CN1546542A - Method for preparing organic silicon modified polyacrylic acid (polyacrylate) emulsion - Google Patents

Method for preparing organic silicon modified polyacrylic acid (polyacrylate) emulsion Download PDF

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CN1546542A
CN1546542A CNA2003101168016A CN200310116801A CN1546542A CN 1546542 A CN1546542 A CN 1546542A CN A2003101168016 A CNA2003101168016 A CN A2003101168016A CN 200310116801 A CN200310116801 A CN 200310116801A CN 1546542 A CN1546542 A CN 1546542A
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monomer
emulsion
vinyl
vinyl monomer
polymerization
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CN1264884C (en
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王俊卿
曾汉民
洪星
蔡国衡
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Guangdong Hongchang Chemical Co ltd
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HONGCHANG CHEMICAL CO Ltd SHUNDE
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Abstract

The invention discloses a process for preparing organic silicon modified polyacrylic acid (polyacrylate) emulsion with high organic silicon content (15%-25%), wherein the ring-opening polymerization of epoxy silane is carried out simultaneously with the free radical polymerization of vinyl monomer, i.e., (1) ring-opening polymerization occurs to epoxy silane at the presence of catalyst, and organic (ring) siloxane containing unsaturated bonds polycondensation is carried out, thus producing organosilicon resin and organosilicon resin containing unsaturated double bonds, (2) at the presence of initiating agent, the free radical polymerization of vinyl monomer is carried out, and in-situ graft polymerization of organosilicon resin containing unsaturated bonds is carried out to prepare organic silicon-g polyacrylic acid (ester) grafted copolymer (as compatiblizing agent).

Description

The preparation method of a kind of organic-silicon-modified polyacrylic acid (ester) emulsion
Technical field
The present invention relates to the preparation method of a kind of organic-silicon-modified polyacrylic acid (ester) emulsion (hereinafter to be referred as organosilicon crylic acid latex), the preparation method of the organosilicon crylic acid latex of particularly high organosilicon content (15%~25%).
Background technology
Vinylformic acid (ester) cold coating is 20th century coating new variety that grow up of the fifties.It has following advantage: look shallow, the transparency is fabulous, nondiscoloration, acidproof alkali salt, grease resistance etc.But also there are some shortcomings: as easy loss of gloss, low-temperature flexibility is relatively poor, water-permeable is more high.In order to remedy these shortcomings on vinylformic acid (ester) resin property, generally to carry out modification to vinylformic acid (ester) resin, the modification technology of vinylformic acid (ester) resin is main relevant with organosilicon.Coating is main chain with Si-O-Si with silicone resin, because the bond energy of Si-O key is greater than the bond energy of C-C key in the common organic polymer, therefore silicone resin has good thermotolerance, anti-ozone, resistance to UV aging, and, because surface tension is little, water and other pollutent are difficult for adhering to, so silicone resin has good moistureproofness, water resisting property and anti-steam etc.Have more excellent weathering resistance, gloss retention, resistance to chalking, anti-stain characteristic etc. through organic-silicon-modified vinylformic acid (ester) cold coating than unmodified vinylformic acid (ester) cold coating, be suitable for as the outdoor decoration building coating.
Prepare organic-silicon-modified polyacrylic acid (ester) emulsion, mainly be divided into cold spelling and chemical method.Cold spelling is simple to operate, is separated but be easy to generate two, and storage period is short.Chemical method generally is to carry out emulsion copolymerization with the organo-siloxane monomer and vinylformic acid (ester) monomer that contain vinyl group, but this siloxanes facile hydrolysis, influenced organosilyl activity, particularly when organic silicone content is big, can in emulsion polymerization process, produce a large amount of condensation products (even whole gelling), reaction can't be proceeded.Chemical method prepares another approach of organosilicon crylic acid latex, and when the silicone resin of band functional group existed, vinylformic acid (ester) monomer carried out letex polymerization, but the emulsion uniformity that this method obtains is poor.
Organosilicon content is less than 15% in organosilicon crylic acid latex, perhaps during the uniformity difference of emulsion and emulsion particle, organosilicon crylic acid latex can not represent its due various over-all propertieies well, so the synthetic relatively research topic of hot topic that remains now of organosilicon crylic acid latex: main research direction is organosilicon crylic acid latex preparation technology's the exploration preferably of high organosilicon content, uniformity.
Summary of the invention
The object of the present invention is to provide a kind of novel process of organosilicon crylic acid latex of synthetic high organosilicon content (15%~25%).
The preparation method of a kind of organic-silicon-modified polyacrylic acid of the present invention (ester) emulsion is a major ingredient with organosilane monomer and vinyl monomer, it is characterized in that preparation process may further comprise the steps successively:
(1) pre-emulsification: emulsifying agent, water soluble starter and catalyzer are put in the deionized water, after treating to dissolve fully, are added and be dissolved with oil-soluble initiator and auxiliary agent and organosilane monomer that mixes and vinyl monomer, stir pre-emulsion;
(2) polyreaction: emulsifying agent is put in the deionized water, add water soluble starter and catalyzer, after the dissolving, logical nitrogen 20 minutes is warmed up to 70~80 ℃ fully, began to drip pre-emulsion 2~5 hours, after being added dropwise to complete, being warming up to 85~100 ℃ and continuing reaction 2~5 hours, be cooled to 40 ℃, regulate pH to 7~8, filter;
Wherein organosilane monomer is epoxy silane and contains the monomeric mixture of vinyl organosilicon.
Described epoxy silane is an octamethylcyclotetrasiloxane, contains the vinyl organosilicon monomer and be in tetramethyl-tetrem thiazolinyl cyclotetrasiloxane, gamma-methyl allyl acyloxypropyl trimethoxysilane, vinyltriethoxysilane, the vinyltriethoxysilane one or more.
Described vinyl monomer is methacrylic acid and (C thereof 1~C 10) alcohol ester, vinylformic acid and (C thereof 1~C 10) in the alcohol ester, vinylbenzene one or more.
The weight ratio of used organosilane monomer and vinyl monomer is 2~30/98~70, is preferably 5~25/95~75.
Described emulsifying agent is the moon/nonionic compound emulsifier, and the ratio of the moon/nonionic emulsifying agent is 1: 0.25~5, and total consumption is 0.5~7% (accounting for the polymerization single polymerization monomer weight percent), and wherein the consumption of pre-emulsion process is 3/4~1/3 of whole consumptions.
Preferred, emulsifying agent is 2~4 kinds in Sodium dodecylbenzene sulfonate, sodium lauryl sulphate, sodium laurylsulfonate, polyoxyethylene nonyl phenyl Vinyl Ether, ethoxylated alkylphenol ammonium sulfate, the octylphenol polyethylene ethylene oxide ether.
Described water soluble starter is one or both of Potassium Persulphate, ammonium persulphate; Oil-soluble initiator is one or both in benzoyl peroxide, the Diisopropyl azodicarboxylate, total consumption is 0.3~1.5% (accounting for the weight percent of vinyl monomer), wherein oil-soluble initiator accounts for 0~50% of total consumption, and the consumption of pre-emulsion process is 3/4~1/3 of whole consumptions.
Described auxiliary agent is one or more in n-Hexadecane, cetyl alcohol, 1-amylalcohol, the polymethyl acrylate, and the total consumption of auxiliary agent is 0~5% (accounting for the polymerization single polymerization monomer weight percent).
The present invention is the preparation method of a kind of organic-silicon-modified polyacrylic acid (ester) emulsion, its polyreaction is undertaken by micro-emulsion polymerization mechanism, the ring-opening polymerization of epoxy silane and the radical polymerization of vinyl monomer is simultaneously carried out synchronously, that is: (1) ring-opening polymerization: epoxy silane ring-opening polymerization under the effect of catalyzer, with organic (ring) siloxanes polycondensation that contains unsaturated double-bond, generate silicone resin and the silicone resin that contains unsaturated link(age) simultaneously.(2) free-radical polymerized: under the initiator effect, radical polymerizable vinyl monomer, and and contain the silicone resin generation in-situ grafting polymerization of unsaturated link(age), generate organosilicon-g-polyacrylic acid (ester) graft copolymer (making compatilizer).
Characteristics of the present invention are: (1) has consistency preferably for making silicone resin and polymers of vinyl monomers, introduces unsaturated link(age) in the silicone resin molecular chain.When vinyl monomer generation Raolical polymerizable, just can with the organosilicon polymer generation in-situ grafting polymerization that contains unsaturated link(age), organosilicon-g-polyacrylic acid (ester) the graft copolymerization deposits yields of some amount is arranged.Graft copolymer is as compatilizer, thereby can improve the consistency of silicone resin and vinyl polymer.(2) adopt the micro-emulsion polymerization technology, reduce the diffusive migration of vinyl monomer in polymerization process to greatest extent, thereby polyreaction is occurred in the specific polymerization place (drop).Like this, because the generation of organosilicon-g-polyacrylic acid (ester) graft copolymer in specific polymerization place and the polymerization process, can obtain silicone resin and vinyl polymer intimate mixing and consistency latex particle preferably, therefore, emulsion has fabulous stably dispersing performance.(3) epoxy silane, the ring-opening polymerization of organic (ring) siloxanes that contains unsaturated link(age) and polycondensation and the monomeric radical polymerization of vinylformic acid (ester) class are carried out synchronously, this helps the uniformity in emulsion and the emulsion particle on the one hand, can simplify preparation technology on the other hand, shorten the production time, reduce cost.
Adopt the technology of the present invention to prepare organosilicon crylic acid latex in a word, there is not the uneven problem of emulsion system in the problem that does not exist silicone resin latex particle and vinyl polymer latex particle to be separated in polyreaction yet.Organosilicon content is 15%~25% in the emulsion, and solid content is greater than 40%.Filming of emulsion has very strong hydrophobicity.This synthesis route is simple and direct, be easy to control, production cost is lower, so the present invention has actual application prospect.
Embodiment
In order to illustrate that better the present invention, spy enumerate following embodiment, but the present invention is not limited in following embodiment.
Embodiment 1:
1) pre-emulsification: with the 0.8g sodium lauryl sulphate, 1.2g polyoxyethylene nonyl phenyl vinyl ether (OP-10), 1.0g ethoxylated alkylphenol ammonium sulfate (RHODAPEX CO-436,58%), 0.25g Potassium Persulphate, 0.4g Witco 1298 Soft Acid is dissolved in the 130.0g deionized water, after stirring, with the 48.5g butyl acrylate, 48.5g methyl methacrylate, 1.5g vinylformic acid, 2.0g N hydroxymethyl acrylamide, 5.0g vinylformic acid α-hydroxypropyl acrylate, 18.5g octamethylcyclotetrasiloxane, 1.3g gamma-methyl allyl acyloxypropyl trimethoxysilane, 1.5g the mixture of cetyl alcohol adds, and stirs to such an extent that pre-emulsion is stand-by.
2) organosilicon crylic acid latex is synthetic: in the reaction flask that disposes thermometer, agitator, reflux exchanger and dropping funnel, 0.5g sodium lauryl sulphate, 0.6g polyoxyethylene nonyl phenyl vinyl ether (OP-10), 0.5g ethoxylated alkylphenol ammonium sulfate (RHODAPEX CO-436), 0.3g Potassium Persulphate, 0.3g Witco 1298 Soft Acid are added in the 50g deionized water, stir, logical nitrogen is warmed up to 80 ℃ after 20 minutes, begin to drip pre-emulsion, drip in 3 hours, insulation is warmed up to 85 ℃ of reactions 3 hours after half an hour.Be cooled to 40 ℃, regulate pH to 7, filter.Can make solid content is 41.1%, the latex product of viscosity 12 seconds (being coated with-4 glasss).Emulsion is coated on the sheet glass, drying at room temperature 2 hours, what get final product transparently films.
The technological process of embodiment 2~5 is identical with example one, and raw material add-on and experimental result are listed in table 1 and the table 2.
Table 1
The raw material add-on Raw material Embodiment 2 Embodiment 3 Embodiment 4 Embodiment 5
Methyl methacrylate (g) ????38.5 ?????39.5 ???61.5 ????31.5
Butyl acrylate (g) ????48.5 ?????46.0 ???36.5 ????42.5
Vinylformic acid (g) ????1.5 ?????1.5 ????1.5 ????1.5
N hydroxymethyl acrylamide (g) ????2.0 ?????3.0 ????4.0 ????2.0
Vinylformic acid α-hydroxypropyl acrylate (g) ????6.0 ?????4.0 ????3.0 ????4.0
Vinylbenzene (g) ????10.0 ?????6.5 ????12.0
Octamethylcyclotetrasiloxane (g) ????18.5 ?????24.5 ???18.5 ????31.5
Tetramethyl-tetrem thiazolinyl cyclotetrasiloxane (g) ?????1.1 ????1.3
Gamma-methyl allyl acyloxypropyl trimethoxysilane (g) ????1.3 ????1.5
Dodecyl sulphate (g) ????1.2 ????0.7
Witco 1298 Soft Acid (g) ?????0.9 ????1.5
Sodium lauryl sulphate (g) ????1.0 ????0.8
Sodium dodecylbenzene sulfonate (g) ?????0.9 ????0.6
Polyoxyethylene nonyl phenyl vinyl ether (OP-10) (g) ????2.0 ?????2.8 ????1.6 ????1.0
Ethoxylated alkylphenol ammonium sulfate (58%) (g) ????1.0 ?????0.6 ????1.5 ????2.5
Potassium Persulphate (g) ????0.42 ?????0.35 ????0.28 ????0.46
Deionized water (g) ????180.0 ?????180.0 ????180.0 ????180.0
Reaction conditions Pre-emulsion drips the time (h) ????3 ?????3 ????3 ????3
The pre-emulsion dropping temperature (℃) ????80 ?????85 ????75 ????80
Polymeric reaction temperature (℃) ????85 ?????90 ????85 ????95
Polymerization reaction time (h) ????3 ?????2.5 ????3.5 ????2
Table 2
Embodiment 1 Embodiment 2 Embodiment 3 Embodiment 4 Embodiment 5
Solid content (%) ????41.1 ????42.1 ????40.7 ????41.8 ????40.3
Gel content (oven dry back) (%) ????0.18 ????0.08 ????0.11 ????0.06 ????0.15
Emulsion particle median size (nm) ????121 ????157 ????187 ?????153 ????146
Organosilicon content (%) ????15.8 ????15.6 ????20.3 ????15.8 ????25.2
The pH value ????7.0 ????7.0 ????7.0 ?????7.0 ????7.0
Viscosity (being coated with-4 glasss/second) ????12.00 ????12.69 ????15.11 ????13.52 ????15.36
Calcium ion stability (5%CaCl 2) By By By By By
Mechanical stability (4000 change) 30min passes through 30min passes through 30min passes through 30min passes through 30min passes through
Freeze-thaw stability (5 ℃) 3 cycle through 3 cycle through 3 cycle through 3 cycle through 3 cycle through
Stability in storage (year) ????0.5 ????0.5 ????0.5 ?????0.5 ????0.5
Dilution stability By By By By By

Claims (9)

1, the preparation method of a kind of organic-silicon-modified polyacrylic acid (ester) emulsion is a major ingredient with organosilane monomer and vinyl monomer, it is characterized in that preparation process may further comprise the steps successively:
(1) pre-emulsification: emulsifying agent, water soluble starter and catalyzer are put in the deionized water, after treating to dissolve fully, are added and be dissolved with oil-soluble initiator and auxiliary agent and organosilane monomer that mixes and vinyl monomer, stir pre-emulsion;
(2) polyreaction: emulsifying agent is put in the deionized water, add water soluble starter and catalyzer, after the dissolving, logical nitrogen 20 minutes is warmed up to 70~80 ℃ fully, began to drip pre-emulsion 2~5 hours, after being added dropwise to complete, being warming up to 85~100 ℃ and continuing reaction 2~5 hours, be cooled to 40 ℃, regulate pH to 7~8, filter;
Wherein organosilane monomer is epoxy silane and contains the monomeric mixture of vinyl organosilicon.
2, according to the described preparation method of claim 1, it is characterized in that described epoxy silane is an octamethylcyclotetrasiloxane, contain the vinyl organosilicon monomer and be in tetramethyl-tetrem thiazolinyl cyclotetrasiloxane, gamma-methyl allyl acyloxypropyl trimethoxysilane, vinyltriethoxysilane, the vinyltriethoxysilane one or more.
Described vinyl monomer is methacrylic acid and (C thereof 1~C 10) alcohol ester, vinylformic acid and (C thereof 1~C 10) in the alcohol ester, vinylbenzene one or more.
3, according to the described preparation method of claim 1, the weight ratio that it is characterized in that organosilane monomer and vinyl monomer is 2~30: 98~70.
4, according to the described preparation method of claim 1, the weight ratio that it is characterized in that organosilane monomer and vinyl monomer is 5~25: 95~75.
5, according to the described preparation method of claim 1, it is characterized in that described emulsifying agent is the moon/nonionic compound emulsifier, the ratio of the moon/nonionic emulsifying agent is 1: 0.25~5, total consumption is 0.5~7% (accounting for the polymerization single polymerization monomer weight percent), and wherein the consumption of pre-emulsion process is 3/4~1/3 of whole consumptions.
6,, it is characterized in that described emulsifying agent is 2~4 kinds in Sodium dodecylbenzene sulfonate, sodium lauryl sulphate, sodium laurylsulfonate, polyoxyethylene nonyl phenyl Vinyl Ether, ethoxylated alkylphenol ammonium sulfate, the octylphenol polyethylene ethylene oxide ether according to the described preparation method of claim 5.
7,, it is characterized in that described water soluble starter is one or both of Potassium Persulphate, ammonium persulphate according to the described preparation method of claim 1; Oil-soluble initiator is one or both in benzoyl peroxide, the Diisopropyl azodicarboxylate, total consumption is 0.3~1.5% (accounting for the weight percent of vinyl monomer), wherein oil-soluble initiator accounts for 0~50% of total consumption, and the consumption of pre-emulsion process is 3/4~1/3 of whole consumptions.
8, according to the described preparation method of claim 1, it is characterized in that described catalyzer is one or more of Witco 1298 Soft Acid, dodecyl sodium sulfonate, dodecyl sulphate, tosic acid, total consumption was 0.5~10% (occupying machine silicon monomer weight percent), and wherein the consumption of pre-emulsion process is 3/4~1/3 of whole consumptions.
9, according to the described preparation method of claim 1, it is characterized in that described auxiliary agent is one or more in n-Hexadecane, cetyl alcohol, 1-amylalcohol, the polymethyl acrylate, the total consumption of auxiliary agent is 0~5% (accounting for the polymerization single polymerization monomer weight percent).
CN 200310116801 2003-11-28 2003-11-28 Method for preparing organic silicon modified polyacrylic acid (polyacrylate) emulsion Expired - Lifetime CN1264884C (en)

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CN1305988C (en) * 2005-09-23 2007-03-21 浙江大学 Prepn of organosilicon modified pressure-sensitive acrylate adhesive
CN100381484C (en) * 2005-03-04 2008-04-16 华东理工大学 Process for preparing core-shell type polysiloxane composite particles
CN1796428B (en) * 2004-12-27 2010-05-05 深圳市海川实业股份有限公司 Method for preparing Silicone acrylic emulsion
CN102015571A (en) * 2008-05-01 2011-04-13 瓦克化学股份公司 Building materials incorporated with hydrophobic silicone resin(s)
CN102321219A (en) * 2011-06-03 2012-01-18 北京化工大学 Method for preparing organic-silicon grafted acrylate copolymer emulsion
CN102977727A (en) * 2012-10-30 2013-03-20 苏州市德莱尔建材科技有限公司 Waterproof coating for exterior wall of building
CN103161082A (en) * 2013-02-26 2013-06-19 中国中化股份有限公司 Organosilicone modification pigment printing adhesion agent and preparation method thereof
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CN104262529A (en) * 2014-09-15 2015-01-07 苏州德捷膜材料科技有限公司 High polymer luminous material of terbium-doped fluorosilicone modified acrylate and preparation method of high polymer luminous material
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CN104262529A (en) * 2014-09-15 2015-01-07 苏州德捷膜材料科技有限公司 High polymer luminous material of terbium-doped fluorosilicone modified acrylate and preparation method of high polymer luminous material
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CN107100336A (en) * 2017-02-17 2017-08-29 新疆亚克希姆建材有限公司 Heat insulation decoration integrated plate and preparation method thereof
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