WO2013097668A1 - 油页岩开采方法 - Google Patents
油页岩开采方法 Download PDFInfo
- Publication number
- WO2013097668A1 WO2013097668A1 PCT/CN2012/087277 CN2012087277W WO2013097668A1 WO 2013097668 A1 WO2013097668 A1 WO 2013097668A1 CN 2012087277 W CN2012087277 W CN 2012087277W WO 2013097668 A1 WO2013097668 A1 WO 2013097668A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas
- oil shale
- oil
- combustible gas
- oxygen
- Prior art date
Links
- 239000004058 oil shale Substances 0.000 title claims abstract description 85
- 238000000034 method Methods 0.000 title claims abstract description 35
- 239000007789 gas Substances 0.000 claims abstract description 96
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000001301 oxygen Substances 0.000 claims abstract description 21
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 21
- 238000002309 gasification Methods 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 11
- 238000005979 thermal decomposition reaction Methods 0.000 claims abstract description 6
- 238000005065 mining Methods 0.000 claims description 15
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 12
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 7
- 239000001294 propane Substances 0.000 claims description 6
- 238000005553 drilling Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000011049 filling Methods 0.000 claims description 2
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 2
- 239000011707 mineral Substances 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract 1
- 238000002485 combustion reaction Methods 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 4
- 229930195733 hydrocarbon Natural products 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 238000000197 pyrolysis Methods 0.000 description 4
- 239000011435 rock Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000009412 basement excavation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000013351 cheese Nutrition 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 238000003895 groundwater pollution Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
- E21B43/243—Combustion in situ
-
- 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
- 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
- E21B43/164—Injecting CO2 or carbonated water
-
- 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
- E21B43/166—Injecting a gaseous medium; Injecting a gaseous medium and a liquid medium
- E21B43/168—Injecting a gaseous medium
-
- 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
- E21B43/34—Arrangements for separating materials produced by the well
- E21B43/40—Separation associated with re-injection of separated materials
-
- 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
- E21B43/243—Combustion in situ
- E21B43/247—Combustion in situ in association with fracturing processes or crevice forming processes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/70—Combining sequestration of CO2 and exploitation of hydrocarbons by injecting CO2 or carbonated water in oil wells
Definitions
- the invention relates to the field of in situ underground oil shale mining methods. Background technique
- Oil shale refers to fine-grained sedimentary rocks with high kerogen content and capable of fractionating a considerable amount of petroleum. Solids combustible organic matter with ash content greater than 40% and oil content between 3.5% and 30%. Oil shale The difference between rock and coal is that its ash mass fraction is greater than 40%.
- Ground treatment includes: oil shale mining and ore preparation; heating decomposition to produce oil mother; processing oil master to produce refining raw materials and useful chemicals, including "underground mining, ground retorting" and "ground mining, ground Dry distillation” two general methods.
- oil shale ore is mined, transported to the ground, pulverized, and then heated in a ground container to produce fuel liquids and gases; for the latter, oil shale ore is mined, then pulverized and retorted.
- the treated slag is piled up at the mine or elsewhere.
- underground processing Heating oil shale resources in the natural sedimentary environment of oil shale to produce oil masters, thereby minimizing or eliminating the thermal decomposition of the mining process and the ground.
- the heat used to reach the underground thermal decomposition temperature was derived from the combustion of one end of the oil shale ore.
- ideas have been changed, such as trying to promote heat transfer and fluid flow in oil shale through fractured rock layers, thereby improving the underground combustion process. Thermal decomposition efficiency and recovery factor.
- Third, mixed processing The oil shale resources of the near surface are first processed on the ground, and then slowly heated for underground mining in the pit formed by excavation of the rock.
- an object of the present invention is to provide an oil shale mining method by introducing an oxygen-containing gas (for example, oxygen) and flammable through a different pipe from an intake pipe end. The gas is then ignited and piped to the underground oil shale layer to heat the oil shale deposit by self-heating and external heat to produce oil and gas to achieve rapid, large-scale, economical and rational exploitation of oil and gas from the oil shale deposit. the goal of.
- an oxygen-containing gas for example, oxygen
- an oil shale mining method comprising: forming an intake duct and an outflow duct in the oil shale; forming the intake duct in the oil shale to communicate with the a gasification passage of the outlet pipe; the combustible gas and the oxygen-containing gas are respectively sent into the oil shale layer through the different intake pipes, and then the flammable gas is sent to the underlying flammable gas in an aerobic environment.
- a lower end nozzle of the combustible gas line is ignited to heat the oil shale; and an oil and gas mixed product formed by thermal decomposition of the kerogen in the oil shale is recovered through an air outlet duct
- the method further comprises: pressurizing the gasification passage to form a gap in the oil shale.
- the method further comprises: separating co 2 from the gas discharged from the gas outlet pipe, and introducing the separated co 2 into the oil shale through a separate pipe or an annulus pipe, wherein The annulus is a portion of the pipe that is placed between two concentric pipes.
- the method further comprises: separating a combustible gas from the mixed oil and gas product recovered from the gas outlet pipe, and introducing the combustible gas into the oil shale through a separate pipe or an annulus tube, wherein The annulus is a portion of the conduit disposed between two concentric conduits.
- the combustible gas comprises decane or propane or a combination thereof.
- the pressurizing comprises pressurizing the pressurized medium by a gas or a liquid.
- heating the oil shale further comprises: introducing a combustible gas from the outside into the oil shale through a separate conduit.
- the combustible gas comprises decane, propane or a combination thereof.
- the outlet duct and the intake duct are communicated by horizontal drilling or filling with high pressure gas or adding water between the intake duct and the outlet duct.
- the oxygen-containing gas has an oxygen content greater than 20%, or the oxygen-containing gas is oxygen.
- the present invention utilizes a simple, inexpensive, and practical process for mining oil shale deposits and is environmentally friendly.
- the method of the invention has simple process, low energy consumption, and can heat the cheese root in the shale layer, thereby more economically and rationally exploiting the oil shale deposit layer to obtain oil and gas products.
- FIG. 1 is a schematic structural view of underground exploitation of oil shale according to an embodiment of the present invention
- FIG. 2 is a flow chart of a method of oil shale mining according to an embodiment of the present invention.
- the present invention provides an oil shale mining method.
- Embodiments of the invention are described in detail below, examples of which are illustrated in the accompanying drawings.
- the embodiments described below with reference to the accompanying drawings are intended to be illustrative only, and are not to be construed as limiting.
- the present invention arranges an intake pipe 1 (or an injection well) and an exhaust pipe 3 (or a production well) at a suitable well spacing by a drilling related technique (shown in FIG. 2).
- Step S1 as shown in Figure 1.
- the prefabricated gasification passage 5 is formed by, for example, horizontally directional drilling of the oil shale layer 7 between the intake duct 1 and the exhaust duct 3 (step S2), thereby constructing an oil shale underground mining structure diagram, as shown in FIG.
- the intake duct 1 and the exhaust duct 3 can also be made to communicate by introducing high-pressure gas into the intake duct 1, thereby forming a gasification passage.
- the oil shale layer 7 between the intake passage 1 and the exhaust passage 3 can be opened by water pressure by pouring water into the intake passage 1, thereby in the intake passage 1 and A gasification passage 5 is formed between the exhaust passages 3.
- the gasification passage may be further pressurized, for example, by using a gas or a liquid as a pressurized medium to the underground oil.
- Shale mine Layer 7 is pressurized to form a gap in the oil shale layer that causes the oil shale layer 7 to loosen, which facilitates heating of the oil shale in subsequent operations.
- An oxygen-containing gas for example, 0 2 , a gas containing more than 20% of oxygen is introduced from the end of the intake pipe, and then the combustible gas is ignited and piped to the underground oil shale layer, or fed in an aerobic environment.
- the lower combustible gas is ignited at the lower end of the pipeline for conveying the combustible gas, and the oil shale layer is heated by the combustion of the external gas, and the oil shale itself is also heated by the combustion of part of the oil shale, that is,
- the oil shale layer is heated by self-heating and external heat (step S3), and the kerogen therein is pyrolyzed to form an oil-gas mixture product.
- the oxygen-containing gas and the combustible gas are respectively introduced through separate pipes. Further, the oil-gas mixture product obtained in the underground gasification furnace is pumped to the surface through the exhaust passage 3, and the light oil product and the gas product are obtained by separation or the like (step S4).
- the above combustible gas can be directly added from the outside through a separate pipe, such as decane, propane or a combination thereof.
- a separate pipe such as decane, propane or a combination thereof.
- the above combustible gas can also be separated from the oil shale pyrolysis oil and gas mixture product.
- a hydrocarbon gas such as decane, propane or a combination thereof, and a combustible gas is introduced through a separate pipe or an annulus tube, which is a pipe portion disposed between two concentric pipes.
- the CO 2 separated from the oil shale pyrolysis oil and gas mixture product is injected back into the oil shale deposit layer 7 through a separate pipeline or an annulus tube.
- a separate pipeline or an annulus tube for introducing an oxygen-containing gas (not shown) is provided in the intake duct 1 in a portion between the intake duct 1 and the other duct for introducing an oxygen-containing gas.
- the combustible gas separated from the oil and gas mixed product obtained through the exhaust passage 3 is returned to the underground oil shale ore layer for combustion, fuels the underground heating, and heats the oil shale deposit layer to make the The kerogen pyrolysis forms a mixture of oil and gas.
- the invention constructs a certain amount of intake/outflow in the oil shale underground deposit layer by means of drilling
- the gas pipeline forms a gasification passage between the inlet and outlet pipes in the underground ore layer by means of pressure fracturing, etc., and then an oxygen-containing gas is introduced into the inlet pipe end, and then ignited and piped to the underground oil shale layer.
- the oil shale layer is heated by self-heating and external heat, and the kerogen therein is pyrolyzed to form an oil-gas mixture product.
- tar and/or other products which may be produced from the oil shale deposit are obtained from the production well, and the obtained combustible gas can be partially returned to the underground oil shale ore layer for combustion and heating, and the above products are continuously produced.
- the present invention achieves the purpose of rapidly and massively and economically rationally extracting oil and gas from an oil shale deposit.
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)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US14/369,764 US9382789B2 (en) | 2011-12-29 | 2012-12-24 | Oil shale exploitation method |
AU2012361948A AU2012361948A1 (en) | 2011-12-29 | 2012-12-24 | Oil shale exploitation method |
CA2861909A CA2861909C (en) | 2011-12-29 | 2012-12-24 | Oil shale exploitation method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110452216.8A CN102425399B (zh) | 2011-12-29 | 2011-12-29 | 油页岩开采方法 |
CN201110452216.8 | 2011-12-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2013097668A1 true WO2013097668A1 (zh) | 2013-07-04 |
Family
ID=45959424
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2012/087277 WO2013097668A1 (zh) | 2011-12-29 | 2012-12-24 | 油页岩开采方法 |
Country Status (5)
Country | Link |
---|---|
US (1) | US9382789B2 (zh) |
CN (1) | CN102425399B (zh) |
AU (1) | AU2012361948A1 (zh) |
CA (1) | CA2861909C (zh) |
WO (1) | WO2013097668A1 (zh) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113374460A (zh) * | 2021-06-23 | 2021-09-10 | 沈阳化工大学 | 自热式地下干馏油页岩提取页岩油和高热值燃料气的方法 |
CN114412419A (zh) * | 2022-01-21 | 2022-04-29 | 中国矿业大学 | 一种叠置煤层气藏高效闭环抽采的方法 |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102425399B (zh) * | 2011-12-29 | 2015-06-10 | 新奥气化采煤有限公司 | 油页岩开采方法 |
CN103232852B (zh) * | 2013-04-28 | 2014-03-26 | 吉林省众诚汽车服务连锁有限公司 | 油页岩原位竖井压裂化学干馏提取页岩油气的方法及工艺 |
CN103470223B (zh) * | 2013-09-23 | 2015-11-25 | 中国矿业大学(北京) | 一种化石能源低碳共采的方法和*** |
CN103790563B (zh) * | 2013-11-09 | 2016-06-08 | 吉林大学 | 一种油页岩原位局部化学法提取页岩油气的方法 |
CN104747143A (zh) * | 2013-12-31 | 2015-07-01 | 天津建筑机械厂 | 井下燃烧甲烷稀释重油工艺 |
CN104653166B (zh) * | 2014-12-24 | 2019-02-12 | 新奥科技发展有限公司 | 煤炭地下气化过程中汇水量控制方法及煤炭地下气化方法 |
CN105840162B (zh) * | 2016-05-17 | 2019-09-17 | 赵金岷 | 地下燃烧对流加热方法 |
CN107091076B (zh) * | 2017-07-06 | 2019-04-12 | 苏州大学 | 页岩气的开采方法及*** |
CN107474868B (zh) * | 2017-09-29 | 2023-06-27 | 新疆国利衡清洁能源科技有限公司 | 油页岩地下制油***及其制油方法 |
CN109113699B (zh) | 2018-07-12 | 2021-03-30 | 中国石油天然气股份有限公司 | 一种页岩油原位轻质化开发方法、装置及*** |
CN109577937A (zh) * | 2018-12-10 | 2019-04-05 | 中国石油大学(北京) | 油页岩原位开采的方法和装置 |
CN110259424B (zh) * | 2019-07-17 | 2020-07-28 | 中国石油大学(北京) | 一种原位开采油页岩的方法和装置 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1814987A (zh) * | 2006-02-24 | 2006-08-09 | 尤尼斯油气技术(中国)有限公司 | 一种变质岩潜山高凝油油藏火驱采油点火方法 |
CN101680284A (zh) * | 2007-05-15 | 2010-03-24 | 埃克森美孚上游研究公司 | 用于原位转化富含有机物岩层的井下燃烧器井 |
US20100175872A1 (en) * | 2009-01-15 | 2010-07-15 | Conocophillips Company | In situ combustion as adjacent formation heat source |
US20110011582A1 (en) * | 2009-07-17 | 2011-01-20 | Conocophillips Company | In situ combustion with multiple staged producers |
CN102287175A (zh) * | 2011-05-13 | 2011-12-21 | 中国海洋石油总公司 | 一种利用热动力开采页岩气和/或页岩油的方法 |
CN102425399A (zh) * | 2011-12-29 | 2012-04-25 | 新奥气化采煤有限公司 | 油页岩开采方法 |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IL158427A0 (en) * | 2001-04-24 | 2004-05-12 | Shell Int Research | In-situ combustion for oil recovery |
US8146664B2 (en) * | 2007-05-25 | 2012-04-03 | Exxonmobil Upstream Research Company | Utilization of low BTU gas generated during in situ heating of organic-rich rock |
-
2011
- 2011-12-29 CN CN201110452216.8A patent/CN102425399B/zh active Active
-
2012
- 2012-12-24 AU AU2012361948A patent/AU2012361948A1/en not_active Abandoned
- 2012-12-24 US US14/369,764 patent/US9382789B2/en active Active
- 2012-12-24 WO PCT/CN2012/087277 patent/WO2013097668A1/zh active Application Filing
- 2012-12-24 CA CA2861909A patent/CA2861909C/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1814987A (zh) * | 2006-02-24 | 2006-08-09 | 尤尼斯油气技术(中国)有限公司 | 一种变质岩潜山高凝油油藏火驱采油点火方法 |
CN101680284A (zh) * | 2007-05-15 | 2010-03-24 | 埃克森美孚上游研究公司 | 用于原位转化富含有机物岩层的井下燃烧器井 |
US20100175872A1 (en) * | 2009-01-15 | 2010-07-15 | Conocophillips Company | In situ combustion as adjacent formation heat source |
US20110011582A1 (en) * | 2009-07-17 | 2011-01-20 | Conocophillips Company | In situ combustion with multiple staged producers |
CN102287175A (zh) * | 2011-05-13 | 2011-12-21 | 中国海洋石油总公司 | 一种利用热动力开采页岩气和/或页岩油的方法 |
CN102425399A (zh) * | 2011-12-29 | 2012-04-25 | 新奥气化采煤有限公司 | 油页岩开采方法 |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113374460A (zh) * | 2021-06-23 | 2021-09-10 | 沈阳化工大学 | 自热式地下干馏油页岩提取页岩油和高热值燃料气的方法 |
CN114412419A (zh) * | 2022-01-21 | 2022-04-29 | 中国矿业大学 | 一种叠置煤层气藏高效闭环抽采的方法 |
CN114412419B (zh) * | 2022-01-21 | 2022-09-09 | 中国矿业大学 | 一种叠置煤层气藏高效闭环抽采的方法 |
Also Published As
Publication number | Publication date |
---|---|
CN102425399A (zh) | 2012-04-25 |
US9382789B2 (en) | 2016-07-05 |
US20140352957A1 (en) | 2014-12-04 |
CN102425399B (zh) | 2015-06-10 |
CA2861909C (en) | 2017-02-28 |
AU2012361948A1 (en) | 2014-06-26 |
CA2861909A1 (en) | 2013-07-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2013097668A1 (zh) | 油页岩开采方法 | |
CN103670357B (zh) | 地下含碳有机矿物储层的裂隙沟通、通道加工及地下气化方法 | |
CN103232852B (zh) | 油页岩原位竖井压裂化学干馏提取页岩油气的方法及工艺 | |
CN103233713B (zh) | 油页岩原位水平井压裂化学干馏提取页岩油气方法及工艺 | |
CN102418476A (zh) | 深层煤炭和煤层气联合开采技术 | |
WO2013026421A1 (zh) | 一种地下煤炭气化的方法 | |
CN108756839B (zh) | 油页岩隔热增效原位转化方法及*** | |
CN103670338A (zh) | 一种煤层气与煤共采方法 | |
CN102444397A (zh) | 开采深层油页岩制取页岩油和油页岩气的方法 | |
CN101871339A (zh) | 一种地下原位提取油页岩中烃类化合物的方法 | |
CN103790563A (zh) | 一种油页岩原位局部化学法提取页岩油气的方法 | |
CN111396010B (zh) | 煤层气田清洁取能***及方法 | |
CN109736762A (zh) | 一种油页岩原位催化氧化法提取页岩油气的方法 | |
CN102383772A (zh) | 钻井式油页岩原位气化干馏制油气***及其工艺方法 | |
CN203499663U (zh) | 用于油页岩原位水平井压裂化学干馏提取页岩油气的装置 | |
CN209569001U (zh) | 一种油页岩原位开采井下点火加热装置 | |
CN101555783A (zh) | 联合开采煤田甲烷气、挥发物及炭或油田油气的设施装置及其开采方法 | |
CN111608624B (zh) | 一种利用地热开采稠油油藏的方法 | |
CN113464103A (zh) | 一种在井下制备纳米催化剂的原位裂解与改质方法 | |
CN109707356A (zh) | 一种油页岩原位开采井下点火加热装置及加热方法 | |
CN102287175A (zh) | 一种利用热动力开采页岩气和/或页岩油的方法 | |
CN103470223A (zh) | 一种化石能源低碳共采的方法和*** | |
CN203476308U (zh) | 一种化石能源共存区域的煤炭地下气化开采*** | |
CN114876429B (zh) | 利用井筒催化生热开采稠油油藏的方法 | |
CN101775309A (zh) | 利用高温气冷堆进行油砂炼油的方法及专用设备 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 12863556 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 2012361948 Country of ref document: AU Date of ref document: 20121224 Kind code of ref document: A |
|
ENP | Entry into the national phase |
Ref document number: 2861909 Country of ref document: CA |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 14369764 Country of ref document: US |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 12863556 Country of ref document: EP Kind code of ref document: A1 |