CN117720684B - Amphoteric polymer and preparation method and application thereof - Google Patents

Amphoteric polymer and preparation method and application thereof Download PDF

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CN117720684B
CN117720684B CN202410177914.9A CN202410177914A CN117720684B CN 117720684 B CN117720684 B CN 117720684B CN 202410177914 A CN202410177914 A CN 202410177914A CN 117720684 B CN117720684 B CN 117720684B
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acrylamide
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acrylic acid
acid sodium
amphoteric polymer
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CN117720684A (en
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宋新旺
成振松
印树明
王旭东
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Shandong Institute Of Petroleum And Chemical Engineering
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Shandong Institute Of Petroleum And Chemical Engineering
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Abstract

The application discloses an amphoteric polymer and a preparation method and application thereof, and belongs to the technical field of petroleum exploitation chemicals. The polymer is prepared from acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine according to a molar ratio of 6-8:1.8-3.8:0.5-1: 0.3-1. The polymer prepared by the application can increase the viscosity of water phase, reduce the tension of oil-water interface, overcome the chromatographic separation effect of a polymer/surfactant binary system in the prior art, and improve the petroleum recovery ratio; the water solubility is good, and the temperature resistance and the salt resistance are good; can also be used as flocculant in sewage treatment.

Description

Amphoteric polymer and preparation method and application thereof
Technical Field
The application belongs to the technical field of petroleum exploitation chemicals, and particularly relates to an amphoteric polymer and a preparation method and application thereof.
Background
The recovery ratio of the water-flooding reservoir is generally only 25-40%, a large amount of ascertained petroleum resources cannot be effectively exploited and utilized, chemical oil extraction is an important means for improving the recovery ratio, and the recovery ratio can be improved by 15-25% on the basis of water flooding. The partially hydrolyzed polyacrylamide and the surfactant are main chemicals used in chemical oil extraction, the polymer has the functions of increasing the viscosity of an aqueous phase, expanding the swept volume, reducing the interfacial tension of oil and water, improving the oil displacement efficiency, and realizing the purpose of improving the recovery ratio through the synergistic effect. However, the difference of adsorption and hydrodynamic retention in oil layers causes different migration speeds, so that chromatographic separation is generated, the synergistic effect is lost, and the oil displacement effect is affected. The above problems can be solved by synthesizing the polymer and the surfactant on the same molecule.
Disclosure of Invention
In order to solve the problems, an amphoteric polymer is provided, which can overcome the chromatographic separation effect of a polymer/surfactant binary system in the prior art and improve the petroleum recovery ratio; greatly reduces the interfacial tension of oil and water, and increases the viscosity of water phase; the water solubility is good, and the temperature resistance and the salt resistance are good; can also be used as flocculant in sewage treatment.
The specific technical scheme of the application is as follows:
in one aspect, the application provides an amphoteric polymer, wherein the molecular structural formula of the polymer is shown as formula I:
formula (I)
In the formula I, R is any one of C6H13、C8H17、C10H21、C12H25、C14H29、C16H33、C18H37、C20H41、C22H45、C24H49.
In another aspect, the present application also provides a method for preparing an amphoteric polymer, comprising the steps of:
firstly, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium and alkyl diallyl hydroxypropyl sulfobetaine, adding deionized water for dissolution, and adjusting the pH value to 7-10 by alkali solution;
Step two, introducing nitrogen for 8-12min at 40-80 ℃, adding an initiator, and reacting for 2-5h to obtain a product;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Optionally, in the first step, the mass percentage of the acrylamide is 60-80%, the mass percentage of the acrylic acid is 18-38%, the mass percentage of the 2-acrylamido-2-methylpropanesulfonic acid sodium is 2-10%, and the mass percentage of the alkyl diallyl hydroxypropyl sulfobetaine is 0.3-1.0%; preferably, 6.5 to 7.5:1.5-3.5:0.6-0.8:0.4-0.8.
Optionally, in the second step, the initiator is any one of azodiisobutylamidine hydrochloride and dibenzoyl peroxide, and is preferably azodiisobutylamidine hydrochloride.
Optionally, in the second step, the addition amount of the initiator is 0.3-1.0% of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium salt and the alkyl diallyl hydroxypropyl sulfobetaine monomer.
In another aspect, the application also provides the following applications:
The application of the amphoteric polymer in oil reservoir recovery.
The preparation method is applied to the improvement of the oil reservoir recovery ratio.
The beneficial effects of the application include, but are not limited to:
1. The amphoteric polymer prepared by the application is introduced with groups such as amide, carboxylic acid, hydroxypropyl sulfo and the like, has stronger hydration capability, and has better water solubility.
2. The amphoteric polymer prepared by the application is introduced with the zwitterionic group, so that the effect of electrolyte in the prepared water can be shielded, and the molecular chain is more stretched, thereby showing better salt resistance.
3. The amphoteric polymer prepared by the application introduces betaine structure monomer, can greatly reduce oil-water interfacial tension and improve oil displacement efficiency.
4. The polymer provided by the application has good water solubility, temperature resistance, salt resistance and shearing resistance, can greatly reduce the interfacial tension of oil and water, and can better improve the oil recovery rate by 18%. Has wide market prospect.
Detailed Description
The present application is described in detail below with reference to examples, but the present application is not limited to these examples.
The starting materials and catalysts in the examples of the present application were purchased commercially, unless otherwise specified.
Example 1
An amphoteric polymer, the molecular structural formula of which is shown in formula I:
formula (I);
In the formula I, R is C 24H49; x: Y: Z: q=6: 2.8:0.5:0.7;
A method for preparing the amphoteric polymer, which comprises the following steps: the method comprises the following steps:
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
The reaction formula of the preparation process is as follows:
Formula (II).
Example 2
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 22H45; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 3
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 20H41; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 4
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 18H37; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 5
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 16H33; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 6
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 14H29; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 7
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 12H25; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 8
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 10H21; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 9
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 8H17; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 10
An amphoteric polymer, the molecular structural formula of which is shown in formula I, wherein R is C 6H13; x: Y: Z: q=6: 2.8:0.5:0.7.
Step one, a molar ratio of 6:2.8:0.5:0.7, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine, dissolving with deionized water, and regulating the pH to 7 with 5% NaOH solution;
Step two, introducing nitrogen for 8min at 60 ℃, adding azo diisobutylamidine hydrochloride, and reacting for 2h to obtain a product; the addition amount of the initiator is 0.3 percent of the total mass of the acrylamide, the acrylic acid, the 2-acrylamide-2-methylpropanesulfonic acid sodium and the alkyl diallyl hydroxypropyl sulfobetaine monomer in the first step;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
Example 11
An ampholytic polymer differs from example 2 in that in the molecular structural formula of the polymer, R is C 4H9; x: Y: Z: q=6: 2.8:0.5:0.7.
Example 12
The difference from example 2 is that the starting materials in this example are, in molar ratio, acrylamide: acrylic acid: sodium 2-acrylamido-2-methylpropanesulfonate: alkyl diallyl hydroxypropyl sulfobetaine = 6.2:2.5:0.5:0.8.
Comparative example 1, using one polymer of the prior art in reservoir recovery; the polymer was free of betaine monomer compared to the polymer prepared in example 2.
Formula (III).
Comparative example 2, using one polymer of the prior art in reservoir recovery; the polymer used was structurally different from the polymer prepared in example 2, and did not contain long hydrophobic chains R. The structural formula of betaine monomer used in the comparative example is specifically shown in a formula (I) in a [0007] section of CN 107739422A.
Comparative example 3
The sulfobetaine type amphoteric ion polymer in the prior art is applied to oil reservoir collection; as shown in formula (IV), the polymer used has a different betaine monomer structure than the polymer prepared in example 2, and does not contain a long hydrophobic chain R. (see, sulfobetaine type zwitterionic polymer synthesis and performance study-Mao Cheng).
Formula (IV).
The polymers of examples 1 to 11 and comparative examples 1 to 3 were examined for interfacial tension, dissolution property and salt resistance, respectively, in petroleum recovery; the specific detection method comprises the following steps:
water solubility: the target block was injected with water to prepare a 0.15% polymer solution, which was stirred at 40 ℃ at 700rpm, and the time of complete dissolution was observed and recorded, and if the solution was uniform and free of fish eyes within 2 hours, it was judged that the solubility was good, otherwise the solubility was poor.
Interfacial tension: a0.15% polymer solution 100 g was prepared with a 1% NaCl solution and the interfacial tension was measured at 70℃using a rotary drop interfacial tensiometer according to the SY/T5370-1999 assay.
Salt resistance: a solution containing 1% NaCl and 2+ mg/L Ca was prepared, a 0.15% polymer solution 100 g was prepared from this water, and the interfacial tension was measured, and if the interfacial tension was kept at the same order of magnitude as that of the solution prepared with no Ca 2+ added, it was judged that the salt resistance was good, otherwise it was judged that the salt resistance was poor.
Apparent viscosity: a0.15% polymer solution was prepared with a 1% NaCl solution and the apparent viscosity was measured at 70℃using a DV-III type rotational viscometer with a 0# spindle.
The crude oil in the experiment was taken from the western region of the island field.
The results of the measurements are shown in Table 1 below.
TABLE 1 comparison of the Properties of the different polymers
As can be seen from the data in the table, in example 1 and example 11, when the hydrophobic chain length R of betaine monomer in the polymer exceeds 22, the solubility is poor, and other data cannot be measured; when R is less than 6, there is no significant advantage in interfacial tension, salt resistance and apparent viscosity as compared with the comparative example; in examples 2-10, the R value is reduced from 22 to 6, the solubility is good, the salt resistance is good, and the interfacial tension can be reduced to the order of magnitude of 10-2mN/m when the R value is between 12 and 20; as the R value decreases, the apparent viscosity decreases because long carbon chains can form an associated structure, increasing the unstructured viscosity; in example 12, apparent viscosity increased due to increased betaine monomer content; in 3 comparative examples, the solubility and the salt resistance are both good, and the effect of reducing the interfacial tension is poor because the long carbon chain is not contained, and the interfacial tension is high; meanwhile, the apparent viscosity is low because an association structure cannot be formed.
The above description is only an example of the present application, and the scope of the present application is not limited to the specific examples, but is defined by the claims of the present application. Various modifications and variations of the present application will be apparent to those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the technical idea and principle of the present application should be included in the protection scope of the present application.

Claims (7)

1. An ampholytic polymer, which is characterized in that the molecular structural formula of the polymer is shown as formula I:
In the formula I, R is any one of C6H13、C8H17、C10H21、C12H25、C14H29、C16H33、C18H37、C20H41、C22H45; x, Y, Z and Q are 6-8:1.8-3.8:0.5-1:0.3-1, and the molecular weight of the polymer is 600-1500 ten thousand.
2. A method of preparing the amphoteric polymer of claim 1, comprising the steps of:
Firstly, weighing acrylamide, acrylic acid, 2-acrylamide-2-methylpropanesulfonic acid sodium and alkyl diallyl hydroxypropyl sulfobetaine, adding into deionized water for dissolution, and adjusting the pH to 7-10 with alkali solution;
Step two, introducing nitrogen for 8-12min at 40-80 ℃, adding an initiator, and reacting for 2-5h to obtain a product;
and thirdly, washing, crushing and drying the product by using absolute ethyl alcohol to obtain the amphoteric polymer.
3. The method according to claim 2, wherein in the first step, the addition amount of acrylamide, acrylic acid, 2-acrylamido-2-methylpropanesulfonic acid sodium salt, alkyl diallyl hydroxypropyl sulfobetaine is 6-8:1.8-3.8:0.5-1:0.3-1.
4. The method according to claim 2, wherein in the second step, the initiator is any one of azobisisobutyrimidine hydrochloride and dibenzoyl peroxide.
5. The preparation method according to claim 2, wherein in the second step, the addition amount of the initiator is 0.3-1.0% of the total mass of acrylamide, acrylic acid, 2-acrylamido-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine monomer.
6. The preparation method according to claim 2, wherein in the second step, the addition amount of the initiator is 0.3-0.85% of the total mass of acrylamide, acrylic acid, 2-acrylamido-2-methylpropanesulfonic acid sodium salt and alkyl diallyl hydroxypropyl sulfobetaine monomer.
7. Use of the amphiphilic polymer of claim 1 in oil reservoir recovery.
CN202410177914.9A 2024-02-09 2024-02-09 Amphoteric polymer and preparation method and application thereof Active CN117720684B (en)

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Publication number Priority date Publication date Assignee Title
CN106753315A (en) * 2016-11-11 2017-05-31 成都佰椿石油科技有限公司 A kind of temperature control type becomes mucic acid and preparation method thereof
CN107739422A (en) * 2017-06-05 2018-02-27 西南石油大学 A kind of betaine type amphoteric ionomer oil displacement agent and synthetic method
CN114163573A (en) * 2021-06-29 2022-03-11 中国石油天然气集团有限公司 Zwitterionic polymer, preparation method and application thereof

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Publication number Priority date Publication date Assignee Title
FR2914647B1 (en) * 2007-04-05 2011-10-21 Rhodia Recherches Et Tech COPOLYMER COMPRISING BETAINIC UNITS AND HYDROPHOBIC AND / OR AMPHIPHILIC UNITS, PREPARATION METHOD, AND USES.

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106753315A (en) * 2016-11-11 2017-05-31 成都佰椿石油科技有限公司 A kind of temperature control type becomes mucic acid and preparation method thereof
CN107739422A (en) * 2017-06-05 2018-02-27 西南石油大学 A kind of betaine type amphoteric ionomer oil displacement agent and synthetic method
CN114163573A (en) * 2021-06-29 2022-03-11 中国石油天然气集团有限公司 Zwitterionic polymer, preparation method and application thereof

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