TW201226480A - Coating composition with (meth) acrylic polymers and coalescents - Google Patents
Coating composition with (meth) acrylic polymers and coalescents Download PDFInfo
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- TW201226480A TW201226480A TW100133798A TW100133798A TW201226480A TW 201226480 A TW201226480 A TW 201226480A TW 100133798 A TW100133798 A TW 100133798A TW 100133798 A TW100133798 A TW 100133798A TW 201226480 A TW201226480 A TW 201226480A
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- Taiwan
- Prior art keywords
- meth
- weight
- acrylate
- acid
- coating material
- Prior art date
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- 229920000058 polyacrylate Polymers 0.000 title claims abstract description 31
- 239000008199 coating composition Substances 0.000 title description 3
- 239000000178 monomer Substances 0.000 claims abstract description 109
- 238000000576 coating method Methods 0.000 claims abstract description 105
- 125000004432 carbon atom Chemical group C* 0.000 claims abstract description 96
- 239000011248 coating agent Substances 0.000 claims abstract description 90
- 239000006185 dispersion Substances 0.000 claims abstract description 89
- 239000000463 material Substances 0.000 claims abstract description 73
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 62
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims description 130
- -1 diallyl ester Chemical class 0.000 claims description 111
- 125000000217 alkyl group Chemical group 0.000 claims description 75
- 229920000642 polymer Polymers 0.000 claims description 56
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 42
- 239000002253 acid Substances 0.000 claims description 39
- 150000002148 esters Chemical group 0.000 claims description 35
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 239000003795 chemical substances by application Substances 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 10
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims description 6
- 239000011258 core-shell material Substances 0.000 claims description 6
- 125000003158 alcohol group Chemical group 0.000 claims description 5
- 238000009835 boiling Methods 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 2
- 239000005977 Ethylene Substances 0.000 claims description 2
- 150000002923 oximes Chemical class 0.000 claims description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 74
- 239000000203 mixture Substances 0.000 description 59
- 235000019441 ethanol Nutrition 0.000 description 51
- 238000002360 preparation method Methods 0.000 description 38
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 36
- 238000006116 polymerization reaction Methods 0.000 description 34
- 239000002904 solvent Substances 0.000 description 28
- 239000007787 solid Substances 0.000 description 27
- 125000004494 ethyl ester group Chemical group 0.000 description 25
- 238000006243 chemical reaction Methods 0.000 description 21
- 150000001875 compounds Chemical class 0.000 description 21
- 125000000250 methylamino group Chemical group [H]N(*)C([H])([H])[H] 0.000 description 20
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 20
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 19
- 150000001412 amines Chemical class 0.000 description 18
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 16
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 16
- 230000015572 biosynthetic process Effects 0.000 description 16
- 239000003995 emulsifying agent Substances 0.000 description 15
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 15
- 239000001257 hydrogen Substances 0.000 description 14
- 229910052739 hydrogen Inorganic materials 0.000 description 14
- 238000000034 method Methods 0.000 description 14
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 14
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical group C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 13
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical group C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 13
- 230000009477 glass transition Effects 0.000 description 13
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 12
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 12
- 238000001035 drying Methods 0.000 description 12
- 239000002245 particle Substances 0.000 description 12
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 12
- YHYGSIBXYYKYFB-VOTSOKGWSA-N (2e)-octa-2,7-dien-1-ol Chemical compound OC\C=C\CCCC=C YHYGSIBXYYKYFB-VOTSOKGWSA-N 0.000 description 11
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 11
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 11
- 150000001298 alcohols Chemical class 0.000 description 11
- 239000000194 fatty acid Substances 0.000 description 11
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 11
- 229910052760 oxygen Inorganic materials 0.000 description 11
- 239000001301 oxygen Substances 0.000 description 11
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 10
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 10
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 10
- 239000002585 base Substances 0.000 description 10
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 10
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 9
- 235000019395 ammonium persulphate Nutrition 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 239000000839 emulsion Substances 0.000 description 9
- MHZGKXUYDGKKIU-UHFFFAOYSA-N Decylamine Chemical compound CCCCCCCCCCN MHZGKXUYDGKKIU-UHFFFAOYSA-N 0.000 description 8
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 8
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 8
- 125000003342 alkenyl group Chemical group 0.000 description 8
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 8
- 235000019387 fatty acid methyl ester Nutrition 0.000 description 8
- 125000005842 heteroatom Chemical group 0.000 description 8
- AOESAXAWXYJFNC-UHFFFAOYSA-N bis(prop-2-enyl) propanedioate Chemical compound C=CCOC(=O)CC(=O)OCC=C AOESAXAWXYJFNC-UHFFFAOYSA-N 0.000 description 7
- 125000002704 decyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 7
- 235000014113 dietary fatty acids Nutrition 0.000 description 7
- 150000002170 ethers Chemical class 0.000 description 7
- 229930195729 fatty acid Natural products 0.000 description 7
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 7
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 6
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 6
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 239000000084 colloidal system Substances 0.000 description 6
- 238000007720 emulsion polymerization reaction Methods 0.000 description 6
- 125000000031 ethylamino group Chemical group [H]C([H])([H])C([H])([H])N([H])[*] 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- GEMHFKXPOCTAIP-UHFFFAOYSA-N n,n-dimethyl-n'-phenylcarbamimidoyl chloride Chemical compound CN(C)C(Cl)=NC1=CC=CC=C1 GEMHFKXPOCTAIP-UHFFFAOYSA-N 0.000 description 6
- 239000012038 nucleophile Substances 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- 230000001681 protective effect Effects 0.000 description 6
- 239000000376 reactant Substances 0.000 description 6
- 150000003440 styrenes Chemical class 0.000 description 6
- PLCFYBDYBCOLSP-UHFFFAOYSA-N tris(prop-2-enyl) 2-hydroxypropane-1,2,3-tricarboxylate Chemical compound C=CCOC(=O)CC(O)(CC(=O)OCC=C)C(=O)OCC=C PLCFYBDYBCOLSP-UHFFFAOYSA-N 0.000 description 6
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 6
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 6
- VZXTWGWHSMCWGA-UHFFFAOYSA-N 1,3,5-triazine-2,4-diamine Chemical compound NC1=NC=NC(N)=N1 VZXTWGWHSMCWGA-UHFFFAOYSA-N 0.000 description 5
- 239000004908 Emulsion polymer Substances 0.000 description 5
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 5
- 229910052783 alkali metal Inorganic materials 0.000 description 5
- 125000002947 alkylene group Chemical group 0.000 description 5
- 239000008346 aqueous phase Substances 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 150000004665 fatty acids Chemical class 0.000 description 5
- 239000012634 fragment Substances 0.000 description 5
- 239000003999 initiator Substances 0.000 description 5
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 5
- 239000004922 lacquer Substances 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
- 238000012986 modification Methods 0.000 description 5
- 230000000379 polymerizing effect Effects 0.000 description 5
- 238000010526 radical polymerization reaction Methods 0.000 description 5
- 229920006395 saturated elastomer Polymers 0.000 description 5
- 239000007858 starting material Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- HZYABSBSRWFZEG-BSWSSELBSA-N (1E,3E)-octa-1,3-dien-1-ol Chemical compound CCCC\C=C\C=C\O HZYABSBSRWFZEG-BSWSSELBSA-N 0.000 description 4
- MIJJHRIQVWIQGL-UHFFFAOYSA-N 8-methoxyocta-1,6-diene Chemical compound COCC=CCCCC=C MIJJHRIQVWIQGL-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 4
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 4
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical group CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- 150000001721 carbon Chemical group 0.000 description 4
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 description 4
- 235000020778 linoleic acid Nutrition 0.000 description 4
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 4
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 125000005395 methacrylic acid group Chemical group 0.000 description 4
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 description 4
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 4
- 229920000151 polyglycol Polymers 0.000 description 4
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- 230000008569 process Effects 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Chemical compound [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 description 4
- 230000008961 swelling Effects 0.000 description 4
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 4
- YPFDHNVEDLHUCE-UHFFFAOYSA-N 1,3-propanediol Substances OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 3
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
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- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 3
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 description 3
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 3
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 3
- 150000003863 ammonium salts Chemical class 0.000 description 3
- 239000012874 anionic emulsifier Substances 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 125000002511 behenyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 3
- 229910052797 bismuth Inorganic materials 0.000 description 3
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 3
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- 239000012986 chain transfer agent Substances 0.000 description 3
- 229910017052 cobalt Inorganic materials 0.000 description 3
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- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 3
- 150000002009 diols Chemical class 0.000 description 3
- ZQPPMHVWECSIRJ-MDZDMXLPSA-N elaidic acid Chemical compound CCCCCCCC\C=C\CCCCCCCC(O)=O ZQPPMHVWECSIRJ-MDZDMXLPSA-N 0.000 description 3
- 125000004185 ester group Chemical group 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 150000002191 fatty alcohols Chemical class 0.000 description 3
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- BXWNKGSJHAJOGX-UHFFFAOYSA-N hexadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCO BXWNKGSJHAJOGX-UHFFFAOYSA-N 0.000 description 3
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- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 3
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- 125000004079 stearyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 3
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- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
- IHTCZSNKQINGDD-UHFFFAOYSA-M trimethyl-[(5-methylfuran-2-yl)methyl]azanium;iodide Chemical compound [I-].CC1=CC=C(C[N+](C)(C)C)O1 IHTCZSNKQINGDD-UHFFFAOYSA-M 0.000 description 1
- 125000005065 undecenyl group Chemical group C(=CCCCCCCCCC)* 0.000 description 1
- 125000002948 undecyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
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Classifications
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- 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
- C08F220/62—Monocarboxylic acids having ten or more carbon atoms; Derivatives 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
- C08F293/00—Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule
- C08F293/005—Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule using free radical "living" or "controlled" polymerisation, e.g. using a complexing agent
-
- 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
- C09D153/00—Coating compositions based on block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Coating compositions based on derivatives of such polymers
-
- 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
- C08F2438/00—Living radical polymerisation
- C08F2438/03—Use of a di- or tri-thiocarbonylthio compound, e.g. di- or tri-thioester, di- or tri-thiocarbamate, or a xanthate as chain transfer agent, e.g . Reversible Addition Fragmentation chain Transfer [RAFT] or Macromolecular Design via Interchange of Xanthates [MADIX]
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Abstract
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201226480 六、發明說明: 【發明所屬之技術領域】 本發明有關包含(甲基)丙烯酸系聚合物分散液及聚結 劑之水性塗覆材料。 【先前技術】 長久以來’塗覆材料(尤其是漆)係經合成製造。該等 材料的重要群組之一係基於水性分散液者,其在許多情況 中包含(甲基)丙烯酸酯聚合物。例如,公開案DE-A-4 1 05 134描述包含甲基丙烯酸烷酯黏合劑之水性分散液。這種 漆可另外從 US 5,750,75 1、EP-A-1 044 993、WO 2006/013061 及 WO 2008/094503 得知。 前文所述之塗覆材料的性質範圍已屬良好。然而,仍 持續有改良此性質範圍之需求。 特定的缺點係前文所述之塗覆材料在某些情況中顯現 出不足以應付較高需求的加工性質。因此,US 5,750,751 中所述之塗覆材料中必須添加有機溶劑。基於環境保護的 理由,應避免使用該等溶劑。 經由公開案EP-A- 1 044 993之教示,獲致該方面的一 項改善。該文件描述基於(甲基)丙烯酸酯之水性分散液。 其用於聚合之混合物包含經使用不飽和脂肪酸改質之(甲 基)丙烯酸酯。該解決方案的關鍵之一在於使用具有特別 廣之分子量分布之聚合物,該分子量之數量平均落在300 至3 000 g/mol範圍。然而,該系統的缺點在於所獲得之薄 201226480 膜對許多應用而言太軟。 此外,文件 WO 200 6/0 13061描述包含基於(甲基)丙 烯酸酯之粒子的分散液。用於製備該等粒子之單體混合物 包含經使用不飽和脂肪酸改質之(甲基)丙烯酸酯。關於分 散液的具體缺點,WO 2006/0 1 306 1描述其複雜製備以及 高比例殘留單體。 除了水性分散液之外,反應性漆形成另一群組習知之塗 覆材料。此等漆係從例如ΕΡ-0 693 507習知。亦已知的是包含 被稱爲反應性稀釋劑之組成物。例如,公開案EP-A-546 4 1 7 描述特別是包含辛二烯基醚之塗覆組成物。具有反應性溶 劑之塗覆材料係陳述於包括US 2009/ 1 5 1 60 1 A1之公開案 中,所引用之公開案並未指定已使用不飽和脂肪酸改質之 (甲基)丙烯酸酯作爲聚合物。 前文所述之塗覆材料的性質範圍已屬良好。然而,仍 需要改良性質之範圍。因此,可從前文所述之塗覆材料獲 得之塗層展現出機械抗性,尤其是耐刮性,其不足以應付 提高之需求。其他塗覆材料展現出非常高之最低成膜溫度 ,因此必須與溶劑摻合以便加工。 【發明內容】 本著先前技術,本發明目的在於提出展現傑出性質槪 要的塗覆材料。該等性質包括藉由塗覆材料及藉由可從該 等塗覆材料獲得之塗層表現的更明確特徵。 塗覆材料特別是應該非常環保。爲了達到此目的,該 -6- 201226480 材料應具有極低殘留單體含量,且在加工過程中應該只有 少部分有機化合物釋放至環境中》 因此’本發明另一目的係提出具有特別長儲存壽命及 可維持性之塗覆材料。此外,可從塗覆材料獲得之塗層的 硬度應可在廣泛範圍內改變。特別是,應可獲得特別硬之 耐刮塗層。 可從該等水性分散液獲得之塗層應具有高耐候化安定 性’尤其是高耐UV性。此外,可從該等水性分散液獲得 之薄膜在短時間之後應具有低膠黏性。 此外’可從該等塗覆材料獲得之塗層應展現出高化學 抗性。在這方面’應獲致對於眾多不同溶劑以及鹼及酸的 高度安定性。尤其是,應對於甲基異丁基酮(MIBK)具有非 常良好之抗性。 此外,該塗覆材料應展現出良好加工性質,尤其是藉 由低最低成膜溫度但不損及可從該等塗覆材料獲得之塗層 的機械性質或化學抗性來表現。 另一目的可視爲所述之塗覆材料可以非常價廉& & ^ 業規模獲得。 該等及雖然未明確陳述但可從本文引言所討論@ # 下容易明暸之其他目的係藉由具有申請專利範圍第i 所有特徵的水性分散液獲致。該分散液之有用修& $ 附項中受到保護。 因此本發明提出包含至少一種(甲基)丙烯酸系聚& % 分散液與至少一種聚結劑的水性塗覆材料,該材料胃@ & 201226480 於該(甲基)丙烯酸系聚合物包含從烷基中具有至少一個雙 鍵與8至40個碳原子之(甲基)丙烯酸系單體所衍生之單元 ,而該聚結劑具有至少一個乙烯系不飽和雙鍵且分子量低 於 1000g/mol〇 本發明之塗覆材料具有傑出之性質槪要。尤其是,本 發明之塗覆材料非常環保,具有非常低之殘留單體含量, 及在加工過程中僅釋放出少部分之有機化合物至環境中》 可從基於聚合物或組成物的本發明塗覆材料獲得之塗 層的硬度可在廣泛範圍內改變。尤其令人驚異的是,可能 獲得以高斷裂伸長率及/或高抗張強度受注目之機械安定 性塗層。 此外,可從本發明塗覆材料獲得之塗層展現出相對於 硬度及化學抗性而言較低之脆度。 根據一較佳修改,可能根據本發明,特別是獲得特別 硬之耐刮塗層。可從本發明分散液獲得之塗層展現出令人 驚異的高溶劑抗性,其尤其在使用甲基異丁基酮(MIBK)、 氨溶液或乙醇之試驗中表現出。因此,所獲得之塗層在尤 其是根據DIN 68 8 6 1 - 1傢倶試驗的試驗中展現出傑出的分 級。 本發明之塗覆材料尤其展現出良好加工性質,其從低 最低成膜溫度尤其可清楚看出,且不會損及可從該塗覆材 料獲得之塗層的機械性質或化學抗性。可從該等塗覆材料 或聚合物獲得之塗層具有相當的化學抗性及/或相當的垂 擺硬度,因此本發明之塗覆材料展現出特別低之最低成膜 -8- 201226480 溫度。該等分散液具有相當之最低成膜溫度,可從該等分 散液獲得之塗層展現出經改良的化學抗性及提高之垂擺硬 度。 此外,本發明之分散液展現出高儲存安定性、高可維 持性及非常良好之儲存壽命。更明確地說,實質上未形成 聚集體。 關於表現能力,該等分散液展現出經改良之環境相容 性。較佳之具體實例顯示實質上未釋放出有機化合物(更 明確地指溶劑)至大氣中。此外,該等塗覆材料具有極低 之殘留單體含量。 可從本發明塗覆材料獲得之塗層顯示高耐候化安定性 ,更明確地說爲高耐UV性。此外,可從該等分散液獲得 之薄膜在短時間之後具有低膠黏性。 本發明之塗覆材料可以低價方式大規模製造。本發明 之塗覆材料環保,且能可靠地製備及加工而無高昂成本及 複雜性。同時,本發明之塗覆材料展現出非常高之剪切安 定性。 本發明之塗覆材料爲水性分散液。因此’其包含分散 有聚合物粒子之水相。本技術中已習知「分散液」一詞。 水性塗覆材料包含至少一種聚結劑。本技術中已知「 聚結劑」一詞,其係指降低存在分散液中之聚合物的最低 成膜溫度之添加劑。本例中所使用之聚結劑的分子量不超 過1000 g/mol,較佳係不超過800 g/mol。聚結劑的分子 量較佳係落在120至600 g/mol之範圍,更佳係在140至 201226480 500 g/mol之範圍。 根據本發明一特定具體實例,該聚結劑包含不超過3〇 ,較佳係不超過20,特別是不超過15,最佳不超過8個 碳原子。 因此,特別重要的是在大氣壓力(1013 mbar)下沸點爲 至少140°C,較佳爲至少18(TC,更佳爲至少190°C之聚結 劑。根據一較佳具體實例,在大氣壓力下該聚結劑的沸點 可落在140至3 50°C之範圍,更佳在180至300°C之範圍。 根據本發明,該聚結劑具有至少一個,較佳爲至少兩 個乙烯系不飽和雙鍵。在這方面,較佳聚結劑之碳原子對 乙烯系不飽和雙鍵之比例在3: 1至8: 1之範圍,更佳爲 4 : 1 至 6 : I。 該聚結劑較佳可具有在3至19之範圍,更佳在9至16 之範圍的HLB値,該値係藉由0^[^11(3)〇1^^11,\^.(:.,>1· Soc. Cosmetic Chem., 1, 3 1 1 (1 949), b) ICI Bulletin, HLB System,8,(1 984)之方法計算。 根據本發明一具體實施樣態,根據本發明使用之聚結 劑爲醇、胺、醚或酯,更佳爲醇之酯。該聚結劑較佳包含 至少兩個乙烯系不飽和雙鍵。因此,較佳化合物爲具有二 烯基者及/或從多官能化合物衍生者,其實例爲具有二或 更多個官能基之醇及/或酸,更明確地說爲羧酸。 根據本發明一具體實施樣態,較佳者更明確地說爲具 有至少一個辛二烯基之聚結劑。該聚結劑較佳可構成醇、 胺、醚或酯。因此,該等化合物包含至少一個具有式-R之 -10- 201226480 基,其中R代表具有正好8個碳原子且具有兩個碳碳 之基。較佳之具有正好8個碳原子與2個雙鍵的基更 地包括辛-2,7-二烯基、辛-3,7-二烯基、辛-4,7-二烯 辛·5,7-二烯基、辛-2,4-二烯基、辛-2,5-二烯基、辛 二烯基、辛-3,5-二烯基、辛-3,6-二烯基及辛-4,6-二 〇 較佳之醇更具體地包括辛-2,7-二烯醇、辛-3,7·二 、辛-4,7-二烯醇、辛-5,7-二烯醇、辛-2,4-二烯醇 2,5-二烯醇、辛-2,6-二烯醇、辛-3,5-二烯醇、辛-3,6-醇及辛-4,6-二烯醇。 此外,具有一或多個辛二烯基之酯係在較佳使用 結劑當中。適用之衍生出酯的羧酸可爲直鏈、支鏈、 、飽和或不飽和羧酸。 除脂族酸之外,亦可使用芳族酸。在該情況中更 包括者爲從單羧酸衍生之上述辛二烯醇的酯。較佳之 酸具有1至20,較佳爲1至10,更佳爲1至4個碳 。該等較佳單羧酸更具體地包括甲酸、乙酸、丙酸、 、丙烯酸及甲基丙烯酸。該等聚結劑較佳係具有正好 辛二烯基。從較佳具有1至20個碳原子之單羧酸所 的較佳酯之分子量較佳爲150至500 g/mol,更佳爲 至 300 g/mol。 此外,亦可使用具有兩個、三個或更多個羧酸基 酸之酯,例如草酸之酯、檸檬酸之酯、對苯二甲酸之 反丁烯二酸之酯、順丁烯二酸之酯或己二酸之酯。較 雙鍵 具體 基' '2,6- 烯基 烯醇 辛- 二烯 之聚 環狀 具體 單羧 原子 丁酸 一個 衍生 150 的羧 酯、 佳之 -11 - 201226480 多羧酸具有2至20,較佳爲2至10,更佳爲2至6個碳 原子。在這方面特別重要的是具有一個、兩個或更多個辛 二烯基的多羧酸之酯。從較佳具有1至20個碳原子之多 羧酸所衍生的較佳酯之分子量較佳爲200至1000 g/m〇l, 更佳爲300至600 g/mol。 醚更具體地包括從較佳具有1至10個碳原子之單醇 所衍生之醚基的化合物。該等單醇可呈直鏈、環狀或支鏈 形式。此外,可使用不飽和、飽和或芳族醇製備該等醚。 包括於其中者更具體地說爲上述辛二烯醇之甲基醚、乙基 醚、丙基醚、丁基醚、戊基醚及己基醚。該等醚之實例尤 其爲甲氧基辛-2,7-二烯(甲基辛-2,7-二烯基醚)、乙氧基 辛-2,7-二烯及丙氧基辛-2,7二烯。從較佳具有1至1〇個 碳原子之單醇所衍生的較佳醚之分子量較佳爲140至300 g/mol,更佳爲140至25 0 g/mol。特佳之醚爲從寡聚伸烷 基(oligoalkylene)或聚伸烷基(polyalkylene)所衍生且除至 少一個辛二烯基外包含環氧烷單元之化合物,特佳係例如 具有2至40,更佳爲3至10個環氧乙烷單元及/或環氧丙 烷單元之醚。該等化合物包括例如二乙二醇辛-2,7-二烯基 醚、三乙二醇辛-2,7-二烯基醚、四乙二醇辛-2,7-二烯基醚 、五乙二醇辛-2,7-二烯基醚、六乙二醇辛-2,7-二烯基醚、 二丙二醇辛-2,7-二烯基醚、三丙二醇辛-2,7-二烯基醚、四 丙二醇辛-2,7-二烯基醚、五丙二醇辛-2,7-二烯基醚及六丙 二醇辛-2,7-二烯基醚。 根據本發明其他具體實例,可使用具有兩個、三個或 -12- 201226480 更多個羥基的醇之醚。該等多元醇較佳具有 原子,且該等醇可爲直鏈、支鏈、環狀、飽 芳族醇。其特別包括乙二醇、丙二醇、甘油 烷、新戊四醇、二新戊四醇、甘露醇、山梨 等醇之混合物的醚。在該情況中具有上述辛 醇的醚可具有一個、兩個、三個或更多個辛 之化合物更具體地包括單辛-4,6-二烯氧乙 4,6-二烯氧乙烷、單辛-4,6-二烯氧丙二醇、 氧丙醇、三辛-2,7-二烯氧丙烷、單辛-2,7-1,2-二辛-2,7-二烯氧乙烷、單辛-2,7-二烯 辛-2,7-二烯氧丙醇及三辛-2,7-二烯氧丙烷。 使用或作爲二或更多者之混合物使用。從較 個碳原子之多元醇所衍生的較佳醚之分子量 8 00 g/mol > 更佳爲 170 至 600 g/mol。 除了該等醚及醇之外,亦可使用胺。在 使用具有一個、兩個或更多個胺基之化合物 含8至20個碳原子。較佳之胺更具體地包 基胺、辛-3,7-二烯基胺、辛-4,7-二烯基胺 基胺、辛-2,4-二烯基胺、辛-2,5-二烯基胺 基胺、辛-3,5-二烯基胺、辛-3,6-二烯基胺 基胺、(甲基(辛-2,7-二烯基)胺基)乙醇、(2 烯基)胺基)乙醇、2-辛-2,7-辛-2,7-二烯氧乙 2,7-二烯基)胺基)乙胺。較佳之胺的分子量Μ 800 g/mol,更佳爲 170 至 600 g/mol。 2至10個碳 :和、不飽和或 丨、三羥甲基丙 :醇、蔗糖或此 二烯醇之多元 '二烯基。較佳 醇 ' 1,2-二辛-二辛-4,6-二烯 二烯氧乙醇、 氧丙二醇、二 該等醚可個別 佳具有2至10 較佳爲1 7 0至 該情況下,可 。較佳之胺包 括辛-2,7-二烯 、辛-5,7-二烯 、辛-2,6-二烯 、辛-4,6-二烯 L 基(辛-2,7-二 醇及(甲基(辛-較佳爲1 4 0至 -13- 201226480 在所述化合物類別當中,特佳者尤其是具有二或更多 個環氧烷單元之醇及醚,以醇尤佳。 上述醇、胺、醚或酯可藉由各種不同方法獲得,包括 1,3 -丁二烯之短鏈聚合的習知方法。本文所使用之「短鏈 聚合」一詞表示在親核劑存在下具有共軛雙鍵之化合物的 反應。於公開案 WO 2004/002931、WO 03/031379 及 WO 02/ 1 00803中所陳述之方法,尤其是用於該反應之觸媒及 反應條件,諸如壓力及溫度,係出於揭示目的倂入本說明 書中。 1,3 -丁二烯之短鏈聚合較佳可使用包含元素週期表第 8至1 0族之金屬的金屬化合物作爲觸媒來進行,尤佳情況 可使用鈀化合物,更佳爲鈀-碳烯錯合物,此於前文陳述 之公開案中更詳細說明。 至於親核劑,特別是可使用水、氨、單醇、多元醇, 尤其是二醇,諸如乙二醇、1,2-丙二醇及1,3-丙二醇;二 胺,諸如乙二胺、N-甲基乙二胺、N,N'-二甲基乙二胺或 六亞甲二胺;胺基醇,諸如胺乙醇、N-甲胺乙醇、N-乙胺 乙醇、胺丙醇' N-甲胺丙醇或N-乙胺丙醇,或羧酸,更 明確地說爲前文詳細說明之單羧酸及多羧酸。公開案WO 2004/00293 1、WO 03/03 1 3 79 及 WO 02/1 00803 中所述之 親核劑係基於揭示目的倂入本說明書中。 進行短鏈聚合反應之溫度係介於1 0與1 80°c之間,較 佳係介於30與120°C之間,更佳係介於40與100°C之間。 反應壓力爲1至300巴,較佳爲1至120巴,更佳爲1至 -14- 201226480 64巴,最佳1至20巴。 具有辛-2,7-二烯基之化合物的異構物可藉由將存在具 有辛-2,7-二烯基之化合物中的雙鍵異構化而製備。 若在酯化反應中具有辛二烯基醚基之醇與單羧酸或多 殘酸反應及/或與多羧酸酐反應,則獲得根據本發明尤其 適用之聚結劑。特別適用於該等反應者爲於起始點時係至 少基於三元醇或基於平均官能度至少爲三之醇混合物且平 均每個分子具有至少一個自由羥基之短鏈聚合物。尤其適 用於酯化反應者爲羥基含量爲5.5至17重量%之甘油與丁 二烯的短鏈聚合產物及/或羥基含量爲4.9至14.0重量%之 三羥甲基丙烷與丁二烯的短鏈聚合產物。 此外’具有辛二烯基之較佳聚結劑係述於公開案EP-A-0 5 46 4 1 7中,其中所述之反應性稀釋劑及其製備方法 係基於揭示目的倂入本說明書中。 根據本發明另一較佳實施樣態,尤其是具有兩個、三 個或更多個羧酸基之羧酸的酯亦可用作聚結劑,諸如草酸 之酯、丙二酸之酯、檸檬酸之酯、對苯二甲酸之酯、反丁 烯二酸之酯、順丁烯二酸之酯或己二酸之酯,彼等具有至 少一個,較佳爲至少兩個乙烯系不飽和雙鍵。較佳之多羧 酸具有2至20,較佳爲2至10,更佳爲2至6個碳原子 。在這方面尤佳者爲具有2至6,較佳爲2至4個碳原子 之乙烯系不飽和醇。其更具體地包括烯丙醇及乙烯醇。因 此,較佳者尤其是丙二酸二烯丙酯、丙二酸二乙烯酯及檸 檬酸三烯丙酯,以丙二酸二烯丙酯尤佳。 -15- 201226480 除了前文所述之聚結劑以外,本發明之塗覆材料包含 至少一種具有至少一種(甲基)丙烯酸系聚合物的水性分散 液,該(甲基)丙烯酸系聚合物具有從烷基中具有至少一個 雙鍵及8至40個碳原子的(甲基)丙烯酸系單體所衍生之單 元。 「聚合物」一詞意指包含可藉由將烷基中具有至少一 個雙鍵與8至40個碳原子之(甲基)丙烯酸系單體彼此反應 或與其他單體反應獲得之化合物的分散液,該反應可在一 個步驟中發生或在數個階段中發生。 該分散液可包含一或多種具有從烷基中具有至少一個 雙鍵與8至40個碳原子之(甲基)丙烯酸系單體所衍生之重 複單元的聚合物。該等聚合物的例如烷基中具有至少一個 雙鍵與8至40個碳原子之(甲基)丙烯酸系單體的比例、或 鏈長、溶解性表現或其他性質方面可不同。 該聚合物較佳可藉由自由基聚合獲得。因此,「重複 單元」一詞係從用於製備聚合物之單體產生。 烷基中具有至少一個雙鍵與8至40個碳原子之(甲基) 丙烯酸系單體爲烷基具有至少一個碳碳雙鍵及8至40個 碳原子之(甲基)丙烯酸的酯或醯胺。(甲基)丙烯酸表示法 表示甲基丙烯酸及丙烯酸以及其混合物。烷基或醇或醯胺 基較佳可具有10至30,更佳爲12至20個碳原子,且該 基可包含雜原子,更明確地說,包含氧、氮或硫原子。烷 基可具有一個、兩個、三個或更多個碳碳雙鍵。製備該( 甲基)丙烯酸酯聚合物之聚合條件較佳係經選擇以使在該 -16- 201226480 聚合作用中仍保留之烷基的雙鍵之比例最大化。此可例如 藉由位阻該醇基中存在之雙鍵來完成。此外,至少部分或 較佳係所有存在該(甲基)丙烯酸系單體中的烷基中之雙鍵 在自由基聚合作用中的反應性低於(甲基)丙烯酸基,因此 在該烷基中較佳係不存在其他(甲基)丙烯酸基。 用於製備(甲基)丙烯酸系聚合物且烷基中具有至少一 個雙鍵與8至40個碳原子之(甲基)丙烯酸系單體的碘値較 佳爲至少50,更佳爲至少1〇〇,最佳爲至少125 g碘/100 g(甲基)丙烯酸系單體。 該種類之(甲基)丙烯酸系單體大致符合式(I)201226480 VI. Description of the Invention: [Technical Field] The present invention relates to an aqueous coating material comprising a (meth)acrylic polymer dispersion and a coalescent. [Prior Art] Coating materials (especially lacquers) have been synthetically manufactured for a long time. One of the important groups of such materials is based on aqueous dispersions, which in many cases comprise (meth)acrylate polymers. For example, the publication DE-A-4 051 134 describes an aqueous dispersion comprising an alkyl methacrylate binder. Such a lacquer is known from US 5,750,75 1 , EP-A-1 044 993, WO 2006/013061 and WO 2008/094503. The range of properties of the coating materials described above is already good. However, there is still a continuing need to improve the scope of this property. A particular disadvantage is that the coating materials described above appear to be insufficient in some cases to cope with the processing properties of higher demand. Therefore, an organic solvent must be added to the coating material described in US 5,750,751. These solvents should be avoided for reasons of environmental protection. An improvement in this regard has been achieved through the teachings of the publication EP-A-1 044 993. This document describes an aqueous dispersion based on (meth) acrylate. The mixture used for the polymerization contains (meth) acrylate which has been modified with an unsaturated fatty acid. One of the keys to this solution is the use of polymers having a particularly broad molecular weight distribution, the number of which falls on the average range of 300 to 3 000 g/mol. However, the disadvantage of this system is that the thin 201226480 film obtained is too soft for many applications. Furthermore, document WO 200 6/0 13061 describes dispersions comprising particles based on (meth) acrylate. The monomer mixture used to prepare the particles comprises a (meth) acrylate modified with an unsaturated fatty acid. With regard to the specific disadvantages of the dispersion, WO 2006/0 1 306 1 describes its complex preparation as well as a high proportion of residual monomers. In addition to aqueous dispersions, reactive lacquers form another group of conventional coating materials. Such paints are known, for example, from ΕΡ-0 693 507. It is also known to comprise a composition known as a reactive diluent. For example, the publication EP-A-546 4 1 7 describes in particular a coating composition comprising octadienyl ether. A coating material having a reactive solvent is set forth in the publication including US 2009/1 5 1 60 1 A1, the disclosure of which is hereby incorporated by reference in its entirety in its entirety assigned the assigned the the the Things. The range of properties of the coating materials described above is already good. However, there is still a need to improve the range of properties. Therefore, the coating which can be obtained from the coating material described above exhibits mechanical resistance, especially scratch resistance, which is insufficient to cope with the increased demand. Other coating materials exhibit very high minimum film forming temperatures and must therefore be blended with solvents for processing. SUMMARY OF THE INVENTION In view of the prior art, it is an object of the present invention to provide a coating material that exhibits outstanding properties. These properties include more specific features exhibited by the coating material and by coatings obtainable from such coating materials. The coating material should in particular be very environmentally friendly. In order to achieve this, the -6-201226480 material should have a very low residual monomer content, and only a small part of the organic compound should be released into the environment during processing. Therefore, another object of the present invention is to have a particularly long storage life. And maintainable coating materials. Furthermore, the hardness of the coating obtainable from the coating material should be varied over a wide range. In particular, a particularly hard scratch resistant coating should be obtained. The coatings obtainable from such aqueous dispersions should have high weathering stability, especially high UV resistance. Further, the film obtainable from the aqueous dispersions should have a low adhesiveness after a short period of time. Furthermore, coatings obtainable from such coating materials should exhibit high chemical resistance. In this respect, it should be highly stable to many different solvents as well as bases and acids. In particular, it should have very good resistance to methyl isobutyl ketone (MIBK). Moreover, the coating material should exhibit good processing properties, especially by low or low film forming temperatures without compromising the mechanical properties or chemical resistance of the coatings obtainable from such coating materials. Another object is that the coating material described can be obtained at a very low cost && These and other objects, which are not expressly stated but may be discussed from the introduction of the present specification, are readily obtained by an aqueous dispersion having all of the features of the i-fith of the patent application. The useful repair of the dispersion & The invention therefore proposes an aqueous coating material comprising at least one (meth)acrylic poly&% dispersion and at least one coalescent, the material of the stomach @&201226480 comprising the (meth)acrylic polymer a unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group, and the coalescent having at least one ethylenically unsaturated double bond and having a molecular weight of less than 1000 g/mol The coating material of the present invention has outstanding properties. In particular, the coating material of the present invention is very environmentally friendly, has a very low residual monomer content, and only releases a small portion of the organic compound to the environment during processing." It can be coated from the present invention based on a polymer or composition. The hardness of the coating obtained from the coating material can vary over a wide range. It is particularly surprising that it is possible to obtain a mechanically stable coating which is noticed with high elongation at break and/or high tensile strength. Furthermore, the coatings obtainable from the coating materials of the present invention exhibit a lower brittleness with respect to hardness and chemical resistance. According to a preferred modification, it is possible in accordance with the invention to obtain in particular a particularly hard scratch-resistant coating. The coatings obtainable from the dispersions of the invention exhibit surprisingly high solvent resistance, which is especially exhibited in tests using methyl isobutyl ketone (MIBK), ammonia solution or ethanol. Therefore, the coating obtained exhibits an excellent classification in tests which are in particular tested according to DIN 68 8 6 1 -1. The coating materials of the present invention exhibit, inter alia, good processing properties which are particularly evident from the low minimum film forming temperatures and which do not compromise the mechanical properties or chemical resistance of the coatings obtainable from the coating materials. The coatings obtainable from such coating materials or polymers have comparable chemical resistance and/or comparable pendulum hardness, so that the coating materials of the present invention exhibit a particularly low minimum film formation -8 - 201226480 temperature. These dispersions have comparable minimum film forming temperatures, and coatings obtainable from such dispersions exhibit improved chemical resistance and increased pendulum hardness. Further, the dispersion of the present invention exhibits high storage stability, high maintainability, and very good shelf life. More specifically, aggregates are not substantially formed. With regard to performance, these dispersions exhibit improved environmental compatibility. A preferred embodiment shows that substantially no organic compound (more specifically, a solvent) is released into the atmosphere. Moreover, the coating materials have an extremely low residual monomer content. The coatings obtainable from the coating materials of the present invention exhibit high weathering stability, more specifically high UV resistance. Further, the film obtainable from the dispersions has a low adhesiveness after a short time. The coating material of the present invention can be produced on a large scale in a low cost manner. The coating material of the present invention is environmentally friendly and can be reliably prepared and processed without high cost and complexity. At the same time, the coating material of the present invention exhibits a very high shear stability. The coating material of the present invention is an aqueous dispersion. Therefore, it contains an aqueous phase in which polymer particles are dispersed. The term "dispersion" is well known in the art. The aqueous coating material comprises at least one coalescent. The term "agglomerating agent" is used in the art to mean an additive which lowers the minimum film forming temperature of the polymer present in the dispersion. The coalescent used in this example has a molecular weight of not more than 1000 g/mol, preferably not more than 800 g/mol. The molecular weight of the coalescent is preferably in the range of from 120 to 600 g/mol, more preferably in the range of from 140 to 201226480 500 g/mol. According to a particular embodiment of the invention, the coalescent comprises no more than 3 Å, preferably no more than 20, especially no more than 15, most preferably no more than 8 carbon atoms. Thus, particularly important is a coalescent having a boiling point of at least 140 ° C, preferably at least 18 (TC, more preferably at least 190 ° C) at atmospheric pressure (1013 mbar). According to a preferred embodiment, at atmospheric pressure The boiling point of the coalescent may range from 140 to 350 ° C, more preferably from 180 to 300 ° C. According to the invention, the coalescent has at least one, preferably at least two ethylene It is an unsaturated double bond. In this respect, the ratio of the carbon atom to the ethylenically unsaturated double bond of the preferred coalescent is in the range of 3:1 to 8:1, more preferably 4:1 to 6:1. Preferably, the coalescent agent has an HLB 在 in the range of 3 to 19, more preferably in the range of 9 to 16, which is by 0^[^11(3)〇1^^11,\^.(: .,>1. Soc. Cosmetic Chem., 1, 3 1 1 (1 949), b) Method calculation of ICI Bulletin, HLB System, 8, (1 984). According to a specific embodiment of the present invention, The coalescent used in the present invention is an alcohol, an amine, an ether or an ester, more preferably an alcohol ester. The coalescent preferably comprises at least two ethylenically unsaturated double bonds. Therefore, preferred compounds have a dienyl group. And/or from multiple officials A compound derivative, an example of which is an alcohol and/or an acid having two or more functional groups, more specifically a carboxylic acid. According to a particular embodiment of the invention, preferably more specifically having at least An octadiene-based coalescent. The coalescent preferably constitutes an alcohol, an amine, an ether or an ester. Therefore, the compounds comprise at least one of the groups having the formula -R of the group of 2012-0680, wherein R represents exactly 8 carbon atoms and having two carbon-carbon groups. Preferably, the group having exactly 8 carbon atoms and 2 double bonds includes octane-2,7-dienyl and oct-3,7-dienyl. , octyl-4,7-dienoctyl 5,7-dienyl, octane-2,4-dienyl, octane-2,5-dienyl, octadienyl, octane-3,5- Preferred alkenyl, octane-3,6-dienyl and octane-4,6-dioxan alcohols more specifically include octane-2,7-dienol, oct-3,7·di, oct-4 , 7-dienol, oct-5,7-dienol, octane-2,4-dienol 2,5-dienol, octa-2,6-dienol, oct-3,5- Dienol, oct-3,6-ol and oct-4,6-dienol. Further, esters having one or more octadienyl groups are preferably used in the preparation of the ester. The acid may be a linear, branched, saturated or unsaturated carboxylic acid. In addition to the aliphatic acid, an aromatic acid may also be used. In this case, the above-mentioned octadienol derived from a monocarboxylic acid is further included. Preferably, the acid has from 1 to 20, preferably from 1 to 10, more preferably from 1 to 4 carbons. More preferably, the monocarboxylic acids include formic acid, acetic acid, propionic acid, acrylic acid and methyl groups. acrylic acid. Preferably, the coalescents have exactly octadienyl groups. The preferred ester of a preferred monocarboxylic acid having from 1 to 20 carbon atoms preferably has a molecular weight of from 150 to 500 g/mol, more preferably up to 300 g/mol. In addition, esters having two, three or more carboxylic acid acids such as esters of oxalic acid, esters of citric acid, esters of terephthalic acid of terephthalic acid, maleic acid may also be used. Ester or adipic acid ester. More than a double bond specific group ''2,6- alkenyl enol octyl-diene polycyclic one specific carboxylate butyric acid one derived 150 carboxylic acid ester, preferably -11 - 201226480 polycarboxylic acid has 2 to 20, compared Preferably it is from 2 to 10, more preferably from 2 to 6 carbon atoms. Of particular importance in this regard are esters of polycarboxylic acids having one, two or more octadienyl groups. The preferred ester derived from a polycarboxylic acid preferably having 1 to 20 carbon atoms preferably has a molecular weight of 200 to 1000 g/m〇, more preferably 300 to 600 g/mol. The ether more specifically includes a compound derived from an ether group preferably having a monool having 1 to 10 carbon atoms. The monoalcohols may be in the form of a linear, cyclic or branched chain. In addition, such ethers can be prepared using unsaturated, saturated or aromatic alcohols. More specifically, it is methyl ether, ethyl ether, propyl ether, butyl ether, pentyl ether and hexyl ether of the above octadienol. Examples of such ethers are, in particular, methoxyoctane-2,7-diene (methyloctane-2,7-dienyl ether), ethoxyoctane-2,7-diene and propoxyoctane- 2,7 diene. The preferred ether derived from a monool having preferably 1 to 1 carbon atoms preferably has a molecular weight of from 140 to 300 g/mol, more preferably from 140 to 25 0 g/mol. The particularly preferred ether is a compound derived from an oligoalkylene or a polyalkylene and comprising an alkylene oxide unit in addition to at least one octadienyl group, particularly preferably having from 2 to 40, more preferably Preferably, it is an ether of from 3 to 10 ethylene oxide units and/or propylene oxide units. Such compounds include, for example, diethylene glycol octane-2,7-dienyl ether, triethylene glycol octane-2,7-dienyl ether, tetraethylene glycol octane-2,7-dienyl ether, Pentaethylene glycol octane-2,7-dienyl ether, hexaethylene glycol octane-2,7-dienyl ether, dipropylene glycol octane-2,7-dienyl ether, tripropylene glycol bis-2,7 -dienyl ether, tetrapropylene glycol octane-2,7-dienyl ether, pentapropylene glycol octane-2,7-dienyl ether and hexapropylene glycol octane-2,7-dienyl ether. According to other embodiments of the invention, ethers of alcohols having two, three or more hydroxyl groups of -12-201226480 can be used. The polyols preferably have atoms, and the alcohols may be linear, branched, cyclic, saturated aromatic alcohols. It particularly includes ethers of a mixture of alcohols such as ethylene glycol, propylene glycol, glycerin, neopentyl alcohol, dipentaerythritol, mannitol, and sorbitol. The ether having the above octanol in this case may have one, two, three or more octane compounds, more specifically including monooctyl-4,6-dieneoxyethylene 4,6-diene oxyethane , monooctyl-4,6-diallylpropanediol, oxypropanol, trioctane-2,7-diallylpropane, monooctyl-2,7-1,2-dioctane-2,7-diene oxygen Ethane, monooctyl-2,7-dienyl-2,7-dienyloxypropanol and trioctyl-2,7-dienyloxypropane. Use or as a mixture of two or more. The preferred ether derived from a polyol having more carbon atoms has a molecular weight of 8 00 g/mol > more preferably 170 to 600 g/mol. In addition to the ethers and alcohols, amines can also be used. In the case of using a compound having one, two or more amine groups, it contains 8 to 20 carbon atoms. Preferred amines more specifically include amine amine, oct-3,7-dienylamine, oct-4,7-dienylamine, octa-2,4-dienylamine, oct-2,5 -dienylamine, oct-3,5-dienylamine, oct-3,6-dienylamine, (methyl(octyl-2,7-dienyl)amino)ethanol (2 alkenyl)amino)ethanol, 2-octyl-2,7-octane-2,7-dienylethylene 2,7-dienyl)amino)ethylamine. The preferred amine has a molecular weight of Μ 800 g/mol, more preferably from 170 to 600 g/mol. 2 to 10 carbons: and, unsaturated or hydrazine, trimethylolpropane: alcohol, sucrose or a diene of the dienyl alcohol. The preferred alcohol '1,2-dioctyl-dioctane-4,6-diene oxy oxyethylene, oxypropylene glycol, and the like may each independently have 2 to 10, preferably 170, to the case, can. Preferred amines include octane-2,7-diene, oct-5,7-diene, octane-2,6-diene, octane-4,6-diene L-based (oct-2,7-diol) And (methyl (Xin - preferably from 1 40 to -13 to 201226480) Among the compound classes, particularly preferred are alcohols and ethers having two or more alkylene oxide units, particularly preferably an alcohol. The above alcohols, amines, ethers or esters can be obtained by various methods, including conventional methods of short chain polymerization of 1,3 -butadiene. The term "short chain polymerization" as used herein means the presence of a nucleophile. Reactions of compounds having a conjugated double bond. The methods set forth in the publications WO 2004/002931, WO 03/031379 and WO 02/00 803, in particular the catalysts and reaction conditions for the reaction, such as pressure And the temperature is incorporated into the present specification for the purpose of disclosure. The short-chain polymerization of 1,3 -butadiene is preferably carried out using a metal compound containing a metal of Groups 8 to 10 of the periodic table as a catalyst. It is especially preferred to use a palladium compound, more preferably a palladium-carbene complex, as described in more detail in the disclosure set forth above. As for the nucleophile, especially Water, ammonia, monoalcohols, polyhydric alcohols, especially diols such as ethylene glycol, 1,2-propanediol and 1,3-propanediol; diamines such as ethylenediamine, N-methylethylenediamine, N,N'-dimethylethylenediamine or hexamethylenediamine; an amino alcohol such as amine ethanol, N-methylamine ethanol, N-ethylamine ethanol, amine propanol 'N-methylamine propanol or N - Ethylamine propanol, or a carboxylic acid, more specifically a monocarboxylic acid and a polycarboxylic acid as described in detail above, in WO 2004/00293 1, WO 03/03 1 3 79 and WO 02/1 00803 The nucleophile is described in the specification for the purpose of disclosure. The temperature of the short-chain polymerization is between 10 and 180 ° C, preferably between 30 and 120 ° C, preferably The system is between 40 and 100 ° C. The reaction pressure is from 1 to 300 bar, preferably from 1 to 120 bar, more preferably from 1 to -14 to 201226480 64 bar, most preferably from 1 to 20 bar. An isomer of a 7-dienyl compound can be prepared by isomerizing a double bond in a compound having an octa-2,7-dienyl group. If octadienyl is present in the esterification reaction Reaction of an ether-based alcohol with a monocarboxylic acid or a polyresidic acid and/or with a polycarboxylic acid The reaction obtains a coalescent which is especially suitable for use according to the invention. Particularly suitable for use in such reactants is at least based on a trihydric alcohol or an alcohol mixture based on an average functionality of at least three at the starting point and having an average of each molecule a short-chain polymer of at least one free hydroxyl group, particularly suitable for use in an esterification reaction, a short-chain polymerization product of glycerol and butadiene having a hydroxyl group content of 5.5 to 17% by weight and/or a hydroxyl group content of 4.9 to 14.0% by weight A short chain polymerization product of methylolpropane and butadiene. Further, a preferred coalescent having a octadienyl group is described in the publication EP-A-0 5 46 4 1 7 wherein the reactive diluent and its preparation method are incorporated herein by reference. in. According to another preferred embodiment of the present invention, especially esters of carboxylic acids having two, three or more carboxylic acid groups can also be used as coalescents, such as esters of oxalic acid, esters of malonic acid, An ester of citric acid, an ester of terephthalic acid, an ester of fumaric acid, an ester of maleic acid or an ester of adipic acid, which have at least one, preferably at least two, ethylenically unsaturated. Double key. Preferably, the polycarboxylic acid has from 2 to 20, preferably from 2 to 10, more preferably from 2 to 6 carbon atoms. Particularly preferred in this respect are ethylenically unsaturated alcohols having 2 to 6, preferably 2 to 4 carbon atoms. More specifically, it includes allyl alcohol and vinyl alcohol. Therefore, preferred are especially diallyl malonate, divinyl malonate and triallyl citrate, with diallyl malonate being preferred. -15- 201226480 In addition to the coalescing agent described above, the coating material of the present invention comprises at least one aqueous dispersion having at least one (meth)acrylic polymer having A unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group. The term "polymer" means a dispersion of a compound which can be obtained by reacting a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in an alkyl group with each other or with another monomer. The reaction can take place in one step or in several stages. The dispersion may comprise one or more polymers having repeating units derived from (meth)acrylic monomers having at least one double bond and from 8 to 40 carbon atoms in the alkyl group. The ratio of chain length, solubility behavior or other properties of the polymer such as an alkyl group having at least one double bond to a (meth)acrylic monomer having 8 to 40 carbon atoms may be different. The polymer is preferably obtainable by free radical polymerization. Therefore, the term "repeating unit" is derived from the monomer used to prepare the polymer. a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group is an ester of a (meth)acrylic acid having at least one carbon-carbon double bond and 8 to 40 carbon atoms in the alkyl group or Guanamine. (Meth)acrylic acid representation means methacrylic acid and acrylic acid and mixtures thereof. The alkyl or alcohol or guanamine group preferably has from 10 to 30, more preferably from 12 to 20 carbon atoms, and the group may contain a hetero atom, more specifically, an oxygen, nitrogen or sulfur atom. The alkyl group may have one, two, three or more carbon-carbon double bonds. The polymerization conditions for preparing the (meth) acrylate polymer are preferably selected to maximize the proportion of double bonds of the alkyl group remaining in the polymerization of the -16-201226480. This can be accomplished, for example, by sterically hindering the presence of a double bond in the alcohol group. Further, at least a part or preferably all of the double bonds in the alkyl group present in the (meth)acrylic monomer are less reactive in the radical polymerization than the (meth)acrylic group, and thus in the alkyl group Preferably, no other (meth)acrylic groups are present. The iodonium used for preparing the (meth)acrylic polymer and having at least one double bond and a (meth)acrylic monomer having 8 to 40 carbon atoms in the alkyl group is preferably at least 50, more preferably at least 1 Preferably, it is at least 125 g iodine/100 g (meth)acrylic monomer. This type of (meth)acrylic monomer substantially conforms to formula (I)
Η 〇 其中基R爲氫或甲基,X獨立爲氧或式ΝΙΓ之基,其 中π爲氫或具有1至6個碳原子之基,而R1爲具有8至 40,較佳爲10至30,更佳爲12至20個碳原子且含有至 少一個C-C雙鍵之直鏈或支鏈基。 表示法「(甲基)丙烯酸」代表丙烯酸及甲基丙烯酸基 ,以甲基丙烯酸基爲佳。 烷基中具有至少一個雙鍵與8至40個碳原子之(甲基) 丙烯酸系單體可例如藉由以具有至少一個雙鍵及8至40 個碳原子之醇來酯化(甲基)丙烯酸、反應(甲基)丙烯醯鹵 及/或(甲基)丙烯酸酐或轉酯化(甲基)丙烯酸酯而獲得。因 -17- 201226480 此,(甲基)丙烯酸醯胺可藉由與胺反應而獲得。該等反應 可描述於例如 Ullmann's Encyclopedia of Industrial Chemistry ,第 5 版,CD-ROM ’ 或描述於 F.-B· Chen,G. Bufkin,MCrosslinkable Emulsion Polymers by Autooxidation I",Journal of Applied Polymer Science,Vol. 3 0, 457 1 -4582( 1 985 )。 適用於該目的之醇尤其包括辛烯醇、壬烯醇、癸烯醇 、十一烯醇、十二烯醇、十三烯醇、十四烯醇、十五烯醇 、十六烯醇、十七烯醇、十八烯醇、十九烯醇、二十烯醇 、二十二烯醇、辛二烯醇、壬二烯醇、癸二烯醇、十一烷 二烯醇、十二烷二烯醇、十三烷二烯醇、十四烷二烯醇、 十五烷二烯醇、十六烷二烯醇、十七烷二烯醇、十八烷二 烯醇、十九烷二烯醇、二十烷二烯醇及/或二十二烷二烯 醇。該等所謂脂肪醇在某些情況中可從市面購得,或可從 脂肪酸獲得,該反應係描述於例如F.-B. Chen,G. Bufkin, Journal of Applied Polymer Science, Vol. 30, 457 1 - 4582(1985) ° 可由該方法獲得之較佳(甲基)丙烯酸酯尤其包括(甲基 )丙烯酸辛二烯酯、(甲基)丙烯酸十八烷二烯酯、(甲基)丙 烯酸十八烷三烯酯、(甲基)丙烯酸十六烯酯、(甲基)丙烯 酸十八烯酯及(甲基)丙烯酸十六烷二烯酯。 此外,烷基中具有至少一個雙鍵與8至40個碳原子 之(甲基)丙烯酸酯亦可藉由反應不飽和脂肪酸與烷基中具 有反應性基(更明確地說爲醇基)之(甲基)丙烯酸酯而獲得 。該反應性基尤其包括羥基以及環氧基。因此’亦可能使 -18- 201226480 用例如(甲基)丙烯酸羥基烷酯,諸如(甲基)丙烯酸3-羥丙 酯、(甲基)丙烯酸3,4-二羥丁酯、(甲基)丙烯酸2-羥乙酯 、(甲基)丙烯酸2·羥丙酯、(甲基)丙烯酸2,5-二甲基-1,6-己二醇酯、(甲基)丙烯酸1,10-癸二醇酯;或含有環氧基之 (甲基)丙烯酸酯,諸如(甲基)丙烯酸環氧丙酯,以例如用 作製備上述(甲基)丙烯酸酯的反應物。 適於與上述(甲基)丙烯酸酯反應之脂肪酸在許多情況 中可從市面購得及係從天然來源獲得。該等脂肪酸尤其包 括十一烯酸、棕櫊油酸、油酸、反油酸、反Π -十八烯酸 、二十烯酸、鯨油酸、芥子酸、二十四烯酸、亞麻油酸、 次亞麻油酸、花生油酸、二十碳五烯酸、線油酸及/或二 十二碳六烯酸。 可以該方法獲得之較佳(甲基)丙烯酸酯尤其包括(甲基 )丙烯醯氧基-2-羥丙基-亞麻油酸酯、(甲基)丙烯醯氧基-2-羥丙基-次亞麻油酸酯及(甲基)丙烯醯氧基-2-羥丙基-油酸 酯。 不飽和脂肪酸與烷基中具有反應性基(更明確地說爲 醇基)之(甲基)丙烯酸酯的反應本身已爲人知,且係描述於 例如 DE-A-41 0 5 134、DE-A-2 5 13 516、DE-A-26 3 8 544 及 US 5,750,75 1。 根據一較佳具體實例,可能使用通式(Π)之(甲基)丙 烯酸系單體 -19- 201226480Η 〇 wherein R is hydrogen or methyl, and X is independently oxygen or a group of hydrazine, wherein π is hydrogen or a group having 1 to 6 carbon atoms, and R 1 is 8 to 40, preferably 10 to 30. More preferably, it is a linear or branched group of 12 to 20 carbon atoms and containing at least one CC double bond. The expression "(meth)acrylic acid" represents acrylic acid and methacrylic acid groups, preferably methacrylic acid groups. A (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group can be esterified (methyl), for example, by an alcohol having at least one double bond and 8 to 40 carbon atoms. It is obtained by using acrylic acid, reacting (meth)acrylonitrile halide and/or (meth)acrylic anhydride or transesterifying (meth)acrylate. Since -17-201226480, decyl (meth)acrylate can be obtained by reacting with an amine. Such reactions can be described, for example, in Ullmann's Encyclopedia of Industrial Chemistry, 5th edition, CD-ROM' or as described in F.-B. Chen, G. Bufkin, MCrosslinkable Emulsion Polymers by Autooxidation I", Journal of Applied Polymer Science, Vol. 3 0, 457 1 -4582 ( 1 985 ). Alcohols suitable for this purpose include, in particular, octenol, terpene alcohol, terpene alcohol, undecenol, dodecenol, tridecenol, tetradecenol, pentadecenol, cetyl alcohol, Heptaenyl alcohol, stearyl alcohol, nonadecanol, eicosyl alcohol, dodecadienol, octadienol, decadienol, decadienol, undecadienol, twelve Alkadienol, tridecadienol, tetradecadienol, pentadecadienol, hexadecanol, heptadecadienol, octadecadienol, pentadecane Dienol, eicosadienol and/or behenyldienol. These so-called fatty alcohols are commercially available in some cases or may be obtained from fatty acids, which are described, for example, in F.-B. Chen, G. Bufkin, Journal of Applied Polymer Science, Vol. 30, 457. 1 - 4582 (1985) ° Preferred (meth) acrylates obtainable by this method include, in particular, octadienyl (meth) acrylate, stearyl decyl (meth) acrylate, and (meth) acrylate Octatriene triester, cetyl (meth)acrylate, octadecyl (meth)acrylate and cetyl allyl (meth)acrylate. Further, the (meth) acrylate having at least one double bond and 8 to 40 carbon atoms in the alkyl group may also have a reactive group (more specifically, an alcohol group) by reacting the unsaturated fatty acid with the alkyl group. Obtained by (meth) acrylate. The reactive group includes, in particular, a hydroxyl group and an epoxy group. Therefore, it is also possible to use -18-201226480 with, for example, hydroxyalkyl (meth)acrylate, such as 3-hydroxypropyl (meth)acrylate, 3,4-dihydroxybutyl (meth)acrylate, (methyl) 2-Hydroxyethyl acrylate, 2-hydroxypropyl (meth)acrylate, 2,5-dimethyl-1,6-hexanediol (meth)acrylate, 1,10-fluorene (meth)acrylate a glycol ester; or an epoxy group-containing (meth) acrylate such as glycidyl (meth) acrylate, for example, used as a reactant for preparing the above (meth) acrylate. Fatty acids suitable for reaction with the above (meth) acrylates are commercially available in many cases and are obtained from natural sources. Such fatty acids include, in particular, undecylenic acid, palmitic acid, oleic acid, elaidic acid, ruthenium octadecenoic acid, eicosenoic acid, whale oleic acid, sinapic acid, tetracosic acid, linoleic acid , linoleic acid, arachidonic acid, eicosapentaenoic acid, linoleic acid and/or docosahexaenoic acid. Preferred (meth) acrylates obtainable by this process include, inter alia, (meth) propylene oxy-2-hydroxypropyl-linolenic acid ester, (meth) propylene oxime-2-hydroxypropyl- Sublinoleic acid ester and (meth)acryloxy-2-hydroxypropyl-oleate. The reaction of an unsaturated fatty acid with a (meth) acrylate having a reactive group (more specifically, an alcohol group) in an alkyl group is known per se and is described, for example, in DE-A-41 0 5 134, DE- A-2 5 13 516, DE-A-26 3 8 544 and US 5,750,75 1. According to a preferred embodiment, it is possible to use a (meth)acrylic monomer of the formula (Π) -19- 201226480
其中R爲氫或甲基,X1及X2獨立爲氧或式NR'之基,其 中R'爲氫或具有1至6個碳原子之基,其條件爲X1及X2 基中至少一者爲式NR’之基,其中R'爲氫或具有1至6個 碳原子之基,Z爲鍵聯基,而R2爲具有9至25個碳原子 之不飽和基。 此外’經由使用通式(III)之(甲基)丙烯酸系單體可獲 致令人意外的優點Wherein R is hydrogen or methyl, and X1 and X2 are independently oxygen or a group of the formula NR', wherein R' is hydrogen or a group having 1 to 6 carbon atoms, provided that at least one of the X1 and X2 groups is a formula The group of NR' wherein R' is hydrogen or a group having 1 to 6 carbon atoms, Z is a bonding group, and R2 is an unsaturated group having 9 to 25 carbon atoms. Furthermore, surprising advantages can be obtained by using the (meth)acrylic monomer of the formula (III).
r2 (III), 其中R爲氫或甲基,X1爲氧或式NR'之基,其中R’爲氫 或具有1至6個碳原子之基,Z爲鍵聯基,R’爲氫或具有 1至6個碳原子之基,而R2爲具有9至25個碳原子之不 飽和基。 「具有1至6個碳原子之基」一詞代表具有1至6個 碳原子之基。其包括芳族及雜芳族基,以及烷基、環烷基 、烷氧基、環烷氧基、烯基、醯基及烷氧基羰基,以及雜 脂族基。所述之基可爲支鏈或非支鏈。此外,該等基可具 有取代基,更明確地說,爲鹵素原子或羥基。 基V較佳爲烷基。較佳之烷基包括甲基、乙基、丙基 -20- 201226480 、異丙基、1-丁基、2-丁基、2-甲基丙基或三級丁基。 基Z較佳爲包含1至10,較佳爲1至5,最佳2至3 個碳原子之鍵聯基。此等基尤其包括直鏈或支鏈脂族或環 脂族基,諸如例如亞甲基、伸乙基、伸丙基、伸異丙基、 伸正丁基、伸異丁基、伸三級丁基或伸環己基,以伸乙基 尤佳。 式(III)中之基R2爲具有9至25個碳原子之不飽和基 。該等基更具體地包含烯基、環烯基、烯氧基、環烯氧基 、烯醯基以及雜脂族基》此外,該等基可具有取代基,更 明確地說,爲鹵素原子或羥基。較佳基尤其包括烯基,諸 如壬烯基、癸烯基、十一烯基、十二烯基、十三烯基、十 四烯基、十五烯基、十六烯基、十七烯基、十八烯基、十 九烯基、二十烯基、二十一烯基、二十二烯基、辛二烯基 、壬二烯基、癸二烯基、十一烷二烯基、十二烷二烯基、 十三烷二烯基、十四烷二烯基、十五烷二烯基、十六烷二 烯基、十七烷二烯基、十八烷二烯基、十九烷二烯基、二 十烷二烯基、二十一烷二烯基、二十二烷二烯基、二十三 院二儲基及/或十七院三嫌基。 較佳之式(II)或(111)(甲基)丙烯酸系單體尤其包括十七 烯醯氧基-2-乙基-(甲基)丙烯醯胺、十七烷二烯醯氧基-2-乙基-(甲基)丙烯醯胺、十七烷三烯醯氧基-2-乙基-(甲基) 丙烯醯胺、十七烯醯氧基-2-乙基-(甲基)丙烯醯胺、(甲基) 丙烯醯氧基-2-乙基-棕櫚油醯胺、(甲基)丙烯醯氧基-2-乙 基-油醯胺、(甲基)丙烯醯氧基-2-乙基-二十烯醯胺、(甲基 -21 - 201226480 )丙烯醯氧基-2-乙基-鯨油醯胺、(甲基)丙烯醯氧基-2-乙 基-芥子烯醯胺、(甲基)丙烯醯氧基-2-乙基-亞麻油醯胺、( 甲基)丙烯醯氧基-2-乙基-次亞麻油醯胺、(甲基)丙烯醯氧 基-2-丙基-棕櫚油醯胺、(甲基)丙烯醯氧基-2-丙基-油醯胺 、(甲基)丙烯醯氧基-2-丙基-二十烯醯胺、(甲基)丙烯醯氧 基-2-丙基-鯨油醯胺、(甲基)丙烯醯氧基-2-丙基-芥子烯醯 胺、(甲基)丙烯醯氧基-2-丙基-亞麻油醯胺及(甲基)丙烯醯 氧基-2 -丙基-次亞麻油醯胺。 「(甲基)丙烯酸」表示法代表丙烯酸及甲基丙烯酸基 ,以甲基丙烯酸基爲佳。特佳之式(Π)或(III)單體爲甲基 丙烯醯氧基-2-乙基-油醯胺、甲基丙烯醯氧基-2-乙基-亞 麻油醯胺及/或甲基丙烯醯氧基-2-乙基-次亞麻油醯胺。 式(II)或(III)之(甲基)丙烯酸系單體特別可藉由多階段 方法獲得。在第一階段中,例如一或多種不飽和脂肪酸或 脂肪酸酯可與例如胺(諸如乙二胺、乙醇胺、丙二胺或丙 醇胺)反應以產生醯胺。在第二階段中,醯胺之羥基或胺 基係與例如(甲基)丙烯酸酯、(甲基)丙烯酸甲酯反應以產 生式(II)或(III)之單體。爲製備其中X1爲式NR’之基(其中 R’爲氫或具有1至6個碳原子之基且X2爲氧)之單體,因 此可能先反應(甲基)丙烯酸烷酯(例如(甲基)丙烯酸甲酯) 與上述胺其中之一,以產生烷基中具有羥基之(甲基)丙烯 醯胺,然後其與不飽和脂肪酸反應以產生式(Π)或(III)之( 甲基)丙烯酸系單體。醇與(甲基)丙烯酸酯之轉酯化,或( 甲基)丙烯醯胺之製備係描述於下列文件中:CN 1 3 5 5 1 6 1 -22- 201226480 、DE 2 1 29 425、DE 34 23 4 4 3 或 EP - A 0 5 3 4 6 6 6 ’ 該等 公開案中所述之反應條件以及其中所列之觸媒等係基於揭 示目的倂入本說明書中。此外’該等反應係描述於 "Synthesis of Acrylic Esters by Transesterification", J. Haken, 1967。 該等反應中,所獲得之羥基在烷基中的中間物(例如 羧醯胺)可經純化。在本發明一特定具體實例中,所獲得 之中間物可在無高昂成本及不便之純化作用之下經反應, 以產生式(II)或(III)之(甲基)丙烯酸系單體。 烷基中具有8至40,較佳爲10至30,更佳爲12至 20個碳原子及至少一個雙鍵之(甲基)丙烯酸系單體另外尤 其包括通式(IV)之單體R2 (III), wherein R is hydrogen or methyl, and X1 is oxygen or a group of the formula NR', wherein R' is hydrogen or a group having 1 to 6 carbon atoms, Z is a bonding group, and R' is hydrogen or A group having 1 to 6 carbon atoms, and R2 is an unsaturated group having 9 to 25 carbon atoms. The term "base having 1 to 6 carbon atoms" means a group having 1 to 6 carbon atoms. It includes aromatic and heteroaromatic groups, as well as alkyl, cycloalkyl, alkoxy, cycloalkoxy, alkenyl, decyl and alkoxycarbonyl groups, as well as heteroaliphatic groups. The group may be branched or unbranched. Further, the groups may have a substituent, more specifically, a halogen atom or a hydroxyl group. The group V is preferably an alkyl group. Preferred alkyl groups include methyl, ethyl, propyl-20-201226480, isopropyl, 1-butyl, 2-butyl, 2-methylpropyl or tert-butyl. The group Z is preferably a linking group containing from 1 to 10, preferably from 1 to 5, most preferably from 2 to 3 carbon atoms. These groups include, in particular, straight-chain or branched aliphatic or cycloaliphatic groups such as, for example, methylene, ethyl, propyl, isopropyl, n-butyl, isobutyl, and tert-butyl The base or the cyclohexyl group is especially suitable for stretching the ethyl group. The group R2 in the formula (III) is an unsaturated group having 9 to 25 carbon atoms. The groups more specifically include an alkenyl group, a cycloalkenyl group, an alkenyloxy group, a cycloalkenyloxy group, an olefin group and a heteroaliphatic group. Further, the groups may have a substituent, more specifically, a halogen atom. Or hydroxyl. Preferred groups include, in particular, alkenyl groups such as decenyl, decenyl, undecenyl, dodecenyl, tridecenyl, tetradecenyl, pentadecenyl, hexadecenyl, heptadecene , octadecyl, decadecenyl, behenyl, behenyl, icosadienyl, octadienyl, decadienyl, decadienyl, undecadienyl , dodecadienyl, tridecadienyl, tetradecadienyl, pentadecadienyl, hexadecendienyl, heptadecadienyl, octadecadienyl, A nonadecadienyl group, an eicosadienyl group, a hexadecandienyl group, a behenyldienyl group, a twenty-three yards, and/or a seventeen-story tris. Preferred (II) or (111) (meth)acrylic monomers include, in particular, heptadecyloxy-2-ethyl-(meth)acrylamide, heptadecadienyloxy-2 -ethyl-(meth)acrylamide, heptadetrienyloxy-2-ethyl-(methyl) acrylamide, heptadecyloxy-2-ethyl-(methyl) Acrylamide, (meth) propylene oxime-2-ethyl-palmitole amide, (meth) propylene oxime-2-ethyl-oleylamine, (meth) propylene oxime - 2-ethyl-icosyl decylamine, (methyl-21 - 201226480) propylene oxime-2-ethyl-whale decylamine, (meth) propylene oxime-2-ethyl- mustard oxime Amine, (meth) propylene oxime-2-ethyl-linolenic acid amide, (meth) propylene oxime-2-ethyl-linolenic acid decylamine, (meth) propylene oxime - 2-propyl-palmitole amide, (meth) propylene oxime-2-propyl-oleylamine, (meth) propylene oxime-2-propyl-icocosyl decylamine, (A) Base) propylene oxime-2-propyl-whale decylamine, (meth) propylene oxime-2-propyl-sinapinamide, (meth) propylene oxime-2-propyl Amides sesame oil and (meth) Bingxi Xi-2 - propyl - Amides views linseed oil. The "(meth)acrylic acid" represents acrylic acid and methacrylic acid groups, preferably methacrylic acid groups. The preferred formula (Π) or (III) monomer is methacryloxy-2-ethyl-oleylamine, methacryloxy-2-ethyl-linolenic acid and/or methyl Propylene oxime-2-ethyl-linoleic oil decylamine. The (meth)acrylic monomer of the formula (II) or (III) can be obtained in particular by a multistage process. In the first stage, for example, one or more unsaturated fatty acids or fatty acid esters can be reacted with, for example, an amine such as ethylenediamine, ethanolamine, propylenediamine or propylamine to produce the guanamine. In the second stage, the hydroxyl or amine group of the indoleamine is reacted with, for example, (meth) acrylate or methyl (meth) acrylate to produce a monomer of the formula (II) or (III). To prepare a monomer wherein X1 is a group of the formula NR' (wherein R' is hydrogen or a group having 1 to 6 carbon atoms and X2 is oxygen), it is possible to react an alkyl (meth)acrylate first (for example (A) Methyl acrylate) and one of the above amines to produce a (meth) acrylamide having a hydroxyl group in the alkyl group, which is then reacted with an unsaturated fatty acid to produce a formula (Π) or (III) (methyl ) acrylic monomer. The transesterification of an alcohol with a (meth) acrylate or the preparation of a (meth) acrylamide is described in the following documents: CN 1 3 5 5 1 6 1 -22- 201226480, DE 2 1 29 425, DE 34 23 4 4 3 or EP - A 0 5 3 4 6 6 6 ' The reaction conditions described in the publications and the catalysts listed therein are incorporated herein by reference. Further, these reactions are described in "Synthesis of Acrylic Esters by Transesterification", J. Haken, 1967. In such reactions, the intermediate of the obtained hydroxyl group in the alkyl group (e.g., carboxamide) can be purified. In a particular embodiment of the invention, the intermediate obtained can be reacted without cost and inconvenience to produce a (meth)acrylic monomer of formula (II) or (III). The (meth)acrylic monomer having 8 to 40, preferably 10 to 30, more preferably 12 to 20 carbon atoms and at least one double bond in the alkyl group, particularly including the monomer of the formula (IV)
其中R爲氫或甲基’ X爲氧或式NR,之基,其中R,爲氫或 具有1至6個碳原子之基,R3爲具有1至22個碳原子之 伸烷基’Y爲氧、硫或式NR"之基,其中R"爲氫或具有! 至6個碳原子之基,而R4爲具有至少8個碳原子及至少 兩個雙鍵之不飽和基。 式(IV)中’基R3爲1至η個碳原子,較佳係具有i 至10,更佳係具有2至6個碳原子之伸烷基。在本發明— 特定具體實例中,基R3爲具有2至4,更佳爲2個碳原子 -23- 201226480 之伸烷基。具有1至22個碳原子之伸烷基尤其包括亞甲 基、伸乙基、伸两基、伸異丙基、伸正丁基、伸異丁基、 伸三級丁基或伸環己基,以伸乙基尤佳。 基R4包含至少兩個C-C雙鍵,其並非芳族系統的一 部分。較佳係該基R4爲具有正好8個碳原子且具有正好 兩個雙鍵之基。基R4較佳爲不含雜原子之直鏈烴基。根 據本發明一特定具體實例,式(IV)中之基R4可包含末端雙 鍵。在本發明另一修改中,式(IV)中之基R4可不含末端雙 鍵。存在基R4中之雙鍵較佳可爲共軛。根據本發明其他 較佳具體實例’存在基R4中之雙鍵不爲共軛。較佳之具 有至少兩個雙鍵的基R4尤其包括辛-2,7-二烯基、辛-3,7-二烯基、辛·4,7·二烯基 '辛-5,7-二烯基、辛-2,4-二烯基 、辛-2,5·二烯基、辛-2,6-二烯基、辛-3,5-二烯基、辛-3,6-二烯基及辛-4,6-二烯基。 通式(IV)之(甲基)丙烯酸系單體尤其包括例如2_甲基 丙-2-烯酸2-[((2-£)辛-2,7-二烯基)甲胺基]乙酯、2-甲基 丙-2-烯酸2-[((2-Z)辛-2,7-二烯基)甲胺基]乙酯、2_甲基 丙-2-烯酸2-[((3-E)辛_3,7-二烯基)甲胺基]乙酯、2_甲基 丙-2-烯酸2-[((4-2)辛.4,7-二烯基)甲胺基]乙酯、2_甲基 丙-2·烯酸2-[(辛-2,4 -二烯基)甲胺基]乙酯、2_甲基丙_2_烯 酸2-[(辛-2,4-二烯基)甲胺基]乙酯、2•甲基丙_2_嫌酸2_[( 辛-3,5-二烯基)甲胺基]乙酯、2_[((2_引辛_2,7二烯基)甲胺 基]乙基-(甲基)丙烯醯胺、2-[((2-Z)辛_2,7-二烯基)甲胺基 ]乙基-(甲基)丙烯醯胺、2-[((3·Ε)辛_3,7_二烯基)甲胺基] -24- 201226480 乙基-(甲基)丙儲酿胺' 2·[((4-Ζ)辛·4,7-二烯基)甲胺基]乙 基-(甲基)丙燃醯胺、2-[(辛-2,6 -二烯基)甲胺基]乙基-(甲 基)丙嫌醒胺、2-[(辛-2,4-二烯基)甲胺基]乙基_(甲基)丙烯 釀胺、2-[(辛-3,5-二烯基)甲胺基]乙基_(甲基)丙烯醯胺、 2-甲基丙-2-燦酸2-[((2-£)辛-2,7-二烯基)乙胺基]乙酯、2-甲基丙-2-烯酸2-[((2-Z)辛-2,7-二烯基)乙胺基]乙酯、2-甲 基丙-2-烯酸2-[((3-E)辛_3,7-二烯基)乙胺基]乙酯、2-甲基 丙-2-稀酸2-[((4-Z)辛·4,7-二烯基)乙胺基]乙酯、2_甲基 丙-2-稀酸2-[(辛-2,6 -二烯基)乙胺基]乙酯、2_甲基丙-2_烯 酸2-[(辛-2,4-二烯基)乙胺基]乙酯、2_甲基丙-2_烯酸2_[( 辛-3,5-—烯基)乙胺基]乙酯、丙-2_烯酸2-[((2-£)辛-2,7-—烯基)甲胺基]乙醋 '丙-2-嫌酸2-[((2-Ζ)辛-2,7-二嫌基) 甲胺基]乙酯、丙-2-烯酸2-[((3-Ε)辛-3,7-二烯基)甲胺基] 乙酯、丙-2-烯酸2-[((4-Ζ)辛_4,7_二烯基)甲胺基]乙酯、 丙-2-烯酸2-[(辛-2,6-二烯基)甲胺基]乙酯、丙_2_烯酸2_[( 辛-2,4 -二烯基)甲胺基]乙酯、丙·2·烯酸2-[(辛-3,5 -二稀基 )甲胺基]乙酯、2-甲基丙-2-烯酸2-((24)辛-2,7-二烧氧基) 乙酯、2-甲基丙-2-烯酸2-((2-Ζ)辛-2,7-二烯氧基)乙酯、 2-甲基丙-2-烯酸2-((3-Ε)辛-3,7-二烯氧基)乙酯、2·甲基 丙-2-烯酸2-((4-Ζ)辛-4,7-二烯氧基)乙酯、2·甲基丙·2-稀 酸2-(辛-2,6 -—燒氧基)乙醋、2 -甲基丙-2-烧酸2-(辛-2 4_ 二烯氧基)乙酯、2-甲基丙-2-烯酸2-(辛-3,5-二燒氧基)乙 酯、丙-2-烯酸2-((2-Ε)辛-2,7-二烯氧基)乙酯、丙_2_稀酸 2-((2-Ζ)辛 _2,7-二烯氧基)乙酯、丙 _2_ 烯酸 2_((3_£)辛_3,7- -25- 201226480 二烯氧基)乙酯、丙-2-烯酸2-((4-Z)辛-4,7-二烯氧基)乙酯 、丙-2-烯酸2-(辛-2,6-二烯氧基)乙酯、丙-2-烯酸2-(辛- 2,4-二烯氧基)乙酯及丙-2-烯酸2-(辛-3,5-二烯氧基)乙酯 〇 上述之式(IV)(甲基)丙烯酸系單體尤其可藉由令(甲基 )丙烯酸或(甲基)丙烯酸酯(更明確地說,(甲基)丙烯酸甲 酯或(甲基)丙烯酸乙酯)與醇及/或胺反應之方法而獲得。 該等反應已於前文說明。 待與(甲基)丙烯酸或(甲基)丙烯酸酯反應之反應物可 有利地符合式(V) H-X—R—Y-R4 (V), 其中X爲氧或式NR'之基,其中R’爲氫或具有1至6個碳 原子之基’ R3爲具有1至22個碳原子之伸烷基,Y爲氧 、硫或式NR"之基,其中R"爲氫或具有1至6個碳原子之 基,而R4爲具有至少8個碳原子之至少雙重不飽和基。 至於較佳R'、R"、R3、Y及R4基之定義係參考式 (IV)之說明。 較佳之式(V)反應物包括(甲基(辛-2,7-二烯基)胺基)乙 醇、(乙基(辛-2,7-二烯基)胺基)乙醇、2-辛-2,7·二烯氧基 乙醇、(甲基(辛-2,7-二烯基)胺基)乙胺、(甲基(辛·3,7-二 烯基)胺基)乙醇、(乙基(辛-3,7-二烯基)胺基)乙醇、2-辛-3,7-二烯氧基乙醇、(甲基(辛-3,7-二烯基)胺基)乙胺、(甲 -26- 201226480 基(辛-4,7-二烯基)胺基)乙醇、(乙基(辛-4,7-二烯基)胺基) 乙醇、2-辛-4,7-二烯氧基乙醇 '(甲基(辛_4,7-二烯基)胺基 )乙胺、(甲基(辛-5,7-二烯基)胺基)乙醇、(乙基(辛-5,7-二 烯基)胺基)乙醇、2-辛-5,7 -二烯氧基乙醇、(甲基(辛- 5,7-二烯基)胺基)乙胺、(甲基(辛-2,6-二烯基)胺基)乙醇、(乙 基(辛-2,6-二烯基)胺基)乙醇、2-辛‘-2,6-二烯氧基乙醇、( 甲基(辛-2,6-二烯基)胺基)乙胺、(甲基(辛-2,5-二烯基)胺 基)乙醇、(乙基(辛-2,5-二烯基)胺基)乙醇、2-辛-2,5-二烯 氧基乙醇、(甲基(辛-2,5-二烯基)胺基)乙胺、(甲基(辛- 2.4- 二烯基)胺基)乙醇、(乙基(辛-2,4-二烯基)胺基)乙醇、 2-辛-2,4-二烯氧基乙醇、(甲基(辛-2,4-二烯基)胺基)乙胺 、(甲基(辛-3,6-二烯基)胺基)乙醇、(乙基(辛-3,6-二烯基) 胺基)乙醇、2-辛-3,6-二烯氧基乙醇、(甲基(辛-3,6-二烯基 )胺基)乙胺、(甲基(辛-3,5-二烯基)胺基)乙醇、(乙基(辛- 3.5- 二烯基)胺基)乙醇' 2-辛-3,5-二烯氧基乙醇、(甲基( 辛-3,5-二烯基)胺基)乙胺、(甲基(辛-4,6-二烯基)胺基)乙 醇、(乙基(辛-4,6-二烯基)胺基)乙醇、2-辛-4,6-二烯氧乙 醇及(甲基(辛-4,6-二烯基)胺基)乙胺。式(V)之反應物可個 別使用或作爲混合物使用。 式(V)之反應物可藉由包括1,3-丁二烯之短鏈聚合之 已知方法等方法獲得。本文所使用之「短鏈聚合」一詞表 示在親核劑存在下具有共軛雙鍵之化合物的反應。於公開 案 WO 2004/00293 1、WO 03 /03 1 3 79 及 WO 02/ 1 00 8 03 中 所陳述之方法,尤其是用於該反應之觸媒及反應條件,諸 -27- 201226480 如壓力及溫度,係出於揭示目的倂入本說明書中。 1,3-丁二烯之短鏈聚合較佳可使用包含元素週期表第 8至1 〇族之金屬的金屬化合物作爲觸媒來進行,尤佳情況 可使用鈀化合物,更佳爲鈀-碳烯錯合物,此於前文陳述 之公開案中更詳細說明。 至於親核劑,尤其可使用二醇,諸如乙二醇、1,2 -丙 二醇及1,3 -丙二醇;二胺,諸如乙二胺、N -甲基乙二胺、 Ν,Ν’-二甲基乙二胺或六亞甲二胺;或胺基醇,諸如胺乙 醇、Ν-甲胺乙醇、Ν-乙胺乙醇、胺丙醇、Ν-甲基胺丙醇或 Ν-乙基胺丙醇。 在(甲基)丙烯酸爲所使用之親核劑情況下,可能例如 獲得(甲基)丙烯酸辛二烯酯,其特別適於用作具有8至40 個碳原子之(甲基)丙烯酸系單體。 可進行短鏈聚合反應之較佳壓力及溫度値係於前文說 明,因此亦參考前文之値。 具有辛-2,7-二烯基之化合物的異構物之製備可藉由將 存在具有辛-2,7-二烯基之化合物中的雙鍵異構化來進行。 根據本發明使用之(甲基)丙烯酸系聚合物較佳包含以 其重量計爲0.5重量%至60重量%,更佳爲1重量%至4〇 重量%,最佳爲1 · 5重量%至2 5重量%,尤佳爲2重量%至 20重量%之從烷基中具有至少一個雙鍵與8至40個碳原 子之(甲基)丙烯酸系單體衍生的單元。 該等(甲基)丙烯酸系聚合物較佳可藉由自由基聚合獲 得。因此,由於從起始劑或分子量調節劑(鏈轉移劑)所衍 -28- 201226480 生之基的重量分率通常可忽視,該等聚合物所含之個別單 元的重量分率係由用於製備該等聚合物之對應單體的重量 分率提供。 前文所述之烷基中具有至少一個雙鍵與8至40個碳 原子之(甲基)丙烯酸系單體可個別使用或作爲二或更多種 單體的混合物使用。 除了從上述烷基中具有至少一個雙鍵與8至40個碳 原子之(甲基)丙烯酸系單體中至少一者衍生之重複單元以 外,本發明之分散液中存在之較佳聚合物可能包含從其他 單體衍生之重複單元。 該等可共聚單體尤其包括具有酸基之單體、包含酯基 之單體A,及苯乙烯系單體。 含有酸基之單體爲較佳可與前文所述之光起始劑單體 自由基共聚的化合物。其包括例如具有磺酸基之單體,例 如乙烯磺酸;具有膦酸基之單體,例如乙烯膦酸;及不飽 和羧酸,例如甲基丙烯酸、丙烯酸、反丁烯二酸及順丁烯 二酸。以甲基丙烯酸及丙烯酸尤佳。含有酸基之單體可個 別使用或作爲二、三或更多種含有酸基之單體的混合物使 m 用。 較佳之包含酯基的單體A尤其包括與前文所述之單體 不同的(甲基)丙烯酸酯、反丁烯二酸酯、順丁烯二酸酯及/ 或乙酸乙烯酯。(甲基)丙烯酸酯一詞包括甲基丙烯酸酯及 丙烯酸酯以及二者之混合物。該等單體已廣爲人知。 所述之共聚單體尤其包括烷基中不含雙鍵或雜原子且 -29- 201226480 其烷基中具有1至10個碳原子之(甲基)丙烯酸酯。 烷基中不含雙鍵或雜原子且其烷基中具有1至10個 碳原子之(甲基)丙烯酸酯尤其包括具有直鏈或支鏈烷基之( 甲基)丙烯酸酯,例如(甲基)丙烯酸甲酯、(甲基)丙烯酸乙 酯、(甲基)丙烯酸正丙酯、(甲基)丙烯酸異丙酯、(甲基) 丙烯酸正丁酯、(甲基)丙烯酸異丁酯、(甲基)丙烯酸三級 丁酯及(甲基)丙烯酸戊酯、(甲基)丙烯酸己酯、(甲基)丙 烯酸2-乙基己酯、(甲基)丙烯酸庚酯、(甲基)丙烯酸辛酯 、(甲基)丙烯酸3-異丙基庚酯、(甲基)丙烯酸壬酯、(甲基 )丙烯酸癸酯;及(甲基)丙烯酸環烷酯,諸如(甲基)丙烯酸 環戊酯、(甲基)丙烯酸環己酯、(甲基)丙烯酸莰酯、(甲基 )丙烯酸降莰酯及(甲基)丙烯酸異莰酯。前文所述之烷基中 具有1至10個碳原子的(甲基)丙烯酸酯可個別使用或作爲 混合物使用。 根據本發明一具體實施樣態,更佳者爲包含高比例之 烷基中具有1至6,較佳爲1至4,更佳爲1或2個碳原 子之(甲基)丙烯酸酯的(甲基)丙烯酸系聚合物,該等單體 的烷基中不具雙鍵或雜原子。因此,更佳者爲具有至少20 重量%,較佳爲至少40重量%,更佳爲至少50重量%,最 佳爲至少55重量%之(甲基)丙烯酸甲酯,更佳爲甲基丙烯 酸甲酯之(甲基)丙烯酸系聚合物。根據本發明一特定具體 實例’(甲基)丙烯酸甲酯對烷基中具有2至10個碳原子且 該烷基中不具雙鍵或雜原子之(甲基)丙烯酸酯的重量比可 爲至少0.5 : 1 ’更佳爲至少2 :丨,該重量比較佳係落在 -30- 201226480 10:1至1:2’更佳爲6:1至1:1,最佳4:1至3:2 之範圍。 另一類共聚單體爲從飽和醇所衍生且烷基中不具雜原 子之烷基中具有至少11個碳原子的(甲基)丙烯酸酯,例如 (甲基)丙烯酸十一酯、(甲基)丙烯酸5_甲基十一酯、(甲基 )丙烯酸十二酯、(甲基)丙烯酸2-甲基十二酯、(甲基)丙烯 酸十三酯、(甲基)丙烯酸5-甲基十三酯、(甲基)丙烯酸十 四酯、(甲基)丙烯酸十五酯、(甲基)丙烯酸十六酯、(甲基 )丙烯酸2-甲基十六酯、(甲基)丙烯酸十七酯、(甲基)丙烯 酸5-異丙基十七酯、(甲基)丙烯酸4-三級丁基十八酯、( 甲基)丙烯酸5-乙基十八酯、(甲基)丙烯酸3-異丙基十八 酯、(甲基)丙烯酸十八酯、(甲基)丙烯酸十九酯、(甲基) 丙烯酸二十酯、(甲基)丙烯酸鯨蠘基二十酯、(甲基)丙烯 酸硬脂醯二十酯、(甲基)丙烯酸二十二酯及/或(甲基)丙烯 酸二十基三十四酯; (甲基)丙烯酸環烷酯,諸如(甲基)丙烯酸2,4,5-三-三級丁 基-3-乙烯基環己酯、(甲基)丙烯酸2,3,4,5-四-三級丁基環 己酯; 雜環(甲基)丙烯酸酯,諸如(甲基)丙烯酸2-(1-咪唑基)乙 酯、(甲基)丙烯酸2-(4-味啉基)乙酯、1-(2-甲基丙烯醯氧 乙基)-2-吡咯啶酮、甲基丙烯酸2-(3-噁唑啶基)乙酯;N-(2-(甲基)丙烯醯氧乙基)伸乙脲、N-(2-(甲基)丙烯醯胺基 乙基)伸乙脲); 含羰基之(甲基)丙烯酸酯,諸如甲基丙烯酸乙醯乙醯基氧 -31 - 201226480 乙酯(AAEMA); (甲基)丙烯酸之腈及其他含氮之甲基丙烯酸酯,諸如N-( 甲基丙烯醯氧乙基)二異丁基酮亞胺、N-(甲基丙烯醯氧乙 基)雙十六基酮亞胺、甲基丙烯醯基醯胺基乙腈、2-甲基丙 烯醯氧乙基-甲基氰醯胺、甲基丙烯酸氰基甲酯; (甲基)丙烯酸芳酯,諸如(甲基)丙烯酸苯甲酯、二苯甲酮 甲基丙烯酸酯(BPMA)或(甲基)丙烯酸苯酯,各情況中之芳 基可未經取代或經取代至高達四次; 烷基中具有羥基之(甲基)丙烯酸酯,更明確地說爲(甲基) 丙烯酸2-羥乙酯,較佳爲甲基丙烯酸2·羥乙酯(HEMA)、( 甲基)丙烯酸羥丙酯,例如(甲基)丙烯酸2-羥丙酯及(甲基) 丙烯酸3-羥丙酯,較佳爲甲基丙烯酸羥丙酯(HPMA)、(甲 基)丙烯酸羥丁酯,較佳爲甲基丙烯酸羥丁酯(HBMA)、(甲 基)丙烯酸3,4-二羥丁酯、(甲基)丙烯酸2,5-二甲基-1,6-己 二醇酯、(甲基)丙烯酸1,10-癸二醇酯、(甲基)丙烯酸甘油 酯及(甲基)丙烯酸之多烷氧化衍生物,更明確地說爲具有 2至10’較佳爲3至6個環氧丙烷單元之一(甲基)丙烯酸 聚丙二醇酯,較佳爲具有約5個環氧丙烷單元之一甲基丙 烯酸聚丙二醇酯(PPM 5)、具有2至10,較佳爲3至6個 環氧乙烷單元之一(甲基)丙烯酸聚乙二醇酯,較佳爲具有 約5個環氧乙烷單元之一甲基丙烯酸聚乙二醇酯(PEM5)、 一(甲基)丙烯酸聚丁二醇酯、一(甲基)丙烯酸聚乙二醇·聚 丙二醇酯; (甲基)丙烯醯胺,更明確地說爲N -羥甲基(甲基)丙烯醯胺 -32- 201226480 、Ν,Ν·二甲胺基丙基(甲基)丙烯醯胺、甲基丙烯酸三級丁 胺基乙酯、二丙酮丙烯醯胺(DAAM)、甲基丙烯醯胺及丙 烯醯胺; 甘油碳酸甲基丙烯酸酯; 甲基丙烯酸2-胺甲醯基氧乙酯,及從飽和脂肪酸衍生之( 甲基)丙烯酸酯,諸如(甲基)丙烯醯氧基-2-羥丙基-棕櫚酸 酯、(甲基)丙烯醯氧基-2-羥丙基-硬脂酸酯及(甲基)丙烯醯 氧基-2-羥丙基-月桂酸酯。 其他類共聚單體係以交聯單體表示。該等單體具有至 少兩個於自由基聚合中具有相似反應性的雙鍵。其更具體 地包括從二醇或從更高級多元醇衍生之(甲基)丙烯酸酯, 例如二(甲基)丙烯酸二醇酯,諸如二(甲基)丙烯酸乙二醇 酯、二(甲基)丙烯酸二乙二醇酯、二(甲基)丙烯酸三乙二 醇酯、二(甲基)丙烯酸四乙二醇酯及二(甲基)丙烯酸聚乙 二醇酯、(甲基)丙烯酸1,3-丁二醇、(甲基)丙烯酸i,4-丁 二醇酯、二(甲基)丙烯酸16 —己二醇酯、二(甲基)丙烯酸 甘油酯、乙氧化雙兩A之二甲基丙烯酸酯及二甲基丙烯酸 二胺甲酸乙酯;具有三或更多個雙鍵之(甲基)丙烯酸酯, 諸如二(甲基)丙烯酸甘油酯、三(甲基)丙烯酸三羥甲基丙 烷酯四(甲基)丙烯酸新戊四醇酯,及五(甲基)丙烯酸二新 戊四醇。 該等共聚單體另外包括乙烯基酯,諸如乙酸乙烯酯、 氯乙烯、柯赫酸乙烯酯(vinyl Versatate)、乙燃-乙酸乙稀 酯、乙烯-氯乙烯;順丁烯二酸衍生物,諸如順丁烯二酸 -33- 201226480 酐、順丁烯二酸之酯,例如順丁烯二酸二甲酯、甲基順丁 烯二酸酐;及反丁烯二酸衍生物,諸如反丁烯二酸二甲酯 0 其他群組之共聚單體爲苯乙烯系單體,諸如苯乙烯、 側鏈中具有烷基取代基之經取代苯乙烯,例如α-甲基苯乙 烯及α-乙基苯乙烯,環上具有烷基取代基之經取代苯乙烯 ,諸如乙烯基甲苯及對-甲基苯乙烯、經鹵化苯乙烯,例 如一氯苯乙烯、二氯苯乙烯、三溴苯乙烯及四溴苯乙烯。 雜環乙烯基化合物,諸如2-乙烯基吡啶、3-乙烯基吡 啶、2 -甲基-5-乙烯基吡啶、3 -乙基-4 -乙烯基吡啶、2,3-二 甲基-5-乙烯基吡啶、乙烯基嘧啶、乙烯基哌啶、9-乙烯基 咔唑、3 -乙烯基咔唑、4 -乙烯基咔唑、1-乙烯基咪唑、2-甲基-1-乙烯基咪唑、Ν -乙烯基吡咯啶酮、2 -乙烯基吡咯啶 酮、Ν-乙烯基吡咯啶、3-乙烯基吡咯啶、Ν-乙烯基己內醯 胺、Ν-乙烯基丁內醯胺、乙烯基噁茂烷、乙烯基呋喃、乙 烯基噻吩、乙烯基噻崠、乙烯基噻唑及氫化乙烯基噻唑、 乙烯基噁唑及氫化乙烯基噁唑; 順丁烯二醯亞胺、甲基順丁烯二醯亞胺; 乙烯基醚及異平基醚;及 乙烯基鹵,諸如氯乙烯、氟乙烯、偏二氯乙烯及偏二氟乙 烯,代表共聚單體之其他實例。 令人意外的優點特別由根據(甲基)丙稀酸系聚合物重 量計較佳含有1重量%至9 9重量% ’更佳爲2 0重量%至 95重量%,最佳40重量%至90重量%之從烷基中不具雙 -34- 201226480 鍵或雜原子且烷基中具有丨至1〇個碳原子之(甲基)丙烯酸 酯所衍生的單元的(甲基)丙烯酸系聚合物所顯示。 特別重要的是(甲基)丙烯酸系聚合物’尤其是根據該( 甲基)丙烯酸系聚合物重量計,其具有〇重量%至1〇重量 %,較佳爲0 · 5重量%至8重量%,更佳爲丨重量%至5重 量%之從含有酸基的單體所衍生之單元。 根據本發明一具體修改,本發明之(甲基)丙烯酸系聚 合物可具有根據其重量計爲0重量%至60重量%,更佳爲 5重量%至5 0重量。/。,最佳丨〇重量%至4 〇重量%之從苯乙 嫌系單體(更明確地說係從苯乙烯、側鏈中具有烷基取代 基之經取代苯乙烯、環上具有烷基取代基之經取代苯乙烯 及/或經鹵化苯乙烯)所衍生之單元。 此外’較佳者係具有非常小比例之具有二或更多個反 應性與(甲基)丙烯酸酯基相同的碳碳雙鍵之(甲基)丙烯酸 醋之(甲基)丙烯酸系聚合物。根據本發明—具體修改,根 據(甲基)丙烯酸系聚合物之重量計,具有二或更多個(甲基 )丙燃酸酯基之化合物的比例較佳限制在不超過5重量。/。, 尤其是不超過2重量% ’特佳係不超過1重量%,更佳爲 不超過0.5重量%,最佳不超過〇,丨重量%。 根據本發明使用之較佳聚合物包含 0.5重量%至60重量%,較佳爲1重量%至40重量%,更 佳爲2重量%至20重量%之從烷基中具有至少—個雙鍵與 8至40個碳原子之(甲基)丙烯酸系單體所衍生之單元; 〇重量%至99重量%,較佳爲30重量%至95重量%,更佳 -35- 201226480 爲40重量%至90重量%之從包含酯基的單體A所衍生之 單元; 〇重量%至10重量%,較佳爲1重量%至8重量%之從具有 酸基的單體所衍生之單元; 0重量%至1 0重量%,較佳爲1重量%至5重量%之一或多 種選自下列之單體:N-(2-(甲基)丙烯醯氧乙基)伸乙脲、 N-(2-(甲基)丙烯醯胺基乙基)-伸乙脲、甲基丙烯酸乙醯乙 醯基氧乙酯、二丙酮丙烯醯胺及二苯甲酮甲基丙烯酸酯; 0重量%至50重量%之從苯乙烯單體所衍生之單元;及 0重量%至50重量%從其他共聚單體所衍生之單元;各情 況中該等數値係根據聚合物之總重計。 根據另一較佳修改,根據本發明使用之聚合物包含 0.5重量%至6 0重量%,較佳爲1重量%至3 0重量%,更 佳爲4重量%至20重量%之從烷基中具有至少一個雙鍵與 8至40個碳原子之(甲基)丙烯酸系單體所衍生之單元; 〇%至99%,較佳爲30%至95%,更佳爲40%至90重量% 之從烷基中具有1至6個碳原子之(甲基)丙烯酸酯所衍生 之單元; 0重量%至1 0重量%,較佳爲1重量%至8重量%之從具有 酸基的單體所衍生之單元; 0重量%至5 0重量%之從苯乙烯單體所衍生之單元;及 0重量%至50重量%從其他共聚單體所衍生之單元;各情 況中該等數値係根據聚合物之總重計。 另外可能使用核殼聚合物作爲(甲基)丙烯酸系聚合物 -36- 201226480 ,該情況中,該核殼聚合物的最外殼較佳係具有包含下列 者之(甲基)丙烯酸酯片段 1重量%至3 0重量%,較佳爲1 5重量%至2 5重量%之從烷 基中具有至少一個雙鍵與8至40個碳原子之(甲基)丙烯酸 系單體所衍生之單元, 0.1重量%至10重量%之從含有酸基之單體所衍生之單元 ,及 50重量%至98.9重量%之從烷基中具有1至6個碳原子之 (甲基)丙烯酸酯所衍生之單元,在各情況中係以該(甲基) 丙烯酸酯片段之重量計。 根據本發明使用之聚合物的碘値較佳落在每100 g聚 合物爲2至250g碘,更佳係每100g聚合物爲5至100g 碘,最佳係每1〇〇 g聚合物爲10至50 g碘之範圍,其係 根據DIN 53 24 1- 1測量。該碘値尤其亦可在本發明分散液 之基礎上測量。 根據本發明使用之聚合物可有益地具有在0至40 mg KOH/g之範圍,較佳爲1至20 mg KOH/g,最佳在2至10 mg KOH/g之範圍的酸値。該酸値可根據DIN EN ISO 2114 且亦以分散液爲基礎測定。 根據本發明使用之聚合物的羥基値較佳可落在0至200 mg KOH/g之範圍,更佳爲1至1 〇〇 mg KOH/g,最佳係在3 至50 mg KOH/g之範圍。該羥基値可根據DIN EN ISO 4629 且亦以分散液爲基礎測定。 根據本發明使用之聚合物的粒子半徑可在廣泛範圍中 -37- 201226480 。因此尤其可能使用粒子半徑在1至500 nm,較佳爲10 至100 nm,更佳爲10至59 nm範圍之乳化聚合物。根據 本發明另一實施樣態,粒子之半徑較佳在60 nm至500 nm,更佳爲70至150 nm,最佳75至100 nm之範圍。粒 子之半徑可利用PCS(光子雙關頻譜法)測定,報告數據係 與d50値(粒子的50%較小,50%較大)相關。爲該目的, 可能利用例如Beckman Coulter N5次微米粒度分析儀。 聚合物的玻璃轉化溫度較佳在〇 °C至7 0 °C之範圍,更 佳在5至60 °C之範圍,最佳在10至50°C之範圍。該玻璃 轉化溫度可受到製備該聚合物所使用的單體之性質與比例 影響。聚合物的玻璃轉化溫度Tg可採已知方式並利用微 差掃描熱量測定法(DSC)測定,更明確地說,係根據DIN ΕΝ I S 0 1 1 3 5 7測定。玻璃轉化溫度較佳可測定爲加熱速率 爲每分鐘10°C的第二加熱曲線之玻璃階段中點。此外,玻 璃轉化溫度Tg亦可利用Fox方程式事先大約計算。根據 Fox T. G., Bull. Am. Physics Soc. 1,3,第 1 23 頁(1 9 5 6) ,其中: 丄=五+ + iWherein R is hydrogen or methyl 'X is oxygen or a group of the formula NR, wherein R is hydrogen or a group having 1 to 6 carbon atoms, and R3 is an alkyl group having 1 to 22 carbon atoms 'Y Oxygen, sulfur or the base of the formula NR", where R" is hydrogen or has! To a group of 6 carbon atoms, and R4 is an unsaturated group having at least 8 carbon atoms and at least two double bonds. The base R3 in the formula (IV) is from 1 to n carbon atoms, preferably from i to 10, more preferably an alkylene group having from 2 to 6 carbon atoms. In a particular embodiment of the invention, the radical R3 is an alkylene radical having from 2 to 4, more preferably 2 carbon atoms, from 23 to 201226480. The alkylene group having 1 to 22 carbon atoms includes, in particular, a methylene group, an exoethyl group, a stretched base group, an extended isopropyl group, an exobutyl group, an exobutyl group, a tert-butyl group or a cyclohexyl group. Stretching ethyl is especially good. The radical R4 contains at least two C-C double bonds which are not part of the aromatic system. Preferably, the group R4 is a group having exactly 8 carbon atoms and having exactly two double bonds. The group R4 is preferably a linear hydrocarbon group containing no hetero atom. According to a particular embodiment of the invention, the group R4 in formula (IV) may comprise a terminal double bond. In another modification of the invention, the group R4 in formula (IV) may be free of terminal double bonds. The double bond present in the group R4 may preferably be conjugated. According to other preferred embodiments of the present invention, the double bond in the group R4 is not conjugated. Preferably, the group R4 having at least two double bonds includes, in particular, octane-2,7-dienyl, oct-3,7-dienyl, octane 4,7·dienyl 'oct-5,7-di Alkenyl, octane-2,4-dienyl, octane-2,5.dienyl, octane-2,6-dienyl, oct-3,5-dienyl, oct-3,6-di Alkenyl and octyl-4,6-dienyl. The (meth)acrylic monomer of the formula (IV) includes, for example, 2-[((2-£)octyl-2,7-dienyl)methylamino] 2-methylprop-2-enoate] Ethyl ester, 2-methylprop-2-enoic acid 2-[((2-Z)octyl-2,7-dienyl)methylamino]ethyl ester, 2-methylprop-2-enoic acid 2 -[((3-E)octyl-3,7-dienyl)methylamino]ethyl ester, 2-methylpropan-2-enoic acid 2-[((4-2) xin.4,7- Dialkenyl)methylamino]ethyl ester, 2-methylpropan-2-enoic acid 2-[(octyl-2,4-dienyl)methylamino]ethyl ester, 2-methylpropan-2-yl 2-[(octyl-2,4-dienyl)methylamino]ethyl acrylate, 2·methylpropan-2-disindolated acid 2_[(oct-3,5-dienyl)methylamino] Ethyl ester, 2_[((2_引辛_2,7-dienyl)methylamino]ethyl-(methyl) acrylamide, 2-[((2-Z) octyl-2,7-di Alkenyl)methylamino]ethyl-(methyl)propenylamine, 2-[((3·Ε)octyl-3,7-dienyl)methylamino]-24- 201226480 Ethyl-(A) Base) C storage amine ' 2 · [((4-Ζ) octyl 4,7-dienyl) methylamino] ethyl-(methyl) propyl decylamine, 2-[(Xin-2, 6-dienyl)methylamino]ethyl-(methyl)propanoid amine, 2-[(octyl-2,4-dienyl)methylamino]ethyl-(methyl)acrylamide , 2-[(oct-3,5-diene )methylamino]ethyl-(methyl)propenylamine, 2-methylpropan-2-butyric acid 2-[((2-£)octyl-2,7-dienyl)ethylamine] Ester, 2-methylprop-2-enoic acid 2-[((2-Z)octyl-2,7-dienyl)ethylamino]ethyl ester, 2-methylprop-2-enoic acid 2- [((3-E)octyl-3,7-dienyl)ethylamino]ethyl ester, 2-methylpropan-2-dicarboxylic acid 2-[((4-Z) 辛·4,7-二Alkenyl)ethylamino]ethyl ester, 2-methylpropan-2-dicarboxylic acid 2-[(octyl-2,6-dienyl)ethylamino]ethyl ester, 2-methylpropan-2-ene 2-[(octyl-2,4-dienyl)ethylamino]ethyl ester, 2-methyl-2-propenoic acid 2-[(octyl-3,5--alkenyl)ethylamino] Ester, propan-2-enoic acid 2-[((2-£) octyl-2,7--alkenyl)methylamino]acetic acid 'propan-2-ylic acid 2-[((2-Ζ) octyl -2,7-dione) methylamino]ethyl ester, prop-2-enoic acid 2-[((3-indolyl)-3,7-dienyl)methylamino]ethyl ester, C- 2-enoic acid 2-[((4-Ζ)octyl_4,7-dienyl)methylamino]ethyl ester, prop-2-enoic acid 2-[(octyl-2,6-dienyl) Methylamino]ethyl ester, prop-2-enic acid 2_[(octyl-2,4-dienyl)methylamino]ethyl ester, propyl-2-enoic acid 2-[(xin-3,5-di Dilute)methylamino]ethyl ester, 2-methylprop-2-enoic acid 2-((24)octyl-2,7-dioxaoxy)ethyl ester, 2-methyl 2-((2-indolyl)-2,7-dienyloxy)ethyl 2-enoate, 2-((3-indolyl)-3,7 2-methylprop-2-enoic acid -dienyloxy)ethyl ester, 2-((4-indolyl)-4,7-dienyloxy)ethyl 2-methylpropan-2-enoate, 2·methylpropyl·2-thin Acid 2-(octyl-2,6--alkoxy)ethyl acetonate, 2-(methyl-2-propenyl)ethyl 2-methylpropan-2-carboxylate, 2-methylpropane-2 2-enoic acid 2-(oct-3,5-dioxaoxy)ethyl ester, prop-2-enoic acid 2-((2-indolyl)-2,7-dienyloxy)ethyl ester, propyl _ 2_Diluted acid 2-((2-Ζ)octyl-2,7-dienyloxy)ethyl ester, prop-2-enoic acid 2_((3_£) 辛_3,7- -25- 201226480 diene oxygen Ethyl ester, prop-2-enoic acid 2-((4-Z)octyl-4,7-dienyloxy)ethyl ester, prop-2-enoic acid 2-(oct-2,6-diene Oxy)ethyl ester, prop-2-enoic acid 2-(octyl-2,4-dienyloxy)ethyl ester and prop-2-enoic acid 2-(oct-3,5-dienyloxy)B The above-mentioned (meth)acrylic monomer of the formula (IV) can be especially obtained by (meth)acrylic acid or (meth)acrylic acid ester (more specifically, methyl (meth)acrylate or (methyl) Ethyl acrylate) is obtained by a method of reacting an alcohol and/or an amine. These reactions have been described above. The reactant to be reacted with (meth)acrylic acid or (meth) acrylate may advantageously conform to formula (V) HX-R-Y-R4 (V), wherein X is oxygen or a group of formula NR', wherein R 'A hydrogen or a group having 1 to 6 carbon atoms' R3 is an alkylene group having 1 to 22 carbon atoms, and Y is an oxygen, sulfur or a group of the formula NR", wherein R" is hydrogen or has 1 to 6 One of the carbon atom groups, and R4 is at least a double unsaturated group having at least 8 carbon atoms. The definitions of preferred R', R", R3, Y and R4 groups are given by reference to formula (IV). Preferred reactants of formula (V) include (methyl(octyl-2,7-dienyl)amino)ethanol, (ethyl (octyl-2,7-dienyl)amino)ethanol, 2-octyl -2,7·dienyloxyethanol, (methyl(octyl-2,7-dienyl)amino)ethylamine, (methyl(octyl 3,7-dienyl)amino)ethanol, (ethyl (octyl-3,7-dienyl)amino)ethanol, 2-oct-3,7-dienyloxyethanol, (methyl(oct-3,7-dienyl)amino) Ethylamine, (A-26-201226480-based (oct-4,7-dienyl)amino)ethanol, (ethyl (oct-4,7-dienyl)amino)ethanol, 2-oct-4 , 7-dienyloxyethanol '(methyl(octyl-4,7-dienyl)amino)ethylamine, (methyl(oct-5,7-dienyl)amino)ethanol, (B) (octyl-5,7-dienyl)amino)ethanol, 2-oct-5,7-dienyloxyethanol, (methyl(oct-5,7-dienyl)amino)ethylamine , (methyl (octyl-2,6-dienyl)amino)ethanol, (ethyl (octyl-2,6-dienyl)amino)ethanol, 2-octyl-2,6-diene Oxyethanol, (methyl(octyl-2,6-dienyl)amino)ethylamine, (methyl(octyl-2,5-dienyl)amine Ethyl alcohol, (ethyl (octyl-2,5-dienyl)amino)ethanol, 2-octane-2,5-dienyloxyethanol, (methyl (octyl-2,5-dienyl) Amino)ethylamine, (methyl(octyl-2.4-dienyl)amino)ethanol, (ethyl(octyl-2,4-dienyl)amino)ethanol, 2-oct-2,4 -dienyloxyethanol, (methyl(octyl-2,4-dienyl)amino)ethylamine, (methyl(oct-3,6-dienyl)amino)ethanol, (ethyl ( Octyl-3,6-dienyl)amino)ethanol, 2-octyl-3,6-dienyloxyethanol, (methyl(oct-3,6-dienyl)amino)ethylamine, ( Methyl (oct-3,5-dienyl)amino)ethanol, (ethyl(oct-3-5)diamino)ethanol]2-oct-3,5-dienyloxyethanol, ( Methyl (octyl-3,5-dienyl)amino)ethylamine, (methyl(oct-4,6-dienyl)amino)ethanol, (ethyl (oct-4,6-diene) Ethyl)ethanol, 2-oct-4,6-dienyloxyethanol and (methyl(oct-4,6-dienyl)amino)ethylamine. The reactants of formula (V) can be used individually or as a mixture. The reactant of the formula (V) can be obtained by a known method including short-chain polymerization of 1,3-butadiene. The term "short chain polymerization" as used herein refers to a reaction of a compound having a conjugated double bond in the presence of a nucleophile. The method set forth in the publications WO 2004/00293 1, WO 03 /03 1 3 79 and WO 02/1 00 8 03, in particular the catalyst and reaction conditions for the reaction, -27-201226480 And the temperature is incorporated into this specification for the purpose of disclosure. The short-chain polymerization of 1,3-butadiene is preferably carried out by using a metal compound containing a metal of Groups 8 to 1 of the periodic table as a catalyst, and more preferably a palladium compound, more preferably palladium-carbon. The olefin complex is described in more detail in the disclosure set forth above. As the nucleophile, especially diols such as ethylene glycol, 1,2-propylene glycol and 1,3 -propylene glycol; diamines such as ethylenediamine, N-methylethylenediamine, hydrazine, Ν'-two can be used. Methylethylenediamine or hexamethylenediamine; or an amino alcohol such as amine ethanol, hydrazine-methylamine ethanol, hydrazine-ethylamine ethanol, amine propanol, hydrazine-methylamine propanol or hydrazine-ethylamine Propanol. In the case where (meth)acrylic acid is the nucleophile used, it is possible, for example, to obtain octadienyl (meth)acrylate, which is particularly suitable for use as a (meth)acrylic acid having 8 to 40 carbon atoms. body. The preferred pressures and temperatures at which short chain polymerization can be carried out are described above, and therefore reference is also made to the foregoing. The preparation of the isomer of the compound having an octa-2,7-dienyl group can be carried out by isomerizing a double bond in the presence of a compound having an octa-2,7-dienyl group. The (meth)acrylic polymer used in accordance with the present invention preferably comprises from 0.5% by weight to 60% by weight, more preferably from 1% by weight to 4% by weight, most preferably from 5% by weight to 25% by weight, particularly preferably 2% by weight to 20% by weight, of a unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group. These (meth)acrylic polymers are preferably obtainable by radical polymerization. Therefore, since the weight fraction of the base derived from the initiator or the molecular weight regulator (chain transfer agent) is generally negligible, the weight fraction of the individual units contained in the polymers is used for The weight fraction of the corresponding monomers from which the polymers are prepared is provided. The (meth)acrylic monomers having at least one double bond and 8 to 40 carbon atoms in the alkyl group described above may be used singly or as a mixture of two or more monomers. In addition to the repeating unit derived from at least one of the above (meth)acrylic monomers having at least one double bond and 8 to 40 carbon atoms in the alkyl group, the preferred polymer present in the dispersion of the present invention may Contains repeating units derived from other monomers. The copolymerizable monomers include, in particular, a monomer having an acid group, a monomer A containing an ester group, and a styrene monomer. The acid group-containing monomer is preferably a compound which is free-radically copolymerizable with the photoinitiator monomer described above. It includes, for example, a monomer having a sulfonic acid group such as ethylenesulfonic acid; a monomer having a phosphonic acid group such as a vinylphosphonic acid; and an unsaturated carboxylic acid such as methacrylic acid, acrylic acid, fumaric acid, and cis-butane Aenedioic acid. It is especially preferred to methacrylic acid and acrylic acid. The acid group-containing monomer may be used alone or as a mixture of two, three or more acid group-containing monomers. The monomer A comprising an ester group preferably comprises, in particular, a (meth) acrylate, a fumarate, a maleate and/or a vinyl acetate different from the monomers described above. The term (meth) acrylate includes methacrylate and acrylate as well as mixtures of the two. These monomers are well known. The comonomers include, inter alia, (meth) acrylates having no double bonds or heteroatoms in the alkyl group and -29 to 201226480 having from 1 to 10 carbon atoms in the alkyl group. The (meth) acrylate having no double bond or hetero atom in the alkyl group and having 1 to 10 carbon atoms in the alkyl group includes, in particular, a (meth) acrylate having a linear or branched alkyl group, for example (A) Methyl acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, isopropyl (meth) acrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, Tertiary butyl (meth)acrylate and amyl (meth)acrylate, hexyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, heptyl (meth)acrylate, (methyl) Octyl acrylate, 3-isopropylheptyl (meth)acrylate, decyl (meth)acrylate, decyl (meth)acrylate; and cycloalkyl (meth)acrylate, such as (meth)acrylic acid ring Amyl ester, cyclohexyl (meth)acrylate, decyl (meth)acrylate, norbornyl (meth)acrylate and isodecyl (meth)acrylate. The (meth) acrylate having 1 to 10 carbon atoms in the alkyl group described above may be used singly or as a mixture. According to a specific embodiment of the present invention, more preferably a (meth) acrylate having a high proportion of alkyl groups having 1 to 6, preferably 1 to 4, more preferably 1 or 2 carbon atoms ( A methyl)acrylic polymer having no double or hetero atom in the alkyl group of the monomers. Accordingly, it is more preferred to have at least 20% by weight, preferably at least 40% by weight, more preferably at least 50% by weight, most preferably at least 55% by weight of methyl (meth) acrylate, more preferably methacrylic acid. Methyl (meth)acrylic polymer. According to a specific embodiment of the present invention, the weight ratio of methyl (meth) acrylate to (meth) acrylate having 2 to 10 carbon atoms in the alkyl group and having no double bond or hetero atom in the alkyl group may be at least 0.5 : 1 'More preferably at least 2 : 丨, the weight is better at -30- 201226480 10:1 to 1:2' better 6:1 to 1:1, best 4:1 to 3: 2 range. Another type of comonomer is a (meth) acrylate having at least 11 carbon atoms in an alkyl group derived from a saturated alcohol and having no hetero atom in the alkyl group, such as undecyl (meth) acrylate, (methyl) 5-methylundecyl acrylate, dodecyl (meth)acrylate, 2-methyldodecyl (meth)acrylate, tridecyl (meth)acrylate, 5-methyl-dodecyl (meth)acrylate Triester, tetradecyl (meth)acrylate, penta(meth)acrylate, hexadecyl (meth)acrylate, 2-methylhexadecyl (meth)acrylate, (meth)acrylic acid Ester, 5-isopropylheptadecylide (meth)acrylate, 4-tert-butyl octadecyl (meth)acrylate, 5-ethyl octadecyl (meth)acrylate, (meth)acrylic acid 3 -isopropyl octadecyl ester, octadecyl (meth) acrylate, decyl (meth) acrylate, hexadecyl (meth) acrylate, whale decyl (meth) acrylate, (methyl) ) stearyl octadecyl acrylate, behenyl (meth) acrylate and/or hexyl trimethyl methacrylate; (methyl Cycloalkyl acrylates such as 2,4,5-tris-tert-butyl-3-vinylcyclohexyl (meth)acrylate, 2,3,4,5-tetra-tertiary (meth)acrylate Hexacyclohexyl ester; heterocyclic (meth) acrylate such as 2-(1-imidazolyl)ethyl (meth)acrylate, 2-(4- tyrosolinyl)ethyl (meth)acrylate, 1- (2-Methyl propylene oxiranyl)-2-pyrrolidone, 2-(3-oxazolidinyl)ethyl methacrylate; N-(2-(methyl) propylene oxiranyl) Ethyl urea, N-(2-(methyl) acrylamidoethyl) ethyl acetal); carbonyl-containing (meth) acrylate, such as ethyl acetyl methacrylate - 31 - 201226480 ethyl ester (AAEMA); nitrile (meth)acrylic acid and other nitrogen-containing methacrylates, such as N-(methacryloyloxyethyl)diisobutyl ketone imine, N-(methacrylofluorene Dihexyl ketimine, methacryl oxime guanamine acetonitrile, 2-methyl propylene oxiranyl-methyl cyanoguanamine, cyanomethyl methacrylate; (meth) acrylate Esters such as benzyl (meth) acrylate, benzophenone methacrylate (BPMA) Or phenyl (meth) acrylate, in each case the aryl group may be unsubstituted or substituted up to four times; the (meth) acrylate having a hydroxyl group in the alkyl group, more specifically (meth) acrylate 2-Hydroxyethyl ester, preferably 2-hydroxyethyl methacrylate (HEMA), hydroxypropyl (meth) acrylate, such as 2-hydroxypropyl (meth) acrylate and 3-hydroxy (meth) acrylate Propyl ester, preferably hydroxypropyl methacrylate (HPMA), hydroxybutyl (meth) acrylate, preferably hydroxybutyl methacrylate (HBMA), 3,4-dihydroxybutyl (meth) acrylate Ester, 2,5-dimethyl-1,6-hexanediol (meth)acrylate, 1,10-decane (meth)acrylate, glyceryl (meth)acrylate and (methyl) a polyalkylene oxide derivative of acrylic acid, more specifically a polypropylene glycol (meth)acrylate having 2 to 10', preferably 3 to 6 propylene oxide units, preferably having about 5 propylene oxides. One of the units is polypropylene glycol methacrylate (PPM 5), one of 2 to 10, preferably 3 to 6 ethylene oxide units (meth)acrylic acid polyethylene An alcohol ester, preferably having one of about 5 ethylene oxide units, polyethylene glycol methacrylate (PEM5), poly(butylene glycol) acrylate, and poly(ethylene) methacrylate Alcohol-polypropylene glycol ester; (meth) acrylamide, more specifically N-hydroxymethyl (meth) acrylamide-32-201226480, hydrazine, hydrazine dimethylaminopropyl (methyl) Acrylamide, butylaminoethyl methacrylate, diacetone acrylamide (DAAM), methacrylamide and acrylamide; glycerol carbonate methacrylate; 2-aminomethyl methacrylate Oxyethyl ester, and (meth) acrylate derived from saturated fatty acids, such as (meth) propylene methoxy-2-hydroxypropyl-palmitate, (meth) propylene oxy-2-hydroxypropyl Base-stearate and (meth)acryloxy-2-hydroxypropyl-laurate. Other types of copolymerization systems are represented by crosslinking monomers. The monomers have at least two double bonds having similar reactivity in the free radical polymerization. It more specifically includes (meth) acrylate derived from a diol or from a higher polyol, such as a di(meth) acrylate glycol such as ethylene glycol di(meth)acrylate, di(methyl) Diethylene glycol acrylate, triethylene glycol di(meth)acrylate, tetraethylene glycol di(meth)acrylate, polyethylene glycol di(meth)acrylate, (meth)acrylic acid 1 , 3-butanediol, i,4-butylene glycol (meth)acrylate, 16-hexanediol di(meth)acrylate, glycerol di(meth)acrylate, bis, Methacrylate and ethyl dimethacrylate; a (meth) acrylate having three or more double bonds, such as glyceryl di(meth)acrylate, trishydroxypropyl tri(meth)acrylate Propyl ester neopentyl glycol tetra(meth)acrylate, and neopentyltetrakis(penta)acrylate. The comonomers additionally include vinyl esters such as vinyl acetate, vinyl chloride, vinyl Versatate, ethylene-vinyl acetate, ethylene-vinyl chloride; maleic acid derivatives, Such as maleic acid-33-201226480 anhydride, ester of maleic acid, such as dimethyl maleate, methyl maleic anhydride; and fumaric acid derivatives, such as anti-butyl Dimethyl enedionate 0 Other groups of comonomers are styrenic monomers such as styrene, substituted styrenes having an alkyl substituent in the side chain, such as α-methylstyrene and α-B. a styrene, a substituted styrene having an alkyl substituent on the ring, such as vinyl toluene and p-methyl styrene, a halogenated styrene such as monochlorostyrene, dichlorostyrene, tribromostyrene, and Tetrabromostyrene. 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-vinyl Imidazole, oxime-vinylpyrrolidone, 2-vinylpyrrolidone, oxime-vinylpyrrolidine, 3-vinylpyrrolidine, fluorene-vinyl caprolactam, fluorene-vinyl butyrolactam, Vinyl oxane, vinyl furan, vinyl thiophene, vinyl thiazide, vinyl thiazole and hydrogenated vinyl thiazole, vinyl oxazole and hydrogenated vinyl oxazole; maleimide, methyl cis Butylene diimine; vinyl ether and isobutyl ether; and vinyl halides such as vinyl chloride, vinyl fluoride, vinylidene chloride and vinylidene fluoride, representing other examples of comonomers. The surprising advantage is particularly preferably from 1% by weight to 99% by weight, based on the weight of the (meth)acrylic polymer, more preferably from 20% to 95% by weight, most preferably from 40% by weight to 90% by weight. (%) by weight of a (meth)acrylic polymer derived from a unit derived from a (meth) acrylate having no bis-34-201226480 bond or a hetero atom in the alkyl group and having from 丨 to 1 carbon atom in the alkyl group. display. It is particularly important that the (meth)acrylic polymer 'in particular, based on the weight of the (meth)acrylic polymer, has from 〇% by weight to 1% by weight, preferably from 0.001 to 8% by weight. %, more preferably from 5% by weight to 5% by weight of the unit derived from the acid group-containing monomer. According to a specific modification of the present invention, the (meth)acrylic polymer of the present invention may have a weight of from 0% by weight to 60% by weight, more preferably from 5% by weight to 50% by weight. /. , the optimum 丨〇 weight% to 4 〇% by weight of the styrene monomer (more specifically, from styrene, substituted styrene having an alkyl substituent in the side chain, having an alkyl group on the ring) A unit derived from a substituted styrene and/or halogenated styrene. Further, 'the preferred one is a (meth)acrylic polymer having a very small proportion of (meth)acrylic acid having two or more carbon-carbon double bonds having the same reactivity as the (meth) acrylate group. According to the present invention - specifically modified, the proportion of the compound having two or more (meth)propionate groups is preferably limited to not more than 5 parts by weight based on the weight of the (meth)acrylic polymer. /. In particular, it does not exceed 2% by weight, and the amount is not more than 1% by weight, more preferably not more than 0.5% by weight, and most preferably not more than 〇, 丨% by weight. Preferred polymers for use in accordance with the invention comprise from 0.5% to 60% by weight, preferably from 1% to 40% by weight, more preferably from 2% to 20% by weight, having at least one double bond from the alkyl group. a unit derived from a (meth)acrylic monomer having 8 to 40 carbon atoms; 〇% by weight to 99% by weight, preferably 30% by weight to 95% by weight, more preferably -35-201226480 is 40% by weight Up to 90% by weight of the unit derived from the monomer A containing an ester group; 〇% by weight to 10% by weight, preferably 1% by weight to 8% by weight of the unit derived from the monomer having an acid group; From 100% by weight to 10% by weight, preferably from 1% by weight to 5% by weight, of one or more monomers selected from the group consisting of N-(2-(methyl)acryloyloxyethyl) acetal, N- (2-(Methyl)acryloylaminoethyl)-e-ethylurea, acetamyl ethoxyethyl methacrylate, diacetone acrylamide and benzophenone methacrylate; 0% by weight to 50% by weight of units derived from styrene monomer; and 0% to 50% by weight of units derived from other comonomers; According based on the total weight of the polymer. According to another preferred modification, the polymer used according to the invention comprises from 0.5% by weight to 60% by weight, preferably from 1% by weight to 30% by weight, more preferably from 4% by weight to 20% by weight, based on the alkyl group. a unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms; 〇% to 99%, preferably 30% to 95%, more preferably 40% to 90% by weight % of a unit derived from a (meth) acrylate having 1 to 6 carbon atoms in the alkyl group; 0% by weight to 10% by weight, preferably 1% by weight to 8% by weight, based on having an acid group Monomer-derived unit; 0% to 50% by weight of units derived from styrene monomer; and 0% to 50% by weight of units derived from other comonomers; The lanthanide is based on the total weight of the polymer. It is also possible to use a core-shell polymer as the (meth)acrylic polymer-36-201226480, in which case the outermost shell of the core-shell polymer preferably has a weight of (meth)acrylate fragment 1 comprising: % to 30% by weight, preferably 15 to 25 % by weight of a unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group, 0.1% by weight to 10% by weight of the unit derived from the acid group-containing monomer, and 50% by weight to 99.9% by weight of the (meth) acrylate having 1 to 6 carbon atoms in the alkyl group The unit, in each case, is based on the weight of the (meth) acrylate fragment. The iodonium of the polymer used according to the invention preferably falls between 2 and 250 g of iodine per 100 g of polymer, more preferably between 5 and 100 g of iodine per 100 g of polymer, and the optimum is 10 per 1 g of polymer. Up to 50 g of iodine, measured according to DIN 53 24 1- 1. The iodonium can also be measured in particular on the basis of the dispersion of the invention. The polymer used according to the invention may advantageously have an acid bismuth in the range from 0 to 40 mg KOH/g, preferably from 1 to 20 mg KOH/g, most preferably from 2 to 10 mg KOH/g. The acid bismuth can be determined according to DIN EN ISO 2114 and also on a dispersion basis. The hydroxy hydrazine of the polymer used according to the invention preferably falls within the range of from 0 to 200 mg KOH/g, more preferably from 1 to 1 〇〇mg KOH/g, most preferably from 3 to 50 mg KOH/g. range. The hydroxy oxime can be determined according to DIN EN ISO 4629 and also on a dispersion basis. The particle radius of the polymer used in accordance with the present invention can range from -37 to 201226480. It is therefore particularly possible to use an emulsified polymer having a particle radius of from 1 to 500 nm, preferably from 10 to 100 nm, more preferably from 10 to 59 nm. According to another embodiment of the invention, the radius of the particles is preferably from 60 nm to 500 nm, more preferably from 70 to 150 nm, most preferably from 75 to 100 nm. The radius of the particles can be determined by PCS (photon spectroscopy) and the reported data is related to d50値 (50% smaller, 50% larger). For this purpose, it is possible to utilize, for example, a Beckman Coulter N5 submicron particle size analyzer. The glass transition temperature of the polymer is preferably in the range of from 〇 ° C to 70 ° C, more preferably in the range of from 5 to 60 ° C, most preferably in the range of from 10 to 50 ° C. The glass transition temperature can be affected by the nature and proportion of the monomers used to prepare the polymer. The glass transition temperature Tg of the polymer can be determined in a known manner and measured by differential scanning calorimetry (DSC), more specifically, according to DIN ΕΝ I S 0 1 1 3 5 7 . The glass transition temperature is preferably determined as the midpoint of the glass phase of the second heating curve at a heating rate of 10 ° C per minute. Further, the glass transition temperature Tg can also be calculated in advance using the Fox equation. According to Fox T. G., Bull. Am. Physics Soc. 1, 3, p. 1 23 (1 9 5 6), where: 丄=five + + i
Tg Tgl Tg2 Tgn 其中Xn爲單體n之質量分率(重量%/100),而Tgn表示單 體η之同元聚合物的玻璃轉化溫度(以克氏度數計)。熟悉 本技術之人士可於Polymer Handbook(第2版,J. Wiley & Sons,New York( 1 975))中發現其他可用資訊,該書提供最 -38- 201226480 常用之同元聚合物的Tg値。此處之聚合物可具有一或多 個不同玻璃轉化溫度。因此,該等數値適用於可藉由聚合 本發明之單體混合物獲得之片段。 根據本發明使用之具有從烷基中具有至少一個雙鍵與 8至40個碳原子之(甲基)丙烯酸系單體所衍生之單元的( 甲基)丙烯酸系聚合物之分散液的最低成膜溫度較佳爲至 少1 0 °C,更佳爲至少2 5 °C,最佳爲至少4 0 °C,此可根據 DIN ISΟ 2 1 1 5測量。該等値涉及不含聚結劑之分散液。 就許多應用及性質而言,聚合物之結構並非關鍵。因 此,該等聚合物(尤其是乳化聚合物)可代表雜亂共聚物、 梯度共聚物、嵌段共聚物及/或接枝共聚物。嵌段共聚物 及梯度共聚物可藉由例如在鏈增長過程中不連續地改變單 體組成而獲得。根據本發明一較佳實施樣態,乳化聚合物 爲雜亂共聚物,其中在聚合期間該單體組成實質上不變。 因此,由於單體可能具有不同共聚參數,在整體聚合物之 聚合物鏈上的精確組成可能變化。 該聚合物(較佳爲乳化聚合物)可構成均質聚合物,其 於例如分散液中形成具有一致組成之粒子。在該情況中, 乳化聚合物可例如由一或更多個可藉由聚合上述單體或單 體混合物而獲得之片段所構成。 根據本發明其他具體實例,該聚合物可包含二或更多 個片段。例如,可能使用具有核殼結構之乳化聚合物,其 可具有一、二、三或更多個殻。在該情況中,可藉由聚合 上述單體混合物而獲得之片段較佳形成該核殼聚合物的最 -39- 201226480 外殼。該殻可藉由共價鍵連接至該核或連接至內殼。此外 ,該殼亦可經聚合而不接枝於該核或內殼。在該具體實例 中,可藉由聚合上述單體或單體混合物而獲得之片段在許 多情況中可利用適用溶劑而自該核分開並分離。 可藉由聚合具有烷基中具有至少一個雙鍵與8至4〇 個碳原子之(甲基)丙烯酸系單體的單體混合物而獲得之片 段對核的重量比較佳可落在10:1至1:6,更佳爲5:1 至1 : 3之範圍。 該核較佳可由包含50重量%至100重量%,較佳爲60 重量%至90重量%之從(甲基)丙烯酸酯所衍生之單元的聚 合物形成。此處較佳者爲醇基較佳包含1至30個碳原子 ,更佳爲1至20個碳原子,最佳1至10個碳原子之(甲 基)丙烯酸的酯。此等(甲基)丙烯酸酯更具體地包括從飽和 醇衍生之(甲基)丙烯酸酯,諸如(甲基)丙烯酸甲酯、(甲基 )丙烯酸乙酯、(甲基)丙烯酸正丙酯、(甲基)丙烯酸異丙酯 、(甲基)丙烯酸正丁酯、(甲基)丙烯酸三級丁酯、(甲基) 丙烯酸戊酯及(甲基)丙烯酸己酯。 根據本發明一特定具體實例,該核可使用包含甲基丙 烯酸酯及丙烯酸酯的混合物來製備。因此,更明確地說, 可能使用甲基丙烯酸甲酯及具有2至6個碳原子之丙烯酸 酯(諸如丙烯酸乙酯、丙烯酸丁酯及丙烯酸己酯)的混合物 〇 此外,該核之聚合物可包含前文所述之共聚單體。根 據一較佳修改,該核可經交聯。該交聯可經由使用具有二 -40- 201226480 、三或更多個可自由基聚合雙鍵的單體而獲致。當需要將 殼接枝於核時,甲基丙烯酸烯丙酯爲較佳之多不飽和單體 〇 較佳使用之乳化聚合物的殼較佳可包含1 5重量%至 50重量%之從烷基中具有至少一個雙鍵及8至40個碳原 子的(甲基)丙烯酸系單體所衍生之單元。 根據一具體實施樣態,該核的玻璃轉化溫度較佳可 在-30至200°C之範圍,更佳可在-20至150°C之範圍。該 殼的玻璃轉化溫度較佳可在-3(TC至70°C之範圍,更佳可 在-0至50°C之範圍,最佳可在10至40°C之範圍。根據本 發明一具體實施樣態,該核之玻璃轉化溫度可大於該殼之 玻璃轉化溫度。較有利狀況係,該核之玻璃轉化溫度可高 於該殼之玻璃轉化溫度至少1 (TC,較佳爲至少20°C。 上述包含從烷基中具有至少一個雙鍵與8至40個碳 原子之(甲基)丙烯酸系單體所衍生之重複單元的(甲基)丙 烯酸系聚合物可採已知方式製備,例如藉由溶液聚合、整 體聚合或乳化聚合,亦可使用該等聚合方法的變化,諸如 ATRP(原子轉移自由基聚合)、NMP(氮氧化物媒介之聚合) 或RAFT(可逆力口成片段鏈轉移)方法。該聚合較佳係以乳 化聚合方式進行。 乳化聚合法係描述於包括Ullmann's Encyclopedia of Industrial Chemistry第5版之來源中。就該等方法而言, 該一般途徑係用以製備可包括水以及典型添加劑(更明確 地說,用於安定該乳液之乳化劑及保護膠體)的水相。Tg Tgl Tg2 Tgn where Xn is the mass fraction of the monomer n (% by weight/100), and Tgn is the glass transition temperature (in degrees Kelvin) of the homopolymer of the monomer η. Other useful information can be found in the Polymer Handbook (2nd Edition, J. Wiley & Sons, New York (1 975)), which provides the Tg of the most common meta-polymers of -38-201226480. value. The polymer herein may have one or more different glass transition temperatures. Accordingly, the numbers are applicable to fragments obtainable by polymerizing the monomer mixture of the present invention. The minimum dispersion of a (meth)acrylic polymer having a unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group used in accordance with the present invention The film temperature is preferably at least 10 ° C, more preferably at least 25 ° C, most preferably at least 40 ° C, which can be measured according to DIN IS Ο 2 1 15 . These crucibles involve dispersions that do not contain coalescents. The structure of the polymer is not critical for many applications and properties. Thus, such polymers (especially emulsion polymers) may represent scrambled copolymers, gradient copolymers, block copolymers and/or graft copolymers. The block copolymer and the gradient copolymer can be obtained by, for example, discontinuously changing the monomer composition during chain growth. According to a preferred embodiment of the invention, the emulsified polymer is a scrambled copolymer wherein the monomer composition is substantially unchanged during polymerization. Thus, as monomers may have different copolymerization parameters, the exact composition of the polymer chains of the overall polymer may vary. The polymer, preferably an emulsified polymer, may constitute a homogeneous polymer which forms, for example, particles having a uniform composition in the dispersion. In this case, the emulsified polymer may, for example, be composed of one or more fragments obtainable by polymerizing the above monomers or monomer mixtures. According to other embodiments of the invention, the polymer may comprise two or more fragments. For example, it is possible to use an emulsion polymer having a core-shell structure, which may have one, two, three or more shells. In this case, the fragment obtained by polymerizing the above monomer mixture preferably forms the most -39-201226480 outer shell of the core-shell polymer. The shell may be attached to the core by a covalent bond or to the inner shell. Further, the shell may also be polymerized without being grafted to the core or inner shell. In this embodiment, the fragment obtainable by polymerizing the above monomer or monomer mixture can be separated and separated from the core in many cases by using a suitable solvent. The weight of the core obtained by polymerizing a monomer mixture having a (meth)acrylic monomer having at least one double bond and 8 to 4 carbon atoms in the alkyl group may preferably be 10:1 by weight. To 1:6, more preferably in the range of 5:1 to 1:3. The core may preferably be formed of a polymer comprising 50% by weight to 100% by weight, preferably 60% by weight to 90% by weight, of the unit derived from (meth) acrylate. Preferred herein are esters of (meth)acrylic acid having an alcohol group preferably containing from 1 to 30 carbon atoms, more preferably from 1 to 20 carbon atoms, most preferably from 1 to 10 carbon atoms. These (meth) acrylates more particularly include (meth) acrylates derived from saturated alcohols, such as methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, Isopropyl (meth)acrylate, n-butyl (meth)acrylate, butyl (meth)acrylate, amyl (meth)acrylate and hexyl (meth)acrylate. According to a particular embodiment of the invention, the core can be prepared using a mixture comprising methacrylate and acrylate. Therefore, more specifically, it is possible to use a mixture of methyl methacrylate and an acrylate having 2 to 6 carbon atoms such as ethyl acrylate, butyl acrylate and hexyl acrylate. Contains the comonomers described above. According to a preferred modification, the core can be crosslinked. This crosslinking can be achieved by using a monomer having two -40 to 201226480, three or more radically polymerizable double bonds. When it is desired to graft the shell to the core, the allyl acrylate is preferably a polyunsaturated monomer. Preferably, the shell of the emulsified polymer preferably comprises from 15 to 50% by weight of the alkyl group. A unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms. According to a specific embodiment, the glass transition temperature of the core is preferably in the range of -30 to 200 ° C, more preferably in the range of -20 to 150 ° C. The glass transition temperature of the shell is preferably in the range of -3 (TC to 70 ° C, more preferably in the range of -0 to 50 ° C, and most preferably in the range of 10 to 40 ° C. According to the present invention In a specific implementation, the glass transition temperature of the core may be greater than the glass transition temperature of the shell. Advantageously, the glass transition temperature of the core may be higher than the glass transition temperature of the shell by at least 1 (TC, preferably at least 20). The above (meth)acrylic polymer comprising a repeating unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group can be prepared in a known manner. For example, by solution polymerization, bulk polymerization or emulsion polymerization, changes in the polymerization methods such as ATRP (atomic transfer radical polymerization), NMP (polymerization of nitrogen oxide medium) or RAFT (reversible force fragmentation) may also be used. Chain transfer method. The polymerization is preferably carried out by emulsion polymerization. The emulsion polymerization process is described in a source comprising Ullmann's Encyclopedia of Industrial Chemistry, version 5. For these processes, the general route is used to prepare include The aqueous phase of water and typical additives (more specifically, the emulsifier and protective colloid used to stabilize the emulsion).
C -41 - 201226480 然後將該水相與單體混合,並在該水相中進行聚合。 可在某一時間間隔中分批或連續添加呈混合物或在水中之 乳液形式的單體。 可呈例如迷你乳液或微乳液來進行該乳化聚合。彼等 係更詳細描述於 Chemistry and Technology of Emulsion Polymerisation,Α·Μ. van Herk(編者),Blackwell Publishing, O x f o r d 2 0 0 5 及 J · O ’ D ο η n e 11,E · W · K a 1 e r,M a c r o m o 1 e c u 1 a r Rapid Communications 2007,28(14),1445-1454。迷你乳 液的一般特徵係使用共安定劑或潤脹劑,經常使用長鏈烷 或醇。在迷你乳液之情況中的液滴大小較佳落在0.05至 2 0 μηι之範圍。在微乳液之情況中的液滴大小較佳落在低 於1 μιη之範圍’使得欲獲得之粒子小於50 nm之大小。 在微乳液之情況中,一般使用額外界面活性劑,其實例爲 己醇或相似化合物。 含單體相在水相中之分散可使用已知方式進行。其更 具體地包括亦施加超音波之機械性方法。 在均質乳化聚合物之製備中,較佳可使用較佳包含 0.5至60重量% ’較佳爲1至40重量%之烷基中具有至少 一個雙鍵及8至40個碳原子的(甲基)丙烯酸系單體之單體 混合物。 當製備核殼聚合物時,可在數個步驟中改變該單體混 合物之組成’聚合較佳係在該組成改變之前進行至轉化率 爲至少8 0重量% ’更佳爲至少9 5重量%,各情況中係根 據所使用之單體混合物的總重計。可採已知方式監測各步 -42- 201226480 驟中之聚合反應的進程,諸如藉由重量測定法或氣體層析 術監測。 用於製備核之單體混合物較佳包含50重量%至1〇〇重 量%之(甲基)丙烯酸酯,尤佳係使用丙烯酸酯與甲基丙烯 酸酯之混合物。製備該核之外,可將(較佳)包含1重量% 至60重量%,較佳爲15重量%至25重量%之烷基中具有 至少一個雙鍵及8至40個碳原子的(甲基)丙烯酸系單體的 單體混合物接枝或聚合於該核。 乳化聚合較佳係在〇至120 °C之範圍,更佳係在30至 1 00 °C之範圍的溫度下進行。已證實在本文尤其適用之聚 合溫度係在高於60°C至低於90°C之範圍,通常係在高於 7〇°C至低於85°C之範圍,較佳係在高於75°C至低於85°C之 範圍的溫度。 該聚合作用係使用慣用於乳化聚合的起始劑引發。適 用之有機起始劑爲例如氫過氧化物,諸如過氧化三級丁基 或氫過氧化異丙苯。適用之無機起始劑爲過氧化氫以及過 氧二硫酸之鹼金屬鹽及銨鹽,更明確地說,爲過氧二硫酸 銨、過氧二硫酸鈉及過氧二硫酸鉀。適用之氧化還原起始 劑系統爲例如三級胺與過氧化物或二亞硫酸鈉及過氧二硫 酸之鹼金屬鹽及銨鹽(更明確地說,爲過氧二硫酸鈉及過 氧二硫酸鉀)之組合物。其他細節可自技術文獻得知,更 明確地說,得自 H. Rauch-Puntigam, Th. V5lker, "Acryl-und Methacrylverbindungen", Springer, Heidelberg, 19 6 7 或 Kirk-Othmer,Encyclopedia of Chemical Technology, -43- 201226480C -41 - 201226480 The aqueous phase is then mixed with the monomer and polymerized in the aqueous phase. Monomers in the form of a mixture or emulsion in water may be added in batches or continuously over a certain time interval. The emulsion polymerization can be carried out, for example, as a mini emulsion or a microemulsion. They are described in more detail in Chemistry and Technology of Emulsion Polymerisation, Her·Μ. van Herk (editor), Blackwell Publishing, Oxford 2 0 0 5 and J · O ' D ο η ne 11, E · W · K a 1 er,M acromo 1 ecu 1 ar Rapid Communications 2007, 28(14), 1445-1454. Mini-milk is generally characterized by the use of co-stabilizers or swelling agents, often using long chain alkanes or alcohols. The droplet size in the case of the miniemulsion preferably falls within the range of 0.05 to 20 μm. The droplet size in the case of the microemulsion preferably falls within a range of less than 1 μη so that the particles to be obtained are smaller than 50 nm. In the case of microemulsions, additional surfactants are typically employed, examples of which are hexanol or similar compounds. The dispersion of the monomer-containing phase in the aqueous phase can be carried out in a known manner. It more specifically includes a mechanical method of applying ultrasonic waves as well. In the preparation of the homogeneous emulsion polymer, it is preferred to use a methyl group which preferably contains 0.5 to 60% by weight, preferably 1 to 40% by weight, of an alkyl group having at least one double bond and 8 to 40 carbon atoms. a monomer mixture of acrylic monomers. When preparing a core-shell polymer, the composition of the monomer mixture can be varied in several steps. The polymerization is preferably carried out until the composition is changed to a conversion of at least 80% by weight, more preferably at least 9.55% by weight. In each case, based on the total weight of the monomer mixture used. The progress of the polymerization in each step -42 - 201226480 can be monitored in a known manner, such as by gravimetric or gas chromatography. The monomer mixture used for the preparation of the core preferably comprises from 50% by weight to 1% by weight of the (meth) acrylate, and more preferably a mixture of acrylate and methacrylate. In addition to preparing the core, (preferably) comprising from 1% by weight to 60% by weight, preferably from 15% by weight to 25% by weight, of the alkyl group having at least one double bond and from 8 to 40 carbon atoms (A) A monomer mixture of an acrylic monomer is grafted or polymerized to the core. The emulsion polymerization is preferably carried out at a temperature of from 120 ° C to 120 ° C, more preferably from 30 to 100 ° C. It has been found that the polymerization temperatures particularly useful herein are in the range of from more than 60 ° C to less than 90 ° C, usually in the range of from more than 7 ° C to less than 85 ° C, preferably above 75 ° Temperature from °C to below 85 °C. The polymerization is initiated using an initiator which is customary for emulsion polymerization. Suitable organic starters are, for example, hydroperoxides such as tertiary butyl peroxide or cumene hydroperoxide. Suitable inorganic initiators are the alkali metal salts and ammonium salts of hydrogen peroxide and peroxodisulfuric acid, more specifically ammonium peroxodisulphate, sodium peroxodisulfate and potassium peroxodisulfate. Suitable redox initiator systems are, for example, tertiary amines and peroxides or alkali metal salts and ammonium salts of sodium disulfite and peroxodisulfuric acid (more specifically, sodium peroxodisulfate and potassium peroxodisulfate) a composition. Further details are known from the technical literature, more specifically from H. Rauch-Puntigam, Th. V5lker, "Acryl-und Methacrylverbindungen", Springer, Heidelberg, 19 6 7 or Kirk-Othmer, Encyclopedia of Chemical Technology , -43- 201226480
Vol. 1,第 386 頁之後,J. Wiley,New York, 1978。本發 明這方面尤佳者係使用有機及/或無機起始劑。 所述之起始劑二者可個別使用或作爲混合物使用。彼 等之較佳用量以個別階段之單體的總重計爲0.05重量%至 3.0重量%。亦可能較佳係使用具有不同半衰期之不同聚 合起始劑的混合物來進行聚合作用,以維持聚合過程且在 不同聚合溫度下之自由基流不變。 批料之安定化較佳係利用乳化劑及/或保護保護膠體 達成。該乳液較佳係藉由乳化劑安定,以獲得低分散液黏 度。乳化劑之總量以所使用之單體的總重計較佳爲0.1重 量%至1 5重量%,尤其是1重量%至1 〇重量%,更佳爲2 重量%至5重量%。根據本發明一具體實施樣態,可在聚 合期間添加一部分該等乳化劑。 特別適用之乳化劑爲陰離子或非離子乳化劑或其混合 物,更明確地說係 -硫酸烷酯,較佳爲烷基中具有8至18個碳原子之 硫酸烷酯,烷基中具有8至18個碳原子及具有1至50個 環氧乙烷單元之硫酸烷基醚及硫酸烷基芳基醚; -磺酸酯,較佳爲烷基中具有8至18個碳原子之烷 基磺酸酯,烷基中具有8至18個碳原子之烷基芳基磺酸 酯,烷基中具有4至15個碳原子之磺琥珀酸與一元醇或 烷基酚之酯及單酯;若情況適當,該等醇或烷基酚亦可經 1至40個環氧乙烷單元乙氧化; -磷酸偏酯及其鹼金屬及銨鹽,較佳爲烷基或烷基芳 -44 - 201226480 基中具有8至20個碳原子及具有1至5個環氧乙烷單元 之磷酸烷酯及磷酸烷基芳酯; -烷基聚二醇醚,較佳係烷基中具有8至20個碳原 子及具有8至40個環氧乙烷單元; -烷基芳基聚二醇醚,較佳係烷基或烷基芳基中具有 8至20個碳原子及具有8至40個環氧乙烷單元; -環氧乙烷/環氧丙烷共聚物,較佳爲嵌段共聚物, 較宜具有8至40個環氧乙烷及/或環氧丙烷單元。 尤佳之陰離子乳化劑更具體地包括硫酸脂肪醇醚、磺 琥珀酸二辛酯、硫酸月桂酯、C15-烷烴磺酸酯,可能使用 通常呈鹼金屬鹽(尤其是鈉鹽)形式之該等化合物。該等化 合物可從市面購得,更明確地說,其商標爲 Disponil® FES 32、Aerosol® OT 75、Texapon® Κ 1 296 及 Statexan® K1,得自 Cognis GmbH、Cytec Industries,Inc.及 Bayer AG等公司。 可用之非離子乳化劑包括具有30個環氧乙烷單元之 三級辛基酚乙氧化物及較佳係烷基中具有8至20個碳原 子且具有8至40個環氧乙烷單元之脂肪醇聚乙二醇醚。 該等乳化劑可從市面購得,其商標爲Triton® X 305(Fluka)、 Tergitol® 15-S-7(Sigma-Aldrich Co.)、Marlipal® 1618/25(Sasol Germany)及 Marlipal® 0 13/400(Sasol Germany)。 較佳可使用陰離子乳化劑及非離子乳化劑之混合物。 陰離子乳化劑對非離子乳化劑之重量比可在20 : 1至1 : 20,較佳爲2: 1至1: 10,更佳爲1: 1至1:5之範圍。 -45- 201226480 已證實尤其適用之混合物爲包含硫酸酯(尤其是硫酸脂肪 醇醚)、硫酸月桂酯或磺酸酯(尤其是磺琥珀酸二辛酯)或烷 烴磺酸酯作爲陰離子乳化劑,以及烷基酚乙氧化物或脂肪 醇聚乙二醇醚(各情況中較佳係烷基中具有8至20個碳原 子且具有8至40個環氧乙烷單元)作爲非離子乳化劑之混 合物。 若情況適當’該等乳化劑亦可作爲與保護膠體之混合 物使用。適用之保護膠體包括部分水解聚乙酸乙烯酯、聚 乙烯基吡咯啶酮、羧甲基纖維素、甲基纖維素、羥乙基纖 維素及羥丙基纖維素、澱粉、蛋白質、聚(甲基)丙烯酸、 聚(甲基)丙烯醯胺、聚乙烯磺酸、三聚氰胺-甲醛磺酸酯、 萘-甲醛磺酸酯、苯乙烯-順丁烯二酸及乙烯基醚-順丁烯二 酸共聚物。若使用保護膠體,其甩量以該等單體的總量計 較佳爲〇·〇1重量%至1.0重量%。該等保護膠體可在聚合 作用開始之前包括於起始進料中或計量加入。起始劑可包 括在起始進料中或計量加入。此外,亦可能一部分該起始 劑包括在該起始進料中,並計量加入其餘部分。 聚合作用較佳係藉由將批料加熱至聚合溫度並計量加 入起始劑而開始’較佳係於水溶液中進行。乳化劑及單體 之計量加入進料可分別進行或作爲混合物進行,尤其是作 爲在水中之乳液進行。在計量添加乳化劑及單體之混合物 的情況中’採用的途徑係在該聚合反應器之混合機上游在 水中乳化或預混合乳化劑及單體。較佳情況係,首先將一 部分單體(例如1至10%)引至該反應器,並藉由添加起始 -46 - 201226480 劑而開始該聚合作用。其餘單體的計量加入較佳係在聚合 反應開始之後(例如’該聚合作用開始之後5至15分鐘)開 始。 較佳使用且具有高不可溶比例之聚合物的乳化聚合物 可以前文所述之方式獲得’獲得高分子量之反應參數已爲 人知。因此,更明確地說,在這方面可能省略使用分子量 調節劑(鏈轉移劑)。在目標爲低比例不可溶聚合物的情況 下,可使用分子量調節劑(鏈轉移劑)。 可經由乳化劑之比例而影響調節粒子半徑的方式之一 。該比例愈高,尤其是在聚合作用開始時,所獲得之粒子 愈小。 在塗覆組成物製備之後或調配期間,分散液較佳係藉 由添加鹼來調整爲pH爲7至10。 爲製備本發明之水性分散液,可將上述乳化聚合物與 —或多種聚結劑混合。 乳化聚合物與至少一種聚結劑之混合較佳可在_ 1 0至 50 °C之範圍,更佳係在0至40 °C之範圍的溫度下發生。此 步驟可在聚合之後或只在調配成塗覆材料階段完成。 聚結劑及包含從烷基中具有至少一個雙鍵與8至40 個碳原子之(甲基)丙烯酸系單體所衍生之重複單元的(甲基 )丙烯酸系聚合物的重量分率可在廣泛範圍中,其通常可 應所需之性質槪要而調配。聚結劑對包含從烷基中具有至 少一個雙鍵與8至40個碳原子之(甲基)丙烯酸系單體所衍 生之重複單元的(甲基)丙烯酸系聚合物之重量比較佳在1 47- 201226480 :1至1: 100,更佳爲1:5至1:50,最佳】 30之範圍。 可將該等分散液用作塗覆材料。該等水性 體含量較佳在1 〇重量%至70重量%,更佳爲 60重量%之範圍。 爲製備本發明之塗覆材料,較佳可使用動育 至 1 0000 mPas,較佳爲 1 至 1 000 mPas,最佳 10 之範圍的聚合物分散液,該黏度係根據DIN EN 2 5 °C 下測量(Brookfield)。 除了水、聚結劑及上述包含從烷基中具有 鍵與8至40個碳原子之(甲基)丙烯酸系單體所 單元的(甲基)丙烯酸系聚合物之外,本發明之 根據本發明使用之水性分散液可包括添加劑或 料之性質適應特定需求的其他組分。該等額外 地包括助染劑,其被稱爲催乾劑,以及流動改 及染料。 本發明之塗覆材料不需要催乾劑,但可存 爲該等組成物之隨意成分。特佳係可添加催乾 分散液中。該等催乾劑更具體地包括有機金屬 實例爲過渡金屬(諸如鈷、錳、鉛及鍩)之金屬 或鹼土金屬,諸如鋰、鉀及鈣。可提及之實例 酸鈷及乙酸鈷。該等催乾劑可個別使用或作爲 ,在該情況中,尤佳者係包含鈷鹽、鍩鹽及鋰 :10 至 1 : 分散液的固 2 0重量%至 层黏度在〇. 1 至 500 mPas ISO 2555 在 至少一個雙 衍生之重複 塗覆材料或 使該塗覆材 物質更具體 良劑、顏料 在催乾劑作 劑至該水性 化合物,其 皂;鹼金屬 包括萘二甲 混合物使用 鹽之混合物 -48- 201226480 本發明之塗覆材料的最低成膜溫度較佳係不超過50 °C ,尤佳係不超過30°C,最佳係不超過20°C,該溫度可根據 DIN ISO 2 1 1 5 測量。 具有上述本發明聚結劑的水性分散液更明確地說可用 作塗覆材料或用作添加劑。此等材料更具體地包括漆及清 漆、浸漬組成物、黏著劑及/或底漆系統。特佳情況係該 等水性分散液可用於製造在木材及/或金屬上之應用的漆 、清漆或浸漬組成物。 可從本發明塗覆材料獲得之塗層展現出高溶劑抗性; 更明確地說,只有少部分因溶劑而從塗層溶解。較佳之塗 層展現出尤其是對於甲基異丁基酮(MIBK)之高度抗性。因 此,在以MIBK處理之後重量損失之量較佳係不超過50 重量%,更佳係不超過3 5重量%。MIBK之吸收量以所使 用之塗層之重量計較佳係不超過5 00重量%,更佳係不超 過3 00重量%。該等値係在約25 °C之溫度下在至少4小時 曝露時間期間測量,接受該測量的塗層爲完全乾燥之塗層 。乾燥作用係在例如氧、空氣之存在下發生,以使得能夠 交聯。 從本發明塗覆材料獲得之塗層顯示出高機械安定性。 垂擺硬度較佳爲至少2 5 s,較佳爲至少3 5 s,最佳爲至少 50 s,此係根據DIN ISO 1 522測量。 本發明之塗層展現出令人意外的良好機械性質。特別 重要的塗層之標稱斷裂伸長率較佳爲至少1 〇〇%,更佳爲 至少200%,此係根據DIN EN ISO 527第3部分測量。 -49- 201226480 此外,另外較佳之塗層顯示出根據DIN ΕΝ ISO 527 第3部分測量的抗張強度爲至少0.5 MPa,更佳爲至少2 Μ P a 〇 此外,令人意外的是本發明提出結合至少1 MPa,更 佳爲至少2 MPa之抗張強度與至少100%,更佳爲至少 200 %之斷裂伸長率的塗層。 此外,可從本發明塗覆材料獲得之較佳塗層記錄令人 意外之高黏著強度,更明確地說,其可根據橫切試驗測定 。因此,特別是根據標準DIN EN ISO 2409可獲得0至1 之分級,更佳爲〇。 以下茲參考發明實例及對照實例更詳細說明本發明, 且其不限制本發明。 ’ 【實施方式】 製備實例1 所使用之甲基丙烯醯氧基-2-乙基-脂肪酸醯胺混合物的製備 在配備有具攪拌套及攪拌馬達之刀式攪拌器、氮入口 、液相溫度計及蒸氣橋的四頸圓底燒瓶中裝入206·3 g( 0.70 mol)之脂肪酸甲酯混合物、42.8 g(0_70 mol)之乙醇胺 及0.27 g(0.26%)之LiOH。該脂肪酸甲酯混合物包含6重 量%之飽和C12至C16脂肪酸甲酯、2.5重量%之飽和C17 至C20脂肪酸甲酯、52重量%之單飽和C18脂肪酸甲酯、 1.5重量%之單飽和C20至C24脂肪酸甲酯、36重量%之 多飽和C18脂肪酸甲酯及2重量%之多飽和C20至c24脂 -50- 201226480 肪酸甲酯。 將該反應混合物加熱至1 5 0 °C。在2小時期間,藉由 蒸餾去除19.5 ml之甲醇。所得之反應產物含有86.5 %之 脂肪酸乙醇醯胺。獲得之反應混合物在未純化之情況下經 進一步加工。 冷卻之後,添加1919 g(19.2 mol)之甲基丙烯酸甲酯 、3_1 g之LiOH及由500 ppm之氫醌一甲基醚與500 ppm 之啡噻哄所組成之起始劑混合物。 在攪拌之下,以氮沖洗反應裝置10分鐘。然後,將 該反應混合物加熱至沸騰。將甲基丙烯酸甲酯/甲醇共沸 物分離,然後以數步驟將塔頂溫度升高至100°C。在反應 結束時,將該反應混合物冷卻至約70°c並過濾之。 在一旋轉蒸發器上分離過多的甲基丙烯酸甲酯。此產 生 37 0g 之產物(MUMA II)。 分散液(MMA-共聚-BA-MUMA II-MAS 64-20- 1 5 - 1 )之製備 首先,在一2 1 PE燒杯中,利用Ultra-Turrax以4000 rpm操作3分鐘,將280 g之丙烯酸丁酯(BA)、896 g之甲 基丙烯酸甲酯(MMA)、210 g之甲基丙烯醯氧基-2-乙基-脂 肪酸醯胺混合物、14 g之甲基丙烯酸(MAS)、4.2 g之過氧 二硫酸銨(APS)、42.0 g 之 Disponil FES 32(30%形式)及 1 202 g之水乳化。 在一具有水浴加熱設備並配備有翼式攪拌器的2 1玻 璃反應器中裝入8 3 0 g之水及1.05 g之Disponil FES 32( -51 - 201226480 30%形式),並將該起始進料力卩熱至80°C並與1.05 g之過 氧二硫酸銨(APS)於1 0 g水中之溶液混合。添加APS之後 5分鐘,在240分鐘期間計量加入前文所製備的乳液(間隔 :3分鐘進料,4分鐘暫停,237分鐘進料其餘部分)。 在進料結束之後,在80°C下攪拌該批料1小時。之後 ,將其冷卻至室溫及經由0.09 mm篩孔大小之VA網狀織 物過濾該分散液。 所製備之分散液的固體含量爲39.5%,PH爲5.9,黏 度爲1 1 mPas,rN5値爲91 nm,且最低成膜溫度爲52°C。 製備實例 2(MMA -共聚- BA-MUMA II-MAS 59-25-15-1) 基本上重複製備實例1,但使用包含350 g之丙烯酸 丁酯(BA)、826 g之甲基丙烯酸甲酯(MMA)、210 g之甲基 丙烯醯氧基-2-乙基-脂肪酸醯胺混合物及14 g之甲基丙烯 酸(MAS)的單體混合物。 所製備之分散液的固體含量爲39.7%,pH爲5.8,黏 度爲12·5 mPas,rN5値爲73 nm,且最低成膜溫度爲36.5 〇C。 製備實例 3(MMA-共聚-BA-MUMA I-MAS 64-20- 1 5- 1 ) 首先,在一2 1 PE燒杯中,利用Ultra-Turrax以4000 rpm操作3分鐘,將280 g之丙烯酸丁酯(BA)、896 g之甲 基丙烯酸甲酯(MMA)、210 g之甲基丙烯醯氧基-2-羥丙基-亞麻油酸酯、14g之甲基丙烯酸(MAS)、4.2 g之過氧二硫 -52- 201226480 酸銨(八?3)、42.0§之0丨8?〇11丨1?£8 32(30%形式)及 1202 § 之水乳化。該甲基丙烯醯氧基-2 -羥丙基·亞麻油酸酯係令 亞麻油酸與甲基丙烯酸環氧丙酯反應而獲得。 在一具有水浴加熱設備並配備有翼式攪拌器的2 1玻 璃反應器中裝入83 5 g之水及1.05 g之Disponil FES 32( 30%形式),並將該起始進料加熱至80°C並與1.05 g之過 氧二硫酸銨(APS)於10 g水中之溶液混合。添加APS之後 5分鐘,在240分鐘期間計量加入前文所製備的乳液(間隔 :3分鐘進料,4分鐘暫停,237分鐘進料其餘部分)。 在進料結束之後,在80 °C下攪拌該批料1小時。之後 ,將其冷卻至室溫及經由〇.〇9 mm篩孔大小之VA網狀織 物過濾該分散液。Vol. 1, after page 386, J. Wiley, New York, 1978. It is especially preferred in this aspect of the invention to use organic and/or inorganic initiators. Both of the starters can be used individually or as a mixture. These preferred amounts are from 0.05% by weight to 3.0% by weight based on the total weight of the monomers in the individual stages. It may also be preferred to carry out the polymerization using a mixture of different polymerization initiators having different half-lives to maintain the polymerization process and the free radical flow at different polymerization temperatures. The stabilization of the batch is preferably achieved by the use of an emulsifier and/or a protective colloid. The emulsion is preferably stabilized by an emulsifier to obtain a low dispersion viscosity. The total amount of the emulsifier is preferably from 0.1% by weight to 15% by weight, based on the total weight of the monomers used, especially from 1% by weight to 1% by weight, more preferably from 2% by weight to 5% by weight. According to one embodiment of the invention, a portion of the emulsifiers may be added during the polymerization. Particularly suitable emulsifiers are anionic or nonionic emulsifiers or mixtures thereof, more specifically an alkyl-sulfate, preferably an alkyl sulphate having from 8 to 18 carbon atoms in the alkyl group and from 8 to 8 in the alkyl group. 18 carbon atoms and alkyl ether sulfates having 1 to 50 ethylene oxide units and alkyl aryl sulfates; - sulfonate, preferably alkyl sulfonate having 8 to 18 carbon atoms in the alkyl group An acid ester, an alkyl aryl sulfonate having 8 to 18 carbon atoms in the alkyl group, an ester and a monoester of a sulfosuccinic acid having 4 to 15 carbon atoms in the alkyl group and a monohydric or alkyl phenol; Suitably, the alcohol or alkylphenol may also be ethoxylated via from 1 to 40 ethylene oxide units; - a partial ester of phosphoric acid and its alkali metal and ammonium salts, preferably an alkyl or alkyl aryl-44 - 201226480 An alkyl phosphate having from 8 to 20 carbon atoms and having from 1 to 5 ethylene oxide units and an alkyl aryl phosphate; - an alkyl polyglycol ether, preferably having from 8 to 20 in the alkyl group a carbon atom and having 8 to 40 ethylene oxide units; an alkylaryl polyglycol ether, preferably having 8 to 20 carbon atoms in the alkyl or alkylaryl group and having 8 to 40 ethylene oxide units; - an ethylene oxide/propylene oxide copolymer, preferably a block copolymer, preferably having from 8 to 40 ethylene oxide and/or propylene oxide units. More particularly preferred anionic emulsifiers include fatty acid ether sulfates, dioctyl sulfosuccinate, lauryl sulfate, C15-alkane sulfonates, possibly in the form of an alkali metal salt, especially a sodium salt. Compound. These compounds are commercially available, more specifically under the trademarks Disponil® FES 32, Aerosol® OT 75, Texapon® Κ 1 296 and Statexan® K1, available from Cognis GmbH, Cytec Industries, Inc. and Bayer AG. And other companies. Useful nonionic emulsifiers include tertiary octylphenol ethoxylates having 30 ethylene oxide units and preferably having 8 to 20 carbon atoms and having 8 to 40 ethylene oxide units in the alkyl group. Fatty alcohol polyglycol ether. These emulsifiers are commercially available under the trademarks Triton® X 305 (Fluka), Tergitol® 15-S-7 (Sigma-Aldrich Co.), Marlipal® 1618/25 (Sasol Germany) and Marlipal® 0 13 /400 (Sasol Germany). It is preferred to use a mixture of an anionic emulsifier and a nonionic emulsifier. The weight ratio of the anionic emulsifier to the nonionic emulsifier may range from 20:1 to 1:20, preferably from 2:1 to 1:10, more preferably from 1:1 to 1:5. -45- 201226480 It has proven to be particularly suitable mixtures comprising a sulphate (especially a fatty acid ether of sulphuric acid), a lauryl sulfate or a sulphonate (especially dioctyl sulfosuccinate) or an alkane sulfonate as an anionic emulsifier. And an alkylphenol ethoxylate or a fatty alcohol polyglycol ether (in each case preferably having 8 to 20 carbon atoms in the alkyl group and having 8 to 40 ethylene oxide units) as a nonionic emulsifier mixture. If appropriate, the emulsifiers may also be used as a mixture with a protective colloid. Suitable protective colloids include partially hydrolyzed polyvinyl acetate, polyvinylpyrrolidone, carboxymethylcellulose, methylcellulose, hydroxyethylcellulose and hydroxypropylcellulose, starch, protein, poly(methyl) Acrylic acid, poly(meth)acrylamide, polyvinylsulfonic acid, melamine-formaldehyde sulfonate, naphthalene-formaldehyde sulfonate, styrene-maleic acid and vinyl ether-maleic acid copolymerization Things. When a protective colloid is used, the amount of niobium is preferably from 1% by weight to 1.0% by weight based on the total of the monomers. These protective colloids may be included in the initial charge or metered in prior to the start of polymerization. The starter may be included in the initial charge or metered in. In addition, it is also possible that a portion of the initiator is included in the initial charge and the remainder is metered in. The polymerization is preferably carried out by heating the batch to the polymerization temperature and metering the addition of the starter, preferably in an aqueous solution. The metered addition of the emulsifier and monomer can be carried out separately or as a mixture, especially as an emulsion in water. In the case of metered addition of a mixture of emulsifier and monomer, the route employed is to emulsify or premix the emulsifier and monomer in water upstream of the mixer of the polymerization reactor. Preferably, a portion of the monomer (e.g., 1 to 10%) is first introduced to the reactor and the polymerization is initiated by the addition of the starting agent -46 - 201226480. The metering of the remaining monomers is preferably started after the start of the polymerization (e.g., 5 to 15 minutes after the start of the polymerization). Emulsified polymers which are preferably used and have a polymer having a high insoluble ratio can be obtained in the manner described above. It is known to obtain a reaction parameter having a high molecular weight. Therefore, more specifically, the use of a molecular weight regulator (chain transfer agent) may be omitted in this respect. In the case where the target is a low proportion of insoluble polymer, a molecular weight modifier (chain transfer agent) can be used. One of the ways to adjust the particle radius can be influenced by the ratio of the emulsifier. The higher the ratio, especially at the beginning of the polymerization, the smaller the particles obtained. The dispersion is preferably adjusted to have a pH of from 7 to 10 by the addition of a base after the preparation of the coating composition or during the formulation. To prepare the aqueous dispersion of the present invention, the above emulsion polymer may be mixed with - or a plurality of coalescents. The mixing of the emulsified polymer with at least one coalescent is preferably carried out at a temperature ranging from _10 to 50 °C, more preferably from 0 to 40 °C. This step can be done after the polymerization or only during the formulation into the coating material stage. a coalescent agent and a (meth)acrylic polymer comprising a repeating unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group may have a weight fraction In a wide range, it can usually be formulated in accordance with the desired properties. The coalescent agent preferably has a weight of a (meth)acrylic polymer comprising a repeating unit derived from a (meth)acrylic monomer having at least one double bond and 8 to 40 carbon atoms in the alkyl group. 47- 201226480: 1 to 1: 100, more preferably 1:5 to 1:50, the best 30 range. These dispersions can be used as a coating material. The water content is preferably in the range of from 1% by weight to 70% by weight, more preferably 60% by weight. For the preparation of the coating material of the invention, it is preferred to use a polymer dispersion which is incubated to a range of 1 0000 mPas, preferably 1 to 1 000 mPas, optimally 10, according to DIN EN 2 5 °C. Lower measurement (Brookfield). In addition to water, a coalescent, and the above (meth)acrylic polymer comprising a unit of a (meth)acrylic monomer having a bond from 8 to 40 carbon atoms in the alkyl group, the present invention is based on the present invention. The aqueous dispersions used in the invention may include other components of the nature of the additives or materials to suit particular needs. These additionally include a dye aid, which is referred to as a drier, and a flow modifying dye. The coating material of the present invention does not require a driers, but may be a random component of the compositions. The special system can be added to the wicking dispersion. These driers more specifically include metals or alkaline earth metals such as lithium, potassium and calcium in which the organometallic is exemplified by transition metals such as cobalt, manganese, lead and bismuth. Examples which may be mentioned are cobalt acid and cobalt acetate. These driers may be used individually or as a mixture. In this case, it is preferred to include a cobalt salt, a cerium salt and lithium: 10 to 1 : a solids of 20% by weight of the dispersion to a layer viscosity of 〇. 1 to 500 mPas ISO 2555 in at least one double-derived repetitive coating material or a more specific agent of the coating material, a pigment in a drier to the aqueous compound, a soap thereof; an alkali metal comprising a naphthalene dimethane mixture using a salt Mixture -48- 201226480 The minimum film forming temperature of the coating material of the present invention is preferably not more than 50 ° C, particularly preferably not more than 30 ° C, and the optimum is not more than 20 ° C, which can be according to DIN ISO 2 1 1 5 Measurement. The aqueous dispersion having the above-mentioned coalescent of the present invention is more specifically used as a coating material or as an additive. These materials more specifically include lacquers and varnishes, impregnating compositions, adhesives and/or primer systems. A particularly preferred condition is that the aqueous dispersions can be used in the manufacture of lacquers, varnishes or impregnating compositions for use on wood and/or metals. The coatings obtainable from the coating materials of the present invention exhibit high solvent resistance; more specifically, only a small portion is dissolved from the coating due to the solvent. Preferred coatings exhibit high resistance, especially for methyl isobutyl ketone (MIBK). Therefore, the amount of weight loss after treatment with MIBK is preferably not more than 50% by weight, more preferably not more than 5% by weight. The absorption of MIBK is preferably not more than 50,000% by weight, more preferably not more than 30,000% by weight, based on the weight of the coating used. The tantalum is measured at a temperature of about 25 ° C for at least 4 hours of exposure time, and the coating that accepts the measurement is a completely dry coating. The drying action takes place in the presence of, for example, oxygen or air to enable crosslinking. The coating obtained from the coating material of the present invention shows high mechanical stability. The pendulum hardness is preferably at least 2 5 s, preferably at least 3 5 s, most preferably at least 50 s, as measured according to DIN ISO 1 522. The coatings of the present invention exhibit surprisingly good mechanical properties. Particularly important coatings preferably have a nominal elongation at break of at least 1%, more preferably at least 200%, as measured according to DIN EN ISO 527 part 3. -49- 201226480 Furthermore, a further preferred coating exhibits a tensile strength measured according to DIN ΕΝ ISO 527 part 3 of at least 0.5 MPa, more preferably at least 2 Μ P a 〇 Furthermore, it is surprisingly proposed by the present invention A coating having a tensile strength of at least 1 MPa, more preferably at least 2 MPa and an elongation at break of at least 100%, more preferably at least 200%. Moreover, the preferred coatings obtainable from the coating materials of the present invention record surprisingly high adhesion strengths and, more specifically, can be determined according to cross-cutting tests. Therefore, in particular, according to the standard DIN EN ISO 2409, a classification of 0 to 1 can be obtained, more preferably 〇. The invention is described in more detail below with reference to the invention examples and comparative examples, and does not limit the invention. [Examples] Preparation of a mixture of methacryloxy-2-ethyl-fatty acid guanamine used in Preparation Example 1 was equipped with a knife stirrer equipped with a stirring sleeve and a stirring motor, a nitrogen inlet, and a liquid phase thermometer. A four-necked round bottom flask with a vapor bridge was charged with 206.3 g (0.70 mol) of a fatty acid methyl ester mixture, 42.8 g (0-70 mol) of ethanolamine, and 0.27 g (0.26%) of LiOH. The fatty acid methyl ester mixture comprises 6 wt% saturated C12 to C16 fatty acid methyl ester, 2.5% by weight saturated C17 to C20 fatty acid methyl ester, 52% by weight of monosaturated C18 fatty acid methyl ester, 1.5% by weight of monosaturated C20 to C24 Fatty acid methyl ester, 36% by weight of saturated C18 fatty acid methyl ester and 2% by weight of saturated C20 to c24 lipid -50-201226480 fatty acid methyl ester. The reaction mixture was heated to 150 °C. 19.5 ml of methanol was removed by distillation over a period of 2 hours. The resulting reaction product contained 86.5 % of fatty acid ethanolamine. The reaction mixture obtained was further processed without purification. After cooling, 1919 g (19.2 mol) of methyl methacrylate, 3_1 g of LiOH, and a starter mixture consisting of 500 ppm of hydroquinone monomethyl ether and 500 ppm of morphiathene were added. The reaction apparatus was flushed with nitrogen for 10 minutes with stirring. The reaction mixture is then heated to boiling. The methyl methacrylate/methanol azeotrope was separated and the temperature at the top of the column was raised to 100 ° C in several steps. At the end of the reaction, the reaction mixture was cooled to about 70 ° C and filtered. Excess methyl methacrylate was separated on a rotary evaporator. This produced 37 0 g of product (MUMA II). Preparation of Dispersion (MMA-Copolymer-BA-MUMA II-MAS 64-20- 1 5 - 1 ) First, 280 g of acrylic acid was operated in a 2 1 PE beaker using an Ultra-Turrax at 4000 rpm for 3 minutes. Butyl ester (BA), 896 g of methyl methacrylate (MMA), 210 g of methacryloxy-2-ethyl-fatty acid decylamine mixture, 14 g of methacrylic acid (MAS), 4.2 g Ammonium peroxydisulfate (APS), 42.0 g of Disponil FES 32 (30% form) and 1 202 g of water were emulsified. In a 21 glass reactor equipped with a water bath heating device and equipped with a wing agitator, 830 g of water and 1.05 g of Disponil FES 32 (-51 - 201226480 30% form) were charged and the starting The feed was heated to 80 ° C and mixed with 1.05 g of a solution of ammonium peroxodisulphate (APS) in 10 g of water. Five minutes after the addition of APS, the emulsion prepared previously was metered in over 240 minutes (interval: 3 minutes feed, 4 minute pause, 237 minutes feed the remainder). After the end of the feed, the batch was stirred at 80 ° C for 1 hour. Thereafter, it was cooled to room temperature and the dispersion was filtered through a VA mesh fabric having a mesh size of 0.09 mm. The prepared dispersion had a solid content of 39.5%, a pH of 5.9, a viscosity of 11 mPas, a rN5値 of 91 nm, and a minimum film formation temperature of 52 °C. Preparation Example 2 (MMA - Co-BAT-MUMA II-MAS 59-25-15-1) Preparation Example 1 was substantially repeated, but using 350 g of butyl acrylate (BA), 826 g of methyl methacrylate (MMA), 210 g of a mixture of methacryloxy-2-ethyl-fatty acid decylamine and 14 g of a monomer mixture of methacrylic acid (MAS). The prepared dispersion had a solid content of 39.7%, a pH of 5.8, a viscosity of 12·5 mPas, a rN5値 of 73 nm, and a minimum film formation temperature of 36.5 〇C. Preparation Example 3 (MMA-Copolymer-BA-MUMA I-MAS 64-20- 1 5- 1 ) First, in a 2 1 PE beaker, using Ultra-Turrax at 4000 rpm for 3 minutes, 280 g of butyl acrylate Ester (BA), 896 g of methyl methacrylate (MMA), 210 g of methacryloxy-2-hydroxypropyl-linoleate, 14 g of methacrylic acid (MAS), 4.2 g Peroxydisulfide-52-201226480 Ammonium sulphate (8-3), 42.0 § 0丨8?〇11丨1?£8 32 (30% form) and 1202 § water emulsification. The methacryloxy-2-hydroxypropyl·linoleic acid ester is obtained by reacting linoleic acid with glycidyl methacrylate. In a 21 glass reactor equipped with a water bath heating device and equipped with a wing agitator, 83 5 g of water and 1.05 g of Disponil FES 32 (30% form) were charged and the initial charge was heated to 80. °C and mixed with 1.05 g of a solution of ammonium peroxodisulphate (APS) in 10 g of water. Five minutes after the addition of APS, the emulsion prepared previously was metered in over 240 minutes (interval: 3 minutes feed, 4 minute pause, 237 minutes feed the remainder). After the end of the feed, the batch was stirred at 80 ° C for 1 hour. Thereafter, it was cooled to room temperature and the dispersion was filtered through a VA mesh fabric having a mesh size of 〇.
所製備之分散液的固體含量爲39.8%,pH爲2.5,黏 度爲14 mPas,rN5値爲71 nm,且最低成膜溫度爲44.0°C 製備實例 4(MMA-共聚-BA-MUMA I-MAS 5 9-2 5 - 1 5 - 1 ) 基本上重複製備實例3’但使用包含350 g之丙烯酸 丁酯(BA)、826 g之甲基丙烯酸甲酯(MMA)、210 g之甲基 丙烯醯氧基-2-羥丙基-亞麻油酸酯及14 g之甲基丙烯酸 (MAS)的單體混合物。 所製備之分散液的固體含量爲39·8% ’ pH爲2.3,黏 度爲13.5 mPas,ΓΝ5値爲74 nm,且最低成膜溫度爲34.5 -53- 201226480 製備實例 5(MMA-共聚-BA-MUMA I-MAS 64-20- 1 5 - 1 ) 首先,在一2 1 PE燒杯中,利用Ultra-Turrax以4000 rpm操作3分鐘,將80 g之丙嫌酸丁酯(BA)、273.9 g之 甲基丙烯酸甲酯(MMA)、70.9 g之甲基丙烯醯氧基-2-乙 基-脂肪酸醯胺混合物4.28 g之甲基丙烯酸(MAS)、1.2 g 之過氧二硫酸敍(APS)、12.0 g 之 Disponil FES 32(30°/。形 式)及3 75.5 g之水乳化。該甲基丙烯醯氧基-2-羥丙基-亞 麻油酸酯係令亞麻油酸與甲基丙烯酸環氧丙酯反應而獲得 〇 在一具有水浴加熱設備並配備有翼式攪拌器的2 1玻 璃反應器中裝入23 0 g之水及0.3 g之Disponil FES 32( 30%形式),並將該起始進料力口熱至80°C並與0.3 g之過氧 二硫酸銨(APS)於10 g水中之溶液混合。添加APS之後5 分鐘,在240分鐘期間計量加入前文所製備的乳液(間隔 :3分鐘進料,4分鐘暫停,237分鐘進料其餘部分)。 在進料結束之後,在80°C下攪拌該批料1小時。之後 ,將其冷卻至室溫及經由0.09 mm篩孔大小之VA網狀織 物過濾該分散液。 所製備之分散液的固體含量爲38.5%,pH爲2.5,黏 度爲14 mPas,rN5値爲59 nm,且最低成膜溫度爲41°C。 從前文所述之分散液,藉由添加聚結劑製備本發明之 塗覆材料。此尤其是使用2,7-辛二烯醇及2,7-辛二烯醇*5 PO(莫耳質量416 g/mol)完成。因此,特別進行降低最低 -54- 201226480 成膜溫度之探討,獲得該塗覆材料的化學安定性及機械性 質0 實施例1至14 藉由添加2,7-辛二烯醇來降低最低成膜溫度 將製備實例1及3中所述之分散液與不同量之2,7-辛 二烯-1-醇混合,並測量最低成膜溫度(MFT)之降低。所獲 得之數據及所使用之2,7-辛二烯醇的量係示於表1及2 ^ 該等數値與個別組分之重量相關,分散液之數量係基於固 體含量計。 表1 : i,7-辛二烯醇 Γ%1 得自製備實例1之分散液 [基於固體含量計之%] MFT rci 0 100 52 實施例1 2 98 46.5 實施例2 4 96 34.5 實施例3 6 94 25.5 實施例4 8 92 17 實施例5 12 88 <0 實施例6 16 84 <0 實施例7 20 80 <0 -55- 201226480 表2 : 2,7·辛二烯醇 ί%1 得自製備實例3之分散液 [基於固體含量計之%] MFT r°ci 0 100 44 實施例8 2 98 34 實施例9 4 96 23.7 實施例10 6 94 21.5 實施例11 8 92 <0 實施例12 12 88 <0 實施例13 16 84 <0 . 實施例14 20 80 <0 實施例1 5至1 9 藉由添加2,7-辛二烯醇*5 PO來降低最低成膜溫度 將製備實例3中所述之分散液與不同量之2,7-辛二烯 醇*5 PO混合,並測量最低成膜溫度(MFT)之降低。所獲 得之數據及所使用之2,7-辛二烯醇*5 PO的量係示於表3 。該等數値與個別組分之重量相關,分散液之數量係基於 固體含量計。 表3 : 2,7-辛二烯醇*5 PO 得自製備實例3之分散液 MFT Γ%1 [基於固體含量計之%] [°C1 0 100 44 實施例15 4 96 30 實施例16 8.3 91.7 19 實施例17 12.8 87.2 15 實施例18 16.4 83.6 <0 實施例19 20.3 79.7 <0 -56- 201226480 實施例2 0至2 2 藉由添加丙二酸二烯丙酯來降低最低成膜溫度 將製備實例5中所述之分散液與不同量之丙二酸二烯 丙酯混合,並測量最低成膜溫度(MFT)之降低。所獲得之 數據及所使用之丙二酸二烯丙酯的量係示於表4。該等數 値與個別組分之重量相關,分散液之數量係基於固體含量 計。 表4 : 丙二酸二烯丙酯 ί%1 得自製備實例5之分散液 [基於固體含量計之%] MFT rci 0 100 41 實施例20 2 98 19 實施例21 4 96 9 實施例22 5 95 0 實施例23至25 藉由添加檸檬酸三烯丙酯來降低最低成膜溫度 將製備實例5中所述之分散液與不同量之檸檬酸三烯 丙酯混合,並測量最低成膜溫度(MFT)之降低。‘所獲得之 數據及所使用之檸檬酸三烯丙酯的量係示於表5。該等數 値與個別組分之重量相關,分散液之數量係基於固體含量 計。 ’ -57- 201226480 表5 : 檸檬酸三烯丙酯 得自製備實例5之分散液 MFT r%i [基於固體含量計之%] rci 0 100 41 實施例23 2 98 27 實施例24 4 96 19 實施例25 5 95 15 實施例26至28 藉由添加三(甲基)丙烯酸三羥甲基丙烷酯(TMPTMA)來降 低最低成膜溫度 將製備實例5中所述之分散液與不同量之三(甲基)丙 烯酸三羥甲基丙烷酯(TMPTMA)混合,並測量最低成膜溫 度(MFT)之降低。所獲得之數據及所使用之TMPTMA的量 係示於表6。該等數値與個別組分之重量相關,分散液之 數量係基於固體含量計。 表6 : TMPTMA 得自製備實例5之分散液 MFT f%1 [基於固體含量計之%1 rci 0 100 41 實施例26 2 98 27 實施例27 4 96 27 實施例28 5 95 25 性質探討 使用不同方法探討所得之塗覆材料的性質。爲此目的 ,在乾燥之膜上進行溶劑抗性、吸水性及硬度之試驗。 -58- 201226480 使用甲基異丁基酮(mibk)測定溶劑抗性,其中樣本係 在室溫下經MIBK膨潤4小時。然後從該溶劑取出該樣本 ,去除過量之溶劑。 接著在約1 4 0 °c下乾燥該樣本1小時。表7中所示之 値與經MIBK處理後之塗層的重量有關,本文中亦稱爲「 真實膨潤」。 塗層之硬度(通常代表耐刮性之測量標準)係藉由 Kiinig 垂擺試驗(DIN ISO 1 522)探討。 實施例29至34 將製備實例2中所述之分散液與不同量之2,7-辛二烯 醇*5-P〇(〇CP)與催乾劑(環烷酸鈷(Fluka))混合。表7中以 重量百分比表示之數値與分散液之固體含量有關。在探討 溶劑抗性之前,乾燥塗層1 〇天。在不同乾燥時間之後測 量垂擺硬度。 表7(溶劑抗' 性) OCP [重量%] 催乾劑 [重量%] 真實膨潤 Γ%1 溶劑吸收率 r%i 質量損失 r%i 實施例29 10 0 446 326 22 實施例30 10 0.75 343 251 21 實施例31 10 1.5 308 227 20 實施例32 14 0 426 307 23 實施例33 14 0.75 352 245 24 實施例34 14 1.5 325 227 23 -59- 201226480 表7(垂擺硬度) OCM [重量%] 催乾劑 [重量%] 樣本乾燥之後的垂擺硬度 7天 isl 13天 rsi 36天 「si 實施例29 10 0 38 36 46 實施例30 10 0.75 43 45 55 實施例31 10 1.5 43 43 57 實施例32 14 0 22 21 29 實施例33 14 0.75 32 32 48 實施例34 14 1.5 32 34 45 實施例3 5至3 7 將製備實例2中所述之分散液與不同量之甲氧基辛-2,7-二烯(辛- 2,7-二烯基甲基醚)(OCM)及催乾劑(環烷酸鈷 (Fluka))混合。表8中以重量百分比表示之數値與分散液 之固體含量有關。在探討溶劑抗性之前,乾燥塗層1 〇天 。在不同乾燥時間之後測量垂擺硬度。 表8 (溶劑抗' 生) OCM [重量%] 催乾劑 [重量%] 真實膨潤 ί%1 溶劑吸收率 質量損失 [%1 實施例35 20 0 555 425 20 實施例36 20 0.75 340 263 17 實施例37 20 1.5 316 239 19 表8(垂擺硬度) OCM [重量%] 催乾劑 [重量%] 樣本乾燥之後的垂彳 罷硬度 7天 Tsl 13天 rsl 30天 rsi 實施例35 20 0 67 74 83 實施例36 20 0.75 83 78 73 實施例37 20 1.5 57 63 63 -60- 201226480 實施例38至40 將製備實例2中所述之分散液與不同量之辛-2,7-二烯 醇(OCL)與催乾劑(環烷酸鈷(Fluka))混合。表9中以重量 百分比表示之數値與分散液之固體含量有關。在探討溶劑 抗性之前,乾燥塗層1 〇天。在不同乾燥時間之後測量垂 擺硬度。 表9(溶劑抗性) OCL [重量%] 催乾劑 [重量%] 真實膨潤 Γ%1 溶劑吸收率 r%i 質量損失 Γ%1 實施例38 10 0 501 380 20 實施例39 10 0.75 344 265 18 實施例40 10 1.5 321 256 15 表9(垂擺硬度) OCL [重量%] 催乾劑 [重量%] 樣本乾燥夕徬的粜彳 擺硬度 7天 rsi 16天 _ rsi 23天 Μ 實施例38 10 0 62 64 95 實施例39 10 0.75 59 94 109 實施例40 10 1.5 59 90 101 實施例4 1至4 3 將製備實例4中所述之分散液與不同量之2,7_辛二稀 醇*5-P0(0CP)與催乾劑(環烷酸鈷(Fluka))混合。表10中 以重量百分比表示之數値與分散液之固體含量有關。在探 討溶劑抗性之前,乾燥塗層10天。 -61 - 201226480 表10 : OCM [雷量%] 催乾劑 [重量%] 真實膨潤 Γ%1 溶劑吸收率 ί%1 質量損失 ί%1 實施例41 8 0 571 416 23 實施例42 8 0.75 574 411 24 實施例43 8 1.5 548 391 23 實施例44至46 將製備實例4中所述之分散液與不同量之甲氧基-2,7-二烯(辛-2,7-二烯基甲基醚)(0 CM)及催乾劑(環烷酸鈷 (Fluka))混合。表11中以重量百分比表示之數値與分散液 之固體含量有關。在探討溶劑抗性之前,乾燥塗層1〇天 表1 1 : OCM [重量%] 催乾劑 [重量%] 真實膨潤 Γ%1 溶劑吸收率 Γ%1 質量損失 Γ%1 實施例44 20 0 610 455 22 實施例45 20 0.75 584 426 23 實施例46 20 1.5 555 408 22 實施例4 7至4 9 將製備實例2中所述之分散液與不同量之辛-2,7-二烯 醇(OCL)與催乾劑(環烷酸鈷(Fluka))混合。表12中以重量 百分比表示之數値與分散液之固體含量有關。在探討溶劑 抗性之前,乾燥塗層1 〇天。 -62- 201226480 表12 : OCL [重量%1 催乾劑 [重量%] 真實膨潤 r%i 溶劑吸收率 r%i 質量損失 Γ%1 實施例47 8 0 858 573 30 實施例48 8 0.75 557 411 22 實施例49 8 1.5 526 394 21 實施例5 0至5 2 將製備實例1中所述之分散液與不同量之2,7_辛二烯 醇*5-P0(0CP)與催乾劑(環烷酸鈷(Fluka))混合。表13中 以重量百分比表示之數値與分散液之固體含量有關。在不 同塗層乾燥時間之後測量垂擺硬度。 表13(垂擺硬度) OCP [重量%] 催乾劑 [重量%] 樣本乾燥之後的垂1 铺硬度 7天 rsl 15天 「si 29天 [s] _ 實施例50 8 0 41 53 57 實施例51 8 0.75 43 50 49 實施例52 8 1.5 42 49 50 實施例5 3至5 5 將製備實例1中所述之分散液與不同量之甲氧基辛-2,7-二烯(辛-2,7-二烯基甲基醚)(〇CM)及催乾劑(環烷酸鈷 (Fluka))混合。表14中以重量百分比表示之數値與分散液 之固體含量有關。在不同塗層乾燥時間之後測量垂擺硬度 -63- 201226480 表14(垂擺硬度) OCM [重量%] 催乾劑 [重量%] 樣本乾燥之後的垂3 罷硬度 7天 『si 10天 rsi 29天 rsi 實施例53 20 0 73 81 92 實施例54 20 0.75 62 66 66 實施例55 20 1.5 70 63 66 實施例5 6至5 8 將製備實例1中所述之分散液與不同量之辛-2,7-二烯 醇(OCL)與催乾劑(環烷酸鈷(Fluka))混合。表15中以重量 百分比表示之數値與分散液之固體含量有關。在不同塗層 乾燥時間之後測量垂擺硬度。 表15(垂擺硬度) OCL [重量%] 催乾劑 [重量〇/〇] 樣本乾燥之後的垂彳 罷硬度 4天 isl 14天 isl 23天 [si 實施例56 8 0 41 52 78 實施例57 8 0.75 38 73 90 實施例58 8 1.5 42 73 90 實施例5 9至6 1 將製備實例5中所述之分散液與5重量%之表16中所 表示的聚結劑及1.5重量%之催乾劑(Nuodex®)混合,以重 量百分比表示之數値係基於分散液之固體含量計。垂擺硬 度係在塗層經乾燥不同時間之後測量。 -64 - 201226480 表16(垂擺硬度) 樣本乾燥之後的垂措 i硬度 1天 7天 21天 Tsl 『si Tsl 實施例59 丙二酸二烯丙酯 61.6 71.4 96.6 實施例60 檸檬酸三烯丙酯 42.0 46.2 47.6 實施例61 TMPTMA 61.6 58.3 85.4 -65-The prepared dispersion had a solid content of 39.8%, a pH of 2.5, a viscosity of 14 mPas, a rN5値 of 71 nm, and a minimum film formation temperature of 44.0 ° C. Preparation Example 4 (MMA-co-polymer-BA-MUMA I-MAS 5 9-2 5 - 1 5 - 1 ) Preparation of Example 3' was substantially repeated but using 350 g of butyl acrylate (BA), 826 g of methyl methacrylate (MMA), 210 g of methacryl oxime A monomer mixture of oxy-2-hydroxypropyl-linolenic acid ester and 14 g of methacrylic acid (MAS). The prepared dispersion had a solid content of 39.8% 'pH of 2.3, viscosity of 13.5 mPas, ΓΝ5値 of 74 nm, and minimum film formation temperature of 34.5-53-201226480. Preparation Example 5 (MMA-co--BA- MUMA I-MAS 64-20- 1 5 - 1 ) First, in an 2 1 PE beaker, operate at 4000 rpm for 3 minutes using an Ultra-Turrax, 80 g of butyl citrate (BA), 273.9 g Methyl methacrylate (MMA), 70.9 g of methacryloxy-2-ethyl-fatty acid decylamine mixture 4.28 g of methacrylic acid (MAS), 1.2 g of peroxydisulfate (APS), 12.0 g of Disponil FES 32 (30°/. format) and 3 75.5 g of water are emulsified. The methacryloxy-2-hydroxypropyl-linolenic acid ester reacts linoleic acid with glycidyl methacrylate to obtain hydrazine in a water bath heating device equipped with a wing agitator 2 1 Glass reactor was charged with 23 0 g of water and 0.3 g of Disponil FES 32 (30% form), and the initial feed force was heated to 80 ° C with 0.3 g of ammonium peroxodisulfate ( APS) is mixed in 10 g of water. Five minutes after the addition of APS, the emulsion prepared previously was metered in over 240 minutes (interval: 3 minutes feed, 4 minute pause, 237 minutes feed the remainder). After the end of the feed, the batch was stirred at 80 ° C for 1 hour. Thereafter, it was cooled to room temperature and the dispersion was filtered through a VA mesh fabric having a mesh size of 0.09 mm. The prepared dispersion had a solid content of 38.5%, a pH of 2.5, a viscosity of 14 mPas, a rN5値 of 59 nm, and a minimum film forming temperature of 41 °C. The coating material of the present invention is prepared from the dispersion described above by adding a coalescent. This is done in particular using 2,7-octadienol and 2,7-octadienol*5 PO (mole mass 416 g/mol). Therefore, in particular, the investigation of the film formation temperature of the lowest -54 - 201226480 was carried out to obtain the chemical stability and mechanical properties of the coating material. 0 Examples 1 to 14 The minimum film formation was reduced by adding 2,7-octadienol. Temperature The dispersions described in Preparation Examples 1 and 3 were mixed with varying amounts of 2,7-octadien-1-ol and the minimum film formation temperature (MFT) reduction was measured. The data obtained and the amount of 2,7-octadienol used are shown in Tables 1 and 2. The numbers are related to the weight of the individual components, and the amount of the dispersion is based on the solid content. Table 1: i,7-octadienol oxime %1 From the dispersion of Preparation Example 1 [% based on solid content] MFT rci 0 100 52 Example 1 2 98 46.5 Example 2 4 96 34.5 Example 3 6 94 25.5 Example 4 8 92 17 Example 5 12 88 <0 Example 6 16 84 <0 Example 7 20 80 <0 -55-201226480 Table 2: 2,7·octadienol 1 Dispersion from Preparation Example 3 [% based on solid content] MFT r°ci 0 100 44 Example 8 2 98 34 Example 9 4 96 23.7 Example 10 6 94 21.5 Example 11 8 92 <0 Example 12 12 88 <0 Example 13 16 84 <0. Example 14 20 80 <0 Example 1 5 to 19 Reduce the minimum by adding 2,7-octadienol*5 PO Film Temperature The dispersion described in Preparation Example 3 was mixed with varying amounts of 2,7-octadienol*5 PO and the minimum film formation temperature (MFT) reduction was measured. The data obtained and the amount of 2,7-octadienol*5 PO used are shown in Table 3. The numbers are related to the weight of the individual components and the amount of dispersion is based on the solids content. Table 3: 2,7-octadienol*5 PO From the dispersion of Preparation Example 3 MFT Γ%1 [% based on solid content] [°C1 0 100 44 Example 15 4 96 30 Example 16 8.3 91.7 19 Example 17 12.8 87.2 15 Example 18 16.4 83.6 <0 Example 19 20.3 79.7 <0-56-201226480 Example 2 0 to 2 2 Reduce the minimum film formation by adding diallyl malonate Temperature The dispersion described in Preparation Example 5 was mixed with different amounts of diallyl malonate and the minimum film formation temperature (MFT) was measured. The data obtained and the amount of diallyl malonate used are shown in Table 4. These numbers are related to the weight of the individual components and the amount of dispersion is based on the solids content. Table 4: Diallyl malonate %%1 The dispersion obtained from Preparation Example 5 [% based on solid content] MFT rci 0 100 41 Example 20 2 98 19 Example 21 4 96 9 Example 22 5 95 0 Examples 23 to 25 The dispersion described in Preparation Example 5 was mixed with different amounts of triallyl citrate by adding triallyl citrate to reduce the minimum film formation temperature, and the minimum film formation temperature was measured. (MFT) reduction. The data obtained and the amount of triallyl citrate used are shown in Table 5. These numbers are related to the weight of the individual components and the amount of dispersion is based on the solids content. '-57- 201226480 Table 5: Triallyl citrate was obtained from the dispersion of Preparation Example 5 MFT r%i [% based on solid content] rci 0 100 41 Example 23 2 98 27 Example 24 4 96 19 Example 25 5 95 15 Examples 26 to 28 The dispersion described in Example 5 was prepared with the same amount by adding trimethylolpropane tris(meth)acrylate (TMPTMA) to lower the minimum film formation temperature. Trimethylolpropane (meth)acrylate (TMPTMA) was mixed and the minimum film formation temperature (MFT) was measured. The data obtained and the amount of TMPTMA used are shown in Table 6. The numbers are related to the weight of the individual components and the amount of dispersion is based on the solids content. Table 6: TMPTMA Dispersion MFT from Preparation Example 5 M% f%1 [%1 based on solid content rci 0 100 41 Example 26 2 98 27 Example 27 4 96 27 Example 28 5 95 25 Discussion of properties Methods The properties of the resulting coating materials were investigated. For this purpose, tests for solvent resistance, water absorption and hardness were carried out on the dried film. -58- 201226480 Solvent resistance was determined using methyl isobutyl ketone (mibk), wherein the samples were swollen by MIBK for 4 hours at room temperature. The sample is then removed from the solvent to remove excess solvent. The sample was then dried at about 140 ° C for 1 hour. The enthalpy shown in Table 7 is related to the weight of the MIBK-treated coating, which is also referred to herein as "true swell." The hardness of the coating (usually the measure of scratch resistance) is explored by the Kiinig pendulum test (DIN ISO 1 522). Examples 29 to 34 The dispersion described in Preparation Example 2 was mixed with different amounts of 2,7-octadienol*5-P〇(〇CP) and a drier (cobalt naphthenate (Fluka)). . The number 値 expressed as a percentage by weight in Table 7 is related to the solid content of the dispersion. Dry the coating for 1 day before discussing solvent resistance. The pendulum hardness was measured after different drying times. Table 7 (solvent resistance) OCP [% by weight] Drier [% by weight] true swelling Γ%1 Solvent absorption rate r%i Mass loss r%i Example 29 10 0 446 326 22 Example 30 10 0.75 343 251 21 Example 31 10 1.5 308 227 20 Example 32 14 0 426 307 23 Example 33 14 0.75 352 245 24 Example 34 14 1.5 325 227 23 -59- 201226480 Table 7 (pendulum hardness) OCM [% by weight] Drier [% by weight] The pendulum hardness after drying of the sample 7 days isl 13 days rsi 36 days "si Example 29 10 0 38 36 46 Example 30 10 0.75 43 45 55 Example 31 10 1.5 43 43 57 Example 32 14 0 22 21 29 Example 33 14 0.75 32 32 48 Example 34 14 1.5 32 34 45 Example 3 5 to 3 7 The dispersion described in Preparation Example 2 was treated with different amounts of methoxyoctane-2, 7-diene (octyl-2,7-dienylmethyl ether) (OCM) and driers (cobalt naphthenate (Fluka)) are mixed. The number of ruthenium and dispersion in Table 8 is expressed by weight. The solids content is related. The coating is dried for 1 day before the solvent resistance is investigated. The pendulum hardness is measured after different drying times. Table 8 (solvent anti-'s) O CM [% by weight] Drier [% by weight] true swelling %%1 Solvent absorption rate mass loss [%1 Example 35 20 0 555 425 20 Example 36 20 0.75 340 263 17 Example 37 20 1.5 316 239 19 Table 8 (pendulum hardness) OCM [% by weight] Drier [% by weight] Coveted hardness after drying of the sample 7 days Tsl 13 days rsl 30 days rsi Example 35 20 0 67 74 83 Example 36 20 0.75 83 78 73 Example 37 20 1.5 57 63 63 -60- 201226480 Examples 38 to 40 The dispersion described in Preparation Example 2 was prepared with different amounts of octane-2,7-dienol (OCL) and drier (ring Cobalt alkoxide (Fluka) was mixed. The number in liters expressed in Table 9 is related to the solids content of the dispersion. The coating was dried for 1 day before the solvent resistance was investigated. The pendulum hardness was measured after different drying times. Table 9 (solvent resistance) OCL [% by weight] driers [% by weight] true swell Γ%1 solvent absorption rate r%i mass loss Γ%1 Example 38 10 0 501 380 20 Example 39 10 0.75 344 265 18 Example 40 10 1.5 321 256 15 Table 9 (pendulum hardness) OCL [% by weight] Drier [% by weight] Drying 彷 粜彳 pendulum hardness 7 days rsi 16 days _ rsi 23 days 实施 Example 38 10 0 62 64 95 Example 39 10 0.75 59 94 109 Example 40 10 1.5 59 90 101 Example 4 1 to 4 3 The dispersion described in Preparation Example 4 was mixed with different amounts of 2,7-octanediamine*5-P0 (0CP) and a drier (cobalt naphthenate (Fluka)). The number 値 expressed in weight percent in Table 10 is related to the solids content of the dispersion. The coating was dried for 10 days before solvent resistance was explored. -61 - 201226480 Table 10: OCM [Ray %] Drier [% by weight] Real swelling Γ%1 Solvent absorption rate %%1 Mass loss ί%1 Example 41 8 0 571 416 23 Example 42 8 0.75 574 411 24 Example 43 8 1.5 548 391 23 Examples 44 to 46 The dispersion described in Preparation Example 4 was prepared with different amounts of methoxy-2,7-diene (octyl-2,7-dienyl) (ether) (0 CM) and a drier (cobalt naphthenate (Fluka)). The number 値 expressed in weight percent in Table 11 is related to the solid content of the dispersion. Before investigating solvent resistance, dry coating 1 〇1 1 : OCM [% by weight] driers [% by weight] true swell Γ%1 solvent absorption Γ%1 mass loss Γ%1 Example 44 20 0 610 455 22 Example 45 20 0.75 584 426 23 Example 46 20 1.5 555 408 22 Example 4 7 to 4 9 The dispersion described in Preparation Example 2 was prepared with different amounts of octa-2,7-dienol ( OCL) is mixed with a drier (Fluka naphthenate). The number 値 expressed as a percentage by weight in Table 12 is related to the solid content of the dispersion. The coating was dried for 1 day before the solvent resistance was investigated. -62- 201226480 Table 12: OCL [% by weight 1 driers [% by weight] true swell r%i solvent absorption rate r%i mass loss Γ %1 Example 47 8 0 858 573 30 Example 48 8 0.75 557 411 22 Example 49 8 1.5 526 394 21 Example 5 0 to 5 2 The dispersion described in Preparation Example 1 was treated with different amounts of 2,7-octadienol*5-P0 (0CP) and a drier ( Cobalt naphthenate (Fluka) is mixed. The number 値 expressed as a percentage by weight in Table 13 is related to the solid content of the dispersion. The pendulum hardness was measured after different coating drying times. Table 13 (pendulum hardness) OCP [% by weight] Drier [% by weight] Drop 1 after drying of the sample 7 days rsl 15 days "si 29 days [s] _ Example 50 8 0 41 53 57 Example 51 8 0.75 43 50 49 Example 52 8 1.5 42 49 50 Example 5 3 to 5 5 The dispersion described in Preparation Example 1 was treated with different amounts of methoxyoctane-2,7-diene (xin-2). , 7-dienyl methyl ether) (〇CM) and a drier (cobalt naphthenate (Fluka)). The number in liters expressed in Table 14 is related to the solid content of the dispersion. Measurement of pendulum hardness after layer drying time -63- 201226480 Table 14 (pendulum hardness) OCM [% by weight] Drier [% by weight] Dangling after sample drying 3 Hardness 7 days "si 10 days rsi 29 days rsi implementation Example 53 20 0 73 81 92 Example 54 20 0.75 62 66 66 Example 55 20 1.5 70 63 66 Example 5 6 to 5 8 The dispersion described in Preparation Example 1 was treated with different amounts of xin-2,7- The dienol (OCL) is mixed with a drier (Fluka). The number in liters expressed in Table 15 is related to the solids content of the dispersion. Then measure the pendulum hardness. Table 15 (pendulum hardness) OCL [% by weight] Drier [weight 〇 / 〇] The coveted hardness after drying of the sample 4 days isl 14 days isl 23 days [si Example 56 8 0 41 52 78 Example 57 8 0.75 38 73 90 Example 58 8 1.5 42 73 90 Example 5 9 to 6 1 The dispersion described in Preparation Example 5 and 5 % by weight of the coalescent represented by Table 16 And 1.5% by weight of driers (Nuodex®) are mixed and expressed in weight percent based on the solid content of the dispersion. The pendulum hardness is measured after the coating has been dried for different time. -64 - 201226480 Table 16 (Pitch hardness) Dip after the sample was dried i Hardness 1 day 7 days 21 days Tsl "si Tsl Example 59 Diallyl malonate 61.6 71.4 96.6 Example 60 Triallyl citrate 42.0 46.2 47.6 Example 61 TMPTMA 61.6 58.3 85.4 -65-
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DE2129425C3 (en) | 1971-06-14 | 1975-05-22 | Chemische Werke Huels Ag, 4370 Marl | Process for the production of fatty acid ethanolamides |
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AT337850B (en) | 1975-11-26 | 1977-07-25 | Vianova Kunstharz Ag | PROCESS FOR THE PRODUCTION OF OXIDATIVE DRYING AQUATIC POLYMERISATE DISPERSIONS |
DE3423443A1 (en) | 1984-06-26 | 1986-01-02 | Röhm GmbH, 6100 Darmstadt | METHOD FOR THE PRODUCTION OF ESTERS OF ACRYLIC AND METHACRYLIC ACID BY TRANSESTERATION |
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DE4141190A1 (en) | 1991-12-13 | 1993-06-17 | Bayer Ag | USE OF OCTADIENYL ETHERS AS A REACTIVE REDUCER |
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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 |
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US6177510B1 (en) | 1999-04-12 | 2001-01-23 | Michigan Molecular Institute | Air curing water base copolymers and method of preparation |
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US8188183B2 (en) | 2004-08-03 | 2012-05-29 | Imperial Chemical Industries, Plc | Low VOC coatings and paints |
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