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CN107916096A - The displacement of reservoir oil Surfactant Used in Viscoelastic Fracturing Fluids composition and preparation method and application - Google Patents

The displacement of reservoir oil Surfactant Used in Viscoelastic Fracturing Fluids composition and preparation method and application Download PDF

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Publication number
CN107916096A
CN107916096A CN201610877491.7A CN201610877491A CN107916096A CN 107916096 A CN107916096 A CN 107916096A CN 201610877491 A CN201610877491 A CN 201610877491A CN 107916096 A CN107916096 A CN 107916096A
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oil
surfactant
displacement
reservoir
composition
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CN107916096B (en
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王辉辉
沈之芹
何良好
翟晓东
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China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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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
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/30Viscoelastic surfactants [VES]

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Abstract

The present invention relates to a kind of composition of displacement of reservoir oil Surfactant Used in Viscoelastic Fracturing Fluids, and mainly solving surfactant in current production technology, oil displacement efficiency is poor in LOW PERMEABILITY RESERVOIR in high temperature as oil displacement agent, simultaneously because containing alkali, huge injury is brought to stratum and oil well.By using the composition for displacement of reservoir oil Surfactant Used in Viscoelastic Fracturing Fluids, including amphoteric surfactant and acylate in formula shown in (I);The acylate in formula at least one of (II);R1Selected from C8~C29Alkyl, any one in alkenyl, the R2And R3It is independently chosen from C1~C5Alkylidene, any one in hydroxyl substituted alkylene, any one of X in carboxylate radical, sulfonate radical, the molar ratio of the amphoteric surfactant and acylate is 1:0.01~1:100 technical solution, preferably resolves the technical problem, available in the displacement of reservoir oil production in oil field.

Description

The displacement of reservoir oil Surfactant Used in Viscoelastic Fracturing Fluids composition and preparation method and application
Technical field
The present invention relates to synthesis of the displacement of reservoir oil by the use of the composition of Surfactant Used in Viscoelastic Fracturing Fluids and the composition to be used as the displacement of reservoir oil The application of agent.
Background technology
With increasing rapidly for national economy, domestic petroleum disparities between supply and demand become increasingly conspicuous, and are mainly shown as petroleum resources phase It is relatively low that the growth of demand, the recovery percent of reserves ratio of crude oil are not caught up with to poorer, oil exploration and development and proved reserves.To alleviate China's oil scarcity of resources, reduce crude output notch, ensure China's oil safety, it is necessary to which one of important measures taken are exactly Increase substantially the recovery ratio of crude oil in China.For example, the average recovery ratio of Sinopec is only 28% at present, still have more than 70% petroleum resources fail to obtain effective exploitation utilization, cause a large amount of remaining reserves to be retained in underground.How further to tap the latent power Synergy, carry out tertiary oil recovery, it has also become one of problem urgently to be resolved hurrily.
In tertiary oil recovery technology, chemical flooding is main attack technology and the direction that recovery ratio is improved in China, including caustic waterflooding, table Face surfactant flooding (micella drives and microemulsion drives), polymer flooding and combination flooding.In these chemical flooding technologies, all it be unable to do without efficient Surfactant, by reduce oil water interfacial tension to ultra low degree (be less than 10-2MN/m residual oil flowing) is made to be carried to reach The purpose of high oil recovery factor.Surfactant oil displacement uses Recompounded multielement system mostly at present, while comprising non-ionic Surfactant and ionic surfactant, are additionally added the auxiliary agents such as alkali and alcohol in part formulation.Such as patent CN101024764A A kind of surfactant of oil-field thick-oil well is provided, which is by water, piece alkali, ethanol, oleic acid, alkyl phenol polyoxy second Alkene ether, sodium dodecyl benzenylsulfonate composition.For another example patent CN1394935 has invented a kind of chemical oil displacement agent, it mainly includes pungent Base benzene sulfonic acid receives the clean property agent of anionic surface, surfactant adjuvant, surfactant synergist, surface active agent solubilization agent. This oil displacement agent can significantly reduce the structural viscosity of viscous crude, while can reduce oil water interfacial tension, so as to improve oil recovering Rate.However, above-mentioned surface active agent for tertiary oil recovery still suffers from more problem, the salt resistant character of anion surfactant compared with Difference, nonionic surfactant temperature is sensitive, easily separates out, should not largely use under high temperature.For this reason, people started it is cloudy-non- The research of ionic surface active agent, will two kinds of non-ionic groups and anionic group of different nature designs on same surface In active agent molecule, the advantages of making it have anion and nonionic surfactant concurrently, have complementary advantages, and there is excellent heatproof to resist Salt performance, shows good application prospect.Gemini surface active agent has the special construction for being different from conventional surfactant, It is assigned with a series of uniquenesses such as ultralow interfacial tension, low critical micelle concentration, low Krafft points and excellent wetabilitys Property, also result in the great interest of people.However, the Gemini surface active agent of domestic-developed is mainly cation double seasons at present , there is the shortcomings of absorption loss is big, of high cost in ammonium salt type, lose the economic base of application.Special surfactant is due to valency Lattice are extremely expensive, most of also to stop phase of basic research indoors, it is difficult to promote and apply at the scene.Amphion surface-active Existing anionic hydrophilic base has cationic hydrophilic base and shows both sexes again in agent molecule, adapts to wider pH range, right Metal ion has stronger chelation, available for high salinity, the oil reservoir displacement of reservoir oil of higher temperature, and can substantially reduce nonionic Chromatographic fractionation effect when type surfactant is compounded with anionic surfactant.Therefore, zwitterionic surfactant Research and development obtained people more and more pay attention to and concern, especially beet alkali ampholytic surface active agent has become three One of hot spot of secondary oil recovery area research.
It is increasingly deep with oilfield exploitation degree, apply common oil reservoir it is neutral can preferable surfactant in high temperature Ultralow interfacial tension cannot be formed with crude oil in middle LOW PERMEABILITY RESERVOIR, cause oil displacement efficiency to be deteriorated, seriously constrain oil recovery rate Raising.In order to reduce oil/water interfacial tension to a greater extent, alkali (such as sodium hydroxide, sodium carbonate of high concentration are often added Deng), for example, patent CN1439689A disclose a kind of alkali, mixed surfactant and polymer ternary composite oil-displacing system and It is applied, wherein the alkali selected is Na2CO3.However, alkali brings huge injury to stratum and oil well etc. in use, seriously Etching apparatus and pipeline, spend substantial contribution in maintenance, maintenance, considerably increase the financial cost of tertiary oil recovery.Patent CN201310166961.5 proposes a kind of displacement composition for the vermiculate glues that anion surfactant is formed, Ke Yi Recovery ratio is improved to a certain degree.Therefore, with single surfactant it is difficult to meet in view of the deficiencies of the prior art hypotonic in high temperature Oil water interfacial tension is down to the displacement of reservoir oil requirements such as ultralow, heat endurance is good, compatibility is good under reservoir condition, offer one kind is provided and is existed Steady chemical structure under the conditions of LOW PERMEABILITY RESERVOIR in alkali-free, high temperature, can form 10 with crude oil- 3~10- 4MN/m ultralow interfacial tensions, The new oil displacement system of oil recovery factor is effectively improved, the scope for improving recovery ratio is extended to the harsh oil field such as hypotonic in high temperature Application in.
The content of the invention
The first technical problem to be solved by the present invention is that there are hypotonic condition in high temperature for surfactant in the prior art The problem of lower oil displacement efficiency is low, there is provided a kind of composition of new Surfactant Used in Viscoelastic Fracturing Fluids, the surfactant have the displacement of reservoir oil The characteristics of efficient, be particularly suitable for husky seven oil fields of Jiangsu oilfield.
The second technical problem to be solved by the present invention is to provide a kind of with solving one of technical problem corresponding glutinous bullet The preparation method of composition of property surfactant.
The third technical problem to be solved by the present invention is the combination of one of technical problem Surfactant Used in Viscoelastic Fracturing Fluids Application of the thing in the displacement of reservoir oil of oil field.
To solve one of above-mentioned technical problem, the technical solution adopted by the present invention is as follows:The group of Surfactant Used in Viscoelastic Fracturing Fluids Compound, including amphoteric surfactant and acylate;The amphoteric surfactant and the molar ratio of acylate are 1: 0.01~1:100;The amphoteric surfactant is selected from least one of structure shown in formula (I);The acylate choosing At least one of structure shown in (II) from formula;
R in formula (I)1Selected from C8~C29Alkyl, any one in alkenyl, the R2And R3It is independently chosen from C1~C5 Alkylidene, any one in hydroxyl substituted alkylene, the R4And R5It is independently chosen from C1~C4Alkyl, hydroxyl takes At least one of substituted alkyl;Any one of X in carboxylate radical, sulfonate radical in formula (II), Y be selected from hydrogen, alkyl, hydroxyl, Any one in halogen, amino.
In above-mentioned technical proposal, the R4And R5Independently it preferably is selected from C1~C4Alkyl;More preferably R4And R5Select From methyl, at this time, the glycine betaine Surfactant is selected from least one of structure as shown in (I ') in formula:
At this time, with acylate combined interface tension force performance more preferably.
Preferred R in above-mentioned technical proposal1For C12~C25Alkyl or alkenyl in any one, R2For C2~C3Alkylene In base or hydroxyl substituted alkylene any one, R3For C1~C3Alkylidene.
The most preferred technique scheme from the angle for improving recovery ratio, above-mentioned technical proposal:R1For C16~C22Alkyl Or any one in alkenyl, R2For C3Alkylidene or hydroxyl substituted alkylene in any one, R3For C1~C2Alkylene Base;Acylate be selected from naphthalene sulfonate, amino substitution naphthalene sulfonate, hydroxyl substitution naphthalene sulfonate, hydroxyl substitution naphthalene-carboxylic acid salt with And at least one of alkyl substitution naphthalene-carboxylic acid salt.
Interfacial tension is reduced from collaboration, improves the consideration of recovery ratio angle, and in above-mentioned technical proposal, the glycine betaine surface is lived Property agent be selected from it is two or more in structure shown in formula (I) or formula (I '), such as R1The different two or more glycine betaine tables of carbon number Face activating agent, at this time, R1The different two or more beet alkali surface activators of carbon number have with anion surfactant Good synergistic function, the R as shown in preferred formula (I) or formula (I ')1For C15~C29Long carbon chain amphoteric surfactant At least one of R shown in formula (I) or formula (I ')1For C8~C14At least one of short carbon chain amphoteric surfactant Combination.
In above-mentioned technical proposal, the molar ratio of the amphoteric surfactant and acylate is preferably (1:0.1)~ (1:10)。
In above-mentioned technical proposal, the displacement of reservoir oil further includes water with the composition of Surfactant Used in Viscoelastic Fracturing Fluids, especially suitable for surface Surfactant waterflood.
To solve the two of above-mentioned technical problem, the technical solution adopted by the present invention is as follows:Described in one of above-mentioned technical problem The preparation method of the composition of Surfactant Used in Viscoelastic Fracturing Fluids, comprises the following steps:
A) by aliphatic acid acid or its ester and required amidation reagent when 100~160 DEG C of reactions 3~20 are small;Then plus Enter carboxylating reagent ZR3COOM in 50~100 DEG C the reaction was continued 2~20 it is small when, obtain the Long carbon chain glycine betaine surface described in formula (I) Activating agent;Wherein, Long carbon chain fatty acid methyl ester:Amidation reagent:The molar ratio of carboxylating reagent is 1:(1~3):(1~4);Z is selected From any one in hydrogen, hydroxyl, halogen, amino, any one of M in alkali metal, alkaline-earth metal, ammonium ion;
B) it is dissolved in water by acylate and according to the obtained amphoteric surfactantes of step a), then according to rubbing You are than being (1:0.1)~(1:10) it is uniformly mixed, obtains the surface activator composition.
In above-mentioned technical proposal, step a) preferred amides reagent is NH2-R2-N(CH3)2;Amphoteric surface lives in step b) Property agent and acylate molar ratio preferred scope be (1:0.1)~(1:10).
It is as follows to solve three the technical solution adopted by the present invention of present invention problem:One of above-mentioned technical problem sticks Application of the composition of elastic surface activating agent in the displacement of reservoir oil of oil field.
The technical solution adopted by the present invention is as follows:The group of Surfactant Used in Viscoelastic Fracturing Fluids any one of above-mentioned technical proposal Application of the compound in the displacement of reservoir oil of oil field.The reservoir temperature is preferably 60~100 DEG C.The oil displacement system is to the infiltration in oil reservoir Rate amount is not particularly limited, and can reach preferable oil displacement efficiency, but during middle-low permeability in oil reservoir this area face it is prominent The technical difficulty gone out, from this angle, present invention is particularly suitable for high temperature middle and low permeable reservoir, such as oil reservoir temperature in oil reservoir Spend for 85 DEG C, permeability is 30 millidarcies.
Technical solution using the present invention, uses surface activator composition of the present invention, has boundary during tertiary oil recovery Face activity is high:Under the conditions of compound surfactant composition dosage is 0.01~0.6w.t.%, in salinity in 30,000 mg/L, In seven live water of calcium ions and magnesium ions content 400mg/L sand, remain to form 10 with underground crude oil-3~10-4MN/m ultralow interface Tension force;Washing oil ability is strong, improves recovery ratio up to 14.9%;The advantages that surface activator composition system is simple, achieve compared with Good technique effect.
Below by embodiment, the present invention is further elaborated.
Embodiment
【Embodiment 1】
1. prepared by surfactant
(1) erucyl amide carboxybetaine amphoteric surfactant (R1=C21, R2=C3、R3=C2) preparation
A) 0.5 mole of methyl erucate and the desired amount of amidation reagent N, N- dimethylated propyl diethylenetriamine are added into reaction kettle In, when 140 DEG C of reactions 8 are small, vacuum pump is opened, extracts methanol and excessive N that reaction produces, N- dimethylated propyl diethylenetriamines, obtain To erucic acid acyl group tertiary amine product, the desired amount of sodium chloroacetate is added, when 75 DEG C of reactions 9 are small, is carried with absolute ethyl alcohol recrystallization Long carbon chain beet alkali ampholytic surface active agent is obtained after pure;Wherein, methyl erucate:N, N- dimethylated propyl diethylenetriamine:Sodium chloroacetate Molar ratio is 1:2.5:1.5.
B) erucyl amide carboxybetaine amphoteric surfactant prepared by naphthalene sulfonate and the present invention is dissolved separately in In water, stir 30 minutes, aqueous solution is configured to, then by above-mentioned surfactant according to amphoteric surfactant and acylate Molar ratio is 1:0.7 is uniformly mixed, and obtains the composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
A) viscosity measurement
Using III type viscosimeters of U.S. Brookfield DV-, at 85 DEG C, rotating speed 7.34S-1Under the conditions of, measure is above-mentioned The oil displacement agent of 0.3% concentration and the viscosity of the husky seven Oil Field water (being shown in Table 3) in Jiangsu the results are shown in Table 2.
B) interfacial tension is evaluated
TX-500C rotating interfacial tensimeters, at 85 DEG C, rotating speed 6000 are produced using Texas ,Usa university Under the conditions of rev/min, the interfacial tension knot between the dewatered oil in husky seven oil fields of oil displacement agent and Jiangsu for measuring above-mentioned 0.1% concentration Fruit is shown in Table 2.
C) oil displacement experiment is evaluated
According to the composite oil-displacing system physical simulation flooding test in SY/T6424-2000 composite oil-displacing system performance test methods Measure of merit, at 87 DEG C, length 30cm, a diameter of 2.5cm, permeability is to carry out imitation oil displacement experiment on the rock core of 30 millidarcies Experiment.Water drive is first carried out to aqueous 98%, after water drive, the drive of above-mentioned 0.3% concentration of metaideophone 0.3pv (rock pore volume) After finish, then water drive to aqueous 100%, improves oil recovery factor and the results are shown in Table 2.
【Embodiment 2】
1. prepared by surfactant
(1) triacontanoic acid amido carboxyl beet alkali ampholytic surface active agent (R1=C29, R2=C2、R3=C2) preparation
A) 0.5 mole of Long carbon chain triacontanoic acid methyl esters and the desired amount of amidation reagent N, N- dimethyl-ethylenediamine are added In reaction kettle, when 130 DEG C of reactions 6 are small, vacuum pump is opened, extracts methanol and excessive N that reaction produces, N- dimethyl second two Amine, obtains triacontanoic acid acyl group tertiary amine product, adds the desired amount of sodium chloroacetate, when 85 DEG C of reactions 15 are small, through absolute ethyl alcohol Long carbon chain beet alkali surface activator is obtained after recrystallization purification;Wherein, triacontanoic acid methyl esters:N, N- dimethyl-ethylenediamine:Chloroethene The molar ratio of sour sodium is 1:2:1.5.
B) triacontanoic acid amido carboxyl beet alkali ampholytic surface active agent prepared by naphthalene sulfonate and the present invention is dissolved respectively Yu Shuizhong, stirs 30 minutes, aqueous solution is configured to, then by above-mentioned surfactant according to amphoteric surfactant and organic acid Salt molar ratio is 1:0.7 is uniformly mixed, and obtains the composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
【Embodiment 3】
1. prepared by surfactant
(1) n-nonanoic acid amido carboxyl beet alkali ampholytic surface active agent (R1=C8, R2=C3、R3=C3) preparation
A) 0.5 mole of methyl pelargonate and the desired amount of amidation reagent N, N- dimethylated propyl diethylenetriamine are added into reaction kettle In, when 135 DEG C of reactions 10 are small, vacuum pump is opened, extracts methanol and excessive N that reaction produces, N- dimethylated propyl diethylenetriamines, obtain To n-nonanoic acid acyl group tertiary amine product, the desired amount of β-chloropropionic acid sodium is added, when 75 DEG C of reactions 10 are small, is tied again through absolute ethyl alcohol Long carbon chain beet alkali surface activator is obtained after crystalline substance purification;Wherein, methyl pelargonate:N, N- dimethylated propyl diethylenetriamine:β-chloropropionic acid The molar ratio of sodium is 1:2:1.6.
B) n-nonanoic acid amido carboxyl beet alkali ampholytic surface active agent prepared by naphthalene sulfonate and the present invention is dissolved separately in In water, stir 30 minutes, aqueous solution is configured to, then by above-mentioned surfactant according to amphoteric surfactant and acylate Molar ratio is 1:0.7 is uniformly mixed, and obtains the composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
【Embodiment 4】
1. prepared by surfactant
(1) lauric amide carboxybetaine amphoteric surfactant (R1=C11, R2=C3、R3=C3) preparation
A) 0.5 mole of methyl laurate and the desired amount of amidation reagent N, N- dimethylated propyl diethylenetriamine are added into reaction kettle In, when 140 DEG C of reactions 10 are small, vacuum pump is opened, extracts methanol and excessive N that reaction produces, N- dimethylated propyl diethylenetriamines, obtain To laurate acyl group tertiary amine product, the desired amount of β-chloropropionic acid sodium is added, when 75 DEG C of reactions 10 are small, with absolute ethyl alcohol weight Long carbon chain beet alkali surface activator is obtained after crystallization and purification;Wherein, methyl laurate:N, N- dimethylated propyl diethylenetriamine:β-chloro The molar ratio of sodium propionate is 1:2.5:1.5.
B) lauric amide carboxybetaine amphoteric surfactant prepared by naphthalene sulfonate and the present invention is dissolved respectively Yu Shuizhong, stirs 30 minutes, aqueous solution is configured to, then by above-mentioned surfactant according to amphoteric surfactant and organic acid Salt molar ratio is 1:0.7 is uniformly mixed, and obtains the composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
【Embodiment 5】
1. prepared by surfactant
By the erucyl amide carboxybetaine amphoteric surfactant in embodiment 1, the lauric amide carboxylic in embodiment 4 Base beet alkali ampholytic surface active agent and naphthalene sulfonate are dissolved in water, and are stirred 30 minutes, are configured to aqueous solution, then will Above-mentioned surfactant is according to the both sexes of erucyl amide carboxybetaine, n-nonanoic acid amido carboxyl beet alkali ampholytic surface active agent and has Machine hydrochlorate molar ratio is 0.5:0.5:0.7 is uniformly mixed, and obtains the composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
【Embodiment 6】
1. prepared by surfactant
By the erucyl amide carboxybetaine amphoteric surfactant in embodiment 1, the n-nonanoic acid amido carboxyl in embodiment 3 Beet alkali ampholytic surface active agent and naphthalene sulfonate are dissolved in water, and are stirred 30 minutes, are configured to aqueous solution, then will be upper Surfactant is stated according to the both sexes of erucyl amide carboxybetaine, n-nonanoic acid amido carboxyl beet alkali ampholytic surface active agent and organic Hydrochlorate molar ratio is 0.5:0.5:0.7 is uniformly mixed, and obtains the composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
【Comparative example 1】
1. prepared by surfactant
Naphthalene sulfonate and docosyl carboxybetaine amphoteric surfactant are dissolved in water, stir 30 points Clock, is configured to aqueous solution, is then 1 according to amphoteric surfactant and acylate molar ratio by above-mentioned surfactant:1 is mixed Close uniformly, obtain the composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
【Comparative example 2】
1. prepared by surfactant
According to the method described in patent CN103242816B, the surfactant of synthesis such as lower structure:C11H23CON (CH2CH2OH)2, naphthalene sulfonate and the surfactant of synthesis are dissolved in water, stirs 30 minutes, is configured to water-soluble Liquid, is then 1 according to the surfactant and acylate molar ratio of synthesis by above-mentioned surfactant:1 is uniformly mixed, and obtains The composition of Surfactant Used in Viscoelastic Fracturing Fluids.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
【Comparative example 3】
1. prepared by surfactant
By the erucyl amide carboxybetaine amphoteric surfactant in embodiment 2, the n-nonanoic acid amido carboxyl in embodiment 6 Beet alkali ampholytic surface active agent is dissolved in water, and is stirred 30 minutes, aqueous solution is configured to, then by above-mentioned surface-active Agent is 1 according to the both sexes of erucyl amide carboxybetaine, n-nonanoic acid amido carboxyl beet alkali ampholytic surface active agent molar ratio:1 mixing Uniformly, the composition of Surfactant Used in Viscoelastic Fracturing Fluids is obtained.
2. surfactant properties are evaluated
In addition to oil displacement agent composition is different, method of evaluating performance is the same as embodiment 1.For ease of comparing the composition of oil displacement agent Table 1 is listed in, evaluation result is listed in table 2.
Surface activator composition composition in 1 embodiment of table and comparative example
Oil displacement agent performance evaluation in 2 embodiment of table and comparative example
Viscosity (mPa.s) Interfacial tension (mN/m) Improve recovery ratio %
Embodiment 1 20.1 0.00086 14.0
Embodiment 2 15.2 0.0062 13.3
Embodiment 3 15.0 0.0089 12.1
Embodiment 4 15.7 0.0082 12.0
Embodiment 5 20.5 0.00037 14.9
Embodiment 6 19.9 0.00060 14.5
Comparative example 1 8.5 0.013 7.5
Comparative example 2 2.5 0.017 5.0
Comparative example 3 9.0 0.0018 6.9
3 Jiangsu oilfield of table sand, seven live water
Unit Na++K+ Mg2+ Ca2+ Cl- SO4 2- HCO3 - TDS
mg/L 8730.8 154 220 10224 1507.7 5152.5 25830

Claims (10)

1. a kind of displacement of reservoir oil plays surface activator composition, including amphoteric surfactant and acylate with glutinous;The both sexes The molar ratio of surfactant and acylate is 1:0.01~1:100;The amphoteric surfactant is selected from knot shown in formula (I) At least one of structure;The acylate at least one of structure shown in (II) in formula;
R in formula (I)1Selected from C8~C29Alkyl, any one in alkenyl, the R2And R3It is independently chosen from C1~C5Asia Any one in alkyl, hydroxyl substituted alkylene, the R4And R5It is independently chosen from C1~C4Alkyl, hydroxyl substitution alkane At least one of base;Any one of X in carboxylate radical, sulfonate radical in formula (II), Y be selected from hydrogen, alkyl, hydroxyl, halogen, Any one in amino.
2. composition according to claim 1, it is characterised in that R in the amphoteric surfactant1For C12~C25's Any one in alkyl or alkenyl, R2For C2~C3Alkylidene or hydroxyl substituted alkylene in any one, R3For C1~ C3Alkylidene.
3. composition according to claim 2, it is characterised in that R in the amphoteric surfactant1For C16~C22's Any one in alkyl or alkenyl, R2For C3Alkylidene or hydroxyl substituted alkylene in any one, R3For C1~C2's Alkylidene.
4. surface activator composition according to any one of claim 1 to 3, it is characterized in that the composition includes Water.
5. composition according to claim 1, it is characterised in that the acylate is selected from naphthalene sulfonate, amino substitutes At least one of naphthalene sulfonate, hydroxyl substitution naphthalene sulfonate, hydroxyl substitution naphthalene-carboxylic acid salt and alkyl substitution naphthalene-carboxylic acid salt.
6. composition according to claim 1, it is characterised in that the amphoteric surfactant is the R shown in formula (I)1For C15~C29R shown in formula (I) of at least one of Long carbon chain amphoteric surfactant1For C8~C14Short carbon chain both sexes table The combination of at least one of face activating agent.
7. claim 1~6 any displacement of reservoir oil glutinous preparation method for playing surface activator composition, including following step Suddenly:
A) by aliphatic acid acid or its ester and required amidation reagent when 100~160 DEG C of reactions 3~20 are small;Then add carboxylic Change reagent ZR3COOM in 50~100 DEG C the reaction was continued 2~20 it is small when, obtain the amphoteric surfactant described in formula (I);Wherein, Fatty acid methyl ester:Amidation reagent:The molar ratio of carboxylating reagent is 1:(1~3):(1~4);Z is selected from hydrogen, hydroxyl, halogen, ammonia Any one in base, any one of M in alkali metal, alkaline-earth metal, ammonium ion;
B) it is dissolved in water by acylate and according to the obtained amphoteric surfactantes of step a), then according to molar ratio For (1:0.1)~(1:10) it is uniformly mixed, obtains the displacement of reservoir oil and play surface activator composition with glutinous.
8. application of the displacement of reservoir oil Surfactant Used in Viscoelastic Fracturing Fluids in the displacement of reservoir oil of oil field any one of claim 1 to 6.
9. application of the Surfactant Used in Viscoelastic Fracturing Fluids according to claim 8 in the displacement of reservoir oil of oil field, it is characterised in that described to answer It is LOW PERMEABILITY RESERVOIR with applicable oil reservoir.
10. application of the Surfactant Used in Viscoelastic Fracturing Fluids according to claim 9 in the displacement of reservoir oil of oil field, it is characterised in that described low The temperature that permeability is hidden is 60~100 DEG C.
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