CN104594859B - A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation - Google Patents

A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation Download PDF

Info

Publication number
CN104594859B
CN104594859B CN201510014844.6A CN201510014844A CN104594859B CN 104594859 B CN104594859 B CN 104594859B CN 201510014844 A CN201510014844 A CN 201510014844A CN 104594859 B CN104594859 B CN 104594859B
Authority
CN
China
Prior art keywords
nano
fine
water
fluid
oil reservoir
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510014844.6A
Other languages
Chinese (zh)
Other versions
CN104594859A (en
Inventor
鹿腾
李兆敏
李松岩
王继乾
张兴鲁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China University of Petroleum East China
Original Assignee
China University of Petroleum East China
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China University of Petroleum East China filed Critical China University of Petroleum East China
Priority to CN201510014844.6A priority Critical patent/CN104594859B/en
Publication of CN104594859A publication Critical patent/CN104594859A/en
Application granted granted Critical
Publication of CN104594859B publication Critical patent/CN104594859B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
    • C09K8/584Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/20Displacing by water
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/10Nanoparticle-containing well treatment fluids

Abstract

The present invention relates to a kind of method that nano-fluid exploits fine and close oily oil reservoir.This method comprises the following steps:Nano-fluid slug is injected into fine and close oily oil reservoir, then water filling and is exploited into oil reservoir by injection well, waterflood injection rate is less than 1.4m/d.In the method for the present invention, the close oily reservoir of oily humectation can be the wet reservoir of water anyway by nano-fluid slug, and the water being subsequently implanted into dialysis can enter Medium Culture under the action of capillary force, so as to employ Medium Culture remaining oil;Low speed water filling can be to avoid sudden water flooding caused by injection water along the quick channelling in crack;Water filling can supplement the stratum energy after compact oil reservoir primary oil recovery.

Description

A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation
Technical field
The invention belongs to fine and close oily oil reservoir production technique field, is related to a kind of side of the fine and close oil oil reservoir of nano-fluid exploitation Method.
Background technology
With the development that deepens continuously of oil-gas exploration and development, the unconventional oil such as tight gas, shale gas, coal bed gas, fine and close oil Gas illustrates huge potentiality under the conditions of existing economic technology, and Global Oil and Gas Resources will welcome secondary extension.Fine and close oil refers to Stored up with absorption or free state preservation in oil source rock or with oil source rock alternating layers, adjacent tight sand, dense carbonate etc. Collect in rock, without the oil accumulation of extensive long-distance migration.The fine and close oily reservoir in China has the spies such as low hole, hypotonic, low pressure Sign, effective exploitation face lot of challenges.The fine and close oily reservoir exploitation general oil production at initial stage in China is of a relatively high, but by reservoir properties Difference, strata pressure is low and single well controlled reserves is few influence, production decline quickly, lapse rate up to 40%~90%, even if using Horizontal well massive hydraulic fracture, fine and close oil reservoir primary recovery efficiency is also only 5%~10%, and massive hydraulic fracture is transformed to be formed After Fracture Systems, subsequent waterflooding exploitation injection water is easily quickly advanced by leaps and bounds along crack, causes sudden water flooding, the crude oil of Medium Culture can not have Effect is employed, and water flooding effectiveness is poor.Therefore fine and close oily reservoir During Natural Depletion later stage energy supplement mode and use rate are inquired into Method is of great significance.
At present, fine and close oily reservoir is mainly using the exploitation of exhaustion formula and waterflooding extraction.The general oil production of exhaustion formula initial stage of development It is of a relatively high, but influenced by reservoir properties are poor, strata pressure is low and single well controlled reserves is few, natural energy is extremely limited, production Measure universal rapid decrement, the well that long 7 sections of conventional pressure breaks obtain commercial oil is averaged individual well tested production value 5.8t/d, and production yield is only 0.6~0.9t/d.Even if using horizontal well massive hydraulic fracture, fine and close oil reservoir primary recovery efficiency is also only 5%~10%. And fine and close oily massive hydraulic fracture is transformed after forming Fracture Systems, waterflooding development injection water is easily quickly advanced by leaps and bounds along crack, causes sudden and violent property Water logging, the crude oil of Medium Culture can not be employed effectively, and water flooding effectiveness is poor, and long 7 sections of fine and close oil is using straight well water filling, horizontal well The combination well pattern exploitation of oil recovery, horizontal well are shown in that injection water risk is big, and water breakthrough ratio reaches 65%.
The content of the invention
In view of the deficiencies of the prior art, the method that the present invention provides a kind of fine and close oily oil reservoir of nano-fluid exploitation.
Technical scheme is as follows:
A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation, step are as follows:
(1) nano-fluid slug is injected into fine and close oily oil reservoir;
The described oily oil reservoir porosity of densification is 7%-10%, permeability 0.05mD-0.1mD, and reservoir pore throat is straight Footpath is more than 500nm;
Particle diameter is the SiO of 10nm-30nm in the nano-fluid2The mass fraction of nano particle is 0.05%- 0.1%, anion surfactant mass fraction is 0.1%-0.5%, and surplus is water;
(2) into fine and close oily oil reservoir, water filling is exploited;
Alternatively, alternately injection water and nano-fluid are exploited into fine and close oily oil reservoir.
, according to the invention it is preferred to, the anion surfactant described in step (1) is petroleum sulfonate or oil carboxylic Hydrochlorate, it is further preferred that petroleum sodium sulfonate or oil carboxylic acid sodium.
The nano-fluid slug the controlling of injecting quantity is 0.03PV-0.05PV, nano-fluid injection rate≤1.4m/d, More preferably 0.8m/d-1.4m/d.
, according to the invention it is preferred to, in step (2), when into fine and close oily oil reservoir, water filling is exploited, the speed of water filling ≤ 1.4m/d, more preferably 0.8m/d-1.4m/d.
When into fine and close oily oil reservoir, alternately injection water and nano-fluid are exploited, the volume ratio of water and nano-fluid >= 20:1 more preferably (20-50):1, water filling and the speed for noting nano-fluid are 0.8m/d-1.4m/d.
The principle of the present invention is as follows:
The present invention before water flood recovery, be initially injected nano-fluid slug, be because nano-fluid can effectively by The close oily reservoir of oily humectation is reversed to that water is wet, and Medium Culture pore throat can be entered with dialysis by being so subsequently implanted into water, and it is remaining to employ Medium Culture Oil.In order to preferably play dialyzing, waterflood injection rate is low, is less than 1.4m/d, can also so avoid injection water edge from splitting Sudden water flooding caused by stitching quick channelling.
The oily oil reservoir of densification that the method for the present invention is applicable in is:Reservoir porosity is 7%-10%, permeability 0.05mD- 0.1mD, reservoir pore throat diameter are more than 500nm.When pore throat in reservoirs is too small, the nano particle in nano-fluid cannot be introduced into pore throat Inside, so that the effect that nano-fluid dialysis improves recovery ratio can not be played, the viscosity of crude in fine and close oil oil reservoir≤ 10mPa.s, oil saturation >=40%.
The present invention unless otherwise specified, by this area routine operation.
The present invention has the following advantages:
1st, the close oily reservoir of oily humectation can be anyway the wet reservoir of water by present invention injection nano-fluid slug, be subsequently implanted into Water dialysis can enter Medium Culture under the action of capillary force, so as to employ Medium Culture remaining oil.
2nd, following injected water of the present invention can supplement the stratum energy after compact oil reservoir primary oil recovery, improve recovery ratio.
Embodiment
Below by specific embodiment, the invention will be further described, but not limited to this.
Raw materials used in embodiment is convenient source, is commercial products.
Embodiment 1
The fine and close oil rock heart is placed in core holding unit, saturated water is first injected, is then injected into saturated oils, it is fine and close to obtain simulation Oil reservoir;Nano-fluid slug is injected into the fine and close oily oil reservoir of simulation and carries out the displacement of reservoir oil, then carries out water drive.
The internal diameter of the fine and close oil rock heart is 2.54cm, length 5cm, permeability 0.08mD.The nanometer stream Particle diameter is the SiO of 10nm-30nm in body2The mass fraction of nano particle is 0.05%, anion surfactant mass fraction For 0.1%, surplus is water, and anion surfactant is petroleum sodium sulfonate, and nano-fluid injection rate is 0.1PV, nano-fluid Injection rate with water is 1.0m/d.
Embodiment 2
The fine and close oil rock heart is placed in core holding unit, saturated water is first injected, is then injected into saturated oils, it is fine and close to obtain simulation Oil reservoir;Nano-fluid slug is injected into the fine and close oil oil reservoir of simulation and carries out the displacement of reservoir oil, then carries out water filling and injection nano-fluid friendship For the displacement of reservoir oil.
The internal diameter of the fine and close oil rock heart is 2.54cm, length 5cm, permeability 0.08mD.The nanometer stream Particle diameter is the SiO of 10nm-30nm in body2The mass fraction of nano particle is 0.05%, anion surfactant mass fraction For 0.1%, surplus is water, and anion surfactant is petroleum sodium sulfonate, and nano-fluid injection rate is 0.2PV, nano-fluid Injection rate with water is 0.8m/d;When water filling and the injection nano-fluid alternating displacement of reservoir oil, the volume ratio of water and nano-fluid is 20:1.
Embodiment 3
The fine and close oil rock heart is placed in core holding unit, saturated water is first injected, is then injected into saturated oils, it is fine and close to obtain simulation Oil reservoir;Nano-fluid slug is injected into the fine and close oily oil reservoir of simulation and carries out the displacement of reservoir oil, then carries out water drive.
The internal diameter of the fine and close oil rock heart is 2.54cm, length 5cm, permeability 0.08mD.The nanometer stream Particle diameter is the SiO of 10nm-30nm in body2The mass fraction of nano particle is 0.05%, anion surfactant mass fraction For 0.1%, surplus is water, and anion surfactant is petroleum sodium sulfonate, and nano-fluid injection rate is 0.3PV, nano-fluid Injection rate with water is 1.2m/d.
Embodiment 4
The fine and close oil rock heart is placed in core holding unit, saturated water is first injected, is then injected into saturated oils, it is fine and close to obtain simulation Oil reservoir;Nano-fluid slug is injected into the fine and close oil oil reservoir of simulation and carries out the displacement of reservoir oil, then carries out water filling and injection nano-fluid friendship For the displacement of reservoir oil.
The internal diameter of the fine and close oil rock heart is 2.54cm, length 5cm, permeability 0.08mD.The nanometer stream Particle diameter is the SiO of 10nm-30nm in body2The mass fraction of nano particle is 0.1%, and anion surfactant mass fraction is 0.2%, surplus is water, and anion surfactant is petroleum sodium sulfonate, and nano-fluid injection rate is 0.1PV, nano-fluid and The injection rate of water is 1.4m/d;When water filling and the injection nano-fluid alternating displacement of reservoir oil, the volume ratio of water and nano-fluid is 50: 1。
Embodiment 5
The fine and close oil rock heart is placed in core holding unit, saturated water is first injected, is then injected into saturated oils, it is fine and close to obtain simulation Oil reservoir;Nano-fluid slug is injected into the fine and close oily oil reservoir of simulation and carries out the displacement of reservoir oil, then carries out water drive.
The internal diameter of the fine and close oil rock heart is 2.54cm, length 5cm, permeability 0.08mD.The nanometer stream Particle diameter is the SiO of 10nm-30nm in body2The mass fraction of nano particle is 0.2%, and anion surfactant mass fraction is 0.4%, surplus is water, and anion surfactant is petroleum sodium sulfonate, and nano-fluid injection rate is 0.1PV, nano-fluid and The injection rate of water is 1.0m/d.
Comparative example 1
The fine and close oil rock heart is placed in core holding unit, saturated water is first injected, is then injected into saturated oils, it is fine and close to obtain simulation Oil reservoir;Water drive is carried out into the fine and close oily oil reservoir of simulation, is not injected into nano-fluid slug.The internal diameter of the fine and close oil rock heart is 2.54cm, length 5cm, permeability 0.08mD, the injection rate of water is 1.0m/d.
Comparative example 2
The fine and close oil rock heart is placed in core holding unit, saturated water is first injected, is then injected into saturated oils, it is fine and close to obtain simulation Oil reservoir;Anionic surfactant solution is injected into the fine and close oily oil reservoir of simulation and carries out the displacement of reservoir oil, then carries out water drive.
The internal diameter of the fine and close oil rock heart is 2.54cm, length 5cm, permeability 0.08mD.The anion Surfactant qualities fraction is 0.1%, and surplus is water, and anion surfactant is petroleum sodium sulfonate, and anionic surface is lived Property agent solution injection rate is 0.1PV, and the injection rate of anionic surfactant solution and water is 1.0m/d.
Experimental example
The obtained recovery ratio of embodiment 1-5 and comparative example 1-2 is listed in Table 1 below, as shown in Table 1:Add nano-fluid ratio Simple waterflood recovery efficiency factor improves more than 9.6%, and more than 5.4% is improved than driving recovery ratio using anion surfactant merely.
1 experiment parameter of table and result

Claims (1)

1. a kind of method of the fine and close oily oil reservoir of nano-fluid exploitation, step are as follows:
(1)Nano-fluid slug is injected into fine and close oily oil reservoir;
The described oily oil reservoir porosity of densification is 7%-10%, permeability 0.05mD-0.1mD, and reservoir pore throat diameter is more than 500nm;
Particle diameter is the SiO of 10nm-30nm in the nano-fluid2The mass fraction of nano particle is 0.05%-0.1%, anion Surfactant qualities fraction is 0.1%-0.5%, and surplus is water;
The nano-fluid slug the controlling of injecting quantity is 0.03PV-0.05PV;
The anion surfactant is petroleum sodium sulfonate or oil carboxylic acid sodium;
The nano-fluid injection rate is 0.8 m/d -1.4m/d;
(2)Into fine and close oily oil reservoir, water filling is exploited;
Alternatively, alternately injection water and nano-fluid are exploited into fine and close oily oil reservoir;
When into fine and close oily oil reservoir, water filling is exploited, the speed of water filling is 0.8 m/d -1.4m/d;
When into fine and close oily oil reservoir, alternately injection water and nano-fluid are exploited, the volume ratio of water and nano-fluid is(20- 50):1.
CN201510014844.6A 2015-01-12 2015-01-12 A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation Active CN104594859B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510014844.6A CN104594859B (en) 2015-01-12 2015-01-12 A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510014844.6A CN104594859B (en) 2015-01-12 2015-01-12 A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation

Publications (2)

Publication Number Publication Date
CN104594859A CN104594859A (en) 2015-05-06
CN104594859B true CN104594859B (en) 2018-04-27

Family

ID=53120868

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510014844.6A Active CN104594859B (en) 2015-01-12 2015-01-12 A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation

Country Status (1)

Country Link
CN (1) CN104594859B (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106010493A (en) * 2016-05-25 2016-10-12 中国石油大学(北京) Composite oil displacement agent as well as preparation method and application thereof
CN106118624B (en) * 2016-06-20 2019-02-12 中国石油大学(华东) A kind of method that nano-fluid inhibits asphaltene deposits injury during low permeability reservoir carbon dioxide flooding
CN106448421B (en) * 2016-07-05 2019-02-19 中国石油大学(北京) Fine and close oil reservoir exploitation simulator and method
CN106566511B (en) * 2016-10-24 2019-03-01 中国石油大学(华东) A kind of surfactant micellar oil displacement agent
JP2021006595A (en) * 2017-09-13 2021-01-21 日産化学株式会社 Crude oil recovery chemical
CN110029989B (en) * 2018-01-11 2021-11-02 中国石油化工股份有限公司 Unconventional oil and gas extraction degree calculation method and system
CN109111905B (en) * 2018-07-17 2021-01-08 中国石油大学(北京) Bio-based nanofluid and application thereof in improving recovery ratio of low-permeability oil reservoir
CN111909678A (en) * 2020-08-25 2020-11-10 大庆中联信实石油科技开发有限公司 Efficient nano oil displacement agent and preparation method thereof
CN114437695B (en) * 2021-12-22 2023-05-12 中国石油天然气集团有限公司 Microemulsion multifunctional nano oil displacement agent and preparation method and application thereof
CN116285926A (en) * 2022-12-02 2023-06-23 西安交通大学 High-calcium and magnesium ion resistant composite nano fluid oil displacement agent and batch preparation method
CN117189049B (en) * 2023-09-28 2024-04-23 大庆油田有限责任公司 Nano profile control and flooding method suitable for low-permeability fractured reservoir

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1696240A (en) * 2005-05-27 2005-11-16 北京交通大学 Chemical oil displacement agent
CN101074601A (en) * 2007-06-26 2007-11-21 上海大学 Method for decreasing rock microporous flow resistance
CN102797443A (en) * 2012-08-27 2012-11-28 北京科技大学 Method for exploiting residual crude oil in low-permeability oilfield by using polymer micro/nanoparticle
CN103362485A (en) * 2013-06-03 2013-10-23 中国石油天然气股份有限公司 Method and well pattern structure for exploiting heavy oil reservoir through gravity assisted nano magnetofluid flooding
CN103897683A (en) * 2014-03-10 2014-07-02 中国石油天然气股份有限公司 Authigenic heat injection composition for underground catalytic oxidation of crude oil

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1696240A (en) * 2005-05-27 2005-11-16 北京交通大学 Chemical oil displacement agent
CN101074601A (en) * 2007-06-26 2007-11-21 上海大学 Method for decreasing rock microporous flow resistance
CN102797443A (en) * 2012-08-27 2012-11-28 北京科技大学 Method for exploiting residual crude oil in low-permeability oilfield by using polymer micro/nanoparticle
CN103362485A (en) * 2013-06-03 2013-10-23 中国石油天然气股份有限公司 Method and well pattern structure for exploiting heavy oil reservoir through gravity assisted nano magnetofluid flooding
CN103897683A (en) * 2014-03-10 2014-07-02 中国石油天然气股份有限公司 Authigenic heat injection composition for underground catalytic oxidation of crude oil

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
纳微米级聚合物调驱技术优选及应用;赵玉武等;《大庆石油学院学报》;20091231;第33卷(第06期);第77-80页 *
表面亲油纳米二氧化硅改变岩石表面润湿性的研究;陈兴隆等;《油田化学》;20051230;第22卷(第04期);第328-331页 *
面活性剂聚合物体系驱油段塞优化研究;赵劲毅;《化工时刊》;20130606;第27卷(第6期);第77-80页 *

Also Published As

Publication number Publication date
CN104594859A (en) 2015-05-06

Similar Documents

Publication Publication Date Title
CN104594859B (en) A kind of method of the fine and close oily oil reservoir of nano-fluid exploitation
CN105626006B (en) Low-permeability oil deposit CO2Drive technical limit well space and determine method
CN102925133B (en) Fracturing fluid for controlling extension of fracture and fracturing method
Samanta et al. Surfactant and surfactant-polymer flooding for enhanced oil recovery
CN108131122B (en) Method for improving CO2 sequestration and crude oil recovery
CN104895537B (en) Oily recovery method is replaced in water filling suitable for fracture-cavity type carbonate gas condensate reservoir
WO1999051854A1 (en) A foam drive method
RU2679027C2 (en) Use of alkali metal silicides in post-chops oilfield recovery operations
CN108868736A (en) Utilize the double L well constructions and method of pressure break exploiting ocean hydrate hiding
CN104929597B (en) A kind of horizontal well chemical flooding recovery method
CN110552671B (en) CO auxiliary by dimethyl ether 2 Method for realizing high-efficiency development of heavy oil reservoir by flooding
CN104870744A (en) Process for producing oil
CA2996151C (en) Supplementing the immiscible water injection cycle with nutrients to improve oil release in oil-containing rock formations
CN109209306A (en) Oil in Super-low Permeability compact oil reservoir horizontal well infuses CO2The asynchronous method for supplementing energy of handling up
CN104265254A (en) Oil production technological method for multi-stage plug injection of oil-soluble viscosity reducer and liquid CO2 in deep super-heavy oil
CN103628846A (en) Method for improving CO2 displacement efficiency of low-permeability reservoir
US9334717B2 (en) Enhanced oil recovery method
CN104895538A (en) A method for increasing the strongly water-sensitive heavy oil reservoir recovery ratio
CN104929598A (en) Method for increasing foam swept volume
CN105134146A (en) Method for oil displacement using carbon dioxide and foam
Li et al. Field application of alkali/surfactant/polymer flood with novel mixtures of anionic/cationic surfactants for high-temperature and high-water-cut mature sandstone reservoir
CN107246257B (en) Heterogeneous reservoir is acidified remodeling method
CN110318719A (en) A kind of two-way displacement method of positive rhythm thick formation
RU2597305C1 (en) Method for development of oil deposit in carbonate reservoirs
Qing et al. Study and application of gelled foam for in-depth water shutoff in a fractured oil reservoir

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant