 2007-02-16 | 2009-08-13 | Siemens Ag | Apparatus and method for recovering a hydrocarbonaceous substance while reducing its viscosity from an underground deposit |
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2007
- 2007-08-03 DE DE102007036832A patent/DE102007036832B4/en not_active Expired - Fee Related
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2008
- 2008-07-31 US US12/670,898 patent/US20100252249A1/en not_active Abandoned
- 2008-07-31 CA CA2695246A patent/CA2695246C/en not_active Expired - Fee Related
- 2008-07-31 RU RU2010107611/03A patent/RU2426868C1/en not_active IP Right Cessation
- 2008-07-31 WO PCT/EP2008/060074 patent/WO2009019197A2/en active Application Filing
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| WO2009019197A2 (en) | 2009-02-12 |
| RU2426868C1 (en) | 2011-08-20 |
| CA2695246A1 (en) | 2009-02-12 |
| DE102007036832B4 (en) | 2009-08-20 |
| DE102007036832A1 (en) | 2009-02-05 |
| WO2009019197A3 (en) | 2010-10-21 |
| US20100252249A1 (en) | 2010-10-07 |
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