CN105647506B - Oil-gas field fracturing clay stabilizer and preparation method thereof - Google Patents

Oil-gas field fracturing clay stabilizer and preparation method thereof Download PDF

Info

Publication number
CN105647506B
CN105647506B CN201610041585.0A CN201610041585A CN105647506B CN 105647506 B CN105647506 B CN 105647506B CN 201610041585 A CN201610041585 A CN 201610041585A CN 105647506 B CN105647506 B CN 105647506B
Authority
CN
China
Prior art keywords
clay stabilizer
preparation
oil
integer
takes
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
CN201610041585.0A
Other languages
Chinese (zh)
Other versions
CN105647506A (en
Inventor
罗懿
李国锋
姚昌宇
胡艾国
王迁伟
赵楠
黄启亮
邱小庆
王娟娟
徐成法
王璇
王瑞霞
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 Petroleum and Chemical Corp
Petroleum Engineering Technology Research Institute of Sinopec North China oil and Gas Co
Original Assignee
China Petroleum and Chemical Corp
Petroleum Engineering Technology Research Institute of Sinopec North China oil and Gas Co
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 Petroleum and Chemical Corp, Petroleum Engineering Technology Research Institute of Sinopec North China oil and Gas Co filed Critical China Petroleum and Chemical Corp
Priority to CN201610041585.0A priority Critical patent/CN105647506B/en
Publication of CN105647506A publication Critical patent/CN105647506A/en
Application granted granted Critical
Publication of CN105647506B publication Critical patent/CN105647506B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/62Compositions for forming crevices or fractures
    • C09K8/66Compositions based on water or polar solvents
    • C09K8/68Compositions based on water or polar solvents containing organic compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2618Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing nitrogen
    • C08G65/2621Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing nitrogen containing amine groups
    • C08G65/2624Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing nitrogen containing amine groups containing aliphatic amine groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/329Polymers modified by chemical after-treatment with organic compounds
    • C08G65/331Polymers modified by chemical after-treatment with organic compounds containing oxygen
    • C08G65/332Polymers modified by chemical after-treatment with organic compounds containing oxygen containing carboxyl groups, or halides, or esters thereof
    • C08G65/3322Polymers modified by chemical after-treatment with organic compounds containing oxygen containing carboxyl groups, or halides, or esters thereof acyclic
    • 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
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/607Compositions for stimulating production by acting on the underground formation specially adapted for clay formations
    • C09K8/608Polymer compositions
    • 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
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/84Compositions based on water or polar solvents
    • C09K8/86Compositions based on water or polar solvents containing organic compounds
    • C09K8/88Compositions based on water or polar solvents containing organic compounds macromolecular compounds
    • C09K8/885Compositions based on water or polar solvents containing organic compounds macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2650/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G2650/28Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type
    • C08G2650/50Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing nitrogen, e.g. polyetheramines or Jeffamines(r)
    • 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
    • C09K2208/12Swell inhibition, i.e. using additives to drilling or well treatment fluids for inhibiting clay or shale swelling or disintegrating

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Dispersion Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Polyethers (AREA)

Abstract

The invention discloses a kind of oil-gas field fracturing clay stabilizers and preparation method thereof, belong to exploitation of oil-gas field technical field.The clay stabilizer is using polyethylene polyamine as initiator, after ethylene oxide and/or propylene oxide open loop addition, the positive ionization for carrying out amine again is made, it can effectively prevent clay, mud shale expansion, with various water soluble polymer thickeners, there is especially artificial synthesized polyacrylamide polymer drag reducing agent good compatibility to be suitble to use in the extensive volume fracturing drag reduction water fracturing fluid of oil gas field suitable for hyposmosis densification oil shale and the fracturing reform of sensitive reservoir.The general structure of clay stabilizer is as follows:

Description

Oil-gas field fracturing clay stabilizer and preparation method thereof
Technical field
The present invention relates to a kind of oil-gas field fracturing clay stabilizers, also relate to the preparation side of the clay stabilizer Method belongs to exploitation of oil-gas field technical field.
Background technique
Oil gas field reservoir contains a certain amount of clay mineral, and (such as kaolin, montmorillonite, illite, chlorite, she deceives people Layer etc.), when carrying out water-based fracturing transformation to reservoir, clay can expand, migrate, easily blocking stratum duct and pore structure larynx Portion reduces in-place permeability, so as to cause the oil well underproduction.
For the hydration swelling for reducing clay mineral, expansion-resisting agent must be added in fracturing fluid to stablize clay.Currently, domestic oil Field is directed to hyposmosis, water-sensitive oil-gas Layer frequently with Cationic Polymers Containing Quaternary Ammonium Salts, such as polyepichlorohydrin-dimethylamine, poly- three Methacrylic chlorination ammonium, polydimethyl diallyl ammonium chloride and acrylamide, dimethyl diallyl ammonium chloride, propylene The copolymer etc. of acyloxyethyl trimethyl ammonium chloride.But Cationic Polymers Containing Quaternary Ammonium Salts contain a large amount of cationic species, After contacting with anionic additive, since there are electrostatic adsorptions between zwitterion, the compatibility of fracturing fluid is easily reduced And preventive effect of expansion, serious or even appearance muddiness, flocculation and delamination phenomenon greatly limit its application.
The patent of invention of publication No. CN102433110A discloses a kind of amine shale stabilizer for drilling fluid, by polyethers Diamines reacts generation according to molar ratio 10:1~1:20 with epoxyalkane, and structural formula is as follows:
In formula 1: R, R ' be respectively carbon atom number 2~4 alkylidene, m, n take any integer in 0~10 respectively.Preferably, Polyether diamine be polyethyleneoxide diamine, polypropyleneoxide diamine or polyoxyethylenepropylene diamines, molecular weight less than 1000, R be hydrogen or Methyl, 1≤x+y+z≤20.The stabilizer can effectively inhibit hydration and expansion of clay and aquation to disperse, but its compatibility is poor, prevent It still needs further improvement for swollen performance.
Summary of the invention
The object of the present invention is to provide a kind of oil-gas field fracturing clay stabilizer, prevent it is swollen have excellent performance, compatibility is good It is good.
Meanwhile the present invention also provides a kind of preparation methods of above-mentioned clay stabilizer.
In order to achieve the goal above, the technical scheme adopted by the invention is that:
Oil-gas field fracturing clay stabilizer, general structure are as follows:
In formula 2: A is polyoxyethylene groups (EO), and B is polyoxypropylene base (PO), and x, y take any integer in 0~10, z respectively Take any integer in 2~10;R is the hydroxyalkyl or-CH of hydrogen, the alkyl of 1~5 carbon, 1~5 carbon2-COONa;N takes 0~5 Middle any integer.
Preferably, in formula 2, x takes any integer in 0~6, and y takes any integer in 0~4, and z takes any integer in 2~5, R For hydrogen, methyl or-CH2-COONa。
It is further preferred that it is hydrogen or methyl that x, which takes 0, y that 0 or 3, z is taken to take 4 or 5, R, in formula 2.
More preferably, in formula 2, it is methyl that x, which takes 0, y that 0 or 3, z is taken to take 5, R,.
Optimal, in formula 2, it is methyl that x, which takes 0, y that 3, z is taken to take 5, R,.
The preparation method of oil-gas field fracturing clay stabilizer, be using polyethylene polyamine as initiator, with ethylene oxide and/ Or after propylene oxide open loop addition, then carry out the positive ionization of amine.
The general structure of the polyethylene polyamine is as follows:
In formula 3: n takes any integer in 0~5.
The molar ratio of the polyethylene polyamine and ethylene oxide and/or propylene oxide is 1:(n+4) × (x+y+z).
The concrete operations of the cationoid reaction are as follows: solvent and cationization examination are added in open loop addition products therefrom 0.5~15h is reacted in agent at 25~100 DEG C of temperature.Wherein, cationic reagent can be selected formic acid, acetic acid, phosphoric acid, Citric acid, the alkyl halide (such as chloromethanes, chloroethanes) of 1~5 carbon, the halohydrin (such as chlorethanol) of 1~5 carbon or 2~5 The halogenated carboxylic acid salt (such as sodium chloroacetate) of carbon.Solvent can be selected the aqueous solution of ethyl alcohol, isopropanol or ethylene glycol, alcoholic solution it is dense Degree is 20%~80%;The additional amount of solvent be opening product (polyethylene polyamine polyethers) quality 20%~ 70%, namely it is made into the polyethylene polyamine polyether solutions of concentration 58.8%~80%.On the one hand solvent, which is added, can make to be cationized Reaction is gone on smoothly, and on the other hand can control the freezing point of final products, meets low temperature requirement.Gained clay stabilizer PH value is 7~9.
Beneficial effects of the present invention:
In the present invention oil-gas field fracturing with clay stabilizer be using polyethylene polyamine as initiator, with ethylene oxide and/or After propylene oxide open loop addition, then carry out amine positive ionization be made, which can effectively prevent clay, mud page Rock expansion, with various water soluble polymer thickeners, especially artificial synthesized polyacrylamide polymer drag reducing agent has good Good compatibility is suitble to extensive in oil gas field suitable for hyposmosis densification oil shale and the fracturing reform of sensitive reservoir It is used in volume fracturing drag reduction water fracturing fluid.
Specific embodiment
Only invention is further described in detail for following embodiments, but does not constitute any limitation of the invention.
Embodiment 1
The structural formula of oil-gas field fracturing clay stabilizer is as follows in the present embodiment:
Its preparation step includes:
1) triethylene tetramine 146g (1mol) and catalyst potassium hydroxide 1.5g are added in autoclave, are warming up to At 100 ± 5 DEG C, gauge pressure is pumped it to vacuum pump and is stirred and is risen with nitrogen sparge tube road and reaction kettle 2 times for -0.08MPa Temperature is slowly added to ethylene oxide 1584g (36mol) when temperature rises to 130 ± 5 DEG C, controls 140 ± 5 DEG C of reaction temperature, into Speed is expected to maintain 0.25 ± 0.05MPa of gauge pressure, and end of reaction is cooled to room temperature, and obtains faint yellow liquid product;
2) above-mentioned product 173g is weighed, dehydrated alcohol 50g and water 200g is added, acetic acid 20g is added dropwise to get transparent clay Stabilizer.
Embodiment 2
The structural formula of oil-gas field fracturing clay stabilizer is as follows in the present embodiment:
Its preparation step includes:
1) tetraethylenepentamine 189g (1mol) and catalyst potassium hydroxide 2.0g are added in autoclave, are warming up to At 100 ± 5 DEG C, gauge pressure is pumped it to vacuum pump and is stirred and is risen with nitrogen sparge tube road and reaction kettle 2 times for -0.08MPa Temperature is slowly added to ethylene oxide 1232g (28mol) when temperature rises to 130 ± 5 DEG C, controls 140 ± 5 DEG C of reaction temperature, into Speed is expected to maintain 0.25 ± 0.05MPa of gauge pressure, and end of reaction is cooled to room temperature, and obtains faint yellow liquid product;
2) above-mentioned product 142g is weighed, dehydrated alcohol 50g and water 200g is added, sodium chloroacetate 55g is added dropwise, is warming up to 80 DEG C Back flow reaction 8h, cooling obtain transparent clay stabilizer.
Embodiment 3
The structural formula of oil-gas field fracturing clay stabilizer is as follows in the present embodiment:
Its preparation step includes:
1) by polyethylene polyamine 253.5g (pentaethylene hexamine, each 0.5mol of six ethylene, seven amine) and catalyst potassium hydroxide 2.5g is added in autoclave, and when being warming up to 100 ± 5 DEG C, pumping it to gauge pressure with vacuum pump is -0.08MPa, uses nitrogen Scavenging pipeline and reaction kettle 2 times, stir and heat up, when temperature rises to 130 ± 5 DEG C, be slowly added to ethylene oxide 1870g (42.5mol) controls 140 ± 5 DEG C of reaction temperature, and for charging rate to maintain 0.25 ± 0.05MPa of gauge pressure, end of reaction is cooling To room temperature, faint yellow liquid product is obtained;
2) above-mentioned product 142g is weighed, dehydrated alcohol 50g and water 200g is added, chloromethanes 52.8g is added dropwise, is warming up to 60 DEG C Back flow reaction 3h, cooling obtain transparent clay stabilizer.
Embodiment 4
The structural formula of oil-gas field fracturing clay stabilizer is as follows in the present embodiment:
Its preparation step includes:
1) by polyethylene polyamine 253.5g (pentaethylene hexamine, each 0.5mol of six ethylene, seven amine) and catalyst potassium hydroxide 2.5g is added in autoclave, and when being warming up to 100 ± 5 DEG C, pumping it to gauge pressure with vacuum pump is -0.08MPa, uses nitrogen Scavenging pipeline and reaction kettle 2 times, stir and heat up, when temperature rises to 130 ± 5 DEG C, be slowly added to propylene oxide 1479g (25.5mol) controls 140 ± 5 DEG C of reaction temperature, and charging rate is to maintain 0.25 ± 0.05MPa of gauge pressure, end of reaction, then delays It is slow that ethylene oxide 1496g (34mol) is added, 140 ± 5 DEG C of reaction temperature are controlled, end of reaction is cooled to room temperature, and is obtained yellowish Color liquid product;
2) above-mentioned product 323g is weighed, dehydrated alcohol 100g and water 300g is added, formic acid 28g is added dropwise and is glued to get transparent Soil stabilizer.
Embodiment 5
The structural formula of oil-gas field fracturing clay stabilizer is as follows in the present embodiment:
Its preparation step includes:
1) by polyethylene polyamine 253.5g (pentaethylene hexamine, each 0.5mol of six ethylene, seven amine) and catalyst potassium hydroxide 2.5g is added in autoclave, and when being warming up to 100 ± 5 DEG C, pumping it to gauge pressure with vacuum pump is -0.08MPa, uses nitrogen Scavenging pipeline and reaction kettle 2 times, stir and heat up, when temperature rises to 130 ± 5 DEG C, be slowly added to propylene oxide 1479g (25.5mol) controls 140 ± 5 DEG C of reaction temperature, and charging rate is to maintain 0.25 ± 0.05MPa of gauge pressure, end of reaction, then delays It is slow that ethylene oxide 1870g (42.5mol) is added, 140 ± 5 DEG C of reaction temperature are controlled, end of reaction is cooled to room temperature, and is obtained light Yellow liquid product;
2) above-mentioned product 362g is weighed, dehydrated alcohol 100g and water 300g is added, chloromethanes 52.8g is added dropwise, is warming up to 60 DEG C back flow reaction 3h, cooling obtain transparent clay stabilizer.
Embodiment 6
The structural formula of oil-gas field fracturing clay stabilizer is as follows in the present embodiment:
Its preparation step includes:
1) by polyethylene polyamine 253.5g (pentaethylene hexamine, each 0.5mol of six ethylene, seven amine) and catalyst potassium hydroxide 2.5g is added in autoclave, and when being warming up to 100 ± 5 DEG C, pumping it to gauge pressure with vacuum pump is -0.08MPa, uses nitrogen Scavenging pipeline and reaction kettle 2 times, stir and heat up, when temperature rises to 130 ± 5 DEG C, be slowly added to ethylene oxide 1496g (34mol) controls 140 ± 5 DEG C of reaction temperature, and to maintain 0.25 ± 0.05MPa of gauge pressure, end of reaction slowly adds charging rate Enter propylene oxide 1479g (25.5mol), controls 140 ± 5 DEG C of reaction temperature, end of reaction is slow added into ethylene oxide 1496g (34mol) controls 140 ± 5 DEG C of reaction temperature, and end of reaction is cooled to room temperature, and obtains faint yellow liquid product;
2) above-mentioned product 472g is weighed, isopropanol 300g and water 450g is added, sodium chloroacetate 99g is added dropwise, is warming up to 60 DEG C Back flow reaction 3h, cooling obtain transparent clay stabilizer.
Test example
1, prevent swollen performance test
Clay stabilizer prepared by Example 1~6, according to People's Republic of China (PRC) oil and gas industry standard SY/T 5971-94 water filling measures anti-dilative with clay stabilizer method of evaluating performance, according to China PetroChemical Corporation standard Q/ SH 0053-2010 clay stabilizer technical requirements measure water-fastness rate, as a result see the table below 1.
Clay stabilizer prevents swollen the performance test results in 1 Examples 1 to 6 of table
As shown in Table 1, clay stabilizer has and excellent prevents swollen performance in Examples 1 to 6.
2, compatibility is tested
Clay stabilizer prepared by Example 1~6, (+1% clay stabilization of 0.3% thickening agent is compounded with commercially available thickening agent Agent, surplus are water), its compatibility is investigated, as a result see the table below 2.
The compatibility evaluation result of clay stabilizer and commercially available thickening agent in 2 Examples 1 to 6 of table
As shown in Table 2, clay stabilizer and non-ionic hydroxypropyl guar gum, anionic polyacrylamide in Examples 1 to 6 Occur after amine, cationic-type polyacrylamide class thickener compounding without floccule or flocculation phenomenon, compatibility is good.

Claims (10)

1. oil-gas field fracturing clay stabilizer, it is characterised in that: the general structure of the clay stabilizer is as follows:
In formula 2: A is polyoxyethylene groups, and B is polyoxypropylene base, and x, y take any integer in 0~10 respectively, and z takes any in 2~10 Integer;R is the hydroxyalkyl or-CH of hydrogen, the alkyl of 1~5 carbon, 1~5 carbon2-COONa;N takes any integer in 2~5.
2. clay stabilizer according to claim 1, it is characterised in that: in formula 2, x takes any integer in 0~6, and y takes 0~ Any integer in 4, z take any integer in 2~5, and R is hydrogen, methyl or-CH2-COONa。
3. clay stabilizer according to claim 2, it is characterised in that: in formula 2, x takes 0, y that 0 or 3, z is taken to take 4 or 5, the R to be Hydrogen or methyl.
4. clay stabilizer according to claim 3, it is characterised in that: in formula 2, it is first that x, which takes 0, y that 0 or 3, z is taken to take 5, R, Base.
5. the preparation method of clay stabilizer as described in any one of Claims 1 to 4, it is characterised in that: with polyethylene polyamine Ethylene oxide progress is added after ethylene oxide and/or propylene oxide progress open loop addition are added according to actual needs for initiator Then open loop addition carries out the positive ionization of amine.
6. preparation method according to claim 5, it is characterised in that: the general structure of the polyethylene polyamine is as follows:
In formula 3: n takes any integer in 2~5.
7. preparation method according to claim 6, it is characterised in that: the polyethylene polyamine and ethylene oxide and/or ring The molar ratio of Ethylene Oxide is 1:(n+4) × (x+y+z).
8. preparation method according to claim 7, it is characterised in that: the cationoid reaction are as follows: obtained by open loop addition Solvent and cationic reagent are added in product, 0.5~15h is reacted at 25~100 DEG C of temperature.
9. preparation method according to claim 8, it is characterised in that: the cationic reagent is formic acid, acetic acid, phosphorus Acid, citric acid, the alkyl halide of 1~5 carbon, the halohydrin of 1~5 carbon or 2~5 carbon halogenated carboxylic acid salt.
10. preparation method according to claim 8, it is characterised in that: the solvent is ethyl alcohol, isopropanol or ethylene glycol Aqueous solution.
CN201610041585.0A 2016-01-21 2016-01-21 Oil-gas field fracturing clay stabilizer and preparation method thereof Active CN105647506B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610041585.0A CN105647506B (en) 2016-01-21 2016-01-21 Oil-gas field fracturing clay stabilizer and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610041585.0A CN105647506B (en) 2016-01-21 2016-01-21 Oil-gas field fracturing clay stabilizer and preparation method thereof

Publications (2)

Publication Number Publication Date
CN105647506A CN105647506A (en) 2016-06-08
CN105647506B true CN105647506B (en) 2018-12-21

Family

ID=56486946

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610041585.0A Active CN105647506B (en) 2016-01-21 2016-01-21 Oil-gas field fracturing clay stabilizer and preparation method thereof

Country Status (1)

Country Link
CN (1) CN105647506B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018104133A1 (en) * 2016-12-09 2018-06-14 Evonik Degussa Gmbh Shale hydration inhibition agent
CN108329902A (en) * 2018-01-23 2018-07-27 中国石油天然气股份有限公司 Salt-tolerant clay stabilizer for preparing fracturing fluid from oilfield effluent and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104559958A (en) * 2013-10-23 2015-04-29 中国石油化工股份有限公司 Compound type polyamine shale inhibitor and preparation method thereof
CN104556771A (en) * 2014-10-11 2015-04-29 江苏苏博特新材料股份有限公司 Clay inhibitor as well as preparation method and application thereof
CN104592955A (en) * 2013-11-01 2015-05-06 中国石油化工股份有限公司 Polyamine shale inhibitor and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104559958A (en) * 2013-10-23 2015-04-29 中国石油化工股份有限公司 Compound type polyamine shale inhibitor and preparation method thereof
CN104592955A (en) * 2013-11-01 2015-05-06 中国石油化工股份有限公司 Polyamine shale inhibitor and preparation method thereof
CN104556771A (en) * 2014-10-11 2015-04-29 江苏苏博特新材料股份有限公司 Clay inhibitor as well as preparation method and application thereof

Also Published As

Publication number Publication date
CN105647506A (en) 2016-06-08

Similar Documents

Publication Publication Date Title
CA1247270A (en) Gelled aqueous compositions
EP0187451B1 (en) Gelled aqueous compositions
US10442973B1 (en) Super-amphiphobic strongly self-cleaning high-performance water-based drilling fluid and drilling method
CN109369848B (en) Functional temperature-resistant salt-resistant plugging agent and preparation method thereof
CN105647506B (en) Oil-gas field fracturing clay stabilizer and preparation method thereof
US9845421B1 (en) Encapsulating agent and preparing method thereof, and drilling fluid for petroleum drilling
US20180022985A1 (en) Method of using cationic polymers comprising imidazolium groups for permanent clay stabilization
RU2011153364A (en) METHODS AND COMPOSITIONS FOR INCREASING THE VISCOSITY OF HEAVY WATER BRAINS
JP2005504630A5 (en)
CN103044679A (en) Cationic polyamine polymer, and preparation method and application thereof
US11192964B2 (en) Ionic liquid shale inhibitor for drilling fluid and preparation method and application thereof
CN103773353A (en) Clay stabilizer for water base fracturing as well as preparation method and application thereof
CN106432708A (en) Multi-branched polyether amine, preparation method and applications thereof
CN106496048B (en) A kind of alkyl gemini quaternary ammonium salt suitable for shale gas horizontal well
CN104592955A (en) Polyamine shale inhibitor and preparation method thereof
EP0506192B1 (en) Aqueous gellable composition, useful for modifying the permeability of a petroleum reservoir
CN104559958A (en) Compound type polyamine shale inhibitor and preparation method thereof
CN107384361A (en) A kind of erucic acid base quaternary ammonium alkyl salt surfactant and preparation method thereof
CN112646559A (en) Sand carrying fluid with functions of improving flow resistance of thickened oil and stabilizing clay
EP0475325B1 (en) Gelatin of acrylamide-containing polymers with aminobenzoic acid compounds and water dispersible aldehydes
CN106147739A (en) A kind of pressure break clay stabilizer and preparation method thereof
CN108715755A (en) A kind of Swelling-resistant shrinking and swelling agent and preparation method thereof
EP0446865B1 (en) Gelation of acrylamide-containing polymers with hydroxyphenyl alkanols
CN104559957A (en) Preparation method of shale inhibitor with filtrate reduction property
CN104327278B (en) Hydrophobic associated polymer oil-displacing agent containing chitosan and preparation method of hydrophobic associated polymer oil-displacing agent

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