EP0447428B1 - Process for the production of a multi-layer coating, water-dilutable coating compositions, water-dilutable emulsion polymers and process for the production of water-dilutable emulsion polymers - Google Patents
Process for the production of a multi-layer coating, water-dilutable coating compositions, water-dilutable emulsion polymers and process for the production of water-dilutable emulsion polymers Download PDFInfo
- Publication number
- EP0447428B1 EP0447428B1 EP90900099A EP90900099A EP0447428B1 EP 0447428 B1 EP0447428 B1 EP 0447428B1 EP 90900099 A EP90900099 A EP 90900099A EP 90900099 A EP90900099 A EP 90900099A EP 0447428 B1 EP0447428 B1 EP 0447428B1
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- EP
- European Patent Office
- Prior art keywords
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- monomer
- monomers
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- 239000004908 Emulsion polymer Substances 0.000 title claims abstract description 49
- 239000008199 coating composition Substances 0.000 title claims abstract description 42
- 238000000576 coating method Methods 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims abstract description 20
- 239000011248 coating agent Substances 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title abstract description 13
- 239000000178 monomer Substances 0.000 claims abstract description 135
- 239000000203 mixture Substances 0.000 claims abstract description 126
- 229920000642 polymer Polymers 0.000 claims abstract description 38
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims abstract description 27
- 230000009477 glass transition Effects 0.000 claims abstract description 24
- -1 aliphatic ester Chemical class 0.000 claims description 48
- 238000006243 chemical reaction Methods 0.000 claims description 30
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 29
- 239000003995 emulsifying agent Substances 0.000 claims description 27
- 150000002148 esters Chemical class 0.000 claims description 25
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 23
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 21
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 17
- 239000000049 pigment Substances 0.000 claims description 14
- 239000003999 initiator Substances 0.000 claims description 13
- 229920005749 polyurethane resin Polymers 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims description 12
- 239000000758 substrate Substances 0.000 claims description 8
- 238000002360 preparation method Methods 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 5
- 239000008346 aqueous phase Substances 0.000 claims description 5
- 230000001681 protective effect Effects 0.000 claims description 5
- 239000004411 aluminium Substances 0.000 claims 2
- BDHFUVZGWQCTTF-UHFFFAOYSA-N sulfonic acid Chemical group OS(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-N 0.000 claims 2
- 238000007720 emulsion polymerization reaction Methods 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 39
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 37
- 239000002585 base Substances 0.000 description 31
- 239000006185 dispersion Substances 0.000 description 31
- 239000002253 acid Substances 0.000 description 30
- 239000000839 emulsion Substances 0.000 description 24
- 239000000243 solution Substances 0.000 description 22
- 239000008367 deionised water Substances 0.000 description 21
- 229910021641 deionized water Inorganic materials 0.000 description 21
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 20
- 239000012935 ammoniumperoxodisulfate Substances 0.000 description 17
- 125000004432 carbon atom Chemical group C* 0.000 description 16
- 150000002009 diols Chemical class 0.000 description 16
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 14
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- 150000003077 polyols Chemical class 0.000 description 13
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 12
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 12
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 12
- 150000007513 acids Chemical class 0.000 description 11
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 10
- 230000000694 effects Effects 0.000 description 10
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 9
- 229920000768 polyamine Polymers 0.000 description 9
- 229920000728 polyester Polymers 0.000 description 9
- GNSFRPWPOGYVLO-UHFFFAOYSA-N 3-hydroxypropyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCCO GNSFRPWPOGYVLO-UHFFFAOYSA-N 0.000 description 8
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 8
- 125000001931 aliphatic group Chemical group 0.000 description 8
- 150000001875 compounds Chemical class 0.000 description 8
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 8
- 125000001424 substituent group Chemical group 0.000 description 8
- 239000007864 aqueous solution Substances 0.000 description 7
- 125000005442 diisocyanate group Chemical group 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 125000002768 hydroxyalkyl group Chemical group 0.000 description 7
- 239000012948 isocyanate Substances 0.000 description 7
- 150000002513 isocyanates Chemical class 0.000 description 7
- 229920000570 polyether Polymers 0.000 description 7
- 239000002904 solvent Substances 0.000 description 7
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 6
- SJRJJKPEHAURKC-UHFFFAOYSA-N N-Methylmorpholine Chemical compound CN1CCOCC1 SJRJJKPEHAURKC-UHFFFAOYSA-N 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical class OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 125000000217 alkyl group Chemical group 0.000 description 6
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 6
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 6
- 239000004721 Polyphenylene oxide Substances 0.000 description 5
- 150000003863 ammonium salts Chemical class 0.000 description 5
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 150000002596 lactones Chemical class 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- OVLGNUHSJCCFPG-UHFFFAOYSA-N nonoxybenzene;sulfuric acid Chemical compound OS(O)(=O)=O.CCCCCCCCCOC1=CC=CC=C1 OVLGNUHSJCCFPG-UHFFFAOYSA-N 0.000 description 5
- 238000006116 polymerization reaction Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000011541 reaction mixture Substances 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- 239000004970 Chain extender Substances 0.000 description 4
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 4
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 4
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 4
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 4
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 4
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 4
- KBLWLMPSVYBVDK-UHFFFAOYSA-N cyclohexyl prop-2-enoate Chemical compound C=CC(=O)OC1CCCCC1 KBLWLMPSVYBVDK-UHFFFAOYSA-N 0.000 description 4
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 4
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 4
- 150000002334 glycols Chemical class 0.000 description 4
- 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 4
- 229930195733 hydrocarbon Natural products 0.000 description 4
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 4
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 4
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 4
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical compound C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 description 4
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 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 4
- 238000003756 stirring Methods 0.000 description 4
- 150000003512 tertiary amines Chemical class 0.000 description 4
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 4
- PTBDIHRZYDMNKB-UHFFFAOYSA-N 2,2-Bis(hydroxymethyl)propionic acid Chemical compound OCC(C)(CO)C(O)=O PTBDIHRZYDMNKB-UHFFFAOYSA-N 0.000 description 3
- OMIGHNLMNHATMP-UHFFFAOYSA-N 2-hydroxyethyl prop-2-enoate Chemical compound OCCOC(=O)C=C OMIGHNLMNHATMP-UHFFFAOYSA-N 0.000 description 3
- GWZMWHWAWHPNHN-UHFFFAOYSA-N 2-hydroxypropyl prop-2-enoate Chemical compound CC(O)COC(=O)C=C GWZMWHWAWHPNHN-UHFFFAOYSA-N 0.000 description 3
- QZPSOSOOLFHYRR-UHFFFAOYSA-N 3-hydroxypropyl prop-2-enoate Chemical compound OCCCOC(=O)C=C QZPSOSOOLFHYRR-UHFFFAOYSA-N 0.000 description 3
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 3
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 3
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 description 3
- 239000005058 Isophorone diisocyanate Substances 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 3
- UEEJHVSXFDXPFK-UHFFFAOYSA-N N-dimethylaminoethanol Chemical compound CN(C)CCO UEEJHVSXFDXPFK-UHFFFAOYSA-N 0.000 description 3
- 125000003277 amino group Chemical group 0.000 description 3
- 150000008064 anhydrides Chemical class 0.000 description 3
- 239000012874 anionic emulsifier Substances 0.000 description 3
- 125000000129 anionic group Chemical group 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 229960002887 deanol Drugs 0.000 description 3
- 150000004985 diamines Chemical class 0.000 description 3
- 150000001991 dicarboxylic acids Chemical class 0.000 description 3
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 3
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 3
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- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 description 3
- 150000002576 ketones Chemical class 0.000 description 3
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- GSGDTSDELPUTKU-UHFFFAOYSA-N nonoxybenzene Chemical compound CCCCCCCCCOC1=CC=CC=C1 GSGDTSDELPUTKU-UHFFFAOYSA-N 0.000 description 3
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- 238000003860 storage Methods 0.000 description 3
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- RNLHGQLZWXBQNY-UHFFFAOYSA-N 3-(aminomethyl)-3,5,5-trimethylcyclohexan-1-amine Chemical compound CC1(C)CC(N)CC(C)(CN)C1 RNLHGQLZWXBQNY-UHFFFAOYSA-N 0.000 description 2
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- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 description 2
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- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
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- DNTMQTKDNSEIFO-UHFFFAOYSA-N n-(hydroxymethyl)-2-methylprop-2-enamide Chemical compound CC(=C)C(=O)NCO DNTMQTKDNSEIFO-UHFFFAOYSA-N 0.000 description 2
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- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- UFDHBDMSHIXOKF-UHFFFAOYSA-N tetrahydrophthalic acid Natural products OC(=O)C1=C(C(O)=O)CCCC1 UFDHBDMSHIXOKF-UHFFFAOYSA-N 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
- SRPWOOOHEPICQU-UHFFFAOYSA-N trimellitic anhydride Chemical compound OC(=O)C1=CC=C2C(=O)OC(=O)C2=C1 SRPWOOOHEPICQU-UHFFFAOYSA-N 0.000 description 1
- 238000005829 trimerization reaction Methods 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- 150000003673 urethanes Chemical class 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 125000005287 vanadyl group Chemical group 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000003799 water insoluble solvent Substances 0.000 description 1
- 238000004383 yellowing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/50—Multilayers
- B05D7/52—Two layers
- B05D7/53—Base coat plus clear coat type
- B05D7/532—Base coat plus clear coat type the two layers being cured or baked together, i.e. wet on wet
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D2451/00—Type of carrier, type of coating (Multilayers)
Definitions
- the invention also relates to water-thinnable coating compositions, water-thinnable emulsion polymers and a process for the preparation of water-thinnable emulsion polymers.
- aqueous base coating compositions used are composed such that they can be applied to the substrate in relatively thin, fast-drying layers, in particular with the aid of automatic painting systems, and after carrying out process steps (3) and (4), the metal pigment particles in parallel alignment to the substrate surface.
- the aqueous base coating compositions must be composed in such a way that the base layer of the baked metal effect coating adheres well to the substrate and the transparent cover layer adheres well to the base layer. Furthermore, the aqueous base coating compositions must be composed in such a way that the baked-on metallic effect coating shows no matting, delamination phenomena or even bubbles after exposure to a constant temperature of condensed water.
- aqueous basecoat compositions exhibit high storage stability.
- DE-A-36 28 124 discloses aqueous base coating compositions which contain, as film-forming material, a mixture of a water-dilutable emulsification polymer and a water-dilutable polyurethane resin. These basecoat compositions do not optimally meet the requirements set out above.
- the object on which the present invention is based is to provide aqueous base coating compositions which are suitable for the process in question and which optimally meet the requirements set out above.
- aqueous coating compositions which can be used as wood lacquers and which contain a water-thinnable emulsion polymer which is free of hydroxyl groups and can be obtained via a two-stage emulsion polymerization process.
- U.S. Patent 4,150,005 discloses aqueous coating compositions containing a water-thinnable emulsion polymer which can be obtained by preparing a highly hydrophilic polymer with a low glass transition temperature in a first emulsion polymerization stage and in its presence in a second emulsion polymerization stage a hydrophobic polymer with a high glass transition temperature is produced.
- Multi-layer protective and / or decorative coatings of the type described above and the problems encountered in the manufacture of these coatings are not addressed in U.S. Patent No. 4,150,005.
- GB-A-2,034,334 describes aqueous coating compositions which contain a water-thinnable emulsion polymer which can be obtained via a two-stage emulsion polymerisation process and which must have N-methylol groups.
- GB-A-2,034,334 is not indicative of the fact that the two polymer stages have to differ in their glass transition temperatures in the manner according to the invention.
- Multilayer protective and / or decorative coatings of the type described above and the problems encountered in the manufacture of these coatings are not addressed in GB-A-2,034,334.
- EP-A-287 144 describes a process for producing a multilayer coating of the type described above, in which aqueous base coating compositions are used which contain a water-dilutable emulsification polymer which can be obtained via a two-stage emulsion polymerization process and which in the second stage ("shell" ) has a very high proportion of acid groups and in which the first and second polymer stages differ in their glass transition temperatures in such a way that the first stage has a lower glass transition temperature than the second stage.
- aqueous base coating compositions which contain a water-dilutable emulsification polymer which can be obtained via a two-stage emulsion polymerization process and which in the second stage (“shell" ) has a very high proportion of acid groups and in which the first and second polymer stages differ in their glass transition temperatures in such a way that the first stage has a lower glass transition temperature than the second stage.
- the water-dilutable emulsion polymers used according to the invention are, in a known manner, for example in a stirred tank, by a two-stage emulsion polymerization in an aqueous medium with heating and cooling device, producible.
- the monomers can be added in such a way that a solution of all of the water, the emulsifier and part of the initiator is introduced and the monomer or monomer mixture and separately therefrom, but in parallel the rest of the initiator is slowly added at the polymerization temperature.
- the water and the emulsifier it is also possible to introduce some of the water and the emulsifier and to prepare a pre-emulsion from the rest of the water and the emulsifier and from the monomer or monomer mixture, which is added slowly at the polymerization temperature, the initiator again being added separately. It is preferred in the first stage to add the monomer or monomer mixture in the form of a pre-emulsion and in the second stage to add the monomer or monomer mixture in bulk, ie without water and emulsifier, and to add the initiator separately but in parallel.
- the polymerization temperature is generally in the range from 20 to 100 ° C., preferably 40 to 90 ° C.
- the quantitative ratio between the monomers and the water can be selected so that the resulting dispersion has a solids content of 30 to 60% by weight, preferably 35 to 50% by weight.
- An anionic emulsifier is preferably used alone or in a mixture as the emulsifier.
- anionic emulsifiers are the alkali metal salts of sulfuric acid half-esters of alkylphenols or alcohols, furthermore the sulfuric acid half-esters of oxethylated alkylphenols or oxethylated alcohols, preferably the alkali metal salts of sulfuric acid half-esters of a nonylphenol, alkyl or with 4-5 moles of ethylene oxide per mole Aryl sulfonate, sodium lauryl sulfate, sodium lauryl ethoxylate sulfate and secondary sodium alkane sulfonates, the carbon chain of which contains 8-20 carbon atoms.
- the amount of the anionic emulsifier is 0.1-5.0% by weight, based on the monomers, preferably 0.5-3.0% by weight.
- a nonionic emulsifier of the ethoxylated alkylphenol or fatty alcohol type for example an addition product of 1 mol of nonylphenol and 4-30 mol of ethylene oxide, can be used in a mixture with the anionic emulsifier.
- a peroxide compound is preferably used as the radical-forming initiator.
- the initiator is water-soluble or monomer-soluble.
- a water-soluble initiator is preferably used.
- Suitable initiators are the customary inorganic per compounds, such as ammonium persulfate, potassium persulfate, ammonium or alkali metal peroxydiphosphate and organic peroxides, such as e.g. Benzoyl peroxide, organic peresters, such as perisopivalate, partly in combination with reducing agents, such as sodium disulfite, hydrazine, hydroxylamine and catalytic amounts of accelerators, such as iron, cobalt, cerium and vanadyl salts, preferably alkali metal or ammonium peroxydisulfates.
- reducing agents such as sodium disulfite, hydrazine, hydroxylamine
- accelerators such as iron, cobalt, cerium and vanadyl salts, preferably alkali metal or ammonium peroxydisulfates.
- the redox initiator systems disclosed in EP-A-107300 can also be used.
- the first stage 10 to 90, preferably 35 to 65 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers are emulsion polymerized.
- the monomer or monomer mixture used in the first stage is selected so that when the monomer or monomer mixture used in the first stage is completely polymerized out, a polymer with a glass transition temperature (T G1 ) of + 30 ° C. to + 110 ° C, preferably 60 to 95 ° C is obtained. Since the glass transition temperature of emulsion polymers according to the equation
- Examples of monomers which can be used in the first stage are: vinylaromatic hydrocarbons, such as styrene, ⁇ -alkylstyrene and vinyltoluene, esters of acrylic acid or methacrylic acid, in particular aliphatic and cycloaliphatic acrylates or methacrylates with up to 20 carbon atoms in the alcohol radical, such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl, lauryl and cyclohexyl acrylate or methacrylate, acrylic and / or methacrylic acid, acrylic and / or methacrylamide, N-methylolacrylamide and / or N-methylol methacrylamide, hydroxyalkyl esters of acrylic acid, methacrylic acid or another ⁇ , ⁇ -ethylenically unsaturated carboxylic acid, such as 2-hydroxyethyl acrylate, 2-hydroxypropyl
- ethylenically unsaturated monomers or mixtures of ethylenically unsaturated monomers which are essentially free of hydroxyl and carboxyl groups preference is given to using ethylenically unsaturated monomers or mixtures of ethylenically unsaturated monomers which are essentially free of hydroxyl and carboxyl groups.
- substantially free is intended to mean that it is preferred to use monomers or monomer mixtures which are free from hydroxyl and carboxyl groups, but that the monomers or monomer mixtures used also contain small amounts (for example as a result of impurities) of hydroxyl and / or may contain carboxyl groups.
- the content of hydroxyl and carboxyl groups should preferably be at most so high that a polymer prepared from the monomer or monomer mixture used in the first stage has an OH number of at most 5 and an acid number of at most 3.
- component (a1) can be used, for example: cyclohexyl acrylate, cyclohexyl methacrylate, alkyl acrylates and alkyl methacrylates with up to 20 carbon atoms in the alkyl radical, such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl and lauryl acrylate and methacrylate or mixtures of these monomers.
- alkyl radical such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl and lauryl acrylate and methacrylate or mixtures of these monomers.
- component (a2) e.g. vinylaromatic hydrocarbons such as styrene, ⁇ -alkylstyrene and vinyltoluene, acrylic and methacrylamide and acrylonitrile and methacrylonitrile or mixtures of these monomers are used.
- vinylaromatic hydrocarbons such as styrene, ⁇ -alkylstyrene and vinyltoluene, acrylic and methacrylamide and acrylonitrile and methacrylonitrile or mixtures of these monomers are used.
- the monomer or monomer mixture used in the first stage and the monomer or monomer mixture used in the second stage are selected in such a way that the emulsion polymer obtained has a hydroxyl number of 2 to 100, preferably 10 to 50 and the difference T G1 - T G2 is 10 to 170, preferably 80 to 150 ° C.
- Examples of monomers which can be used in the second stage are: vinylaromatic hydrocarbons, such as styrene, ⁇ -alkylstyrene and vinyltoluene, Esters of acrylic acid or methacrylic acid, in particular aliphatic and cycloaliphatic acrylates or methacrylates with up to 20 carbon atoms in the alcohol radical, such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl, lauryl and cyclohexyl acrylate or - methacrylate, acrylic and / or methacrylic acid, acrylic and / or methacrylamide, N-methylolacrylamide and / or N-methylolmethacrylamide, hydroxyalkyl esters of acrylic acid, methacrylic acid or another ⁇ , ⁇ -ethylenically unsaturated carboxylic acid, such as 2-hydroxyethyl acrylate, 2-hydroxypropy
- component (b1) e.g. are used: cyclohexyl acrylate, cyclohexyl methacrylate, alkyl acrylates and alkyl methacrylates with up to 20 carbon atoms in the alkyl radical, such as e.g. Methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl and lauryl acrylate and methacrylate or mixtures of these monomers.
- alkyl radical such as e.g. Methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl and lauryl acrylate and methacrylate or mixtures of these monomers.
- hydroxyalkyl esters of acrylic acid, methacrylic acid or another ⁇ , ⁇ -ethylenically unsaturated carboxylic acid can be derived from an alkylene glycol esterified with the acid, or can be obtained by reacting the acid with an alkylene oxide.
- Hydroxyalkyl esters of acrylic acid and methacrylic acid, in which the hydroxyalkyl group contains up to 4 carbon atoms, or mixtures of these hydroxyalkyl esters are preferably used as component (b2).
- hydroxyalkyl esters examples include 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 3-hydroxypropyl acrylate, 2-hydroypropyl methacrylate, 3-hydroxypropyl methacrylate, 2-hydroxyethyl methacrylate, 4-hydroxybutyl acrylate or 4-hydroxybutyl methacrylate.
- esters of other unsaturated acids such as ethacrylic acid, crotonic acid and similar acids with up to about 6 carbon atoms per molecule, can also be used.
- Acrylic acid and / or methacrylic acid and / or acrylamidomethylpropanesulfonic acid are preferably used as component (b3).
- ethylenically unsaturated acids with up to 6 carbon atoms in the molecule can also be used.
- examples of such acids are ethacrylic acid, crotonic acid, maleic acid, fumaric acid and itaconic acid.
- component (b4) e.g. are used: vinyl aromatic hydrocarbons, such as styrene, ⁇ -alkylstyrene and vinyl toluene, acrylic and methacrylamide and acrylonitrile and methacrylonitrile, or mixtures of these monomers.
- vinyl aromatic hydrocarbons such as styrene, ⁇ -alkylstyrene and vinyl toluene, acrylic and methacrylamide and acrylonitrile and methacrylonitrile, or mixtures of these monomers.
- the emulsion polymer used according to the invention should have a number average molar mass (determination: gel permeation chromatography using polystyrene as the standard) of 200,000 to 2,000,000, preferably 300,000 to 1,500,000.
- aqueous base coating compositions according to the invention contain, in addition to the emulsion polymer described above, a water-dilutable polyurethane resin as the film-forming material.
- the base coating compositions according to the invention preferably contain water-thinnable, urea-containing polyurethane resins which have a number average molecular weight (determination: gel permeation chromatography using polystyrene as the standard) of 1000 to 60,000, preferably 1500 to 50,000 and an acid number of 5 to 70, preferably 10 to 30 and by reaction, preferably chain extension of prepolymers containing isocyanate groups with polyamines and / or hydrazine can be produced.
- a number average molecular weight determination: gel permeation chromatography using polystyrene as the standard
- the prepolymer containing isocyanate groups can be prepared by reacting polyalcohols having a hydroxyl number from 10 to 1800, preferably 50 to 500, with excess polyisocyanates at temperatures up to 150 ° C., preferably 50 to 130 ° C., in organic solvents which do not react with isocyanates can, succeed.
- the equivalence ratio of NCO to OH groups is between 1.5 and 1.0 to 1.0, preferably between 1.4 and 1.2 to 1.
- the polyols used to prepare the prepolymer can be low molecular weight and / or high molecular weight and they can contain inert anionic groups.
- Low molecular weight polyols can be used to increase the hardness of the polyurethane. They have a molecular weight from 60 to about 400 and can contain aliphatic, alicyclic or aromatic groups. Amounts of up to 30% by weight of the total polyol constituents, preferably about 2 to 20% by weight, are used.
- the low molecular weight polyols with up to about 20 carbon atoms per molecule such as ethylene glycol, diethylene glycol, triethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, 1,2-butylene glycol, 1,6-hexanediol, are advantageous , Trimethylolpropane, castor oil or hydrogenated castor oil, di-trimethylolpropane ether, pentaerythritol, 1,2-cyclohexanediol, 1,4-cyclohexanedimethanol, bisphenol A, bisphenol F, neopentylglycol, hydroxypivalic acid-neopentylglycol ester, hydroxyethylated or hydroxypropylated bisphenol A, bisphenol A, mixtures thereof .
- a high proportion of a predominantly linear polyol with a preferred hydroxyl number of 30 to 150 should be added.
- Up to 97% by weight of the total polyol can consist of saturated and unsaturated polyesters and / or polyethers with a molecular weight Mn exist from 400 to 5000.
- polyether diols such as poly (oxyethylene) glycols, poly (oxypropylene) glycols and / or poly (oxybutylene) glycols.
- the selected polyether diols should not introduce excessive amounts of ether groups, otherwise the polymers formed will swell in water.
- the preferred polyether diols are poly (oxypropylene) glycols in the molecular weight range Mn from 400 to 3000.
- Polyester diols are produced by esterification of organic dicarboxylic acids or their anhydrides with organic diols or are derived from a hydroxycarboxylic acid or a lactone.
- polyols or polycarboxylic acids with a higher valency can be used to a small extent.
- the dicarboxylic acids and diols can be linear or branched aliphatic, cycloaliphatic or aromatic dicarboxylic acids or diols.
- the diols used to prepare the polyesters consist, for example, of alkylene glycols, such as ethylene glycol, propylene glycol, butylene glycol, 1,4-butanediol, 1,6-hexanediol, neopentyl glycol and other diols, such as dimethylcyclohexane.
- the acid component of the polyester consists primarily of low molecular weight dicarboxylic acids or their anhydrides with 2 to 30, preferably 4 to 18, carbon atoms in the molecule.
- Suitable acids are, for example, o-phthalic acid, isophthalic acid, terephthalic acid, tetrahydrophthalic acid, cyclohexanedicarboxylic acid, succinic acid, adipic acid, azelaic acid, sebacic acid, maleic acid, fumaric acid, glutaric acid, hexachlorheptanedicarboxylic acid, tetrachlorophthalic acid and / or.
- their anhydrides if they exist, can also be used.
- polyester polyols smaller ones can also be used Amounts of carboxylic acids with 3 or more carboxyl groups, for example trimellitic anhydride or the adduct of maleic anhydride with unsaturated fatty acids, are present.
- polyester diols are also used which are obtained by reacting a lactone with a diol. They are characterized by the presence of a terminal hydroxyl group and recurring polyester content of the formula - (- CO- (CHR) n -CH2-0 -) -.
- n is preferably 4 to 6 and the substituent R is hydrogen, an alkyl, cycloalkyl or alkoxy radical.
- No substituent contains more than 12 carbon atoms. The total number of carbon atoms in the substituent does not exceed 12 per lactone ring. Examples include hydroxycaproic acid, hydroxybutyric acid, hydroxydecanoic acid and / or hydroxystearic acid.
- the lactone used as a raw material can be represented by the following general formula in which n and R have the meaning already given.
- Unsubstituted -caprolactone in which n has the value 4 and all R substituents are hydrogen, is preferred for the preparation of the polyester diols.
- the reaction with lactone is started by low molecular weight polyols, such as ethylene glycol, 1,3-propanediol, 1,4-butanediol, dimethylolcyclohexane.
- other reaction components such as ethylenediamine, alkyldiacanolamines or urea, can also be reacted with caprolactone.
- polylactam diols which are produced by reacting, for example, ⁇ -caprolactam with low molecular weight diols.
- Aliphatic, cycloaliphatic and / or aromatic poly are used as typical multifunctional isocyanates isocyanates with at least two isocyanate groups per molecule.
- the isomers or isomer mixtures of organic diisocyanates are preferred.
- Suitable aromatic diisocyanates are phenylene diisocyanate, tolylene diisocyanate, xylylene diisocyanate, biphenylene diisocyanate, naphthylene diisocyanate and diphenylmethane diisocyanate. Due to their good resistance to ultraviolet light, (cyclo) aliphatic diisocyanates produce products with a low tendency to yellowing.
- Examples include isophorone diisocyanate, cyclopentylene diisocyanate and the hydrogenation products of aromatic diisocyanates, such as cyclohexylene diisocyanate, methylcyclohexylene diisocyanate and dicyclohexylmethane diisocyanate.
- aromatic diisocyanates such as cyclohexylene diisocyanate, methylcyclohexylene diisocyanate and dicyclohexylmethane diisocyanate.
- aliphatic diisocyanates are trimethylene diisocyanate, tetramethylene diisocyanate, pentamethylene diisocyanate, hexamethylene diisocyanate, propylene diisocyanate, ethylethylene diisocyanate, dimethylethylene diisocyanate, methyltrimethylene diisocyanate and trimethylhexane diisocyanate.
- Isophorone diisocyanate and dicyclohexyl methane diisocyanate are particularly preferred as diisocyanates.
- the polyisocyanate component used to form the prepolymer can also contain a proportion of higher-quality polyisocyanates, provided that this does not cause gel formation.
- Products which have been found to be suitable as triisocyanates are those which are formed by trimerization or oligomerization of diisocyanates or by reaction of diisocyanates with compounds containing polyfunctional OH or NH groups.
- the average functionality can optionally be reduced by adding monoisocyanates.
- chain terminating monoisocyanates are phenyl isocyanate, cyclohexyl isocyanate and stearyl isocyanate.
- Polyurethanes are generally not compatible with water Lich, if special components are not incorporated in their synthesis and / or special manufacturing steps are carried out. So large an acid number is built in that the neutralized product can be dispersed stably in water.
- compounds which contain two H-active groups reacting with isocyanate groups and at least one group capable of forming anions.
- Suitable groups which react with isocyanate groups are, in particular, hydroxyl groups and primary and / or secondary amino groups.
- Groups which are capable of forming anions are carboxyl, sulfonic acid and / or phosphonic acid groups.
- Carboxylic acid or carboxylate groups are preferably used. They should be so inert that the isocyanate groups of the diisocyanate preferably react with the other groups of the molecule that are reactive toward isocyanate groups.
- alkanoic acids with two substituents on the carbon atom are used.
- the substituent can be a hydroxyl group, an alkyl group or an alkylol group.
- These polyols have at least one, generally 1 to 3 carboxyl groups in the molecule. They have two to about 25, preferably 3 to 10, carbon atoms. Examples of such compounds are dihydroxypropionic acid, dihydroxysuccinic acid and dihydroxybenzoic acid.
- Examples of such compounds are 2,2-dimethylol acetic acid, 2,2-dimethylol propionic acid, 2,2-dimethylol butyric acid and 2,2-dimethylol pentanoic acid.
- the preferred dihydroxyalkanoic acid is 2,2-dimethylolpropionic acid.
- Compounds containing amino groups are, for example, -diaminovaleric acid, 3,4-diaminobenzoic acid, 2,4-diaminotoluenesulfonic acid and 2,4-diaminodiphenyl ether sulfonic acid.
- the polyol containing carboxyl groups can be 3 to Make up 100% by weight, preferably 5 to 50% by weight, of the total polyol component in the NCO prepolymer.
- the amount of ionizable carboxyl groups available through the carboxyl group neutralization in salt form is generally at least 0.4% by weight, preferably at least 0.7% by weight, based on the solid.
- the upper limit is about 6% by weight.
- the amount of dihydroxyalkanoic acids in the unneutralized prepolymer gives an acid number of at least 5, preferably at least 10.
- the upper limit of the acid number is 70, preferably 40, based on the solids.
- this dihydroxyalkanoic acid is advantageously at least partially neutralized with a tertiary amine in order to avoid a reaction with the isocyanates.
- the NCO prepolymers used according to the invention can be prepared by simultaneously reacting the polyol or polyol mixture with an excess of diisocyanate.
- the implementation can also be carried out in stages in the prescribed order. Examples are described in DE 26 24 442 and DE 32 10 051.
- the reaction temperature is up to 150 ° C, with a temperature in the range of 50 to 130 ° C being preferred. The reaction continues until practically all of the hydroxyl functions have been converted.
- the NCO prepolymer contains at least about 0.5% by weight of isocyanate groups, preferably at least 1% by weight of NCO, based on the solid.
- the upper limit is approximately 15% by weight, preferably 10% by weight, particularly preferably 5% by weight.
- the reaction can optionally be carried out in the presence of a catalyst such as organotin compounds and / or tertiary amines.
- a catalyst such as organotin compounds and / or tertiary amines.
- organic that do not contain Zerewitinoff active hydrogen are possible.
- Usable solvents are, for example, dimethylformamide, esters, ethers, such as diethylene glycol dimethyl ether, keto esters, ketones, such as methyl ethyl ketone and acetone, ketones substituted with methoxy groups, such as methoxy hexanone, glycol ether esters, chlorinated hydrocarbons, aliphatic and alicyclic hydrocarbon pyrrolidones, such as N-methylpyrrolidone Furans, aromatic hydrocarbons and their mixtures.
- the amount of solvent can vary within wide limits and should be sufficient to form a prepolymer solution with a suitable viscosity.
- Suitable tertiary amines are, for example, trimethylamine, triethylamine, dimethylethylamine, diethylmethylamine, N-methylmorpholine.
- the NCO prepolymer is diluted with water and then results in a finely divided dispersion.
- the isocyanate groups still present are included Di- and / or polyamines reacted with primary and / or secondary amino groups as chain extenders. This reaction leads to a further linkage and increase in the molecular weight.
- the competitive reaction between amine and water with the isocyanate must be well coordinated (time, temperature, concentration) in order to obtain optimum properties and well monitored for reproducible production.
- Water-soluble compounds are preferred as chain extenders because they increase the dispersibility of the polymeric end product in water.
- Hydrazine and organic diamines are preferred because they usually build up the highest molecular weight without gelling the resin.
- the prerequisite for this is that the ratio of the amino groups to the isocyanate groups is selected appropriately.
- the amount of chain extender is determined by its functionality, the NCO content of the prepolymer and the duration of the reaction.
- the ratio of the active hydrogen atoms in the chain extender to the NCO groups in the prepolymer should generally be less than 2: 1 and preferably in the range from 1.0: 1 to 1.75: 1.
- the presence of excess active hydrogen, especially in the form of primary amino groups, can result in polymers with undesirably low molecular weights.
- Polyamines are essentially alkylene polyamines having 1 to 40 carbon atoms, preferably about 2 to 15 carbon atoms. They can carry substituents that have no hydrogen atoms that are reactive with isocyanate groups. Examples are polyamines with a linear or branched aliphatic, cycloaliphatic or aromatic structure and at least two primary amino groups.
- the diamines include ethylenediamine, propylenediamine, 1,4-butylenediamine, piperazine, 1,4-cyclohexyldimethylamine, 1,6-hexamethylenediamine, trimethylhexamethylenediamine, methanediamine, isophoronediamine, 4,4'-diaminodicyclohexylmethane and aminoethylethanolamine.
- Preferred diamines are alkyl or cycloalkyl diamines, such as propylenediamine and 1-amino-3-aminomethyl-3,5,5-trimethylcyclohexane.
- the chain can be extended at least partially with a polyamine that has at least three amine groups with a reactive hydrogen.
- This type of polyamine can be used in such an amount that unreacted amine nitrogen atoms with 1 or 2 reactive hydrogen atoms are present after the polymer has been extended.
- useful polyamines are diethylenetriamine, triethylenetetraamine, dipropylenetriamine and dibutylenetriamine.
- Preferred polyamines are the alkyl or cycloalkyl triamines, such as diethylenetriamine.
- monoamines such as ethylhexylamine, can also be added.
- the mixture of emulsion polymer and polyurethane resin contained in the preferred aqueous base coating compositions as a film-forming material consists of 95 to 40% by weight of emulsion polymer and 5 to 60% by weight of polyurethane resin, the proportions each referring to the solids content and their total always 100% by weight .-%.
- the aqueous base coating compositions according to the invention advantageously also contain further compatible water-dilutable synthetic resins, such as, for example, aminoplast resins, polyesters and polyethers, which generally serve as grind resins for the pigments.
- the aqueous base coating compositions according to the invention preferably contain 5 to 20, particularly preferably 10 to 16% by weight, based on the total solids content of the base coating compositions, of a water-dilutable aminoplast resin, preferably melamine resin and 5 to 20, preferably 8 to 15% by weight, of a water-dilutable polyether (eg polypropylene glycol with a number average molecular weight of 400 to 900).
- a water-dilutable aminoplast resin preferably melamine resin and 5 to 20, preferably 8 to 15% by weight
- a water-dilutable polyether eg polypropylene glycol with a number average molecular weight of 400 to 900.
- the base coating compositions according to the invention can contain coloring pigments on an inorganic basis, such as e.g. Titanium dioxide, iron oxide, soot, etc., coloring pigments on an organic basis as well as common metal pigments (e.g. commercially available aluminum bronzes, stainless steel bronzes ...) and non-metallic effect pigments (e.g. pearlescent or interference pigments).
- the base coating compositions according to the invention preferably contain metal pigments and / or effect pigments.
- the pigmentation level is in the usual ranges.
- crosslinked polymeric microparticles such as are disclosed in EP-A-38 127 and / or customary rheological inorganic or organic additives, can be added to the base coating compositions according to the invention.
- water-soluble cellulose ethers such as hydroxyethyl cellulose, methyl cellulose or carboxymethyl cellulose
- synthetic polymers with ionic and / or associative groups such as polyvinyl alcohol, poly (meth) acrylamide, poly (meth) acrylic acid, polyvinyl pyrrolidone, styrene-maleic anhydride or ethylene-maleic anhydride, act as thickeners Copolymers and their derivatives or also hydrophobically modified ethoxylated urethanes or polyacrylates.
- Carboxyl group-containing polyacrylate copolymers are particularly preferred with an acid number of 60 to 780, preferably 200 to 500.
- the base coating compositions according to the invention generally have a solids content of about 15 to 50% by weight.
- the solids content varies with the intended use of the coating compositions.
- metallic paints for example, it is preferably 17 to 25% by weight.
- plain-colored paints it is higher, for example 30 to 45% by weight.
- the coating compositions according to the invention can additionally contain customary organic solvents. Their share is kept as low as possible. For example, it is below 15% by weight.
- the base coating compositions according to the invention are generally adjusted to a pH between 6.5 and 9.0.
- the pH can be adjusted with conventional amines, e.g. Ammonia, triethylamine, dimethylaminoethanol and N-methylmorpholine can be adjusted.
- the task explained at the outset is solved.
- the base coating compositions according to the invention high-quality coatings can be produced even without overcoating with a transparent top coating composition.
- the coating compositions according to the invention can be applied to any substrates, such as metal, wood, plastic or paper.
- Emulsion polymer dispersion 1 Emulsion polymer dispersion 1
- Emulsion polymer dispersion 2 Emulsion polymer dispersion 2
- An emulsion is prepared in the stirrable feed vessel from 720 g deionized water, 24 g emulsifier 1, 10.8 g acrylamide, 518 g methyl methacrylate, 292 g n-butyl methacrylate and 205 g styrene. 30% by weight of this emulsion are added for presentation. A solution of 0.9 g of ammonium peroxodisulfate APS in 55 g of deionized water is then added dropwise in the course of 5 minutes. An exothermic reaction occurs. The reaction temperature is kept between 80 and 85 ° C.
- a mixture of 700 g of n-butyl acrylate, 89.8 g of hydroxypropyl methacrylate, 35.9 g of methyl methacrylate, 35.9 g of methacrylic acid, 26.9 g of acrylamide and 4.5 g is then added within 2 hours Eikosa (ethylene glycol) nonylphenyl ether (Antarox®CO 850 from GAF Corp., emulsifier 2) was added. After the addition has ended, the reaction mixture is kept at 82 ° C. for a further 1.5 hours. It is then cooled and the dispersion is spread over a fabric 30 ⁇ m mesh size given. A finely divided dispersion with a non-volatile content of 45% by weight, a pH of 2.5, an acid number of 14 and an OH number of 20 is obtained.
- Emulsion polymer dispersion 5 Emulsion polymer dispersion 5
- stirrable feed vessel 720 g of deionized water 24 g of emulsifier 1, 43.2 g of acrylamide, 907 g of methyl methacrylate and 216 g of n-butyl methacrylate, 842 g of n-butyl acrylate, 108 g of hydroxypropyl methacrylate, 43.2 g of methacrylic acid and 5.4 g emulsifier 2 an emulsion is prepared. 10% by weight of this emulsion are added for presentation. A solution of 0.87 g of ammonium peroxodisulfate in 53 g of deionized water is then added dropwise in the course of 5 minutes. An exothermic reaction occurs.
- reaction temperature is kept between 82 and 88 ° C. 15 minutes after the addition of the APS solution has ended, the remaining 90% by weight of the emulsion are added within 3 hours and a solution of 2.23 g of APS in 478 g of deionized water is added within 3.5 hours, the temperature being at Is held at 82 ° C.
- reaction mixture is kept at 82 ° C. for a further 1.5 hours. It is then cooled and the dispersion is passed over a 30 ⁇ m mesh. A finely divided dispersion with a non-volatile content of 45% by weight, a pH of 5.8, an acid number of 13 and an OH number of 20 is obtained.
- the mass obtained is poured into 1840 g of cold deionized water with vigorous stirring. 86 g of a 15% hydrazine solution are added to the dispersion obtained within 20 minutes, with vigorous stirring. The resulting, very finely divided dispersion has a solids content of 35% and a run-out time of 27 seconds in the DIN cup 4.
- the mixture is adjusted to a pH value of 7.7 with a 5% aqueous dimethylethanolamine solution and with 9.4 g of a 3.5% solution of a commercially available polyacrylic acid thickener (Viscalex®HV 30 from Allied Colloids, pH value: 8 , 0) offset.
- Mixture 2 is obtained.
- Mixtures 1 and 2 are produced at 800-1000 rpm for 30 minutes to produce the basecoats of the invention. mixed and then adjusted to a pH of 7.7 with a 5% aqueous solution of dimethylethanolamine. The viscosity is then adjusted to an outflow time of 25 seconds in a DIN 4 cup by adding deionized water.
- the base coating compositions BB1, BB2, BB3 and BB4 according to the invention are obtained.
- the base coating composition BB5 is obtained by incorporating 36.2 g of the emulsion polymer dispersion 1 into the mixture 2. BB5 does not contain a polyurethane resin dispersion.
- the base coating compositions thus obtained show excellent storage stability.
- the base coating compositions are sprayed onto well-known methods onto phosphated steel sheets (Bonder 132) coated with a commercially available electrodeposition coating and a commercially available filler, overcoated with a commercially available clearcoat after a flash-off time of 10 minutes and baked at 140 ° C. for 20 minutes.
- the metallic effect coatings obtained in this way show a good metallic effect, good adhesion to the filler, good adhesion between the basecoat and topcoat, good gloss and good resistance in a condensed water constant climate according to DIN 50 017.
- BB1, BB2, BB3 and BB4 show a better metallic effect than BB5.
- a part of the painted sheets is coated again with the base coating compositions BB1, BB2, BB3, BB4 and BB5 and overcoated with a commercially available clear coat.
- the coatings obtained in this way are baked at 80 ° C. for 40 minutes.
- the coatings baked at 80 ° C adhere well to the coatings baked at 140 ° C.
- a basecoat composition prepared as described above using the emulsion polymer dispersion 5 shows insufficient storage stability.
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Abstract
Description
Die Erfindung betrifft ein Verfahren zur Herstellung eines mehrschichtigen schützenden und/oder dekorativen Überzugs auf einer Substratoberfläche, bei dem
- (1) als Basisbeschichtungszusammensetzung eine pigmentierte wäßrige Beschichtungszusammensetzung, die als filmbildendes Material ein wasserverdünnbares Emulsionspolymer enthält, auf die Substratoberfläche aufgebracht wird
- (2) aus der in Stufe (1) aufgebrachten Zusammensetzung ein Polymerfilm gebildet wird
- (3) auf der so erhaltenen Basisschicht eine geeignete transparente Deckbeschichtungszusammensetzung aufgebracht wird und anschließend
- (4) die Basisschicht zusammen mit der Deckschicht eingebrannt wird.
- (1) a pigmented aqueous coating composition containing a water-thinnable emulsion polymer as the film-forming material is applied as a base coating composition to the substrate surface
- (2) a polymer film is formed from the composition applied in step (1)
- (3) a suitable transparent top coating composition is applied to the base layer thus obtained and then
- (4) the base layer is baked together with the cover layer.
Die Erfindung betriffft auch wasserverdünnbare Beschichtungszusammensetzungen, wasserverdünnbare Emulsionspolymere und ein Verfahren zur Herstellung von wasserverdünnbaren Emulsionspolymeren.The invention also relates to water-thinnable coating compositions, water-thinnable emulsion polymers and a process for the preparation of water-thinnable emulsion polymers.
Das oben beschriebene Verfahren zur Herstellung von mehrschichtigen schützenden und/oder dekorativen Überzügen ist bekannt und wird insbesondere zur Herstellung von Metalleffektlackierungen auf Automobilkarosserien eingesetzt (vgl. z.B. EP-A-89497, DE-A-3 628 124 und EP-A-38 127).The process described above for the production of multilayer protective and / or decorative coatings is known and is used in particular for the production of metallic effect coatings on automobile bodies (cf. for example EP-A-89497, DE-A-3 628 124 and EP-A-38 127 ).
Mit dem in Rede stehenden Verfahren können nur dann Metalleffektlackierungen mit einem guten Metalleffekt hergestellt werden, wenn die eingesetzten wäßrigen Basisbeschichtungszusammensetzungen so zusammengesetzt sind, daß sie - insbesondere mit Hilfe von automatischen Lackieranlagen - in relativ dünnen, schnell trocknenden Schichten auf das Substrat aufgebracht werden können und nach Durchführung der Verfahrensschritte (3) und (4) die Metallpigmentteilchen in paralleler Ausrichtung zur Substratoberfläche enthalten.With the process in question, metallic effect coatings with a good metallic effect can only be produced if the aqueous base coating compositions used are composed such that they can be applied to the substrate in relatively thin, fast-drying layers, in particular with the aid of automatic painting systems, and after carrying out process steps (3) and (4), the metal pigment particles in parallel alignment to the substrate surface.
Außerdem müssen die wäßrigen Basisbeschichtungszusammensetzungen so zusammengesetzt sein, daß die Basisschicht der eingebrannten Metalleffektlackierung am Untergrund gut haftet und die transparente Deckschicht auf der Basisschicht gut haftet. Weiter müssen die wäßrigen Basisbeschichtungszusammensetzungen so zusammengesetzt sein, daß die eingebrannte Metalleffektlackierung nach Belastung im Schwitzwasserkonstantklima keine Vermattung, Enthaftungsphänomene oder gar Bläschen zeigt.In addition, the aqueous base coating compositions must be composed in such a way that the base layer of the baked metal effect coating adheres well to the substrate and the transparent cover layer adheres well to the base layer. Furthermore, the aqueous base coating compositions must be composed in such a way that the baked-on metallic effect coating shows no matting, delamination phenomena or even bubbles after exposure to a constant temperature of condensed water.
Schließlich ist es wünschenswert, daß die wäßrigen Basisbeschichtungszusammensetzungen eine hohe Lagerstabilität zeigen.Finally, it is desirable that the aqueous basecoat compositions exhibit high storage stability.
In der DE-A-36 28 124 werden wäßrige Basisbeschichtungszusammensetzungen offenbart, die als filmbildendes Material ein Gemisch aus einem wasserverdünnbaren Emulbionspolymer und einem wasserverdünnbaren Polyurethanharz enthalten. Diese Basisbeschichtungszusammensetzungen erfüllen die oben dargelegten Anforderungen nicht in optimaler Weise.DE-A-36 28 124 discloses aqueous base coating compositions which contain, as film-forming material, a mixture of a water-dilutable emulsification polymer and a water-dilutable polyurethane resin. These basecoat compositions do not optimally meet the requirements set out above.
Die der vorliegenden Erfindung zugrundeliegende Aufgabenstellung besteht darin, für das in Rede stehende Verfahren geeignete wäßrige Basisbeschichtungszusammensetzungen bereitzustellen, die die oben dargelegten Anforderungen optimal erfüllen.The object on which the present invention is based is to provide aqueous base coating compositions which are suitable for the process in question and which optimally meet the requirements set out above.
Diese Aufgabe wird überraschenderweise durch wäßrige Basisbeschichtungszusammensetzungen gelöst, die ein wasserverdünnbares Emulsionspolymer enthalten, das erhältlich ist, indem
- (a) in einer ersten Stufe 10 bis 90 Gewichtsteile eines Gemisches aus
- (a1) 100 bis 60, vorzugsweise 99,5 bis 75 Gew.-% eines cycloaliphatischen oder aliphatischen Esters der Methacrylsäure oder Acrylsäure oder eines Gemisches aus solchen Estern und
- (a2) 0 bis 40, vorzugsweise 0,5 bis 25 Gew.-% eines mit (a1) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren
- (b) nachdem mindestens 80 Gew.-% des in der ersten Stufe eingesetzten ethylenisch ungesättigten Monomers bzw. Monomerengemisches umgesetzt worden sind, in einer zweiten Stufe 90 bis 10 Gewichtsteile eines Gemisches aus
- (b1) 47 bis 99, vorzugsweise 75 bis 90 Gew.-% eines cycloaliphatischen oder aliphatischen Esters der Methacrylsäure oder Acrylsäure oder eines Gemisches aus solchen Estern
- (b2) 1 bis 20, vorzugsweise 5 bis 15 Gew.-% eines mindestens eine Hydroxylgruppe tragenden mit (b1), (b3) und (b4) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren
- (b3) 0 bis 8, vorzugsweise 2 bis 6 Gew.-% eines mindestens eine Carboxyl- oder Sulfonsäuregruppe tragenden mit (b1), (b2) und (b4) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren und
- (b4) 0 bis 25, vorzugsweise 2 bis 15 Gew.-% eines weiteren mit (b1), (b2) und (b3) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren
- (a) in a first stage 10 to 90 parts by weight of a mixture
- (a1) 100 to 60, preferably 99.5 to 75% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters and
- (a2) 0 to 40, preferably 0.5 to 25% by weight of a monomer copolymerizable with (a1) or a mixture of such monomers
- (b) after at least 80% by weight of the ethylenically unsaturated monomer or monomer mixture used in the first stage has been reacted, in a second stage 90 to 10 parts by weight of a mixture
- (b1) 47 to 99, preferably 75 to 90% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters
- (b2) 1 to 20, preferably 5 to 15% by weight of a monomer carrying at least one hydroxyl group and copolymerizable with (b1), (b3) and (b4) or a mixture of such monomers
- (b3) 0 to 8, preferably 2 to 6% by weight of a monomer which carries at least one carboxyl or sulfonic acid group and can be copolymerized with (b1), (b2) and (b4) or a mixture of such monomers and
- (b4) 0 to 25, preferably 2 to 15% by weight of another with (b1), (b2) and (b3) copolymerizable monomers or a mixture of such monomers
In der nicht vorveröffentlichten EP-A-332 011 werden wäßrige Beschichtungszusammensetzungen offenbart, die als Holzlacke verwendbar sind und die ein hydroxylgruppenfreies, über ein zweistufiges Emulsionspolymerisationsverfahren erhältliches, wasserverdünnbares Emulsionspolymer enthalten. In der US-PS-4,150,005 werden wäßrige Beschichtungszusammensetzungen offenbart, die ein wasserverdünnbares Emulsionspolymer enthalten, das erhältlich ist, indem in einer ersten Emulsionspolymerisationsstufe ein stark hydrophiles Polymer mit einer niedrigen Glasübergangstemperatur hergestellt wird und in dessen Gegenwart in einer zweiten Emulsionspolymerisationsstufe ein hydrophobes Polymer mit einer hohen Glasübergangstemperatur hergestellt wird. Mehrschichtige schützende und/oder dekorative Überzüge der oben beschriebenen Art und die bei der Herstellung dieser Überzüge auftretenden Probleme werden in der US-PS-4,150,005 nicht angesprochen. In der GB-A-2,034,334 werden wäßrige Beschichtungszusammensetzungen beschrieben, die ein wasserverdünnbares, über ein zweistufiges Emulsionspolymeribatlonsverfahren erhältliches Emulsionspolymer enthalten, das zwingend N-Methylolgruppen aufweisen muß. Der GB-A-2,034,334 bind keine Hinweise darauf zu entnehmen, daß die beiden polymerstufen sich in ihren Glasübergangstemperaturen in der erfindungsgemäßen Art und Weise unterscheiden müssen. Mehrschichtige schützende und/oder dekorative Überzüge der oben beschriebenen Art und die bei der Herstellung dieser Überzüge auftretenden Probleme werden in der GB-A-2,034,334 nicht angesprochen. In der EP-A-287 144 wird ein Verfahren zur Herstellung eines mehrschichtigen Überzugs der oben beschriebenen Art beschrieben, bei dem wäßrige Basisbeschichtungszusammensetzungen eingesetzt werden, die ein über ein zweistufiges Emulsionspolymerisationsverfahren erhältliches, wasserverdünnbares Emulbionspolymer enthalten, das in der zweiten Stufe ("Schale") einen sehr hohen Anteil an Säuregruppen aufweist und bei dem sich die erste und zweite Polymerstufe in ihren Glasübergangstemperaturen derart unterscheiden, daß die erste Stufe eine tiefere Glasübergangstemperatur aufweist als die zweite Stufe.In the unpublished EP-A-332 011 aqueous coating compositions are disclosed which can be used as wood lacquers and which contain a water-thinnable emulsion polymer which is free of hydroxyl groups and can be obtained via a two-stage emulsion polymerization process. U.S. Patent 4,150,005 discloses aqueous coating compositions containing a water-thinnable emulsion polymer which can be obtained by preparing a highly hydrophilic polymer with a low glass transition temperature in a first emulsion polymerization stage and in its presence in a second emulsion polymerization stage a hydrophobic polymer with a high glass transition temperature is produced. Multi-layer protective and / or decorative coatings of the type described above and the problems encountered in the manufacture of these coatings are not addressed in U.S. Patent No. 4,150,005. GB-A-2,034,334 describes aqueous coating compositions which contain a water-thinnable emulsion polymer which can be obtained via a two-stage emulsion polymerisation process and which must have N-methylol groups. GB-A-2,034,334 is not indicative of the fact that the two polymer stages have to differ in their glass transition temperatures in the manner according to the invention. Multilayer protective and / or decorative coatings of the type described above and the problems encountered in the manufacture of these coatings are not addressed in GB-A-2,034,334. EP-A-287 144 describes a process for producing a multilayer coating of the type described above, in which aqueous base coating compositions are used which contain a water-dilutable emulsification polymer which can be obtained via a two-stage emulsion polymerization process and which in the second stage ("shell" ) has a very high proportion of acid groups and in which the first and second polymer stages differ in their glass transition temperatures in such a way that the first stage has a lower glass transition temperature than the second stage.
Die erfindungsgemäß eingesetzten wasserverdünnbaren Emulsionspolymere sind durch eine zweistufige Emulsionspolymerisation in einem wäßrigen Medium in den bekannten Apparaturen, beispielsweise in einem Rührkessel mit Heiz- und Kühlvorrichtung, herstellbar. Die Zugabe der Monomeren kann in der Weise erfolgen, daß eine Lösung aus dem gesamten Wasser, dem Emulgator und einem Teil des Initiators vorgelegt wird und das Monomer bzw. Monomerengemisch und getrennt davon, aber parallel dazu der Rest des Initiators bei der Polymerisationstemperatur langsam zugegeben wird. Es ist jedoch auch möglich, einen Teil des Wassers und des Emulgators vorzulegen und aus dem Rest des Wassers und des Emulgators und aus dem Monomer bzw. Monomerengemisch eine Voremulsion herzustellen, die bei der Polymerisationstemperatur langsam zugegeben wird, wobei der Initiator wiederum getrennt zugegeben wird.
Es ist bevorzugt, in der ersten Stufe das Monomer bzw. Mono- merengemisch in Form einer Voremulsion zuzugeben und in der zweiten Stufe das Monomer bzw. Monomerengemisch in Substanz, d.h. ohne Wasser und Emulgator zuzugeben und den Initiator getrennt, aber parallel dazu zuzugeben. Es ist besonders bevorzugt, in der ersten Stufe aus einem Teil (in der Regel etwa 30 Gew.-% der insgesamt einzusetzenden Voremulsion) der in der ersten Stufe einzusetzenden Voremulsion zuerst ein Saatpolymer herzustellen und danach den Rest der in der ersten Stufe einzusetzenden Voremulsion zuzugeben. Die Polymerisationstemperatur liegt im allgemeinen im Bereich von 20 bis 100°C, vorzugsweise 40 bis 90°C.The water-dilutable emulsion polymers used according to the invention are, in a known manner, for example in a stirred tank, by a two-stage emulsion polymerization in an aqueous medium with heating and cooling device, producible. The monomers can be added in such a way that a solution of all of the water, the emulsifier and part of the initiator is introduced and the monomer or monomer mixture and separately therefrom, but in parallel the rest of the initiator is slowly added at the polymerization temperature. However, it is also possible to introduce some of the water and the emulsifier and to prepare a pre-emulsion from the rest of the water and the emulsifier and from the monomer or monomer mixture, which is added slowly at the polymerization temperature, the initiator again being added separately.
It is preferred in the first stage to add the monomer or monomer mixture in the form of a pre-emulsion and in the second stage to add the monomer or monomer mixture in bulk, ie without water and emulsifier, and to add the initiator separately but in parallel. It is particularly preferred in the first stage to first prepare a seed polymer from a part (generally about 30% by weight of the total pre-emulsion to be used) of the pre-emulsion to be used in the first stage and then to add the rest of the pre-emulsion to be used in the first stage . The polymerization temperature is generally in the range from 20 to 100 ° C., preferably 40 to 90 ° C.
Das Mengenverhältnis zwischen den Monomeren und dem Wasser kann so ausgewählt werden, daß die resultierende Dispersion einen Feststoffgehalt von 30 bis 60 Gew.-%, vorzugsweise 35 bis 50 Gew.-% aufweist.The quantitative ratio between the monomers and the water can be selected so that the resulting dispersion has a solids content of 30 to 60% by weight, preferably 35 to 50% by weight.
Als Emulgator wird vorzugsweise ein anionischer Emulgator allein oder im Gemisch eingesetzt.An anionic emulsifier is preferably used alone or in a mixture as the emulsifier.
Beispiele für anionische Emulgatoren sind die Alkalisalze von Schwefelsäurehalbestern von Alkylphenolen oder Alkoholen, ferner die Schwefelsäurehalbester von oxethylierten Alkylphenolen oder oxethylierten Alkoholen, vorzugsweise die Alkalisalze des Schwefelsäurehalbesters eines mit 4 - 5 Mol Ethylenoxid pro Mol umgesetzten Nonylphenols, Alkyl- oder Arylsulfonats, Natriumlaurylsulfat, Natriumlaurylethoxylatsulfat und sekundäre Natriumalkansulfonate, deren Kohlenstoffkette 8 - 20 Kohlenstoffatome enthält. Die Menge des anionischen Emulgators beträgt 0,1 - 5,0 Gew.-%, bezogen auf die Monomeren, vorzugsweise 0,5 - 3,0 Gew.-%. Ferner kann zur Erhöhung der Stabilität der wässrigen Dispersionen zusätzlich ein nichtionischer Emulgator vom Typ eines ethoxylierten Alkylphenols oder Fettalkohols, z.B. ein Additionsprodukt von 1 Mol Nonylphenol und 4 - 30 Mol Ethylenoxid in Mischung mit dem anionischen Emulgator eingesetzt werden.Examples of anionic emulsifiers are the alkali metal salts of sulfuric acid half-esters of alkylphenols or alcohols, furthermore the sulfuric acid half-esters of oxethylated alkylphenols or oxethylated alcohols, preferably the alkali metal salts of sulfuric acid half-esters of a nonylphenol, alkyl or with 4-5 moles of ethylene oxide per mole Aryl sulfonate, sodium lauryl sulfate, sodium lauryl ethoxylate sulfate and secondary sodium alkane sulfonates, the carbon chain of which contains 8-20 carbon atoms. The amount of the anionic emulsifier is 0.1-5.0% by weight, based on the monomers, preferably 0.5-3.0% by weight. In addition, to increase the stability of the aqueous dispersions, a nonionic emulsifier of the ethoxylated alkylphenol or fatty alcohol type, for example an addition product of 1 mol of nonylphenol and 4-30 mol of ethylene oxide, can be used in a mixture with the anionic emulsifier.
Als radikalbildender Initiator wird vorzugsweise eine Peroxidverbindung eingesetzt. Der Initiator ist wasserlöslich oder monomerlöslich. Vorzugsweise wird ein wasserlöslicher Initiator verwendet.A peroxide compound is preferably used as the radical-forming initiator. The initiator is water-soluble or monomer-soluble. A water-soluble initiator is preferably used.
Als Initiatoren eignen sich die üblichen anorganischen Perverbindungen, wie Ammoniumpersulfat, Kaliumpersulfat, Ammonium- oder Alkalimetallperoxydiphosphat und organische Peroxide, wie z.B. Benzoylperoxid, organische Perester, wie Perisopivalat, zum Teil in Kombination mit Reduktionsmitteln, wie Natriumdisulfit, Hydrazin, Hydroxylamin und katalytische Mengen Beschleuniger, wie Eisen-, Kobalt-, Cer- und Vanadylsalze eingesetzt, vorzugsweise Alkali- bzw. Ammoniumperoxydisulfate. Es können auch die Redox-Initiatorsysteme, die in der EP-A-107300 offenbart werden, eingesetzt werden.Suitable initiators are the customary inorganic per compounds, such as ammonium persulfate, potassium persulfate, ammonium or alkali metal peroxydiphosphate and organic peroxides, such as e.g. Benzoyl peroxide, organic peresters, such as perisopivalate, partly in combination with reducing agents, such as sodium disulfite, hydrazine, hydroxylamine and catalytic amounts of accelerators, such as iron, cobalt, cerium and vanadyl salts, preferably alkali metal or ammonium peroxydisulfates. The redox initiator systems disclosed in EP-A-107300 can also be used.
In der ersten Stufe werden 10 bis 90, vorzugsweise 35 bis 65 Gewichtsteile eines ethylenisch ungesättigten Monomeren oder eines Gemisches aus ethylenisch ungesättigten Monomeren emulsionspolymerisiert. Das in der ersten Stufe eingesetzte Monomer bzw. Monomerengemisch wird so ausgewählt, daß bei völliger Auspolymerisation des in der ersten Stufe eingesetzten Monomers bzw. Monomerengemisches ein Polymer mit einer Glasübergangstemperatur (TG1) von + 30°C bis + 110°C, vorzugsweise 60 bis 95°C erhalten wird. Da die Glasüber- gangstemperatur von Emulsionspolymeren nach der Gleichung
- TG
- = Glasübergangstemp. des Copolymers in °K
- Wn
- = Gewichtsanteil des n-ten Monomers
- TGn
- = Glasübergangstemp. des Homopolymers aus dem n-ten Monomer
- x
- = Anzahl der verschiedenen Monomeren
näherungsweise berechnet werden kann, bereitet es dem Fachmann keine Probleme, das in der ersten Stufe einzusetzende Monomer bzw. Monomerengemisch so auszuwählen, daß bei völliger Auspolymerisation des in der ersten Stufe eingesetzten Monomers bzw. Monomerengemisches ein polymer mit einer Glasübergangstemperatur (TG1) von + 30 bis + 110°C, vorzugsweise 60 bis 95°C erhalten wird.
- T G
- = Glass transition temp. of the copolymer in ° K
- W n
- = Weight fraction of the nth monomer
- T Gn
- = Glass transition temp. of the homopolymer from the nth monomer
- x
- = Number of different monomers
can approximately be calculated, the person skilled in the art has no problem selecting the monomer or monomer mixture to be used in the first stage such that, when the monomer or monomer mixture used in the first stage is completely polymerized out, a polymer having a glass transition temperature (T G1 ) of + 30 to + 110 ° C, preferably 60 to 95 ° C is obtained.
Als Beispiele für Monomere, die in der ersten Stufe eingesetzt werden können, werden genannt: vinylaromatische Kohlenwasserstoffe, wie Styrol, α -Alkylstyrol und Vinyltoluol, Ester der Acrylsäure oder Methacrylsäure, insbesondere aliphatische und cycloaliphatische Acrylate oder Methacrylate mit bis zu 20 Kohlenstoffatomen im Alkoholrest, wie z.B. Methyl-, Ethyl-, Propyl-, Butyl-, Hexyl-, Ethylhexyl-, Stearyl-, Lauryl- und Cyclohexylacrylat oder -methacrylat, Acryl- und/oder Methacrylsäure, Acryl- und/oder Methacrylamid, N-Methylolacrylamid und/oder N-Methylolmethacrylamid, Hydroxyalkylester der Acrylsäure,Methacrylsäure oder einer anderenα ,β-ethylenisch ungesättigten Carbonsäure, wie z.B. 2-Hydroxyethylacrylat, 2-Hydroxypropylacrylat, 3-Hydroxypropylacrylat, 2-Hydroxypropylmethacrylat, 3-Hydroxypropylmethacrylat, 2-Hydroxyethylmethacrylat, 4-Hydroxybutylacrylat, 4-Hydroxybutylmethacrylat usw.Examples of monomers which can be used in the first stage are: vinylaromatic hydrocarbons, such as styrene, α-alkylstyrene and vinyltoluene, esters of acrylic acid or methacrylic acid, in particular aliphatic and cycloaliphatic acrylates or methacrylates with up to 20 carbon atoms in the alcohol radical, such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl, lauryl and cyclohexyl acrylate or methacrylate, acrylic and / or methacrylic acid, acrylic and / or methacrylamide, N-methylolacrylamide and / or N-methylol methacrylamide, hydroxyalkyl esters of acrylic acid, methacrylic acid or another α, β-ethylenically unsaturated carboxylic acid, such as 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 3-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl methacrylate, 2-hydroxyethyl methacrylate, 4-hydroxyethyl methacrylate, 4-hydroxyl acrylate 4-hydroxybutyl methacrylate etc.
In der ersten Stufe werden vorzugsweise ethylenisch ungesättigte Monomere bzw. Gemische aus ethylenisch ungesättigten Monomeren eingesetzt, die im wesentlichen frei von Hydroxyl- und Carboxylgruppen sind. "Im wesentlichen frei" soll bedeuten, daß es bevorzugt ist, Monomere bzw. Monomerengemische einzusetzen, die frei von Hydroxyl- und Carboxylgruppen sind, daß die eingesetzten Monomere bzw. Monomerengemische aber auch geringe Mengen (z.B. infolge von Verunreinigungen) an Hydroxyl- und/oder Carboxylgruppen enthalten können. Der Gehalt an Hydroxyl- und Carboxylgruppen sollte vorzugsweise höchstens so hoch sein, daß ein aus dem in der ersten Stufe eingesetzten Monomer bzw. Monomerengemisch hergestelltes Polymer eine OH-Zahl von höchstens 5 und eine Säurezahl von höchstens 3 aufweist.In the first stage, preference is given to using ethylenically unsaturated monomers or mixtures of ethylenically unsaturated monomers which are essentially free of hydroxyl and carboxyl groups. "Substantially free" is intended to mean that it is preferred to use monomers or monomer mixtures which are free from hydroxyl and carboxyl groups, but that the monomers or monomer mixtures used also contain small amounts (for example as a result of impurities) of hydroxyl and / or may contain carboxyl groups. The content of hydroxyl and carboxyl groups should preferably be at most so high that a polymer prepared from the monomer or monomer mixture used in the first stage has an OH number of at most 5 and an acid number of at most 3.
In der ersten Stufe wird besonders bevorzugt ein Gemisch aus
- (a1) 100 bis 60, vorzugsweise 99,5 bis 75 Gew.-% eines cycloaliphatischen oder aliphatischen Esters der Methacrylsäure oder Acrylsäure oder eines Gemisches aus solchen Estern und
- (a2) 0 bis 40, vorzugsweise 0,5 bis 25 Gew.-% eines mit (a1) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren
eingesetzt, wobei die Summe der Gewichtsanteile von (a1) und (a2) stets 100 Gew.-% ergibt.In the first stage, a mixture of is particularly preferred
- (a1) 100 to 60, preferably 99.5 to 75% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters and
- (a2) 0 to 40, preferably 0.5 to 25% by weight of a monomer copolymerizable with (a1) or a mixture of such monomers
used, the sum of the proportions by weight of (a1) and (a2) always giving 100% by weight.
Als Komponente (a1) können z.B. eingesetzt werden: Cyclohexylacrylat, Cyclohexylmethacrylat, Alkylacrylate und Alkylmethacrylate mit bis zu 20 Kohlenstoffatomen im Alkylrest, wie z.B. Methyl-, Ethyl-, Propyl-, Butyl-, Hexyl-, Ethylhexyl-, Stearyl- und Laurylacrylat und -methacrylat oder Gemische aus diesen Monomeren.As component (a1) can be used, for example: cyclohexyl acrylate, cyclohexyl methacrylate, alkyl acrylates and alkyl methacrylates with up to 20 carbon atoms in the alkyl radical, such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl and lauryl acrylate and methacrylate or mixtures of these monomers.
Als Komponente (a2) können z.B. eingesetzt werden vinylaromatische Kohlenwasserstoffe, wie Styrol, α-Alkylstyrol und Vinyltoluol, Acryl und Methacrylamid und Acryl- und Methacrylnitril oder Gemische aus diesen Monomeren.As component (a2) e.g. vinylaromatic hydrocarbons such as styrene, α-alkylstyrene and vinyltoluene, acrylic and methacrylamide and acrylonitrile and methacrylonitrile or mixtures of these monomers are used.
Nachdem mindestens 80 Gew.-%, vorzugsweise mindestens 95 Gew.-% des in der ersten Stufe eingesetzten ethylenisch ungesättigten Monomers bzw. Monomerengemisches umgesetzt worden sind, werden in einer zweiten Stufe 90 bis 10, vorzugsweise 65 bis 35 Gewichtsteile eines ethylenisch ungesättigten Monomeren oder eines Gemisches aus ethylenisch ungesättigten Monomeren in Gegenwart des in der ersten Stufe erhaltenen Polymers emulsionspolymerisiert, wobei das in der zweiten Stufe eingesetzte Monomer bzw. Monomerengemisch so ausgewählt wird, daß eine alleinige Polymerisation des in der zweiten Stufe eingesetzten Monomers bzw. Monomerengemisches zu einem Polymer mit einer Glasübergangstemperatur (TG2) von -60 bis +20°C, vorzugsweise -50 bis 0°C führen würde. Diese Auswahl bereitet dem Fachmann keine Schwierigkeiten, da die Glasübergangstemperaturen von Emulsionspolymeren - wie oben bereits dargelegt - leicht näherungsweise berechnet werden können.After at least 80% by weight, preferably at least 95% by weight, of the ethylenically unsaturated monomer or monomer mixture used in the first stage has been reacted, 90 to 10, preferably 65 to 35 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers is emulsion polymerized in the presence of the polymer obtained in the first stage, the monomer or monomer mixture used in the second stage being selected such that a sole polymerization of the monomer or monomer mixture used in the second stage into a polymer with a glass transition temperature (T G2 ) of -60 to + 20 ° C, preferably -50 to 0 ° C would lead. This selection presents no difficulties for the person skilled in the art, since the glass transition temperatures of emulsion polymers - as already explained above - can easily be approximately calculated.
Es ist weiter erfindungswesentlich, daß das in der ersten Stufe eingesetzte Monomer bzw. Monomerengemisch und das in der zweiten Stufe eingesetzte Monomer bzw. Monomerengemisch in der Art und Menge so ausgewählt werden, daß das erhaltene Emulsionspolymer eine Hydroxylzahl von 2 bis 100, vorzugsweise von 10 bis 50 aufweist und die Differenz TG1 - TG2 10 bis 170, vorzugsweise 80 bis 150°C beträgt.It is further essential to the invention that the monomer or monomer mixture used in the first stage and the monomer or monomer mixture used in the second stage are selected in such a way that the emulsion polymer obtained has a hydroxyl number of 2 to 100, preferably 10 to 50 and the difference T G1 - T G2 is 10 to 170, preferably 80 to 150 ° C.
Als Beispiele für Monomere, die in der zweiten Stufe eingesetzt werden können, werden genannt: vinylaromatische Kohlenwasserstoffe, wie Styrol, α-Alkylstyrol und Vinyltoluol, Ester der Acrylsäure oder Methacrylsäure, insbesondere aliphatische und cycloaliphatische Acrylate oder Methacrylate mit bis zu 20 Kohlenstoffatomen im Alkoholrest, wie z.B. Methyl-, Ethyl-, Propyl-, Butyl-, Hexyl-, Ethylhexyl-, Stearyl-, Lauryl- und Cyclohexylacrylat oder -methacrylat, Acryl- und/oder Methacrylsäure, Acryl und/oder Methacrylamid, N-Methylolacrylamid und/oder N-Methylolmethacrylamid, Hydroxyalkylester der Acrylsäure, Methacrylsäure oder einer anderenα, β-ethylenisch ungesättigten Carbonsäure, wie z.B. 2-Hydroxyethylacrylat, 2-Hydroxypropylacrylat, 3-Hydroxypropylacrylat, 2-Hydroxypropylmethacrylat, 3-Hydroxypropylmethacrylat, 2-Hydroxyethylmethacrylat, 4-Hydroxybutylacrylat, 4-Hydroxybutylmethacrylat usw.Examples of monomers which can be used in the second stage are: vinylaromatic hydrocarbons, such as styrene, α-alkylstyrene and vinyltoluene, Esters of acrylic acid or methacrylic acid, in particular aliphatic and cycloaliphatic acrylates or methacrylates with up to 20 carbon atoms in the alcohol radical, such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl, lauryl and cyclohexyl acrylate or - methacrylate, acrylic and / or methacrylic acid, acrylic and / or methacrylamide, N-methylolacrylamide and / or N-methylolmethacrylamide, hydroxyalkyl esters of acrylic acid, methacrylic acid or another α, β-ethylenically unsaturated carboxylic acid, such as 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 3-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl methacrylate, 2-hydroxyethyl methacrylate, 4-hydroxybutyl acrylate, 4-hydroxybutyl methacrylate, etc.
In der zweiten Stufe wird vorzugsweise ein Gemisch aus
- (b1) 47 bis 99, vorzugsweise 75 bis 90 Gew.-% eines cycloaliphatischen oder aliphatischen Esters der Methacrylsäure oder Acrylsäure oder eines Gemisches aus solchen Estern
- (b2) 1 bis 20, vorzugsweise 5 bis 15 Gew.-% eines mindestens eine Hydroxylgruppe tragenden mit (b1), (b3) und (b4) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren
- (b3) 0 bis 8, vorzugsweise 2 bis 6 Gew.-% eines mindestens eine Carboxyl- oder Sulfonsäuregruppe tragenden, mit (b1), (b2) und (b4) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren und
- (b4) 0 bis 25, vorzugsweise 2 bis 15 Gew.-% eines weiteren mit (b1), (b2) und (b3) copolymerisierbaren Monomeren oder eines Gemisches aus solchen Monomeren eingesetzt, wobei die Summe der Gewichtsanteile von (b1), (b2), (b3) und (b4) stets 100 Gew. % ergibt.
- (b1) 47 to 99, preferably 75 to 90% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters
- (b2) 1 to 20, preferably 5 to 15% by weight of a monomer carrying at least one hydroxyl group and copolymerizable with (b1), (b3) and (b4) or a mixture of such monomers
- (b3) 0 to 8, preferably 2 to 6% by weight of a monomer carrying at least one carboxyl or sulfonic acid group and copolymerizable with (b1), (b2) and (b4) or a mixture of such monomers and
- (b4) 0 to 25, preferably 2 to 15% by weight of a further monomer which can be copolymerized with (b1), (b2) and (b3) or a mixture of such monomers used, the sum of the parts by weight of (b1), (b2), (b3) and (b4) always giving 100% by weight.
Als Komponente (b1) können z.B. eingesetzt werden: Cyclohexylacrylat, Cyclohexylmethacrylat, Alkylacrylate und Alkylmethacrylate mit bis zu 20 Kohlenstoffatomen im Alkylrest, wie z.B. Methyl-, Ethyl-, Propyl-, Butyl-, Hexyl-, Ethylhexyl-, Stearyl- und Laurylacrylat und -methacrylat oder Gemische aus diesen Monomeren.As component (b1) e.g. are used: cyclohexyl acrylate, cyclohexyl methacrylate, alkyl acrylates and alkyl methacrylates with up to 20 carbon atoms in the alkyl radical, such as e.g. Methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl and lauryl acrylate and methacrylate or mixtures of these monomers.
Als Komponente (b2) können z.B. eingesetzt werden: Hydroxyalkylester der Acrylsäure, Methacrylsäure oder einer anderen α,β-ethylenisch ungesättigten Carbonsäure. Diese Ester können sich von einem Alkylenglykol ableiten, das mit der Säure verestert ist, oder sie können durch Umsetzung der Säure mit einem Alkylenoxid erhalten werden. Als Komponente (b2) werden vorzugsweise Hydroxyalkylester der Acrylsäure und Methacrylsäure, in denen die Hydroxyalkylgruppe bis zu 4 Kohlenstoffatome enthält, oder Mischungen aus diesen Hydroxyalkylestern eingesetzt. Als Beispiele für derartige Hydroxyalkylester werden 2-Hydroxyethylacrylat, 2-Hydroxypropylacrylat, 3-Hydroxypropylacrylat, 2-Hydroypropylmethacrylat, 3-Hydroxypropylmethacrylat, 2-Hydroxyethylmethacrylat, 4-Hydroxybutylacrylat oder 4-Hydroxybutylmethacrylat genannt. Entsprechende Ester von anderen ungesättigten Säuren, wie z.B. Ethacrylsäure, Crotonsäure und ähnliche Säuren mit bis zu etwa 6 Kohlenstoffatomen pro Molekül können auch eingesetzt werden.
Als Komponente (b3) werden vorzugsweise Acrylsäure und/oder Methacrylsäure und/oder Acrylamidomethylpropansulfonsäure eingesetzt. Es können aber auch andere ethylenisch ungesättigte Säuren mit bis zu 6 Kohlenstoffatomen im Molekül eingesetzt werden. Als Beispiele für solche Säuren werden Ethacrylsäure, Crotonsäure, Maleinsäure, Fumarsäure und Itaconsäure genannt.The following can be used as component (b2): hydroxyalkyl esters of acrylic acid, methacrylic acid or another α, β-ethylenically unsaturated carboxylic acid. These esters can be derived from an alkylene glycol esterified with the acid, or can be obtained by reacting the acid with an alkylene oxide. Hydroxyalkyl esters of acrylic acid and methacrylic acid, in which the hydroxyalkyl group contains up to 4 carbon atoms, or mixtures of these hydroxyalkyl esters are preferably used as component (b2). Examples of such hydroxyalkyl esters are 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 3-hydroxypropyl acrylate, 2-hydroypropyl methacrylate, 3-hydroxypropyl methacrylate, 2-hydroxyethyl methacrylate, 4-hydroxybutyl acrylate or 4-hydroxybutyl methacrylate. Corresponding esters of other unsaturated acids, such as ethacrylic acid, crotonic acid and similar acids with up to about 6 carbon atoms per molecule, can also be used.
Acrylic acid and / or methacrylic acid and / or acrylamidomethylpropanesulfonic acid are preferably used as component (b3). However, other ethylenically unsaturated acids with up to 6 carbon atoms in the molecule can also be used. Examples of such acids are ethacrylic acid, crotonic acid, maleic acid, fumaric acid and itaconic acid.
Als Komponente (b4) können z.B. eingesetzt werden: vinylaromatische Kohlenwasserstoffe, wie Styrol, α-Alkylstyrol und Vinyltoluol, Acryl- und Methacrylamid und Acryl- und Methacrylnitril oder Gemische aus diesen Monomeren.As component (b4) e.g. are used: vinyl aromatic hydrocarbons, such as styrene, α-alkylstyrene and vinyl toluene, acrylic and methacrylamide and acrylonitrile and methacrylonitrile, or mixtures of these monomers.
Das erfindungsgemäß eingesetzte Emulsionspolymer sollte eine zahlenmittlere Molmasse (Bestimmung: gelpermeationschromatographisch mit Polystyrol als Standard) von 200.000 bis 2.000.000, vorzugsweise von 300.000 bis 1.500.000 aufweisen.The emulsion polymer used according to the invention should have a number average molar mass (determination: gel permeation chromatography using polystyrene as the standard) of 200,000 to 2,000,000, preferably 300,000 to 1,500,000.
Dem Fachmann ist bekannt, wie er die Reaktionsbedingungen während der Emulsionspolymerisation zu wählen hat, damit er Emulsionspolymere erhält, die die oben angegebenen zahlenmittleren Molmassen aufweisen (vgl. z.B. Chemie, Physik und Technologie der Kunststoffe in Einzeldarstellungen, Dispersionen synthetischer Hochpolymerer, Teil 1 von F. Hölscher, Springer Verlag, Berlin, Heidelberg, New York, 1969).The person skilled in the art knows how to select the reaction conditions during the emulsion polymerization in order to obtain emulsion polymers which have the number-average molar masses given above (see, for example, chemistry, physics and technology of the plastics in individual representations, dispersions of synthetic high polymers, part 1 of F Hölscher, Springer Verlag, Berlin, Heidelberg, New York, 1969).
Es ist bevorzugt, daß die erfindungsgemäßen wäßrigen Basisbeschichtungszusammensetzungen neben dem oben beschriebenen Emulsionspolymer noch ein wasserverdünnbares Polyurethanharz als filmbildendes Material enthalten.It is preferred that the aqueous base coating compositions according to the invention contain, in addition to the emulsion polymer described above, a water-dilutable polyurethane resin as the film-forming material.
Die erfindungsgemäßen Basisbeschichtungszusammensetzungen enthalten vorzugsweise wasserverdünnbare, Harnstoffgruppen enthaltende Polyurethanharze, die ein zahlenmittleres Molekulargewicht (Bestimmung: gelpermeationschromatographisch mit Polystyrol als Standard) von 1000 bis 60.0000, vorzugsweise 1500 bis 50.000 und eine Säurezahl von 5 bis 70, vorzugsweise 10 bis 30 aufweisen und durch Umsetzung, vorzugsweise Kettenverlängerung von Isocyanatgruppen aufweisenden Präpolymeren mit Polyaminen und/oder Hydrazin herstellbar sind.The base coating compositions according to the invention preferably contain water-thinnable, urea-containing polyurethane resins which have a number average molecular weight (determination: gel permeation chromatography using polystyrene as the standard) of 1000 to 60,000, preferably 1500 to 50,000 and an acid number of 5 to 70, preferably 10 to 30 and by reaction, preferably chain extension of prepolymers containing isocyanate groups with polyamines and / or hydrazine can be produced.
Die Herstellung des isocyanatgruppenhaltigen präpolymeren kann durch Reaktion von Polyalkoholen mit einer Hydroxylzahl von 10 bis 1800, bevorzugt 50 bis 500, mit überschüssigen Polyisocyanaten bei Temperaturen bis zu 150°C, bevorzugt 50 bis 130°C, in organischen Lösemitteln, die nicht mit Isocyanaten reagieren können,-erfolgen. Das Äquivalenzverhältnis von NCO zu OH-Gruppen liegt zwischen 1,5 und 1,0 zu 1,0, bevorzugt zwischen 1,4 und 1,2 zu 1. Die zur Herstellung des Präpolymeren eingesetzten Polyole können niedrigmolekular und/oder hochmolekular sein und sie können reaktionsträge anionische Gruppen enthalten.The prepolymer containing isocyanate groups can be prepared by reacting polyalcohols having a hydroxyl number from 10 to 1800, preferably 50 to 500, with excess polyisocyanates at temperatures up to 150 ° C., preferably 50 to 130 ° C., in organic solvents which do not react with isocyanates can, succeed. The equivalence ratio of NCO to OH groups is between 1.5 and 1.0 to 1.0, preferably between 1.4 and 1.2 to 1. The polyols used to prepare the prepolymer can be low molecular weight and / or high molecular weight and they can contain inert anionic groups.
Um die Härte des Polyurethans zu erhöhen, kann man niedrigmolekulare Polyole einsetzen. Sie haben ein Molekulargewicht von 60 bis zu etwa 400 und können aliphatische, alicyclische oder aromatische Gruppen enthalten. Es werden dabei Mengen bis zu 30 Gew.-% der gesamten Polyol-Bestandteile, bevorzugt etwa 2 bis 20 Gew.-% eingesetzt. Vorteilhaft sind die niedermolekularen Polyole mit bis zu etwa 20 Kohlenstoffatomen je Molekül, wie Ethylenglykol, Diethylenglykol, Triethylenglykol, 1,2-Propandiol, 1,3-Propandiol, 1,4-Butandiol, 1,2-Butylenglykol, 1,6-Hexandiol, Trimethylolpropan, Rizinusöl oder hydriertes Rizinusöl, Di-trimethylolpropanether, Pentaerythrit, 1,2-Cyclohexandiol, 1,4-Cyclohexandimethanol, Bisphenol A, Bisphenol F, Neopentylglykol, Hydroxypivalinsäure-neopentylglykolester, hydroxyethyliertes oder hydroxypropyliertes Bisphenol A, hydriertes Bisphenol A und deren Mischungen.
Um ein NCO-Präpolymeres hoher Flexibilität zu erhalten, sollte ein hoher Anteil eines überwiegend lineares Polyols mit einer bevorzugten Hydroxylzahl von 30 bis 150 zugesetzt werden. Bis zu 97 Gew.-% des gesamten Polyols können aus gesättigten und ungesättigten Polyestern und/oder Polyethern mit einer Molmasse
Die zur Herstellung der Polyester verwendeten Diole bestehen beispielsweise aus Alkylenglykolen, wie Ethylenglykol, Propylenglykol, Butylenglykol, Butandiol-1,4, Hexandiol-1,6, Neopentylglykol und andere Diole, wie Dimethylcyclohexan. Die Säurekomponente des Polyesters besteht in erster Linie aus niedermolekularen Dicarbonsäuren oder ihren Anhydriden mit 2 bis 30, bevorzugt 4 bis 18 Kohlenstoffatomen im Molekül. Geeignete Säure sind beispielsweise o-Phthalsäure, Isophthalsäure, Terephthalsäure, Tetrahydrophthalsäure, Cyclohexandicarbonsäure, Bernsteinsäure, Adipinsäure, Azelainsäure, Sebazinsäure, Maleinsäure, Fumarsäure, Glutarsäure, Hexachlorheptandicarbonsäure, Tetrachlorphthalsäure und/oder dimersisierte Fettsäuren. Anstelle dieser Säuren können auch ihre Anhydride, soweit diese existieren, verwendet werden. Bei der Bildung von Polyesterpolyolen können auch kleinere Mengen an Carbonsäuren mit 3 oder mehr Carboxylgruppen, beispielsweise Trimellithsäureanhydrid oder das Addukt von Maleinsäureanhydrid an ungesättigten Fettsäuren anwesend sein.Low molecular weight polyols can be used to increase the hardness of the polyurethane. They have a molecular weight from 60 to about 400 and can contain aliphatic, alicyclic or aromatic groups. Amounts of up to 30% by weight of the total polyol constituents, preferably about 2 to 20% by weight, are used. The low molecular weight polyols with up to about 20 carbon atoms per molecule, such as ethylene glycol, diethylene glycol, triethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, 1,2-butylene glycol, 1,6-hexanediol, are advantageous , Trimethylolpropane, castor oil or hydrogenated castor oil, di-trimethylolpropane ether, pentaerythritol, 1,2-cyclohexanediol, 1,4-cyclohexanedimethanol, bisphenol A, bisphenol F, neopentylglycol, hydroxypivalic acid-neopentylglycol ester, hydroxyethylated or hydroxypropylated bisphenol A, bisphenol A, mixtures thereof .
In order to obtain a high flexibility NCO prepolymer, a high proportion of a predominantly linear polyol with a preferred hydroxyl number of 30 to 150 should be added. Up to 97% by weight of the total polyol can consist of saturated and unsaturated polyesters and / or polyethers with a molecular weight
The diols used to prepare the polyesters consist, for example, of alkylene glycols, such as ethylene glycol, propylene glycol, butylene glycol, 1,4-butanediol, 1,6-hexanediol, neopentyl glycol and other diols, such as dimethylcyclohexane. The acid component of the polyester consists primarily of low molecular weight dicarboxylic acids or their anhydrides with 2 to 30, preferably 4 to 18, carbon atoms in the molecule. Suitable acids are, for example, o-phthalic acid, isophthalic acid, terephthalic acid, tetrahydrophthalic acid, cyclohexanedicarboxylic acid, succinic acid, adipic acid, azelaic acid, sebacic acid, maleic acid, fumaric acid, glutaric acid, hexachlorheptanedicarboxylic acid, tetrachlorophthalic acid and / or. Instead of these acids, their anhydrides, if they exist, can also be used. When forming polyester polyols, smaller ones can also be used Amounts of carboxylic acids with 3 or more carboxyl groups, for example trimellitic anhydride or the adduct of maleic anhydride with unsaturated fatty acids, are present.
Erfindungsgemäß werden auch Polyesterdiole eingesetzt, die durch Umsetzung eines Lactons mit einem Diol erhalten werden. Sie zeichnen sich durch die Gegenwart einer endständigen Hydroxylgruppe und wiederkehrende Polyesteranteil der Formel -(-CO-(CHR)n-CH₂-0-)- aus. Hierbei ist n bevorzugt 4 bis 6 und der Substituent R Wasserstoff, ein Alkyl-, Cycloalkyl- oder Alkoxy-Rest. Kein Substituent enthält mehr als 12 Kohlenstoffatome. Die gesamte Anzahl der Kohlenstoffatome im Substituenten übersteigt nicht 12 pro Lactonring. Beispiele hierfür sind Hydroxycapronsäure, Hydroxybuttersäure, Hydroxydecansäure und/oder Hydroxystearinsäure. Das als Ausgangsmaterial verwendete Lacton kann durch die folgende allgemeine Formel dargestellt werden
in der n und R die bereits angegebene Bedeutung haben. Für die Herstellung der Polyesterdiole wird das unsubstituierte -Caprolacton, bei dem n den Wert 4 hat und alle R-Substituenten Wasserstoff sind, bevorzugt. Die Umsetzung mit Lacton wird durch niedermolekulare Polyole, wie Ethylenglykol, 1,3-Propandiol, 1,4-Butandiol, Dimethylolcyclohexan gestartet. Es können jedoch auch andere Reaktionskomponenten, wie Ethylendiamin, Alkyldiakanolamine oder auch Harnstoff mit Caprolacton umgesetzt werden.According to the invention, polyester diols are also used which are obtained by reacting a lactone with a diol. They are characterized by the presence of a terminal hydroxyl group and recurring polyester content of the formula - (- CO- (CHR) n -CH₂-0 -) -. Here, n is preferably 4 to 6 and the substituent R is hydrogen, an alkyl, cycloalkyl or alkoxy radical. No substituent contains more than 12 carbon atoms. The total number of carbon atoms in the substituent does not exceed 12 per lactone ring. Examples include hydroxycaproic acid, hydroxybutyric acid, hydroxydecanoic acid and / or hydroxystearic acid. The lactone used as a raw material can be represented by the following general formula
in which n and R have the meaning already given. Unsubstituted -caprolactone, in which n has the value 4 and all R substituents are hydrogen, is preferred for the preparation of the polyester diols. The reaction with lactone is started by low molecular weight polyols, such as ethylene glycol, 1,3-propanediol, 1,4-butanediol, dimethylolcyclohexane. However, other reaction components, such as ethylenediamine, alkyldiacanolamines or urea, can also be reacted with caprolactone.
Als höhermolekulare Diole eigenen sich auch Polylactamdiole, die durch Reaktion von beispielsweise ε-Caprolactam mit niedermolekularen Diolen hergestellt werden.Also suitable as higher molecular weight diols are polylactam diols, which are produced by reacting, for example, ε-caprolactam with low molecular weight diols.
Als typische multifunktionelle Isocyanate werden verwendet aliphatische, cycloaliphatische und/oder aromatische Poly isocyanate mit mindestens zwei Isocyanatgruppen pro Molekül. Bevorzugt werden die Isomeren oder Isomerengemische von organischen Diisocyanaten. Als aromatische Diisocyanate eignen sich Phenylendiisocyanat, Toluylendiisocyanat, Xylylendiisocyanat, Biphenylendiisocyanat, Naphthylendiisocyanat und Diphenylmethandiisocyanat.
Aufgrund ihrer guten Beständigkeit gegenüber ultraviolettem Licht ergeben (cyclo)aliphatische Diisocyanate Produkte mit geringer Vergilbungsneigung. Beispiele hierfür sind Isophorondiisocyanat, Cyclopentylendiisocyant sowie die Hydrierungsprodukte der aromatischen Diisocyanate, wie Cyclohexylendiisocyanat, Methylcyclohexylendiisocyanat und Dicyclohexylmethandiisocyanat. Als Beispiele für aliphatische Diisocyanate werden Trimethylendiisocyanat, Tetramethylendiisocyanat, Pentamethylendiisocyanat, Hexamethylendiisocyanat, Propylendiisocyanat, Ethylethylendiisocyanat, Dimethylethylendiisocyanat, Methyltrimethylendiisocyanat und Trimethylhexandiisocyanat. Besonders bevorzugt werden als Diisocyanate Isophorondiisocyanat und Dicyclohexyl-methandiisocyanat. Die zur Bildung des Präpolymeren gebrauchte Polyisocyanat-Komponente kann auch einen Anteil höherwertiger Polyisocyanate enthalten, vorausgesetzt dadurch wird keine Gelbildung verursacht. Als Triisocyanate haben sich Produkte bewährt, die durch Trimerisation oder Oligomerisation von Diisocyanaten oder durch Reaktion von Diisocyanaten mit polyfunktionellen OH- oder NH-Gruppen enthaltenden Verbindungen entstehen. Hierzu gehören beispielsweise das Biuret von Hexamethylendiisocyanat und Wasser, das Isocyanurat des Hexamethylendiisocyanats oder das Addukt von Isophorondiisocyanat an Trimethylolpropan.
Die mittlere Funktionalität kann gegebenenfalls durch Zusatz von Monoisocyanaten gesenkt werden. Beispiele für solche kettenabbrechenden Monoisocyanate sind Phenylisocyanat, Cyclohexylisocyanat und Stearylisocyanat.
Polyurethane sind im allgemeinen nicht mit Wasser verträg lich, wenn nicht bei ihrer Synthese spezielle Bestandteile eingebaut und/oder besondere Herstellungsschritte vorgenommen werden. So wird eine so große Säurezahl eingebaut, daß das neutralisierte Produkt stabil in Wasser zu dispergieren ist. Hierzu dienen Verbindungen, die zwei mit Isocyanatgruppen reagierende H-aktive Gruppen und mindestens eine zur Anionenbildung befähigte Gruppe enthalten. Geeignete, mit Isocyanatgruppen reagierende Gruppen, sind insbesondere Hydoxylgruppen sowie primäre und/oder sekundäre Aminogruppen. Gruppen, die zur Anionenbildung befähigt sind, sind Carboxyl-, Sulfonsäure und/oder Phosphonsäuregruppen. Bevorzugt werden Carbonsäure- oder Carboxylatgruppen verwendet. Sie sollen so reaktionsträge sein, daß die Isocyanatgruppen des Diisocyanats vorzugsweise mit den anderen gegenüber Isocyanatgruppen reaktiven Gruppen des Moleküls reagieren. Es werden dazu Alkansäuren mit zwei Substituenten am -ständigen Kohlenstoffatöm eingesetzt. Der Substituent kann eine Hydroxylgruppe, eine Alkylgruppe oder eine Alkylolgruppe sein. Diese Polyole haben wenigstens eine, im allgemeinen 1 bis 3 Carboxylgruppen im Molekül. Sie haben zwei bis etwa 25, vorzugsweise 3 bis 10 Kohlenstoffatome. Beispiele für solche Verbindungen sind Dihydroxypropionsäure, Dihydroxybernsteinsäure und Dihydroxybenzoesäure. Eine besonders bevorzugte Gruppe von Dihydroxyalkansäuren sind dieα ,α-Dimethylolalkansäuren, die durch die Strukturformel RC(CH₂OH)₂COOH gekennzeichnet sind, worin R=Wasserstoff oder eine Alkylgruppe mit bis zu etwa 20 Kohlenstoffatomen bedeutet. Beispiele für solche Verbindungen sind 2,2-Dimethylolessigsäure, 2,2-Dimethylolpropionsäure, 2,2-Dimethylolbuttersäure und 2,2-Dimethylolpentansäure. Die bevorzugte Dihydroxyalkansäure ist 2,2-Dimethylolpropionsäure. Aminogruppenhaltige Verbindungen sind beispielsweise , -Diaminovaleriansäure, 3,4-Diaminobenzoesäure, 2,4-Diaminotoluolsulfonsäure und 2,4-Diamino-diphenylethersulfonsäure. Das Carboxylgruppen enthaltende Polyol kann 3 bis 100 Gew.-%, vorzugsweise 5 bis 50 Gew.-% des gesamten Polyolbestandteiles im NCO-Präpolymeren ausmachen.
Die durch die Carboxylgruppen-Neutralisation in Salzform verfügbare Menge an ionisierbaren Carboxylgruppen beträgt im allgemeinen wenigstens 0,4 Gew.-%, vorzugsweise wenigstens 0,7 Gew.-%, bezogen auf den Feststoff. Die obere Grenze beträgt etwa 6 Gew.-%. Die Menge an Dihydroxyalkansäuren im unneutralisierten Präpolymeren ergibt eine Säurezahl von wenigstens 5, vorzugsweise wenigstens 10. Die obere Grenze der Säurezahl liegt bei 70, vorzugsweise bei 40, bezogen auf den Feststoff.
Diese Dihydroxyalkansäure wird vor der Umsetzung mit Isocyanaten vorteilhafterweise mindestens anteilweise mit einem tertiären Amin neutralisiert, um eine Reaktion mit den Isocyanaten zu vermeiden.
Die erfindungsgmäß verwendeten NCO-Präpolymere können durch gleichzeitige Umsetzung des Polyols oder Polyolgemisches mit einem Diisocyanat-Überschuß hergestellt werden. Andererseits kann die Umsetzung auch in vorgeschriebener Reihenfolge stufenweise vorgenommen werden.
Beispiele sind in den DE 26 24 442 und DE 32 10 051 beschrieben. Die Reaktionstemperatur beträgt bis zu 150°C, wobei eine Temperatur im Bereich von 50 bis 130°C bevorzugt wird. Die Umsetzung wird fortgesetzt, bis praktisch alle Hydroxylfunktionen umgesetzt sind.Aliphatic, cycloaliphatic and / or aromatic poly are used as typical multifunctional isocyanates isocyanates with at least two isocyanate groups per molecule. The isomers or isomer mixtures of organic diisocyanates are preferred. Suitable aromatic diisocyanates are phenylene diisocyanate, tolylene diisocyanate, xylylene diisocyanate, biphenylene diisocyanate, naphthylene diisocyanate and diphenylmethane diisocyanate.
Due to their good resistance to ultraviolet light, (cyclo) aliphatic diisocyanates produce products with a low tendency to yellowing. Examples include isophorone diisocyanate, cyclopentylene diisocyanate and the hydrogenation products of aromatic diisocyanates, such as cyclohexylene diisocyanate, methylcyclohexylene diisocyanate and dicyclohexylmethane diisocyanate. Examples of aliphatic diisocyanates are trimethylene diisocyanate, tetramethylene diisocyanate, pentamethylene diisocyanate, hexamethylene diisocyanate, propylene diisocyanate, ethylethylene diisocyanate, dimethylethylene diisocyanate, methyltrimethylene diisocyanate and trimethylhexane diisocyanate. Isophorone diisocyanate and dicyclohexyl methane diisocyanate are particularly preferred as diisocyanates. The polyisocyanate component used to form the prepolymer can also contain a proportion of higher-quality polyisocyanates, provided that this does not cause gel formation. Products which have been found to be suitable as triisocyanates are those which are formed by trimerization or oligomerization of diisocyanates or by reaction of diisocyanates with compounds containing polyfunctional OH or NH groups. These include, for example, the biuret of hexamethylene diisocyanate and water, the isocyanurate of hexamethylene diisocyanate or the adduct of isophorone diisocyanate with trimethylolpropane.
The average functionality can optionally be reduced by adding monoisocyanates. Examples of such chain terminating monoisocyanates are phenyl isocyanate, cyclohexyl isocyanate and stearyl isocyanate.
Polyurethanes are generally not compatible with water Lich, if special components are not incorporated in their synthesis and / or special manufacturing steps are carried out. So large an acid number is built in that the neutralized product can be dispersed stably in water. For this purpose, compounds are used which contain two H-active groups reacting with isocyanate groups and at least one group capable of forming anions. Suitable groups which react with isocyanate groups are, in particular, hydroxyl groups and primary and / or secondary amino groups. Groups which are capable of forming anions are carboxyl, sulfonic acid and / or phosphonic acid groups. Carboxylic acid or carboxylate groups are preferably used. They should be so inert that the isocyanate groups of the diisocyanate preferably react with the other groups of the molecule that are reactive toward isocyanate groups. For this purpose, alkanoic acids with two substituents on the carbon atom are used. The substituent can be a hydroxyl group, an alkyl group or an alkylol group. These polyols have at least one, generally 1 to 3 carboxyl groups in the molecule. They have two to about 25, preferably 3 to 10, carbon atoms. Examples of such compounds are dihydroxypropionic acid, dihydroxysuccinic acid and dihydroxybenzoic acid. A particularly preferred group of dihydroxyalkanoic acids are the α, α-dimethylolalkanoic acids, which are characterized by the structural formula RC (CH₂OH) ₂COOH, in which R = hydrogen or an alkyl group having up to about 20 carbon atoms. Examples of such compounds are 2,2-dimethylol acetic acid, 2,2-dimethylol propionic acid, 2,2-dimethylol butyric acid and 2,2-dimethylol pentanoic acid. The preferred dihydroxyalkanoic acid is 2,2-dimethylolpropionic acid. Compounds containing amino groups are, for example, -diaminovaleric acid, 3,4-diaminobenzoic acid, 2,4-diaminotoluenesulfonic acid and 2,4-diaminodiphenyl ether sulfonic acid. The polyol containing carboxyl groups can be 3 to Make up 100% by weight, preferably 5 to 50% by weight, of the total polyol component in the NCO prepolymer.
The amount of ionizable carboxyl groups available through the carboxyl group neutralization in salt form is generally at least 0.4% by weight, preferably at least 0.7% by weight, based on the solid. The upper limit is about 6% by weight. The amount of dihydroxyalkanoic acids in the unneutralized prepolymer gives an acid number of at least 5, preferably at least 10. The upper limit of the acid number is 70, preferably 40, based on the solids.
Before the reaction with isocyanates, this dihydroxyalkanoic acid is advantageously at least partially neutralized with a tertiary amine in order to avoid a reaction with the isocyanates.
The NCO prepolymers used according to the invention can be prepared by simultaneously reacting the polyol or polyol mixture with an excess of diisocyanate. On the other hand, the implementation can also be carried out in stages in the prescribed order.
Examples are described in DE 26 24 442 and DE 32 10 051. The reaction temperature is up to 150 ° C, with a temperature in the range of 50 to 130 ° C being preferred. The reaction continues until practically all of the hydroxyl functions have been converted.
Das NCO-Präpolymer enthält wenigstens etwa 0,5 Gew.-% Isocyanatgruppen, vorzugsweise wenigstens 1 Gew.-% NCO, bezogen auf Feststoff. Die obere Grenze liegt bei etwa 15 Gew.-%, vorzugsweise 10 Gew.-%, besonders bevorzugt bei 5 Gew.-%. Die Umsetzung kann gegebenenfalls in Gegenwart eines Katalysators, wie Organozinnverbindungen und/oder tertiären Aminen durchgeführt werden. Um die Reaktionsteilnehmer in flüssigem Zustand zu halten und eine bessere Temperaturkontrolle während der Reaktion zu ermöglichen, ist der Zusatz von organischen Lösemitteln, die keinen aktiven Wasserstoff nach Zerewitinoff enthalten, möglich. Verwendbare Lösemittel sind beispielsweise Dimethylformamid, Ester, Ether, wie Diethylenglykol-dimethylether, Ketoester, Ketone, wie Methylethylketon und Aceton, mit Methoxygruppen substituierte Ketone, wie Methoxy-hexanon, Glykoletherester, chlorierte Kohlenwasserstoffe, aliphatische und alicyclische Kohlenwasserstoffpyrrolidone, wie N-Methylpyrrolidon, hydrierte Furane, aromatische Kohlenwasserstoffe und deren Gemische. Die Menge an Lösemittel kann in weiten Grenzen variieren und sollte zur Bildung einer Präpolymer-Lösung mit geeigneter Viskosität ausreichen. Meistens genügen 0,01 bis 15 Gew.-% Lösemittel, vorzugsweise 0,02 bis 8 Gew.-% Lösemittel, bezogen auf den Festkörper. Sieden die gegebenenfalls nicht wasserlöslichen Lösemittel niedriger als das Wasser, so können sie nach der Herstellung der harnstoffhaltigen Polyurethan-Dispersion durch Vakuumdestillation oder Dünnschichtverdampfung schonend abdestilliert werden. Höhersiedende Lösemittel sollten wasserlöslich sein und verbleiben in der wäßrigen Polyurethan-Dispersion, um das Zusammenfließen der polymer-Teilchen während der Filmbildung zu erleichtern. Besonders bevorzugt sind als Lösemittel N-Methylpyrrolidon, gegebenenfalls im Gemisch mit Ketonen, wie Methylethylketon.
Die anionischen Gruppen des NCO-Präpolymeren werden mit einem tertiären Amin mindestens teilweise neutralisiert. Die dadurch geschaffene Zunahme der Dispergierbarkeit in Wasser reicht für eine unendliche Verdünnbarkeit aus. Sie reicht auch aus, um das neutralisierte harnstoffgruppenhaltige Polyurethan beständig zu dispergieren. Geeignete tertiäre Amine sind beispielsweise Trimethylamin, Triethylamin, Dimethylethylamin, Diethylmethylamin, N-Methylmorpholin. Das NCO-Präpolymer wird nach der Neutralisation mit Wasser verdünnt und ergibt dann eine feinteilige Dispersion. Kurz danach werden die noch vorhandenen Isocyanatgruppen mit Di- und/oder Polyaminen mit primären und/oder sekundären Aminogruppen als Kettenverlängerer umgesetzt. Diese Reaktion führt zu einer weiteren Verknüpfung und Erhöhung des Molekulargewichts. Die Konkurrenzreaktion zwischen Amin und Wasser mit dem Isocyanat muß, um optimale Eigenschaften zu erhalten, gut abgestimmt (Zeit, Temperatur, Konzentration) und für eine reproduzierbare Produktion gut überwacht werden. Als Kettenverlängerer werden wasserlösliche Verbindungen bevorzugt, weil sie die Dispergierbarkeit des polymeren Endproduktes in Wasser erhöhen. Bevorzugt werden Hydrazin und organische Diamine, weil sie in der Regel die höchste Molmasse aufbauen, ohne das Harz zu gelieren. Vorausssetzung hierfür ist jedoch, daß das Verhältnis der Aminogruppen zu den Isocyanatgruppen zweckentsprechend gewählt wird. Die Menge des Kettenverlängerers wird von seiner Funktionalität, vom NCO-Gehalt des Präpolymeren und von der Dauer der Reaktion bestimmt. Das Verhältnis der aktiven Wasserstoffatome im Kettenverlängerer zu den NCO-Gruppen im Präpolymeren sollte in der Regel geringer als 2 : 1 und vorzugsweise im Bereich von 1,0 : 1 bis 1,75 : 1 liegen. Die Anwesenheit von überschüssigem aktiven Wasserstoff, insbesondere in Form von primären Aminogruppen, kann zu Polymeren mit unerwünscht niedriger Molmasse führen.
Polyamine sind im wesentlichen Alkylen-Polyamine mit 1 bis 40 Kohlenstoffatomen, vorzugsweise etwa 2 bis 15 Kohlenstoffatomen. Sie können Substituenten tragen, die keine mit Isocyanat-Gruppen reaktionsfähige Wasserstoffatome haben. Beispiele sind Polyamine mit linearer oder verzweigter aliphatischer, cycloaliphatischer oder aromatischer Struktur und wenigstens zwei primären Aminogruppen. Als Diamine sind zu nennen Ethylendiamin, Propylendiamin, 1,4-Butylendiamin, Piperazin, 1,4-Cyclohexyldimethylamin, Hexamethylendiamin-1,6, Trimethylhexamethylendiamin, Methandiamin, Isophorondiamin, 4,4'-Diaminodicyclohexylmethan und Aminoethylethanolamin. Bevorzugte Diamine sind Alkyl- oder Cycloalkyldiamine, wie Propylendiamin und 1-Amino-3-aminomethyl-3,5,5-trimethylcyclohexan.
Die Ketterverlängerung kann wenigstens teilweise mit einem Polyamin erfolgen, das mindestens drei Amingruppen mit einem reaktionsfähigen Wasserstoff aufweist. Dieser Polyamin-Typ kann in einer solchen Menge eingesetzt werden, daß nach der Verlängerung des Polymers nicht umgesetzte Aminstickstoffatome mit 1 oder 2 reaktionsfähigen Wasserstoffatomen vorliegen. Solche brauchbaren Polyamine sind Diethylentriamin, Triethylentetraamin, Dipropylentriamin und Dibutylentriamin. Bevorzugte Polyamine sind die Alkyl- oder Cycloalkyltriamine, wie Diethylentriamin. Um ein Gelieren bei der Kettenverlängerung zu verhindern, können auch kleine Anteil von Monoaminen, wie Ethylhexylamin zugesetzt werden.The NCO prepolymer contains at least about 0.5% by weight of isocyanate groups, preferably at least 1% by weight of NCO, based on the solid. The upper limit is approximately 15% by weight, preferably 10% by weight, particularly preferably 5% by weight. The reaction can optionally be carried out in the presence of a catalyst such as organotin compounds and / or tertiary amines. In order to keep the reactants in a liquid state and to enable better temperature control during the reaction, the addition of organic is Solvents that do not contain Zerewitinoff active hydrogen are possible. Usable solvents are, for example, dimethylformamide, esters, ethers, such as diethylene glycol dimethyl ether, keto esters, ketones, such as methyl ethyl ketone and acetone, ketones substituted with methoxy groups, such as methoxy hexanone, glycol ether esters, chlorinated hydrocarbons, aliphatic and alicyclic hydrocarbon pyrrolidones, such as N-methylpyrrolidone Furans, aromatic hydrocarbons and their mixtures. The amount of solvent can vary within wide limits and should be sufficient to form a prepolymer solution with a suitable viscosity. Mostly 0.01 to 15 wt .-% solvent, preferably 0.02 to 8 wt .-% solvent, based on the solid. If the water-insoluble solvents boil lower than water, they can be gently distilled off after the production of the urea-containing polyurethane dispersion by vacuum distillation or thin-film evaporation. Higher boiling solvents should be water soluble and remain in the aqueous polyurethane dispersion to facilitate the confluence of the polymer particles during film formation. Particularly preferred solvents are N-methylpyrrolidone, optionally in a mixture with ketones, such as methyl ethyl ketone.
The anionic groups of the NCO prepolymer are at least partially neutralized with a tertiary amine. The resulting increase in dispersibility in water is sufficient for infinite dilutability. It is also sufficient to permanently disperse the neutralized polyurethane containing urea groups. Suitable tertiary amines are, for example, trimethylamine, triethylamine, dimethylethylamine, diethylmethylamine, N-methylmorpholine. After neutralization, the NCO prepolymer is diluted with water and then results in a finely divided dispersion. Shortly thereafter, the isocyanate groups still present are included Di- and / or polyamines reacted with primary and / or secondary amino groups as chain extenders. This reaction leads to a further linkage and increase in the molecular weight. The competitive reaction between amine and water with the isocyanate must be well coordinated (time, temperature, concentration) in order to obtain optimum properties and well monitored for reproducible production. Water-soluble compounds are preferred as chain extenders because they increase the dispersibility of the polymeric end product in water. Hydrazine and organic diamines are preferred because they usually build up the highest molecular weight without gelling the resin. However, the prerequisite for this is that the ratio of the amino groups to the isocyanate groups is selected appropriately. The amount of chain extender is determined by its functionality, the NCO content of the prepolymer and the duration of the reaction. The ratio of the active hydrogen atoms in the chain extender to the NCO groups in the prepolymer should generally be less than 2: 1 and preferably in the range from 1.0: 1 to 1.75: 1. The presence of excess active hydrogen, especially in the form of primary amino groups, can result in polymers with undesirably low molecular weights.
Polyamines are essentially alkylene polyamines having 1 to 40 carbon atoms, preferably about 2 to 15 carbon atoms. They can carry substituents that have no hydrogen atoms that are reactive with isocyanate groups. Examples are polyamines with a linear or branched aliphatic, cycloaliphatic or aromatic structure and at least two primary amino groups. The diamines include ethylenediamine, propylenediamine, 1,4-butylenediamine, piperazine, 1,4-cyclohexyldimethylamine, 1,6-hexamethylenediamine, trimethylhexamethylenediamine, methanediamine, isophoronediamine, 4,4'-diaminodicyclohexylmethane and aminoethylethanolamine. Preferred diamines are alkyl or cycloalkyl diamines, such as propylenediamine and 1-amino-3-aminomethyl-3,5,5-trimethylcyclohexane.
The chain can be extended at least partially with a polyamine that has at least three amine groups with a reactive hydrogen. This type of polyamine can be used in such an amount that unreacted amine nitrogen atoms with 1 or 2 reactive hydrogen atoms are present after the polymer has been extended. Such useful polyamines are diethylenetriamine, triethylenetetraamine, dipropylenetriamine and dibutylenetriamine. Preferred polyamines are the alkyl or cycloalkyl triamines, such as diethylenetriamine. To prevent gelling during chain extension, small amounts of monoamines, such as ethylhexylamine, can also be added.
Die erfindungsgemäß einzusetzenden wasserverdünnbaren Polyurethanharze und deren Herstellung werden auch in der EP-A-89497 und US-PS 4,719,132 beschrieben.The water-dilutable polyurethane resins to be used according to the invention and their preparation are also described in EP-A-89497 and US Pat. No. 4,719,132.
Das in den bevorzugten wäßrigen Basisbeschichtungszusammensetzungen als filmbildende Material enthaltene Gemisch aus Emulsionspolymer und Polyurethanharz besteht aus 95 bis 40 Gew.-% Emulsionspolymer und 5 bis 60 Gew.-% Polyurethanharz, wobei sich die Mengenanteile jeweils auf den Festkörperanteil beziehen und ihre Summe stets 100 Gew.-% beträgt.The mixture of emulsion polymer and polyurethane resin contained in the preferred aqueous base coating compositions as a film-forming material consists of 95 to 40% by weight of emulsion polymer and 5 to 60% by weight of polyurethane resin, the proportions each referring to the solids content and their total always 100% by weight .-%.
Die erfindungsgemäßen wäßrigen Basisbeschichtungszusammensetzungen enthalten neben dem Emulsionspolymer bzw. dem Gemisch aus Emulsionspolymer und Polyurethanharz vorteilhafterweise noch weitere verträgliche wasserverdünnbare Kunstharze, wie z.B. Aminoplastharze, Polyester und Polyether, die im allgemeinen als Anreibeharze für die Pigmente dienen.In addition to the emulsion polymer or the mixture of emulsion polymer and polyurethane resin, the aqueous base coating compositions according to the invention advantageously also contain further compatible water-dilutable synthetic resins, such as, for example, aminoplast resins, polyesters and polyethers, which generally serve as grind resins for the pigments.
Die erfindungsgemäßen wäßrigen Basisbeschichtungszusammensetzungen enthalten vorzugsweise 5 bis 20, besonders bevorzugt 10 bis 16 Gew.-%, bezogen auf den Gesamtfeststoffgehalt der Basisbeschichtungszusammensetzungen, eines wasserverdünnbaren Aminoplastharzes, vorzugsweise Melaminharz und 5 bis 20, vorzugsweise 8 bis 15 Gew.-%, eines wasserverdünnbaren Polyethers (z.B. Polypropylenglykol mit einem zahlenmittleren Molekulargewicht von 400 bis 900).The aqueous base coating compositions according to the invention preferably contain 5 to 20, particularly preferably 10 to 16% by weight, based on the total solids content of the base coating compositions, of a water-dilutable aminoplast resin, preferably melamine resin and 5 to 20, preferably 8 to 15% by weight, of a water-dilutable polyether (eg polypropylene glycol with a number average molecular weight of 400 to 900).
Als Pigmente können die erfindungsgemäßen Basisbeschichtungszusammensetzungen farbgebende Pigmente auf anorganischer Basis, wie z.B. Titandioxid, Eisenoxid, Ruß usw., farbgebende Pigmente auf organischer Basis sowie übliche Metallpigmente (z.B. handelsübliche Aluminiumbronzen, Edelstahlbronzen ...) und nicht-metallische Effektpigmente (z.B. Perlglanz bzw. Interferenzpigmente) enthalten. Die erfindungsgemäßen Basisbeschichtungszusammensetzungen enthalten vorzugsweise Metallpigmente und/oder Effektpigmente. Die Pigmentierungshöhe liegt in üblichen Bereichen.As the pigments, the base coating compositions according to the invention can contain coloring pigments on an inorganic basis, such as e.g. Titanium dioxide, iron oxide, soot, etc., coloring pigments on an organic basis as well as common metal pigments (e.g. commercially available aluminum bronzes, stainless steel bronzes ...) and non-metallic effect pigments (e.g. pearlescent or interference pigments). The base coating compositions according to the invention preferably contain metal pigments and / or effect pigments. The pigmentation level is in the usual ranges.
Weiterhin können den erfindungsgemäßen Basisbeschichtungszusammensetzungen vernetzte polymere Mikroteilchen, wie sie in der EP-A-38 127 offenbart sind und/oder übliche rheologische anorganische oder organische Additive zugesetzt werden. So wirken als Verdicker beispielsweise wasserlösliche Celluloseether, wie Hydroxyethylcellulose, Methylcellulose oder Carboxymethylcellulose sowie synthetische Polymere mit ionischen und/oder assoziativ wirkenden Gruppen, wie Polyvinylalkohol, Poly(meth)acrylamid, Poly(meth)acrylsäure, Polyvinylpyrrolidon, Styrol-Maleinsäureanhydrid oder Ethylen-Maleinsäureanhydrid-Copolymere und ihre Derivate oder auch hydrophob modifizierte ethoxylierte Urethane oder Polyacrylate. Besonders bevorzugt werden carboxylgruppenhaltige Polyacrylat-Copolymere mit einer Säurezahl von 60 bis 780, bevorzugt 200 bis 500.Furthermore, crosslinked polymeric microparticles, such as are disclosed in EP-A-38 127 and / or customary rheological inorganic or organic additives, can be added to the base coating compositions according to the invention. For example, water-soluble cellulose ethers, such as hydroxyethyl cellulose, methyl cellulose or carboxymethyl cellulose, as well as synthetic polymers with ionic and / or associative groups, such as polyvinyl alcohol, poly (meth) acrylamide, poly (meth) acrylic acid, polyvinyl pyrrolidone, styrene-maleic anhydride or ethylene-maleic anhydride, act as thickeners Copolymers and their derivatives or also hydrophobically modified ethoxylated urethanes or polyacrylates. Carboxyl group-containing polyacrylate copolymers are particularly preferred with an acid number of 60 to 780, preferably 200 to 500.
Die erfindungsgemäßen Basisbeschichtungszusammensetzungen weisen im allgemeinen einen Festkörpergehalt von etwa 15 bis 50 Gew.-% auf. Der Festkörpergehalt variiert mit dem Verwendungszweck der Beschichtungszusammensetzungen. Für Metalliclacke liegt er beispielsweise bevorzugt bei 17 bis 25 Gew.-%. Für unifarbige Lacke liegt er höher, beispielsweise bei 30 bis 45 Gew.-%.
Die erfindungsgemäßen Beschichtungszusammensetzungen können zusätzlich übliche organische Lösemittel enthalten. Deren Anteil wird möglichst gering gehalten. Er liegt beispielsweise unter 15 Gew.-%.The base coating compositions according to the invention generally have a solids content of about 15 to 50% by weight. The solids content varies with the intended use of the coating compositions. For metallic paints, for example, it is preferably 17 to 25% by weight. For plain-colored paints it is higher, for example 30 to 45% by weight.
The coating compositions according to the invention can additionally contain customary organic solvents. Their share is kept as low as possible. For example, it is below 15% by weight.
Die erfindungsgemäßen Basisbeschichtungszusammensetzungen werden im allgemeinen auf einen pH-Wert zwischen 6,5 und 9,0 eingestellt. Der pH-Wert kann mit üblichen Aminen, wie z.B. Ammoniak, Triethylamin, Dimethylaminoethanol und N-Methylmorpholin eingestellt werden.The base coating compositions according to the invention are generally adjusted to a pH between 6.5 and 9.0. The pH can be adjusted with conventional amines, e.g. Ammonia, triethylamine, dimethylaminoethanol and N-methylmorpholine can be adjusted.
Mit der Bereitstellung der erfindungsgemäßen Basisbeschichtungszusammensetzungen wird die eingangs erläuterte Aufgabenstellung gelöst.
Mit den erfindungsgemäßen Basisbeschichtungszusammensetzungen können auch ohne Überlackierung mit einer transparenten Deckbeschichtungszusammensetzung qualitativ hochwertige Überzüge hergestellt werden.
Die erfindungsgemäßen Beschichtungszusammensetzungen können auf beliebige Substrate, wie z.B. Metall, Holz, Kunststoff oder Papier aufgebracht werden.With the provision of the base coating compositions according to the invention, the task explained at the outset is solved.
With the base coating compositions according to the invention, high-quality coatings can be produced even without overcoating with a transparent top coating composition.
The coating compositions according to the invention can be applied to any substrates, such as metal, wood, plastic or paper.
In den folgenden Beispielen wird die Erfindung näher erläutert.The invention is explained in more detail in the following examples.
In einem zylindrischen Glasdoppelwandgefäß mit Rührer, Rückflußkühler, rührbarem Zulaufgefäß, Tropftrichter und Thermometer werden 1344 g deionisiertes Wasser und 12 g einer 30 %igen wäßrigen Lösung des Ammoniumsalzes des Penta(ethylenglykol)nonylphenylethersulfats (Fenopon® EP 110 der GAF Corp., Emulgator 1) vorgelegt und auf 82°C aufgeheizt. Im rührbaren Zulaufgefäß wird aus 720 g deionisiertem Wasser, 24 g Emulgator 1, 10,8 g Acrylamid, 864 g Methylmethacrylat und 216 g n-Butylmethacrylat eine Emulsion hergestellt. 30 Gew.-% dieser Emulsion werden zur Vorlage gegeben. Dann werden 28 Gew.-% einer Lösung von 3,1 g Ammoniumperoxodisulfat (APS) in 188 g deionisiertem Wasser innerhalb von 5 Minuten zugetropft. Es tritt eine exotherme Reaktion ein. Die Reaktionstemperatur wird zwischen 82 und 88°C gehalten. 15 Minuten nach Beendigung der Zugabe der Ammoniumperoxodisulfatlösung werden die restlichen 70 Gew.-% der Emulsion zusammen mit den restlichen 72 Gew.-% der Ammoniumperoxodisulfatlösung innerhalb einer Stunde zugegeben, wobei die Temperatur bei 85°C gehalten wird. Danach wird auf 82°C abgekühlt und innerhalb von 2 Stunden werden eine Mischung aus 842 g n-Butylacrylat, 108 g Hydroxypropylmethacrylat, 43 g Methylmethacrylat, 43,2 g Methacrylsäure, 32,4 g Acrylamid und 5,4 g Eikosa(ethylenglykol)nonylphenylether (Antarox® CO 850 der GAF Corp., Emulgator 2) sowie 343 g deionisiertes Wasser zugegeben. Nach Beendigung der Zugabe wird die Reaktionsmischung noch für 1,5 Stunden bei 85°C gehalten. Danach wird abgekühlt und die Dispersion über ein Gewebe mit 30 µm Maschenweite gegeben. Man erhält eine feinteilige Dispersion mit einem nichtflüchtigen Anteil von 45 Gew.-%, einem pH-Wert von 3,4, einer Säurezahl von 13 und einer OH-Zahl von 20.1344 g of deionized water and 12 g of a 30% strength aqueous solution of the ammonium salt of penta (ethylene glycol) nonylphenyl ether sulfate (Fenopon® EP 110 from GAF Corp., emulsifier 1) are placed in a cylindrical glass double-walled vessel with stirrer, reflux condenser, stirrable feed vessel, dropping funnel and thermometer. submitted and heated to 82 ° C. An emulsion is prepared in the stirrable feed vessel from 720 g deionized water, 24 g emulsifier 1, 10.8 g acrylamide, 864 g methyl methacrylate and 216 g n-butyl methacrylate. 30% by weight of this emulsion are added for presentation. 28% by weight of a solution of 3.1 g of ammonium peroxodisulfate (APS) in 188 g of deionized water are then added dropwise over the course of 5 minutes. An exothermic reaction occurs. The reaction temperature is kept between 82 and 88 ° C. 15 minutes after the addition of the ammonium peroxodisulfate solution has ended, the remaining 70% by weight of the emulsion together with the remaining 72% by weight of the ammonium peroxodisulfate solution are added over the course of an hour, the temperature being kept at 85.degree. The mixture is then cooled to 82 ° C. and within 2 hours a mixture of 842 g n-butyl acrylate, 108 g hydroxypropyl methacrylate, 43 g methyl methacrylate, 43.2 g methacrylic acid, 32.4 g acrylamide and 5.4 g eikosa (ethylene glycol) nonylphenyl ether (Antarox® CO 850 from GAF Corp., emulsifier 2) and 343 g of deionized water were added. When the addition is complete, the reaction mixture kept at 85 ° C for 1.5 hours. It is then cooled and the dispersion is passed over a 30 μm mesh. A finely divided dispersion having a non-volatile content of 45% by weight, a pH of 3.4, an acid number of 13 and an OH number of 20 is obtained.
In einem zylindrischen Glasdoppelwandgefäß mit Rührer, Rückflußkühler, rührbarem Zulaufgefäß, Tropftrichter und Thermometer werden 1344 g deionisiertes Wasser und 12 g einer 40 %igen wäßrigen Lösung des Ammoniumsalzes des Penta(ethylenglykol)nonylphenylethersulfats (Fenopon® EP 110 der GAF Corp., Emulgator 1) vorgelegt und auf 80°C aufgeheizt. Im rührbaren Zulaufgefäß wird aus 720 g deionisiertem Wasser, 24 g Emulgator 1, 10,8 g Acrylamid, 518 g Methylmethacrylat, 292 g n-Butylmethacrylat und 205 g Styrol eine Emulsion hergestellt.
30 Gew.-% dieser Emulsion werden zur Vorlage gegeben. Dann wird eine Lösung von 0,9 g Ammoniumperoxodisulfat APS in 55 g deionisiertem Wasser innerhalb von 5 Minuten zugetropft. Es tritt eine exotherme Reaktion ein. Die Reaktionstemperatur wird zwischen 80 und 85°C gehalten. 15 Minuten nach Beendigung der Zugabe der obengenannten APS-Lösung werden eine Lösung von 2,2 g APS in 480 g Wasser innerhalb von 3 Stunden und die restlichen 70 Gew.-% der obengenannten Emulsion innerhalb von einer Stunde zugegeben, wobei die Reaktionstemperatur bei 80°C gehalten wird. Nach Beendigung der Zugabe der Emulsion wird auf 77°C abgekühlt und innerhalb von 2 Stunden eine Mischung aus 745 g n-Butylacrylat, 119 g Methylmethacrylat, 108 g Hydroxypropylmethacrylat, 54 g Styrol, 42,7 g Ethylhexylacrylat, 42,7 g Methacrylsäure, 21,6 g Acrylamid und 2,2 g Emulgator 2 zugegeben. Nach Beendigung der Zugabe wird die Reaktionsmischung noch für 1,5 Stunden bei 80°C gehalten.1344 g of deionized water and 12 g of a 40% strength aqueous solution of the ammonium salt of penta (ethylene glycol) nonylphenyl ether sulfate (Fenopon® EP 110 from GAF Corp., emulsifier 1) are placed in a cylindrical glass double-walled vessel with stirrer, reflux condenser, stirrable feed vessel, dropping funnel and thermometer. submitted and heated to 80 ° C. An emulsion is prepared in the stirrable feed vessel from 720 g deionized water, 24 g emulsifier 1, 10.8 g acrylamide, 518 g methyl methacrylate, 292 g n-butyl methacrylate and 205 g styrene.
30% by weight of this emulsion are added for presentation. A solution of 0.9 g of ammonium peroxodisulfate APS in 55 g of deionized water is then added dropwise in the course of 5 minutes. An exothermic reaction occurs. The reaction temperature is kept between 80 and 85 ° C. 15 minutes after the addition of the above-mentioned APS solution has ended, a solution of 2.2 g of APS in 480 g of water is added within 3 hours and the remaining 70% by weight of the above-mentioned emulsion are added within one hour, the reaction temperature being 80 ° C is maintained. After the addition of the emulsion has ended, the mixture is cooled to 77 ° C. and within 2 hours a mixture of 745 g of n-butyl acrylate, 119 g of methyl methacrylate, 108 g of hydroxypropyl methacrylate, 54 g of styrene, 42.7 g of ethylhexyl acrylate, 42.7 g of methacrylic acid, 21.6 g of acrylamide and 2.2 g of emulsifier 2 were added. After the addition has ended, the reaction mixture is kept at 80 ° C. for a further 1.5 hours.
Danach wird abgekühlt und die Dispersion über ein Gewebe mit 30 µm Maschenweite gegeben. Man erhält eine feinteilige Dispersion mit einem nichtflüchtigen Anteil von 45 Gew.-%, einen pH-Wert von 3,8, einer Säurezahl von 13 und einer OH-Zahl von 19.It is then cooled and the dispersion is passed over a 30 μm mesh. A finely divided dispersion with a non-volatile content of 45% by weight, a pH of 3.8, an acid number of 13 and an OH number of 19 is obtained.
In einem zylindrischen Glasdoppelwandgefäß mit Rührer, Rückflußkühler, rührbarem Zulaufgefäß, Tropftrichter und Thermometer werden 1109 g deionisiertes Wasser und 10 g einer 30 %igen wäßrigen Lösung des Ammoniumsalzes des Penta(ethylenglykol)nonylphenylethersulfats (Fenopon®EP 110 der GAF Corp., Emulgator 1) vorgelegt und auf 82°C aufgeheizt. Im rührbaren Zulaufgefäß wird aus 748,2 g deionisiertem Wasser, 20,3 g Emulgator 1, 9,0 g Acrylamid, 718,1 g Methylmethacrylat und 179,5 g n-Butylmethacrylat eine Emulsion hergestellt. 30 Gew.-% dieser Emulsion werden zur Vorlage gegeben. Dann werden 10 Gew.-% einer Lösung von 7,2 g Ammoniumperoxodisulfat in 305 g deionisiertem Wasser innerhalb von 5 Minuten zugetropft. Es tritt eine exotherme Reaktion ein. Die Reaktionstemperatur wird zwischen 82 und 88°C gehalten. 15 Minuten nach Beendigung der Zugabe der Ammoniumperoxodisulfatlösung werden die restlichen 70 Gew.-% der Emulsion zusammen mit den restlichen 90 Gew.-% der Ammoniumperoxodisulfatlösung innerhalb einer Stunde zugegeben, wobei die Temperatur bei 82°C gehalten wird. Danach wird innerhalb von 2 Stunden eine Mischung aus 700 g n-Butylacrylat, 89,8 g Hydroxypropylmethacrylat, 35,9 g Methylmethacrylat, 35,9 g Methacrylsäure, 26,9 g Acrylamid und 4,5 g
Eikosa(ethylenglykol)nonylphenylether (Antarox®CO 850 der GAF Corp., Emulgator 2) zugegeben. Nach Beendigung der Zugabe wird die Reaktionsmischung noch für 1,5 Stunden bei 82°C gehalten. Danach wird abgekühlt und die Dispersion über ein Gewebe mit 30 µm Maschenweite gegeben. Man erhält eine feinteilige Dispersion mit einem nichtflüchtigen Anteil von 45 Gew.-%, $inem pH-Wert von 2,5, einer Säurezahl von 14 und einer OH-Zahl von 20.1109 g of deionized water and 10 g of a 30% strength aqueous solution of the ammonium salt of penta (ethylene glycol) nonylphenyl ether sulfate (Fenopon®EP 110 from GAF Corp., emulsifier 1) are placed in a cylindrical glass double-walled vessel with stirrer, reflux condenser, stirrable feed vessel, dropping funnel and thermometer. submitted and heated to 82 ° C. An emulsion is prepared in the stirrable feed vessel from 748.2 g deionized water, 20.3 g emulsifier 1, 9.0 g acrylamide, 718.1 g methyl methacrylate and 179.5 g n-butyl methacrylate. 30% by weight of this emulsion are added for presentation. 10% by weight of a solution of 7.2 g of ammonium peroxodisulfate in 305 g of deionized water are then added dropwise over the course of 5 minutes. An exothermic reaction occurs. The reaction temperature is kept between 82 and 88 ° C. 15 minutes after the addition of the ammonium peroxodisulfate solution has ended, the remaining 70% by weight of the emulsion together with the remaining 90% by weight of the ammonium peroxodisulfate solution are added over the course of an hour, the temperature being kept at 82.degree. A mixture of 700 g of n-butyl acrylate, 89.8 g of hydroxypropyl methacrylate, 35.9 g of methyl methacrylate, 35.9 g of methacrylic acid, 26.9 g of acrylamide and 4.5 g is then added within 2 hours
Eikosa (ethylene glycol) nonylphenyl ether (Antarox®CO 850 from GAF Corp., emulsifier 2) was added. After the addition has ended, the reaction mixture is kept at 82 ° C. for a further 1.5 hours. It is then cooled and the dispersion is spread over a fabric 30 µm mesh size given. A finely divided dispersion with a non-volatile content of 45% by weight, a pH of 2.5, an acid number of 14 and an OH number of 20 is obtained.
In einem zylindrischen Glasdoppelwandgefäß mit Rührer, Rückflußkühler, rührbarem Zulaufgefäß, Tropftrichter und Thermometer werden 1344 g deionisiertes Wasser und 12 g einer 30 %igen wäßrigen Lösung des Ammoniumsalzes des Penta(ethylenglykol)nonylphenylethersulfats (Fenopon® EP 110 der GAF Corp., Emulgator 1) vorgelegt und auf 82°C aufgeheizt. Im rührbaren Zulaufgefäß wird aus 477 g deionisiertem Wasser, 66,7 g Emulgator 1, 10,8 g Acrylamid, 864 g Methylmethacrylat und 216 g n-Butylmethacrylat eine Emulsion hergestellt. 30 Gew.-% dieser Emulsion werden zur Vorlage gegeben. Dann werden 3,6 Gew.-% einer Lösung von 8,6 g Ammoniumperoxodisulfat in 183 g deionisiertem Wasser innerhalb von 5 Minuten zugetropft. Es tritt eine exotherme Reaktion ein. Die Reaktionstemperatur wird zwischen 82 und 88°C gehalten. 15 Minuten nach Beendigung der Zugabe der Ammoniumperoxodisulfatlösung werden die restlichen 70 Gew.-% der Emulsion zusammen mit den restlichen 96,4 Gew.-% der Ammoniumperoxodisulfatlösung innerhalb einer Stunde zugegeben, wobei die Temperatur bei 82°C gehalten wird. Danach wird innerhalb von 2 Stunden eine Mischung aus 842 g n-Butylacrylat, 108 g Hydroxypropylmethacrylat, 43,2 g Methylmethacrylat, 43,2 g Acrylamidomethylpropansulfonsäure, 32,4 g Acrylamid, 66,7 g Emulgator 1 und 5,4 g Eikosa(ethylenglykol)nonylphenylether (Antarox® CO 850 der GAF Corp., Emulgator 2) zugegeben. Nach Beendigung der Zugabe wird die Reaktionsmischung noch für 1,5 Stunden bei 82°C gehalten. Danach wird abgekühlt und die Dispersion über ein Gewebe mit 30 µm Maschenweite gegeben. Man erhält eine feinteilige Dispersion mit einem nichtflüchtigen Anteil von 46 Gew.-%, einem pH-Wert von 2,5, einer Säurezahl von 6 und einer OH-Zahl von 19.1344 g of deionized water and 12 g of a 30% strength aqueous solution of the ammonium salt of penta (ethylene glycol) nonylphenyl ether sulfate (Fenopon® EP 110 from GAF Corp., emulsifier 1) are placed in a cylindrical glass double-walled vessel with stirrer, reflux condenser, stirrable feed vessel, dropping funnel and thermometer. submitted and heated to 82 ° C. An emulsion is prepared in the stirrable feed vessel from 477 g of deionized water, 66.7 g of emulsifier 1, 10.8 g of acrylamide, 864 g of methyl methacrylate and 216 g of n-butyl methacrylate. 30% by weight of this emulsion are added for presentation. Then 3.6% by weight of a solution of 8.6 g of ammonium peroxodisulfate in 183 g of deionized water are added dropwise within 5 minutes. An exothermic reaction occurs. The reaction temperature is kept between 82 and 88 ° C. 15 minutes after the addition of the ammonium peroxodisulfate solution has ended, the remaining 70% by weight of the emulsion together with the remaining 96.4% by weight of the ammonium peroxodisulfate solution are added over the course of an hour, the temperature being kept at 82.degree. A mixture of 842 g of n-butyl acrylate, 108 g of hydroxypropyl methacrylate, 43.2 g of methyl methacrylate, 43.2 g of acrylamidomethylpropanesulfonic acid, 32.4 g of acrylamide, 66.7 g of emulsifier 1 and 5.4 g of eikosa ( ethylene glycol) nonylphenyl ether (Antarox® CO 850 from GAF Corp., emulsifier 2) added. After the addition has ended, the reaction mixture is kept at 82 ° C. for a further 1.5 hours. It is then cooled and the dispersion is passed over a 30 μm mesh. You get a finely divided Dispersion with a non-volatile content of 46% by weight, a pH of 2.5, an acid number of 6 and an OH number of 19.
In einem zylindrischen Glasdoppelwandgefäß mit Rührer, Rückflußkühler, rührbarem Zulaufgefäß, Tropftrichter und Thermometer werden 1344 g deionisiertes Wasser und 12 g einer 30 %igen wäßrigen Lösung des Ammoniumsalzes des Penta(ethylenglykol)nonylphenylethersulfats (Fenopon® EP 110 der GAF Corp., Emulgator 1) vorgelegt und auf 82°C aufgeheizt. Im rührbaren Zulaufgefäß wird aus 720 g deionisiertem Wasser, 24 g Emulgator 1, 43,2 g Acrylamid, 907 g Methylmethacrylat und 216 g n-Butylmethacrylat, 842 g n-Butylacrylat, 108 g Hydroxypropylmethacrylat, 43,2 g Methacrylsäure und 5,4 g Emulgator 2 eine Emulsion hergestellt. 10 Gew.-% dieser Emulsion werden zur Vorlage gegeben. Dann wird eine Lösung von 0,87 g Ammoniumperoxodisulfat in 53 g deionisiertem Wasser innerhalb von 5 Minuten zugetropft. Es tritt eine exotherme Reaktion ein. Die Reaktionstemperatur wird zwischen 82 und 88°C gehalten. 15 Minuten nach Beendigung der Zugabe der APS-Lösung werden die restlichen 90 Gew.-% der Emulsion innerhalb von 3 Stunden und eine Lösung von 2,23 g APS in 478 g deionisiertem Wasser innerhalb von 3,5 Stunden zugegeben, wobei die Temperatur bei 82°C gehalten wird.1344 g of deionized water and 12 g of a 30% strength aqueous solution of the ammonium salt of penta (ethylene glycol) nonylphenyl ether sulfate (Fenopon® EP 110 from GAF Corp., emulsifier 1) are placed in a cylindrical glass double-walled vessel with stirrer, reflux condenser, stirrable feed vessel, dropping funnel and thermometer. submitted and heated to 82 ° C. In the stirrable feed vessel 720 g of deionized water, 24 g of emulsifier 1, 43.2 g of acrylamide, 907 g of methyl methacrylate and 216 g of n-butyl methacrylate, 842 g of n-butyl acrylate, 108 g of hydroxypropyl methacrylate, 43.2 g of methacrylic acid and 5.4 g emulsifier 2 an emulsion is prepared. 10% by weight of this emulsion are added for presentation. A solution of 0.87 g of ammonium peroxodisulfate in 53 g of deionized water is then added dropwise in the course of 5 minutes. An exothermic reaction occurs. The reaction temperature is kept between 82 and 88 ° C. 15 minutes after the addition of the APS solution has ended, the remaining 90% by weight of the emulsion are added within 3 hours and a solution of 2.23 g of APS in 478 g of deionized water is added within 3.5 hours, the temperature being at Is held at 82 ° C.
Nach Beendigung der Zugabe wird die Reaktionsmischung noch für 1,5 Stunden bei 82°C gehalten. Danach wird abgekühlt und die Dispersion über ein Gewebe mit 30 µm Maschenweite gegeben. Man erhält eine feinteilige Dispersion mit einem nichtflüchtigen Anteil von 45 Gew.-%, einem pH-Wert von 5,8, einer Säurezahl von 13 und einer OH-Zahl von 20.After the addition has ended, the reaction mixture is kept at 82 ° C. for a further 1.5 hours. It is then cooled and the dispersion is passed over a 30 μm mesh. A finely divided dispersion with a non-volatile content of 45% by weight, a pH of 5.8, an acid number of 13 and an OH number of 20 is obtained.
570 g eines handelsüblichen aus Caprolacton und Ethylenglykol hergestellten Polyesters mit einer Hydroxylzahl von 196 werden bei 100°C l Stunde im Vakuum entwässert. Bei 80°C werden 524 g 4,4'-Dicyclohexylmethandiisocyanat zugegeben und bei 90°C so lange gerührt, bis der Isocyanatgehalt 7,52 Gew.-%, bezogen auf die Gesamteinwaage, beträgt. Nach Abkühlen auf 60°C werden eine Lösung von 67 g Dimethylolpropionsäure und 50 g Triethylamin in 400 g N-Methylpyrrolidon zugegeben und 1 Stunde bei 90°C gerührt. Die erhaltene Masse wird unter intensivem Rühren in 1840 g kaltes deionisiertes Wasser gegeben. Zu der erhaltenen Dispersion werden unter intensivem Rühren innerhalb von 20 Minuten 86 g einer 15 %igen Hydrazinlösung zugegeben. Die resultierende, sehr feinteilige Dispersion hat einen Festkörpergehalt von 35 % und eine Auslaufzeit von 27 Sekunden im DIN-Becher 4.570 g of a commercially available polyester made from caprolactone and ethylene glycol with a hydroxyl number of 196 are dewatered at 100 ° C. for 1 hour in vacuo. 524 g of 4,4'-dicyclohexylmethane diisocyanate are added at 80 ° C. and the mixture is stirred at 90 ° C. until the isocyanate content is 7.52% by weight, based on the total weight. After cooling to 60 ° C., a solution of 67 g of dimethylolpropionic acid and 50 g of triethylamine in 400 g of N-methylpyrrolidone are added and the mixture is stirred at 90 ° C. for 1 hour. The mass obtained is poured into 1840 g of cold deionized water with vigorous stirring. 86 g of a 15% hydrazine solution are added to the dispersion obtained within 20 minutes, with vigorous stirring. The resulting, very finely divided dispersion has a solids content of 35% and a run-out time of 27 seconds in the DIN cup 4.
830 g eines Polyesters aus Neopentylglykol, Hexandiol-1,6 und Adipinsäure mit einer Hydroxylzahl von 135 und einer Säurezahl unter 3 werden bei 100°C l Stunde im Vakuum entwässert. Bei 80°C werden 524 g 4,4'-Dicyclohexylmethandiisocyanat zugegeben und bei 90°C gerührt, bis der Gehalt an freien Isocyanatgruppen 6,18 Gew.-%, bezogen auf die Gesamteinwaage, beträgt. Nach Abkühlung auf 60°C werden eine Lösung von 67 g Dimethylpropionsäure und 50 g Triethylamin in 400 g N-Methylpyrrolidon zugegeben und 1 Stunde bei 90°C gerührt.
Die erhaltene Masse wird unter intensivem Rühren in 2400 g kaltes deionisiertes Wasser gegeben. Man erhält eine feinteilige Dispersion. Zu dieser Dispersion werden unter intensivem Rühren innerhalb von 20 Minuten 80 g einer 30 %igen wäßrigen Lösung von Ethylendiamin zugegeben. Die resultierende, sehr feinteilige Dispersion hat einen Festkörpergehalt von 35 % und eine Auslaufzeit von 23 Sekunden im DIN-Becher 4.830 g of a polyester composed of neopentyl glycol, 1,6-hexanediol and adipic acid with a hydroxyl number of 135 and an acid number below 3 are dewatered at 100 ° C. for 1 hour in vacuo. 524 g of 4,4'-dicyclohexylmethane diisocyanate are added at 80 ° C. and the mixture is stirred at 90 ° C. until the free isocyanate group content is 6.18% by weight, based on the total weight. After cooling to 60 ° C., a solution of 67 g of dimethylpropionic acid and 50 g of triethylamine in 400 g of N-methylpyrrolidone are added and the mixture is stirred at 90 ° C. for 1 hour.
The mass obtained is poured into 2400 g of cold deionized water with vigorous stirring. You get a finely divided Dispersion. 80 g of a 30% strength aqueous solution of ethylenediamine are added to this dispersion with vigorous stirring within 20 minutes. The resulting, very finely divided dispersion has a solids content of 35% and a run-out time of 23 seconds in the DIN cup 4.
18,2 g Butylglykol, 3,7 g eines handelsüblichen Melamin-Formaldehydharzes (Cymel® 301), 3,1 g Polypropylenglykol (mittleres Molekulargewicht = 400) und 7,2 g einer Aluminiumbronze gemäß DE-OS-36 36 183 (Aluminiumgehalt: 60 Gew.-%) werden mit einem Schnellrührer 15 Minuten bei 300-500 U/min. gerührt. Es wird eine Mischung 1 erhalten.
27,2 g Emulsionspolymerdispersion 1, 2, 3 oder 4 werden mit 11,6 g Polyurethanharzdispersion 1 und 19,6 g deionisiertem Wasser gemischt. Die Mischung wird mit einer 5 %igen wäßrigen Dimethylethanolaminlösung auf einen pH-Wert von 7,7 eingestellt und mit 9,4 g einer 3,5 %igen Lösung eines handelsüblichen Polyacrylsäureverdickers (Viscalex®HV 30 der Allied Colloids, pH-Wert: 8,0) versetzt. Es wird die Mischung 2 erhalten.18.2 g of butyl glycol, 3.7 g of a commercially available melamine-formaldehyde resin (Cymel® 301), 3.1 g of polypropylene glycol (average molecular weight = 400) and 7.2 g of an aluminum bronze according to DE-OS-36 36 183 (aluminum content: 60 wt .-%) with a high speed stirrer for 15 minutes at 300-500 U / min. touched. A mixture 1 is obtained.
27.2 g of emulsion polymer dispersion 1, 2, 3 or 4 are mixed with 11.6 g of polyurethane resin dispersion 1 and 19.6 g of deionized water. The mixture is adjusted to a pH value of 7.7 with a 5% aqueous dimethylethanolamine solution and with 9.4 g of a 3.5% solution of a commercially available polyacrylic acid thickener (Viscalex®HV 30 from Allied Colloids, pH value: 8 , 0) offset. Mixture 2 is obtained.
Zur Herstellung der erfindungsgemäßen Basislacke werden die Mischungen 1 und 2 30 Minuten bei 800-1000 U/min. gemischt und danach mit einer 5 %gen wäßrigen Dimethylethanolaminlösung auf einen pH-Wert von 7,7 eingestellt. Anschließend wird die Viskosität durch Zugabe von deionisiertem Wasser auf eine Auslaufzeit von 25 sec. im DIN 4-Becher eingestellt. Es werden die erfindungsgemäßen Basisbeschichtungszusammensetzungen BB1, BB2, BB3 und BB4 erhalten.Mixtures 1 and 2 are produced at 800-1000 rpm for 30 minutes to produce the basecoats of the invention. mixed and then adjusted to a pH of 7.7 with a 5% aqueous solution of dimethylethanolamine. The viscosity is then adjusted to an outflow time of 25 seconds in a DIN 4 cup by adding deionized water. The base coating compositions BB1, BB2, BB3 and BB4 according to the invention are obtained.
Die Basisbeschichtungszusammensetzung BB5 wird erhalten, indem in die Mischung 2 36,2 g der Emulsionspolymerdispersion 1 eingearbeitet werden. BB5 enthält keine Polyurethanharzdispersion.The base coating composition BB5 is obtained by incorporating 36.2 g of the emulsion polymer dispersion 1 into the mixture 2. BB5 does not contain a polyurethane resin dispersion.
Die so erhaltenen Basisbeschichtungszusammensetzungen zeigen ausgezeichnete Lagerstabilitäten.The base coating compositions thus obtained show excellent storage stability.
Die Basisbeschichtungszusammensetzungen werden nach gut bekannten Methoden auf mit einer handelsüblichen Elektrotauchlackierung und einem handelsüblichen Füller beschichtete phosphatierte Stahlbleche (Bonder 132) gespritzt, nach einer Ablüftzeit von 10 Minuten mit einem handelsüblichen Klarlack überlackiert und 20 Minuten bei 140°C eingebrannt.
Die so erhaltene Metalleffektlackierungen zeigen einen guten Metalleffekt, gute Haftung zum Füller, gute Haftung zwischen Basislack und Decklack, guten Glanz und gute Beständigkeit im Schwitzwasserkonstantklima nach DIN 50 017. BB1, BB2, BB3 und BB4 zeigen einen besseren Metalleffekt als BB5.The base coating compositions are sprayed onto well-known methods onto phosphated steel sheets (Bonder 132) coated with a commercially available electrodeposition coating and a commercially available filler, overcoated with a commercially available clearcoat after a flash-off time of 10 minutes and baked at 140 ° C. for 20 minutes.
The metallic effect coatings obtained in this way show a good metallic effect, good adhesion to the filler, good adhesion between the basecoat and topcoat, good gloss and good resistance in a condensed water constant climate according to DIN 50 017. BB1, BB2, BB3 and BB4 show a better metallic effect than BB5.
Ein Teil der lackierten Bleche wird nochmals mit den Basisbeschichtungszusammensetzungen BB1, BB2, BB3, BB4 und BB5 beschichtet und mit einem handelsüblichen Klarlack überlackiert. Die so erhaltenen Lackierungen werden 40 Minuten bei 80°C eingebrannt. Die bei 80°C eingebrannten Lackierungen haften ausgezeichnet auf den bei 140°C eingebrannten Lackierungen.A part of the painted sheets is coated again with the base coating compositions BB1, BB2, BB3, BB4 and BB5 and overcoated with a commercially available clear coat. The coatings obtained in this way are baked at 80 ° C. for 40 minutes. The coatings baked at 80 ° C adhere well to the coatings baked at 140 ° C.
Eine gemäß obiger Beschreibung unter Verwendung der Emulsionspolymerdispersion 5 hergestellte Basisbeschichtungszusammensetzung zeigt eine unzureichende Lagerstabilität.A basecoat composition prepared as described above using the emulsion polymer dispersion 5 shows insufficient storage stability.
Claims (11)
- Process for the preparation of a multicoat protective and/or decorative coating on a substrate surface, in which process(1) a pigmented aqueous coating composition which comprises as the film-former a water-thinnable emulsion polymer, is applied to the substrate surface as basecoat composition(2) a polymeric film is formed from the composition applied in stage (1)(3) a suitable clear topcoat composition is applied to the basecoat obtained in this manner and subsequently(4) the basecoat and the topcoat are baked together, characterised in that the basecoat composition comprises a water-thinnable emulsion polymer, which polymer can be obtained(a) by polymerising in a first stage 10 to 90 parts by weight of a mixture of(a1) 100 to 60 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid, or a mixture of such esters, and(a2) 0 to 40 % by weight of a monomer which is copolymerisable with (a1), or a mixture of such monomersin aqueous phase in the presence of one or more emulsifiers and one or more radical-forming initiators, the total of the weight percentages of (a1) and (a2) always being 100 % by weight and (a1) and (a2) being chosen such that the first stage gives rise to a polymer having a glass transition temperature (TG1) of + 30 to + 110°C, and(b) by polymerising in a second stage 90 to 10 parts by weight of a mixture of(b1) 47 to 99 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid, or a mixture of such esters(b2) 1 to 20 % by weight of a monomer which carries at least one hydroxyl group and is copolymerisable with (b1), (b3) and (b4), or a mixture of such monomers(b3) 0 to 8 % by weight of a monomer which carries at least one carboxyl or sulphonyl group and is copolymerisable with (b1), (b2) and (b4), or a mixture of such monomers, and(b4) 0 to 25 % by weight of a further monomer which is copolymerisable with (b1), (b2) and (b3), or a mixture of such monomersafter at least 80% by weight of the monomer or the mixture of monomers used in the first stage has reacted, in the presence of the polymer obtained in the first stage, the total of the weight percentages of (b1), (b2), (b3) and (b4) always being 100 % by weight and (b1), (b2), (b3) and (b4) being chosen such that an exclusive polymerisation of the mixture of monomer used in the second stage gives rise to a polymer having a glass transition temperature (TG2) of - 60 to + 20°C, the reaction conditions being chosen such that the resultant emulsion polymer has a number average molecular mass of 200,000 to 2,000,000, and the nature and amount of the ethylenically unsaturated monomer or the mixture of monomers used in the first stage and the mixture of monomers used in the second stage are chosen such that the resultant emulsion polymer has a hydroxyl value of 2 to 100 and the difference TG1 - TG2 is 10 to 170°C.
- Process according to Claim 1, characterised in that the basecoat composition comprises a metallic pigment, preferably an aluminium pigment.
- Process according to Claim 1 or 2, characterised in that 99.5 to 75 % by weight of component (a1) and/or 0.5 to 25 % by weight of component (a2) and/or 75 to 90 % by weight of component (b1) and/or 5 to 15 % by weight of component (b2) and/or 2 to 6 % by weight of component (b3) and/or 2 to 15 % by weight of component (b4) are polymerised.
- Process according to one of Claims 1 to 3, characterised in that the film-former consists of 95 to 40% by weight of the emulsion polymer and 5 to 60% by weight of a water-thinnable polyurethane resin, the weight percentages in each case referring to the solids content and their sum being always 100% by weight.
- Water-thinnable coating compositions characterised in that they contain as the film-former a water-thinnable emulsion polymer which can be obtained(a) by polymerising in a first stage 10 to 90 parts by weight of a mixture which consists of(a1) 100 to 60 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters, and(a2) 0 to 40 % by weight of a monomer which is copolymerisable with (a1) or a mixture of such monomers, in aqueous phase in the presence of one or more emulsifiers and one or more radical-forming initiators, the total of the weight percentages of (a1) and (a2) always being 100 % by weight and (a1) and (a2) being chosen such that the first stage gives rise to a polymer having a glass transition temperature (TG1) of +30 to +110°C, and(b) by polymerising in a second stage 90 to 10 parts by weight of a mixture of(b1) 47 to 99 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters(b2) 1 to 20 % by weight of a monomer which carries at least one hydroxyl group and is copolymerisable with (b1), (b3) and (b4), or a mixture of such monomers(b3) 0 to 8 % by weight of a monomer which carries at least one carboxyl or sulphonic acid group and is copolymerisable with (b1), (b2) and (b4), or a mixture of such monomers, and(b4) 0 to 25 % by weight of a further monomer which is copolymerisable with (b1), (b2) and (b3), or a mixture of such monomers after at least 80 % by weight of the ethylenically unsaturated monomer or the mixture of monomers used in the first stage has reacted, in the presence of the polymer obtained in the first stage, the total of the weight percentages of (b1), (b2), (b3) and (b4) always being 100 % by weight and (b1), (b2), (b3) and (b4) being chosen such that an exclusive polymerisation of the mixture of monomers used in the second stage gives rise to a polymer having a glass transition temperature (TG₂) of - 60 to + 20°C, the reaction conditions being chosen such that the resultant emulsion polymer has a number average molecular mass of 200,000 to 2,000,000, and the nature and amount of the ethylenically unsaturated monomer or the mixture of monomers used in the first stage and the nature and amount of the mixture of monomers used in the second stage are chosen such that the resultant emulsion polymer has a hydroxyl value of 2 to 100 and the difference TG1 - TG2 is 10 to 170°C.
- Coatings compositions according to Claim 5, characterised in that they contain a metallic pigment, preferably an aluminium pigment.
- Coating compositions according to Claim 5 or 6, characterised in that 99.5 to 75 % by weight of component (a1) and/or 0.5 to 25 % by weight of component (a2) and/or 75 to 90 % by weight of component (b1) and/or 5 to 15 % by weight of component (b2) and/or 2 to 6 % by weight of component (b3) and/or 2 to 15 % by weight of component (b4) are polymerised.
- Water-thinnable emulsion polymers, characterised in that they can be obtained(a) by polymerising in a first stage 10 to 90 parts by weight of a mixture of(a1) 100 to 60 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid, or a mixture of such esters and(a2) 0 to 40 % by weight of a monomer which is copolymerisable with (a1), or a mixture of such monomers, in aqueous phase in the presence of one or more emulsifiers and one or more radical-forming initiators, the total of the weight percentages of (a1) and (a2) always being 100 % by weight and (a1) and (a2) being chosen such that the first stage gives rise to a polymer having a glass transition temperature (TG₁) of + 30 to + 110°C, and(b) by polymerising in a second stage 90 to 10 parts by weight of a mixture of(b1) 47 to 99 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid, or a mixture of such esters(b2) 1 to 20 % by weight of a monomer which carries at least one hydroxyl group and is copolymerisable with (b1), (b3) and (b4), or a mixture of such monomers(b3) 0 to 8 % by weight of a monomer which carries at least one carboxyl or sulphonyl group and is copolymerisable with (b1), (b2) and (b4), or a mixture of such monomers, and(b4) 0 to 25 % by weight of a further monomer which is copolymerisable with (b1), (b2) and (b3), or a mixture of such monomers, after at least 80% by weight of the ethylenically unsaturated monomer or the mixture of monomers used in the first stage has reacted, in the presence of the polymer obtained in the first stage, the total of the weight percentages of (b1), (b2), (b3) and (b4) always being 100 % by weight and (b1), (b2), (b3) and (b4) being chosen such that an exclusive polymerisation of the mixture of monomers used in the second stage gives rise to a polymer having a glass transition temperature (TG2) of - 60 to + 20°C, the reaction conditions being chosen such that the resultant emulsion polymer has a number average molecular mass of 200,000 to 2,000,000, and the nature and amount of the ethylenically unsaturated monomer or the mixture of monomers used in the first stage and the nature and amount of the mixture of monomers used in the second stage are chosen such that the resultant emulsion polymer has a hydroxyl value of 2 to 100 and the difference TG1 - TG2 is 10 to 170°C.
- Emulsion polymers according to Claim 8, characterised in that 99.5 to 75 % by weight of component (a1) and/or 0.5 to 25 % by weight of component (a2) and/or 75 to 90 % by weight of component (b1) and/or 5 to 15 % by weight of component (b2) and/or 2 to 6 % by weight of component (b3) and/or 2 to 15 % by weight of component (b4) are polymerised.
- Process for the preparation of water-thinnable emulsion polymers characterised in that(a) in a first stage 10 to 90 parts by weight of a mixture which consists of(a1) 100 to 60 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters, and(a2) 0 to 40 % by weight of a monomer which is copolymerisable with (a1) or a mixture of such monomers,in aqueous phase in the presence of one or more emulsifiers and one or more radical-forming initiators, the sum of the parts by weight of (a1) and (a2) always being 100 % by weight and (a1) and (a2) being chosen such that the first stage gives rise to a polymer having a glass transition temperature (TG₁) of +30 to +110°C, and(b) by polymerising in a second stage 90 to 10 parts by weight of(b1) 47 to 99 % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters(b2) 1 to 20 % by weight of a monomer which carries at least one hydroxyl group and is copolymerisable with (b1), (b3) and (b4), or a mixture of such monomers(b3) 0 to 8 % by weight of a monomer which carries at least one carboxyl or sulphonic acid group and is copolymerisable with (b1), (b2) and (b4), or a mixture of such monomers, and(b4) 0 to 25 % by weight of a further monomer which is copolymerisable with (b1), (b2) and (b3), or a mixture of such monomers,after at least 80 % by weight of the monomer or the mixture of monomers used in the first stage has reacted, in the presence of the polymer obtained in the first stage, the sum of the parts by weight of (b1), (b2), (b3) and (b4) always being 100 % by weight and (b1), (b2), (b3) and (b4) being chosen such that an exclusive polymerisation of the mixture of monomers used in the second stage gives rise to a polymer having a glass transition temperature (TG₂) of -60 to +20°C, the reaction conditions being chosen such that the resultant emulsion polymer has a number average molecular mass of 200,000 to 2,000,000, and the nature and amount of the ethylenically unsaturated monomer or the mixture of monomers used in the first stage and the nature and amount of the mixture of monomers used in the second stage are chosen such that the resultant emulsion polymer has a hydroxyl value of 2 to 100 and the difference TG₁ - TG₂ is 10 to 170°C.
- Process according to Claim 10 characterised in that 99.5 to 75 % by weight of component (a1) and/or 0.5 to 25 % by weight of component (a2) and/or 75 to 90 % by weight of component (b1) and/or 5 to 15 % by weight of component (b2) and/or 2 to 6 % by weight of component (b3) and/or 2 to 15 % by weight of component (b4) are polymerised.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT90900099T ATE91923T1 (en) | 1988-12-09 | 1989-11-27 | PROCESSES FOR MANUFACTURE OF MULTI-LAYER COATING, WATER-THINNABLE COATING COMPOSITIONS, WATER-THINNABLE EMULSION POLYMERS AND METHOD FOR MANUFACTURE OF WATER-THINNABLE EMULSION POLYMERS. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3841540 | 1988-12-09 | ||
DE3841540A DE3841540A1 (en) | 1988-12-09 | 1988-12-09 | METHOD FOR PRODUCING A MULTILAYER COATING, WATER-DUMBABLE COATING COMPOSITIONS, WATER-DUMBABLE EMULSION POLYMERS AND METHOD FOR PRODUCING WATER-DUMPABLE EMULSION POLYMERS |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0447428A1 EP0447428A1 (en) | 1991-09-25 |
EP0447428B1 true EP0447428B1 (en) | 1993-07-28 |
Family
ID=6368825
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90900099A Expired - Lifetime EP0447428B1 (en) | 1988-12-09 | 1989-11-27 | Process for the production of a multi-layer coating, water-dilutable coating compositions, water-dilutable emulsion polymers and process for the production of water-dilutable emulsion polymers |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP0447428B1 (en) |
JP (1) | JPH075860B2 (en) |
AU (1) | AU630645B2 (en) |
BR (1) | BR8907816A (en) |
CA (1) | CA2004988C (en) |
DE (2) | DE3841540A1 (en) |
ES (1) | ES2060136T3 (en) |
WO (1) | WO1990006186A1 (en) |
ZA (1) | ZA899023B (en) |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3942804A1 (en) * | 1989-12-23 | 1991-06-27 | Basf Lacke & Farben | METHOD FOR PRODUCING A MULTILAYER COATING |
DE4009000A1 (en) * | 1990-03-21 | 1991-09-26 | Basf Lacke & Farben | METHOD FOR PRODUCING A MULTI-LAYER REPAIR LACQUER |
DE4143688B4 (en) | 1991-03-30 | 2007-03-29 | Basf Coatings Ag | Use of a mixing system and process for the preparation of water-based paints and water-dilutable coating compositions |
DE4216613A1 (en) * | 1992-05-20 | 1993-11-25 | Basf Lacke & Farben | Process for producing a two-layer coating and aqueous coatings suitable for this process |
AT400440B (en) * | 1993-12-06 | 1995-12-27 | Vianova Kunstharz Ag | METHOD FOR THE PRODUCTION OF WATER-THINNABLE LACQUER AND THE USE THEREOF |
EP1241237A1 (en) * | 1995-06-07 | 2002-09-18 | The Sherwin-Williams Company | Waterborne basecoat compositions for use in basecoat/clearcoat applications |
DE19904330A1 (en) | 1999-01-28 | 2000-08-10 | Basf Coatings Ag | Aqueous coating material and module system for its production |
DE19930067A1 (en) | 1999-06-30 | 2001-01-11 | Basf Coatings Ag | Coating material and its use for the production of filler layers and stone chip protection primers |
DE19930066A1 (en) | 1999-06-30 | 2001-01-11 | Basf Coatings Ag | Color and / or effect multi-layer coating, process for their preparation and their use |
DE19930665A1 (en) | 1999-07-02 | 2001-01-11 | Basf Coatings Ag | Basecoat and its use for the production of color and / or effect basecoats and multi-layer coating |
DE19930664A1 (en) | 1999-07-02 | 2001-01-11 | Basf Coatings Ag | Clear varnish and its use for the production of clear varnishes and color and / or effect multilayer varnishes |
DE19938759A1 (en) | 1999-08-16 | 2001-02-22 | Basf Coatings Ag | Coating material and its use for the production of highly scratch-resistant multi-layer clear coats |
US6437036B1 (en) * | 1999-11-17 | 2002-08-20 | Basf Corporation | Waterborne primer with improved chip resistance |
DE19959923A1 (en) | 1999-12-11 | 2001-06-28 | Basf Coatings Ag | Aqueous primary dispersions and coating materials, processes for their preparation and their use |
DE10005819A1 (en) | 2000-02-10 | 2001-08-23 | Basf Coatings Ag | Aqueous primary dispersions, processes for their preparation and their use |
DE10018078A1 (en) | 2000-04-12 | 2001-11-08 | Basf Coatings Ag | Molding compositions and process for the production of moldings |
DE10018601A1 (en) | 2000-04-14 | 2001-10-25 | Basf Coatings Ag | Aqueous primary dispersion and coating agent useful in motor vehicle manufacture, is prepared by radical (co)polymerization of monomers dispersed in an aqueous dispersion of the cross-linking agent |
DE10029802A1 (en) | 2000-06-16 | 2002-01-03 | Basf Coatings Ag | Color and / or effect aqueous coating materials and their use for the production of color and / or effect, deformable laminates |
DE10106566A1 (en) | 2001-02-13 | 2002-08-22 | Basf Coatings Ag | Aqueous coating material substantially or completely free of volatile organic substances, process for its preparation and its use |
DE10106567A1 (en) | 2001-02-13 | 2002-08-22 | Basf Coatings Ag | Aqueous primary dispersion essentially or completely free of volatile organic substances, process for their preparation and their use |
DE10126651A1 (en) | 2001-06-01 | 2002-12-12 | Basf Coatings Ag | Use of copolymers with diphenylethylene units as emulsifiers for the production of powder slurry and coating powder for use in coating materials, adhesives and sealants, e.g. for painting cars |
US6822040B2 (en) * | 2001-09-25 | 2004-11-23 | Basf Corporation | Basecoat composition with improved repair properties |
EP3009248A1 (en) | 2014-10-13 | 2016-04-20 | RECTICEL Automobilsysteme GmbH | Method for producing an elastomeric skin having a grained surface |
CN109476816B (en) * | 2016-07-15 | 2021-09-03 | 巴斯夫涂料有限公司 | Aqueous base coat and preparation of multicoat paint system using the base coat |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4150005A (en) * | 1977-03-17 | 1979-04-17 | Rohm And Haas Company | Internally plasticized polymer latex |
GB1598419A (en) * | 1978-05-17 | 1981-09-23 | Ici Ltd | Coating process |
GB2034334B (en) * | 1978-10-24 | 1983-03-02 | Canadian Ind | Process for preparing emulsions of copolymers containing n-methylol or n-methylol ether groups |
US4973621A (en) * | 1987-04-07 | 1990-11-27 | Akzo N.V. | Aqueous coating composition based on a dispersion of an addition polymer, especially suited to be used in an aqueous base coat |
DE3807531A1 (en) * | 1988-03-08 | 1989-09-21 | Basf Ag | PRODUCTION OF AQUEOUS POLYALKYL METHACRYLATE DISPERSIONS BY EMULSION POLYMERIZATION IN TWO STAGES AND THEIR USE IN WOODEN VARNISHES |
-
1988
- 1988-12-09 DE DE3841540A patent/DE3841540A1/en not_active Withdrawn
-
1989
- 1989-11-27 JP JP2500544A patent/JPH075860B2/en not_active Expired - Fee Related
- 1989-11-27 ZA ZA899023A patent/ZA899023B/en unknown
- 1989-11-27 AU AU46550/89A patent/AU630645B2/en not_active Ceased
- 1989-11-27 BR BR898907816A patent/BR8907816A/en not_active IP Right Cessation
- 1989-11-27 DE DE9090900099T patent/DE58905068D1/en not_active Expired - Fee Related
- 1989-11-27 WO PCT/EP1989/001434 patent/WO1990006186A1/en active IP Right Grant
- 1989-11-27 ES ES90900099T patent/ES2060136T3/en not_active Expired - Lifetime
- 1989-11-27 EP EP90900099A patent/EP0447428B1/en not_active Expired - Lifetime
- 1989-12-08 CA CA002004988A patent/CA2004988C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP0447428A1 (en) | 1991-09-25 |
DE3841540A1 (en) | 1990-06-13 |
ES2060136T3 (en) | 1994-11-16 |
ZA899023B (en) | 1990-08-29 |
BR8907816A (en) | 1991-10-22 |
AU630645B2 (en) | 1992-11-05 |
AU4655089A (en) | 1990-06-26 |
CA2004988C (en) | 1999-08-24 |
WO1990006186A1 (en) | 1990-06-14 |
JPH075860B2 (en) | 1995-01-25 |
CA2004988A1 (en) | 1990-06-09 |
DE58905068D1 (en) | 1993-09-02 |
JPH04501737A (en) | 1992-03-26 |
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