CN115305074B - Water-based crude oil pour point depressant, preparation method and application thereof - Google Patents

Water-based crude oil pour point depressant, preparation method and application thereof Download PDF

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CN115305074B
CN115305074B CN202211204892.8A CN202211204892A CN115305074B CN 115305074 B CN115305074 B CN 115305074B CN 202211204892 A CN202211204892 A CN 202211204892A CN 115305074 B CN115305074 B CN 115305074B
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pour point
point depressant
crude oil
water
stirring
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CN115305074A (en
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崔仕章
王黎明
吕志凤
修宗明
王开永
牟国毅
张海涛
石自娥
白海青
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Deshi Energy Technology Group Co ltd Qingdao Branch
Deshi Energy Technology Group Co Ltd
Shandong Deshi Chemical Co Ltd
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Deshi Energy Technology Group Co ltd Qingdao Branch
Deshi Energy Technology Group Co Ltd
Shandong Deshi Chemical Co Ltd
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    • 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
    • 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
    • C09K8/588Compositions 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 polymers
    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/08Pipe-line systems for liquids or viscous products
    • F17D1/16Facilitating the conveyance of liquids or effecting the conveyance of viscous products by modification of their viscosity
    • F17D1/17Facilitating the conveyance of liquids or effecting the conveyance of viscous products by modification of their viscosity by mixing with another liquid, i.e. diluting
    • 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
    • C09K2208/32Anticorrosion additives

Abstract

The invention belongs to the technical field of oilfield chemicals, and particularly relates to a water-based crude oil pour point depressant, and a preparation method and application thereof. The invention provides a water-based crude oil pour point depressant, a preparation method and application thereof, wherein the water-based crude oil pour point depressant comprises a pour point depressing main agent, an emulsifying agent, a stabilizing agent and a pour point depressing auxiliary agent; the pour point depressing main agent is an alcoholysis product of a methacrylate-crotonic acid-oleic acid terpolymer. The water-based crude oil pour point depressant provided by the invention is stable in state and safe to use, can be compatible with hydraulic fracturing fluid and tertiary oil recovery fluid, effectively prevents wax precipitation of a shaft, reduces the condensation point of crude oil, and thus improves the recovery ratio of the crude oil.

Description

Water-based crude oil pour point depressant, preparation method and application thereof
Technical Field
The application relates to the technical field of oilfield chemicals, in particular to a water-based crude oil pour point depressant, a preparation method and application thereof.
Background
The hydraulic fracturing is characterized in that a fracturing fluid is injected into an underground coal seam or rock stratum through ground equipment under the pressure transmission effect of the fluid, fractures of the coal seam or the rock stratum are pressed, a plurality of permeable zones with flow conductivity are formed, fractures of a reservoir stratum are communicated, and the purpose of efficiently exploiting resources is achieved.
In the process of hydraulic fracturing, a large volume of low temperature water-based fluid is pumped at high pressure into the reservoir formation, which can fracture the formation, allowing the crude oil to pool with the fractures into the production tubing. In the process, the low-temperature fluids fracture the stratum, but simultaneously reduce the temperature of the stratum, so that long carbon chain paraffin in the crude oil is condensed into the stratum fracture, the crude oil is blocked, and the yield is reduced. Conventional pour point depressants, wax inhibitors, are dissolved in organic solvents and are incompatible with hydraulic fracturing fluids and therefore cannot be used in hydraulic fracturing. Therefore, it is necessary to develop a water-based pour point depressant product, which is compatible with hydraulic fracturing fluid and tertiary oil recovery fluid, can be used in a large amount in the hydraulic fracturing and tertiary oil recovery processes to prevent wax precipitation of a shaft and reduce the condensation point of crude oil, thereby improving the recovery rate of the crude oil.
In view of this, the present invention is proposed.
Disclosure of Invention
The invention aims to provide a water-based crude oil pour point depressant and a preparation method thereof, wherein the water-based crude oil pour point depressant is compatible with hydraulic fracturing fluid and tertiary oil recovery fluid, so that the water-based crude oil pour point depressant can be used in a large amount in the hydraulic fracturing and tertiary oil recovery processes to prevent wax precipitation of a shaft and reduce the condensation point of crude oil, thereby improving the recovery ratio of the crude oil.
In order to achieve the above purpose of the present invention, the following technical solutions are adopted:
a water-based pour point depressant for crude oil, which comprises a pour point depressant main agent, an emulsifier, a stabilizer and a pour point depressant auxiliary agent;
the pour point depressing main agent is an alcoholysis product of a methacrylate-crotonic acid-oleic acid terpolymer.
In the application, an alcoholysis product of a methacrylate-crotonic acid-oleic acid terpolymer is used as a pour point depressing main agent, an alcoholysis type methacrylate-crotonic acid-oleic acid terpolymer is of a comb-shaped structure, and alkyl branched chains in the comb-shaped structure can act with colloid and asphaltene in high-condensation-point crude oil to prevent the colloid asphaltene from forming a three-dimensional network structure. So that wax crystal molecules are not easy to intertwine with each other to form macromolecules, and the pour point depressing and viscosity reducing effects are enhanced.
The weight ratio of the pour point depressing main agent to the emulsifier to the stabilizer to the pour point depressing auxiliary agent is (20 to 40): (1 to 4): (0.5 to 1.5): (1 to 5).
In the application, the pour point depressant is formed by compounding the pour point depressant main agent, the emulsifier, the stabilizer and the pour point depressant auxiliary agent in a specific proportion, so that the pour point depressant provided by the application is stable in state and excellent in pour point depression effect, and has a certain effect of relieving corrosion of an oil well casing.
The emulsifier is a mixture of OP-4 and OP-10;
preferably, the mass ratio of OP-4 to OP-10 in the emulsifier is (1 to 3): (5 to 10).
In the application, the emulsifier is formed by compounding OP-4 and OP-10 in a specific mass ratio, so that the emulsifying and dispersing effect is more excellent.
Preferably, the mass ratio of OP-4 to OP-10 in the emulsifier is (1 to 2): (5 to 9).
The stabilizer is one or more of sodium hydroxymethyl cellulose, sodium hydroxyethyl cellulose and polyacrylate.
The pour point depressing auxiliary agent comprises one or more of bactericide, corrosion inhibitor and scale inhibitor;
in the application, the pour point depressing additive is added, and comprises one or more of a bactericide, a corrosion inhibitor and a scale inhibitor, and the scale inhibitor effectively solves the scaling problem and avoids the problems of heat transfer effect reduction, local corrosion of equipment and pipelines and the like caused by scaling; the bactericide can avoid the problems that the product of microorganism corrodes metal, causes pipeline blockage or generates oxygen concentration difference to corrode a battery and the like; the corrosion inhibitor can relieve the corrosivity of corrosive gases such as dissolved oxygen, hydrogen sulfide, carbon dioxide and the like on equipment and pipelines.
Preferably, the mass ratio of the bactericide to the corrosion inhibitor to the scale inhibitor in the pour point depressant additive is (1 to 3): (1 to 3): (1 to 3).
In the application, the bactericide, the corrosion inhibitor and the scale inhibitor are compounded according to a specific mass ratio to prepare the pour point depressing auxiliary agent, and the bactericide, the corrosion inhibitor and the scale inhibitor have synergistic effect, so that the sterilization, scale inhibition and corrosion inhibition effects are enhanced, and the function of protecting an equipment pipeline is achieved.
The invention also provides a preparation method of the water-based crude oil pour point depressant, which comprises the following steps:
heating the pour point depressant main agent to 70-90 ℃, stirring for 30min to 40min, adding the emulsifier, continuously stirring for 30min to 50min, adding deionized water, stirring for 60min to 90min, adding the pour point depressant additive, stirring for 60min to 75min, adding the stabilizer, and stirring for 30min to 45min to obtain the water-based crude oil pour point depressant.
In the application, the pour point depressant for the water-based crude oil is prepared by compounding a pour point depressant main agent with an emulsifier, a pour point depressant auxiliary agent and a stabilizer. The pour point depressant can be used in a shaft to prevent wax precipitation in the shaft, reduce the condensation point of crude oil and improve the extraction rate of the crude oil.
The preparation method of the pour point depressing main agent comprises the following steps: adding methacrylate, crotonic acid and oleic acid into a solvent, keeping the temperature at 70-90 ℃, stirring for 30min-45min, adding an initiator, and reacting for 5-7h to obtain a terpolymer; heating to 110-120 ℃, adding higher aliphatic alcohol, and stirring for 6-8 h until the water yield reaches the theoretical water yield, thereby obtaining the alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer.
In the method, methacrylate, crotonic acid and oleic acid are polymerized to obtain a terpolymer, and then alcoholysis is performed on the terpolymer and a higher fatty alcohol to obtain an alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer. The alcoholysis product is used as a pour point depressing main agent in the application, the alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer is of a comb-shaped structure, alkyl branched chains in the comb-shaped structure can act with colloid and asphaltene in the crude oil with high condensation point, wax crystal nuclei can be effectively inhibited from growing, a network structure formed by crosslinking of the wax crystal nuclei can be damaged, and the condensation point of the crude oil can be effectively reduced.
The mass ratio of the methacrylate to the crotonic acid to the oleic acid is (7 to 8): (2 to 6): (5 to 9);
the initiator comprises benzoyl peroxide or azobisisobutyronitrile;
in the application, benzoyl peroxide or azobisisobutyronitrile is added as an initiator to improve the polymerization rate. The azodiisobutyronitrile is an oil-soluble azo initiator, and the azo initiator has stable reaction, is a first-order reaction, has no side reaction and is better controlled. Can increase the polymerization reaction rate, inhibit the self-crosslinking of the precipitated wax crystal structure and enable the rapid polymerization.
The higher fatty alcohols include tetradecanol, hexadecanol and octadecanol.
The using amount of the initiator is 0.05-0.15% of the total mass of the methacrylate, the crotonic acid and the oleic acid;
the polymerization reaction rate is gradually increased along with the increase of the dosage of the initiator, the self-crosslinking effect of the precipitated wax crystal structure is inhibited, the rapid polymerization can be realized, and the action effect is obvious when the dosage of the initiator is 0.05-0.15 percent of the total mass of the methacrylate, the crotonic acid and the oleic acid. Because each monomer in the reaction system is well polymerized. With the continuous increase of the dosage, the effect is not obvious, so that the initiator dosage can achieve better effect within the range.
Preferably, the mass ratio of the higher aliphatic alcohol to the terpolymer is (1 to 5): 1.
it is another object of the present invention to provide the use of the above water-based pour point depressant for crude oil in the recovery and transportation of crude oil.
The invention has the following beneficial effects:
1. the water-based crude oil pour point depressant provided by the invention is stable in state, is not easy to delaminate, and can relieve the corrosion of an oil well casing; the water-soluble paint is water-soluble, so that the safety of the paint is greatly improved, and meanwhile, the on-site storage tank and the pipeline can be directly cleaned by water, so that the injection process flow is greatly simplified, and the workload and the working strength are greatly reduced; the additive can be compatible with hydraulic fracturing fluid and tertiary oil recovery fluid, can be used in the hydraulic fracturing and tertiary oil recovery processes in a large amount, prevents wax precipitation of a shaft, reduces the condensation point of crude oil, and accordingly improves the recovery rate of the crude oil.
2. The preparation method of the water-based crude oil pour point depressant provided by the invention has the advantages of low cost, simple process flow, strong operability, good completeness and repeatability and capability of realizing large-scale industrial continuous production.
Detailed Description
In order to more clearly explain the overall concept of the present application, the following detailed description is given by way of example in conjunction with the description. In the following description, numerous specific details are set forth in order to provide a more thorough understanding of the present invention. It will be apparent, however, to one skilled in the art, that the present invention may be practiced without one or more of these specific details. In other instances, well-known features have not been described in order to avoid obscuring the invention.
The examples, in which specific conditions are not specified, were conducted under conventional conditions or conditions recommended by the manufacturer.
In the following embodiments, reagents or instruments used are not indicated by manufacturers, and are all conventional products available by commercial purchase, unless otherwise specified.
Example 1
Preparation of pour point depressing main agent
Adding 7kg of methacrylate, 2kg of crotonic acid and 5kg of oleic acid into 39kg of aromatic solvent, keeping the temperature at 70 ℃, stirring for 30min, adding 7g of initiator benzoyl peroxide, and reacting for 5h to obtain a terpolymer; taking 5kg of the terpolymer, heating the temperature to 110 ℃, adding 5kg of hexadecanol, stirring for 6h until the water yield reaches the theoretical water yield, and obtaining the alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer, which is marked as a pour point depressing main agent 1.
The preparation of the water-based crude oil pour point depressant comprises the following steps:
weighing 20kg of pour point depressant main agent 1, heating to 70 ℃, stirring for 30min, adding 286gOP-4 and 714gOP-10, continuing stirring for 30min, then adding 38.5kg of deionized water, stirring for 60min, then adding 333g of bactericide, 333g of corrosion inhibitor and 334g of scale inhibitor, stirring for 60min, finally adding 0.5kg of stabilizer sodium carboxymethylcellulose, and stirring for 30min to obtain the water-based crude oil pour point depressant, which is marked as sample 1.
Example 2
Preparation of pour point depressing main agent
Adding 7kg of methacrylate, 4kg of crotonic acid and 9kg of oleic acid into 25kg of aromatic solvent, stirring at the temperature of 90 ℃ for 45min under heat preservation, adding 16g of azodiisobutyronitrile serving as an initiator, and reacting for 7h to obtain a terpolymer; taking 5kg of the terpolymer, heating the temperature to 120 ℃, adding 10kg of octadecanol, stirring for 8h until the water yield reaches the theoretical water yield, and obtaining an alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer, which is marked as a pour point depressing main agent 2.
The preparation method of the water-based crude oil pour point depressant comprises the following steps:
weighing 40kg of pour point depressant 2, heating to 90 ℃, stirring for 40min, adding 571g of OP-4 and 3429g of OP-10, continuing stirring for 50min, then adding 24.5kg of deionized water, stirring for 90min, then adding 1250g of bactericide, 1250g of corrosion inhibitor and 2500g of scale inhibitor, stirring for 75min, finally adding 1.5kg of sodium hydroxyethyl cellulose as a stabilizer, and stirring for 45min to obtain the water-based crude oil pour point depressant, which is marked as sample 2.
Example 3
Preparation of pour point depressing main agent
Adding 8kg of methacrylate, 6kg of crotonic acid and 9kg of oleic acid into 34kg of aromatic hydrocarbon solvent, keeping the temperature at 80 ℃, stirring for 40min, adding 25.3g of initiator benzoyl peroxide, and reacting for 6h to obtain a terpolymer; taking 5kg of the terpolymer, heating the temperature to 115 ℃, adding 20kg of tetradecanol, stirring for 7h until the water yield reaches the theoretical water yield, and obtaining an alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer, which is marked as a pour point depressing main agent 3.
The preparation of the water-based crude oil pour point depressant comprises the following steps:
weighing 30kg of pour point depressant main agent 3, heating to 80 ℃, stirring for 35min, adding 375g of OP-4 and 2625g of OP-10, continuing to stir for 40min, then adding 27.5kg of deionized water, stirring for 80min, then adding 1000g of bactericide, 2000g of corrosion inhibitor and 1000g of scale inhibitor, stirring for 70min, finally adding 1.5kg of stabilizer polyacrylate, and stirring for 40min to obtain the water-based crude oil pour point depressant, which is marked as sample 3.
Example 4
Preparation of pour point depressing main agent
Adding 8kg of methacrylate, 5kg of crotonic acid and 5kg of oleic acid into 32kg of aromatic solvent, keeping the temperature at 80 ℃, stirring for 40min, adding 27g of initiator azobisisobutyronitrile, and reacting for 6h to obtain a terpolymer; taking 5kg of the terpolymer, heating the temperature to 115 ℃, adding 25kg of hexadecanol, stirring for 7h until the water yield reaches the theoretical water yield, and obtaining an alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer, which is marked as a pour point depressing main agent 4.
The preparation method of the water-based crude oil pour point depressant comprises the following steps:
weighing 30kg of pour point depressant 4, heating to 80 ℃, stirring for 35min, adding 364gOP-4 and 1636gOP-10, continuing to stir for 40min, then adding 32kg of deionized water, stirring for 80min, then adding 1200g of bactericide, 600g of corrosion inhibitor and 1200g of scale inhibitor, stirring for 70min, finally adding 1kg of stabilizer polyacrylate, and stirring for 40min to obtain the water-based crude oil pour point depressant, which is marked as sample 4.
Comparative example 1
The difference from sample 1 is that no emulsifier was used and the rest is the same.
Comparative example 2
The difference from sample 1 is that no stabilizer is used, and the rest is the same.
Comparative example 3
The difference from sample 1 is that the preparation of the pour point depressant is not subject to alcoholysis, i.e. the pour point depressant is methacrylate-crotonic acid-oleic acid terpolymer, and the rest is the same.
Comparative example 4
According to the method of the embodiment provided by an oil field pour point depressant and a preparation method thereof (CN 113087836A), the pour point depressant is prepared by the following steps:
(1) 150.66g of vinyl acetate (1.75 mol), 37.04g of vinyl benzoate (0.25 mol), 57.07g of caprolactone (0.5 mol) and 100.10g of caprolactone methacrylate (0.5 mol) were introduced into the reactor;
(2) Then 1000g of mixed benzene, 377.00g of toluene, 500g of dimethylbenzene (10 times) and 0.1877g of titanium isopropoxide catalyst (1 per mill) are added, nitrogen protection and stirring are started, and the temperature is raised to 50 ℃;
(3) Dissolving 5.631g (3%) of LPO in 50.68g of benzene, controlling the temperature to be 50-95 ℃, dropwise adding 10% benzene solution of an initiator, controlling the temperature to be 85-95 ℃ after dropwise adding, and reacting for 10-15 hours to obtain an intermediate product A1;
(4) 68.35g (3%) of fumaric acid-vinyl acetate-fluorobutyl acrylate copolymer 113.92g (5%) of tween-40 are mixed and stirred uniformly to obtain the pour point depressant for the oil field.
Test example 1
In the test example, pour point depression amplitude test experiments are carried out on crude oil in a certain area of the victory oil field by using the pour point depressants prepared in examples 1 to 4 and comparative examples 1 to 2 respectively according to the method in GB/T26985-2018, and the pour point test experiments are carried out on each group of pour point depressants at the temperature of 80 ℃. The test results are shown in table 1.
TABLE 1 pour point depression amplitude test results
Figure DEST_PATH_IMAGE001
As can be seen from Table 1, the pour point depressant for crude oil provided in examples 1-4 has a large pour point depression, effectively prevents wax deposition in the well, lowers the pour point of crude oil, and is stable, while the systems of comparative examples 1-2 are unstable and cannot be applied on site. The pour point depressing main agent of the comparative example 3 is not subjected to alcoholysis, namely, the methacrylate-crotonic acid-oleic acid terpolymer is used as the pour point depressing main agent, so that the pour point depressing amplitude is obviously reduced.
The above description is only an example of the present application and is not intended to limit the present application. Various modifications and changes may occur to those skilled in the art to which the present application pertains. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present application should be included in the scope of the claims of the present application.

Claims (7)

1. The water-based crude oil pour point depressant is characterized by comprising a pour point depressant main agent, an emulsifier, a stabilizer and a pour point depressant auxiliary agent;
the pour point depressing main agent is an alcoholysis product of a methacrylate-crotonic acid-oleic acid terpolymer;
the pour point depressing main agent, the emulsifier, the stabilizer and the pour point depressing auxiliary agent are in a weight ratio of (20-40): (1-4): (0.5-1.5): (1-5);
the emulsifier is a mixture of OP-4 and OP-10;
the stabilizer is one or more of sodium hydroxymethyl cellulose, sodium hydroxyethyl cellulose and polyacrylate;
the methacrylate-crotonic acid-oleic acid terpolymer is prepared from methacrylate, crotonic acid and oleic acid, wherein the mass ratio of the methacrylate to the crotonic acid to the oleic acid is (7-8): (2-6): (5-10);
the alcohol used in alcoholysis is higher aliphatic alcohol, and the higher aliphatic alcohol comprises tetradecanol, hexadecanol and octadecanol.
2. The pour point depressant of claim 1, wherein the pour point depressant additive comprises one or more of a bactericide, a corrosion inhibitor, and a scale inhibitor.
3. The preparation method of the water-based crude oil pour point depressant according to any one of claims 1 to 2, which is characterized by comprising the following steps of:
heating the pour point depressant main agent to 70-90 ℃, stirring for 30-40 min, adding the emulsifier, continuously stirring for 30-50 min, adding deionized water, stirring for 60-90 min, adding the pour point depressant auxiliary agent, stirring for 60-75 min, finally adding the stabilizer, and stirring for 30-45 min to obtain the water-based crude oil pour point depressant.
4. The method according to claim 3, wherein the preparation method of the pour point depressant main agent comprises the following steps:
adding methacrylate, crotonic acid and oleic acid into a solvent, stirring for 30-45 min at the temperature of 70-90 ℃, adding an initiator, and reacting for 5-7 h to obtain a terpolymer; heating to 110-120 ℃, adding higher fatty alcohol, stirring for 6-8 h until the water yield reaches the theoretical water yield, and obtaining the alcoholysis product of the methacrylate-crotonic acid-oleic acid terpolymer.
5. The method of claim 4, wherein the initiator comprises benzoyl peroxide or azobisisobutyronitrile.
6. The method of claim 5, wherein the amount of the initiator is 0.05% to 0.15% of the total mass of the methacrylate, the crotonic acid and the oleic acid.
7. Use of the water-based crude oil pour point depressant according to any one of claims 1 to 2 in crude oil extraction and transportation processes.
CN202211204892.8A 2022-09-30 2022-09-30 Water-based crude oil pour point depressant, preparation method and application thereof Active CN115305074B (en)

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