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CN106633103A - Preparation method of high-internal-phase-viscosity polysiloxane emulsion - Google Patents

Preparation method of high-internal-phase-viscosity polysiloxane emulsion Download PDF

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Publication number
CN106633103A
CN106633103A CN201611255953.8A CN201611255953A CN106633103A CN 106633103 A CN106633103 A CN 106633103A CN 201611255953 A CN201611255953 A CN 201611255953A CN 106633103 A CN106633103 A CN 106633103A
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preparation
internal phase
polysiloxane emulsion
high internal
emulsion
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CN106633103B (en
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姜宇嵘
龙娇秀
黄素萄
伞振鑫
武丽美
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Jiangxi Bluestar Xinghuo Silicone Co Ltd
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Jiangxi Bluestar Xinghuo Silicone Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/03Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L83/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
    • C08L83/04Polysiloxanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L83/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
    • C08L83/04Polysiloxanes
    • C08L83/06Polysiloxanes containing silicon bound to oxygen-containing groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2383/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen, or carbon only; Derivatives of such polymers
    • C08J2383/04Polysiloxanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2383/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen, or carbon only; Derivatives of such polymers
    • C08J2383/04Polysiloxanes
    • C08J2383/06Polysiloxanes containing silicon bound to oxygen-containing groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2471/00Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
    • C08J2471/02Polyalkylene oxides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2483/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen, or carbon only; Derivatives of such polymers
    • C08J2483/04Polysiloxanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Colloid Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Cosmetics (AREA)

Abstract

The invention discloses a method of preparing high-internal-phase-viscosity polysiloxane emulsion through a high-effective shear emulsifying mechanical device. The method is simple and high-effective and is convenient to carry out. The polysiloxane emulsion has excellent stability and excellent application performance. The emulsion can be used in the fields of household and personal care, and is free of roll sticking, demulsification and oil floating during a post-finishing process of fabrics and leather.

Description

A kind of preparation method of the polysiloxane emulsion of high internal phase viscosities
Technical field
The present invention relates to a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities, belongs to chemical products field.
Background technology
Organopolysiloxane due to fabulous chemical stability, heat resistance, hydrophobicity and relatively low surface tension with And good biocompatibility so that it is widely used.But due to the hydrophobicity of silicone oil it is very strong, it is difficult to be dispersed in water In system.And the appearance of organic silicon emulsion solves this problem, it is widely used in the form of an emulsion spinning more than current silicone oil The sides such as weaver's industry, plastic processing, papermaking, finishing agent, defoamer, releasing agent, building surface waterproofing, cosmetics and ink formulations Face.
Using Mechanical Method prepare organic silicon emulsion be silicone oil is dispersed under strong mechanical shearing effect it is tiny micro- Grain is used as dispersion phase, and emulsifying agent forms one layer of molecular interface film with certain mechanical strength on the interface of water and oil, with Enable that oil phase particulate is stable to be dispersed in water phase, be difficult aggregation and become big and be layered, so as to obtain water oil uniformly emulsion.For many years Come, have been used up high pressure homogenizer, colloid mill and high-efficient homogeneous vacuum emulsifying machine next life galactopoiesis liquid.Patent US2755194, US4784844, US530028 to be referred to and can be readily available the relatively low emulsion of internal phase viscosities by the said equipment.But but it is difficult water In being added to viscous silicone fluid, and while give emulsion of enough emulsification pretreatments into high stability.
It is silicon rubber that patent CN100500742C is mentioned by preparing interior phase with double screw extruder, silane elastomer, The oil-in-water emulsions such as organic siliconresin.But this kind of method can only prepare the emulsion that interior phase is silane elastomer class.
The content of the invention
It is an object of the invention to provide a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities, by a kind of machinery The method of conversion is prepared for the organic silicon emulsion of high internal phase viscosities, compared with other conventional arts, organosilicon prepared by the method Emulsion has more high stability, there is provided the interior phase organosiloxane of higher molecular weight, and the more excellent property of product is imparted in application Energy.
A kind of preparation method of the polysiloxane emulsion of high internal phase viscosities, concretely comprises the following steps:
(1)The component of following parts by weight is added in high-efficient shear emulsifying equipment at 20-30 DEG C of temperature and normal pressure:
The silicone oil of 30-80 parts, the emulsifying agent of 1-10 parts, the purified water of 0.5-20 parts, after mixing in high-efficient shear emulsifying equipment Mixture is applied shearing force 60-300min to emulsify;
(2)Add purified water, assistant for emulsifying agent, bactericide, PH conditioning agents and finally give oil-in-water emulsion.
The step(1)In silicone oil represent for following structural formula:
Wherein, R2For methyl, R1For methyl or hydroxyl, R3For methyl, aminoethylaminopropyl, phenyl, alkyl or silicon hydrogen, m and n is each From for positive integer or 0.
The step(1)In silicon oil viscosity be from 5000mpa s to 1000000mpa s.
The step(1)In silicone oil be made up of one or more silicone oil, such as various, need first be well mixed oil phase Afterwards, then next step operation is carried out.
The step(1)In silicone oil be preferably polydimethyl siloxane fluid, hydroxyl polydimethyl siloxane fluid, amido silicon oil.
The step(1)In emulsifying agent be anion, cation, nonionic, amphoteric surfactant in one kind or Several, in the C8-C15 alkylation APEOs of preferred nonionic compounds of one or more.
The step(1)The homogeneous oil phase viscosity obtained after emulsification is from 50000mpa s to 1000000mpa s.
Described step(2)In assistant for emulsifying agent be anion surfactant, cationic surfactant, nonionic table One or more in the activating agent of face, preferably anionic emulsifier.
Described step(2)In bactericide be preferably methylisothiozoline, methyl chloride isothiazoline or diformazan hydantoins.
Described step(2)In PH conditioning agents be weak acid or weak base, preferably triethanolamine or acetic acid.
Described high-efficient shear emulsifying equipment can be EKATO KOAX equipment.
It is an advantage of the current invention that:The emulsion prepared by this kind of method not only has excellent stability, size tunable, Narrowly distributing, and preparation process is simple, reproducible, easy to operate, quick, the oil-in-water emulsion of preparation has compared with stiff stability, Room temperature storage is more than 12 months, and 50 DEG C are more than 30 days.The silicone oil good film-forming property of high internal phase viscosities, while giving smooth soft hand Sense, this product is all widely used in personal care product, coating products, household care products or leather product.
The difference of the present invention and other patented methods
This patent Screw extruder technique Super-pressure emulsion polymerization technique Anionic polymerization process
Pressure Normal pressure Micro-vacuum >1Mpa Normal pressure
Temperature 20-30℃ 60℃ 10-50℃ 85℃
Particle diameter >5um 0.3 um 0.4 um <0.5 um
Internal phase viscosities 50,000-1,000,000 mpa•s 1,000,000,000 mpa•s 300,000 mpa•s 113,000 mpa•s
As can be seen from the above table, at the present invention is using temperature 20-30 DEG C and condition of normal pressure, it is possible to prepare the emulsion and produce Product, and additive method must react under high temperature or condition of high voltage, it is seen that present invention reaction is gentle, the oil-in-water emulsion of preparation Also have compared with stiff stability.
Specific embodiment
To more fully understand the present invention, technical scheme is described in detail with specific embodiment below, but this Invention is not limited to this.
Embodiment 1
The hydroxy silicon oil of 45 parts of 550,000mpas, 4 parts of alkylation APEOs, 2 parts of purified waters are added into efficiently shearing breast In change equipment, temperature is 20~300C, under normal pressure after stirring and emulsifying 150min, adds 1 part of lauryl sodium sulfate, methyl chloride different Final product emulsion is obtained after thiazolinone, acetic acid and 48 parts of purified waters.
Embodiment 2
High-efficient shear emulsifying is added to set the dimethicone of 5 parts of 5000mpas, the hydroxy silicon oil of 40 parts of 550,000mpas In standby, whole system is well mixed after uniform stirring, adds 4 parts of alkylation APEOs, 2 parts of purified waters, and temperature is 20~ 300C, under normal pressure after stirring and emulsifying 120min, 1 part of lauryl sodium sulfate of addition, methylchloroisothiazandnone, acetic acid and 48 parts Final product emulsion is obtained after purified water.
Embodiment 3
The dimethicone of 45 parts of 60,000mpas is added in high-efficient shear emulsifying equipment, 4 parts of alkylation polyoxy second are added Alkene ether and 2 parts of purified waters, temperature is 20~300C, stirs after 180min under normal pressure, adds 1 part of lauryl sodium sulfate, methyl Final emulsion is obtained after OIT, acetic acid and 48 parts of purified water.
Embodiment 4
45 parts of 80,000mpas hydroxy silicon oils are added in high-efficient shear emulsifying equipment, 4 parts of emulsifying agents of addition, 2 parts of purified waters, Temperature is 20~300C, stirs after 180min under normal pressure, adds 1 part of sldium lauryl sulfate, methylisothiazolinone, acetic acid and 38 Final emulsion is obtained after the purified water of part.
If table 1 below is the test result of organic silicon emulsion
The present invention is as follows to the method for testing of every physicochemical property of the organic silicon emulsion for preparing:
Dewatering ability:Emulsion 20ml, a is added to be put into centrifuge in 20ml centrifuge tubes, 3000rpm rotation speed operations 30min Afterwards, sample is observed without layering, belong to steady quality.
Heat endurance:Emulsion is put into vial with cover, 50 are put into0In the constant temperature oven of C after 30 days, sample without point Layer, without demulsifying phenomenon, belong to steady quality.
Storage stability:By emulsion(It is with cover)After placing 12 months at room temperature, without breakdown of emulsion, without lamination, belong to quality It is stable.
Stability towards electrolytes:By 15g emulsions, 20gNaCl, 80g H2O is added in beaker, 500rpm rotation speed operations 10min, after standing 24h, sample breakdown of emulsion, without lamination belongs to steady quality.

Claims (10)

1. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities, it is characterized by:Concretely comprise the following steps:
(1)The component of following parts by weight is added in high-efficient shear emulsifying equipment at 20-30 DEG C of temperature and normal pressure:
The silicone oil of 30-80 parts, the emulsifying agent of 1-10 parts, the purified water of 0.5-20 parts, after mixing in high-efficient shear emulsifying equipment Mixture is applied shearing force 60-300min to emulsify;
(2)Add purified water, assistant for emulsifying agent, bactericide, PH conditioning agents and finally give oil-in-water emulsion.
2. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:Step (1)In silicone oil represent for following structural formula:
Wherein, R2For methyl, R1For methyl or hydroxyl, R3For methyl, aminoethylaminopropyl, phenyl, alkyl or silicon hydrogen, m and n is each From for positive integer or 0.
3. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:The step Suddenly(1)In silicon oil viscosity be from 5000mpa s to 1000000mpa s.
4. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:The step Suddenly(1)In silicone oil be made up of one or more silicone oil, such as various, after needing first be well mixed oil phase, then carry out next step Operation.
5. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:The step Suddenly(1)In silicone oil be preferably polydimethyl siloxane fluid, hydroxyl polydimethyl siloxane fluid, amido silicon oil.
6. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:The step Suddenly(1)In emulsifying agent be anion, cation, nonionic, amphoteric surfactant in one or more, preferred nonionic The compound of one or more in the C8-C15 alkylation APEOs of type.
7. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:The step Suddenly(1)The homogeneous oil phase viscosity obtained after emulsification is from 50000mpa s to 1000000mpa s.
8. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:Described Step(2)In assistant for emulsifying agent be anion surfactant, cationic surfactant, nonionic surfactant in one Plant or several, preferably anionic emulsifier.
9. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:Described Step(2)In bactericide be preferably methylisothiozoline, methyl chloride isothiazoline or diformazan hydantoins.
10. a kind of preparation method of the polysiloxane emulsion of high internal phase viscosities as claimed in claim 1, it is characterized by:It is described The step of(2)In PH conditioning agents be weak acid or weak base, preferably triethanolamine or acetic acid.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110403853A (en) * 2019-09-06 2019-11-05 广州宏翼新材料有限公司 A kind of novel polymeric silicone oil emulsion and preparation method
CN110922891A (en) * 2019-12-17 2020-03-27 山东易石环保新材料有限公司 Emulsion type silicone paper machine drying cylinder stripping agent and preparation method thereof
CN110964436A (en) * 2019-12-17 2020-04-07 山东易石环保新材料有限公司 Organic silicon emulsion type paper machine dry net stripping agent and preparation method thereof
CN113214498A (en) * 2021-04-29 2021-08-06 南京威尔生物科技有限公司 Preparation method of emulsified silicone oil with high viscosity and good stability

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EP0463431A2 (en) * 1990-06-07 1992-01-02 Dow Corning Corporation Process for making polysiloxane emulsions
CN1711305A (en) * 2002-11-14 2005-12-21 瓦克化学有限公司 Highly concentrated oil-in-water silicone emulsions
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CN101130634A (en) * 2007-08-08 2008-02-27 浙江大学 Amino silicone oil microemulsion with high solid content and preparation method thereof
CN105199395A (en) * 2015-09-28 2015-12-30 江苏惠丰润滑材料股份有限公司 Organosilicon waterborne emulsion and preparation method thereof

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EP0463431A2 (en) * 1990-06-07 1992-01-02 Dow Corning Corporation Process for making polysiloxane emulsions
CN1711305A (en) * 2002-11-14 2005-12-21 瓦克化学有限公司 Highly concentrated oil-in-water silicone emulsions
CN101080440A (en) * 2004-12-15 2007-11-28 瓦克化学股份公司 Manufacturation of stable polysiloxane emulsion
CN101130634A (en) * 2007-08-08 2008-02-27 浙江大学 Amino silicone oil microemulsion with high solid content and preparation method thereof
CN105199395A (en) * 2015-09-28 2015-12-30 江苏惠丰润滑材料股份有限公司 Organosilicon waterborne emulsion and preparation method thereof

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110403853A (en) * 2019-09-06 2019-11-05 广州宏翼新材料有限公司 A kind of novel polymeric silicone oil emulsion and preparation method
CN110922891A (en) * 2019-12-17 2020-03-27 山东易石环保新材料有限公司 Emulsion type silicone paper machine drying cylinder stripping agent and preparation method thereof
CN110964436A (en) * 2019-12-17 2020-04-07 山东易石环保新材料有限公司 Organic silicon emulsion type paper machine dry net stripping agent and preparation method thereof
CN113214498A (en) * 2021-04-29 2021-08-06 南京威尔生物科技有限公司 Preparation method of emulsified silicone oil with high viscosity and good stability

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