WO2016195511A1 - Subsurface heater configuration for in situ hydrocarbon production - Google Patents
Subsurface heater configuration for in situ hydrocarbon production Download PDFInfo
- Publication number
- WO2016195511A1 WO2016195511A1 PCT/NO2016/050115 NO2016050115W WO2016195511A1 WO 2016195511 A1 WO2016195511 A1 WO 2016195511A1 NO 2016050115 W NO2016050115 W NO 2016050115W WO 2016195511 A1 WO2016195511 A1 WO 2016195511A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- heaters
- subsurface
- oil shale
- columns
- shale formation
- Prior art date
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 41
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 15
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 15
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 15
- 238000011065 in-situ storage Methods 0.000 title description 4
- 239000004058 oil shale Substances 0.000 claims abstract description 68
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 62
- 239000010410 layer Substances 0.000 description 58
- 238000005755 formation reaction Methods 0.000 description 55
- 238000010438 heat treatment Methods 0.000 description 20
- 239000012530 fluid Substances 0.000 description 15
- 230000004907 flux Effects 0.000 description 13
- 238000000197 pyrolysis Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 7
- 238000005553 drilling Methods 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000000605 extraction Methods 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 238000004088 simulation Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910021532 Calcite Inorganic materials 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- -1 and if necessary Substances 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002734 clay mineral Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002506 iron compounds Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
-
- 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
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
-
- 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
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/005—Heater surrounding production tube
-
- 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
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/006—Combined heating and pumping means
-
- 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
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/008—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using chemical heat generating means
-
- 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
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/04—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using electrical heaters
Definitions
- the invention is concerned with a configuration of subsurface heaters for use in hydrocarbon production, and more particular to a configuration of subsurface heaters for heating kerogen.
- Oil shale is a sedimentary rock which includes an organic mixture of complex chemical compounds, collectively referred to as "kerogen".
- the oil shale consists of laminated sedimentary rock containing mainly clay minerals, quartz, calcite, dolomite, and iron compounds. Oil shale can vary in its mineral and chemical composition.
- oil shale When oil shale is heated to around 350 °C, pyrolysis (a destructive distillation of the kerogen) occurs to produce hydrocarbon products in the form of inter alia oil and gas.
- the hydrocarbon products resulting from the pyrolysis of the kerogen have characteristics that are similar to that of other petroleum products. Oil shale is considered to have potential to become an important future source of liquid fuels and natural gas, which are currently produced from other petroleum sources.
- Heating methods include hot gas or liquid injection, closed loop circulation of hot gas (such as flue gas, propane, methane or superheated steam), closed loop circulation of hot liquid (such as a molten salt, water or oil), electric resistive heating, dielectric heating, microwave heating, downhole gas burners or oxidant injection to support in situ pyrolysis.
- hot gas such as flue gas, propane, methane or superheated steam
- closed loop circulation of hot liquid such as a molten salt, water or oil
- electric resistive heating dielectric heating
- microwave heating downhole gas burners or oxidant injection to support in situ pyrolysis.
- heating wells and production wells are provided in the subsurface oil shale formation. Hot fluid is pumped down into the heating wells, where its heat is transferred to the oil shale, and the cooled fluid is then returned to the surface. The fluid can be reheated in surface facilities before being returned to the oil shale, and if necessary, impurities in the heating fluid that have been picked up in the subsurface oil shale formation can be removed. The hydrocarbon products resulting from the pyrolysis of the kerogen can be extracted through the production wells. In situ production of oil and gas from kerogen in oil shale has not yet been carried out commercially. Both vertical and horizontal heating and production wells are described in various publications. Various configurations and geometries of patterns of heating wells and production wells have been proposed in an attempt to optimize heating of the subsurface formation.
- a problem with the heating process is that that the heating rate is very slow. Heat is transported in the subsurface formation mainly by thermal conduction, and is limited by the low thermal conductivity of the oil shale. Because of the slow heating rate, the use of a closely spaced regular pattern of heating wells has been suggested, but this leads to a high surface footprint, and increases the risk of drilling into heaters that are already in operation Even with closely spaced heaters, it is predicted that a subsurface formation may take years to come to a suitable uniform temperature.
- the invention has been made in view of the above circumstances, and it is an object of at least the preferred embodiments of the invention to increase the rate of heating of subsurface oil shale formations.
- a configuration of elongate subsurface heaters in a subsurface oil shale formation for use in hydrocarbon production wherein the heaters are grouped into a series of columns, the columns extending generally perpendicular to the sedimentary layers of the subsurface oil shale formation.
- each column will generate a "wall" of heat, in that the heat flux from each heater will be augmented by the heat flux from the heaters above and below it. This provides a much larger heat flux than can be generated by a single heater, and allows the subsurface oil shale formation to be brought to a desired temperature more quickly.
- the heaters can be arranged at any suitable distance from each other.
- the distance between adjacent columns, measured along the sedimentary layers is between 10 and 100 metres.
- This provides large gaps between the columns, and production wells may be arranged between the columns of heaters without any risk of the heaters being damaged during drilling of the production wells.
- the heaters are arranged to extend generally along the sedimentary layers of the subsurface oil shale formation. It is known that the thermal conductivity of a subsurface oil shale formation is larger along the sedimentary layers than across the sedimentary layers. As the heaters extend generally along the sedimentary layers of the subsurface oil shale formation, the heat flux generated will be in the preferred direction of thermal conductivity, and this will reduce the time required to bring the subsurface oil shale formation to a desired temperature.
- the heaters may also be grouped into a series of layers, each layer of heaters extending in one sedimentary layer of the subsurface oil shale formation.
- the heaters need not extend exactly along a single sedimentary layer; for example, if the sedimentary layers are not completely planar, the heaters can approximately follow the layer.
- the orientation of the heaters also does not need to be perfectly aligned with the orientation of the layers, and the heaters can extend at an angle of up to 30 degrees to the sedimentary layers.
- the distance between adjacent heaters, measured across the sedimentary layers is between 2 and 30 metres.
- a layer of crossing heaters is arranged in a layer above the uppermost heaters in the columns, the angle between the crossing heaters and the uppermost heaters in the columns being at least 60°, and preferably around 90°.
- Other layers of crossing heaters may also be provided lower in the column.
- the crossing heaters will increase the temperature of the formation around them. It is known that the permeability of a subsurface oil shale formation increases with increasing temperature, and so the heated regions around the crossing heaters will be more susceptible to fluid flow. The crossing heaters thus allow products generated by pyrolysis near the columns to flow to the production wells more easily.
- At least one generally vertical production well is arranged between each pair of columns.
- a single production well can be used to gather products arising from pyrolysis near two adjacent columns of heaters. It is also possible to use two production wells, one near each column, or more production wells if appropriate.
- a production well is arranged in a layer above the crossing heaters, and extends generally parallel to the heaters in the columns. With this arrangement, the production well will extend across the crossing heaters. Products generated by pyrolysis, flowing near the crossing heaters, can thus be gathered by a single production well, simplifying the necessary
- Figure 1 is a schematic cross-sectional side view of a subsurface oil shale formation, showing an exemplary arrangement of heaters
- Figure 2 is a schematic cross-sectional side view of a second subsurface oil shale formation, showing how the arrangement of heaters can be changed depending on the characteristics of the subsurface oil shale formation;
- Figure 3 is a schematic view of a model of an exemplary arrangement of heaters and production piping
- Figure 4 is a schematic cross-sectional view showing heat flux in the exemplary arrangement of Figure 3.
- Figure 5 is a schematic view showing the order in which the various wells in the exemplary arrangement of Figure 3 are formed.
- a series of horizontal heaters (which may be of any suitable length) are drilled into the subsurface oil shale formation in a pattern in which the heaters are grouped into columns.
- Figure 1 shows a schematic cross-sectional view of the subsurface oil shale formation 10 with the heaters 20 drilled into it, and it can be seen that the heaters 20 are arranged in columns 40 which are generally parallel to each other, and generally perpendicular to the sedimentary structure 50 of the subsurface oil shale formation 10. Further, the heaters are arranged in layers 30 which extend generally parallel to the sedimentary layers 50 of the subsurface oil shale formation 10.
- the heaters 20 use a closed-loop circulating fluid, which can be any suitable fluid, such as molten salt, water, oil, steam, flue gas, oils, or gases.
- a closed-loop circulating fluid can be any suitable fluid, such as molten salt, water, oil, steam, flue gas, oils, or gases.
- the heaters 20 can use an injection fluid, and any suitable fluid can be used as the injection fluid, such as hydrocarbon liquids, gases and/or steam.
- electrical heating could also be used.
- the heat flux from a single heater placed relatively far from other heaters is small due to the nature of thermal conduction in radial geometry. Placing a number of heaters 20 close to one another in a column 40 will create a temperature front of a more linear character, since the heat flux from each individual heater will be reinforced by the heat flux from the heaters above and below. This gives a much higher heat flux than can be generated by a single heater, and reduces the time necessary to bring the subsurface oil shale formation 10 to a suitable temperature.
- the thermal conductivity of the subsurface oil shale formation 10 is lower for heat flux in the vertical direction (across the sedimentary layers 50 of the subsurface oil shale formation 10) than for heat flux in the horizontal direction (along the sedimentary layers 50 of the subsurface oil shale formation 10).
- Arranging the heaters 20 as a column 40, with the heaters 20 extending generally parallel to the sedimentary layers 50, and the column 40 extending in a direction generally perpendicular to the sedimentary layers 50, will create a heat flux in the direction in which the thermal conductivity is greatest (that is, parallel to the sedimentary layers 50), and so further reduce the time necessary to bring the subsurface oil shale formation to a suitable temperature.
- providing a layer 30 of heaters 20 in a single sedimentary layer 50 will also increase the heat flux within that particular layer, and will also reduce the time necessary to bring the subsurface oil shale formation to a suitable temperature.
- production wells will be placed between the heaters 20.
- the production wells can take any suitable form, and any combination of horizontal and/or vertical production wells, and any position of and number of production wells, may be used.
- Figure 2 shows an arrangement in which the sedimentary layers 150 of the oil shale are not horizontal throughout the entire subsurface oil shale formation 1 10 (which will in practice be the case). Specifically, Figure 2 shows an arrangement with a change 160 in the direction of the layers in the subsurface oil shale formation 1 10, so that the sedimentary layers 150 are substantially horizontal at the left side of Figure 2, but are angled downwards to the right at the right side of Figure 2.
- the layers 1 30 on the left side of Figure 2 are shown as extending horizontally, along the horizontal sedimentary layers 150 of the subsurface oil shale formation 1 10, and the columns 140 on the left side of Figure 2 are shown as extending vertically, perpendicular to the horizontal sedimentary layers 150 of the subsurface oil shale formation 110.
- the layers 130 on the right side of Figure 2 extend at an angle to the horizontal, so that they still extend along the (non-horizontal) sedimentary layers 150 of the subsurface oil shale formation 110.
- the columns 140 on the right side of Figure 2 extend upwards at an angle to the vertical, so that they are still perpendicular to the (non- horizontal) sedimentary layers 150 of the subsurface oil shale formation 110.
- the heaters when the heaters are referred to as "horizontal”, this means that the heaters extend generally along the sedimentary layers of the subsurface oil shale formation. If the sedimentary layers of the subsurface oil shale formation are not completely horizontal, but are angled with respect to the horizontal (in a direction extending into or out of the plane of the Figures), then the heaters can be formed at a corresponding angle, to ensure that they extend along the sedimentary layers.
- the heaters need not be arranged exactly parallel with the sedimentary layers of the subsurface oil shale formation; beneficial effects can still be achieved with differences of up to 30 degrees between the orientation of the sedimentary layers and the directions of the heaters, as long as the heaters extend along the sedimentary layers.
- a disadvantage of arranging a large number of heating wells in a closely spaced regular pattern is that the resulting surface footprint is very large, as each new heater requires a new well to be drilled.
- This problem may be overcome by arranging heaters in columns, as each column of heaters may be drilled horizontally from a single wellpad. The arrangement of columns of heaters will result in rows of closely spaced wellheads, which will be gathered in distributed well pads, and this will reduce the surface footprint.
- the vertical distance between the layers (that is, the distance between adjacent heaters in a column measured across the sedimentary layers of the subsurface oil shale formation), and the horizontal distance between the columns (that is, the distance between adjacent columns measured along the sedimentary layers of the subsurface oil shale formation), can be varied depending on the characteristics of the subsurface oil shale formation.
- the vertical distance may be between 2 and 30 metres, and the horizontal distance may be between 10 and 100 meters.
- configuration according to the invention can have a lower surface footprint, and can be implemented using a simpler drilling programme, than the configuration with evenly distributed heaters.
- Figures 3 to 5 show a further exemplary arrangement of heaters and a production well.
- the arrangement consists of two vertical parallel columns 300 of horizontal heaters 310, above which is a layer of crossing heaters 320 (only one of which is visible in Figure 4).
- These crossing heaters 320 are shown as extending perpendicular to the heaters 310 in the columns 300; however, the angle between the heaters does not need to be 90°. If the heaters do not cross perpendicularly, then it is preferred for the acute angle at the crossing point to be no less than 60°.
- the horizontal distance between two adjacent crossing heaters in the actual subsurface oil shale formation may be between 20 and 200 metres.
- a production well 330 Above the layer of crossing heaters 320 is arranged a production well 330.
- the production well 330 is shown as extending parallel to the heaters 310 in the columns 300 and perpendicular to the crossing heaters 320; however, any appropriate orientation can be used for the production well. Further, the production well 330 is placed between the columns 300 of heaters, and is preferably located generally horizontally midway between two adjacent columns.
- the "horizontal" heaters will in practice extend generally along the sedimentary layers of the subsurface shale formation, and so may not be exactly horizontal.
- Figure 4 shows the pattern of fluid flow in the arrangement of Figure 3.
- a heated oil shale formation has higher permeability than a cold oil shale formation, and so fluid flow will be greater in the areas which are warmer.
- Figure 5 shows the order in which the various wells and heaters are preferably formed in the third exemplary embodiment.
- the production well 330 is formed.
- the layer of crossing heaters 320 underneath the production well 330 is formed, and operation of this first layer of crossing heaters 320 is commenced, to start to heat the subsurface oil shale formation.
- the regions near the crossing heaters 320 will undergo pyrolysis to produce hydrocarbon products before the rest of the subsurface oil shale formation, as they are the first regions to be heated. Extraction of hydrocarbon products resulting from pyrolysis in the regions near the crossing heaters 320 can begin while the vertical parallel columns 300 of horizontal heaters 310 are still heating the subsurface oil shale formation (and, in some cases, even before the columns 300 have been completed), and so extraction of the hydrocarbon products can be started earlier. The heat supply to the crossing heaters can be stopped once extraction of the hydrocarbon products has started.
- Figure 5 shows two columns 300 of heaters 310 and the production well 330 being arranged in a "block"; several blocks can be arranged side by side in a repeating pattern in the subsurface oil shale formation.
- Figures 3 to 5 show an arrangement with a single layer of crossing heaters, arranged between the top layer of the vertical parallel columns of horizontal heaters and the production well.
- the layer of crossing heaters it would of course be possible for the layer of crossing heaters to be placed further down in the columns. It would also be possible to provide more than one layer of crossing heaters, so that the heaters would have a lattice arrangement.
- the exact details of the arrangement of heaters will of course depend on the particular details of the subsurface oil shale formation.
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201680032882.7A CN108026767A (zh) | 2015-06-05 | 2016-06-03 | 用于原位烃生产的地下加热器布置 |
US15/579,380 US20180179875A1 (en) | 2015-06-05 | 2016-06-03 | Subsurface heater configuration for in situ hydrocarbon production |
CA2988309A CA2988309A1 (en) | 2015-06-05 | 2016-06-03 | Subsurface heater configuration for in situ hydrocarbon production |
EP16803826.3A EP3303764A4 (en) | 2015-06-05 | 2016-06-03 | UNDERGROUND HEATER CONFIGURATION FOR IN-SITU HYDROCARBON PRODUCTION |
AU2016271985A AU2016271985A1 (en) | 2015-06-05 | 2016-06-03 | Subsurface heater configuration for in situ hydrocarbon production |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1509772.8A GB2539045A (en) | 2015-06-05 | 2015-06-05 | Subsurface heater configuration for in situ hydrocarbon production |
GB1509772.8 | 2015-06-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2016195511A1 true WO2016195511A1 (en) | 2016-12-08 |
Family
ID=53785005
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/NO2016/050115 WO2016195511A1 (en) | 2015-06-05 | 2016-06-03 | Subsurface heater configuration for in situ hydrocarbon production |
Country Status (7)
Country | Link |
---|---|
US (1) | US20180179875A1 (zh) |
EP (1) | EP3303764A4 (zh) |
CN (1) | CN108026767A (zh) |
AU (1) | AU2016271985A1 (zh) |
CA (1) | CA2988309A1 (zh) |
GB (1) | GB2539045A (zh) |
WO (1) | WO2016195511A1 (zh) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108487888B (zh) * | 2018-05-24 | 2023-04-07 | 吉林大学 | 用于提高油页岩原位开采油气采收率辅助加热装置及方法 |
CN114034125B (zh) * | 2021-10-20 | 2024-03-19 | 深圳市思野精机有限公司 | 一种注射针热风加温机构 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001081239A2 (en) * | 2000-04-24 | 2001-11-01 | Shell Internationale Research Maatschappij B.V. | In situ recovery from a hydrocarbon containing formation |
WO2002086276A2 (en) * | 2001-04-24 | 2002-10-31 | Shell Internationale Research Maatschappij B.V. | Method for in situ recovery from a tar sands formation and a blending agent produced by such a method |
US20040020642A1 (en) * | 2001-10-24 | 2004-02-05 | Vinegar Harold J. | In situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden |
WO2009129143A1 (en) * | 2008-04-18 | 2009-10-22 | Shell Oil Company | Systems, methods, and processes utilized for treating hydrocarbon containing subsurface formations |
US20100089584A1 (en) * | 2008-10-13 | 2010-04-15 | David Booth Burns | Double insulated heaters for treating subsurface formations |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4545435A (en) * | 1983-04-29 | 1985-10-08 | Iit Research Institute | Conduction heating of hydrocarbonaceous formations |
US4645004A (en) * | 1983-04-29 | 1987-02-24 | Iit Research Institute | Electro-osmotic production of hydrocarbons utilizing conduction heating of hydrocarbonaceous formations |
US7831134B2 (en) * | 2005-04-22 | 2010-11-09 | Shell Oil Company | Grouped exposed metal heaters |
KR101434226B1 (ko) * | 2005-10-24 | 2014-08-27 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | 지층으로부터 실질적으로 전기절연된 도관을 갖는 온도제한 히터 |
MX2009004127A (es) * | 2006-10-20 | 2009-06-05 | Shell Int Research | Calentamiento de formaciones de arenas de alquitran a temperaturas reductoras de la viscosidad. |
WO2012177346A1 (en) * | 2011-06-23 | 2012-12-27 | Exxonmobil Upstream Research Company | Electrically conductive methods for in situ pyrolysis of organic-rich rock formations |
CN103321618A (zh) * | 2013-06-28 | 2013-09-25 | 中国地质大学(北京) | 油页岩原位开采方法 |
-
2015
- 2015-06-05 GB GB1509772.8A patent/GB2539045A/en not_active Withdrawn
-
2016
- 2016-06-03 WO PCT/NO2016/050115 patent/WO2016195511A1/en active Application Filing
- 2016-06-03 EP EP16803826.3A patent/EP3303764A4/en not_active Withdrawn
- 2016-06-03 CA CA2988309A patent/CA2988309A1/en not_active Abandoned
- 2016-06-03 AU AU2016271985A patent/AU2016271985A1/en not_active Abandoned
- 2016-06-03 CN CN201680032882.7A patent/CN108026767A/zh active Pending
- 2016-06-03 US US15/579,380 patent/US20180179875A1/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001081239A2 (en) * | 2000-04-24 | 2001-11-01 | Shell Internationale Research Maatschappij B.V. | In situ recovery from a hydrocarbon containing formation |
WO2002086276A2 (en) * | 2001-04-24 | 2002-10-31 | Shell Internationale Research Maatschappij B.V. | Method for in situ recovery from a tar sands formation and a blending agent produced by such a method |
US20040020642A1 (en) * | 2001-10-24 | 2004-02-05 | Vinegar Harold J. | In situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden |
WO2009129143A1 (en) * | 2008-04-18 | 2009-10-22 | Shell Oil Company | Systems, methods, and processes utilized for treating hydrocarbon containing subsurface formations |
US20100089584A1 (en) * | 2008-10-13 | 2010-04-15 | David Booth Burns | Double insulated heaters for treating subsurface formations |
Non-Patent Citations (1)
Title |
---|
See also references of EP3303764A4 * |
Also Published As
Publication number | Publication date |
---|---|
US20180179875A1 (en) | 2018-06-28 |
CA2988309A1 (en) | 2016-12-08 |
AU2016271985A1 (en) | 2017-12-21 |
EP3303764A1 (en) | 2018-04-11 |
CN108026767A (zh) | 2018-05-11 |
GB201509772D0 (en) | 2015-07-22 |
GB2539045A (en) | 2016-12-07 |
EP3303764A4 (en) | 2019-02-13 |
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