CN106750255B - A kind of preparation method and applications of anionic and nonionic type reactive emulsifier - Google Patents

A kind of preparation method and applications of anionic and nonionic type reactive emulsifier Download PDF

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CN106750255B
CN106750255B CN201611216316.XA CN201611216316A CN106750255B CN 106750255 B CN106750255 B CN 106750255B CN 201611216316 A CN201611216316 A CN 201611216316A CN 106750255 B CN106750255 B CN 106750255B
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anionic
reactive emulsifier
nonionic type
type reactive
polyoxyethylene ether
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CN106750255A (en
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余龙飞
黄淋佳
李欢玲
郑小珊
李莉
韩从辉
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Institute of Chemical Engineering of Guangdong Academy of Sciences
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Guangdong Petroleum And Fine Chemical Research Institute
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    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
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    • C07C309/02Sulfonic acids having sulfo groups bound to acyclic carbon atoms
    • C07C309/03Sulfonic acids having sulfo groups bound to acyclic carbon atoms of an acyclic saturated carbon skeleton
    • C07C309/07Sulfonic acids having sulfo groups bound to acyclic carbon atoms of an acyclic saturated carbon skeleton containing oxygen atoms bound to the carbon skeleton
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    • C08F2/12Polymerisation in non-solvents
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    • C08F2/16Aqueous medium
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    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
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    • C08F220/16Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms
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    • C08F283/06Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
    • C08F283/065Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals on to unsaturated polyethers, polyoxymethylenes or polyacetals
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    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
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Abstract

The invention discloses a kind of preparation method and applications of anionic and nonionic type reactive emulsifier.The structural formula of the anionic and nonionic type reactive emulsifier is as follows:Wherein

Description

A kind of preparation method and applications of anionic and nonionic type reactive emulsifier
Technical field
The present invention relates to a kind of preparation method and applications of anionic and nonionic type reactive emulsifier, belong to polymer emulsion The field of middle emulsifier.
Background technique
Emulsifier is one of the main component in emulsion polymerization systems, plays decisive role to the performance of polymer.It passes The emulsifier of system is adsorbed in emulsion particle surface by physical action, when temperature change, imposing shearing force or electrolyte being added, cream The stability of liquid can change or even be demulsified;Emulsifier can migrate to film coated surface and form one layer of non-ization in film forming procedure The hydrophilic emulsifying agent layer for learning bonding, will lead to film water absorption and swelling once encounteing water or be affected with dump, and cause frosting, whiting, gloss decline The defects of, reduce coating film gloss, rate of film build and water resistance.
In emulsion polymerization, reactive emulsifier is bonded in the way of covalent bond by the double bond functional group in molecule Polymer particle surface becomes a part of polymer, avoids emulsifier from desorption on polymer particle or in latex film Migration, greatly reduce the hydrophilic radical of latex film surface, not only effectively solve water paint ink system in emulsifier in base Expect surface and surface of pigments competitive Adsorption problem, and increase substantially emulsion intercalation method, coating film gloss, rate of drying, Filming performance and water-resistance property of coating.It is dry in order to improve film using that can be greatly reduced in ordinary emulsion in water paint ink Dry speed and a large amount of volatility low-carbon alcohols, ethers, esters quick dry agent and the coalescing agent added, so that printing be greatly reduced Ink VOC emission.In addition, most reactive emulsifiers are linked in polymer segment by participating in reaction, high degree Reduce using existing for free form, using APEO class emulsifier be representative, difficult to degrade conventional emulsifier in water body environment Discharge reduces water body COD content, reduces environmental pollution and the generation of foam, reduces wastewater treatment difficulty, increases waste water circulation Utilization rate.
Since polymerisable emulsifier is used for emulsion polymerization for the first time by Greene et al., many scholars and research institution exist This respect has done many researchs.According to the difference of reactive group, reactive emulsifier is divided into allylic, phenylethylene, third Acrylamide, maleic acid esters etc..Model sage, which forces, makees reactive emulsifier with hydroxypropyl sodium alkyl sulfonate (SAHS), has synthesized bullet Property acrylic acid ester emulsion, the results showed that the PA lotion of SAHS modified synthesis is more stable and viscosity is lower.Chern etc. will be reactive newborn Agent sodium dodecyl allyl base Succinate sodium sulfonate is for adding on a small quantity in the semi-continuous emulsion polymerizing of butyl acrylate In the case of electrolyte, more stable polymer emulsion can be obtained;It wears obviously with 2- acrylamide-2-methylpro panesulfonic acid sodium (APMS) solid content height is successfully prepared using styrene and butyl acrylate as comonomer for a kind of polymerisable emulsifier Up to 50% styrene-acrylic emulsion, and the properties such as the electrolyte resistance of lotion, pH stability, mechanical stability are all preferable;Deng Sword such as utilizes maleic anhydride to polymerize as a kind of reactive emulsifier for pure-acrylic emulsion with the single-esterification product of lauryl alcohol In, compared with conventional emulsifier, shear strength, water resistance, transparency, pollution resistance of film etc. all have clear improvement.Pich etc. It is prepared for a kind of fluorine-containing reactive emulsifier first, obtains a kind of fluorine-containing cream after it is copolymerized with styrene, butyl acrylate Liquid, the emulsion intercalation method and film forming are preferable, and the corrosion resistance of film, the transparency, glossiness are also fine;It closes in recent years It is more in the research of maleic diester type reactive emulsifier.Xu Jian etc. has synthesized maleic anhydride list decylene glycol ester first, so Carry out reacting under alkaline condition with 2,3- epoxypropyltrimethylchloride chloride afterwards generate a kind of maleic diester type sun from Sub- emulsifier can significantly reduce the surface tension of water, and have lower critical micelle concentration (0.2-0.6mmol.L-1)。He Etc. having synthesized a kind of diester-type reactive emulsifier maleic anhydride decylene glycol ester sulfopropyl sodium salt (M-12), it to be used for styrene, third The ultrasonic radiation polymerization reaction of olefin(e) acid butyl ester.With the increase of M-12 dosage, emulsion particle diameter gradually becomes smaller and is distributed and broadens, simultaneously Since emulsifier is chemically bound in the surface of emulsion particle securely, gained emulsion intercalation method is preferable.
Reactivity and bonding rate of the allylic reactive emulsifier in emulsion polymerization are low, are generally only used for acrylic acid Class, vinyl acetate esters isoreactivity be higher, in water-soluble biggish monomer polymerization;Phenylethylene reactive emulsifier is due to phenyl ring Draw electronic effect, reactivity is moderate, and the stability of emulsion being prepared is not good enough, thus usually require add a certain amount of emulsifier Or change the feeding mode of monomer;Acrylic amide reactive emulsifier reactivity is higher, can be applied to styrene, propylene In the polymerization reaction of esters of gallic acid monomer, but emulsifier homopolymerization risk can be faced;Maleic acid esters reactive emulsifier reactivity It is moderate, and it is not easy autohemagglutination, keep participation copolymerization probability higher, emulsifier can effectively be avoided to reduce emulsification effect because of itself homopolymerization Fruit applies applied to the good combination property in emulsion polymerization and can get high-performance emulsions film in coating and printing ink, be to study most For extensive a kind of reactive emulsifier.
In maleic acid esters reactive emulsifier, domestic and international correlative study mainly uses C12-C16Straight chain primary alcohol/alcohol ether, Alkyl phenol polyoxyethylene ether is starting material, through maleated, obtain non-ionic, anionic, anionic and nonionic type and The maleic acid esters reactive emulsifier of double ion type is simultaneously applied in emulsion polymerization.However, since primary alconol is free of EO hydrophilic chain Section, spatial stability is poor, the emulsion particle diameter of synthesis is bigger than normal, and resistance to hard water deviation;And the alkyl with excellent emulsifying capacity Phenol has environmental organism toxicity again, and domestic and international relevant industries are being phased out use.With the C of ordinary construction12-C16Linear primary Alcohol/alcohol ether, alkyl phenol polyoxyethylene ether are compared, and secondary alcohol is located at carbochain centre rather than both ends, the special space structure of umbrella Secondary alcohol is imparted with good spatial stability, high emulsifying strength, narrow hydrogel range, low bubble, low hydrodynamic(al) state and balance surface Tension, to substrate wetting good and there is fine dispersion, wettability to pigment, be the instead of APEO class surfactant One selection.
Therefore, the maleic acid list secondary alcohol polyoxyethylene ether -2- hydroxyl reacted using secondary alcohol polyoxyethylene ether as starting material Base propyl sulfonic acid salt anionic and nonionic type reactive emulsifier has than conventional emulsifier and common reactive emulsifier more The performances such as excellent emulsion dispersion wetting and water-resistance property of coating.
Summary of the invention
The purpose of the present invention is to provide a kind of preparation method and applications of anionic and nonionic type reactive emulsifier.
The technical solution used in the present invention is:
A kind of anionic and nonionic type reactive emulsifier, structural formula are as follows:
WhereinN=5~40.
A kind of preparation method of the anionic and nonionic type reactive emulsifier, comprising the following steps:
1) maleic anhydride and secondary alcohol polyoxyethylene ether react synthesis secondary alcohol polyoxyethylene ether maleic acid under the action of catalyst Monoesters;
2) it uses in aqueous slkali with secondary alcohol polyoxyethylene ether maleic acid monoester, obtains secondary alcohol polyoxyethylene ether maleic acid monoester Salt;
3) it after secondary alcohol polyoxyethylene ether maleic acid monoester salt is reacted with 3- chlorine-2-hydroxyl propanesulfonate, then adjusts system and consolidates Anionic and nonionic type reactive emulsifier is made after content.
The maleic anhydride, secondary alcohol polyoxyethylene ether, catalyst, alkali, 3- chlorine-2-hydroxyl propanesulfonate mass ratio be (50~60): (195~970): (0.3~6): (18~30): (90~110).
The secondary alcohol polyoxyethylene ether is the 6- tridecyl alcohol polyoxyethylene ether or 2,6 that ethylene oxide number is 5~40, 8- trimethyl -4- nonane alcohol polyoxyethylene ether.
The secondary alcohol polyoxyethylene ether is using preceding in 80~110 DEG C of 5~6h of vacuum drying.
The catalyst be p-methyl benzenesulfonic acid or alkali alcoholate, hydroxide, carbonate, in acetate at least It is a kind of;The alkali is one of alkali alcoholate, hydroxide.
In step 3), the solid content is 25~50%.
The reaction temperature of step 1) is 80~140 DEG C, and the reaction time is 1.5~6h, and reaction carries out under protective atmosphere;Step System temperature before rapid 2) neutralization is 50~80 DEG C, and neutralization system pH is 6~7 after alkali is added, and reaction temperature is 60~90 DEG C, instead It is 1~3h between seasonable;The reaction temperature of step 3) is 80~120 DEG C, and the reaction time is 2~6h.
The anionic and nonionic type reactive emulsifier is preparing the application in polymer.
The application, be in the presence of at least one described anionic and nonionic type reactive emulsifier, make monomer into Row emulsion polymerization.
The beneficial effects of the present invention are: reactive emulsifier disclosed by the invention has spatial stability, high emulsion dispersion The excellent properties such as ability, low bubble, low surface tension, wetting, applying can prepare in emulsion polymerization especially Styrene-Acrylate Emulsion Polymerization The high-performance emulsions of the characteristics such as high stability, high glaze, small particle out.
Specific embodiment
A kind of anionic and nonionic type reactive emulsifier, structural formula are as follows:
Wherein(6- tridecyl) or
(2,6,8- trimethyl -4- nonyl);N=5~40.
A kind of preparation method of the anionic and nonionic type reactive emulsifier, comprising the following steps:
1) maleic anhydride and secondary alcohol polyoxyethylene ether react synthesis secondary alcohol polyoxyethylene ether maleic acid under the action of catalyst Monoesters;
2) it uses in aqueous slkali with secondary alcohol polyoxyethylene ether maleic acid monoester, obtains secondary alcohol polyoxyethylene ether maleic acid monoester Salt;
3) it after secondary alcohol polyoxyethylene ether maleic acid monoester salt is reacted with 3- chlorine-2-hydroxyl propanesulfonate, then adjusts system and consolidates Anionic and nonionic type reactive emulsifier is made after content.
Preferably, the maleic anhydride, secondary alcohol polyoxyethylene ether, catalyst, alkali, 3- chlorine-2-hydroxyl propanesulfonate Mass ratio is (50~60): (195~970): (0.3~6): (18~30): (90~110);It is further preferred that the horse Come acid anhydrides, secondary alcohol polyoxyethylene ether, catalyst, alkali, 3- chlorine-2-hydroxyl propanesulfonate mass ratio be (50~55): (220~ 760): (1~4.5): (19~26.5): (98~105).
Preferably, the secondary alcohol polyoxyethylene ether is the 6- tridecyl alcohol polyoxyethylene that ethylene oxide number is 5~40 Ether or 2,6,8- trimethyl -4- nonane alcohol polyoxyethylene ether.
The structural formula of 6- tridecyl alcohol polyoxyethylene ether is as follows:
N=5~40 in formula.
The structural formula of 2,6,8- trimethyl -4- nonane alcohol polyoxyethylene ether is as follows:
N=5~40 in formula.
Preferably, the secondary alcohol polyoxyethylene ether is using preceding in 80~110 DEG C of 5~6h of vacuum drying.
Preferably, the catalyst is p-methyl benzenesulfonic acid or alkali alcoholate, hydroxide, carbonate, acetate At least one of;It is further preferred that the catalyst is p-methyl benzenesulfonic acid, sodium alkoxide, potassium alcoholate, sodium hydroxide, hydroxide At least one of potassium, sodium carbonate, potassium carbonate, sodium acetate, potassium acetate;Still further preferably, the catalyst is to first At least one of benzene sulfonic acid, sodium methoxide, sodium hydroxide, potassium hydroxide, sodium carbonate, sodium acetate.
Preferably, the alkali is one of alkali alcoholate, hydroxide;It is further preferred that the alkali For one of sodium alkoxide, potassium alcoholate, sodium hydroxide, potassium hydroxide;Still further preferably, the alkali is sodium methoxide, hydroxide One of sodium, potassium hydroxide.
Preferably, in step 3), the solid content is 25~50%;It is further preferred that described consolidates in step 3) Content is 30~45%.
Preferably, the reaction temperature of step 1) is 80~140 DEG C, and the reaction time is 1.5~6h, is reacted under protective atmosphere It carries out;Step 2) neutralize before system temperature be 50~80 DEG C, be added alkali after neutralize system pH be 6~7, reaction temperature be 60~ 90 DEG C, the reaction time is 1~3h;The reaction temperature of step 3) is 80~120 DEG C, and the reaction time is 2~6h;Further preferably , the protective atmosphere is one of nitrogen or inert gas;Still further preferably, the protective atmosphere is nitrogen Gas.
The anionic and nonionic type reactive emulsifier is preparing the application in polymer.
Preferably, the application is made in the presence of at least one described anionic and nonionic type reactive emulsifier Monomer carries out emulsion polymerization.
Preferably, the monomer is acrylate, methacrylate, unsaturated amides, unsaturated nitrile, styrene spread out At least one of biology, diene derivatives, polyethyleneglycol diacrylate and polyethylene glycol dimethacrylate;Into one Step is preferred, the monomer be in acrylate, methacrylate, styrene derivative and diene derivatives at least It is a kind of;Still further preferably, the monomer is ethyl acrylate, butyl acrylate, 2-EHA, methyl-prop E pioic acid methyl ester, ethyl methacrylate, 2-Hydroxyethyl methacrylate, glycidyl methacrylate, α-methylstyrene, At least one of butadiene and isoprene.
Preferably, the anionic and nonionic type reactive emulsifier accounts for polymerization reaction system (amount based on whole monomers) Mass fraction is 0.1~20%;It is further preferred that the anionic and nonionic type reactive emulsifier accounts for polymerization reaction system Mass fraction is 0.2~5%;Still further preferably, the anionic and nonionic type reactive emulsifier accounts for polymerization reaction system Mass fraction be 0.5~4%.
Furthermore, it is understood that the application, is selected one or more of the anionic and nonionic type reactive emulsifier, or Use at least one anionic and nonionic type reactive emulsifier and other emulsifiers or protecting colloid.
Preferably, other emulsifiers are dodecyl benzene sulfonate, alkyl sulfate, alkyl polyoxyethylene ether sulphur Hydrochlorate, alkyl phenyl polyethylene oxides ether sulfate, dialkyl sulfosuccinates, alkyl polyoxyethylene ether and alkyl phenyl polyoxy At least one of vinethene.
Preferably, the protecting colloid is polyacrylic acid hard resin protective glue, polyvinyl alcohol and hydroxyethyl cellulose At least one of.
Preferably, other emulsifiers or protecting colloid account for the quality of total emulsifiers no more than 50%;It is further excellent Choosing, other emulsifiers or protecting colloid account for the quality of total emulsifiers no more than 25%.
Preferably, described to be aggregated in that initiator effect is lower to be carried out, the initiator be inorganic peroxide initiator, At least one of organic peroxide evocating agent, azo initiator, redox initiator;It is further preferred that described Initiator is hydrogen peroxide, potassium peroxydisulfate, ammonium persulfate, isopropyl benzene hydroperoxide, diisopropylbenzene hydroperoxide, two isobutyl of azo Nitrile, azo isobutyl cyano formamide or the compositions such as peroxide and sodium hydrogensulfite, sodium thiosulfate, ferrous sulfate, carbohydrate At least one of redox initiator.
The contents of the present invention are described in further detail below by way of specific embodiment.
In these embodiments, unless otherwise noted, all percentage is weight percent.6- tridecyl alcohol is poly- Ethylene oxide ether or 2,6,8- trimethyl -4- nonane alcohol polyoxyethylene ether are to buy gained from commercial channel import.
Synthetic example 1:
By mass fraction, takes 300 parts of 6- ammonium trideceth 9EO into four-hole boiling flask, 52 parts of maleic acids are added Acid anhydride and 1.0 parts of sodium methoxides are in N2The lower 88 DEG C of reactions 6h of gas shielded;80 DEG C are cooled to, is added in 26.5 parts of sodium methoxides and system pH is arrived 6.5~7.0,85 DEG C vacuumize 2h;It is added 98 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium, after 100 DEG C of reaction 4h, stirs at low speed down Quantitative water adjustment system solid content is added to 35%, obtains maleic acid list secondary alcohol polyoxyethylene ether -2- propane sulfonate Anionic and nonionic type reactive emulsifier.
Synthetic example 2:
By mass fraction, takes 255 parts of 6- ammonium trideceth 7EO into four-hole boiling flask, 50 parts of maleic acids are added Acid anhydride and 1.0 parts of potassium hydroxide are in N2The lower 100 DEG C of reactions 4.0h of gas shielded;70 DEG C are cooled to, is added in 25.5 parts of sodium methoxides and body It is pH to 6.5~6.8,90 DEG C vacuumize 1h;It is added 100 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium, it is low after 110 DEG C of reaction 3.5h Speed is added with stirring quantitative water adjustment system solid content to 30%, obtains maleic acid list secondary alcohol polyoxyethylene ether -2- hydroxyl third Base sulfonate anionic and nonionic type reactive emulsifier.
Synthetic example 3:
By mass fraction, takes 760 parts of 6- ammonium trideceth 30EO into four-hole boiling flask, 55 parts of maleic acids are added Acid anhydride and 4.5 parts of sodium acetates are in N2The lower 120 DEG C of reactions 6h of gas shielded;65 DEG C are cooled to, is added in 19 parts of sodium hydroxides and system pH 2.5h is vacuumized to 6.3~6.8,90 DEG C;It is added 105 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium, after 105 DEG C of reaction 5h, low speed is stirred The quantitative water adjustment system solid content of lower addition is mixed to 35%, obtains maleic acid list secondary alcohol polyoxyethylene ether -2- hydroxypropyl sulphur Hydrochlorate anionic and nonionic type reactive emulsifier.
Synthetic example 4:
By mass fraction, 220 part 2 is taken, 6,8- trimethyl -4- nonane alcohol polyoxyethylene ether 6EO are added into four-hole boiling flask 50 parts of maleic anhydrides and 1.0 parts of p-methyl benzenesulfonic acid are in N2The lower 83 DEG C of reactions 3.5h of gas shielded;80 DEG C are cooled to, 26 parts of methanol are added With system pH to 6.5~6.8 in sodium, 85 DEG C vacuumize 2h;98 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium, 100 DEG C of reaction 4h are added Afterwards, the quantitative water adjustment system solid content of lower addition is stirred at low speed to 45%, obtains maleic acid list secondary alcohol polyoxyethylene ether -2- hydroxyl Base propyl sulfonic acid salt anionic and nonionic type reactive emulsifier.
Synthesize comparative example 1:
By mass fraction, 240 parts of C are taken1252 parts of maleic anhydrides are added into four-hole boiling flask in fatty alcohol polyoxyethylene ether 7EO With 1.5 parts of sodium methoxides in N2The lower 95 DEG C of reactions 5h of gas shielded, it is 7 that the product sodium hydroxide solution of 5wt%, which adjusts pH, and low speed stirs The quantitative water adjustment system solid content of lower addition is mixed to 35wt%, obtains 1 reactive emulsifier of comparative example.
Synthesize comparative example 2:
It by mass fraction, takes 95 parts of lauryl alcohols into four-hole boiling flask, 50 parts of maleic anhydrides and 1.0 parts of sodium methoxides is added in N2 The lower 95 DEG C of reactions 5h of gas shielded, it is 7 that the product sodium hydroxide solution of 5wt%, which adjusts pH, stirs at low speed the quantitative water of lower addition Adjustment system solid content obtains 2 reactive emulsifier of comparative example to 35wt%.
According to following aggregation schemes, with the reactive emulsifier of reactive emulsifier and comparative example 1 to 2 of the invention Carry out emulsion polymerization.Then the evaluation of polymerization stability, particle size and mechanical stability is carried out to resulting polymerized emulsion, and The water resistance of emulsion film forming caudacoria is evaluated.The results are shown in Table 1.It will be also found in the resulting data of common emulsifier In table 1, with comparing.
Aggregation scheme
2 are added in 1 liter of glass reactor equipped with thermometer, blender, condenser, nitrogen inlet and dropping funel Gram emulsifier, 300 grams of distilled water, 10 grams of n-butyl acrylates and 0.4 gram of ammonium persulfate.Logical nitrogen, then heats mixture Stirring, when temperature is raised to 70 DEG C, is being added dropwise to 80 grams of styrene, 20 grams of methacrylic acids and 90 grams of acrylic acid just in 3 hours The mixture of butyl ester.After being added dropwise to complete, keep reaction temperature be 80 DEG C the reaction was continued 2 hours, then with water-bath cooling to 30~ 40 DEG C, emulsion system pH to 8-9 is adjusted to get styrene-acrylic emulsion with 10% ammonium hydroxide.
Polymerized emulsion performance test is as follows:
1, polymerization stability (gel fraction)
After the completion of polymerization, polymerized emulsion is filtered by the wire cloth of 100 mesh.The residue of filtering is washed with water, It is dried overnight under 200mmHg in 105 DEG C, then weighs.Based on amount of monomer used, thus resulting value " weight will be expressed as Measure % ".
2, partial size
After the wire cloth filtering of 100 mesh of polymerized emulsion, using 3000 laser particle analyzer of Mastersize of Malvern Carry out partial size test.
3, mechanical stability
It is mechanical with MARON method under conditions of 10kg and 1000rpm after the wire cloth filtering of 100 mesh of polymerized emulsion Stability test machine rotates 50 grams of polymerized emulsions 5 minutes.By the aggregation being consequently formed by the wire cloths of one 100 mesh into Row filtering.The residue of filtering is washed with water, is dried overnight under 200mmHg in 105 DEG C, then weighs.And the amount with polymer, Thus resulting value it will be expressed as " weight % ".
4, glossiness is tested
After the wire cloth filtering of 100 mesh of polymerized emulsion, polymerized emulsion is coated in glass with 150um wet film maker On plate, it is poly- that the ZGM1022Glossmeter glossometer after paint film is dry using ZEHNTNER company carries out 60 ° of glossiness tests The gloss of compound film.To exclude the interference such as ground water absorption rate, flatness, shrinkage stress, first coated one side is wiped with alcohol It wipes completely, to dispel influence of the grease stain to test.
5, water resistance (film-brightens test)
After the wire cloth filtering of 100 mesh of polymerized emulsion, polymerized emulsion is coated on a slide glass (76 × 26mm), it is thick Degree is 125 μm, and the film forming for carrying out it at 100 DEG C 5 minutes.After being cooled to room temperature, a testing piece is obtained.One with 8 points Type is placed in the petrie dish on newspaper, and the slide glass for having film attached thereto is immersed in the water at room temperature.Measurement is until lead The word time required until becoming unable to identification.
Test result is shown in Table 1.
Polymerized emulsion the performance test results obtained by 1 different emulsifiers of table
Show from the test result of table 1: can obtain that there is high cream using anionic and nonionic type reactive emulsifier of the invention The lotion of liquid stability, low partial size.Moreover, the polymer film of gained polymerized emulsion has splendid water resistance and high glaze etc. excellent Benign energy.

Claims (7)

1. a kind of preparation method of anionic and nonionic type reactive emulsifier, it is characterised in that: the following steps are included:
1) maleic anhydride and secondary alcohol polyoxyethylene ether react synthesis secondary alcohol polyoxyethylene ether maleic acid monoester under the action of catalyst;
2) alkali neutralization secondary alcohol polyoxyethylene ether maleic acid monoester is used, secondary alcohol polyoxyethylene ether maleic acid monoester salt is obtained;
3) after secondary alcohol polyoxyethylene ether maleic acid monoester salt is reacted with 3- chlorine-2-hydroxyl propanesulfonate, then system solid content is adjusted Anionic and nonionic type reactive emulsifier is made afterwards;
Its structural formula of the anionic and nonionic type reactive emulsifier is as follows:
WhereinN=5~40.
2. a kind of preparation method of anionic and nonionic type reactive emulsifier according to claim 1, it is characterised in that: described Maleic anhydride, secondary alcohol polyoxyethylene ether, catalyst, alkali, 3- chlorine-2-hydroxyl propanesulfonate mass ratio be (50~60): (195~970): (0.3~6): (18~30): (90~110).
3. a kind of preparation method of anionic and nonionic type reactive emulsifier according to claim 2, it is characterised in that: described Secondary alcohol polyoxyethylene ether using preceding in 80~110 DEG C of 5~6h of vacuum drying.
4. a kind of preparation method of anionic and nonionic type reactive emulsifier according to claim 2, it is characterised in that: described Catalyst be p-methyl benzenesulfonic acid, alkali alcoholate, the hydroxide of alkali metal, the carbonate of alkali metal, alkali metal vinegar At least one of hydrochlorate;The alkali is one of alkali alcoholate, the hydroxide of alkali metal.
5. a kind of preparation method of anionic and nonionic type reactive emulsifier according to claim 1, it is characterised in that: step 3) in, the solid content is 25~50%.
6. a kind of preparation method of anionic and nonionic type reactive emulsifier according to claim 1, it is characterised in that: step 1) reaction temperature is 80~140 DEG C, and the reaction time is 1.5~6h, and reaction carries out under protective atmosphere;Before step 2) neutralizes System temperature be 50~80 DEG C, be added alkali after neutralize system pH be 6~7, reaction temperature be 60~90 DEG C, the reaction time be 1~ 3h;The reaction temperature of step 3) is 80~120 DEG C, and the reaction time is 2~6h.
7. any one of claim 1~6 prepares resulting anionic and nonionic type reactive emulsifier and is preparing the application in polymer, It is characterized by: making monomer carry out emulsion polymerization in the presence of at least one described anionic and nonionic type reactive emulsifier.
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