+

CN1688614A - Aqueous polymer dispersions, method for the production thereof and use thereof, especially in anti-corrosion coatings - Google Patents

Aqueous polymer dispersions, method for the production thereof and use thereof, especially in anti-corrosion coatings Download PDF

Info

Publication number
CN1688614A
CN1688614A CN 03819209 CN03819209A CN1688614A CN 1688614 A CN1688614 A CN 1688614A CN 03819209 CN03819209 CN 03819209 CN 03819209 A CN03819209 A CN 03819209A CN 1688614 A CN1688614 A CN 1688614A
Authority
CN
China
Prior art keywords
weight
copolymer
monomer
acid
polymer dispersion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN 03819209
Other languages
Chinese (zh)
Other versions
CN100345869C (en
Inventor
C·迈纳斯
S·克里格
U·德索尔
G·默滕
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Publication of CN1688614A publication Critical patent/CN1688614A/en
Application granted granted Critical
Publication of CN100345869C publication Critical patent/CN100345869C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/22Emulsion polymerisation
    • C08F2/24Emulsion polymerisation with the aid of emulsifying agents

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Paints Or Removers (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

本发明涉及用于抗腐蚀保护的聚合物分散液,其具有良好的防锈性能,并涉及其制备方法和用途。该聚合物分散液含有包含磷酸基团和/或膦酸基团的乳化剂,并在聚合之前通过加入碱(部分地)中和。结果,生产出根据冷凝水试验DIN 50017具有改善的防锈性能的聚合物分散液,并可获得低凝结物含量。该聚合分散液还使得由其生产的抗腐蚀底漆具有改善的稳定性。使用所述聚合物分散液,可获得高光泽的涂层。The invention relates to a polymer dispersion used for anti-corrosion protection, which has good anti-rust performance, and relates to its preparation method and use. The polymer dispersion contains an emulsifier comprising phosphoric acid groups and/or phosphonic acid groups and is (partially) neutralized by adding a base before the polymerization. As a result, polymer dispersions are produced which have improved antirust properties according to the condensation water test DIN 50017, and low condensate contents can be obtained. The polymeric dispersion also allows improved stability of the anti-corrosion primers produced therefrom. Using said polymer dispersions, high-gloss coatings can be obtained.

Description

Aqueous polymer dispersion, its production method and purposes, especially for the purposes of protective system
The present invention relates to novel aqueous polymer dispersion, its production method and uses thereof, especially for the purposes of protective system.
The aqueous polymer dispersion that is used for anticorrosive coating is subjected to the restriction of multiple final condition, in order to ensure in the sufficient provide protection aspect the corrosion formation, must observe these final conditions.For example, because water is a kind of key component in corrosion process, so coating must have sufficient hydrophobicity and is diffused into the interface between base material and the coating to prevent water.In addition, also should guarantee effectively bonding between base material and the coating, so as to make since on base material/coating interface that the migration of the water under the corrosionproof protection coating causes formed bubble minimize.At last, this preservative coat reply carbonic acid gas has good diffusing barrier effect.The comonomer of the increased sticking power of determining in the prior art comprises undersaturated beta-diketonate compound, for example acetoacetic acid allyl ester and methacrylic acid acetoacetoxy ethyl ester.
In WO 99/14278, solved effective adherent problem of guaranteeing between base material and the coating by means of the acetoacetoxy group in the polymer.Poly-(alkylene imine) is added in the polymer dispersion liquid, and crosslinked with the acetoacetoxy group in film process, forms enamine.The anionic emulsifier of Jia Ruing can suppress the too early crosslinking reaction in the polymer dispersion liquid subsequently.In for example WO99/14275 and WO 99/14279, disclose equally with nonionic emulsifying agent labile cross linker system.In the latter's specification sheets, add nonionic emulsifying agent subsequently as stablizer.The phosphoric acid salt emulsifying agent is used for polymerization.The foaming tendency of resulting dispersion liquid is lower.
A shortcoming of these coating is need be subsequently by adding emulsifying agent to stablize the dispersion liquid of gained.According to disclosed embodiment, must add a large amount of relatively emulsifying agents so that realize required storage stability.On the one hand, it is expensive adding poly-(alkylene imine) emulsifying agent subsequently, and on the other hand, water-absorbent also can strengthen when emulsifier content increased in coating, and this antagonism corrosive nature is deleterious.In addition, the danger that also exists emulsifying agent to move to base material/coating interface and cause it that sticking power of base material is reduced.This is strengthening the absorptive coating foaming that also caused simultaneously.
At last, the amine in the aqueous solution forms the brown degraded product easily, and this product itself is unwanted and obviously can causes coating color-changing.Use described admixture preparation dispersion liquid subsequently, and need to use buffering system to reduce final pH value, this has all further increased the manufacturing cost of this product.
In WO 98/54256, described based on the polyamines of aqueous polymer dispersion and the mechanism of crosslinking of acetoacetoxy group.
US 5,122, and 566 disclose a kind of method for preparing grid, and this method is to implement by the aqueous emulsion polymerization in the presence of the phosphoric acid salt emulsifying agent and under the condition of pH<3.5.The described dispersion liquid of the document also comprises at least a water-fast, non-ionic tensio-active agent, and its pH value is adjusted in 7 to 10.5 the scope after polymerization.But openly can not improve the use of (methyl) acrylic acid acetoacetoxy derivative of sticking power.
EP-A-0 476 528 discloses a kind of method that is used for the preparation of industrialization grid, and the multipolymer of therein ethylene base aromatic compound and acrylate is by in the presence of seed polymer, under the condition of pH<3.5 and carry out the aqueous emulsion polymerization prepare in the presence of phosphoric acid salt emulsifying agent and water-fast, nonionogenic tenside.Except having at least a seed polymer, this method and US 5,122,566 disclosed methods are identical.According to EP-A-0 476 528, if do not use described at least a seed polymer, promptly according to US 5,122,566 method, the polymkeric substance that obtains in commercial production scale has very high coagulum content.
Therefore, target of the present invention provides a kind of aqueous polymer dispersion, it demonstrates higher erosion resistance in anticorrosive coating in the agglutination,cold test that carries out according to DIN 50017, this dispersion liquid can and can need not the expensive inconvenient synthetic method of prior art with the technical scale preparation and be prepared.
The characteristics of this polymeric membrane also should be to have high-clarity, promptly do not have the division scattering center that produces because of formation aggregation in polymerization process, thereby also can be used for transparent coating material.
According to the present invention, can realize the target of setting by a kind of aqueous polymer dispersion, this dispersion liquid has the solids component of 20 weight % to 74 weight %, preferred 40 weight % to 70 weight %, and contains at least a copolymer A that comprises the following compound of copolymerization attitude):
A) based on the monomeric gross weight that is used to prepare this multipolymer, at least a single or oligomeric ethylenically unsaturated monomers of 40 weight % to 99.95 weight %, preferred 60 weight % to 90 weight %, this monomer can carry out polymerization by the free radical emulsion polymerized,
B) based on the monomeric gross weight that is used to prepare this multipolymer, at least a ethylenic unsaturated monocarboxylic and/or the low poly carboxylic acid of 0.05 weight % to 10 weight %, preferred 0.05 weight % to 5 weight %, and/or its salt, and
C) based on the monomeric gross weight that is used to prepare this multipolymer, at least a other unsaturated monoprotic acid of ethylenic and/or the oligomeric acid of 0 weight % to 5 weight %, preferred 0.05 weight % to 2 weight %, it is derived from phosphoric acid, phosphonic acids, sulfuric acid and/or sulfonic acid and/or its salt
Wherein, based on the monomeric gross weight that is used to prepare this multipolymer, this dispersion liquid comprises the emulsifying agent that comprises phosphate group and/or phosphonyl group of at least 0.3 weight %, preferred 0.3 weight % to 5 weight %, and wherein at least aly contains described at least a monomer b) and (if existence) described at least a monomer c) pH 〉=4.7 of initial monomer emulsion feed.
The copolymer A that the present invention is used) glass transition temperature T gUsually in-35 ℃ to 80 ℃ scope, a preferred Tg is in 0 ℃ to 40 ℃ scope or two T gAt-30 ℃ to+20 ℃ (T g) and+40 ℃ to+80 ℃ (the 2nd T g) scope in.
The used copolymer A of property quality and quantity adjusting the present invention by the selection comonomer) glass transition temperature.
Monomer is a) to c) weight part preferably select to such an extent that only can make the glass transition temperature T of the multipolymer that constitutes by them gIn-35 ℃ to 80 ℃ scope.
Be surprised to find that aqueous dispersions of the present invention has the erosion resistance of remarkable improvement in according to the agglutination,cold test of DIN 50017 in the protective system that obtains.In addition, aqueous dispersions of the present invention less coagulum that occurs in polymerization process.Institute's dispersion liquid that obtains can be produced with technical scale zero defect ground, and (storage) stability of the anti-corrosive primer coating of preparing with their is improved.At last, use dispersion liquid of the present invention can produce coating with high gloss.
The preferred construction unit of this at least a multipolymer is α a), β-ethylenic unsaturated carboxylic acid and the ester that contains the alkanol of 1 to 18 carbon atom, the ester of preferred acrylic or methacrylic acid and methyl alcohol, ethanol, propyl alcohol, butanols, amylalcohol, 2-Ethylhexyl Alcohol, isooctyl alcohol, nonylcarbinol and n-dodecane alcohol.Other preferred monomer comprises vi-ny l aromatic monomers, for example vinylbenzene and alkyl derivative thereof, for example vinyl toluene, ethyl styrene and oligomeric (alkyl) vinylbenzene.In addition, the alkene of ethene, propylene, iso-butylene and so on, and the derivative of these compounds, for example ester of vinylchlorid, Vinyl Ether and (aliphatics) carboxylic acid and alkene, the ethylenic unsaturated ester of preferred vinyl-acetic ester or Versatic acid also can be used as structural unit a).
Used structural unit b) is undersaturated monocarboxylic acid of single or oligomeric ethylenic or low poly carboxylic acid and acid anhydrides thereof and/or their salt.Preferred vinylformic acid, methacrylic acid, methylene-succinic acid, toxilic acid and/or fumaric acid and their salt of using.If comprise structural unit b) and pH value<4.7 of water-based initial monomer emulsion feed c), just it must be increased to pH 〉=4.7 at least.This can finish as follows: with the structural unit b in the water) and (if use) c) structural unit d when suitable) and emulsifying agent and non-essential initiator add water-based initial monomer emulsion feed, and before remaining monomer of adding, the pH value is adjusted to pH 〉=4.7 with alkali.Can be in advance in the initial monomer emulsion feed, add the water miscible structural unit d of part), AAEMA for example.
The initial monomer emulsion feed is meant the mixture of the following material that is used to prepare monomer milk sap in the feed chute in the specification sheets: water, structural unit b), structural unit c) (if existence), emulsifying agent and non-essential structural unit d when suitable) and initiator.
For improving the pH value of initial monomer emulsion feed, preferably use sodium hydroxide and potassium hydroxide.Especially preferably use ammonia with in and the initial monomer emulsion feed because this alkali can volatilize the film forming of polymkeric substance after, the reduction polymer moieties water-absorbent.
Preferred construction unit c) is sodium, potassium and the ammonium salts of sulfuric acid, sulfonic acid, phosphoric acid and/or the unsaturated derivative of phosphonic ethylenic.Especially preferably use vinyl sulfonic acid sodium, 2-acrylamido-2-methyl propane sulfonic acid ( AMPS) salt and methacrylic acid sulfopropyl ester potassium.Especially preferably use ammonium salt, contain free acid because solidify the post polymerization thing at film, this free acid produces lower water-absorbent with respect to corresponding salt at polymer moieties.
When the weight part of mentioning as various (comonomer) structural unit of the ratio of at least a multipolymer, suppose that all comonomers are sneaked in this multipolymer by 100% ground.
Based on the monomeric gross weight that is used to prepare this multipolymer, aqueous polymer dispersion of the present invention also comprises the emulsifying agent that comprises phosphate group and/or phosphonyl group of at least 0.3 weight %, preferred 0.3 weight % to 5 weight %.This emulsifying agent preferably uses the form of ammonium, sodium and the sylvite of phosphoric acid ester and/or phosphonic acid ester.But the salt that also can use these compounds and other alkali to form.When using free phosphoric acid ester and/or phosphonic acid ester, can their (partly) original positions be neutralized to pH 〉=7 by the aqueous solution and alkali (preferably with the ammonia) reaction of emulsifying agent as base material.
The preferred ester of the adducts that comprises the emulsifying agent, particularly phosphoric acid of phosphate group and the ester of pure and mild phenol (also can be the form of mixture of monoesters, diester and three esters of phosphoric acid), phosphoric acid and pure and/or (alkyl) phenol and oxyethane and/or propylene oxide and sodium salt, sylvite and the ammonium salt of these compounds of using.These compounds can obtain from the commercial channel usually, and are for example commercial by name Berol 522 (alkylphosphonic acid carboxylic acid sylvite), Hostaphat 1306 (alkyl hangs down the polyethoxye phosphoric acid ester) and Berol 733 (alkylphenol hangs down the polyethoxye potassium phosphate salt).As the emulsifying agent that comprises phosphate group, can also use the ethylenic unsaturated ester of phosphoric acid and hydrocarbon and by the neutralized reaction product of its deutero-and alkali.
In a preferred embodiment; based on the monomeric gross weight that is used to prepare this multipolymer, at least a multipolymer of described aqueous dispersions also comprises 0.05 weight % to 10 weight %, the more preferably monomer d of the free redical polymerization that comprises at least one acetoacetoxy of 0.5 weight % to 3 weight % with the copolymerization attitude).
Preferred monomer d) be methacrylic acid acetoacetoxy ethyl ester (AAEMA) and vinylformic acid acetoacetoxy ethyl ester (AAEA).Can also use the etheric acid Vinyl Ether.According to the present invention, if monomer d) be that part is water miscible, for example under the situation that is AAEMA, they can also be with monomer b) to c) be included in the initial monomer emulsion feed.
Respectively based on the monomeric gross weight that is used to prepare this multipolymer, at least a multipolymer of described aqueous dispersions can also comprise 0 weight % to 10 weight % of copolymerization attitude, preferred 0 weight % to 2 weight %, the more preferably unsaturated reactive cross-linking monomer e of 0.05 weight % to 1 weight % at least a (list) or (oligomeric) ethylenic), and 0 weight % to 30 weight % of copolymerization attitude, but (list) or (oligomeric) ethylenically unsaturated monomers f of other copolymerization of preferred 0 weight % to 5 weight %) and 0 weight % to 5 weight %, preferred 0 weight % to 2 weight %, more preferably 0 weight % to 0.5 weight %'s can have reactive molecule g to polymkeric substance by similar polymer reaction).
As reactive cross-linking monomer e), i.e. crosslinked monomer in film process, the preferred unsaturated derivative of ethylenic that uses silane, for example vinyltrimethoxy silane, vinyltriethoxysilane, vinyl silane triisopropoxide, (γ-methacryloxypropyl) Trimethoxy silane, vinyl three (2-methoxy ethoxy) silane and γ-methacryloxypropyl three (2-methoxy ethoxy) silane.
Other suitable monomers e) the unsaturated derivative of other ethylenic of (methyl) glycidyl acrylate and/or Racemic glycidol is arranged, for example the glycidyl vinyl ether.
As monomer e), can also use diacetone-acryloamide(DAA).But should add two hydrazides co-crosslinkers in this case.Also can use the derivative of sheltering of N hydroxymethyl acrylamide, for example N-tert.-butoxy methyl acrylamide crosslinkedly.
As other monomer f), can use undersaturated nitrogen containing monomer, for example Methacrylamide and (methyl) vinylformic acid dimethylaminoethyl ester; The derivative of urea, for example vinylformic acid beta-carbamido ethyl ester, beta-carbamido Vinyl Ether and (methyl) vinylformic acid -hydroxy alkyl ester preferably use Methacrylamide.
Can also use dual functional (methyl) acrylate, two (methyl) vinylformic acid 1 for example, 4-and 1,3-butanediol ester and two (methyl) vinylformic acid 1,6-hexylene glycol ester, dual functional ethene derivatives, for example Vinylstyrene and divinyl, with (methyl) acrylate of trifunctional, trimethylolpropane trimethacrylate for example is as other unsaturated monomer f) to increase the elasticity of coating.
As structural unit g), generally can use material by the functional group reactions of similar polymer reaction and polymkeric substance.The present invention preferably uses epoxy silane, more preferably glycidoxypropyltrimewasxysilane, β-(3, the 4-epoxycyclohexyl) ethyl triethoxysilane, β-(3, the 4-epoxycyclohexyl) ethyl trimethoxy silane, perhaps oligomeric functional silane, for example 1-(triethoxysilyl)-2-(diethoxymethyl silyl) ethane or isocyanuric acid three [3-(trimethoxysilyl) propyl group] ester.
In another embodiment, based on the monomeric gross weight that is used to prepare this multipolymer, aqueous polymer dispersion of the present invention comprises 0 weight % to 5 weight %, preferred 0 weight % to 0.5 weight %, the more preferably UV-crosslinked material of 0 weight % to 0.3 weight %, and this material is not that ethylenic is undersaturated.Preferred ultraviolet-crosslinkable agent is methyl phenyl ketone, benzophenone and acetophenone derivs or the benzophenone derivates that does not comprise ethylenic unsaturated polymerizable group.The preferred especially derivative that uses at room temperature the benzophenone that exists with the liquid mixture form adds proper assistant where necessary, and reason is that these derivatives have the advantage on the performance.Can also use the phosphine oxide derivative.
Except comprising the emulsifying agent of phosphate group and/or phosphonyl group, aqueous polymer dispersion of the present invention can also comprise other emulsifying agent.Based on the monomeric total amount of polymkeric substance, the total amount of emulsifying agent is preferably at 0.3 weight % to 10 weight %, more preferably in the scope of 0.3 weight % to 3.5 weight %.Preferred other emulsifying agent is the emulsifying agent that comprises alkyl, aryl or alkylaryl group.Can use poly-(oxyethane), poly-(propylene oxide) or poly-(ethylene oxide/propylene oxide) as the spacer groups between hydrocarbon free radical and the terminal polar group.Outside phosphate group and/or phosphonyl group emulsifying agent, other ionic emulsifying agent of less preferred use based on vitriol/ester, sulfonate/ester and/or carboxylate salt/ester.Except phosphate group and/or phosphonyl group emulsifying agent, also can use non-ionic co-emulsifier.Preferably adding emulsifying agent before the polymerization and/or between polymerization period.But can also in final dispersion liquid, add ionic and emulsifying agent nonionic, to increase its stability.It is low as far as possible that the amount of used emulsifying agent should keep, so that the water-absorbent of coating minimizes.
In another embodiment, based on the monomeric gross weight that is used to prepare this multipolymer, aqueous polymer dispersion of the present invention comprises the protective colloid of 0 weight % to 5 weight %, preferred 0 weight % to 1 weight %.Can use the protective colloid of the known and suitable the object of the invention of all those skilled in the art.But preferably use water miscible carboxymethyl cellulose, more preferably use the form of its ammonium salt or an alkali metal salt.The example of commercially available prod comprises Blanose 7M, Blanose 7UL, Blanose 7EL and Ambergum 3021 (Aqualon).In due course, this carboxymethyl cellulose also can have other substituting group, for example alkyl or hydroxyalkyl, alkoxyalkyl and dialkyl amido.Example has methyl carboxymethyl cellulose, ethyl carboxymethyl cellulose, hydroxyethyl carboxymethyl cellulose, hydroxypropyl carboxy methyl Mierocrystalline cellulose, methoxyethyl carboxymethyl cellulose and ethoxyethyl carboxymethyl cellulose.
In addition,, also can use macromolecular compound, for example polyvinyl alcohol, polyvinylpyrrolidone, polyacrylamide, PMAm or poly carboxylic acid, and their an alkali metal salt and/or ammonium salt as protective colloid.
In another embodiment preferred, based on the monomeric gross weight that is used to prepare this multipolymer, aqueous polymer dispersion of the present invention comprises the dispersion agent of 0 weight % to 10 weight %, preferred 0.05 weight % to 3 weight %, preferred polymeric dispersion agent.As dispersion agent, can use well known by persons skilled in the art and be suitable for any dispersion agent of the object of the invention.The example is water-soluble poly-(methyl) vinylformic acid and/or their alkali metal salts or ammonium salt.But the preferred dispersion agent that uses, for example water solubility copolymer of vinyl aromatic compound (particularly vinylbenzene) and ethylenic unsaturated carboxylic acid and/or their acid anhydrides (particularly maleic anhydride) with hydrophobic parts.The form of preferred especially corresponding ammonium salt of these multipolymers and an alkali metal salt.Can between polymerization period or even before polymerization with they part or all of addings.According to its trade(brand)name, can for example use The SMA resin, for example Cray Valley produces SMA 3000HNa.
If desired, aqueous polymer dispersion of the present invention can also comprise film coalescence aid, for example butyldiglycol and petroleum solvent, such as softening agent and/or other auxiliary agent of dimethyl phthalate and dibutyl phthalate, for example inhibiter, urethane and Polyacrylate thickeners, sanitas, the defoamer such as mineral oil antifoam agent or silicon oil foam killer, wetting agent and other for example often are used to prepare the additive of coating material.
The present invention not only provides aqueous polymer dispersion, but also Its Preparation Method And Use is provided, especially for the purposes of rust proof paint.
Can prepare this multipolymer according to the method for free radical suspension well known by persons skilled in the art, miniemulsion, microemulsion and emulsion polymerized.But preferred manufacturing procedure is the emulsion polymerized method of carrying out in water.Aqueous polymer dispersion by the preparation of this method be multipolymer of the present invention form preferably is provided.
Therefore; preferably under condition well known by persons skilled in the art, in aqueous medium, in the presence of free radical formation initiator and emulsifying agent; and suitably the time in the presence of protective colloid, conditioning agent and other auxiliary agent, prepare described at least a multipolymer by the free radical emulsion polymerized.
By the emulsion polymerized method of routine, in the presence of the protective colloid of monomer at emulsifying agent, initiator and suitably the time in aqueous phase emulsification, and preferably polymerization in 25 to 95 ℃ temperature range of this milk sap.Can be according to method known to those skilled in the art, for example in batches or the emulsion feed method carry out this emulsion polymerized, preferred emulsion feed method, wherein add partial monosomy milk sap as initial charge, and before the form with the monomer aqueous emulsion is metered into residual monomers, finish polymerization.Preferred list (milk sap) chargings that are metered into two or more different compositions continuously.This generation makes the polymeric film of gained have the multistage polymkeric substance of variform.The preparation method of this multistage polymkeric substance is for example having description among the EP-A-0 795 568.Suitable multistage polymkeric substance has lower minimum film-forming temperature (MFFTs) than the homogeneity polymkeric substance of same monomer component, so more preferably.Because MFFT is lower, consequently can significantly reduce consumption volatile, environmentally harmful film coalescence aid.In addition, can prepare multistage polymkeric substance with form with special resistance to blocking.Perhaps, can be metered into monomer with constant or the rapid monomer composition that changes as known according to the power feed method.One or more emulsifying agents not only, and the protective colloid that uses when suitable can be included in the initial charge that (partly) add reactor, and/or are metered into monomer milk sap (partly).
In the method for the invention, can use one or more initial monomer emulsion feed.According to the present invention, comprise described at least a monomer b) and the described at least a monomer c suitably the time) pH value 〉=4.7 of initial emulsion feed, preferred 4.7 to 11, more preferably 4.7 to 8, and preferred especially 5 to 7.
Usually emulsifying agent is added with the initial monomer emulsion feed, different initial monomer emulsion feed can comprise different emulsifying agents.
Contain described at least a monomer b) the initial monomer charging preferably contain the emulsifying agent of phosphoric acid group.
Preferred especially use comprise monomer a), b) and (if use) c) and the initial monomer charging of the emulsifying agent of phosphoric acid group.
In the initial monomer emulsion feed is under two or more the situation, preferably its pH value all 〉=4.7, preferred 4.7 to 11, and more preferably 5 to 7.
Preferably in pH value 〉=4.7, preferred 4.7 to 11, and more preferably carry out polymerization under 5 to 7 the condition.
Use oil soluble and/or water miscible radical initiator or redox initiator system to cause and carry out polymerization.Preferably use for example Potassium Persulfate, Sodium persulfate or ammonium peroxydisulfate, hydrogen peroxide, dibenzoyl peroxide, lauryl peroxide, tertbutyl peroxide, azo isobutyronitrile and other azo initiators, use with reductive agent in due course, for example sodium bisulfite, Rongalit, glucose, xitix or tartrate.Based on the monomeric gross weight that is used to prepare multipolymer, the amount of used polymerization starter is 0.1 weight % to 10 weight % respectively, preferred 0.1 weight % to 1 weight %.
In addition, can also use conditioning agent, for example mercaptan preferably uses n-dodecane mercaptan, thiophenol and 2-methyl-5-tert.-butylbenzene thiophenol in the case.Based on the monomeric gross weight that is used to prepare multipolymer, the amount of used one or more conditioning agents is generally 0 weight % to 1 weight %.
Usually use ammoniacal liquor or alkali hydroxide soln that the final pH value of aqueous dispersions is adjusted to 6 to 10.
Can be by adding common additive, pigment, softening agent and other additive suitably the time, for example weighting agent, dispersion agent, thickening material, corrosion-inhibiting pigment, inhibiter, wetting agent, ultraviolet inhibitor, ultraviolet initiator and/or other polymeric binder are mixed with coating composition with aqueous dispersions of the present invention.They especially are suitable for producing and using undyed or painted coating, for example antirust coating, transparent coating material, gloss varnish and decorative coveringn, and these coatings require to improve base material sticking power.Owing in the synthetic resins preparation, have phosphate group, and may have wet adhesion promoter (for example acetoacetoxy) in due course, thereby guarantee that base material sticking power is improved.Especially preferably use AAEMA and/or AAEA functional monomer in this article as described at least a multipolymer.The suitable substrates preferable alloy, more preferably steel, but also inorganic silicate surface and timber.In addition, the acetoacetoxy of any existence has guaranteed that coating of the present invention has lower bonding tendency, promptly when the desiccated surface that two have been handled through coating is pressed together, seldom might bond.If use reactive cross-linking monomer e) replacement monomer d), also can realize effective base material sticking power.Measure the minimum film-forming temperature (MFFT) of polymkeric substance according to DIN-ISO 2115.Measure the glass transition temperature (T of polymkeric substance by DSC (dsc) g).Heating and cooling speed is respectively 200 ℃/min, and the temperature range that covers is-60 ℃ to+130 ℃.In second heating period, measure the glass transition temperature (mid point evaluation) of polymkeric substance.By using the Fox equation, can estimate the glass transition temperature (consult T.G.Fox, Bull.Am.Phys.Soc. (Ser.II), 1,123[1956]) of this polymkeric substance highly approx.By monomer a), b) and the multiple glass transition temperature of the homopolymer that c) constitutes all be known, and at for example J.Brandrup, E.M.Immergut, " polymer handbook " (Polymer Handbook), second edition in 1975, J.Wiley lists among the NewYork.
Explain the present invention below with reference to exemplary example approach, but these embodiments not limitations of the present invention.
Embodiment 1 to 10:
The preparation of multipolymer aqueous dispersions:
A) preparation of initiator solution:
The 3.75g Potassium Persulphate is dissolved in 96.25g deionized water (DI water).
B) polymerization
The preparation of monomer milk sap
Monomer milk sap (initial monomer emulsion feed): use the stirrer have propeller stirrer with the speed of 1000rpm the 28.8g AAEMA thorough mixing with the emulsifying agent that is used for monomer milk sap (seeing Table 1) of successive 491.2g deionized water, described amount, 19.2g methacrylic acid and suitably the time.Subsequently, where necessary, use the NH of 12.5% concentration of described amount (seeing Table 1) 4OH adjusts to 5 with the pH value.
Final monomer solution: add the mixture of 480g methyl methacrylate and 480g n-butyl acrylate subsequently, and with the speed of 1000rpm with resulting emulsifying mixture 10 minutes.
Have in the glass reactor of anchor stirrer at 3L, under the stirring velocity of 120rpm, the emulsifying agent that is used for initial charge of successive 526.4g deionized water and described amount (seeing Table 1) is heated to 80 ℃, add 15.1g initiator solution (a) and 37g monomer milk sap then, and stirred this mixture 15 minutes.Can observe reaction significantly from the heat of emitting.By outside water-bath the internal temperature of this reactor is remained on 80 to 82 ℃ continuously.Subsequently, add residual monomers milk sap by isolating dropping funnel continuous measurement in 180 minutes time, continuous measurement adds remaining initiator solution in 195 minutes time.After being metered into end, continue heating 1 hour at 80 ℃ again, then this milk sap is cooled to room temperature.Under 30 ℃ of temperature, use the ammoniacal liquor of 12.5% concentration that the pH value is adjusted to 7 to 8.
Table 1
Embodiment ??1 ??(comp.) ??2 ??3 ??(comp.) ?4 ?(comp.) ??5 ??(comp.) ??6 ??7 ??(comp.) ??8 ??(comp.) ??9 ??(comp.) ??10
The pH value of monomer milk sap (is used for neutral concentration and is 12.5% NH 4The amount of OH [g]) ??<4.5 ??5/29.25 ??<4.5 ??5/27.4 ??<4.5 ??5/28.7 ??<4.5 ??5/30.08 ??<4.5 ??5/32.6
Hostaphat?BV 1(amount of monomer milk sap/initial charge [g]) ??13.82/ ??6.91 ??13.82/ ??6.91 ??13.82/ ??6.91 ??13.82/ ??6.91
Hostaphat?1308 2(amount of monomer milk sap/initial charge [g]) ??9.6/4.8 ??9.6/4.8 ??9.6/4.8 ??9.6/4.8
Berol?733 3(amount of monomer milk sap/initial charge [g]) ??21.89/ ??10.94 ??21.89/ ??10.94
AAEMA[g] ??28.8 ??28.8 ??28.8 ??28.8 ??28.8 ??28.8
The particle diameter of aerosil dw [mm] ??164 ??116 ??111 ??112 ??158 ??118 ??113 ??122 ??118 ??118
Wet coagulum [g] ??88.7 ??0.6 ??6.23 ??7.29 ??1.5 ??0 ??0 ??0 ??0 ??0
Tg:[℃] ??18.3 ??15.2 ??19.9 ??17.9 ??20.6 ??20.6 ??17.0 ??14.2 ??22.9 ??18.5
MFFT:[℃] ??10 ??6 ??9 ??9 ??10 ??10 ??10 ??9 ??9 ??9
The solids content of measuring [%] ??46.5 ??46.4 ??46.2 ??46.7 ??47.2 ??47.2 ??47.4 ??46.9 ??46.8 ??46.5
Comp.: Comparative Examples
1: three sec-butyl phenol seven (ethylene glycol) ether sodium sulfates (about 50% form)
2: isotridecyl eight (ethylene glycol) ether list or bisphosphate (about 100% form)
3: the 4-nonylphenol gathers (ethylene glycol) ether phosphoric acid monopotassium salt (about 35% form)
Be increased to 5 by pH value, and AAEMA be incorporated into polymkeric substance, significantly reduced the coagulum part (comprising) of sieving and removing by 180 μ m sieve attached to the coagulum on the agitator by copolymerization with monomer milk sap solution.By comparative example 1 and example 2 and example 1 and example 6 this point as can be seen.
Embodiment 11
Use the copolymer dispersion of embodiment 1 to 10 to prepare antirust linging formulation.
Table 2:
Mashed prod Weight part
Borchigel L 75 (aqueous solution of 5% concentration) ?4.40
Water ?8.00
?AMP?90 ?0.15
?Surfynol?SE-F ?0.30
?Additol?VXW?4973 ?0.30
?Ser?Ad?FA?179 ?0.15
?Heucophos?Zp?10 ?6.40
?Microtalc?AT?extra ?6.40
?Bayferrox?130?M ?5.50
?Millicarb ?4.00
?35.60
Tackiness agent
Embodiment 1 to 10 (about 47%) ?47.20
Water ?15.80
?Texanol ?1.40
?100.00
Under agitation in 8g water, add 4.4g concentration and be the aqueous solution of 5% Borchigel L 75.Add AMP 90, Surfynol SE-F, Additol VXW 4973 and Ser Ad FA 179 then.Add Heucophos ZPIO, Microtalc AT extra, Bayferrox 130 M and Millicarb continuously according to the amount shown in the table 2 then, then in dissolver with this mixture of VELOCITY SHEAR of 5000rpm 20 minutes.
After at room temperature storing 1 day, dispersion liquid (solids content is about 47%), water and the Texanol with embodiment 1 to 10 adds in the described mashed prod with described amount, and stirs final coating 10 minutes under 500rpm.In embodiment 11k to 11l, (see Table 3), before the preparation lacquering, with the SMA of 1.44 weight % (based on thick attitude polymer dispersion liquid) (CrayValley provides form to 3000HNa solution: about 25% solid) add in each dispersion liquid.
Table 3
Priming paint ??11a ??11b ??11c ??11d ??11e ????11f ??11g ??11h ??11i ??11j ??11k ????11l
Dispersion liquid embodiment ??1 ??2 ??3 ??4 ??5 ????6 ??7 ??8 ??9 ??10 ??5 ????6
Additive in the dispersion liquid ??- ??- ??- ??- ??- ????- ??- ??- ??- ??- 1.44 SMA 3000 HNa of weight % 1.44 SMA 3000 HNa of weight %
Embodiment 12:
The antirust coating test under the constant condensing condition of DIN 50017 and the storage stability of priming paint formulation
The Wound-rotor type scraping blade (the about 100 μ m of wet-film thickness, the about 50 μ m of build) that uses 100 μ m is administered to the priming paint of embodiment 11 on the steel plate galvanized, and dry under the relative humidity of 23 ℃ temperature and 50%.Measure build then, and use the cut stylus the center, whole length upper edge of specimen and the longitudinal axis abreast onboard cut make the distance of itself and panel edges maintenance 30mm to base material.In deriving from the alternately climatic test device of Weiss, under the relative humidity of 40 ℃ temperature and 100%, experimentize, exposure duration is 864 hours.Calculate corrosion control index as referred to herein (CCI) by following formula:
CCI=(4 * bubbles volume+1 * bubble size+1 * rusting rate)/6
Each evaluation is to carry out to the rank of 5 (non-constants) from 0 (very good), and therefore, best CCI is 0, and the poorest CCI is 5.Bubbles volume, bubble size and rusting rate are measured according to DIN 53209 and DIN 53210.
Priming paint was at room temperature stored 3 months in the PE container of sealing, measured its storage stability.Estimate on 1 to 5 rank, wherein the excellent storage stability of 1 expression does not deposit any weighting agent and pigment, and the very serious deposition of 5 expressions, and can form slurries.
Table 4
Priming paint ??11a ??11b ?11c ????11d ?11e ????11f ??11g ????11h 11i ??11j ?11k ?11l
??V 1 ??P 1 ?V 1 ????V 1 ?V 1 ????P 2 ??V 1 ????V 1 V 1 ??P 2 ?V 2 ?P 2
Dispersion liquid embodiment ??1 ??2 ?3 ????4 ?5 ????6 ??7 ????8 9 ??10 5+1.44 SMA 3000 HNa of weight % 6+1.44 SMA 3000 HNa of weight %
The pH value of monomer milk sap ??<4.5 ??5 ?<4.5 ????5 ?<4.5 ????5 ??<4.5 ????5 <4.5 ??5 ?<4.5 ?5
The milk sap dispersion liquid ??Ph 3 ??Ph 3 ?S 4 ????S 4 ?Ph 3 ????Ph 3 ??S 4 ????S 4 Ph 3 ??Ph 3 ?Ph 3 ?Ph 3
AAEMA ??- ??- ?- ????- ?+ ????+ ??+ ????+ + ??+ ?+ ?+
CCI ??0.58 ??0.54 ?1.5 ????1.25 ?1 ????0.6 ??1.42 ????0.9 - ??0.29 ?0.54 ?0.5
The storage stability of priming paint ??5 ??4 ?4 ????2 ?4 ????3 ??4 ????3 Coagulum ??3 ?4 ?1
1: the V=Comparative Examples; 2: the P=inventive embodiments; 3: the phosphate group emulsifying agent; 4: vitriol/ester emulsifying agent
Have been found that the stability of using dispersion liquid of the present invention to improve rust-proofing primer.This dispersion liquid the pH value be 5 and therefore with carboxylic acid monomer's group (partly) neutral condition under use the preparation of monomer milk sap.Priming paint 11i just condenses just added tackiness agent in preparation priming paint process after, and formulation 11j of the present invention is stable.
Show (referring to table 4) as the result, owing to have AAEMA in the polymkeric substance, the stability of coating is further enhanced, and, in this dispersion liquid, add the storage stability that styrene-maleic anhydride copolymer has further improved the rust-proofing primer that comprises tackiness agent.This material that adds has subsequently obviously improved the stability of this anti-corrosive primer.
With comprise hydroxy-acid group b) the initial monomer emulsion feed be not adjusted to pH 〉=4.7 and the polymer phase ratio of preparation, the dispersion liquid of the present invention in the rust-proofing primer has significantly improved rust-proof effect surprisingly in the test of constant condensing condition.Only comprise unit b with use by existing this feature of phosphate group emulsifying agent) and the combining of the initial monomer emulsion feed of pH 〉=4.7, just obtained dispersion liquid of the present invention, it has low coagulum content, and in priming paint, demonstrate good storage stability, extraordinary rustless property in constant condensing condition test.

Claims (26)

1.一种聚合物水分散液,该分散液具有20重量%至74重量%、优选40重量%至70重量%的固体成分,并含有至少一种包含共聚态的以下化合物的共聚物A):1. An aqueous polymer dispersion having a solids content of 20% by weight to 74% by weight, preferably 40% by weight to 70% by weight, and containing at least one copolymer comprising the following compounds in the copolymerized state A) : a)基于用于制备该共聚物的单体的总重量,40重量%至99.95重量%、优选60重量%至90重量%的至少一种单或低聚烯键式不饱和单体,该单体可通过自由基乳状液聚合进行聚合,a) 40% to 99.95% by weight, preferably 60% to 90% by weight, based on the total weight of the monomers used to prepare the copolymer, of at least one mono- or oligomeric ethylenically unsaturated monomer, the mono- or oligomeric ethylenically unsaturated monomer The body can be polymerized by free radical emulsion polymerization, b)基于用于制备该共聚物的单体的总重量,0.05重量%至10重量%、优选0.05重量%至5重量%的至少一种烯键式不饱和单羧酸和/或低聚羧酸,和/或其盐,以及b) 0.05% to 10% by weight, preferably 0.05% to 5% by weight, based on the total weight of the monomers used to prepare the copolymer, of at least one ethylenically unsaturated monocarboxylic and/or oligomeric carboxylic acid acids, and/or their salts, and c)基于用于制备该共聚物的单体的总重量,0重量%至5重量%、优选0.05重量%至2重量%的至少一种其它的烯键式不饱和一元酸和/或低聚酸,其衍生自磷酸、膦酸、硫酸、和/或磺酸和/或其盐,c) 0% to 5% by weight, preferably 0.05% to 2% by weight, based on the total weight of the monomers used to prepare the copolymer, of at least one other ethylenically unsaturated monobasic acid and/or oligomeric Acids derived from phosphoric, phosphonic, sulfuric, and/or sulfonic acids and/or salts thereof, 其中in 基于用于制备该共聚物的单体的总重量,该分散液包含至少0.3重量%、优选0.3重量%至5重量%的包含磷酸基团和/或膦酸基团的乳化剂,并且其中至少一种含有所述至少一种单体b)和如果存在的所述至少一种单体c)的初始单体乳状液进料的pH≥4.7。The dispersion comprises at least 0.3% by weight, preferably 0.3% to 5% by weight, of emulsifiers comprising phosphoric acid groups and/or phosphonic acid groups, based on the total weight of the monomers used to prepare the copolymer, and wherein at least An initial monomer emulsion feed comprising said at least one monomer b) and, if present, said at least one monomer c) has a pH > 4.7. 2.如权利要求1所述的聚合物水分散液,其中所述共聚物A)具有至少一个在-35℃至80℃范围内的玻璃态转化温度Tg。2. The aqueous polymer dispersion according to claim 1, wherein the copolymer A) has at least one glass transition temperature Tg in the range -35°C to 80°C. 3.如权利要求1所述的聚合物水分散液,其中在所述共聚物A)中含有作为结构单元a)的共聚形式的α,β-烯键式不饱和羧酸与包含1至18碳原子的烷醇的酯,优选丙烯酸和甲基丙烯酸与甲醇、乙醇、丙醇、丁醇、戊醇、2-乙基己醇、异辛醇、正癸醇及正十二烷醇的酯,以及苯乙烯。3. The aqueous polymer dispersion according to claim 1, wherein the copolymer A) contains as structural unit a) in copolymerized form an α,β-ethylenically unsaturated carboxylic acid containing 1 to 18 Esters of alkanols with carbon atoms, preferably acrylic and methacrylic acid esters with methanol, ethanol, propanol, butanol, pentanol, 2-ethylhexanol, isooctyl alcohol, n-decanol and n-dodecanol , and styrene. 4.如权利要求1所述的聚合物水分散液,其中在所述共聚物A)中含有作为结构单元b)的共聚态的单烯键式不饱和或低聚烯键式不饱和单羧酸或低聚羧酸及其酸酐和/或其盐,优选丙烯酸、甲基丙烯酸、衣康酸、马来酸和/或富马酸及其盐。4. The aqueous polymer dispersion as claimed in claim 1, wherein said copolymer A) contains monoethylenically unsaturated or oligoethylenically unsaturated monocarboxylic acids in a copolymerized state as structural unit b) Acids or oligomeric carboxylic acids and their anhydrides and/or their salts, preferably acrylic acid, methacrylic acid, itaconic acid, maleic acid and/or fumaric acid and their salts. 5.如权利要求1所述的聚合物水分散液,其中在所述共聚物A)中含有作为结构单元c)的共聚态的钠盐、钾盐和铵盐形式的硫酸、磺酸、磷酸和/或膦酸的烯键式不饱和衍生物,特别是酯,优选乙烯磺酸钠、2-丙烯酰胺基-2-甲基丙烷磺酸(AMPS)盐以及甲基丙烯酸磺丙酯钾。5. The aqueous polymer dispersion as claimed in claim 1, wherein in said copolymer A) contain sulfuric acid, sulfonic acid, phosphoric acid in the form of sodium salt, potassium salt and ammonium salt as structural unit c) and/or ethylenically unsaturated derivatives of phosphonic acids, especially esters, preferably sodium ethylene sulfonate, 2-acrylamido-2-methylpropanesulfonic acid (AMPS) salt and potassium sulfopropyl methacrylate. 6.如权利要求1所述的聚合物水分散液,其中含有磷酸与醇和(烷基)苯酚的酯,适当时可为磷酸的单酯、二酯和三酯的混合物,磷酸与醇或(烷基)苯酚和环氧乙烷和/或环氧丙烷的加合物的酯,这些化合物的钠盐、钾盐和铵盐,或者这些化合物与其它碱形成的盐,作为包含磷酸基团的乳化剂。6. Aqueous polymer dispersion as claimed in claim 1, wherein containing phosphoric acid and alcohol and (alkyl) phenol ester, can be the mixture of monoester, diester and triester of phosphoric acid when appropriate, phosphoric acid and alcohol or ( Esters of adducts of alkyl)phenols and ethylene oxide and/or propylene oxide, the sodium, potassium and ammonium salts of these compounds, or the salts of these compounds with other bases, as phosphoric acid group-containing emulsifier. 7.如权利要求1所述的聚合物水分散液,其中基于用于制备所述共聚物A)的单体的总重量,共聚物A)还包括共聚态的0.05重量%至10重量%、更优选0.5重量%至3重量%的至少一种包含至少一个乙酰基乙酰氧基的可自由基共聚单体d),优选甲基丙烯酸乙酰基乙酰氧基乙基酯(AAEMA)以及丙烯酸乙酰基乙酰氧基乙基酯(AAEA)或乙酰乙酸乙烯醚。7. The polymer aqueous dispersion as claimed in claim 1, wherein based on the total weight of the monomers used to prepare the copolymer A), the copolymer A) further comprises 0.05% by weight to 10% by weight of the copolymerized state, More preferably 0.5% to 3% by weight of at least one radically comonomer d) comprising at least one acetoacetoxy group, preferably acetoacetoxyethyl methacrylate (AAEMA) and acetyl acrylate Acetoxyethyl ester (AAEA) or vinyl acetoacetate. 8.如权利要求1所述的聚合物水分散液,其中分别基于用于制备所述共聚物A)的单体的总重量,共聚物A)还含有共聚态的最高可达10重量%、优选最高可达2重量%、更优选0.05重量%至1重量%的至少一种(单)或(低聚)烯键式不饱和共聚态反应性交联单体e),共聚态的最高可达30重量%、优选最高可达5重量%的其它可共聚(单)或(低聚)烯键式不饱和单体f),共聚态的最高可达5重量%、优选至多2重量%、更优选最高可达0.5重量%可通过类似聚合物反应对聚合物具有反应性的结构单元g)。8. The aqueous polymer dispersion according to claim 1, wherein based on the total weight of the monomers used to prepare the copolymer A), the copolymer A) also contains up to 10% by weight of the copolymerized state, Preferably up to 2% by weight, more preferably from 0.05% to 1% by weight, of at least one (mono) or (oligo)ethylenically unsaturated copolymerizable reactive crosslinking monomer e), copolymerized up to 30% by weight, preferably up to 5% by weight of other copolymerizable (mono) or (oligomeric) ethylenically unsaturated monomers f), in the copolymerized state up to 5% by weight, preferably up to 2% by weight, more Preference is given to up to 0.5% by weight of structural units g) which are reactive towards polymers via polymer-like reactions. 9.如权利要求1所述的聚合物水分散液,其中在所述共聚物A)中含有作为反应性交联单体e)的硅烷的烯键式不饱和衍生物,特别是共聚态的乙烯基三甲氧基硅烷、乙烯基三乙氧基硅烷、乙烯基三异丙氧基硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷、乙烯基三(2-甲氧基乙氧基)硅烷和γ-甲基丙烯酰氧基丙基三(2-甲氧基乙氧基)硅烷,或者(甲基)丙烯酸缩水甘油酯和/或缩水甘油基的其它烯键式不饱和衍生物,特别是缩水甘油基乙烯基醚。9. The aqueous polymer dispersion according to claim 1, wherein ethylenically unsaturated derivatives of silanes, in particular copolymerized ethylene, are contained as reactive crosslinking monomers e) in the copolymer A) Trimethoxysilane, Vinyltriethoxysilane, Vinyltriisopropoxysilane, γ-Methacryloxypropyltrimethoxysilane, Vinyltris(2-methoxyethoxy ) silane and γ-methacryloxypropyltris(2-methoxyethoxy)silane, or glycidyl (meth)acrylate and/or other ethylenically unsaturated derivatives of glycidyl , especially glycidyl vinyl ether. 10.如权利要求1所述的聚合物水分散液,其中在所述共聚物A)中含有作为单体f)的不饱和的含氮单体,特别是共聚态的甲基丙烯酰胺和(甲基)丙烯酸二甲基氨基乙基酯,脲的衍生物,例如丙烯酸β-脲基乙基酯、β-脲基乙烯醚和(甲基)丙烯酸φ-羟烷基酯,和/或双官能的(甲基)丙烯酸酯,特别是二(甲基)丙烯酸1,4-和1,3-丁二醇酯以及二(甲基)丙烯酸1,6-己二醇酯,双官能的乙烯衍生物,特别是二乙烯基苯和/或丁二烯,和三官能的(甲基)丙烯酸酯,例如三羟甲基丙烷三甲基丙烯酸酯,10. The aqueous polymer dispersion as claimed in claim 1, wherein in the copolymer A), contain as monomer f) an unsaturated nitrogen-containing monomer, particularly copolymerized methacrylamide and ( Dimethylaminoethyl meth)acrylate, urea derivatives such as β-ureidoethyl acrylate, β-ureido vinyl ether and φ-hydroxyalkyl (meth)acrylate, and/or bis Functional (meth)acrylates, especially 1,4- and 1,3-butanediol di(meth)acrylate and 1,6-hexanediol di(meth)acrylate, difunctional vinyl derivatives, especially divinylbenzene and/or butadiene, and trifunctional (meth)acrylates, such as trimethylolpropane trimethacrylate, 11.如权利要求1所述的聚合物水分散液,其中在所述至少一种共聚物A)中含有作为结构单元g)的通过类似聚合物反应与聚合物的官能团反应的物质,优选环氧硅烷,更优选缩水甘油氧基丙基三甲氧基硅烷、β-(3,4-环氧环己基)乙基三乙氧基硅烷、β-(3,4-环氧环己基)乙基三甲氧基硅烷,或者低聚官能的硅烷,特别是1-(三乙氧基甲硅烷基)-2-(二乙氧基甲基甲硅烷基)乙烷和/或异氰脲酸三[3-(三甲氧基甲硅烷基)丙基]酯。11. The aqueous polymer dispersion according to claim 1, wherein in the at least one copolymer A) there are substances, preferably ring Oxysilane, more preferably glycidoxypropyltrimethoxysilane, β-(3,4-epoxycyclohexyl)ethyltriethoxysilane, β-(3,4-epoxycyclohexyl)ethyl Trimethoxysilane, or oligomeric functional silanes, especially 1-(triethoxysilyl)-2-(diethoxymethylsilyl)ethane and/or tris[isocyanurate 3-(Trimethoxysilyl)propyl] ester. 12.如权利要求1所述的聚合物水分散液,其中基于用于制备所述共聚物A)的单体的总重量,含有最高可达5重量%、优选最高可达0.5重量%、更优选最高可达0.3重量%的紫外交联物质,该物质不是烯键式不饱和的,优选苯乙酮、二苯甲酮及不包含烯键式不饱和可聚合基团的苯乙酮衍生物或二苯甲酮衍生物,更优选在室温下以液体混合物形式存在的二苯甲酮的衍生物,在合适时可加入适当的助剂,或者氧化膦衍生物。12. The aqueous polymer dispersion according to claim 1, wherein based on the total weight of the monomers used to prepare the copolymer A), it contains up to 5% by weight, preferably up to 0.5% by weight, more Preference is given to up to 0.3% by weight of UV crosslinking substances which are not ethylenically unsaturated, preferably acetophenone, benzophenone and acetophenone derivatives which do not contain ethylenically unsaturated polymerizable groups Or benzophenone derivatives, more preferably benzophenone derivatives that exist in the form of a liquid mixture at room temperature, and appropriate additives or phosphine oxide derivatives can be added when appropriate. 13.如权利要求1所述的聚合物水分散液,除含有磷酸基团和/或膦酸基团的乳化剂之外,还含有其它乳化剂,基于共聚物A)的单体的总量,乳化剂的总量优选在0.3重量%至10重量%、更优选0.3重量%至3.5重量%的范围内,优选包含烷基、芳基或烷基芳基的乳化剂,可以使用聚(环氧乙烷)、聚(环氧丙烷)或聚(环氧乙烷/环氧丙烷)作为烃自由基和极性端基之间的间隔基团。13. The aqueous polymer dispersion according to claim 1, which, in addition to emulsifiers containing phosphoric acid groups and/or phosphonic acid groups, also contains other emulsifiers, based on the total amount of monomers in the copolymer A) , the total amount of emulsifier is preferably in the range of 0.3% by weight to 10% by weight, more preferably 0.3% by weight to 3.5% by weight, preferably emulsifiers containing alkyl, aryl or alkylaryl groups, poly(cyclic oxyethylene), poly(propylene oxide) or poly(ethylene oxide/propylene oxide) as a spacer between the hydrocarbon radical and the polar end group. 14.如权利要求1所述的聚合物水分散液,其中基于用于制备所述共聚物A)的单体的总重量,还包括最高可达5重量%、优选最高可达1重量%的保护胶体,优选使用水溶性的羧甲基纤维素,更优选使用其铵盐或碱金属盐的形式,或者在必要时带有其它取代基、特别是烷基或羟烷基、烷氧基烷基以及二烷基氨基的羧甲基纤维素,优选甲基羧甲基纤维素、乙基羧甲基纤维素、羟乙基羧甲基纤维素、羟丙基羧甲基纤维素、甲氧基乙基羧甲基纤维和乙氧基乙基羧甲基纤维素,和/或聚乙烯醇、聚乙烯吡咯烷酮、聚丙烯酰胺、聚甲基丙烯酰胺或聚羧酸以及它们的碱金属盐和/或铵盐。14. The aqueous polymer dispersion according to claim 1, wherein based on the total weight of the monomers used to prepare the copolymer A) also comprises up to 5% by weight, preferably up to 1% by weight of Protective colloid, preferably water-soluble carboxymethylcellulose, more preferably in the form of its ammonium or alkali metal salts, or if necessary with other substituents, especially alkyl or hydroxyalkyl, alkoxyalkane Carboxymethyl cellulose with radical and dialkyl amino groups, preferably methyl carboxymethyl cellulose, ethyl carboxymethyl cellulose, hydroxyethyl carboxymethyl cellulose, hydroxypropyl carboxymethyl cellulose, methoxy ethyl carboxymethyl cellulose and ethoxy ethyl carboxymethyl cellulose, and/or polyvinyl alcohol, polyvinyl pyrrolidone, polyacrylamide, polymethacrylamide or polycarboxylic acid and their alkali metal salts and / or ammonium salts. 15.如权利要求1所述的聚合物水分散液,基于用于制备所述共聚物A)的单体的总重量,还含有最高可可达10重量%、优选0.05重量%至3重量%的分散剂,优选具有疏水性部分的分散剂,特别是苯乙烯与烯键式不饱和羧酸和/或其酸酐的水溶性共聚物,更优选其相应的铵盐和碱金属盐的形式。15. The aqueous polymer dispersion according to claim 1 , based on the total weight of the monomers used to prepare the copolymer A), further comprising up to 10% by weight, preferably 0.05% to 3% by weight, of Dispersants, preferably with hydrophobic moieties, especially water-soluble copolymers of styrene and ethylenically unsaturated carboxylic acids and/or anhydrides thereof, more preferably in the form of their corresponding ammonium and alkali metal salts. 16.一种通过自由基悬浮液、微粒乳状液、微乳状液或乳状液聚合制备如权利要求1所述的聚合物水分散液的方法,包括如下步骤:16. A method for preparing the polymer aqueous dispersion as claimed in claim 1 by free radical suspension, microemulsion, microemulsion or emulsion polymerization, comprising the steps of: i)首先向聚合反应器中加入至少一种含有如权利要求1所述的单体a)和/或b)和/或c)的初始单体乳状液进料,i) initially adding at least one initial monomer emulsion feed containing monomers a) and/or b) and/or c) as claimed in claim 1 in the polymerization reactor, ii)非必要地加入至少一种其它的初始单体乳状液进料,该进料含有共聚物A)的其它组成共聚单体,并ii) optionally adding at least one other initial monomer emulsion feed containing other constituent comonomers of copolymer A), and iii)以常规方式进行聚合,其包括iii) Polymerization is carried out in a conventional manner, which includes iv)在基于用于制备所述共聚物的单体的总重量的至少0.3重量%、优选0.3重量%至5重量%的包含磷酸基团和/或膦酸基团的乳化剂的存在下进行聚合,并包括:iv) in the presence of at least 0.3% by weight, preferably 0.3% to 5% by weight, based on the total weight of the monomers used to prepare the copolymer, of an emulsifier comprising phosphoric acid groups and/or phosphonic acid groups Aggregate, and include: v)所述至少一种含有所述至少一种单体b)和如果存在的所述至少一种单体c)的初始单体乳状液进料的pH≥4.7。v) pH of said at least one initial monomer emulsion feed containing said at least one monomer b) and, if present, said at least one monomer c) > 4.7. 17.如权利要求16所述的方法,其中使用碱,优选氢氧化钠或氢氧化钾并特别优选使用氨水,将所述至少一种含有组分b)和如果存在的组分c)的初始单体乳状液进料的pH值调节到≥4.7。17. The process as claimed in claim 16, wherein the at least one initial compound containing component b) and, if present, component c) is converted using a base, preferably sodium hydroxide or potassium hydroxide and particularly preferably ammonia water. The pH of the monomer emulsion feed was adjusted to > 4.7. 18.如权利要求16所述的方法,其中将所述至少一种初始单体乳状液进料的pH值调节到5.0至7.0的范围内。18. The method of claim 16, wherein the pH of the at least one initial monomer emulsion feed is adjusted to be in the range of 5.0 to 7.0. 19.如权利要求16所述的方法,其中所述共聚物A)是在水溶性介质中、在自由基形成性引发剂和乳化剂的存在下、以及必要时在保护胶体、调节剂和其它助剂的存在下,通过自由基乳状液聚合制备的。19. The process as claimed in claim 16, wherein the copolymer A) is in an aqueous medium, in the presence of free-radical forming initiators and emulsifiers, and if necessary in the presence of protective colloids, regulators and other Prepared by free radical emulsion polymerization in the presence of additives. 20.如权利要求16所述的方法,其中单体是在水相中、在乳化剂、引发剂和适当时的保护胶体的存在下进行乳化的,并且在25至95℃的温度范围内进行聚合,该乳化聚合以分批方式进行,或者,优选以乳状液进料方法进行,其中部分单体乳状液被包含在该初始进料中,并且在完成聚合之后再以单体水乳浊液的形式计量加入剩余的单体。20. A process as claimed in claim 16, wherein the monomers are emulsified in an aqueous phase in the presence of emulsifiers, initiators and where appropriate protective colloids, and carried out at a temperature ranging from 25 to 95°C Polymerization, the emulsion polymerization is carried out in batch mode or, preferably, in the emulsion feed method, wherein part of the monomer emulsion is contained in the initial charge, and after the polymerization is completed, it is carried out as an aqueous monomer emulsion metered in the remaining monomer in the form of 21.如权利要求16所述的方法,其中连续加入两种或多种不同组成的单体(乳状液)进料。21. The process as claimed in claim 16, wherein two or more monomer (emulsion) feeds of different composition are added continuously. 22.如权利要求16所述的方法,其中使用油溶性和/或水溶性的自由基引发剂或氧化还原引发剂系统引发并实施聚合,优选过二硫酸钾、过二硫酸钠或过二硫酸铵、过氧化氢、过氧化二苯甲酰、月桂基过氧化物、叔丁基过氧化氢、偶氮异丁腈及其他偶氮引发剂,在适当时与还原剂一起使用,特别是亚硫酸氢钠、羟基甲烷亚磺酸的钠盐、葡萄糖、抗坏血酸或酒石酸。22. The method according to claim 16, wherein the polymerization is initiated and carried out using an oil-soluble and/or water-soluble free-radical initiator or redox initiator system, preferably potassium peroxodisulfate, sodium peroxodisulfate or peroxodisulfate Ammonium, hydrogen peroxide, dibenzoyl peroxide, lauryl peroxide, tert-butyl hydroperoxide, azoisobutyronitrile and other azo initiators, used together with reducing agents when appropriate, especially Sodium bisulfate, sodium salt of hydroxymethanesulfinic acid, dextrose, ascorbic acid, or tartaric acid. 23.如权利要求16所述的方法,其中分别基于用于制备所述共聚物A)的单体的总重量,所用聚合引发剂的量为0.1重量%至10重量%,优选0.1%至1重量%。23. The method as claimed in claim 16, wherein the amount of polymerization initiator used is 0.1% by weight to 10% by weight, preferably 0.1% to 1% by weight, respectively based on the total weight of the monomers used to prepare the copolymer A) weight%. 24.如权利要求16所述的方法,其中还使用其它调节剂,特别是硫醇,进行乳状液聚合,优选基于用于制备所述共聚物A)的单体的总重量,以最高可达1重量%的量使用正十二烷硫醇、苯硫酚以及2-甲基-5-叔丁基苯硫酚。24. The process as claimed in claim 16, wherein further regulators, in particular mercaptans, are also used for the emulsion polymerization, preferably based on the total weight of monomers used to prepare the copolymer A) up to n-dodecanethiol, thiophenol and 2-methyl-5-tert-butylthiophenol were used in an amount of 1% by weight. 25.如权利要求16所述的方法,其中使用氨水或碱金属氢氧化物溶液将水分散液的最终pH值调节到6至10。25. The method of claim 16, wherein the final pH of the aqueous dispersion is adjusted to 6 to 10 using ammonia or alkali metal hydroxide solution. 26.如权利要求1所述的聚合物分散液的用途,用作防腐蚀涂料中的粘合剂。26. Use of the polymer dispersion according to claim 1 as a binder in anticorrosion coatings.
CNB038192098A 2002-08-08 2003-07-21 Aqueous polymer dispersions, method for the production thereof and use thereof, especially in anti-corrosion coatings Expired - Fee Related CN100345869C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10236395.1 2002-08-08
DE2002136395 DE10236395A1 (en) 2002-08-08 2002-08-08 An aqueous polymer dispersion containing copolymerisate obtained by free radical polymerization useful for coatings having high corrosion and condensation resistance

Publications (2)

Publication Number Publication Date
CN1688614A true CN1688614A (en) 2005-10-26
CN100345869C CN100345869C (en) 2007-10-31

Family

ID=30469599

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB038192098A Expired - Fee Related CN100345869C (en) 2002-08-08 2003-07-21 Aqueous polymer dispersions, method for the production thereof and use thereof, especially in anti-corrosion coatings

Country Status (4)

Country Link
JP (2) JP4979192B2 (en)
CN (1) CN100345869C (en)
DE (1) DE10236395A1 (en)
WO (1) WO2004020477A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107619456A (en) * 2016-07-14 2018-01-23 陶氏环球技术有限责任公司 With phosphoric acid and the latex of photoinitiator group functionalization
WO2018218631A1 (en) 2017-06-02 2018-12-06 Dow Global Technologies Llc Waterborne epoxy coating composition
CN112513173A (en) * 2018-04-02 2021-03-16 聚合物绿色有限责任公司 Method for producing biodegradable superabsorbent polymers with high absorbency under load based on styrene maleic acid copolymers and biopolymers
CN114341217A (en) * 2019-10-07 2022-04-12 Dic株式会社 Water-based resin composition, water-based paint, and plastic molded article coated with the water-based paint

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1582567B2 (en) * 2004-04-01 2011-11-16 Rohm And Haas Company Aqueous coating composition
ES2340197T3 (en) 2005-07-01 2010-05-31 F. Hoffmann-La Roche Ag CARBOXILATED LATEX PARTICLES.
EP1762601A1 (en) 2005-09-12 2007-03-14 Basf Aktiengesellschaft Method to increase resistance against stain penetration of aqueous coating compositions
DE102007033596A1 (en) 2007-07-19 2009-01-22 Celanese Emulsions Gmbh Coatings with high weathering resistance, process for their preparation and their use
DE102007033595A1 (en) 2007-07-19 2009-01-22 Celanese Emulsions Gmbh Polyvinyl ester dispersions, process for their preparation and their use
DE102007059844A1 (en) * 2007-12-12 2009-06-25 Basf Construction Polymers Gmbh Copolymer based on a sulfonic acid-containing compound
US9102848B2 (en) 2011-02-28 2015-08-11 Basf Se Environmentally friendly, polymer dispersion-based coating formulations and methods of preparing and using same
CN103773142B (en) * 2014-01-20 2015-12-02 南通华新环保设备工程有限公司 A kind of equipment Environmentally-frieantirust antirust paint and preparation method thereof
CN105541225A (en) * 2015-12-25 2016-05-04 常熟市奇越新型建材科技有限公司 Dry powder coating for plastering walls
CN106867347B (en) * 2017-04-05 2020-04-24 武汉迪赛环保新材料股份有限公司 Temporary antirust liquid for hot-rolled H-shaped steel
CN107478767B (en) * 2017-09-05 2019-09-06 中国科学院长春应用化学研究所 A method for measuring the content of long-chain fatty alcohol in organic phosphonic acid solution
CN108017972B (en) * 2017-11-24 2020-04-07 鹤山市信兴化工有限公司 Organosilicon modified acrylic polyurethane hybrid emulsion and water-based paint prepared from same
BR112020025078A2 (en) * 2018-07-12 2021-03-23 Dow Global Technologies Llc aqueous dispersion, aqueous dispersion preparation process, and aqueous coating composition
CN111286312A (en) * 2020-02-20 2020-06-16 中国石油天然气股份有限公司 Slow-release corrosion and scale inhibitor capsule for oil well and preparation method thereof
CN113201087B (en) * 2020-11-20 2022-08-19 联固新材料科技(广州)有限公司 Hydroxyacrylic dispersions, process for their preparation and two-component polyurethane paints
FR3117794B1 (en) * 2020-12-23 2023-07-28 Oreal Aqueous dispersion of a specific copolymer and its cosmetic applications
WO2022136114A1 (en) * 2020-12-23 2022-06-30 L'oreal Aqueous dispersion of a specific copolymer, and cosmetic uses thereof
CN114591665B (en) * 2021-12-28 2022-11-01 天津市新丽华色材有限责任公司 Low-VOC emulsion type water-based aluminum mirror back coating
CN115960427B (en) * 2022-12-21 2025-03-14 德爱威(中国)有限公司 Organic-inorganic hybrid polymer hydrogel, preparation method thereof and exterior wall heat preservation intermediate paint
CN117567688B (en) * 2024-01-15 2024-04-05 星宇新材料股份有限公司 Butyronitrile emulsion and synthesis method and application thereof

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4968741A (en) * 1989-10-06 1990-11-06 The Goodyear Tire & Rubber Company Latex for coatings having reduced blushing characteristics
US5990224A (en) * 1997-09-18 1999-11-23 Eastman Chemical Company Stable low foam waterborne polymer compositions containing poly(alkyleneimines)
DE19810658A1 (en) * 1998-03-12 1999-11-25 Basf Ag Aqueous polymer dispersion containing an emulsifier with phosphate groups

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107619456A (en) * 2016-07-14 2018-01-23 陶氏环球技术有限责任公司 With phosphoric acid and the latex of photoinitiator group functionalization
CN107619456B (en) * 2016-07-14 2022-03-29 陶氏环球技术有限责任公司 Latex functionalized with phosphoric acid and photoinitiator groups
WO2018218631A1 (en) 2017-06-02 2018-12-06 Dow Global Technologies Llc Waterborne epoxy coating composition
CN110612335A (en) * 2017-06-02 2019-12-24 陶氏环球技术有限责任公司 Aqueous epoxy coating composition
AU2017416631B2 (en) * 2017-06-02 2020-10-22 Dow Global Technologies Llc Waterborne epoxy coating composition
US11186743B2 (en) 2017-06-02 2021-11-30 Dow Global Technologies Llc Waterborne epoxy coating composition
CN112513173A (en) * 2018-04-02 2021-03-16 聚合物绿色有限责任公司 Method for producing biodegradable superabsorbent polymers with high absorbency under load based on styrene maleic acid copolymers and biopolymers
CN114341217A (en) * 2019-10-07 2022-04-12 Dic株式会社 Water-based resin composition, water-based paint, and plastic molded article coated with the water-based paint

Also Published As

Publication number Publication date
CN100345869C (en) 2007-10-31
JP4979192B2 (en) 2012-07-18
DE10236395A1 (en) 2004-02-19
JP2005534799A (en) 2005-11-17
JP2011225893A (en) 2011-11-10
WO2004020477A1 (en) 2004-03-11

Similar Documents

Publication Publication Date Title
CN100345869C (en) Aqueous polymer dispersions, method for the production thereof and use thereof, especially in anti-corrosion coatings
CN107266626B (en) A kind of multiple self-crosslinking core-shell type lotion of room temperature and its preparation method and application
CN102115517B (en) Preparation method for anti-rust soap-free acrylate emulsion
EP0157928B1 (en) Aqueous dispersion of vinyl copolymer resin
CN101809047B (en) Crosslinkable monomers and polymers and their use
US9139677B2 (en) Composite polymer emulsion
CA2848062C (en) Hydroxyethyl cellulose grafted acrylic latex
CN101283041B (en) Aqueous dispersion
CN101970545A (en) Method for producing composite particles
CN109153739B (en) Amine functional anionic polymer dispersions and coating compositions thereof
WO2011073417A1 (en) Aqueous emulsion
AU2014415515A1 (en) Aqueous emulsion paint with improved stain removal and anticlogging properties
CN103509419A (en) Wood protection paints
WO2001096485A1 (en) Water borne binder composition
AU2016411502A1 (en) Coating composition with improved liquid stain repellency
KR20120008322A (en) High weather resistance acrylic emulsion resin and coating composition comprising the same
JPH0674369B2 (en) Method for producing aqueous dispersion of vinyl copolymer resin
JP2000026514A (en) Aqueous polymer dispersion, rust resisting coating and coated base material
CN114316160A (en) Acrylic emulsion polymer and preparation method of water-based paint based on polymer
KR20040011551A (en) Aqueous resin dispersion, process for producing the same, and use
JP4514258B2 (en) Silicone-containing aqueous coating agent composition
CN111154346A (en) Acrylate emulsion for building interior wall coating and preparation method and application thereof
RU2260602C1 (en) Method for preparing styrene-acrylic copolymers aqueous dispersions
JP2022540029A (en) Alcohol-resistant removable floor care composition
CN116396425A (en) Acrylic emulsion for road and bridge asphalt waterproofing material and its preparation method and application

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20071031

Termination date: 20130721

点击 这是indexloc提供的php浏览器服务,不要输入任何密码和下载