CN110357794A - A kind of spy's hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation preparation method of supercritical carbon dioxide thickening agent - Google Patents

A kind of spy's hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation preparation method of supercritical carbon dioxide thickening agent Download PDF

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CN110357794A
CN110357794A CN201910761998.XA CN201910761998A CN110357794A CN 110357794 A CN110357794 A CN 110357794A CN 201910761998 A CN201910761998 A CN 201910761998A CN 110357794 A CN110357794 A CN 110357794A
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周明
凃宏俊
彭鹏傲
张劲风
李辰
廖茂
左忠华
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Southwest Petroleum University
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Abstract

The present invention relates to a kind of preparation methods of the hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation supercritical carbon dioxide thickening agent of spy.It can solve the problem of conventional mining method damages oil and gas reservoir.Its technical solution: bottle is put into ice-water bath, and perfluoro octyl ethanol, toluene sulfochloride and pyridine is added, and is reacted 3 hours at 0-20 DEG C, filter paper is added after reaction, ultrasonic wave disperses 1 hour, then removes filter paper, and dilute hydrochloric acid is added and washs 3-5 times to obtain intermediate product (1);Then (N- tert-butoxycarbonyl) Pehanorm and intermediate product (1) are added in another bottle, potassium carbonate and N-N- dimethylformamide is added, is warming up to 60 DEG C of reactions 4 hours to obtain intermediate product (2);It is eventually adding trifluoroacetic acid, methylene chloride and intermediate product (2), 50 DEG C are reacted 2 hours, after extraction vacuum drying, 1,6- di-isocyanate are added at 55 DEG C and reacts 2 hours to obtain final product.The thickening agent can increase carbon dioxide viscosity, can be used for fracturing reform and chemical flooding.

Description

A kind of spy's hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation system of supercritical carbon dioxide thickening agent Preparation Method
Technical field
It without using the anhydrous fracturing fluid of water and is mentioned the present invention relates to a kind of for special hypotonic Oil in Super-low Permeability oil-gas reservoir reservoir exploitation High recovery rate technology, the in particular to preparation method of the supercritical carbon dioxide thickening agent containing fluorine element, belong to oilfield chemistry Product field.
Background technique
The features such as special hypotonic Oil in Super-low Permeability oil-gas reservoir reservoir has physical property poor, low porosity and low permeability, usually also shows very strong water Quick property.Therefore, fracturing reform and later period improve the effective means that recovery ratio is a kind of special hypotonic Oil in Super-low Permeability oil-gas reservoir resource of exploitation. It is easy that reservoir is made to form water lock, the permeability reduction of reservoir using conventional mining method, to be damaged to reservoir, influences To the effect of fracturing yield increasing.In order to solve the injury caused by oil and gas reservoir of conventional mining method, people gradually turn to emphasis Anhydrous pressure break, anhydrous pressure break do not need water substantially in fracturing process.Therefore, the anhydrous fracturing technique without using water is developed With important economy and society effect.A kind of patent of invention ZL201710416147.2 (system of liquid carbon dioxide thickening agent Preparation Method) and ZL201710480823.2 (a kind of preparation method of supercritical carbon dioxide thickening agent) can be in special hypotonic Oil in Super-low Permeability It is used in oil-gas reservoir as fracturing fluid base fluid and raising recovery ratio chemical oil displacement agent, but prepared carbon dioxide densif.es agent is all deposited In ester group, can only be used under the conditions of lower temperature and few water.In the active oil-gas reservoir effect of higher temperature and edge-bottom water, two Kind thickening agent thermal stability is deteriorated, and easily hydrolyzes, and causes thickening capabilities to be gradually reduced and even disappears.Based on this, system of the present invention For a kind of six chain thickening agents of ether-containing key, supercritical carbon dioxide viscosity can be improved and improve the stability of thickening agent.
Summary of the invention
The purpose of the present invention is: the case where easily causing injury to oil and gas reservoir for conventional mining method provides one kind The special hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation preparation method of supercritical carbon dioxide thickening agent.
The present invention provides a kind of preparation method of hypotonic Oil in Super-low Permeability oil-gas reservoir supercritical carbon dioxide thickening agent of suitable spy, institute State preparation method the following steps are included:
(1) perfluoro octyl ethanol and tolysulfonyl the preparation to toluene perfluoro octyl sulfonic acid ester: are added into three-necked bottle The molar ratio 1:1.1-1.2 of chlorine, perfluoro octyl ethanol and paratoluensulfonyl chloride, is eventually adding pyrido and is sufficiently stirred.Keep temperature Degree is sufficiently stirred at 0-20 DEG C, reacts 3 hours, and filter paper is added after reaction, and ultrasonic wave disperses 1 hour, removes unreacted Paratoluensulfonyl chloride, then removes filter paper, then is repeatedly washed with 15% dilute hydrochloric acid and removed pyridine, obtains white solid, finally It is repeatedly washed with distilled water, 40 DEG C are dried in vacuo 3 hours, and intermediate product (1) is made to toluene perfluoro octyl sulfonic acid ester, such as I formula It is shown;
(I) toluene perfluoro octyl sulfonic acid ester
(2) preparation of (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane
The preparation of (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane: add into three-necked bottle Enter (N- tert-butoxycarbonyl) Pehanorm and to toluene perfluoro octyl sulfonic acid ester, (N- tert-butoxycarbonyl) trihydroxy methyl Methylamine and to the ratio between toluene perfluoro octyl sulfonic acid ester be 3.1-3.2:1, add potassium carbonate and n,N-Dimethylformamide, sufficiently Stirring, be warming up to 60 DEG C of reaction 4h and repeatedly washed with distilled water after reaction, be dried in vacuo intermediate product (2) i.e. (1, 2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamates) methane, structure is as shown in II formula.
(II) (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane (3) final product [1, 6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane preparation: to three-necked bottle be added methylene chloride and three The mixed solution of fluoroacetic acid, methylene chloride and trifluoroacetic acid volume ratio are 2:1;By 1,2,3- perfluoro capryl ethoxymeyhylene- 4- t-butyl carbamate) methane is add to the above mixed solution, and 50 DEG C of constant temperature are reacted 2 hours, and dichloromethane is added thereto Alkane extracts 3 times, obtains organic layer, anhydrous Na2SO4Dry organic layer, is added the different dicyanate of 1-6,1, hexamethylene-diisocyanate with The molar ratio of (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane is 1:2.05-2.10, at 55 DEG C Under the conditions of react 2 hours, repeatedly wash crude product with the mixed solvent of ethyl acetate and benzene, filter, vacuum drying, finally obtain Final product [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane, structure is as shown in formula III.
(III) [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane
The advantages and beneficial effects of the present invention are: introducing fluorine-containing groups into thickening agent, thickening agent can be effectively reduced Required pressure is dissolved in carbon dioxide, improves dissolution situation of the thickening agent in carbon dioxide.Meanwhile thickening agent is intermolecular Entanglement effect between existing hydrogen bond action and strand can effectively play the role of increasing carbon dioxide viscosity. Thickening agent is by ehter bond rather than ester bond connects close carbon dioxide group and hydrogen bond crosslinks associative groups, effectively increases thickening agent Thermal stability and hydrolytic stability can be applied to the hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation of the active spy of edge-bottom water.
The test method of thickening agent viscosity: the high temperature that thickening agent is first added to rheometer HAAKE MARS according to dosage is high The closed system of pressure installs the corollary apparatus of high temperature high pressure enclosed system, is excluded air in closed system using vacuum pump. Then, supercritical carbon dioxide is imported by the sampling valve of high temperature high pressure enclosed system, meanwhile, internal rotor turns in adjustment system It is dynamic, be sufficiently mixed thickening agent carbon dioxide uniformly, when carbon dioxide is passed into metering, regulating system pressure, temperature, make be Carbon dioxide in system reaches required state, is uniformly mixed, that is, completes the preparation of mixed system, finally, opening rheology Instrument can test the viscosity of mixed system after setting experiment parameter.
Specific embodiment
Illustrate the present invention below by example, but the contents of the present invention are not limited solely to the following examples.
Embodiment 1
(1) perfluoro octyl ethanol and tolysulfonyl the preparation to toluene perfluoro octyl sulfonic acid ester: are added into three-necked bottle The molar ratio 1:1.1 of chlorine, perfluoro octyl ethanol and paratoluensulfonyl chloride, is eventually adding pyrido and is sufficiently stirred.Maintain the temperature at 0 DEG C, it is sufficiently stirred, reacts 3 hours, filter paper is added after reaction, ultrasonic wave disperses 1 hour, removes unreacted to toluene sulphur Then acyl chlorides removes filter paper, then washs 3 times with 15% dilute hydrochloric acid and remove pyridine, obtain white solid, finally with distillation washing It washs 5 times, 40 DEG C are dried in vacuo 3 hours, and intermediate product (1) is made to toluene perfluoro octyl sulfonic acid ester.
(2) preparation of (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane: into three-necked bottle (N- tert-butoxycarbonyl) serinol is added and to toluene perfluoro octyl sulfonic acid ester, (N- tert-butoxycarbonyl) serinol and to first The ratio between benzene perfluoro octyl sulfonic acid ester is 3.2:1, adds potassium carbonate and N, N- dimethylformamide is sufficiently stirred, is warming up to 60 DEG C reaction 4h be washed with distilled water 5 times after reaction, be dried in vacuo to obtain intermediate product (2)-(1,3- perfluoro octyl ethanol third Ether -2- t-butyl carbamate) propane.
(3) preparation of final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane: to The mixed solution of methylene chloride and trifluoroacetic acid is added in three-necked bottle, and methylene chloride and trifluoroacetic acid volume ratio are 2:1;Will (1,2, 3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane is add to the above mixed solution, 50 DEG C of constant temperature reactions 2 hours, methylene chloride is added thereto and extracts 3 times, obtains organic layer, anhydrous Na2SO4Dry organic layer, is added 1,6 different dicyan Acid esters, 1, hexamethylene-diisocyanate and 1,3- perfluoro octyl ethanol propyl ether -2- t-butyl carbamate) molar ratio of propane is 1: 2.05, it reacts 2 hours under the conditions of 55 DEG C, is washed crude product 4 times with the mixed solvent of ethyl acetate and benzene, filtered, vacuum is dry It is dry, finally obtain final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane.
It takes above-mentioned 1wt%, 2wt%, 3wt% supercritical carbon dioxide thickening agent to be added to respectively and installs corollary apparatus In high temperature high pressure enclosed system;99wt%, 98wt%, 97wt% overcritical two is directed respectively into closed system by sampling valve Carbonoxide.Rotor is rotated, regulating system pressure and temperature value, being sufficiently stirred is completely dissolved thickening agent, i.e. completion mixed system Preparation;It is then turned on rheometer, setup pressure value 29MPa, temperature is 60 DEG C, and it is 100s that shear rate is kept in experiment-1, survey The viscosity number for determining mixed system is respectively 5.89mPas, 6.24mPas and 7.89mPas;Be respectively do not thicken it is overcritical 147.3 times, 156.0 times and 197.3 times of carbon dioxide viscosity.
Embodiment 2
(1) perfluoro octyl ethanol and tolysulfonyl the preparation to toluene perfluoro octyl sulfonic acid ester: are added into three-necked bottle The molar ratio 1:1.2 of chlorine, perfluoro octyl ethanol and paratoluensulfonyl chloride, is eventually adding pyrido and is sufficiently stirred.It maintains the temperature at It 20 DEG C, is sufficiently stirred, reacts 3 hours, filter paper is added after reaction, ultrasonic wave disperses 1 hour, removes unreacted to toluene Then sulfonic acid chloride removes filter paper, then washs 4 times with 15% dilute hydrochloric acid and remove pyridine, obtain white solid, finally use distilled water Washing 4 times, 40 DEG C are dried in vacuo 3 hours, and intermediate product (1) is made to toluene perfluoro octyl sulfonic acid ester.
(2) preparation of (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane: into three-necked bottle (N- tert-butoxycarbonyl) serinol is added and to toluene perfluoro octyl sulfonic acid ester, (N- tert-butoxycarbonyl) serinol and to first The ratio between benzene perfluoro octyl sulfonic acid ester is 3.1:1, adds potassium carbonate and N, N- dimethylformamide is sufficiently stirred, is warming up to 60 DEG C reaction 4h be washed with distilled water 4 times after reaction, be dried in vacuo to obtain intermediate product (2) i.e. (1,2,3- perfluoro capryl second Oxygroup methylene -4- t-butyl carbamate) methane.
(3) preparation of final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane: to The mixed solution of methylene chloride and trifluoroacetic acid is added in three-necked bottle, and methylene chloride and trifluoroacetic acid volume ratio are 2:1;Will (1,2, 3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane is add to the above mixed solution, 50 DEG C of constant temperature reactions 2 hours, methylene chloride is added thereto and extracts 3 times, obtains organic layer, anhydrous Na2SO4Dry organic layer, is added 1,6 different dicyan Acid esters, 1, hexamethylene-diisocyanate and 1,3- perfluoro octyl ethanol propyl ether -2- t-butyl carbamate) molar ratio of propane is 1: 2.1, it reacts 2 hours under the conditions of 55 DEG C, is washed crude product 4 times with the mixed solvent of ethyl acetate and benzene, filtered, vacuum is dry It is dry, finally obtain final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane.
It takes above-mentioned 1wt%, 2wt%, 3wt% supercritical carbon dioxide thickening agent to be added to respectively and installs corollary apparatus In high temperature high pressure enclosed system;99wt%, 98wt%, 97wt% overcritical two is directed respectively into closed system by sampling valve Carbonoxide.Rotor is rotated, regulating system pressure and temperature value, being sufficiently stirred is completely dissolved thickening agent, i.e. completion mixed system Preparation;It is then turned on rheometer, setup pressure value 29MPa, temperature is 60 DEG C, it is 100s that shear rate is kept in experiment-1, The viscosity number for measuring mixed system is respectively 5.85mPas, 6.76mPas and 7.82mPas;It is not thicken super face respectively 146.3 times, 169.0 times and 195.5 times of boundary's carbon dioxide viscosity.
Embodiment 3
(1) perfluoro octyl ethanol and tolysulfonyl the preparation to toluene perfluoro octyl sulfonic acid ester: are added into three-necked bottle The molar ratio 1:1.15 of chlorine, perfluoro octyl ethanol and paratoluensulfonyl chloride, is eventually adding pyrido and is sufficiently stirred.It maintains the temperature at It 10 DEG C, is sufficiently stirred, reacts 3 hours, filter paper is added after reaction, ultrasonic wave disperses 1 hour, removes unreacted to toluene Then sulfonic acid chloride removes filter paper, then washs 5 times with 15% dilute hydrochloric acid and remove pyridine, obtain white solid, finally use distilled water Washing 5 times, 40 DEG C are dried in vacuo 3 hours, and intermediate product (1) is made to toluene perfluoro octyl sulfonic acid ester
(2) preparation of (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane: into three-necked bottle (N- tert-butoxycarbonyl) serinol is added and to toluene perfluoro octyl sulfonic acid ester, (N- tert-butoxycarbonyl) serinol and to first The ratio between benzene perfluoro octyl sulfonic acid ester is 3.15:1, adds potassium carbonate and N, N- dimethylformamide is sufficiently stirred, is warming up to 60 DEG C reaction 4h be washed with distilled water 4 times after reaction, be dried in vacuo to obtain intermediate product (2) i.e. (1,2,3- perfluoro capryl second Oxygroup methylene -4- t-butyl carbamate) methane.
(3) preparation of final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane: to The mixed solution of methylene chloride and trifluoroacetic acid is added in three-necked bottle, and methylene chloride and trifluoroacetic acid volume ratio are 2:1;Will (1,2, 3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane is add to the above mixed solution, 50 DEG C of constant temperature reactions 2 hours, methylene chloride is added thereto and extracts 3 times, obtains organic layer, anhydrous Na2SO4Dry organic layer, is added 1,6 different dicyan Acid esters, 1, hexamethylene-diisocyanate and 1,3- perfluoro octyl ethanol propyl ether -2- t-butyl carbamate) molar ratio of propane is 1: 2.1, it reacts 2 hours under the conditions of 55 DEG C, is washed crude product 5 times with the mixed solvent of ethyl acetate and benzene, filtered, vacuum is dry It is dry, finally obtain final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane.
It takes above-mentioned 1wt%, 2wt%, 3wt% supercritical carbon dioxide thickening agent to be added to respectively and installs corollary apparatus In high temperature high pressure enclosed system;99wt%, 98wt%, 97wt% overcritical two is directed respectively into closed system by sampling valve Carbonoxide.Rotor is rotated, regulating system pressure and temperature value, being sufficiently stirred is completely dissolved thickening agent, i.e. completion mixed system Preparation;It is then turned on rheometer, setup pressure value 29MPa, temperature is 60 DEG C, it is 100s that shear rate is kept in experiment-1, The viscosity number for measuring mixed system is respectively 6.43mPas, 6.97mPas and 7.45mPas;It is not thicken super face respectively 160.8 times, 174.3 times and 186.3 times of boundary's carbon dioxide viscosity.

Claims (2)

1. the preparation method that supercritical carbon dioxide thickening agent is used in a kind of hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation of spy, it is characterised in that should Preparation method the following steps are included:
(1) preparation to toluene perfluoro octyl sulfonic acid ester: perfluoro octyl ethanol and paratoluensulfonyl chloride are added into three-necked bottle, entirely The molar ratio 1:1.1-1.2 of fluorine octyl ethyl alcohol and paratoluensulfonyl chloride, is eventually adding pyrido and is sufficiently stirred;Maintain the temperature at 0- It 20 DEG C, is sufficiently stirred, reacts 3 hours, filter paper is added after reaction, ultrasonic wave disperses 1 hour, removes unreacted to toluene Sulfonic acid chloride, then removes filter paper, then is repeatedly washed with 15% dilute hydrochloric acid and removed pyridine, white solid is obtained, finally with distillation Water repeatedly washs, and 40 DEG C are dried in vacuo 3 hours, and intermediate product (1) is made to toluene perfluoro octyl sulfonic acid ester;
(2) it the preparation of (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane: is added into three-necked bottle (N- tert-butoxycarbonyl) Pehanorm and to toluene perfluoro octyl sulfonic acid ester, (N- tert-butoxycarbonyl) trihydroxy methyl first Amine and to toluene perfluoro octyl sulfonic acid ester molar ratio be 3.1-3.2:1, add potassium carbonate and n,N-Dimethylformamide, sufficiently Stirring, be warming up to 60 DEG C of reaction 4h and repeatedly washed with distilled water after reaction, be dried in vacuo intermediate product (2) i.e. (1, 2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamates) methane;
(3) preparation of final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } hexane: to three necks The mixed solution of methylene chloride and trifluoroacetic acid is added in bottle, and methylene chloride and trifluoroacetic acid volume ratio are 2:1;By (1,2,3- is complete Fluorine octyl ethoxymeyhylene -4- t-butyl carbamate) methane is add to the above mixed solution, and 50 DEG C of constant temperature reactions 2 are small When, methylene chloride is added thereto and extracts 3 times, obtains organic layer, uses anhydrous Na2SO4Dry organic layer, is added different two cyanic acid of 1-6 Ester, 1, mole of hexamethylene-diisocyanate and (1,2,3- perfluoro capryl ethoxymeyhylene -4- t-butyl carbamate) methane Than being reacted 2 hours under the conditions of 55 DEG C, repeatedly washing crude product with the mixed solvent of ethyl acetate and benzene for 1:2.05-2.10, Filtering, vacuum drying, finally obtain final product { [1,6- bis- [(1,2,3- perfluoro capryl ethoxymeyhylene) methylurea base] } oneself Alkane.
2. the hypotonic Oil in Super-low Permeability oil-gas reservoir exploitation of spy described in claim 1 application of supercritical carbon dioxide thickener, special Sign is: taking above-mentioned 1wt%, 2wt%, 3wt% supercritical carbon dioxide thickener to be added to respectively and installs corollary apparatus In high temperature high pressure enclosed system;99wt%, 98wt%, 97wt% overcritical two is directed respectively into closed system by sampling valve Carbonoxide;Rotor is rotated, regulating system pressure and temperature value, being sufficiently stirred is completely dissolved thickening agent, i.e. completion mixed system Preparation;Rheometer, setup pressure value 29MPa are opened, temperature is 60 DEG C, measures the viscosity number of mixed system and does not thicken The viscosity of supercritical carbon dioxide is compared, and increases by 146~197 times.
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* Cited by examiner, † Cited by third party
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CN113773438A (en) * 2021-11-08 2021-12-10 德仕能源科技集团股份有限公司 Carbon dioxide thickener for medium-high permeability oil reservoir and preparation method and technology thereof
CN116874789A (en) * 2023-08-03 2023-10-13 西南石油大学 Supercritical carbon dioxide thickener with branched structure and preparation method thereof
CN117307120A (en) * 2023-10-18 2023-12-29 成都赛璐石油科技有限公司 Supercritical CO 2 Thickening fracturing-gas flooding-foam profile control and flooding yield increasing method

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000035998A2 (en) * 1998-12-15 2000-06-22 Yale University Association of compounds in carbon dioxide and the gels and/or foams formed therefrom
US20090047498A1 (en) * 2007-08-13 2009-02-19 E. I. Dupont De Nemours And Company Method for providing nanoweb composite material
CN102703050A (en) * 2012-05-28 2012-10-03 西南石油大学 Tetra-polysulfonate type surfactant and preparation method thereof
CN104388073A (en) * 2014-11-27 2015-03-04 中国石油化工股份有限公司 Supercritical carbon dioxide solid thickening agent as well as preparation method and application thereof
US20150159033A1 (en) * 2013-12-06 2015-06-11 Xerox Corporation Bis-ureas as amorphous materials for phase-change ink
CN105294948A (en) * 2015-12-03 2016-02-03 陕西延长石油(集团)有限责任公司研究院 Fluorinated polyurethane thickener applied to supercritical CO2 tackification and preparation method thereof
CN107043620A (en) * 2017-06-06 2017-08-15 西南石油大学 A kind of preparation method of liquid carbon dioxide thickening agent
CN107253922A (en) * 2017-06-22 2017-10-17 西南石油大学 A kind of preparation method of supercritical carbon dioxide thickener

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000035998A2 (en) * 1998-12-15 2000-06-22 Yale University Association of compounds in carbon dioxide and the gels and/or foams formed therefrom
US20090047498A1 (en) * 2007-08-13 2009-02-19 E. I. Dupont De Nemours And Company Method for providing nanoweb composite material
CN102703050A (en) * 2012-05-28 2012-10-03 西南石油大学 Tetra-polysulfonate type surfactant and preparation method thereof
US20150159033A1 (en) * 2013-12-06 2015-06-11 Xerox Corporation Bis-ureas as amorphous materials for phase-change ink
CN104388073A (en) * 2014-11-27 2015-03-04 中国石油化工股份有限公司 Supercritical carbon dioxide solid thickening agent as well as preparation method and application thereof
CN105294948A (en) * 2015-12-03 2016-02-03 陕西延长石油(集团)有限责任公司研究院 Fluorinated polyurethane thickener applied to supercritical CO2 tackification and preparation method thereof
CN107043620A (en) * 2017-06-06 2017-08-15 西南石油大学 A kind of preparation method of liquid carbon dioxide thickening agent
CN107253922A (en) * 2017-06-22 2017-10-17 西南石油大学 A kind of preparation method of supercritical carbon dioxide thickener

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
PEDRO CINTAS ET AL: "A Family of Hydrogels Based on Ureido-Linked Aminopolyol-Derived Amphiphiles and Bolaamphiphiles: Synthesis, Gelation under Thermal and Sonochemical Stimuli, and Mesomorphic Characterization", 《CHEMISTRY A EUROPEAN JOURNAL》 *
SARAH J ATKINSON ET AL: "Synthesis and characterisation of peripherally functionalised dendritic molecules", 《NEW JOURNAL OF CHEMISTRY》 *
ZHIHUA HUANG ET AL: "Generation of Microcellular Materials via Self-Assembly in Carbon Dioxide", 《CHEM. MATER》 *
刘巍等: "超临界CO2增稠剂研究进展", 《断块油气田》 *
黄洲等: "液体CO2增稠剂的研究现状", 《现代化工》 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113773438A (en) * 2021-11-08 2021-12-10 德仕能源科技集团股份有限公司 Carbon dioxide thickener for medium-high permeability oil reservoir and preparation method and technology thereof
CN116874789A (en) * 2023-08-03 2023-10-13 西南石油大学 Supercritical carbon dioxide thickener with branched structure and preparation method thereof
CN116874789B (en) * 2023-08-03 2023-11-24 西南石油大学 Supercritical carbon dioxide thickener with branched structure and preparation method thereof
CN117307120A (en) * 2023-10-18 2023-12-29 成都赛璐石油科技有限公司 Supercritical CO 2 Thickening fracturing-gas flooding-foam profile control and flooding yield increasing method

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