EP2414412A1 - (meth)acrylat-polymer, beschichtungsmittel, verfahren zur herstellung einer beschichtung und beschichteter gegenstand - Google Patents

(meth)acrylat-polymer, beschichtungsmittel, verfahren zur herstellung einer beschichtung und beschichteter gegenstand

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Publication number
EP2414412A1
EP2414412A1 EP10705397A EP10705397A EP2414412A1 EP 2414412 A1 EP2414412 A1 EP 2414412A1 EP 10705397 A EP10705397 A EP 10705397A EP 10705397 A EP10705397 A EP 10705397A EP 2414412 A1 EP2414412 A1 EP 2414412A1
Authority
EP
European Patent Office
Prior art keywords
meth
acrylate polymer
acrylate
weight
acrylates
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.)
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Application number
EP10705397A
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German (de)
English (en)
French (fr)
Inventor
Stefanie Maus
Christine Maria BREINER
Cornelia Borgmann
Ulrike Behrens
Oliver Marx
Stephan Fengler
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.)
Evonik Roehm GmbH
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Evonik Roehm GmbH
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Application filed by Evonik Roehm GmbH filed Critical Evonik Roehm GmbH
Publication of EP2414412A1 publication Critical patent/EP2414412A1/de
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/62Monocarboxylic acids having ten or more carbon atoms; Derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10Esters
    • C08F220/12Esters of monohydric alcohols or phenols
    • C08F220/14Methyl esters, e.g. methyl (meth)acrylate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10Esters
    • C08F220/12Esters of monohydric alcohols or phenols
    • C08F220/16Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms
    • C08F220/18Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms with acrylic or methacrylic acids
    • C08F220/1804C4-(meth)acrylate, e.g. butyl (meth)acrylate, isobutyl (meth)acrylate or tert-butyl (meth)acrylate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/04Acids; Metal salts or ammonium salts thereof
    • C08F220/06Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof

Definitions

  • the present invention relates to a (meth) acrylate polymer and a coating agent comprising this polymer.
  • the present invention is directed to a method for producing a coating carried out using the coating agent and a coated article obtainable by the method.
  • Coating agents in particular paints, have been produced synthetically for a long time.
  • An important group of these agents is based on aqueous dispersions which often comprise (meth) acrylate polymers.
  • aqueous dispersions which often comprise (meth) acrylate polymers.
  • the publication DE-A-41 05 134 describes aqueous dispersions which contain alkyl methacrylates as binders.
  • paints from US 5,750,751, EP-A-1 044 993 and WO 2006/013061 are known.
  • Aqueous dispersions can be used for the production of many coatings and are characterized in particular by a high environmental compatibility.
  • a disadvantage is that aqueous dispersions have to be processed under controlled conditions of temperature and humidity, since otherwise the quality of the coatings obtained does not meet the upper requirements.
  • reactive coatings form another group of known coating compositions.
  • Such paints are known for example from EP-O 693 507. These coating compositions can be processed in particular to particularly hard and durable coatings. However, the curing conditions must be met very accurately, otherwise no high quality paints are obtained. Temperature and humidity fluctuations preclude the production of a high quality coating. If outdoor objects are provided with a coating, temperature and humidity fluctuations must be taken into account. Therefore, so-called solvent-based paints are often used for these purposes, which could not be replaced due to their performance, especially for the production of protective coatings (protective coatings). This performance comprises in particular a good processability of the coating compositions and a high resistance of the resulting coatings. Such coating compositions are described, for example, in GB 793776. However, since large amounts of solvent are released during processing, solvent-based paints have relatively low environmental impact.
  • the present invention provides polymers and coating compositions having excellent properties.
  • these properties include good processability over a wide temperature and humidity range.
  • the coating composition should have the highest possible solids content.
  • the coating compositions should show improved environmental compatibility.
  • the coating compositions should have a high solids content.
  • the hardness of the coatings obtainable from the coating compositions should be able to be varied over a wide range.
  • particularly hard, scratch-resistant coatings should be able to be obtained.
  • coatings which are obtainable from the coating compositions according to the invention, based on the hardness should have a relatively low brittleness.
  • a further object is to provide polymers, by the use of coating agents with good processability are available.
  • the coatings obtainable from the coating compositions should have a high weather resistance, in particular a high UV resistance.
  • the coatings obtainable from the polymers or coating compositions should show a particularly high resistance to solvents. This stability should be high compared to many different solvents. Likewise, a very good resistance to water, especially salt water should be given.
  • Another object can be seen to provide polymers or coating compositions that can be obtained very inexpensively and on an industrial scale.
  • the present invention accordingly provides a (meth) acrylate polymer for the preparation of a coating composition, which is characterized in that the (meth) acrylate polymer has a weight-average molecular weight in the range from 10,000 to 60,000 g / mol and the (meth) acrylate polymer 0.5 to 40 wt .-% of units derived from (meth) acrylic monomers having in the alkyl radical at least one double bond and 8 to 40 carbon atoms, 0.1 to 10 wt .-% of units derived from acid group-containing monomers, and
  • the polymers of the present invention result in a coating agent that exhibits good processability over a wide range of temperature and humidity. Furthermore, the coating agent may have a very high solids content without the processability of the coating agent is too much impaired.
  • the coating agents are very environmentally friendly.
  • the coating compositions have a high solids content.
  • the polymers of the present invention and the coating compositions show a particularly long shelf life and durability. Furthermore, the hardness of the coating compositions
  • Coatings obtainable from the coating compositions can be varied over a wide range. In particular, particularly hard, scratch-resistant coatings can be obtained.
  • coatings which are obtainable from the coating compositions according to the invention, based on the hardness and the chemical resistance, a relatively low brittleness.
  • the coatings obtainable from the coating compositions show a high weather resistance, in particular a high UV resistance. Furthermore, the coatings obtainable from the polymers or coating compositions show a particularly high resistance to solvents. This stability is high compared to many different solvents. Likewise, a very good resistance to water, especially salt water is given. Therefore, these coating compositions for the production of protective coatings (protective coatings), which are particularly suitable for painting ships or containers, can be used.
  • coating compositions of the invention lead to coatings with a high gloss. Furthermore, the polymers and coating compositions according to the invention are particularly cost-effective and industrially available.
  • the (meth) acrylate polymers can preferably be obtained by free-radical polymerization. Accordingly, the proportion by weight of the respective units which comprise these polymers results from the proportions by weight of corresponding monomers used to prepare the polymers.
  • the (meth) acrylate polymer according to the invention comprises from 0.5 to 40% by weight, preferably from 1 to 20% by weight, and very particularly preferably from 2 to 10% by weight of units derived from (meth) acrylic monomers are derived, which have at least one double bond and 8 to 40 carbon atoms in the alkyl radical.
  • (Meth) acrylic monomers having at least one double bond and 8 to 40 carbon atoms in the alkyl group are esters or amides of (meth) acrylic acid whose alkyl group has at least one carbon-carbon double bond and 8 to 40 carbon atoms.
  • the notation (meth) acrylic acid means methacrylic acid and acrylic acid and mixtures thereof.
  • the alkyl or alcohol or amine radical may preferably have 10 to 30 and more preferably 12 to 20 carbon atoms, which radical may comprise heteroatoms, in particular oxygen, nitrogen or sulfur atoms.
  • the alkyl group may have one, two, three or more carbon-carbon double bonds.
  • the Polymerization conditions in which the polymer is prepared are preferably chosen so that the largest possible proportion of the double bonds of the alkyl radical is maintained in the polymerization. This can be done for example by stubborn hindrance of the double bonds contained in the alcohol radical. Furthermore, at least a part, preferably all of the double bonds contained in the alkyl radical of the (meth) acrylic monomer, has a lower reactivity in a free-radical polymerization than a (meth) acrylic group, so that preferably no further (meth) acrylic groups in the alkyl radical are included.
  • the iodine value of the (meth) acrylic monomers to be used for the preparation of the polymers which have at least one double bond and 8 to 40 carbon atoms in the alkyl radical is preferably at least 40, more preferably at least 80 and most preferably at least 140 g iodine / 100 g (meth ) acrylic monomer.
  • Such (meth) acrylic monomers generally correspond to the formula (I)
  • R is hydrogen or methyl
  • X is independently oxygen or a group of the formula NR ', wherein R' is hydrogen or a radical having 1 to 6 carbon atoms, and R 1 is a linear or branched radical having 8 to 40, preferably 10 to 30 and more preferably 12 to 20 carbon atoms which has at least one double bond.
  • (Meth) acrylic monomers which have at least one double bond and 8 to 40 carbon atoms in the alkyl radical can be obtained, for example, by esterification of (meth) acrylic acid, reaction of (meth) acryloyl halides or transesterification of (meth) acrylates with alcohols which are at least have a double bond and 8 to 40 carbon atoms. Accordingly, (meth) acrylamides can be obtained by reaction with an amine. These reactions are for example in Ullmann's Encyclopedia of Industrial Chemistry 5th edition on CD-ROM or F. -B. Chen, G. Bufkin, "Crosslable Emulsion Polymers by Autooxidation I", Journal of Applied Polymer Science, Vol. 30, 4571-4582 (1985).
  • Suitable alcohols include octenol, nonenol, decenol, undecenol, dodecenol, tridecenol, tetradecenol, pentadecenol, hexadecenol, heptadecenol, octadecenol, nonadecenol, icosenol, docosenol, octadiene-ol, nonanoedia-ol, deca- dien-ol, undecadiene-ol, dodecadiene-ol, trideca-diene-ol, tetradeca-diene-ol, pentadeca-dien-ol, hexadeca-dien-ol, heptadeca-dien-ol, octadecadiene- ol, Nonadeca-dien-ol, Ikosa-dien-ol and
  • fatty alcohols are sometimes commercially available or can be obtained from fatty acids, this reaction being carried out, for example, in F.-B. Chen, G. Bufkin, Journal of Applied Polymer Science, Vol. 30, 4571-4582 (1985).
  • the preferred (meth) acrylates obtainable by this process include, in particular, octadiene-yl (meth) acrylate, octadeca-diene-yl (meth) acrylate, octadeca-then-yl (meth) acrylate, Hexadecenyl (meth) acrylate, octadecenyl (meth) acrylate and hexadecadienyl (meth) acrylate.
  • (meth) acrylates which have at least one double bond and 8 to 40 carbon atoms in the alkyl radical can also be obtained by reacting unsaturated fatty acids with (meth) acrylates which have reactive groups in the alkyl radical, in particular alcohol radical.
  • the reactive groups include in particular hydroxy groups and epoxy groups.
  • hydroxyalkyl (meth) acrylates such as 3-hydroxypropyl (meth) acrylate, 3,4-dihydroxybutyl (meth) acrylate, 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, 2,5-dimethyl -1, 6-hexanediol (meth) acrylate, 1, 10-decanediol (meth) acrylate; or epoxy-containing (meth) acrylates, for example glycidyl (meth) acrylate can be used as starting materials for the preparation of the aforementioned (meth) acrylates.
  • Suitable fatty acids for reaction with the abovementioned (meth) acrylates are often commercially available and are obtained from natural sources. These include undecylenic acid, palmitoleic acid, oleic acid, elaidic acid, vaccenic acid, icosenoic acid, cetoleic acid, erucic acid, nervonic acid, linoleic acid, linolenic acid, arachidonic acid, timnodonic acid, clupanodonic acid and / or cervonic acid.
  • the preferred (meth) acrylates obtainable by this process include, in particular, (meth) acryloyloxy-2-hydroxypropyl linoleic acid ester, (meth) acryloyloxy-2-hydroxypropyl linolenic acid ester and (meth) acryloyloxy-2-hydroxypropyl oleic acid ester.
  • R is hydrogen or a methyl group
  • X 1 and X 2 are independently oxygen or a group of the formula NR ', wherein R' is hydrogen or a radical having 1 to 6 carbon atoms, with the proviso that at least one of the groups X 1 and X 2 a group of the formula NR ', wherein R' is hydrogen or a radical having 1 to 6 carbon atoms, Z is a linking group, and R 2 is an unsaturated radical having 9 to 25 carbon atoms, are used.
  • R is hydrogen or a methyl group
  • X 1 is oxygen or a group of formula NR ', wherein R' is hydrogen or a radical having 1 to 6 carbon atoms, Z is a linking group, R is hydrogen or a radical having 1 to 6 carbon atoms and R 2 is an unsaturated Rest with 9 to 25 carbon atoms, achieve.
  • radical having 1 to 6 carbon atoms represents a group having 1 to 6 carbon atoms and includes aromatic and heteroaromatic groups and also alkyl, cycloalkyl, alkoxy, cycloalkoxy, alkenyl, alkanoyl,
  • Alkoxycarbonyl groups and heteroalipatic groups can be branched or unbranched. Furthermore, these groups may have substituents, in particular halogen atoms or hydroxyl groups.
  • the radicals R ' are preferably alkyl groups.
  • the preferred alkyl groups include the methyl, ethyl, propyl, isopropyl, 1-butyl, 2-butyl, 2-methylpropyl or tert-butyl group.
  • the group Z preferably represents a linking group comprising 1 to 10, preferably 1 to 5 and most preferably 2 to 3 carbon atoms. These include in particular linear or branched, aliphatic or cycloaliphatic radicals, such as a methylene, ethylene, propylene, iso-propylene, n-butylene, iso-butylene, t-butylene or cyclohexylene group, wherein the Ethylene group is particularly preferred.
  • the group R 2 in formula (II) represents an unsaturated radical having 9 to 25 carbon atoms.
  • These groups include in particular alkenyl, cycloalkenyl, Alkenoxy, cycloalkenoxy, alkenoyl and heteroalipatic groups. Furthermore, these groups may have substituents, in particular halogen atoms or hydroxyl groups.
  • the preferred groups include in particular alkenyl groups, such as, for example, the nonenyl, decenyl, undecenyl, dodecenyl, tridecenyl, tetradecenyl, pentadecenyl, hexadecenyl, heptadecenyl, octadecenyl, nonadecenyl, eicosenyl, heneicosenyl, , Docosenyl, octadiene-yl, nonanediazyl, decadiene-yl, undecanediazyl, dodecadienyl, tridecadienyl, tetradecadienyl , Pentadeca-diene-yl, hexadeca-dien-yl, heptadeca-dien-yl, octadeca-dien-yl, nonadeca-dien-yl,
  • the preferred (meth) acrylic monomers of the formula (II) or (III) include heptadecenyloyloxy-2-ethyl (meth) acrylamide, heptadecadienyloxy-2-ethyl (meth) acrylamide, heptadeca- then-yloyloxy-2-ethyl (meth) acrylamide, heptadecenyloyloxy-2-ethyl (meth) acrylamide, (meth) acryloyloxy-2-ethyl-palmitoleic acid amide, (meth) acryloyloxy-2-ethyl-oleic acid amide, (meth) acryloyloxy 2-ethyl-icosenoic acid amide, (meth) acryloyloxy-2-ethyl-cetolenic acid amide, (meth) acryloyloxy-2-ethyl-erucic acid amide, (
  • the notation (meth) acryl stands for acrylic and methacrylic radicals, with methacrylic radicals being preferred.
  • Particularly preferred monomers according to formula (II) or (III) are methacryloyloxy-2-ethyl-oleic acid amide, methacryloyloxy-2-ethyl-linolenic acid amide and / or methacryloyloxy-2-ethyl-linolenic acid amide.
  • the (meth) acrylic monomers of the formula (II) or (III) can be obtained in particular by multistage processes.
  • a first stage for example, an or a plurality of unsaturated fatty acids or fatty acid esters with an amine, for example, ethylenediamine, ethanolamine, propylenediamine or propanolamine, to an amide.
  • an amine for example, ethylenediamine, ethanolamine, propylenediamine or propanolamine
  • the hydroxy group or the amine group of the amide is reacted with a (meth) acrylate, for example methyl (meth) acrylate, to obtain the monomers of the formula (II) or (III).
  • intermediates obtained for example carboxamides which have hydroxyl groups in the alkyl radical
  • intermediates obtained can be purified.
  • intermediates obtained can be reacted without expensive purification to the (meth) acrylic monomers of formula (II) or (III).
  • the (meth) acrylic monomers having 8 to 40, preferably 10 to 30 and particularly preferably 12 to 20 carbon atoms and at least one double bond in the alkyl radical in particular include monomers of the general formula (IV)
  • R is hydrogen or a methyl group
  • X is oxygen or a group of the formula NR ', wherein R' is hydrogen or a radical having 1 to 6 carbon atoms
  • R 3 is an alkylene group having 1 to 22 carbon atoms
  • Y is oxygen, sulfur or a group of the formula NR ", where R" is hydrogen or a radical having 1 to 6 carbon atoms
  • R 4 is an unsaturated radical having at least 8 carbon atoms and at least two double bonds.
  • the radical R 3 is an alkylene group having 1 to 22 carbon atoms, preferably 1 to 10, more preferably 2 to 6 carbon atoms.
  • the radical R 3 represents an alkylene group having 2 to 4, more preferably 2 carbon atoms.
  • the alkylene groups having 1 to 22 carbon atoms include in particular the methylene, ethylene, propylene, iso-propylene, n-butylene, iso-butylene, t-butylene or cyclohexylene group, with the ethylene group being particularly preferred.
  • the radical R 4 comprises at least two CC double bonds which are not part of an aromatic system.
  • the radical R 4 represents a group with exactly 8 carbon atoms, which has exactly two double bonds.
  • the radical R 4 preferably represents a linear hydrocarbon radical which has no heteroatoms.
  • the radical R 4 in formula (IV) may comprise a terminal double bond.
  • the radical R 4 in formula (IV) can not comprise a terminal double bond.
  • the double bonds contained in the radical R 4 may preferably be conjugated. According to another preferred embodiment of the present invention, those contained in the radical R 4 are
  • the preferred R 4 radicals which have at least two double bonds include, among others, the octa-2,7-dienyl group, Octa-3,7-dienyl, octa-4,7-dienyl, octa-5,7-dienyl, octa-2,4-dienyl, octa-2,5-dienyl, octa-2,6-dienyl, octa 3,5-dienyl group, octa-3,6-dienyl group and octa-4,6-dienyl group.
  • the (meth) acrylic monomers of the general formula (IV) include, inter alia, 2 - [((2-E) octa-2,7-dienyl) methylamino] ethyl 2-methylprop-2-enoate, 2 - [( (2-Z) Octa-2,7-dienyl) methylamino] ethyl 2-methylprop-2-enoate, 2 - [((3-E) octa-3,7-dienyl) methylamino] ethyl-2-methylpropyl 2-enoate, 2 - [((4-Z) octa-4,7-dienyl) methylamino] ethyl 2-methylprop-2-enoate, 2 - [(octa-2,6-dienyl) methylamino] ethyl-2 -methylprop-2-enoate, 2 - [(octa-2,4-dienyl) methyl
  • the (meth) acrylic monomers of the formula (IV) set out above can be obtained in particular by processes in which (meth) acrylic acid or a (meth) acrylate, in particular methyl (meth) acrylate or ethyl (meth) acrylate with an alcohol and / or an amine is reacted. These reactions have been previously stated.
  • the starting material to be reacted with the (meth) acrylic acid or the (meth) acrylate may advantageously correspond to the formula (V),
  • X is oxygen or a group of the formula NR ', wherein R' is hydrogen or a radical having 1 to 6 carbon atoms, R 3 is an alkylene group having 1 to 22 carbon atoms, Y is oxygen, sulfur or a group of the formula NR ", where R "Represents hydrogen or a radical having 1 to 6 carbon atoms, and R 4 is an at least double unsaturated radical having at least 8 carbon atoms.
  • the preferred starting materials of the formula (V) include (methyl (octa-2,7-dienyl) amino) ethanol, (ethyl (octa-2,7-dienyl) amino) ethanol, 2-octa-2,7-dienyloxyethanol, (methyl octa-2,7-dienyl) amino () ethylamine,
  • the educts according to formula (V) can be obtained inter alia by known methods of telomerizing 1,3-butadiene.
  • the term means
  • the telomerization of 1, 3-butadiene using metal compounds comprising metals of the 8th to 10th group of the Periodic Table of the Elements can be carried out as a catalyst, wherein palladium compounds, in particular Palladiumcarbenkomplexe, which are set forth in detail in the above-mentioned documents, can be used with particular preference.
  • dialcohols such as ethylene glycol, 1, 2-propanediol, 1, 3-propanediol
  • Diamines such as ethylenediamine, N-methyl-ethylenediamine, N 1 N'-dimethylethylenediamine or hexamethylenediamine
  • aminoalkanols such as aminoethanol, N-methylaminoethanol, N-ethylaminoethanol, aminopropanol, N-methylaminopropanol or N-ethylaminopropanol.
  • (meth) acrylic acid as a nucleophile
  • octadienyl (meth) acrylates can be obtained, which are particularly suitable as (meth) acrylic monomers having 8 to 40 carbon atoms.
  • the temperature at which the Telomehsationsretress is carried out is between 10 and 180 0 C, preferably between 30 and 120 0 C, particularly preferably between 40 and 100 0 C.
  • the reaction pressure is 1 to 300 bar, preferably from 1 to 120 bar, particularly preferably 1 to 64 bar and most preferably 1 to 20 bar.
  • the preparation of isomers from compounds having an octa-2,7-dienyl group can be accomplished by isomerization of the double bonds contained in the compounds having an octa-2,7-dienyl group.
  • the above-mentioned (meth) acrylic monomers having at least one double bond and 8 to 40 carbon atoms in the alkyl group may be used singly or as a mixture of two or more monomers.
  • the (meth) acrylate polymer of the present invention comprises 0.1 to 10% by weight, preferably 0.5 to 8% by weight, and particularly preferably 1 to 5% by weight. Units derived from acid group-containing monomers based on the total weight of the (meth) acrylate polymer.
  • Acid group-containing monomers are compounds which can be preferably radically copolymerized with the previously set forth (meth) acrylic monomers. These include, for example, monomers having a sulfonic acid group, such as vinylsulfonic acid; Monomers having a phosphonic acid group, such as vinylphosphonic acid and unsaturated carboxylic acids, such as methacrylic acid, acrylic acid, fumaric acid and maleic acid. Particularly preferred are methacrylic acid and acrylic acid.
  • the acid group-containing monomers can be used individually or as a mixture of two, three or more acid group-containing monomers.
  • inventive (meth) acrylate polymers comprise 50% by weight to 99.4% by weight. %, preferably 60 wt .-% to 98 wt .-% and most preferably 80 wt .-% to 97 wt .-% of units derived from (meth) acrylates having 1 to 12 carbon atoms in the alkyl radical, which are not double bonds or heteroatoms in the alkyl radical and these (meth) acrylates having 1 to 12
  • Carbon atoms in the alkyl radical are selected so that a polymer consisting of these (meth) acrylates having 1 to 12 carbon atoms in the alkyl radical has a glass transition temperature of at least 40 0 C, based on the weight of the (meth) acrylate polymer.
  • the (meth) set forth above acrylates are selected so that a polymer consisting of these (meth) acrylates having 1 to 12 carbon atoms in the alkyl radical has a glass transition temperature of at least 40 0 C, preferably at least 50 ° C and particularly preferably at least 1 to 12 carbon atoms 60 0 C has.
  • the glass transition temperature Tg of the polymer can be determined in a known manner by means of differential scanning calorimetry (DSC), in particular according to DIN EN ISO 11357 be determined.
  • the glass transition temperature can be determined as the center of the glass stage of the second heating curve at a heating rate of 10 0 C per minute.
  • the glass transition temperature Tg can also be calculated approximately in advance by means of the Fox equation. After Fox TG, Bull. Am. Physics Soc. 1, 3, page 123 (1956): 1 x, X 1 x "
  • Tg Tg 1 Tg Tg n 2 wherein X n is the mass fraction designated n (wt .-% / 100) of monomer n and Tg n is the glass transition temperature in Kelvin of the homopolymer of the monomer. Further helpful hints can be found in the Polymer Handbook 2 nd Edition, J. Wiley & Sons, New York (1975), which gives Tg values for the most common homopolymethylates.
  • poly (methyl methacrylate) has a glass transition temperature of 378K, poly (butyl methacrylate) of 297K, poly (isobornyl methacrylate) of 383K, poly (isobornyl acrylate) of 367K, and poly (cyclohexyl methacrylate) of 356K.
  • the polymer consisting of said (meth) acrylates having 1 to 12 carbon atoms in the alkyl radical may have a weight average molecular weight of at least 100,000 g / mol and a number average molecular weight of at least 80,000 g / mol.
  • the (meth) acrylates having 1 to 12 carbon atoms in the alkyl radical described above can be used individually or as a mixture, the mixtures resulting in copolymers which exhibit a correspondingly high glass transition temperature.
  • the choice of type and amount can be made by the previously described formula of Fox et al. respectively.
  • the (meth) acrylates having 1 to 12 carbon atoms in the alkyl radical which have no double bonds or heteroatoms in the alkyl radical include, inter alia, (meth) acrylates having a linear or branched alkyl radical, such as, for example, methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, iso-propyl (meth) acrylate, n-butyl (meth) acrylate, iso-butyl (meth) acrylate, tert-butyl (meth) acrylate and Pentyl (meth) acrylate, hexyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, heptyl (meth) acrylate, octyl (meth) acrylate, 3-isopropyl-propyl (meth) acrylate, nonyl (
  • (meth) acrylate polymers having from 50 to 99.4% by weight of units derived from methyl methacrylate and / or butyl methacrylate, preferably n-butyl methacrylate, based on the weight of the (meth) acrylate polymer.
  • Particularly preferred in this context are polymers comprising from 25 to 50% by weight of units derived from methyl methacrylate and from 20 to 60% by weight of units derived from butyl methacrylate, based in each case on the weight of (meth ) acrylate polymer.
  • (meth) acrylate polymers which preferably comprise from 0.1 to 99.4% by weight, from 5 to 50% by weight and most preferably from 20 to 40% by weight of units derived from Cycloalkyl (meth) acrylates, in particular of cyclohexyl methacrylate, cyclohexyl acrylate, cyclohexyl (meth) acrylates having at least one substituent on the ring, such as tert-butylcyclohexyl methacrylate and trimethylcyclohexyl (meth) acrylate, preferably 2,4,6-Thmethylcyclohexylmethacrylat, isobornyl acrylate and / or isobornyl methacrylate derived are.
  • the (meth) acrylate polymer may comprise units derived from comonomers. These comonomers differ from the above-described units of the polymer, but can be used with the monomers set forth above copolymerize.
  • the (meth) acrylate polymer comprises at most 20% by weight, more preferably at most 10% by weight of units derived from comonomers.
  • These include, for example, (meth) acrylates having at least 13 carbon atoms in the alkyl radical, which are derived from saturated alcohols, such as, for example
  • Cycloalkyl (meth) acrylates such as 2,4,5-Th-t-butyl-3-vinylcyclohexyl (meth) acrylate, 2,3,4,5-tetra-t-butylcyclohexyl (meth) acrylate;
  • heterocyclic (meth) acrylates such as 2- (1-imidazolyl) ethyl (meth) acrylate, 2- (4-morpholinyl) ethyl (meth) acrylate, 1- (2-methacryloyloxyethyl) -2-pyrrolidone;
  • Nitriles of (meth) acrylic acid and other nitrogen-containing methacrylates such as N- (methacryloyloxyethyl) diisobutylketimine, N- (methacryloyloxyethyl) dihexadecylketimine, methacryloylamidoacetonitrile, 2-methacryloyloxyethylmethylcyanamide, cyanomethylmethacrylate;
  • Aryl (meth) acrylates such as benzyl (meth) acrylate or phenyl (meth) acrylate, wherein the aryl radicals may each be unsubstituted or substituted up to four times;
  • (Meth) acrylates having a hydroxy group in the alkyl radical in particular 2-hydroxyethyl (meth) acrylate, preferably 2-hydroxyethyl methacrylate (HEMA), hydroxypropyl (meth) acrylate, for example 2-hydroxypropyl (meth) acrylate and 3- Hydroxypropyl (meth) acrylate, preferably hydroxypropyl methacrylate (HPMA), hydroxybutyl (meth) acrylate, preferably hydroxybutyl methacrylate (HBMA), 3,4-dihydroxybutyl (meth) acrylate, 2,5-dimethyl-1,6-hexanediol (meth) acrylate, 1, 10-decanediol (meth) acrylate, glycerol mono (meth) acrylate and polyalkoxylated derivatives of (meth) acrylic acid, in particular polypropylene glycol mono (meth) acrylate having 2 to 10, preferably 3 to 6 propylene
  • the comonomers also include vinyl esters, such as vinyl acetate, vinyl chloride,
  • Maleic acid derivatives such as maleic anhydride, esters of maleic acid, for example, dimethyl maleate, methylmaleic anhydride; and fumaric acid derivatives such as dimethyl fumarate.
  • styrenic monomers such as styrene, substituted styrenes having an alkyl substituent in the side chain, such as e.g. As ⁇ -methyl styrene and ⁇ -ethyl styrene, substituted styrenes having an alkyl substituent on the ring, such as vinyl toluene and p-methyl styrene, halogenated styrenes, such as monochlorostyrenes, dichlorostyrenes, tribromostyrenes and tetrabromostyrenes.
  • styrenic monomers such as styrene, substituted styrenes having an alkyl substituent in the side chain, such as e.g. As ⁇ -methyl styrene and ⁇ -ethyl styrene, substituted styrenes having an alkyl substituent on the ring, such as vinyl toluen
  • Heterocyclic vinyl compounds such as 2-vinylpyridine, 3-vinylpyridine, 2-methyl-5-vinylpyridine, 3-ethyl-4-vinylpyridine, 2,3-dimethyl-5-vinylpyridine, vinylpyrimidine, vinylpiperidine, 9-vinylcarbazole, 3-vinylcarbazole, 4-vinylcarbazole, 1-vinylimidazole, 2-methyl-1-vinylimidazole, N-vinylpyrrolidone, 2-vinylpyrrolidone, N-vinylpyrrolidine, 3-vinylpyrrolidine, N-vinylcaprolactam, N-vinylbutyrolactam, vinyloxolane, vinylfuran, vinylthiophene, vinylthiolane, vinylthiazoles and hydrogenated vinylthiazoles, vinyloxazoles and hydrogenated vinyloxazoles; Maleimide, methylmaleimide;
  • Vinyl halides such as vinyl chloride, vinyl fluoride, vinylidene chloride and vinylidene fluoride are further examples of comonomers.
  • the weathering resistance of the coatings can be improved in particular by a reduction in the proportion of styrene monomers in the (meth) acrylate polymer or the coating agent, so that particularly UV-resistant coatings can be obtained by a styrene-free coating composition.
  • the (meth) acrylate polymer preferably has at most 20% by weight, more preferably at most 10% by weight of units derived from styrenic monomers, in particular styrene, substituted styrenes having an alkyl substituent in the side chain Substituted styrenes are derived with an alkyl substituent on the ring and / or halogenated styrenes, based on the total weight of the (meth) acrylate polymer.
  • (meth) acrylate polymers which have at most 20% by weight, particularly preferably at most 10% by weight, of units derived from further functionalized (meth) acrylates.
  • Functionalized (meth) acrylates include (meth) acrylates with hydroxy groups in the alkyl radical, aromatic and heterocyclic (meth) acrylates.
  • Another class of comonomers are crosslinking monomers.
  • Monomers have at least two double bonds with similar reactivity in a radical polymerization.
  • These include, in particular, (meth) acrylates derived from unsaturated alcohols, e.g. Allyl (meth) acrylate and vinyl (meth) acrylate; and (meth) acrylates derived from diols or higher alcohols, e.g.
  • Glycol di (meth) acrylates such as ethylene glycol di (meth) acrylate, diethylene glycol di (meth) acrylate, ethylene glycol di (meth) acrylate, tetra- and polyethylene glycol di (meth) acrylate, 1,3-butanediol di (meth) acrylate, 1,4-butanediol di ( meth) acrylate, 1,6-hexanediol di (meth) acrylate, glycerol di (meth) acrylate and diurethane dimethacrylate; (Meth) acrylates having three or more double bonds, e.g. Glycerin (meth) acrylate, thymethylolpropane (meth) acrylate,
  • the proportion of crosslinking monomers may be in the range from 0.1 to 5% by weight, more preferably in the range from 2 to 3% by weight.
  • the (meth) acrylate polymer according to the invention has a weight average molecular weight in the range from 10,000 to 60,000 g / mol, more preferably in the range from 15,000 to 40,000 g / mol.
  • Number average molecular weight of preferred (meth) acrylate polymers is in the range of 1,000 to 60,000 g / mol, more preferably in the range of 3,000 to 25,000 g / mol.
  • (Meth) acrylate polymers of interest which have a polydispersity index M w / M n in the range of 1 to 10, more preferably in the range of 1, 5 to 7 and most preferably 1, 7 to 3.
  • the molecular weight can be determined by gel permeation chromatography (GPC) against a PMMA standard.
  • the (meth) acrylate polymer may have a molecular weight distribution having at least 2 peaks, as measured by gel permeation chromatography.
  • the glass transition temperature of the (meth) acrylate polymer is preferably in the range of 10 0 C to 80 0 C, more preferably in the range of 25 to 75 ° C and most preferably in the range of 40 to 70 0 C.
  • the glass transition temperature can be over the Art and the proportion of monomers used to prepare the (meth) acrylate polymer.
  • the glass transition temperature Tg of the polymer can be determined in a known manner by means of differential scanning calohmetry (DSC), in particular according to DIN EN ISO 11357 can be determined.
  • DSC differential scanning calohmetry
  • the glass transition temperature can be determined as the center of the glass stage of the second heating curve at a heating rate of 10 0 C per minute.
  • the glass transition temperature Tg can also be calculated approximately in advance by means of the previously described Fox equation.
  • the iodine number of the inventive methacrylate polymers is preferably in the range of 1 to 60 g of iodine per 100 g of polymer, more preferably in the range of 2 to 50 g of iodine per 100 g of polymer and most preferably 5 to 40 g of iodine per 100 g Polymer, measured according to DIN 53241 -1.
  • the hydroxyl number of the polymer may preferably be in the range from 0 to 180 mg KOH / g, more preferably 0.1 to 100 mg KOH / g and most preferably in the range from 0.2 to 20 mg KOH / g.
  • the hydroxyl number can be determined according to DIN EN ISO 4629.
  • the (meth) acrylate polymers to be used according to the invention can be synthesized in particular by solution polymerizations, substance polymerizations,
  • Suspension polymerization or emulsion polymerizations can be obtained, wherein surprising advantages can be achieved by a radical solution polymerization. These methods are set forth in Ullmanns Encyclopedia of Industrial Chemistry, Sixth Edition.
  • ATRP Atom Transfer Radical Polymerization
  • NMP Non-mediated polymerization
  • RAFT Reversible Addition Fragmentation Chain Transfer
  • Useful initiators include the azo initiators well known in the art, such as AIBN and 1,1-azobiscyclohexanecarbonitrile, as well as peroxy compounds such as methyl ethyl ketone peroxide, acetyl acetone peroxide,
  • the initiators mentioned can be used both individually and in mixtures. They are preferably used in an amount of 0.05 to 10.0 wt .-%, particularly preferably 1 to 5 wt .-%, based on the total weight of the monomers. It is also preferable to carry out the polymerization with a mixture of different polymerization initiators having a different half-life.
  • the sulfur-free molecular weight regulators include, but are not limited to, dimeric ⁇ -methylstyrene (2,4-diphenyl-4-methyl-1-pentene), enol ethers of aliphatic and / or cycloaliphatic aldehydes, terpenes, ⁇ -terpinene, terpinolene, 1, 4-cyclohexadiene, 1, 4-dihydronaphthalene, 1, 4,5,8-tetrahydronaphthalene, 2,5-dihydrofuran, 2,5-dimethylfuran and / or 3, 6-dihydro-2H-pyran, preferably is dimeric ⁇ methyl styrene.
  • Mercury compounds, dialkyl sulfides, dialkyl disulfides and / or diaryl sulfides can preferably be used as the sulfur-containing molecular weight regulator.
  • the following polymerization regulators are exemplified: di-n-butylsulfide, di-n-octylsulfide, diphenylsulfide, thiodiglycol, ethylthioethanol, diisopropyl disulfide, di-n-butyl disulfide, di-n-hexyl disulfide, diacetyl disulfide, diethanol sulfide, di-t-butyl sulfide and dimethyl sulfoxide.
  • Preferred compounds used as molecular weight regulators are mercapto compounds, dialkyl sulfides, dialkyl disulfides and / or diaryl sulfides. Examples of these compounds are ethyl thioglycolate, 2-ethylhexyl thioglycolate, cysteine, 2-mercaptoethanol, 1, 3-mercaptopropanol, 3-mercaptopropane-1, 2-diol, 1, 4-mercaptobutanol, mercaptoacetic acid, 3-mercaptopropionic acid, thioglycolic acid, mercaptosuccinic acid, thioglycerol , Thioacetic acid, thiourea and alkylmercaptans such as n-butylmercaptan, n-hexylmercaptan, t-dodecylmercaptan or n-dodecylmercaptan. Particularly preferably used polymerization regulators are
  • the molecular weight regulators are preferably used in amounts of 0.05 to 10, particularly preferably 1 to 4,% by weight, based on that in the polymerization used monomers. Of course, mixtures of polymerization regulators can also be used in the polymerization.
  • the polymerization can be carried out at atmospheric pressure, lower or higher pressure.
  • the polymerization temperature is not critical. In general, however, it is in the range of -20 ° - 200 0 C, preferably 50 ° - 150 0 C and particularly preferably 80 ° - 130 0 C.
  • the polymerization can be carried out with or without solvent.
  • the term of the solvent is to be understood here broadly.
  • the preferred solvents include in particular aromatic hydrocarbons, such as toluene, xylene; Esters, in particular acetates, preferably butyl acetate, ethyl acetate, propyl acetate; Ketones, preferably ethyl methyl ketone, acetone, methyl isobutyl ketone or cyclohexanone; Alcohols, especially isopropanol, n-butanol, isobutanol; Ethers, in particular glycol monomethyl ether, glycol monoethyl ether, glycol monobutyl ether; Aliphatic, preferably pentane, hexane, cycloalkane and substituted cycloalkanes, for example cyclohexane; Mixtures of aliphatics and / or aromatics, preferably naphtha; Gaso
  • the polymers of the invention are used in particular for the preparation of coating compositions, which are also the subject of the present invention. These coating compositions are distinguished by an outstanding property spectrum, which in particular comprises excellent processability and excellent quality of the resulting coating.
  • the coating compositions of the invention can be processed in a wide temperature window, which preferably has a width of at least 20 ° C, more preferably at least 30 0 C, without affecting the quality of the coating, which is characterized in particular by a high solvent and water resistance becomes.
  • a preferred coating agent at a temperature of 15 ° C, 20 0 C, 30 0 C or 40 ° C are processed without a significant deterioration in quality is measurable.
  • the coating compositions according to the invention are very insensitive to variations in moisture during processing, so that the production of coatings with the coating compositions is very independent of weather changes.
  • the dynamic viscosity of the coating agent is dependent on the solids content and the type of solvent and can encompass a wide range. So this can be more than 20,000 mPas at high polymer content. Expediently, a dynamic viscosity in the range from 10 to 10 000 mPas, preferably 100 to 8000 mPas and very particularly preferably 1000 to 6000 mPas, measured according to DIN EN ISO 2555 at 23 ° C (Brookfield) is usually.
  • coating compositions which preferably contain from 10 to 80% by weight, particularly preferably from 25 to 65% by weight, of at least one polymer according to the invention.
  • a surprisingly good processability show coating compositions whose solids content is preferably at least 40% by weight, particularly preferably at least 60% by weight.
  • the coating compositions of the invention can be processed over a much wider temperature range than previously known coating compositions. With comparable processing properties, the coating compositions of the invention are characterized by a surprisingly high solids content, so that the coating compositions of the invention are particularly environmentally friendly.
  • the coating agents set forth above may comprise at least one solvent.
  • preferred solvents have been previously associated with free-radical polymerization so that reference is made to this.
  • the proportion of solvent in preferred coating compositions may in particular be in the range from 0.1 to 60% by weight, particularly preferably in the range from 5 to 40% by weight, based on the total weight of the coating composition.
  • the coating compositions according to the invention can also contain customary auxiliaries and additives such as rheology modifiers, defoamers, deaerators, pigment wetting agents, dispersing additives, substrate wetting agents, lubricants and flow control additives, in each case in an amount of from 0% by weight to 3% by weight, based on the total formulation, and also of water repellents , Plasticizers, thinners, UV stabilizers and adhesion promoters each containing an amount of 0 wt .-% to 20 wt .-%, based on the total formulation.
  • auxiliaries and additives such as rheology modifiers, defoamers, deaerators, pigment wetting agents, dispersing additives, substrate wetting agents, lubricants and flow control additives, in each case in an amount of from 0% by weight to 3% by weight, based on the total formulation, and also of water repellents , Plasticizers, thinners, UV stabilizers and adhesion promoter
  • the coating compositions of the invention may contain conventional fillers and pigments, e.g. Talc, calcium carbonate, titanium dioxide, carbon black, etc. in an amount of up to 50% by weight of the total composition.
  • conventional fillers and pigments e.g. Talc, calcium carbonate, titanium dioxide, carbon black, etc. in an amount of up to 50% by weight of the total composition.
  • the present invention provides a method for producing a coating in which a coating composition of the invention is applied to a substrate and cured.
  • the coating composition of the invention can be applied by conventional application methods such as dipping, rolling, flooding, casting, in particular by brushing, rolling, spraying (high pressure, low pressure, airless or electrostatic (ESTA)).
  • conventional application methods such as dipping, rolling, flooding, casting, in particular by brushing, rolling, spraying (high pressure, low pressure, airless or electrostatic (ESTA)).
  • the curing of the coating agent is carried out by physical drying and by oxidative crosslinking by means of atmospheric oxygen.
  • the oxidative curing can be accelerated by catalysts.
  • siccatives such as compounds of cobalt, manganese, lead, zirconium, iron, cerium and vanadium or alkali metal or alkaline earth metal compounds, for example lithium, Potassium and calcium, in amounts, based on the solid, oxidatively curing binder of greater than 0 wt .-% to 7 wt .-%, preferably greater than 0 to 3 wt .-% and most preferably greater than 0 to 0.5 % By weight.
  • skin preventive agents such as substituted phenols, for example di-tert-butyl-p-cresol or ketoximes can be used.
  • throughput dryers such as sodium perborate can be added if necessary.
  • the substrates which can preferably be provided with a coating composition according to the invention include, in particular, metals, in particular iron and steel, zinc and galvanized steels, as well as plastics and concrete substrates.
  • the present invention provides coated articles obtainable by a method according to the invention.
  • the coating of these objects is characterized by an excellent property spectrum.
  • Preferred coatings obtained from the coating compositions according to the invention show a high König pendulum attenuation.
  • the pendulum hardness after seven days is preferably at least 30 s, preferably at least 50 s, measured in accordance with DIN EN ISO 1522.
  • the coatings obtainable from the coating compositions according to the invention show high solvent resistance.
  • Preferred coatings show particular polar solvents, in particular alcohols, for example 2-propanol, or ketones, for example methyl ethyl ketone (MEK), nonpolar solvents, such as diesel fuel (Al kanen), a excellent resistance.
  • preferred coatings according to the present invention show a pendulum damping according to DIN ISO 1522 of preferably at least 20 s, preferably at least 40 s.
  • preferred coatings show a surprisingly good cupping.
  • preferred coatings can exhibit a depression of at least 1 mm, more preferably at least 3.0 mm, measured according to DIN 53156 (Erichsen).
  • Preferred coatings show an improved course.
  • preferred binders and coating systems of the present invention show a shortwave of preferably at most 40 units, more preferably at most 30 units and most preferably at most 10 units.
  • preferred coatings which are obtainable from the coating compositions of the invention have a surprisingly high adhesive strength, which can be determined in particular according to the cross-cut test.
  • a classification of 0 to 1, particularly preferably of 0 according to the standard DIN EN ISO 2409 can be achieved.
  • binder solution was weighed into an aluminum dish using an analytical balance. 5 ml of acetone was added and mixed with the binder solution by panning. The acetone was evaporated in a fume hood. Subsequently, the aluminum dish was placed in the drying oven at 105 ° C. for two hours. After cooling, the aluminum pan was weighed, then again stored for one hour in a drying oven and weighed again after cooling. If the weight is constant, the solids content of the binder solution is determined according to the following formula:
  • Solid binder solution in weight percent weight solid in g x 100 / initial weight of binder solution
  • the gloss values were measured according to DIN 67630.
  • the measuring angle was 60 °.
  • the molecular weight was determined by GPC on the basis of DIN EN ISO 55672-1. GPC columns from the manufacturer Varian / Polymer Laboratories were used, which were arranged with the pore sizes 10 5 , 10 6 , 10 4 , 10 3 A in succession. The individual columns were 300 mm long and had a diameter of 7.5 mm. A polymer solution with a starting concentration of 2.5 g of polymer per liter of solvent was used. It was worked with the eluent THF and a flow of 1 ml / min. The injection volume was 100 ⁇ l. The column oven is heated to 35 0 C. Detection was carried out via the Rl detector Rl 150 from Thermo Electron. The evaluation of the data was carried out with the program WinGPC of the company Polymer Standard Service (PSS).
  • PSS Polymer Standard Service
  • Mw denotes the weight-average molecular weight
  • D polydispersity index
  • the glass transition temperatures were measured with the apparatus DSC 1 from Mettler Toledo according to DIN EN ISO 11357.
  • the glass transition temperature of the center of the glass stage of the second heating curve, with 10 0 C per minute was defined.
  • the measurement of pendulum damping according to König was carried out in accordance with DIN EN ISO 1522.
  • the coating systems according to the invention and the comparison systems were applied to glass plates with a 200 ⁇ m doctor blade and dried at room temperature (23 ° C.).
  • the hiding power was determined in accordance with DIN EN ISO 6504-3. On contrast maps the Y-value was determined. Pigmentation of the binder or coating agent
  • the respective binder solution was diluted to a solids content of 60% by weight (xylene). Subsequently, a mixture comprising 66.7 wt .-% of the binder solution obtained by dilution, 20 wt .-% OO 2 (Kronos ® 2160), 0.23 wt .-% red pigment (Bayferrox ® 110) and 13.3 wt %
  • xyloo By weight of xyloo and added to 230 g of steatite balls in a 250 ml glass bottle.
  • the well-sealed glass bottle was stored on the roller bench for 24 hours. Thereafter, the steatite balls were separated by filtration from the pigmented paint.
  • the binder solution was diluted to a solids content of 60% and knife-coated onto a CoN coating sheet in a layer thickness of 75 ⁇ m.
  • the film was dried at room temperature.
  • the ripple is analyzed in a range of 0.1 to 30 mm wavelength.
  • the average values of three measurements of the longwave (LW) and the shortwave (SW) are given. The smaller the LW and SW values are, the less pronounced the wave structure is, the smoother the overall impression.
  • the fatty acid methyl ester mixture comprised 6% by weight of saturated C12 to C16 fatty acid methyl ester, 2.5% by weight of saturated C17 to C20 fatty acid methyl ester, 52% by weight of monounsaturated C18 fatty acid methyl ester, 1.5% by weight of monounsaturated C20 to C24 Fatty acid methyl ester, 36% by weight of polyunsaturated C18 fatty acid methyl ester, 2% by weight of polyunsaturated C20 to C24 fatty acid methyl esters.
  • the reaction mixture was heated to 150 0 C. Within 2 h, 19.5 ml of methanol were distilled off. The resulting reaction product contained 86.5%.
  • reaction apparatus While stirring, the reaction apparatus was purged with nitrogen for 10 minutes. Thereafter, the reaction mixture was heated to boiling. The methyl methacrylate / methanol azeotrope was separated and then the head temperature gradually increased to 100 0 C. After completion of the reaction, the reaction mixture was cooled to about 70 ° C and filtered.
  • Monomer mixture of 450 g of n-butyl methacrylate, 297 g of methyl methacrylate, 9 g of methacrylic acid, 84 g of methacryloyloxy-2-hydroxypropyl linolklareester and 25 g of n-dodecyl mercaptan were added to the reactor. Subsequently, 24 g of a 20% solution of dilauryl peroxide in xylene were added. After about 15 minutes, the remainder of the monomer mixture and 73 g of a 20% solution of dilauroyl peroxide in xylene within 120 minutes at 110 0 C was added. After another hour Stirring at 110 0 C were 29 g of a 20% solution of dilauroyl peroxide in xylene was added and stirred for one hour. The binder solution was cooled.
  • the weight average molecular weight determined by GPC was 17600 g / mol, the polydispersity index 1, 9.
  • the solids content of the binder solution was 70.2 wt .-% and the Brookfield viscosity 16800 mPas.
  • the weight average molecular weight determined by GPC was 15,300 g / mol, the polydispersity index was 1.9.
  • the solids content of the binder solution was 68.9 wt .-% and the Brookfield viscosity 3600 mPas.
  • 313 g of XyIoI were placed in a 2I jacketed reactor with paddle stirrer, reflux condenser and Stickstoffinertmaschine and heated to 90 0 C.
  • 199 g of a monomer mixture of 457 g of n-butyl methacrylate, 275 g of methyl methacrylate, 9 g of methacrylic acid, 39 g of methacryloyloxy-2-hydroxypropyl linolklareester and 16 g of n-dodecyl mercaptan were added to the reactor.
  • 30 g of a 20% solution of dilauryl peroxide in xylene were added.
  • the weight average molecular weight determined by GPC was 23,500 g / mol, the polydispersity index 2.0.
  • the resulting coating composition was pigmented in accordance with the procedure set out above. A coating obtained from the pigmented coating showed an opacity of 99.67% and a gloss at 60 ° of 85 gloss units.
  • Methacrylic acid and 16 g of n-dodecylmercaptan were added to the reactor.
  • the weight average molecular weight determined by GPC was 19,300 g / mol, the polydispersity index was 1.7.
  • the coating agent was applied to a glass plate with a 200 ⁇ m doctor blade and dried at room temperature (23 ° C). After 1 day the pendulum attenuation after king was 38 s, after 7 days 69 s and after 1 month 85 s.
  • the flow properties were determined by means of the wave scan method described above, the measured waviness having values of 1, 6 (Longwave) and 19.3 (Shortwave), respectively.
  • the resulting coating composition was pigmented in accordance with the procedure set out above.
  • a coating obtained from the pigmented coating showed an opacity of 99.55% and a gloss at 60 ° of 75 gloss units.
  • the weight average molecular weight determined by GPC was 19,400 g / mol, the polydispersity index 1, 9.
  • the desiccant coating was applied to a glass plate with a 200 ⁇ m knife and dried at room temperature (23 ° C). After 1 day the pendulum attenuation after king was 49 s, after 7 days 85 s and after 1 month 127 s. In addition, the coating agent set out above showed excellent leveling properties. Thus, the ripple measured by the wave scan method described above was only values of 0.4 (long wave) and 2.4 (short wave).
  • the resulting coating composition was pigmented in accordance with the procedure set out above.
  • a coating obtained from the pigmented coating showed an opacity of 99.67% and a gloss at 60 ° of 87 gloss units.
  • methyl methacrylate 605 g of methyl methacrylate, 804 g of n-butyl methacrylate, 17 g of methacrylic acid, 75 g of methacryloyloxy-2-hydroxypropyl linoleic acid ester, 16 g of peroxan LP and 32 g of ethylhexyl thioglycolate (TGEH) were mixed in a beaker and homogenized with stirring.
  • the monomer stock solution was pumped into the reactor.
  • the internal temperature was regulated to 85 ° C.
  • the polymerization was stopped as soon as the heat evolution stopped.
  • the batch was cooled.
  • the mother liquor was separated from the polymer beads through a filter suction filter.
  • the storage stability of the resulting polymer composition was determined by measuring the molecular weight.
  • the weight average molecular weight measured by GPC was 25,000 g / mol immediately after preparation at a polydispersity index Mw / Mn of 1.7. After 3 months storage at room temperature, the weight average molecular weight was 24,000 g / mol and the polydispersity index was 1.8.

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Family Cites Families (15)

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Publication number Priority date Publication date Assignee Title
GB793776A (en) 1954-04-07 1958-04-23 Ici Ltd Esters of drying oil acids with certain vinyl polymers
DE2129425C3 (de) 1971-06-14 1975-05-22 Chemische Werke Huels Ag, 4370 Marl Verfahren zur Herstellung von Fettsäureäthanolamiden
JPS5425530B2 (zh) 1974-03-28 1979-08-29
AT337850B (de) 1975-11-26 1977-07-25 Vianova Kunstharz Ag Verfahren zur herstellung oxidativ trocknender wasseriger polymerisatdispersionen
DE3423443A1 (de) 1984-06-26 1986-01-02 Röhm GmbH, 6100 Darmstadt Verfahren zur herstellung von estern der acryl- und methacrylsaeure durch umesterung
DE4105134C1 (zh) 1991-02-15 1992-10-08 Lankwitzer Lackfabrik Gmbh & Co.Kg, 1000 Berlin, De
GB9120584D0 (en) 1991-09-27 1991-11-06 Bp Chem Int Ltd Process for the preparation of acrylic acid and methacrylic acid esters
US5644010A (en) * 1994-07-22 1997-07-01 Toyo Ink Manufacturing Co., Ltd. Curable liquid resin, process for the production thereof and use thereof
US5750751A (en) 1995-11-02 1998-05-12 Michigan Molecular Institute Glycol co-esters of drying-oil fatty acids and vinyl carboxylic acids made via biphasic catalysis and resulting products
US6177510B1 (en) 1999-04-12 2001-01-23 Michigan Molecular Institute Air curing water base copolymers and method of preparation
CN1140493C (zh) 2000-11-24 2004-03-03 中国石化集团齐鲁石油化工公司 二(甲基)丙烯酸多元醇酯的制造方法
DE10128144A1 (de) 2001-06-09 2002-12-12 Oxeno Olefinchemie Gmbh Verfahren zur Telomerisation von nicht cyclischen Olefinen
DE10149348A1 (de) 2001-10-06 2003-04-10 Oxeno Olefinchemie Gmbh Verfahren zur Herstellung von 1-Olefin mit Palladiumcarbenverbindungen
DE10312829A1 (de) 2002-06-29 2004-01-22 Oxeno Olefinchemie Gmbh Verfahren zur Telomerisation von nicht cyclischen Olefinen
CA2576224C (en) 2004-08-03 2010-09-28 Imperial Chemical Industries Plc Low voc coatings and paints

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2010112285A1 *

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CN102356101A (zh) 2012-02-15
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WO2010112285A1 (de) 2010-10-07
US20120065322A1 (en) 2012-03-15

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