CN106750255A - 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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CN106750255A
CN106750255A CN201611216316.XA CN201611216316A CN106750255A CN 106750255 A CN106750255 A CN 106750255A CN 201611216316 A CN201611216316 A CN 201611216316A CN 106750255 A CN106750255 A CN 106750255A
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anionic
reactive emulsifier
nonionic type
type reactive
preparation
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CN106750255B (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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    • C08F283/06Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
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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 emulsifying agent.
Background technology
Emulsifying agent is one of key component in emulsion polymerization systems, and the performance to polymer plays decisive role.Pass The emulsifying agent of system is adsorbed in emulsion particle surface by physical action, temperature change, impose shearing force or add electrolyte when, breast The stability of liquid can change or even be demulsified;Emulsifying agent can be migrated to film coated surface and form one layer of non-ization in film forming procedure The hydrophilic emulsifying agent layer of bonding is learned, once encounter water can cause film water absorption and swelling, causes frosting, whiting, gloss to decline Etc. defect, coating film gloss, rate of film build and water resistance are reduced.
In emulsion polymerization, reactive emulsifier is bonded to by using the double bond functional group in molecule in the way of covalent bond Polymer particle surface, the part as polymer, it is to avoid emulsifying agent is from desorption on polymer particle or in latex film Migration, greatly reduces the hydrophilic radical on latex film surface, and emulsifying agent is in base in not only effectively solving water paint ink system Material 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 (LC) alcohols, ethers, esters quick dry agent and the coalescents that add, so as to printing is greatly reduced Ink VOC emission.Additionally, most reactive emulsifiers are linked in polymer segment by participating in reaction, high degree Reduce it is existing with free form, with APEO class emulsifying agents as representative, the conventional emulsifier of difficult degradation is in water body environment Discharge, reduces water body COD contents, 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 by Greene et al. first, 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 forces and makees reactive emulsifier with hydroxypropyl sodium alkyl sulfonate (SAHS), has synthesized bullet Property acrylic acid ester emulsion, as a result show the PA emulsions of SAHS modified synthesis compared with stable and viscosity is relatively low.Chern etc. will be reactive newborn Agent sodium dodecyl allyl base Succinate sodium sulfonate is used in the semi-continuous emulsion polymerizing of butyl acrylate, a small amount of adding In the case of electrolyte, the polymer emulsion that can be relatively stablized;Wear obviously with 2- acrylamide-2-methylpro panesulfonic acid sodium (APMS) it is a kind of polymerisable emulsifier, using styrene and butyl acrylate as comonomer, is successfully prepared solid content high Up to 50% styrene-acrylic emulsion, and the properties such as electrolyte resistance, pH stability, the mechanical stability of emulsion are all preferable;Deng Sword is as utilized maleic anhydride to be polymerized for pure-acrylic emulsion as a kind of reactive emulsifier 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. Be prepared for a kind of fluorine-containing reactive emulsifier first, by it with styrene, butyl acrylate copolymerization after obtain a kind of fluorine-containing breast Preferably, and the corrosion resistance of film, the transparency, glossiness are also fine for liquid, the emulsion intercalation method and film forming;Close in recent years It is more in the research of maleic diester type reactive emulsifier.Xu Jian etc. has synthesized maleic anhydride list lauryl alcohol ester first, so Carried out in the basic conditions with 2,3- epoxypropyltrimethylchloride chlorides afterwards reaction generate a kind of maleic diester type sun from Sub- emulsifying agent, its surface tension that can significantly reduce water, and with relatively low critical micelle concentration (0.2-0.6mmol.L-1)。He Etc. a kind of diester-type reactive emulsifier maleic anhydride lauryl alcohol ester sulfopropyl sodium salt (M-12) has been synthesized, for styrene, third The ultrasonic radiation polymerisation of olefin(e) acid butyl ester.With the increase of M-12 consumptions, emulsion particle diameter is tapered into and is distributed and broadens, while It is chemically bound in the surface of emulsion particle securely due to emulsifying agent, 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 During class, vinyl acetate esters isoreactivity are higher, water-soluble larger monomer is polymerized;Phenylethylene reactive emulsifier is due to phenyl ring Draw electronic effect, reactivity is moderate, and the stability of emulsion for preparing is not good enough, therefore generally needs to add a certain amount of emulsifying agent Or change the feeding mode of monomer;Acrylic amide reactive emulsifier reactivity is higher, can be applied to styrene, propylene In the polymerisation of esters of gallic acid monomer, but emulsifying agent homopolymerization risk can be faced;Maleic acid esters reactive emulsifier reactivity It is moderate, and autohemagglutination is difficult, make participation copolymerization probability higher, can effectively avoid emulsifying agent that emulsification effect is reduced because of itself homopolymerization Really, the good combination property in emulsion polymerization is applied to, applying can obtain high-performance emulsions film in coating and printing ink, is to study most It is extensive class reactive emulsifier.
In maleic acid esters reactive emulsifier, domestic and international correlative study mainly uses C12-C16Straight chain primary alcohol/alcohol ether, APES is initiation material, through maleated, obtain nonionic, anionic, anionic and nonionic type and The maleic acid esters reactive emulsifier of double ion type is simultaneously applied in emulsion polymerization.However, because primary alconol is free of EO hydrophilic chains Section, spatial stability is poor, synthesis emulsion particle diameter is bigger than normal, and resistance to hard water deviation;And there is the alkyl of excellent emulsifying capacity Phenol has environmental organism toxicity again, and domestic and international relevant industries are phased out using.With the C of ordinary construction12-C16Linear primary Alcohol/alcohol ether, APES are compared, secondary alcohol in the middle of carbochain rather than two ends, the special space structure of umbrella Imparting secondary alcohol has good spatial stability, high emulsifying strength, narrow hydrogel scope, low bubble, low hydrodynamic(al) state and balance surface Tension force, to substrate wetting good and to pigment there is fine dispersion, wettability, be that instead of the of APEO class surfactants One selection.
Therefore, the maleic acid list secondary alcohol APEO -2- hydroxyls for being obtained as initiation material reaction with secondary alcohol APEO Base propyl sulfonic acid salt anionic and nonionic type reactive emulsifier has than conventional emulsifier and common reactive emulsifying agent more The performance such as excellent emulsion dispersion wetting and water-resistance property of coating.
The content of the invention
It is an object of the invention 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, its structural formula is as follows:
WhereinN=5~40.
A kind of preparation method of described anionic and nonionic type reactive emulsifier, comprises the following steps:
1) maleic anhydride and secondary alcohol APEO are synthesized secondary alcohol APEO maleic acid under catalyst action Monoesters;
2) with aqueous slkali and secondary alcohol APEO maleic mono-ester, secondary alcohol APEO maleic mono-ester is obtained Salt;
3) after the reaction of secondary alcohol APEO maleic mono-ester salt and 3- chlorine-2-hydroxyls propanesulfonate, then adjust system and consolidate Anionic and nonionic type reactive emulsifier is obtained after content.
Described maleic anhydride, secondary alcohol APEO, catalyst, alkali, the mass ratio of 3- chlorine-2-hydroxyl propanesulfonates are (50~60):(195~970):(0.3~6):(18~30):(90~110).
Described secondary alcohol APEO is the 6- tridecyl alcohol APEOs or 2,6 that ethylene oxide number is 5~40, 8- trimethyl -4- nonane alcohol APEOs.
Described secondary alcohol APEO is vacuum dried 5~6h using preceding at 80~110 DEG C.
Described catalyst be in p-methyl benzenesulfonic acid or alkali alcoholate, hydroxide, carbonate, acetate at least It is a kind of;Described alkali is the one kind in alkali alcoholate, hydroxide.
Step 3) in, described solid content is 25~50%.
Step 1) reaction temperature be 80~140 DEG C, the reaction time be 1.5~6h, reaction carried out under protective atmosphere;Step System temperature before rapid 2) neutralization is 50~80 DEG C, and neutralization system pH is 6~7 after adding alkali, and reaction temperature is 60~90 DEG C, instead It is 1~3h between seasonable;Step 3) reaction temperature be 80~120 DEG C, the reaction time be 2~6h.
Application of the described anionic and nonionic type reactive emulsifier in polymer is prepared.
Described application, is in the presence of at least one described anionic and nonionic type reactive emulsifier, to enter monomer Row emulsion polymerization.
The beneficial effects of the invention are as follows:Reactive emulsifier disclosed by the invention has spatial stability, emulsion dispersion high The excellent properties such as ability, low bubble, low surface tension, wetting, applying can prepare in emulsion polymerization particularly Styrene-Acrylate Emulsion Polymerization Go out the high-performance emulsions of the characteristics such as high stability, high glaze, small particle.
Specific embodiment
A kind of anionic and nonionic type reactive emulsifier, its structural formula is as follows:
Wherein(6- tridecyls) or
(2,6,8- trimethyl -4- nonyls);N=5~40.
A kind of preparation method of described anionic and nonionic type reactive emulsifier, comprises the following steps:
1) maleic anhydride and secondary alcohol APEO are synthesized secondary alcohol APEO maleic acid under catalyst action Monoesters;
2) with aqueous slkali and secondary alcohol APEO maleic mono-ester, secondary alcohol APEO maleic mono-ester is obtained Salt;
3) after the reaction of secondary alcohol APEO maleic mono-ester salt and 3- chlorine-2-hydroxyls propanesulfonate, then adjust system and consolidate Anionic and nonionic type reactive emulsifier is obtained after content.
Preferably, described maleic anhydride, secondary alcohol APEO, catalyst, alkali, 3- chlorine-2-hydroxyl propanesulfonates Mass ratio is (50~60):(195~970):(0.3~6):(18~30):(90~110);It is further preferred that described horse It is (50~55) to come acid anhydrides, secondary alcohol APEO, catalyst, alkali, the mass ratio of 3- chlorine-2-hydroxyl propanesulfonates:(220~ 760):(1~4.5):(19~26.5):(98~105).
Preferably, described secondary alcohol APEO is 6- tridecyl alcohol polyoxyethylene that ethylene oxide number is 5~40 Ether or 2,6,8- trimethyl -4- nonane alcohol APEOs.
The structural formula of 6- tridecyl alcohol APEOs is as follows:
N=5~40 in formula.
The structural formula of 2,6,8- trimethyl -4- nonane alcohol APEOs is as follows:
N=5~40 in formula.
Preferably, described secondary alcohol APEO is vacuum dried 5~6h using preceding at 80~110 DEG C.
Preferably, described catalyst is p-methyl benzenesulfonic acid or alkali alcoholate, hydroxide, carbonate, acetate In at least one;It is further preferred that described catalyst is p-methyl benzenesulfonic acid, sodium alkoxide, potassium alcoholate, NaOH, hydroxide At least one in potassium, sodium carbonate, potassium carbonate, sodium acetate, potassium acetate;Still further preferably, described catalyst is to first At least one in benzene sulfonic acid, sodium methoxide, NaOH, potassium hydroxide, sodium carbonate, sodium acetate.
Preferably, described alkali is the one kind in alkali alcoholate, hydroxide;It is further preferred that described alkali It is the one kind in sodium alkoxide, potassium alcoholate, NaOH, potassium hydroxide;Still further preferably, described alkali is sodium methoxide, hydroxide One kind in sodium, potassium hydroxide.
Preferably, step 3) in, described solid content is 25~50%;It is further preferred that step 3) in, described consolidates Content is 30~45%.
Preferably, step 1) reaction temperature be 80~140 DEG C, the reaction time be 1.5~6h, react under protective atmosphere Carry out;Step 2) neutralize before system temperature be 50~80 DEG C, adding and neutralize system pH after alkali is 6~7, reaction temperature is 60~ 90 DEG C, the reaction time is 1~3h;Step 3) reaction temperature be 80~120 DEG C, the reaction time be 2~6h;Further preferably , described protective atmosphere is the one kind in nitrogen or inert gas;Still further preferably, described protective atmosphere is nitrogen Gas.
Application of the described anionic and nonionic type reactive emulsifier in polymer is prepared.
Preferably, described application, is in the presence of at least one described anionic and nonionic type reactive emulsifier, to make Monomer carries out emulsion polymerization.
Preferably, described monomer is that acrylate, methacrylate, unsaturated amides, unsaturated nitrile, styrene spread out At least one in biology, diene derivatives, polyethyleneglycol diacrylate and polyethylene glycol dimethacrylate;Enter one Step is preferred, described monomer in acrylate, methacrylate, styrene derivative and diene derivatives at least It is a kind of;Still further preferably, described monomer is ethyl acrylate, butyl acrylate, 2-EHA, methyl-prop E pioic acid methyl ester, EMA, HEMA, GMA, AMS, At least one in butadiene and isoprene.
Preferably, described 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 described anionic and nonionic type reactive emulsifier accounts for polymerization reaction system Mass fraction is 0.2~5%;Still further preferably, described anionic and nonionic type reactive emulsifier accounts for polymerization reaction system Mass fraction be 0.5~4%.
Furthermore, it is understood that described application, from described anionic and nonionic type reactive emulsifier one or more, or Use at least one described anionic and nonionic type reactive emulsifier and other emulsifying agents or protecting colloid.
Preferably, other described emulsifying agents 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 in vinethene.
Preferably, described protecting colloid is polyacrylic acid hard resin Protection glue, polyvinyl alcohol and hydroxyethyl cellulose In at least one.
Preferably, other described emulsifying agents or protecting colloid account for the quality of total emulsifiers and are not more than 50%;It is further excellent Choosing, the quality that other described emulsifying agents or protecting colloid account for total emulsifiers is not more than 25%.
Preferably, described being aggregated under initiator effect is carried out, described initiator is inorganic peroxide initiator, At least one in 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, DIBHP, the isobutyl of azo two Nitrile, azo isobutyl cyano group formamide or the composition such as peroxide and sodium hydrogensulfite, sodium thiosulfate, ferrous sulfate, carbohydrate At least one in redox initiator.
Present disclosure is described in further detail below by way of specific embodiment.
In these embodiments, unless otherwise noted, all of percentage is percetage by weight.6- tridecyls alcohol gathers Oxygen vinethene or 2,6,8- trimethyl -4- nonane alcohol APEOs are to buy gained from commercial channel import.
Synthetic example 1:
By mass fraction, 300 parts of 6- ammonium trideceths 9EO are taken in four-hole boiling flask, add 52 parts of maleic acids 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 arrived with system pH in 26.5 parts of sodium methoxides of addition 6.5~7.0,85 DEG C vacuumize 2h;98 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium are added, after 100 DEG C of reaction 4h, under stirring at low speed Add quantitative water to adjust system solid content to 35%, obtain maleic acid list secondary alcohol APEO -2- propane sulfonates Anionic and nonionic type reactive emulsifier.
Synthetic example 2:
By mass fraction, 255 parts of 6- ammonium trideceths 7EO are taken in four-hole boiling flask, add 50 parts of maleic acids Acid anhydride and 1.0 parts of potassium hydroxide are in N2The lower 100 DEG C of reactions 4.0h of gas shielded;Cool to 70 DEG C, add in 25.5 parts of sodium methoxides and body It is pH to 6.5~6.8,90 DEG C vacuumize 1h;100 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium are added, it is low after 110 DEG C of reaction 3.5h Speed stirring is lower to add quantitative water to adjust system solid content to 30%, obtains maleic acid list secondary alcohol APEO -2- hydroxyls third Base sulfonate anionic and nonionic type reactive emulsifier.
Synthetic example 3:
By mass fraction, 760 parts of 6- ammonium trideceths 30EO are taken in four-hole boiling flask, add 55 parts of maleic acids 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, with system pH in 19 parts of NaOH of addition To 6.3~6.8,90 DEG C vacuumize 2.5h;105 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium are added, after 105 DEG C of reaction 5h, low speed is stirred Mix the quantitative water of lower addition and adjust system solid content to 35%, obtain maleic acid list secondary alcohol APEO -2- hydroxypropyl sulphurs Hydrochlorate anionic and nonionic type reactive emulsifier.
Synthetic example 4:
By mass fraction, 220 part 2, in 6,8- trimethyl -4- nonanes alcohol APEO 6EO to four-hole boiling flask is taken, added 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 methyl alcohol are added With system pH to 6.5~6.8 in sodium, 85 DEG C vacuumize 2h;Add 98 parts of 3- chlorine-2-hydroxyl propyl sulfonic acid sodium, 100 DEG C of reaction 4h Afterwards, add quantitative water to adjust system solid content to 45% under stirring at low speed, obtain maleic acid list secondary alcohol APEO -2- hydroxyls Base propyl sulfonic acid salt anionic and nonionic type reactive emulsifier.
Synthesis comparative example 1:
By mass fraction, 240 parts of C are taken12AEO 7EO adds 52 parts of maleic anhydrides in four-hole boiling flask With 1.5 parts of sodium methoxides in N2The lower 95 DEG C of reactions 5h of gas shielded, it is 7 that product adjusts pH with the sodium hydroxide solution of 5wt%, and low speed is stirred Mix the quantitative water of lower addition and adjust system solid content to 35wt%, obtain the reactive emulsifier of comparative example 1.
Synthesis comparative example 2:
By mass fraction, 95 parts of lauryl alcohols are taken in four-hole boiling flask, adding 50 parts of maleic anhydrides and 1.0 parts of sodium methoxides in N2 The lower 95 DEG C of reactions 5h of gas shielded, it is 7 that product adjusts pH with the sodium hydroxide solution of 5wt%, and quantitative water is added under stirring at low speed Adjustment system solid content obtains the reactive emulsifier of comparative example 2 to 35wt%.
According to following aggregation schemes, with reactive emulsifier of the invention and the reactive emulsifier of comparative example 1 to 2 Carry out emulsion polymerization.Then the polymerized emulsion to gained carries out the evaluation of polymerization stability, particle size and mechanical stability, and Water resistance to emulsion film forming caudacoria is evaluated.The results are shown in Table 1.To be also found in the data obtained by common emulsifying agent In table 1, with comparing.
Aggregation scheme
2 are added in 1 liter of glass reactor equipped with thermometer, agitator, condenser, nitrogen inlet and dropping funel Gram emulsifying agent, 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, had been 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 to be 80 DEG C and continue to react 2 hours, then 30 are cooled to water-bath~ , emulsion system pH is adjusted to 8-9 with 10% ammoniacal liquor, obtain final product styrene-acrylic emulsion by 40 DEG C.
Polymerized emulsion performance test is as follows:
1st, 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 in 105 DEG C under 200mmHg, is then weighed.Based on amount of monomer used, the value of thus gained is expressed as " weight Amount % ".
2nd, particle diameter
After polymerized emulsion is filtered with the wire cloth of 100 mesh, using the laser particle analyzers of Mastersize 3000 of Malvern Carry out particle diameter test.
3rd, mechanical stability
After polymerized emulsion is filtered with the wire cloth of 100 mesh, under conditions of 10kg and 1000rpm, with MARON methods machinery Stability test machine rotates 50 grams of polymerized emulsions 5 minutes.The aggregation that will be consequently formed is entered by the wire cloth of one 100 mesh Row filtering.The residue of filtering is washed with water, is dried overnight in 105 DEG C under 200mmHg, then weighed.And the amount with polymer, The value of thus gained is expressed as " weight % ".
4th, glossiness test
After polymerized emulsion is filtered with the wire cloth of 100 mesh, polymerized emulsion is coated in glass with 150um wet film makers On plate, 60 ° of glossiness tests are carried out after the ZGM1022Glossmeter glossometers after drying varniss using ZEHNTNER companies poly- The gloss of compound film.To exclude the interference such as ground water absorption rate, flatness, shrinkage stress, coated one side is wiped with alcohol first Wipe clean, to dispel influence of the oil stain to testing.
5th, water resistance (film-brighten test)
After polymerized emulsion is filtered with the wire cloth of 100 mesh, polymerized emulsion is coated on a slide glass (76 × 26mm), it is thick It is 125 μm to spend, and makes the film forming that it carries out 5 minutes at 100 DEG C.After being cooled to room temperature, a test 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.Determine until lead Word becomes the time required untill can not recognizing.
Test result is shown in Table 1.
The different emulsifiers of table 1 gained polymerized emulsion the performance test results
Show from the test result of table 1:Can obtain that there is breast high using anionic and nonionic type reactive emulsifier of the invention The emulsion of liquid stability, low particle diameter.And, the polymer film of gained polymerized emulsion has splendid water resistance and high glaze etc. excellent Benign energy.

Claims (10)

1. a kind of anionic and nonionic type reactive emulsifier, it is characterised in that:Its structural formula is as follows:
WhereinN=5~40.
2. the preparation method of a kind of anionic and nonionic type reactive emulsifier described in claim 1, it is characterised in that:Including following Step:
1) maleic anhydride and secondary alcohol APEO are synthesized secondary alcohol APEO maleic mono-ester under catalyst action;
2) with aqueous slkali and secondary alcohol APEO maleic mono-ester, secondary alcohol APEO maleic mono-ester salt is obtained;
3) after secondary alcohol APEO maleic mono-ester salt reacts with 3- chlorine-2-hydroxyls propanesulfonate, then system solid content is adjusted Anionic and nonionic type reactive emulsifier is obtained afterwards.
3. the preparation method of a kind of anionic and nonionic type reactive emulsifier according to claim 2, it is characterised in that:It is described Maleic anhydride, secondary alcohol APEO, catalyst, alkali, 3- chlorine-2-hydroxyl propanesulfonates mass ratio be (50~60): (195~970): (0.3~6): (18~30): (90~110).
4. the preparation method of a kind of anionic and nonionic type reactive emulsifier according to claim 3, it is characterised in that:It is described Secondary alcohol APEO be the 6- tridecyl alcohol APEOs or 2 that ethylene oxide number is 5~40,6,8- trimethyl -4- Nonane alcohol APEO.
5. the preparation method of a kind of anionic and nonionic type reactive emulsifier according to claim 4, it is characterised in that:It is described Secondary alcohol APEO using it is preceding 80~110 DEG C be vacuum dried 5~6h.
6. the preparation method of a kind of anionic and nonionic type reactive emulsifier according to claim 3, it is characterised in that:It is described Catalyst be at least one in p-methyl benzenesulfonic acid or alkali alcoholate, hydroxide, carbonate, acetate;Described Alkali is the one kind in alkali alcoholate, hydroxide.
7. the preparation method of a kind of anionic and nonionic type reactive emulsifier according to claim 2, it is characterised in that:Step 3) in, described solid content is 25~50%.
8. the preparation method of a kind of anionic and nonionic type reactive emulsifier according to claim 2, it is characterised in that:Step 1) reaction temperature is 80~140 DEG C, and the reaction time is 1.5~6h, and reaction is carried out under protective atmosphere;Step 2) neutralize before System temperature is 50~80 DEG C, and adding and neutralize system pH after alkali is 6~7, and reaction temperature is 60~90 DEG C, the reaction time is 1~ 3h;Step 3) reaction temperature be 80~120 DEG C, the reaction time be 2~6h.
9. application of the anionic and nonionic type reactive emulsifier described in any one of claim 1~8 in polymer is prepared.
10. application according to claim 9, it is characterised in that:In at least one described anionic and nonionic type reactivity breast In the presence of agent, monomer is set to carry out emulsion polymerization.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107353398A (en) * 2017-08-07 2017-11-17 南方医科大学南方医院 A kind of water-soluble unsaturated aliphatic polyester and its preparation method and application
CN107573474A (en) * 2017-08-22 2018-01-12 广东省石油与精细化工研究院 A kind of silicone-modified water-soluble polyurethane acrylic resin emulsion and preparation method thereof
CN110951082A (en) * 2019-12-06 2020-04-03 万华化学集团股份有限公司 Preparation method of comb-shaped anionic-nonionic active epoxy emulsifier and preparation method of epoxy resin emulsion
CN112500532A (en) * 2020-12-14 2021-03-16 九洲生物技术(苏州)有限公司 Multifunctional lubricant, and preparation method and application thereof
CN113292716A (en) * 2021-05-24 2021-08-24 山东瑞捷新材料有限公司 Preparation method of self-emulsifying ester based on meta-phenyl ester

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0364922A1 (en) * 1988-10-17 1990-04-25 Mitsubishi Paper Mills, Ltd. Emulsifier for microcapsules, microcapsules using said emulsifier and process for producing such microcapsules, and non-carbon pressure-sensitive copying paper using said microcapsules
CN1490077A (en) * 2003-08-28 2004-04-21 �Ϻ���ͨ��ѧ Preparation of maleic di-ester cationoid polymerisable emulsifier
CN1966135A (en) * 2006-11-01 2007-05-23 大连理工大学 Maleic acid type anion polymerisable emusifier and its preparation method
CN101327413A (en) * 2008-07-24 2008-12-24 大连理工大学 Boletic acid type polymerisable emulsifier containing negative ion and non-ionic group and preparation method thereof
CN102757317A (en) * 2012-07-30 2012-10-31 西安楚龙达化工有限公司 Synthetic method of secondary alcohol polyether surfactant
CN104829500A (en) * 2015-04-20 2015-08-12 黄河三角洲京博化工研究院有限公司 Preparation method of fatty acid sulphonate surfactant

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0364922A1 (en) * 1988-10-17 1990-04-25 Mitsubishi Paper Mills, Ltd. Emulsifier for microcapsules, microcapsules using said emulsifier and process for producing such microcapsules, and non-carbon pressure-sensitive copying paper using said microcapsules
CN1490077A (en) * 2003-08-28 2004-04-21 �Ϻ���ͨ��ѧ Preparation of maleic di-ester cationoid polymerisable emulsifier
CN1966135A (en) * 2006-11-01 2007-05-23 大连理工大学 Maleic acid type anion polymerisable emusifier and its preparation method
CN101327413A (en) * 2008-07-24 2008-12-24 大连理工大学 Boletic acid type polymerisable emulsifier containing negative ion and non-ionic group and preparation method thereof
CN102757317A (en) * 2012-07-30 2012-10-31 西安楚龙达化工有限公司 Synthetic method of secondary alcohol polyether surfactant
CN104829500A (en) * 2015-04-20 2015-08-12 黄河三角洲京博化工研究院有限公司 Preparation method of fatty acid sulphonate surfactant

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
徐进进等: ""一种阴- 非离子型反应性乳化剂在乳液聚合中的应用"", 《胶体与聚合物》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107353398A (en) * 2017-08-07 2017-11-17 南方医科大学南方医院 A kind of water-soluble unsaturated aliphatic polyester and its preparation method and application
CN107573474A (en) * 2017-08-22 2018-01-12 广东省石油与精细化工研究院 A kind of silicone-modified water-soluble polyurethane acrylic resin emulsion and preparation method thereof
CN110951082A (en) * 2019-12-06 2020-04-03 万华化学集团股份有限公司 Preparation method of comb-shaped anionic-nonionic active epoxy emulsifier and preparation method of epoxy resin emulsion
CN110951082B (en) * 2019-12-06 2022-02-15 万华化学集团股份有限公司 Preparation method of comb-shaped anionic-nonionic active epoxy emulsifier and preparation method of epoxy resin emulsion
CN112500532A (en) * 2020-12-14 2021-03-16 九洲生物技术(苏州)有限公司 Multifunctional lubricant, and preparation method and application thereof
CN113292716A (en) * 2021-05-24 2021-08-24 山东瑞捷新材料有限公司 Preparation method of self-emulsifying ester based on meta-phenyl ester

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