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.