CN113620984B - Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof - Google Patents

Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof Download PDF

Info

Publication number
CN113620984B
CN113620984B CN202111067743.7A CN202111067743A CN113620984B CN 113620984 B CN113620984 B CN 113620984B CN 202111067743 A CN202111067743 A CN 202111067743A CN 113620984 B CN113620984 B CN 113620984B
Authority
CN
China
Prior art keywords
surfactant
organosilicon
sodium
sulfonate
integer
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
CN202111067743.7A
Other languages
Chinese (zh)
Other versions
CN113620984A (en
Inventor
丁锡刚
杨姗
常夕春
吴庆凯
胡朋朋
李金平
姜力华
祝东明
秦玉斌
姚勇
李慎伟
齐书磊
齐高政
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.)
Shandong Xingang Chemical Co ltd
Original Assignee
Shandong Xingang Chemical Co ltd
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 Shandong Xingang Chemical Co ltd filed Critical Shandong Xingang Chemical Co ltd
Priority to CN202111067743.7A priority Critical patent/CN113620984B/en
Publication of CN113620984A publication Critical patent/CN113620984A/en
Application granted granted Critical
Publication of CN113620984B publication Critical patent/CN113620984B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/02Silicon compounds
    • C07F7/08Compounds having one or more C—Si linkages
    • C07F7/0834Compounds having one or more O-Si linkage
    • C07F7/0838Compounds with one or more Si-O-Si sequences
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/02Silicon compounds
    • C07F7/08Compounds having one or more C—Si linkages
    • C07F7/0834Compounds having one or more O-Si linkage
    • C07F7/0838Compounds with one or more Si-O-Si sequences
    • C07F7/0872Preparation and treatment thereof
    • C07F7/0889Reactions not involving the Si atom of the Si-O-Si sequence
    • 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
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • C08G77/38Polysiloxanes modified by chemical after-treatment
    • C08G77/382Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon
    • C08G77/385Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon containing halogens
    • 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
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • C08G77/38Polysiloxanes modified by chemical after-treatment
    • C08G77/382Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon
    • C08G77/388Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon containing nitrogen
    • 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
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • C08G77/38Polysiloxanes modified by chemical after-treatment
    • C08G77/382Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon
    • C08G77/392Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon containing sulfur
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Silicon Polymers (AREA)

Abstract

The invention provides a surfactant containing an organosilicon group for reducing pressure and increasing injection, a preparation method and application thereof, and belongs to the technical field of oil extraction in oil fields. The organic silicon group-containing surfactant for reducing pressure and increasing injection has the structural formula (1):wherein m is an integer of 2-11, n is an integer of 0-9, and m+n is an integer of 2-11; r is R 1 A saturated or unsaturated hydrocarbon chain representing a C8-C20 carbon chain length; r is R 2 Represents alkyl carboxylic acid or sulfonate groups. The surfactant containing the organosilicon group for depressurization and injection increase is prepared by introducing the organosilicon group into hydrocarbon surfactant, so that the surfactant has the property of reducing the surface tension and the interfacial tension, and the defect that the organosilicon surfactant is easy to hydrolyze can be avoided, so that the surfactant can be effectively applied to high-temperature high-salt low-permeability oil reservoirs and oil-wet oil reservoirs, and the oil extraction effect is greatly improved.

Description

Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof
Technical Field
The invention belongs to the technical field of oil extraction in oil fields, and relates to a surfactant containing organic silicon groups for reducing pressure and increasing injection, a preparation method and application thereof.
Background
At present, the surfactant oil displacement technology has been widely applied in the field of tertiary oil recovery in oil fields. The oil displacement surfactant has the effects of improving recovery ratio by reducing oil-water interfacial tension, improving oil washing efficiency, emulsifying oil carrying and the like. However, for low-permeability oil reservoirs and oil-wet reservoirs, the best oil extraction effect cannot be achieved by simply reducing the oil-water interfacial tension, the surface tension, the capillary resistance and the water locking effect of the low-permeability oil reservoirs are reduced, the water injection pressure is reduced, the injection capacity is enhanced, the oil-wet property of the oil reservoirs is converted into water-wet property, and the crude oil recovery rate is further improved.
The existing surfactant for reducing pressure and increasing injection is generally hydrocarbon surfactant, and the surfactant takes hydrocarbon chain as hydrophobic group, so that the surfactant has outstanding performance on reducing the interfacial tension of oil and water, but the minimum surface tension can reach about 30mN/m because the hydrocarbon chain is arranged on the interface by methylene.
The organic silicon surfactant takes the siloxane chain as a hydrophobic group, the siloxane chain is arranged in an umbrella shape on the interface, the siloxane chain can be rapidly spread on an oil-water interface, and the siloxane chain has flexibility and is more tightly arranged on the oil-water interface, so that the organic silicon surfactant has super spreadability and super wettability, and the surface tension can be reduced to about 20 mN/m. Organosilicon surfactants have a greater advantage over hydrocarbon surfactants in reducing surface tension.
At present, the organosilicon surfactant is widely applied to the fields of pesticides, leather, textiles, coatings, petrochemical industry and daily chemicals mainly as a wetting surfactant because of the excellent surface spreadability. However, most of the types contain Si-O-C bonds and are easy to hydrolyze due to high price, and particularly, because the organosilicon hydrophobic groups only spread on an oil-water interface and cannot enter the interior of crude oil, the performance of the organosilicon hydrophobic groups on the oil-water interface tension is lower than that of hydrocarbon surfactants, so that the organosilicon hydrophobic groups have not been widely applied in the oil displacement field.
Patent CN106398677a provides an oil-displacing organosilicon surfactant and a preparation method thereof, wherein allyl polyether is connected with tetramethyl cyclotetrasiloxane and heptamethyl trisiloxane to form a nonionic surfactant with polymethyl siloxane as a hydrophobic chain and polyoxyethylene ether and polyoxypropylene ether as hydrophilic groups, and the organosilicon surfactant can obtain lower surface tension, but has poor interfacial tension, is difficult to achieve better oil-displacing effect, has cloud point and cannot be used at a higher temperature.
Disclosure of Invention
The invention provides a surfactant containing an organosilicon group for reducing pressure and increasing injection, a preparation method and application thereof, and the surfactant has the property of reducing surface tension and interfacial tension, can avoid the defect that the organosilicon surfactant is easy to hydrolyze, can be effectively applied to high-temperature high-salt low-permeability oil reservoirs and oil-wet oil reservoirs, and greatly improves the oil extraction effect.
In order to solve the technical problems, the invention provides a surfactant containing organosilicon groups for reducing pressure and increasing injection, which is characterized by having the structural formula (1):
wherein m is an integer of 2-11, n is an integer of 0-9, and m+n is an integer of 2-11; r is R 1 A saturated or unsaturated hydrocarbon chain representing a C8-C20 carbon chain length; r is R 2 Represents alkyl carboxylic acid or sulfonate groups. It will be appreciated that in the above scheme, m may be specifically 2, 3, 4, 5, 6, 7, 8, 9, 10. 11, n may be specifically 0, 1, 2, 3, 4, 5, 6, 7, 8, 9, and m+n may be specifically 2, 3, 4, 5, 6, 7, 8, 9, 10, 11.
Preferably, R 1 At least one of linear alkyl, cocoyl, tallow, rosin groups with carbon chain length of C8-C20; r is R 2 At least one selected from sodium acetate, sodium ethylsulfonate and sodium hydroxy propane sulfonate.
The invention also provides a preparation method of the surfactant containing the organosilicon group for depressurization and injection increase, which is prepared by adopting the ring-opening reaction of organic primary amine and single-end epoxy polysiloxane and then reacting with halogenated alkyl carboxylate or halogenated alkyl sulfonate.
Preferably, the method comprises the following two steps:
adding 1.0mol of organic primary amine and a certain amount of organic solvent into a three-port reaction vessel, stirring and heating to 50-70 ℃, slowly dropwise adding 1.0-1.1mol of single-end epoxy polysiloxane, dropwise adding for 2-4 hours, and continuing stirring and reacting for 2-4 hours to prepare an organosilicon surfactant intermediate product;
adding 0.01mol of phase transfer catalyst cetyl trimethyl ammonium bromide into the intermediate product, adding 1.2-1.5mol of halogenated alkyl carboxylic acid or sulfonate, stirring at 60-80 ℃ for 3-5h, dropwise adding an alkali solution in the reaction process to adjust the pH value to 8-10, continuing to react for 2-4h after the dropwise adding is finished, cooling to normal temperature, adjusting the pH value to be neutral by hydrochloric acid, standing for layering, removing bottom salt and salt water, and removing part of organic solvent under reduced pressure to obtain the organosilicon surfactant solution.
Preferably, the single-ended epoxy polysiloxane is at least one selected from single-ended epoxy silicone oil or side-ended epoxy silicone oil with a polymerization degree of 3-12, and has a structural formula (2) as follows:
wherein m is an integer of 2 to 11, n is an integer of 0 to 9, and m+n is an integer of 2 to 11.
It will be appreciated that the single-ended epoxy polysiloxane employed is derived from epoxy silicone oils 105-3, 105-4, commercially available from Anhui Ai Yaoda silicone oil Co., ltd, wherein 105-3 is of the terminal side chain type and 105-4 is of the single-ended type. The single-end epoxy polysiloxane contains epoxy bonds, is easy to react with primary amine to introduce polysiloxane groups, has mild reaction conditions, is easy to purchase raw materials, and can customize products with specific polymerization degree models.
Preferably, the molar ratio of organic primary amine to single-ended epoxy polysiloxane added is 1: (1.0-1.1) the molar ratio of organic primary amine added to haloalkylcarboxylic acid or sulfonate is 1: (1.2-1.5);
the molar ratio of the added alkali to the halogenated alkyl carboxylic acid or sulfonate is 1:1, and the volume ratio of the added alkali solution to the organic solvent is 1:3-2:3.
It will be appreciated that the above scheme defines organic primary amine and single-ended epoxy polysiloxane because if the amount added is below this molar ratio, it will result in an excess of single-ended epoxy polysiloxane, producing tertiary amine intermediates, eventually forming quaternary ammonium salt byproducts, whereas above this molar ratio it will result in an excess of organic primary amine, eventually forming organic amine carboxylate free of polysiloxane groups, with reduced levels of target products, affecting the surface tension properties of the product; meanwhile, the molar ratio of the catalyst to the halogenated alkyl carboxylic acid or the sulfonate is limited because if the addition amount is lower than the molar ratio, the halogenated alkyl carboxylic acid or the sulfonate is excessive, and the quaternary ammonium salt with a plurality of hydrophilic groups is generated, and if the addition amount is higher than the molar ratio, the reaction is incomplete, the secondary amine intermediate is excessive, the hydrophilicity is reduced, the content of a target product is low, and meanwhile, the hydrolysis loss condition of the halogenated alkyl carboxylic acid or the sulfonate is considered by the molar ratio; similarly, the molar ratio of base to haloalkylcarboxylic acid or sulfonate is defined because if the amount is below this molar ratio, it will result in incomplete reaction of haloalkylcarboxylic acid or sulfonate, whereas above this molar ratio it will result in too high a pH, exacerbating haloalkylcarboxylic acid or sulfonate hydrolysis, and neutralization consumes more hydrochloric acid, producing excessive by-products; meanwhile, the volume ratio of alkali liquor to organic solvent is limited, because if the addition amount is lower than the volume ratio, the organic solvent is excessive, the burden of subsequent treatment such as distillation concentration is increased, and if the addition amount is higher than the volume ratio, the system contains excessive water, inorganic salt and other impurities are dissolved in the system, the system is not layered and does not precipitate, the impurity content of the system is high, the product performance is reduced, and the subsequent treatment for further purification is quite complicated.
Preferably, the organic primary amine is at least one selected from linear fatty amine with a carbon chain length of C8-C20, cocoamine, tallow amine and rosin amine; the organic solvent is at least one selected from anhydrous ethanol and isopropanol; the alkali is at least one selected from sodium hydroxide, potassium hydroxide and ammonia water; the halogenated alkyl carboxylic acid or sulfonic acid is at least one selected from sodium chloroacetate, sodium chloroethyl sulfonate, sodium 3-chloro-2-hydroxy propane sulfonate, sodium bromoacetate and sodium bromoethyl sulfonate.
The invention also provides application of the surfactant containing the organosilicon group for depressurization and injection increase in the water produced by a certain block of a victory oil field with the total degree of mineralization of 8207 mg/L.
Preferably, when the surfactant is used, a compound sample of the surfactant for reducing pressure and increasing injection and the 6501 surfactant containing the organosilicon group is added, wherein the use concentration of the compound sample is 0.1-0.3%, and the mass percentage of the surfactant for reducing pressure and increasing injection and the 6501 surfactant containing the organosilicon group in the compound sample is 1:4.
Preferably, the interfacial tension of the surfactant compound sample for depressurization and injection enhancement containing the organosilicon group is as low as 10 under the conditions of 70 ℃ and 5000r/min -3 On the order of mN/m.
Preferably, the surface tension of the compounded sample of the surfactant for depressurization and injection enhancement containing the organosilicon group is less than 28mN/m at 25 ℃.
Compared with the prior art, the invention has the beneficial effects that:
1. the organic silicon-containing surfactant provided by the invention has two types of hydrophobic groups, namely hydrocarbon and organic silicon, hydrocarbon chains penetrate into crude oil, the organic silicon groups are spread on an oil-water interface, the surface tension and the interfacial tension can be simultaneously reduced, and the organic silicon-containing surfactant has the advantages of structure and performance in the aspects of pressure reduction, injection increase and oil displacement.
2. The organic silicon surfactant provided by the invention has the advantages that the carboxylic acid, the sulfonic acid and the hydroxyl are all strong hydrophilic groups, and the organic silicon surfactant is matched with hydrocarbon hydrophobic groups and organic silicon hydrophobic groups, so that the organic silicon surfactant can obtain a larger HLB coverage range, is easy to dissolve in water, is free from turbidity and precipitation, has good surface tension and interfacial tension performance, can be effectively applied to oil displacement exploitation of low-permeability oil reservoirs and oil-wet oil reservoirs, and can be applied to the fields of pesticides, leather, textiles, coatings, petrochemical industry, daily chemicals and the like.
3. The organic silicon surfactant provided by the invention belongs to tertiary amine structures, and hydrophilic groups are electronegative as a whole, so that the stratum adsorption consumption can be reduced.
4. The C in the single-end epoxy polysiloxane selected by the invention is directly connected with Si, does not contain Si-O-C bond easy to hydrolyze, and the product is easy to dissolve in water and is not easy to hydrolyze; and the product does not contain long polyoxyethylene ether or polyoxypropylene ether groups, has no cloud point and can be used at higher temperature.
5. The preparation method adopts long-chain organic primary amine to carry out ring opening reaction with epoxy polysiloxane, then reacts with sodium chloroacetate and the like to introduce strong hydrophilic groups, and is classical and reliable. The raw materials are easy to obtain, the price is relatively low, the synthesis process is simple, the reaction condition is mild, the industrial production is easy to realize, the cost performance of the product is high, and the method has good application prospect.
Detailed Description
The following description of the technical solutions in the embodiments of the present invention will be clear and complete, and it is obvious that the described embodiments are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Example 1: synthesis of dodecyl-N-hydroxypropyl-propoxy-poly (3) siloxane-N-sodium acetate surfactant (m=2, n=0)
185.35g (1.0 mol) of dodecylamine and 360mL of absolute ethyl alcohol are added into a 2000mL reaction vessel, the temperature is raised to 50-70 ℃ by stirring, 370g (1.1 mol) of epoxy poly (3) siloxane (m=2, n=0) is slowly added dropwise into the reaction vessel for 2h, and stirring is continued for 2h after the completion of the dropwise addition.
To the above product was added 3.64g (0.01 mol) of cetyltrimethylammonium bromide as a phase transfer catalyst, 175g (1.5 mol) of sodium chloroacetate, and the reaction temperature was controlled at 60 to 80℃and the reaction time was stirred for 3 hours. And (3) dropwise adding 300g of 20% NaOH solution in the reaction process, adjusting the pH value to 8-10, continuing to react for 2 hours after the dropwise adding is completed, cooling to normal temperature, adjusting the pH value to be neutral by hydrochloric acid, standing for 2 hours for layering, removing bottom salt and brine, and decompressing to remove part of organic solvent to obtain the organosilicon surfactant solution. Wherein the effective component amount of the organic silicon surfactant is 75%.
Example 2: synthesis of sodium octadecyl-N-hydroxypropyl-propoxy-poly (6) siloxane-N-ethanesulfonate surfactant (m=5, n=0)
Octadecylamine 135g (0.5 mol) and 200mL isopropyl alcohol are added into a 2000mL reaction vessel, the temperature is raised to 50-70 ℃ by stirring, 293g (0.525 mol) of epoxy poly (6) siloxane (m=5, n=0) is slowly added dropwise into the reaction vessel for 3h, and stirring is continued for 2h after the completion of the dropwise addition.
To the above product was added 1.82g (0.005 mol) of cetyltrimethylammonium bromide as a phase transfer catalyst, 125g (0.75 mol) of sodium chloroethyl sulfonate, and the reaction temperature was controlled at 60 to 80℃and the dropwise addition time was 4 hours. 200g of 25% KOH solution is dripped in the reaction process, the pH is regulated to 8-10, the reaction is continued for 2 hours after the dripping is completed, the temperature is reduced to normal temperature, the pH is regulated to be neutral by hydrochloric acid, the reaction is kept stand for 2 hours for layering, the bottom salt and the salt water are removed, and part of organic solvent is removed under reduced pressure, so that the organosilicon surfactant solution is obtained. Wherein the effective component amount of the organic silicon surfactant is 75%.
Example 3: synthesis of sodium tallow-N-hydroxypropyl-propoxy-poly (12) siloxane-N-hydroxypropyl sulfonate surfactant (m=6, n=5)
135g (0.5 mol) of tallow amine and 400mL of absolute ethyl alcohol are added into a 2000mL reaction vessel, the temperature is raised to 50-70 ℃ by stirring, 500g (0.5 mol) of epoxy poly (12) siloxane (m=6, n=5) is slowly added into the reaction vessel in a dropwise manner for 5h, and stirring is continued for 2h after the dropwise addition is completed.
To the above product was added 1.82g (0.005 mol) of cetyltrimethylammonium bromide as a phase transfer catalyst, 118g (0.6 mol) of sodium 3-chloro-2-hydroxypropanesulfonate as a reaction temperature was controlled at 60 to 80℃and the addition time was 5 hours. 150g of 7% ammonia water solution is added dropwise in the reaction process, and the pH is adjusted to be 8-10. And after the dripping is finished, continuing to react for 2 hours, cooling to normal temperature, regulating the pH value to be neutral by hydrochloric acid, standing for 2 hours for layering, removing bottom salt and salt water, and decompressing to remove part of the organic solvent to obtain the organosilicon surfactant solution. Wherein the effective component amount of the organic silicon surfactant is 75%.
Example 4: synthesis of Di-rosin-N-hydroxypropyl-propoxy-poly (9) siloxane-N-sodium diacetate surfactant (m=6, n=2)
93g (0.5 mol) of rosin amine and 250mL of isopropanol are added into a 2000mL reaction vessel, the temperature is raised to 50-70 ℃ by stirring, 410g (0.525 mol) of epoxy poly (9) siloxane (m=6, n=2) is slowly added dropwise into the reaction vessel for 3h, and stirring is continued for 2h after the completion of the dropwise addition.
To the above product was added 1.82g (0.005 mol) of cetyltrimethylammonium bromide as a phase transfer catalyst, 87.5g (0.75 mol) of sodium chloroacetate, and the reaction temperature was controlled at 60 to 80℃and the dropwise addition time was 3 hours. 150g of 20% NaOH solution is dripped in the reaction process, and the pH is adjusted to be 8-10. And after the dripping is finished, continuing to react for 2 hours, cooling to normal temperature, regulating the pH value to be neutral by hydrochloric acid, standing for 2 hours for layering, removing bottom salt and salt water, and decompressing to remove part of the organic solvent to obtain the organosilicon surfactant solution. Wherein the effective component amount of the organic silicon surfactant is 75%.
Performance test-surface tension test
The organosilicon surfactant (75% content) synthesized in examples 1-4 was prepared into a solution with a certain concentration by tap water, and the surface tension was measured by JYW-200D full-automatic interfacial tensiometer, and the measurement results are shown in Table 1:
table 1 surface tension units of silicone surfactant: mN/m
As can be seen by combining the data in Table 1, examples 1-4 are all less than 28mN/m in the range of 0.01% -0.3%, and are superior to the technical indexes of the surface tension (0.3%) of < 28mN/m in the enterprise standard Q/SH1020 2252-2019 "surfactant technical requirement for depressurization and injection increase", of the Ministry of petroleum of China petrochemicals, inc. The organic silicon surfactant provided by the invention has higher surface activity at a lower concentration, can effectively reduce the surface tension, and can be diluted to 1/10-1/15 of the concentration of a sample for use.
Performance test-interfacial tension test
The organic silicon surfactant provided by the invention can be directly used as a surfactant for pressure reduction and injection increase and oil displacement, but is preferably compounded for use in consideration of cost factors and surface properties of the organic silicon surfactant.
The silicone surfactant solutions synthesized in examples 1-4 were compounded with 6501 surfactant (mass ratio 1:4), and the compounded samples were numbered according to the order of examples, wherein the silicone surfactant solution (active ingredient 75%) was 10%,6501 surfactant 40%, methanol 20%, and the balance was water.
The 6501 surfactant employed in examples 1-4 is a commercially available, conventional diethanolamine coconut acid to diethanolamine composition having a 1:1.5 ratio of coconut acid to diethanolamine, and the surfactant capable of being formulated with the present invention is not limited to diethanolamine coconut acid amide.
Preparing 0.1% -0.3% compound sample solution by using water (total mineralization degree 8207 mg/L) extracted from a certain block of a victory oil field, dehydrating crude oil by using a certain block of the victory oil field, testing the interfacial tension of the compound sample by using a TX-500C interfacial tension meter under the condition of 70 ℃ and 5000r/min, and testing the surface tension of the compound sample by using a JYW-200D full-automatic interfacial tension meter under the condition of 25 ℃, wherein the reference value of the interfacial tension is less than 0.1mN/m, namely 10 -2 An order of magnitude; the reference value of the surface tension is less than or equal to 28mN/m, and the test result is shown in Table 2:
TABLE 2 interfacial tension and surface tension of organosilicon surfactant complex samples
Interfacial tension unit: 10 -3 mN/m, surface tension unit: mN/m
Note that: the composition of the blank sample was: 6501 surfactant 50%, methanol 20% and water the rest.
As can be seen from the data in Table 2, the interfacial tension of the organosilicon surfactant compound sample provided by the invention is as low as 10 in the concentration range of 0.1% -0.3% -3 The mN/m order of magnitude is superior to the technical index of the Chinese petrochemical group winning Petroleum administration company enterprise standard Q/SH1020 2252-2019 'technical requirement for surfactant for pressure reduction and injection increase' (0.3%) which is less than or equal to 0.1mN/m, and is also superior to the interfacial tension of blank samples. The surface tension of the compounded samples at 0.1% -0.3% concentration was better than the 0.01% -0.3% concentration level of the silicone surfactant alone samples of examples 1-4. Therefore, the organosilicon surfactant is compounded into the sample, so that the surface tension is effectively reduced, the interfacial tension is obviously reduced, and the interfacial performance is greatly improved. Therefore, the organic silicon surfactant and the compound sample provided by the invention not only can realize the effects of reducing pressure and increasing injection, but also can improve the oil displacement efficiency, and the organic silicon surfactant has the advantages of structure and performance in the fields of reducing pressure and increasing injection and oil displacement.

Claims (9)

1. The organosilicon group-containing surfactant for reducing pressure and increasing injection is characterized by having the structural formula (1):
(1)
Wherein m is an integer of 2-11, n is an integer of 0-9, and m+n is an integer of 2-11;
R 1 selected from linear alkanes of C8-C20 carbon chain lengthAt least one of a base, a cocoyl, a tallow base, a rosin base; r is R 2 At least one of sodium acetate, sodium ethylsulfonate and sodium hydroxy propane sulfonate;
the obtained organosilicon group-containing surfactant for depressurization and injection increase is applied to the produced water of a certain block of the victory oil field with the total mineralization degree of 8207 mg/L.
2. The preparation method of the surfactant for depressurization and injection increase containing the organosilicon group, which is disclosed in claim 1, is characterized in that the surfactant is prepared by adopting a ring opening reaction of organic primary amine and single-end epoxy polysiloxane and then reacting with halogenated alkyl carboxylate or halogenated alkyl sulfonate, and specifically comprises the following two steps:
adding 1.0mol of organic primary amine and a certain amount of organic solvent into a three-port reaction container, stirring and heating to 50-70 ℃, slowly dropwise adding 1.0-1.1mol of single-end epoxy polysiloxane, dropwise adding for 2-4 hours, and continuing stirring and reacting for 2-4 hours to prepare an organosilicon surfactant intermediate product;
adding 0.01mol of phase transfer catalyst cetyl trimethyl ammonium bromide into the intermediate product, adding 1.2-1.5mol of halogenated alkyl carboxylic acid or sulfonate, stirring at 60-80 ℃ for 3-5h, dropwise adding an alkali solution in the reaction process to adjust the pH value to 8-10, continuing to react for 2-4h after the dropwise adding is finished, cooling to normal temperature, adjusting the pH value to be neutral by hydrochloric acid, standing for layering, removing bottom salt and salt water, and removing part of organic solvent under reduced pressure to obtain the organosilicon surfactant solution.
3. The preparation method according to claim 2, wherein the single-ended epoxy polysiloxane is at least one selected from linear epoxy silicone oil or side-chain epoxy silicone oil having a polymerization degree of 3 to 12, and has a structural formula of the following formula (2):
(2)
Wherein m is an integer of 2 to 11, n is an integer of 0 to 9, and m+n is an integer of 2 to 11.
4. The method of claim 2, wherein the molar ratio of organic primary amine to single-ended epoxy polysiloxane added is 1: (1.0-1.1) the molar ratio of organic primary amine added to haloalkylcarboxylic acid or sulfonate is 1: (1.2-1.5);
the molar ratio of the added alkali to the halogenated alkyl carboxylic acid or sulfonate is 1:1, and the volume ratio of the added alkali solution to the organic solvent is 1:3-2:3.
5. The method according to claim 2, wherein the organic primary amine is at least one selected from the group consisting of linear fatty alkylamines of C8 to C20 carbon chain lengths, cocoamines, tallow amines and rosin amines; the organic solvent is at least one selected from anhydrous ethanol and isopropanol; the alkali is at least one selected from sodium hydroxide, potassium hydroxide and ammonia water; the halogenated alkyl carboxylic acid or sulfonic acid is at least one selected from sodium chloroacetate, sodium chloroethyl sulfonate, sodium 3-chloro-2-hydroxy propane sulfonate, sodium bromoacetate and sodium bromoethyl sulfonate.
6. The use of the surfactant for depressurization and injection enhancement containing an organosilicon group according to claim 1 in the produced water of a certain block of a victory oil field with a total degree of mineralization of 8207 mg/L.
7. The application of claim 6, wherein the organic silicon group-containing surfactant for reducing pressure and increasing injection and the 6501 surfactant are added in the use, wherein the use concentration of the compound sample is 0.1-0.3%, and the mass ratio of the organic silicon group-containing surfactant for reducing pressure and increasing injection to the 6501 surfactant in the compound sample is 1:4.
8. The use according to claim 7, wherein the interfacial tension of the compounded sample of surfactant for lowering and increasing injection containing organosilicon groups is as low as 10 at 70 ℃ and 5000r/min -3 On the order of mN/m.
9. The use according to claim 7, characterized in that the surface tension of the compounded sample of the surfactant for depressurization and injection increase containing organosilicon groups is < 28mN/m at 25 ℃.
CN202111067743.7A 2021-09-13 2021-09-13 Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof Active CN113620984B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111067743.7A CN113620984B (en) 2021-09-13 2021-09-13 Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111067743.7A CN113620984B (en) 2021-09-13 2021-09-13 Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof

Publications (2)

Publication Number Publication Date
CN113620984A CN113620984A (en) 2021-11-09
CN113620984B true CN113620984B (en) 2024-03-15

Family

ID=78389832

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111067743.7A Active CN113620984B (en) 2021-09-13 2021-09-13 Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof

Country Status (1)

Country Link
CN (1) CN113620984B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114806603B (en) * 2022-05-26 2023-06-09 滁州学院 Novel Si-C organosilicon quaternary ammonium salt surfactant and preparation method thereof

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4093642A (en) * 1976-12-20 1978-06-06 Union Carbide Corporation Surface active silicones

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10780305B2 (en) * 2016-03-18 2020-09-22 Tyco Fire Products Lp Organosiloxane compounds as active ingredients in fluorine free fire suppression foams

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4093642A (en) * 1976-12-20 1978-06-06 Union Carbide Corporation Surface active silicones

Also Published As

Publication number Publication date
CN113620984A (en) 2021-11-09

Similar Documents

Publication Publication Date Title
CN113620984B (en) Organosilicon group-containing surfactant for reducing pressure and increasing injection, preparation method and application thereof
CN102690641B (en) Sulfonate surfactant and preparation method thereof
US12030994B2 (en) Preparation method for and application of modified siloxane-based supercritical carbon dioxide thickener
CN113621357B (en) Carbon dioxide response self-thickening intelligent fluid based on supermolecule self-assembly
CN103965480B (en) A kind of hyperbranched polyorganosiloxane modification diphenyl diimide and its preparation method and application
CN113773342B (en) Gemini surfactant with organic silicon groups connected and preparation method and application thereof
CN109265683B (en) High-branching-degree silicone oil with high viscosity index and good high-temperature resistance, and preparation method and application thereof
CN111718490A (en) Modified block silicone oil containing trace low-ring bodies and preparation method thereof
CN114106315B (en) Preparation method of narrow-distribution triethanolamine block polyether, block polyether and application of block polyether
CN111116916B (en) Method for preparing hydroxyl silicone oil emulsion by using Si-OH end-capped dimethyl siloxane oligomer through emulsion polymerization
CN115197428A (en) Preparation method of modified amino silicone oil
CN117645867A (en) Surfactant composition for improving recovery ratio and preparation method thereof
CN112194797B (en) High-flash-point quaternized polyether block silicone oil and preparation method thereof
CN115093351B (en) Modified betaine type gemini surfactant as well as preparation method and application thereof
CN106835719B (en) A kind of betaine type amphoteric silicone softening agent and preparation method thereof
CN111533664A (en) Ester-based polyether betaine surfactant and synthesis method thereof
CN111088012B (en) Composite surfactant for improving crude oil recovery efficiency and preparation method and application thereof
CN111073622B (en) Surfactant composition for improving recovery ratio and preparation method and application thereof
CN111088011B (en) Composite surfactant for improving crude oil recovery ratio and preparation method and application thereof
CN105419765B (en) A kind of glycosyl the moon nand-type surfactant and preparation method thereof
CN108854840B (en) Preparation method of polyquaternium surfactant containing amide connecting chain
CN109825276A (en) A kind of aqueous fracturing fluid composition and aqueous fracturing fluid
US20220186107A1 (en) Thickener for wellbore acid treatment liquid and wellbore acid treatment liquid using same
KR101187307B1 (en) Method of preparing cationic surfactant having good solubility
CN114181689A (en) High-temperature-resistant composite emulsion viscosity-reducing system and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant