EP3430065A1 - Dispersion polymère multiphasique aqueuse à particules fines, procédé pour sa préparation et son utilisation comme liant - Google Patents

Dispersion polymère multiphasique aqueuse à particules fines, procédé pour sa préparation et son utilisation comme liant

Info

Publication number
EP3430065A1
EP3430065A1 EP17710541.8A EP17710541A EP3430065A1 EP 3430065 A1 EP3430065 A1 EP 3430065A1 EP 17710541 A EP17710541 A EP 17710541A EP 3430065 A1 EP3430065 A1 EP 3430065A1
Authority
EP
European Patent Office
Prior art keywords
polymer
weight
stage
monomers
polymerization
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.)
Pending
Application number
EP17710541.8A
Other languages
German (de)
English (en)
Inventor
Roelof Balk
Bastiaan LOHMEIJER
Robert Wrazidlo
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.)
BASF SE
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Publication of EP3430065A1 publication Critical patent/EP3430065A1/fr
Pending legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10—Esters
    • C08F220/12—Esters of monohydric alcohols or phenols
    • C08F220/16—Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms
    • C08F220/18—Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms with acrylic or methacrylic acids
    • C08F220/1804—C4-(meth)acrylate, e.g. butyl (meth)acrylate, isobutyl (meth)acrylate or tert-butyl (meth)acrylate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/12—Polymerisation in non-solvents
    • C08F2/16—Aqueous medium
    • C08F2/22—Emulsion polymerisation
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10—Esters
    • C08F220/12—Esters of monohydric alcohols or phenols
    • C08F220/14—Methyl esters, e.g. methyl (meth)acrylate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F265/00—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00
    • C08F265/04—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00 on to polymers of esters
    • C08F265/06—Polymerisation of acrylate or methacrylate esters on to polymers thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F285/00—Macromolecular compounds obtained by polymerising monomers on to preformed graft polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/04—Oxygen-containing compounds
    • C08K5/07—Aldehydes; Ketones
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D151/00—Coating compositions based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Coating compositions based on derivatives of such polymers
    • C09D151/003—Coating compositions based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Coating compositions based on derivatives of such polymers grafted on to macromolecular compounds obtained by reactions only involving unsaturated carbon-to-carbon bonds
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/02—Emulsion paints including aerosols
    • C09D5/024—Emulsion paints including aerosols characterised by the additives
    • C09D5/027—Dispersing agents
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40—Additives
    • C09D7/65—Additives macromolecular
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02—Monomers containing only one unsaturated aliphatic radical
    • C08F212/04—Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F212/06—Hydrocarbons
    • C08F212/08—Styrene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10—Esters
    • C08F220/26—Esters containing oxygen in addition to the carboxy oxygen
    • C08F220/28—Esters containing oxygen in addition to the carboxy oxygen containing no aromatic rings in the alcohol moiety
    • C08F220/283—Esters containing oxygen in addition to the carboxy oxygen containing no aromatic rings in the alcohol moiety and containing one or more carboxylic moiety in the chain, e.g. acetoacetoxyethyl(meth)acrylate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10—Esters
    • C08F220/34—Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate
    • C08F220/36—Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate containing oxygen in addition to the carboxy oxygen, e.g. 2-N-morpholinoethyl (meth)acrylate or 2-isocyanatoethyl (meth)acrylate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L79/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
    • C08L79/02—Polyamines

Definitions

  • the present invention relates to multistage aqueous polymer dispersions which exhibit excellent film formation at low temperatures, processes for their preparation, and their use as binders for the coating of subgreens.
  • Aqueous polymer dispersions are well known. These are fluid systems which contain a disperse phase in the form of a dispersed phase in an aqueous dispersion medium consisting of a plurality of intertwined polymer chains, the so-called polymer matrix or polymer particles, in disperse distribution.
  • the middle one is a disperse phase in the form of a dispersed phase in an aqueous dispersion medium consisting of a plurality of intertwined polymer chains, the so-called polymer matrix or polymer particles, in disperse distribution.
  • the diameter of the polymer particles is frequently in the range from 10 to 1000 nm, in particular in the range from 30 to 300 nm.
  • Aqueous polymer dispersions are used as binders in a large number of industrial applications. If they are used as a binder for coatings of substrates is one of the important requirements for such coatings that they have a high hardness and thus have a good scratch and block resistance. For environmental reasons, a filming of the binder in the range of ⁇ 0 to 40 ° C is sought, so that no or only small amounts of a film-forming aid are needed. If the binders are used in aqueous opaque coatings such as gloss or silk gloss for Do-It-Yourself (DIY) applications, film-forming auxiliaries must not be used as they evaporate during drying and pollute the environment.
  • DIY Do-It-Yourself
  • aqueous binders for DIY applications contain no components that require labeling or that the amounts of such components used in the binders are so low that they need not be labeled, since such components - from a certain levels - cause skin contact with allergic reactions, such as certain biocide components or additives.
  • multi-stage binders are used for these applications which have a low minimum film-forming temperature and lead to high hardness after drying. From EP-B 0 710 680 it is known that by multi-stage emulsion polymerization, it is possible to prepare polymer dispersions which have a low minimum film-forming temperature (MFT) and form films with good blocking resistance. In the formulations for glazes or silk gloss paints described in this document, film-forming aids are used.
  • WO 2012/130712 A1 describes multistage aqueous polymer dispersions which are film-forming at low temperatures but nevertheless produce films of high hardness and excellent blocking resistance and which are also distinguished by good wet adhesion and storage stability. Also described are methods for their preparation and their use as binders for the coating of substrates. The preparation takes place in the presence of emulsifiers; The crosslinking system used is diacetone acrylamide (DAAM) and adipic dihydrazide (ADDH).
  • DAAM diacetone acrylamide
  • ADH adipic dihydrazide
  • WO 95/29963 A1 describes a process for preparing an aqueous, crosslinkable polymer composition which is free from organic solvents.
  • the composition comprises an acid-functional oligomer A having a Tg of 10 to 125 ° C, crosslinkable functional groups and a polymer B having a Tg of at least 25 ° C below that of the polymer A.
  • the polymer compositions are characterized by a good balance of lower MFT and higher hardness. Achieving the good performance of these binders in the applications described was only possible by using DAAM as the crosslinking monomer and ADDH as the crosslinking additive.
  • an aqueous polymer coating composition comprising at least one vinyl polymer A having a weight average molecular weight Mw in the range from 1000 to 150,000 g / mol and an acid number> 5 mg KOH / g and a vinyl polymer B with a weight average the molecular weight Mw of at least 80,000 g / mol and an acid number of ⁇ 35 mg KOH / g.
  • DAAM is used as crosslinking monomer and ADDH as crosslinking additive.
  • WO 2012/084974 A1 describes an aqueous polymer dispersion comprising a vinyl polymer having at least two phases, comprising: A) 40 to 90% by weight of a vinyl polymer A having a glass transition temperature in the range from -50 to 30 ° C and B) from 10 to 60 % By weight of a vinyl polymer B having a glass transition temperature in the range of 50 to 130 ° C, wherein the vinyl polymer A contains 0.1 to 10 wt .-% of at least one acid-functional olefinically unsaturated monomer, wherein at least 20 wt .-% be used of the vinyl polymer, to form a vinyl polymer, and the vinyl polymer B is derived from at least one biologically derived regenerative olefinically unsaturated monomer.
  • EP 0 338 486 A2 describes a process for preparing stabilized latex, characterized by the steps of: a) mixing latex-forming monomers under emulsion polymerization conditions to form, in a first step, a hydrophilic low molecular weight polymer reaction mixture which, due to a pH adjustment can become water soluble; b) contacting the reaction mixture containing the first-stage polymer with latex-forming monomers under emulsion polymerization conditions to form in a second step a hydrophobic polymer forming an inverse core-shell emulsion with the first-stage polymer; and c) adjusting the pH of the emulsion to dissolve the first stage polymer as well as the prepared latex.
  • the diamine used in these publications causes after drying a crosslinking with the existing acetoacetoxy groups; because of its boiling point ⁇ 250 ° C, however, it contributes to the VOC content of the formulation (Volatile Organic Compound (s)).
  • EP 0916707 A1 describes aqueous coating compositions comprising an emulsion polymer having improved open time.
  • the polymer may, inter alia, have acetoacetoxy functionality;
  • the compositions also contain a polyether mono- or diamine.
  • WO 2012/140042 A1 describes a process for preparing aqueous vinyl polymer dispersions which have good film-forming properties, good stability and clarity, and a polymer dispersions obtainable by the process, and coating compositions prepared from the polymer dispersions.
  • the polymer dispersions prepared in this document are optionally hydroplasticized by the addition of a base only after the polymerization of the second step.
  • EP 2 371 870 A1 describes a multistage emulsion polymer comprising 10 to 30% by weight, based on the weight of the multistage emulsion polymer, of a shell, of a first polymer having an acid number of 5 to 100 .mu.K KOH / g of polymer, the first polymer has a calculated Mn of 1000 to 4500 Da and a calculated Tg of less than 100 ° C, and from 70 to 90% by weight, based on the weight of the multistage emulsion polymer, of a core of a second polymer having a Acid number from 0 to half the acid number of the first polymer, wherein the second polymer has a calculated Mn greater than 20,000 Da.
  • no crosslinking monomers are used in the context of the present invention.
  • crosslinking monomer in both polymerization stages, as well as a subsequent addition of an at least tri-functional alkoxylated amine is not disclosed in any of the documents.
  • DAAM is used as crosslinking monomer
  • ADDH crosslinking additive. If one waives ADDH, one finds that a crack-free filming, especially in pigmented formulations, is not readily available. In addition, you do not reach the desired hardness and other properties such as water resistance, wet grip and mechanical strength are no longer found at the desired level. By suitable measures, such as adjustment of the glass transition temperatures, one can improve the film formation, but usually loses very quickly the desired high hardness of the films.
  • the coating systems In addition to good film formation and high hardness, the coating systems must of course have a number of other properties. A very important requirement for DIY applications is a good water resistance of the coating shortly after it has dried: it must not swell if it is exposed to water and has no surface damage after re-drying. Without further measures, the emulsion polymers described above would have insufficient early water resistance.
  • the object of the present invention was to produce emulsion polymers which, when used in aqueous coating compositions, at low temperatures without the use of film-forming auxiliaries, allow formation of crack-free films which have high hardness and blocking resistance as well as excellent early water resistance.
  • the object is achieved by a very finely divided polymer dispersion, obtainable by at least one two-stage emulsion polymerization, wherein
  • composition comprising
  • (Meth) acrylic acid (cyclo) alkyl esters the vinyl aromatic having up to 20 carbon atoms, a radically polymerizable compound selected from the group of ethylenically unsaturated nitriles having up to 20 carbon atoms, vinyl esters containing up to 20 carbon atoms Carboxylic acids, vinyl halides having up to 10 carbon atoms and vinyl ethers of alcohols containing 1 to 10 carbon atoms
  • a hydrophobic polymer P2 is prepared by free-radical polymerization from a second composition in the presence of the polymer P1 treated under 2)
  • (Meth) acrylic acid (cyclo) alkyl esters the vinyl aromatic having up to 20 carbon atoms, a radically polymerizable compound selected from the group of ethylenically unsaturated nitriles having up to 20 carbon atoms, vinyl esters containing up to 20 carbon atoms Carboxylic acids, vinyl halides having up to 10 carbon atoms and vinyl ethers of alcohols containing 1 to 10 carbon atoms
  • the object is also achieved by a process for the preparation of the polymer dispersion according to the invention, wherein at least one two-stage emulsion polymerization is carried out, comprising the steps:
  • a coating composition in the form of an aqueous composition containing i) at least one polymer dispersion according to the invention, ii) optionally at least one organic filler and / or one organic pigment, iii) optionally an additive, iv ) Water, dissolved.
  • the object is also achieved by the use of the polymer dispersion according to the invention for coating compositions or paints.
  • the implementation of free-radically initiated emulsion polymerizations of monomers, in particular unsaturated monomers, in an aqueous medium has been described many times and is therefore sufficiently known to the person skilled in the art [cf. for this emulsion polymerization in Encyclopedia of Polymer Science and Engineering, Vol. 8, pages 659 et seq. (1987); DC Blackley, in High Polymer Latices, Vol. 1, pp. 35 et seq. (1966); H. Warson, The Applications of Synthetic Resin Emulsions, Chapter 5, pages 246 et seq. (1972); D.
  • the free-radically initiated aqueous emulsion polymerization reactions are usually carried out by dispersing the (ethylenically unsaturated) monomers with the concomitant use of dispersants in the aqueous medium in the form of monomer droplets and polymerizing them by means of a free-radical polymerization initiator.
  • two-stage emulsion polymerization can be understood as meaning an emulsion polymerization in which free-radical emulsion polymerization takes place in a first stage and the monomers comprising the first composition polymerize completely to give a polymer, optionally followed by neutralization with a base The polymerization is then followed by at least one further stage in which new monomers are polymerized by means of a free-radical emulsion polymerization in the presence of the polymer from the first stage to form a polymer.
  • "1)" corresponds to the first stage and "3" ) "of the second stage in the emulsion polymerization.
  • the addition of the monomers of the second stage can take place in the sense of a gradient procedure.
  • the gradient mode of operation for the purposes of the present invention is understood as meaning an emulsion polymerization in which one or more monomers are metered in at a non-constant rate.
  • continuous changes in speed can also be carried out without much additional effort.
  • a "polymer” can be understood as meaning a mixture of polymers which is formed from monomers to form macromolecules during a formation reaction.
  • the term (organic) organic includes inorganic and / or organic.
  • the preparation of the polymer dispersion may take place in the presence of at least one surfactant compound.
  • a detailed description of suitable protective colloids can be found in Houben-Weyl, Methods of Organic Chemistry, Volume XIV / 1, Macromolecular Materials, Georg Thieme Verlag, Stuttgart, 1961, p. 41 1 to 420.
  • Suitable emulsifiers are also found in Houben-Weyl, Methods of Organic Chemistry, Volume 14/1, Macromolecular Materials, Georg Thieme Verlag, Stuttgart, 1961, pages 192 to 208.
  • Suitable emulsifiers are both anionic, cationic and nonionic emulsifiers.
  • Emulsifiers whose relative molecular weights are usually below those of protective colloids are preferably used as surface-active substances.
  • nonionic emulsifiers are araliphatic or aliphatic nonionic emulsifiers, for example ethoxylated mono-, di- and trialkylphenols (EO degree: 3 to 50, alkyl radical: C4-C10), ethoxylates of long-chain alcohols (EO degree: 3 to 100, alkyl radical: C) 8 -C 3 6) and polyethylene oxide / polypropylene oxide homo- and copolymers. These may comprise the alkylene oxide units randomly distributed or in copolymerized form in the form of blocks. Well suited z. B. EO / PO block copolymers.
  • Ethoxylates of long-chain alkanols (alkyl radical C 1 -C 30, average degree of ethoxylation 5 to 100) and, with particular preference, those having a linear C 12 -C 20 -alkyl radical and a mean degree of ethoxylation of from 10 to 50 and ethoxylated monoalkylphenols are preferably used.
  • Suitable anionic emulsifiers are, for example, alkali metal and ammonium salts of alkyl sulfates (alkyl radical: C8-C22), of sulfuric monoesters of ethoxylated alkanols (EO degree: 2 to 50, alkyl radical: C12-C18) and ethoxylated alkylphenols (EO degree: 3 to 50, alkyl radical: C4-C9), of alkylsulfonic acids (alkyl radical: C12-C18) and of alkylarylsulfonic acids (alkyl radical: Cg-Cis) or alkylbenzylsulfonic acids, alkaline earth alkylbenzenesulfonates, sulfonated fatty acids, sulfonated olefins, sulfonated diephenyl ethers, sulfosuccinates, fatty alcohol sulfates, alkylphenol sulfates, al
  • emulsifiers can be found in Houben-Weyl, Methods of Organic Chemistry, Volume XIV / 1, Macromolecular substances, Georg-Thieme-Verlag, Stuttgart, 1961, pp. 192-208.
  • anionic emulsifiers are bis (phenylsulfonic acid) ethers or their alkali metal or ammonium salts which carry a C 4 -C 2 -alkyl group on one or both aromatic rings. These compounds are well known, for. From US-A-4,269,749, and commercially available, for example as Dowfax® 2A1 (Dow Chemical Company).
  • Suitable cationic emulsifiers are preferably quaternary ammonium halides, e.g. B. trimethylcetylammonium chloride, methyltrioctylammonium chloride, Benzyltriethylammonium- chloride or quaternary compounds of N-C6-C2o-alkylpyridines, -morpholinen or - imidazoles, z. B. N-Laurylpyridinium chloride.
  • emulsifiers it is also possible to use those which are incorporated into the polymer during the free-radical polymerization. These are generally compounds which carry at least one free-radically polymerizable group, preferably selected from the group consisting of allyl, acrylate, methacrylate and vinyl ether, and at least one emulsifying group, preferably selected from the group indicated above.
  • incorporatable Bisomer® brand emulsifiers such as Bisomer® MPEG 350 MA from Geo Specialty Chemicals, USA, Hitenol® BC-20 (APEO), Hitenol® BC-2020, Hitenol® KH-10 or Noigen® RN-50 (APEO) from Dai-Ichi Kogyo Seiyaku Co., Ltd., Maxemul® 6106, Maxemul® 61 12, Maxemul® 5010, Maxemul® 501 1 from Croda, Sipomer® PAM 100, Sipomer® PAM 200, Sipomer ® PAM 300, Sipomer® PAM 4000, Sipomer® PAM 5000 from Rhodia, Adeka® Reasoap® PP-70, Adeka® Reasoap® NE-10, Adeka® Reasoap® NE-20, Adeka® Reasoap® NE-30, Adeka ® Reasoap® NE-40
  • co-polymerizable emulsifiers can also be used, as described in EP 14185506.4. According to the invention, however, both the polymerization of the first stage and the polymerization of the second stage take place completely or almost emulsifier-free. Preferably, a total of less than 2.5 or less than 2.0 wt .-% emulsifier, in particular less than 1, 5 wt .-%, based on the solids content of the polymer dispersion used.
  • the polymer of the first stage is used, which is converted in situ by the addition of neutralizing agent from a non-protective as a protective colloid, water-insoluble polymer in a protective colloid effective, water-soluble or water-swollen polymer.
  • the emulsion polymerization of the first and second stage can be started with water-soluble initiators.
  • Water-soluble initiators are, for example, ammonium and alkali metal salts of peroxodisulfuric acid, for example sodium peroxodisulfate, hydrogen peroxide or organic peroxides, for example tert-butyl hydroperoxide.
  • the redox initiator systems consist of at least one usually inorganic reducing agent and one inorganic or organic oxidizing agent.
  • the oxidation component is, for example, the initiators for emulsion polymerization already mentioned above.
  • the reduction components are, for example, alkali metal salts of sulfurous acid, such as sodium sulfite, sodium hydrogen sulfite, alkali metal salts of sulfurous acid such as sodium disulfite, bisulfite addition compounds of aliphatic aldehydes and ketones such as acetone bisulfite or reducing agents such as hydroxymethanesulfinic acid and its salts, or ascorbic acid.
  • the red-ox initiator systems can be used with the concomitant use of soluble metal compounds whose metallic component can occur in multiple valence states.
  • Typical redox initiator systems are, for example, ascorbic acid / iron (II) sulfate / sodium peroxydisulfate, tert-butyl hydroperoxide / sodium disulfite, tert-butyl hydroperoxide / Na-hydroxymethanesulfinic acid.
  • the individual components for example the reduction component, may also be mixtures, for example a mixture of the sodium salt of hydroxymethanesulfinic acid and sodium disulfite.
  • the initiators mentioned can be used in the form of aqueous solutions, the lower concentration being determined by the amount of water acceptable in the dispersion and the upper concentration by the solubility of the compound in question in water.
  • concentration of initiators 0.1 to 30 wt .-%, preferably 0.2 to 20% by weight, particularly preferably 0.3 to 10 wt .-%, based on the monomers to be polymerized in the respective stage . It is also possible to use a plurality of different initiators in the emulsion polymerization.
  • the polymer P1 is mixed with a base.
  • the neutralization can be carried out, for example, by acid groups of the polymer P1, in particular by at least partial addition of a base before and / or during the polymerization of the second stage.
  • the base can be added in a common feed with the monomers to be polymerized or in a separate feed, in particular after the first stage.
  • the amount of base required for the neutralization of at least 70%, preferably 70 to 100% or 70 to 95% acid equivalents, is preferably contained in the polymerization vessel.
  • the neutralization carried out after the first stage with a base is preferably carried out before the beginning of the second stage polymerization.
  • the base results in partial or complete neutralization of the ionic or latent-ionic groups of the first stage polymer; it can cause swelling of the polymer particles, but also completely dissolve them.
  • a partial neutralization is carried out, for example at least 70% of the ionic or latent ionic groups present, especially if in the second stage or subsequent to the polymerization further epoxy-containing monomers or epoxy-containing auxiliaries and additives, as described below among the monomers M o- of the additives described be added.
  • alkali or alkaline earth compounds such as sodium hydroxide, potassium hydroxide, calcium hydroxide, magnesium oxide, sodium carbonate; Ammonia; primary, secondary and tertiary amines, such as ethylamine, propylamine, monoisopropylamine, monobutylamine, hexylamine, ethanolamine, dimethylamine, diethylamine, di-n-propylamine, tributylamine, triethanolamine, dimethoxyethylamine, 2-ethoxyethylamine, 3-ethoxypropylamine, dimethylethanolamine, diisopropanolamine, Morpholine, ethylenediamine, 2-diethylaminethylamine, 2,3-diaminopropane, 1, 2-propylenediamine, dimethylaminopropylamine, nopanopanediamine, hexamethylenediamine, 4,9-dioxadodecane-1, 12-diamine
  • ammonia is used as the base.
  • the polymerization can be carried out in the first stage by means of the in-situ seed method.
  • a portion of a monomer or monomer mixture of the first stage for example, ⁇ 35 wt.%, Preferably ⁇ 20 wt.%, Based on the total weight of the monomers of the first stage, for example ⁇ 10 wt.%, Preferably ⁇ 3 wt. %, based on the total weight of the monomers of the first stage and polymerized by means of an initiator, after which then the remaining amount of the first stage is metered.
  • the monomers of the first stage polymerization are selected such that the glass transition temperature calculated for a polymer prepared from the first stage monomers is greater than 50 ° C, more preferably in the range of 50 ° C to 150 ° C or in the range of 70 ° C to 125 ° C.
  • polymer compositions in particular aqueous polymer compositions, whose polymers have a glass transition temperature in the desired range.
  • Tg 1 / Tg X 1 Tg 1 + X 2 / Tg 2 + .... X n / T g n , where x 1 , x 2 , .. x n are the mass fractions of the monomers 1, 2... N and Tg 1 , Tg 2 ... Tg n mean the glass transition temperatures of each of the monomers 1, 2 ... n built polymers in degrees Kelvin.
  • the Tg values for the homopolymers of most monomers are known and are listed, for example, in Ullmann's Ecyclopedia of Industrial Chemistry, Vol. 5, Vol. A21, page 169, VCH Weinheim, 1992; further sources of glass transition temperatures of homopolymers are, for example, J.
  • the second stage polymerization monomers are selected so that the glass transition temperature calculated for a polymer prepared from the second stage monomers is at least 50 ° C lower than that of the first stage, preferably in the range below 30 ° C, especially in the range from 20 ° C to -80 ° C.
  • the vinyl monomers used, especially the first stage monomers include monomers having functional groups such as crosslinking groups and hydrophilic water-dispersible groups. Some functional groups can have more than one function.
  • (meth) acrylic acid is normally used as a water-dispersible monomer, but may also act as a crosslinking monomer here, and, for example, react with epoxide compounds or carbodiimides.
  • Crosslinking monomers such as acetoacetyl (meth) acrylates or acetoacetoxyethyl (meth) acrylates are used because they can undergo crosslinking reactions with themselves and, for example, with polyamines; they also contribute to wet grip.
  • Wet adhesion refers to the proper adhesion of a coating to a substrate under moist conditions.
  • the crosslinking can take place by reaction of the groups with one another and / or by adding a crosslinking additive. Preferably, the crosslinking takes place only after the actual film formation.
  • the alkyl radical has at least 3 carbon atoms.
  • Examples of (meth) acrylic acid (cyclo) alkyl esters are (meth) acrylic acid methyl ester, (meth) acrylic acid ethyl ester, (meth) acrylic acid n-propyl ester, (meth) acrylic acid n-butyl ester, (meth) acrylic acid iso-butyl ester , Sec-butyl (meth) acrylate, tert-butyl methacrylate, n-pentyl (meth) acrylate, iso-pentyl (meth) acrylate, (2-methyl) methacrylate, (meth) acrylate, (Meth) acrylic acid n-hexyl ester, (meth) acrylic acid 2-ethylbutyl ester, (meth) acrylic acid pentyl ester, (n-heptyl) methacrylate, (n-octyl (meth) acrylate, (meth) acrylic acid 2-ethylhexyl ester (
  • methyl methacrylate methyl acrylate, ethyl acrylate, n-butyl acrylate, n-butyl methacrylate, n-hexyl acrylate, n-octyl acrylate, 2-ethylhexyl acrylate, and 3-propylheptyl acrylate or mixtures thereof.
  • A2) Vinylaromatics with up to 20 C atoms These are optionally substituted aromatic systems with a vinyl group in conjugation to the aromatic ring system.
  • Such substituted vinylaromatics have one or more, preferably a 1 to 10 carbon atoms, preferably 1 to 6 and particularly preferably 1 to 4 carbon atoms having linear or branched alkyl group, which may be located on the aromatic or on the vinyl group.
  • the substituent When the substituent is at the aromatic, the substituent may preferably be in the ortho or para position, more preferably in the para position to the vinyl group.
  • Suitable vinylaromatic compounds are vinyltoluene, vinylnaphthalene, o and p-methylstyrene, .alpha.-butylstyrene, 4-n-butylstyrene, 4-n-decylstyrene and preferably styrene and .alpha.-methylstyrene.
  • the compounds A3) are selected from the group consisting of ethylenically unsaturated nitriles having up to 20 carbon atoms, vinyl esters of carboxylic acids containing up to 20 carbon atoms, vinyl halides having up to 10 carbon atoms and vinyl ethers of 1 to
  • C-containing alcohols preferably selected from the group consisting of ethylenically unsaturated nitriles having up to 20 carbon atoms and vinyl ethers of 1 to
  • ethylenically unsaturated nitriles are fumaronitrile, acrylonitrile and methacrylonitrile, preferably acrylonitrile and methacrylonitrile and particularly preferably acrylonitrile.
  • Vinyl esters of carboxylic acids containing up to 20 carbon atoms are fumaronitrile, acrylonitrile and methacrylonitrile, preferably acrylonitrile and methacrylonitrile and particularly preferably acrylonitrile.
  • Vinyl esters of carboxylic acids having 1 to 20 carbon atoms are e.g. Vinyl laurate, vinyl stearate, vinyl propionate, vinyl versatate, vinyl butyrate and vinyl acetate, preferably vinyl acetate.
  • Vinyl halides with up to 10 carbon atoms The vinyl halides are chloro, fluoro or bromo substituted ethylenically unsaturated compounds, preferably vinyl chloride and vinylidene chloride.
  • Vinyl ethers of 1 to 10 carbon atoms-containing alcohols 1 to 10 carbon atoms-containing alcohols
  • vinyl ethers there are e.g. Methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, isopropyl acrylate, n-butyl vinyl ether, sec-butyl vinyl ether, isobutyl vinyl ether, tert-butyl vinyl ether and n-octyl vinyl ether.
  • Preferred are vinyl ethers having from 1 to 4 carbon atoms-containing alcohol.
  • the ionic groups may also be latent, such as in maleic anhydride, where the acid functionality is in the form of an anhydride group.
  • (meth) acrylic acid, crotonic acid or dicarboxylic acids e.g. Itaconic acid, maleic acid or fumaric acid, more preferably methacrylic acid and acrylic acid.
  • (Meth) acrylic acid in this specification means methacrylic acid and acrylic acid.
  • the ⁇ , ⁇ -ethylenically unsaturated carboxylic acids are used in the first acid-rich stage in amounts of 5 to 15 wt.%, Preferably 5 to 10 wt .-%, and in the second stage from 0 to 2 wt .-%, based on the total monomers of each stage.
  • the keto or aldehyde groups are preferably bonded to the polymer by copolymerization of copolymerizable, ethylenically unsaturated compounds with keto or aldehyde groups.
  • Suitable such compounds are acrolein, methacrolein, vinyl alkyl ketones having 1 to 20, preferably 1 to 10 carbon atoms in the alkyl radical, formylstyrene, (meth) acrylic acid alkyl esters having one or two keto or aldehyde, or an aldehyde and a keto group. pe in the alkyl radical, wherein the alkyl radical preferably comprises a total of 3 to 10 carbon atoms, for. B.
  • (meth) acryloxyalkylpropanale as described in DE-A-2722097.
  • N-oxoalkyl (meth) acrylamides as described, for. From US-A-4226007, the DE- A-2061213 or DE-A-2207209 are known. Particular preference is given to acetoacetyl (meth) acrylate and, in particular, acetoacetoxyethyl (meth) acrylate (AAEM).
  • the crosslinking monomer C) is preferably used in an amount of from 2 to 15% by weight, in the first stage, and in an amount of from 1 to 10% by weight in the second stage, based on the total weight of monomers used for the polymerization used in each stage.
  • Bonding agents D) are, for example, compounds having an amino, urea or an N-heterocyclic group, for example dialkylaminoalkyl esters, dialkylaminoalkylamides of acrylic or methacrylic acid, in particular those having 1 to 5 carbon atoms in the alkyl group; free radically polymerizable compounds of urea, ethylene or propylene urea and polymerizable imidazolines having a -NC (0) N group.
  • N- (2-methacyloyloxyethyl) ethyleneurea methacrylamidoethylethyleneurea, N- (2-methacryloxyacetamidoethyl-N, N, N ', N'-ethyleneurea, allylalkylethyleneurea, N-methacrylamidomethylurea, N-methacryoylurea, N- [3- (1,3 -diazocyclohexan-2-one-propyl)] methacrylamide, 2- (1-imidazolyl) ethyl methacrylate, 2- (1-imidazolidin-2-one) ethyl methacrylate, vinyl imidazole, vinyl pyrrolidone and 3-allyl-4, 5-methoxy- 2-imidazolidinone.
  • N- (2-methacryloyloxyethyl) ethylene urea ureidomethacrylate
  • methacrylamidoethylethyleneurea ureidomethacrylate
  • the monomers D) are used in the first stage in amounts of 0 to 4 wt .-% and in the second stage in amounts of 0 to 2 wt .-% based on the total weight of the monomers used for the polymerization of the respective stage.
  • the monomer E) used is t-butyl acrylate in amounts of at least 1.5% by weight, based on the total weight of the monomers of the first stage used for the polymerization, then the addition of the water-soluble alkoxylated polyamine can be achieved. waive a sufficient water resistance.
  • no t-butyl acrylate is used in the first stage, the amount of water-soluble polyamine used must be greater than 0.
  • the amount of t-butyl acrylate used in the first stage is between 0 and 25% by weight, based on the total weight of the monomers used for the polymerization of FIG. Stage, preferably between 1, 5 and 25 wt .-%.
  • both t-butyl acrylate in amounts greater than 0 wt .-% and an at least tri-functional alkoxylated polyamine, in particular an ethoxy and / or propoxylated triamine min used.
  • Suitable hydroxyalkyl (meth) acrylates as such, and for these esters are those mentioned below as separate monomers, in particular
  • Corresponding dihydrogen phosphate ester monomers include phosphoalkyl (meth) acrylates, such as 2-phosphoethyl (meth) acrylate, 2- Phosphopropyl (meth) acrylate, 3-phosphopropyl (meth) acrylate, phosphobutyl (meth) acrylate and 3-phospho-2-hydroxypropyl (meth) acrylate.
  • phosphoalkyl (meth) acrylates such as 2-phosphoethyl (meth) acrylate, 2- Phosphopropyl (meth) acrylate, 3-phosphopropyl (meth) acrylate, phosphobutyl (meth) acrylate and 3-phospho-2-hydroxypropyl (meth) acrylate.
  • vinylsulfonic acid allylsulfonic acid, sulfoethyl acrylate, sulfoethyl methacrylate, sulfopropyl acrylate, sulfopropyl methacrylate, 2-hydroxy-3-acryloxypropylsulfonic acid, 2-hydroxy-3-methacryloxypropylsulfonic acid, styrenesulfonic acids and 2-acrylamido-2-methylpropane. sulfonic acid.
  • Suitable styrenesulfonic acids and derivatives thereof are styrene-4-sulfonic acid and styrene-3-sulfonic acid and the alkaline earth or alkali metal salts thereof, e.g. For example, sodium styrene-3-sulfonate and sodium styrene-4-sulfonate.
  • Suitable monomers M are also vinyl monomers with alkoxylated side chains, such as (alkoxy) polyethylene glycol (meth) acrylates, in the form of various products of the name Bisomer® from Geo Specialty Chemicals, USA. This includes z. Bisomer® MPEG 350 MA, a methoxypolyethylene glycol monomethacrylate.
  • Suitable monomers M are vinyl monomers with epoxide groups, such as allyl glycidyl ether and 2,3-epoxypropyl (meth) acrylate. These latter monomers are preferably used in the 2nd stage.
  • monomers M also ⁇ , ß-ethylenically unsaturated carboxylic acid amides selected from the group consisting of (meth) acrylamide, Crotonklamid, amides of dicarboxylic acids or mixtures thereof. Particular preference is given to using itaconic diamide, maleic acid diamide or fumaric diamide, particular preference being given to methacrylic acid amide and acrylamide.
  • Other monomers M can also di- and poly (meth) acrylates 1, 2, 1, 3 and 1, 4-butanediol diacrylate, 1, 2 and 1, 3-propylene glycol di (meth) acrylate, 1, 6- Hexanediol di (meth) acrylate, 1, 2-
  • These monomers are preferably used in the 2nd stage.
  • the regulators are bound to the polymer, generally to the chain end.
  • the amount of regulator is in particular 0.05 to 5 parts by weight, particularly preferably 0.05 to 2 parts by weight, based on 100 parts by weight of the total monomers to be polymerized in the first and second stages.
  • Suitable regulators are e.g. Compounds with a thiol group such as tert-butyl mercaptan, thioglycolic acid alkyl ester, mercaptoethanol, mercaptopropionic acid,
  • Ethylhexyl thioglycolate, mercaptopropyltrimethoxysilane, n- or tert-dodecylmercaptan are generally low molecular weight compounds having a molecular weight of less than 2000, in particular less than 1000 g / mol.
  • alkyl esters of thioglycolic acid and mercaptopropionic acid such as 2-ethylhexyl thioglycolate and i-octylmercaptopropionate.
  • EP-A-0 196 783 and EP-A-0 199 436 describe the use of certain and other types of cobalt (II) chelates as chain transfer agents for the preparation of oligomers of olefinically unsaturated monomers by free radical polymerization.
  • WO-A-87/03605 claims the use of certain cobalt (II) chelate complexes for this purpose as well as the use of certain chelate complexes of other metals, such as e.g. Iridium and rhenium.
  • the weight average molecular weight of the first stage polymerization monomers is between 2 and 35 kDa, preferably between 5 and 20 kDa.
  • the weight-average molecular weight of the second stage is preferably greater than 50 kDa.
  • the molecular weights were determined by size exclusion chromatography.
  • the weight ratio of acid-rich first stage to the hydrophobic second stage is preferably in the range of 20/80 to 50/50.
  • water-soluble alkoxylated triamine added after the polymerization of P1 and P2 is meant an ethoxylated and / or propoxylated triamine having a average molecular weight of 140 to 5000.
  • polyoxyalkylenetnamines and their preparation are disclosed in DE 38 25 637, as well as in WO2004056903, the disclosure of which is expressly incorporated herein by reference and which, with regard to the disclosure of these compounds, are intended to form part of the present application.
  • Examples of commercially available ethoxylated and / or propoxylated triamines are Jeffamine® T403 (from Huntsman) or Baxxodur® EC310 (from BASF SE).
  • a propoxylated triamine is used.
  • the ratio of the propoxylated triamine used based on the keto- or aldehyde-functional monomer e) is 1: 1 to 1: 9 (molar).
  • the first composition preferably comprises in the polymer dispersion according to the invention
  • the second composition preferably comprises in the polymer dispersion according to the invention
  • auxiliaries and additives include, for example, pH-adjusting substances, reducing and bleaching agents, such as.
  • reducing and bleaching agents such as.
  • alkali metal salts of hydroxymethanesulfinic acid z. B. Rongalit C ® BASF Stock Corporation society
  • chelating agents such as sodium citrate, sodium tartrate, sodium tartrate, sodium tartrate, sodium tartrate, sodium tartrate, sodium tartrate, sodium tartrate, sodium tartrate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium sulfate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium sulfate, sodium bicarbonate, sodium sulfate, sodium bicarbonate, sodium sulfate, sodium bicarbonate, sodium sulfate, sodium bicarbonate, sodium sulfate, sodium
  • water-soluble or -dispersible epoxysilanes can serve to improve the adhesion to various substrates, as well as to further reduce the water sensitivity of the coating by reaction with the carboxylic acid groups present the polymer dispersion. In addition, they can lead to further crosslinking of the coating by condensation reactions of the silane groups.
  • silanes are described inter alia in WO 98/1451. 1 Typical examples are glycidoxypropyltri (m) ethoxysilane (Geniosil GF 80 and 82 from Wacker) or 3-glycidoxypropylmethyldiethoxysilanes (CoatOSil or Silquest brands from the company Momentive).
  • the solids content of the dispersion is preferably 25-55% by weight, based on the total amount of the liquid components of the dispersion.
  • the solids content is particularly preferably 30-50% by weight.
  • the particle size of the polymer of the first and / or second stage is preferably in the range from 1 nm to 100 nm, in particular in the range from 5 nm to 75 nm and most preferably in the range from 25 to 65 nm.
  • the particle size of the polymer according to the invention was determined by means of hydrodynamic chromatography (HDC).
  • the coating composition of the invention is preferably used in aqueous paints.
  • These paints are for example in the form of an unpigmented system (clearcoat) or a pigmented system.
  • the proportion of pigments can be described by the pigment volume concentration (PVK).
  • paints can be classified using the PVK as follows: Highly filled interior paint, washable, white / matt approx. 85
  • PVK ⁇ 50 more preferably PVK ⁇ 35 and even more preferably in low-filled systems (PVK ⁇ 23) and clearcoats (PVK ⁇ 5).
  • Suitable fillers in clearcoat systems are z. As matting agents, which greatly affect the desired gloss. Matting agents are usually transparent and can be both organic and inorganic. Inorganic fillers based on silica are the most suitable and are widely available commercially. Examples include Syloid ® grades from WR Grace & Company and the Acematt ® brands of the company. Evonik GmbH. Organic matting agents are eg available from BYK-Chemie GmbH under the Ceraflour ® - the and. Ceramat ® brands, from the company deuteron GmbH under the deuteron MK ® -. Brand.
  • Suitable fillers for emulsion paints are aluminosilicates, such as feldspars, silicates, such as kaolin, talc, mica, magnesite, alkaline earth carbonates, such as calcium carbonate, for example in the form of calcite or chalk, magnesium carbonate, dolomite, alkaline earth sulfates, such as calcium sulfate, silicon dioxide, etc. Paints are naturally preferred finely divided fillers. The fillers can be used as individual components. In practice, however, filler mixtures have proven particularly useful, for. As calcium carbonate / kaolin, calcium carbonate / talc. Glossy paints generally have only small amounts of very finely divided fillers or contain no fillers.
  • Finely divided fillers can also be used to increase the hiding power and / or to save on white pigments.
  • blends of color pigments and fillers are preferably used.
  • Suitable pigments are, for example, inorganic white pigments, such as titanium dioxide, preferably in rutile form, barium sulfate, zinc oxide, zinc sulfide, basic lead carbonate, antimony trioxide, lithopones (zinc sulfide + barium sulfate) or colored pigments, for example iron oxides, carbon black, graphite, zinc yellow, zinc green, ultramarine, Manganese black, antimony black, manganese violet, Paris blue or Schweinfurter green.
  • the dispersion paints according to the invention may also contain organic color pigments, eg. B. Sepia, Cambogia,
  • Kasseler Braun Toluidine Red, Para red, Hansa Yellow, Indigo, azo dyes, anthraquinoid and indigo dyes and dioxazine, quinacridone, phthalocyanine, isoindolinone and metal complex pigments.
  • synthetic white pigments with air inclusions for increasing light scattering as the Ropaque ® - and AQACell ® dispersions.
  • Luconyl ® brands from BASF SE such as the Lyconyl ® -Yellow, Lyconyl ® -. Brown and Luconyl ® -Red, in particular the transparent variants.
  • the coating composition according to the invention also called aqueous coating material, may contain, in addition to the polymer dispersion, optionally additional film-forming polymers, pigments and other additives.
  • the usual additives include wetting or dispersing agents, such as sodium, potassium or ammonium polyphosphates, alkali metal and ammonium salts of acrylic acid or maleic anhydride copolymers, polyphosphonates, such as 1-hydroxyethane-1, 1-diphosphonsauresodium and naphthalenesulfonic acid Salts, in particular their sodium salts.
  • Important additives are the film forming aids, thickeners and defoamers. Suitable film-forming aids include Texanol ® by the company.
  • Eastman Chemicals and glycol ethers and esters for example, commercially available from BASF SE under the name Solvenon ® and Lusolvan ®, and from Dow under the trade names Dowanol ®.
  • the amount is preferably ⁇ 10 wt .-% and particularly preferably ⁇ 5 wt .-% of the total formulation. It is also possible to formulate completely without solvents.
  • Suitable additives are leveling agents, defoamers, biocides and thickeners.
  • Suitable thickeners are z.
  • the amount of thickener is preferably less than 2.5 wt .-%, more preferably less than 1, 5 wt .-% thickener, based on solids content of the paint.
  • Further formulation instructions for wood coatings are described in detail in "Waterbased Acrylates for Decorative Coatings" by the authors M. Schwartz and R. Baumstark, ISBN 3-87870-726-6.
  • a further subject of the present invention is the use of the polymer dispersion according to the invention for coating compositions.
  • Another object of the present invention is the use of the polymer dispersion according to the invention for paints.
  • the preparation of the paint according to the invention is carried out in a known manner by mixing the components in mixing devices customary for this purpose. It has proven useful to prepare an aqueous paste or dispersion from the pigments, water and optionally the additives, and then first the polymeric binder, d. H. As a rule, the aqueous dispersion of the polymer is mixed with the pigment paste or pigment dispersion.
  • the paint of the invention can be applied in a conventional manner to substrates, for. B. by brushing, spraying, dipping, rolling, knife coating.
  • the paints of the invention are characterized by easy handling and good processing properties.
  • the paints are low in emissions. They have good performance properties, eg. B. good water resistance, good wet adhesion, and good blocking resistance, good paintability, and they show a good course when applied.
  • the tool used can be easily cleaned with water.
  • FIG. 1 shows elevations on glass of the formulation according to the invention after drying for 2 days at RT and 2 hours of contact with water.
  • FIG. 1 shows four different coatings of the formulation according to the invention on glass plate, where after drying at room temperature (RT), demineralized water (demineralized water) was placed in the lower region.
  • the formulations contain a polymer dispersion with crosslinking monomer only in the first stage (VB 1A and 1 C) and this monomer in both stages (B 1A and 1 C, according to the invention). It can be seen that the coatings based on the polymer dispersions of the invention have no destruction or damage to the surfaces.
  • Example 1 A polymerization vessel equipped with metering devices and temperature control was placed at 20 to 25 ° C (room temperature) under a nitrogen atmosphere
  • Feed 4a (homogeneous mixture of):
  • Feed 4b (homogeneous mixture of):
  • the resulting 3307 g of the aqueous polymer dispersion had a solids content of 43.3% by weight and a pH of 7.4.
  • the MFT was ⁇ 0 ° C.
  • the weight-average molecular weight of the polymer of the dispersion was about 800 kDa.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 36 nm.
  • Example 1 500.0 g of Example 1 was initially charged and stirred
  • Solids content of the mixture was 41.3% by weight, pH was 9.5.
  • Example 1 500.0 g of Example 1 was initially charged and stirred
  • Solids content of the mixture was 42.3% by weight, pH was 8.7.
  • Example 1 500.0 g of Example 1 was initially charged and stirred
  • Example 2 In a equipped with dosing and temperature control polymerization vessel were at 20 to 25 ° C (room temperature) under a nitrogen atmosphere
  • the 3291 g of the aqueous polymer dispersion obtained had a solids content of 43.5% by weight and a pH of 7.3.
  • the MFT was ⁇ 0 ° C.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 40 nm.
  • Example 2 500.0 g of Example 2 was initially charged and stirred
  • Solids content of the mixture was 42.2% by weight, pH was 8.7.
  • Feed 4a (homogeneous mixture of):
  • Feed 4b (homogeneous mixture of):
  • the polymerization mixture was allowed to react for a further 30 minutes at 80.degree. then 1 17 g of deionized water was added and stirring was continued for 60 minutes at 80 ° C.
  • the resulting 3307 g of the aqueous polymer dispersion had a solids content of 43.5% by weight and a pH of 7.3.
  • the MFT was ⁇ 0 ° C.
  • the weight-average molecular weight of the polymer of the dispersion was about 810 kDa.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 38 nm. Comparative Example 1A (VB 1A)
  • Solids content of the mixture was 42.0% by weight, pH was 8.5.
  • feed 1 was started and metered within 45 minutes. After the end of feed 2, polymerization was continued for 10 minutes, then feed 3 was added and stirred in for 10 minutes. Subsequently, feed 4 was started and metered in 90 minutes. After the first half of feed 4 was metered, feed 5 was started and metered in parallel to the remaining feed 4 in 45 min.
  • Feed 4a (homogeneous mixture of):
  • the obtained 3296 g of the aqueous polymer dispersion had a solids content of 43.3 wt .-% and a pH of 7.3.
  • the MFT was ⁇ 0 ° C.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 40 nm.
  • Feed 4 (homogeneous mixture of):
  • the 3146.9 g of the aqueous polymer dispersion obtained had a solids content of 43.5% by weight and a pH of 7.6.
  • the MFT was ⁇ 0 ° C.
  • the weight-average molecular weight of the polymer of the dispersion was about 720 kDa.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 45 nm.
  • the polymerization mixture was allowed to react at 80 ° C. for a further 30 minutes; then 1 17 g of deionized water was added and stirring was continued for 60 minutes at 80 ° C.
  • the 3146.9 g of the aqueous polymer dispersion obtained had a solids content of 45.0% by weight and a pH of 7.5.
  • the MFT was ⁇ 0 ° C.
  • the weight-average molecular weight of the polymer of the dispersion was about 730 kDa.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 45 nm.
  • feed 1 was started and metered within 45 minutes. After the end of feed 2, polymerization was continued for 10 minutes, then feed 3 was added and stirred in for 10 minutes. Subsequently, feed 4 was started and metered in 90 minutes. After the first half of feed 4 was metered, feed 5 was started and metered in parallel to the remaining feed 4 in 45 min.
  • Feed 4a (homogeneous mixture of):
  • the obtained 3296 g of the aqueous polymer dispersion had a solids content of 43.5% by weight and a pH of 7.6.
  • the MFT was ⁇ 0 ° C.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 45 nm.
  • Example 5 500.0 g of Example 5 was initially charged and stirred
  • Solids content of the mixture was 42.3 wt%, pH was 9.5.
  • feed 4 was started and metered in 90 minutes. After the first half of feed 4 was metered in, feed 5 was started and metered in parallel to the remaining feed 4 in 45 minutes.
  • Feed 1 (homogeneous solution 55.8 g of deionized water and
  • Feed 4 (homogeneous mixture of):
  • the polymerization mixture was allowed to react at 80 ° C. for a further 30 minutes; then 1 17 g of deionized water was added and stirring was continued for 60 minutes at 80 ° C.
  • the 3146.9 g of the aqueous polymer dispersion obtained had a solids content of 45.0% by weight and a pH of 7.5.
  • the MFT was ⁇ 0 ° C.
  • the weight-average molecular weight of the polymer of the dispersion was about 690 kDa.
  • the with deionized water Dilute aqueous polymer dispersion has a weight-average particle diameter of 42 nm.
  • feed 1 was started and metered within 45 minutes. After the end of feed 2, polymerization was continued for 10 minutes, then feed 3 was added and stirred in for 10 minutes. Subsequently, feed 4 was started and metered in 90 minutes. After the first half of feed 4 was metered, feed 5 was started and metered in parallel to the remaining feed 4 in 45 min.
  • Feed 4a (homogeneous mixture of):
  • the 3295.7 g of the aqueous polymer dispersion obtained had a solids content of 43.6% by weight and a pH of 7.6.
  • the MFT was ⁇ 0 ° C.
  • the aqueous polymer dispersion diluted with deionized water has a weight-average particle diameter of 37 nm.
  • Example 6 500.0 g of Example 6 was initially charged and stirred
  • Solids content of the mixture was 42.0% by weight, pH was 9.5.
  • Example 6 500.0 g of Example 6 was initially charged and stirred
  • Solids content of the mixture was 43.7% by weight, pH was 9.8. measurement methods
  • the weight average molecular weight Mw is determined by size exclusion chromatography (SEC) with tetrahydrofuran + 0.1% by weight trifluoroacetic acid as eluent at a flow rate of 1 ml / min and 35 ° C column temperature.
  • SEC size exclusion chromatography
  • the sample is diluted in the eluent to a concentration of 2 mg / ml and injected with 100 ⁇ of it after the sample solution has been filtered through a 0.2 ⁇ filter (Sartorius Minisart SRP 25) to remove any gel fraction.
  • any gel fraction of the polymer is removed, so that the stated values relate to the sol fraction.
  • the solids content (FG) was generally determined by drying a defined amount of the aqueous polymer dispersion (about 1 g) in an aluminum crucible with an inner diameter of about 5 cm at 140 ° C in a drying oven to constant weight. Two separate measurements were made. The values given in the examples represent the mean value of the respective two measurement results.
  • the determination of the minimum film-forming temperature was carried out in accordance with Ullmanns Enzyklopadie der ischen Chemie, 4th ed., Vol. 19, Verlag Chemie, Weinheim (1980), p. 17.
  • the measuring apparatus used was a film formation bank of Coesfeld (metal plate, to which a temperature gradient is applied). The filming took place at a wet layer thickness of 1 mm.
  • the minimum film-forming temperature is the temperature at which the film begins to crack. particle size
  • the particle size of the polymer according to the invention was determined by means of hydrodynamic chromatography (HDC). Glass transition temperature
  • the glass transition temperature Tg was determined using the Fox equation.
  • a formulation of the particular polymer dispersion, as defined in Table 1, is applied wet on glass at a thickness of 300 ⁇ m. It is then dried for X days at RT (standard climate). Then deionized water is placed on the coating and it is maintained. The assessment was in grades 0 to 5 after Y Std.
  • Example 1 shows the effect on the water resistance of the coating when the crosslinking monomer is used in both stages; the series A - C shows the effect of different added amount of the propoxylated triamine.
  • Example 2 shows the effect on the water resistance of the coating when in the 2nd stage an epoxy group-carrying monomer M is used.
  • Examples 3, 4 and 5 show the effect on the water resistance of the coating when t-butyl acrylate is used in Step 1; moreover, Example 5A shows the additional improvement when the propoxylated triamine is added.
  • Example 6A and Comparative Example 6B show the comparison of the use of a propoxylated triamine and an aliphatic diamine.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Paints Or Removers (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

L'invention concerne une dispersion polymère à particules très fines pouvant être obtenue par au moins une polymérisation en émulsion biphasique. 1) Un premier polymère P1 acide étant préparé par polymérisation radicalaire à partir d'une première composition, comprenant : A) au moins un monomère choisi dans le groupe des (cyclo)alkylesters de l'acide (méth)acrylique, des composés vinyle aromatiques ayant jusqu'à 20 atomes de carbone, d'un composé polymérisable par voie radicalaire choisi dans le groupe des nitriles à insaturation éthylénique ayant jusqu'à 20 atomes de carbone, des esters de vinyle d'acides carboxyliques contenant jusqu'à 20 atomes de carbone, des halogénures de vinyle ayant jusqu'à 10 atomes de carbone et des éthers vinyliques d'alcools contenant de 1 à 10 atomes de carbone ; B) au moins un acide carboxylique à insaturation éthylénique α,β ; C) au moins un monomère réticulant ayant un groupe céto ou aldéhyde ; D) le cas échéant, au moins un agent promoteur d'adhérence ; E) le cas échéant, de l'acrylate de t-butyle ; F) le cas échéant, d'autres monomères M en présence d'un régulateur de longueur de chaîne. 2) Le polymère P1 préparé au point 1) est mélangé à une base. 3) Un polymère hydrophobe P2 est préparé par polymérisation radicalaire à partir d'une seconde composition en présence du polymère P1 traité au point 2), comprenant : A) au moins un monomère choisi dans le groupe des (cyclo)alkylesters de l'acide (méth)acrylique, des composés vinyle aromatiques ayant jusqu'à 20 atomes de carbone, d'un composé polymérisable par voie radicalaire choisi dans le groupe des nitriles à insaturation éthylénique ayant jusqu'à 20 atomes de carbone, des esters de vinyle d'acides carboxyliques contenant jusqu'à 20 atomes de carbone, des halogénures de vinyle ayant jusqu'à 10 atomes de carbone et des éthers vinyliques d'alcools contenant de 1 à 10 atomes de carbone ; B) le cas échéant au moins un acide carboxylique à insaturation α,β-éthylénique ; C) au moins un monomère réticulant ayant un groupe céto ou aldéhyde ; D) le cas échéant, au moins un agent promoteur d'adhérence ; ainsi que E) le cas échéant, d'autres monomères M, 4) et le cas échéant après la polymérisation de P1 et de P2, une polyamine alcoxylée aqueuse au moins trifonctionnelle, en particulier une triamine éthoxylée et/ou propoxylée, est ajoutée.
EP17710541.8A 2016-03-18 2017-03-14 Dispersion polymère multiphasique aqueuse à particules fines, procédé pour sa préparation et son utilisation comme liant Pending EP3430065A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP16161067 2016-03-18
PCT/EP2017/055985 WO2017157934A1 (fr) 2016-03-18 2017-03-14 Dispersion polymère multiphasique aqueuse à particules fines, procédé pour sa préparation et son utilisation comme liant

Publications (1)

Publication Number Publication Date
EP3430065A1 true EP3430065A1 (fr) 2019-01-23

Family

ID=55650141

Family Applications (1)

Application Number Title Priority Date Filing Date
EP17710541.8A Pending EP3430065A1 (fr) 2016-03-18 2017-03-14 Dispersion polymère multiphasique aqueuse à particules fines, procédé pour sa préparation et son utilisation comme liant

Country Status (8)

Country Link
US (1) US10913811B2 (fr)
EP (1) EP3430065A1 (fr)
KR (1) KR20180126517A (fr)
CN (1) CN109071733B (fr)
AU (1) AU2017234180B2 (fr)
BR (1) BR112018068556A2 (fr)
CA (1) CA3017548A1 (fr)
WO (1) WO2017157934A1 (fr)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112166132B (zh) * 2018-06-07 2023-05-05 国际人造丝公司 聚合物分散体、它们的制备和用途
ES2966064T3 (es) 2018-08-02 2024-04-18 Basf Se Procedimiento para producir una dispersión polimérica acuosa
BR112021010033A2 (pt) * 2019-03-21 2021-10-13 Sika Technology Ag Composição à base de água com transparência aprimorada
US20220363938A1 (en) * 2019-09-20 2022-11-17 Basf Se Coatings with improved adhesion
CN114787205B (zh) * 2019-12-18 2024-04-16 陶氏环球技术有限责任公司 封闭聚合物粒子的含水分散体的制备
CA3168208A1 (fr) * 2020-02-21 2021-08-26 Swimc Llc Polymeres antitaches, amorces, kits et procedes
CN116057128B (zh) * 2020-08-11 2024-06-28 湛新荷兰有限公司 水性涂料组合物
WO2024040010A1 (fr) * 2022-08-15 2024-02-22 Ppg Industries Ohio, Inc. Compositions de revêtement comprenant des polymères acryliques pour ustensile de cuisson, ustensile de cuisson et autres appareils de cuisson

Family Cites Families (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1329126A (en) 1969-12-11 1973-09-05 Mitsubishi Rayon Co Acrylic fibre and a method for manufacturing the same
JPS5033767B1 (fr) 1971-03-11 1975-11-04
DE2722097C3 (de) 1977-05-16 1981-09-17 Basf Ag, 6700 Ludwigshafen (Meth)acryloxy-alkylpropanale, Verfahren zu dessen Herstellung und Verwendung derselben
US4226007A (en) 1979-03-16 1980-10-07 Signode Corporation Sealless strap connection
US4269749A (en) 1979-04-30 1981-05-26 The Dow Chemical Company Method of imparting salt and/or mechanical stability to aqueous polymer microsuspensions
FR2528434B1 (fr) 1982-06-11 1985-07-19 Roussel Uclaf Nouveaux 19-nor steroides substitues en 11b et eventuellement en 2, leur procede de preparation et leur application comme medicament
US4526945A (en) 1984-03-21 1985-07-02 Scm Corporation Low molecular weight polymers and copolymers
US4680352A (en) 1985-03-01 1987-07-14 E. I. Du Pont De Nemours And Company Cobalt (II) chelates as chain transfer agents in free radical polymerizations
US4694054A (en) 1985-03-01 1987-09-15 E. I. Du Pont De Nemours And Company Cobalt(II) chelates as chain transfer agents in free radical polymerizations
DE3685583T3 (de) 1985-12-03 1997-04-10 Commw Scient Ind Res Org Verfahren zur oligomerisation.
US4733005A (en) 1986-04-21 1988-03-22 The Dow Chemical Company Phosphinyl-containing ethylenically unsaturated compounds
US4680354A (en) 1986-05-21 1987-07-14 The Glidden Company Low molecular weight polymers and copolymers
US4894397A (en) 1988-04-21 1990-01-16 S. C. Johnson & Son, Inc. Stable emulsion polymers and methods of preparing same
DE3825637A1 (de) 1988-07-28 1990-03-08 Rwe Dea Ag Sekundaere polyetheramine, ihre herstellung und verwendung zur herstellung von polyharnstoffen
DE4003422A1 (de) 1990-02-06 1991-08-08 Basf Ag Waessrige polyurethanzubereitungen
US5391624A (en) 1992-02-10 1995-02-21 S. C. Johnson & Son, Inc. Thermosettable compositions
GB9408725D0 (en) 1994-05-03 1994-06-22 Zeneca Resins Bv Production of aqueous polymer compositions
DE4439459A1 (de) 1994-11-04 1995-05-04 Basf Ag Wäßrige Polymerisatdispersion
AT402504B (de) * 1994-11-29 1997-06-25 Vianova Kunstharz Ag Verfahren zur herstellung von wässrigen, selbstvernetzenden copolymerisatdispersionen und ihre verwendung als bindemittel für lagerstabile einkomponentenlacke
DE59503548D1 (de) 1994-11-29 1998-10-15 Vianova Kunstharz Ag Verfahren zur zweistufigen herstellung von wässrigen, selbstvernetzenden copolymerisatdispersionen und deren verwendung für lacke
US5739196A (en) 1995-11-30 1998-04-14 Union Carbide Chemicals & Plastics Technology Corporation Latex compositions having wet adhesion and other improved rheological properties and methods of producing same
EP0868476B1 (fr) 1996-10-02 2005-08-24 General Electric Company Compositions d'additifs constitues d'une emulsion d'epoxysilane dans des dispersions de polymeres reactifs a base d'eau, et leurs procedes de preparation
CA2252266A1 (fr) 1997-11-13 1999-05-13 Rohm And Haas Company Compose de revetement aqueux a temps ouvert etendu
DE19750618A1 (de) 1997-11-14 1999-05-20 Basf Ag Pigmenthaltige Zubereitungen auf der Basis wässriger Polymerisatdispersionen
ATE376015T1 (de) 2002-12-23 2007-11-15 Dow Global Technologies Inc Reaktive polyurethanzusammensetzung
US7285590B2 (en) 2003-11-13 2007-10-23 Hexion Specialty Chemicals, Inc. Aqueous dispersions containing multi-stage emulsion polymers
JP2006219559A (ja) * 2005-02-09 2006-08-24 Mitsubishi Rayon Co Ltd アクリル系重合体微粒子及びそれを用いたプラスチゾル組成物
US8153721B2 (en) * 2007-06-11 2012-04-10 Basf Se Process for the preparation of an aqueous polymer dispersion
EP2371870B1 (fr) 2010-04-01 2012-07-11 Rohm and Haas Company Polymère d'émulsion à phases multiples et revêtements formés à partir de celui-ci
ES2529671T3 (es) 2010-12-20 2015-02-24 Dsm Ip Assets B.V. Composición acuosa bio-renovable de polímero vinílico
US9458346B2 (en) 2010-12-20 2016-10-04 Dsm Ip Assets B.V. Bio-renewable sequential vinyl polymer
EP2691428B1 (fr) 2011-03-30 2019-01-16 Basf Se Procédé de préparation d´une dispersion aqueuse multi-étape de polymérisat et son utilisation comme liant pour le revêtement de supports
SG193940A1 (en) 2011-04-11 2013-11-29 Nuplex Resins Bv Process for preparing aqueous vinyl polymer dispersions
CA2961590C (fr) 2014-09-19 2023-03-14 Basf Se Produits de polymerisation en emulsion aqueux a fines particules et leur utilisation pour des revetements hydrophobes

Also Published As

Publication number Publication date
KR20180126517A (ko) 2018-11-27
US20190100613A1 (en) 2019-04-04
AU2017234180A1 (en) 2018-10-25
BR112018068556A2 (pt) 2019-02-12
CA3017548A1 (fr) 2017-09-21
WO2017157934A1 (fr) 2017-09-21
US10913811B2 (en) 2021-02-09
CN109071733B (zh) 2022-03-29
AU2017234180B2 (en) 2021-05-20
CN109071733A (zh) 2018-12-21

Similar Documents

Publication Publication Date Title
EP2691428B1 (fr) Procédé de préparation d´une dispersion aqueuse multi-étape de polymérisat et son utilisation comme liant pour le revêtement de supports
WO2017157934A1 (fr) Dispersion polymère multiphasique aqueuse à particules fines, procédé pour sa préparation et son utilisation comme liant
EP3194454B1 (fr) Produits de polymérisation en émulsion aqueux à fines particules et leur utilisation pour des revêtements hydrophobes
EP2336254B1 (fr) Dispersions de polymères
EP2370516B1 (fr) Composition aqueuse de liant contenant des oligomères
US20120252972A1 (en) Aqueous multistage polymer dispersion, process for its preparation, and use thereof as binder for coating substrates
EP2611844B1 (fr) Emulsion aqueuse de polymères, preparation et utilisation
US20150099843A1 (en) Aqueous binder compositions
EP2791180B1 (fr) Utilisation de dispersions polymères aqueuses pour améliorer la résistance aux agressions chimiques
EP2870208A1 (fr) Utilisation de liants hybrides et de systèmes alkydes aqueux dans des produits de revêtement
EP3707213A1 (fr) Dispersions polymères aqueuses
EP2066756B1 (fr) Utilisation de dispersions de polymères dans des matériaux de revêtement
EP3818087B1 (fr) Procédé de production d'une dispersion de polymère aqueuse
NZ614963B2 (en) Aqueous multistage polymer dispersion, process for its preparation and use thereof as binder for coating substrates

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: UNKNOWN

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20181018

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

17Q First examination report despatched

Effective date: 20211015