CN110229317A - UV curable unsaturated polyester resin of high-vinyl degree of functionality and the preparation method and application thereof - Google Patents
UV curable unsaturated polyester resin of high-vinyl degree of functionality and the preparation method and application thereof Download PDFInfo
- Publication number
- CN110229317A CN110229317A CN201910509998.0A CN201910509998A CN110229317A CN 110229317 A CN110229317 A CN 110229317A CN 201910509998 A CN201910509998 A CN 201910509998A CN 110229317 A CN110229317 A CN 110229317A
- Authority
- CN
- China
- Prior art keywords
- polyester resin
- unsaturated polyester
- glycidyl ether
- preparation
- curable unsaturated
- 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.)
- Granted
Links
- 238000002360 preparation method Methods 0.000 title claims abstract description 44
- 229920006337 unsaturated polyester resin Polymers 0.000 title claims abstract description 35
- 229920002554 vinyl polymer Polymers 0.000 title abstract description 9
- 238000000576 coating method Methods 0.000 claims abstract description 73
- 239000011248 coating agent Substances 0.000 claims abstract description 58
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims abstract description 46
- 238000006243 chemical reaction Methods 0.000 claims abstract description 26
- 239000002253 acid Substances 0.000 claims abstract description 23
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 22
- 150000008065 acid anhydrides Chemical class 0.000 claims abstract description 22
- 239000003054 catalyst Substances 0.000 claims abstract description 20
- JJRUAPNVLBABCN-UHFFFAOYSA-N 2-(ethenoxymethyl)oxirane Chemical compound C=COCC1CO1 JJRUAPNVLBABCN-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 11
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 11
- 239000002904 solvent Substances 0.000 claims abstract description 11
- 239000003112 inhibitor Substances 0.000 claims abstract description 9
- 239000000178 monomer Substances 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims description 25
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical group CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 12
- 238000007151 ring opening polymerisation reaction Methods 0.000 claims description 12
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N 1,4-Benzenediol Natural products OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 claims description 11
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 claims description 11
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 claims description 11
- 239000004593 Epoxy Substances 0.000 claims description 10
- YSUQLAYJZDEMOT-UHFFFAOYSA-N 2-(butoxymethyl)oxirane Chemical compound CCCCOCC1CO1 YSUQLAYJZDEMOT-UHFFFAOYSA-N 0.000 claims description 9
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims description 9
- 150000001875 compounds Chemical class 0.000 claims description 9
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical compound C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 claims description 7
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 claims description 6
- 239000003085 diluting agent Substances 0.000 claims description 6
- JRMUNVKIHCOMHV-UHFFFAOYSA-M tetrabutylammonium bromide Chemical compound [Br-].CCCC[N+](CCCC)(CCCC)CCCC JRMUNVKIHCOMHV-UHFFFAOYSA-M 0.000 claims description 6
- QNYBOILAKBSWFG-UHFFFAOYSA-N 2-(phenylmethoxymethyl)oxirane Chemical compound C1OC1COCC1=CC=CC=C1 QNYBOILAKBSWFG-UHFFFAOYSA-N 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- STMDPCBYJCIZOD-UHFFFAOYSA-N 2-(2,4-dinitroanilino)-4-methylpentanoic acid Chemical compound CC(C)CC(C(O)=O)NC1=CC=C([N+]([O-])=O)C=C1[N+]([O-])=O STMDPCBYJCIZOD-UHFFFAOYSA-N 0.000 claims description 4
- DKPFZGUDAPQIHT-UHFFFAOYSA-N Butyl acetate Natural products CCCCOC(C)=O DKPFZGUDAPQIHT-UHFFFAOYSA-N 0.000 claims description 4
- ZOIORXHNWRGPMV-UHFFFAOYSA-N acetic acid;zinc Chemical compound [Zn].CC(O)=O.CC(O)=O ZOIORXHNWRGPMV-UHFFFAOYSA-N 0.000 claims description 4
- 239000000654 additive Substances 0.000 claims description 4
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 claims description 4
- 239000003960 organic solvent Substances 0.000 claims description 4
- NWVVVBRKAWDGAB-UHFFFAOYSA-N p-methoxyphenol Chemical compound COC1=CC=C(O)C=C1 NWVVVBRKAWDGAB-UHFFFAOYSA-N 0.000 claims description 4
- 239000000758 substrate Substances 0.000 claims description 4
- 239000000080 wetting agent Substances 0.000 claims description 4
- 239000004246 zinc acetate Substances 0.000 claims description 4
- MUTGBJKUEZFXGO-OLQVQODUSA-N (3as,7ar)-3a,4,5,6,7,7a-hexahydro-2-benzofuran-1,3-dione Chemical compound C1CCC[C@@H]2C(=O)OC(=O)[C@@H]21 MUTGBJKUEZFXGO-OLQVQODUSA-N 0.000 claims description 3
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 claims description 3
- HRWYHCYGVIJOEC-UHFFFAOYSA-N 2-(octoxymethyl)oxirane Chemical compound CCCCCCCCOCC1CO1 HRWYHCYGVIJOEC-UHFFFAOYSA-N 0.000 claims description 3
- ZADXFVHUPXKZBJ-UHFFFAOYSA-N 2-[(4-ethenylphenyl)methoxymethyl]oxirane Chemical compound C1=CC(C=C)=CC=C1COCC1OC1 ZADXFVHUPXKZBJ-UHFFFAOYSA-N 0.000 claims description 3
- NCAVPEPBIJTYSO-UHFFFAOYSA-N 4-hydroxybutyl prop-2-enoate;2-(oxiran-2-ylmethoxymethyl)oxirane Chemical compound C1OC1COCC1CO1.OCCCCOC(=O)C=C NCAVPEPBIJTYSO-UHFFFAOYSA-N 0.000 claims description 3
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 3
- 239000013530 defoamer Substances 0.000 claims description 3
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 claims description 3
- VYKXQOYUCMREIS-UHFFFAOYSA-N methylhexahydrophthalic anhydride Chemical compound C1CCCC2C(=O)OC(=O)C21C VYKXQOYUCMREIS-UHFFFAOYSA-N 0.000 claims description 3
- 229940014800 succinic anhydride Drugs 0.000 claims description 3
- HWCKGOZZJDHMNC-UHFFFAOYSA-M tetraethylammonium bromide Chemical compound [Br-].CC[N+](CC)(CC)CC HWCKGOZZJDHMNC-UHFFFAOYSA-M 0.000 claims description 3
- QBVXKDJEZKEASM-UHFFFAOYSA-M tetraoctylammonium bromide Chemical compound [Br-].CCCCCCCC[N+](CCCCCCCC)(CCCCCCCC)CCCCCCCC QBVXKDJEZKEASM-UHFFFAOYSA-M 0.000 claims description 3
- SRPWOOOHEPICQU-UHFFFAOYSA-N trimellitic anhydride Chemical compound OC(=O)C1=CC=C2C(=O)OC(=O)C2=C1 SRPWOOOHEPICQU-UHFFFAOYSA-N 0.000 claims description 3
- 229920002818 (Hydroxyethyl)methacrylate Polymers 0.000 claims description 2
- VLDPXPPHXDGHEW-UHFFFAOYSA-N 1-chloro-2-dichlorophosphoryloxybenzene Chemical compound ClC1=CC=CC=C1OP(Cl)(Cl)=O VLDPXPPHXDGHEW-UHFFFAOYSA-N 0.000 claims description 2
- 239000012956 1-hydroxycyclohexylphenyl-ketone Substances 0.000 claims description 2
- XLPJNCYCZORXHG-UHFFFAOYSA-N 1-morpholin-4-ylprop-2-en-1-one Chemical compound C=CC(=O)N1CCOCC1 XLPJNCYCZORXHG-UHFFFAOYSA-N 0.000 claims description 2
- VOBUAPTXJKMNCT-UHFFFAOYSA-N 1-prop-2-enoyloxyhexyl prop-2-enoate Chemical compound CCCCCC(OC(=O)C=C)OC(=O)C=C VOBUAPTXJKMNCT-UHFFFAOYSA-N 0.000 claims description 2
- XMLYCEVDHLAQEL-UHFFFAOYSA-N 2-hydroxy-2-methyl-1-phenylpropan-1-one Chemical compound CC(C)(O)C(=O)C1=CC=CC=C1 XMLYCEVDHLAQEL-UHFFFAOYSA-N 0.000 claims description 2
- GNSFRPWPOGYVLO-UHFFFAOYSA-N 3-hydroxypropyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCCO GNSFRPWPOGYVLO-UHFFFAOYSA-N 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 claims description 2
- DAKWPKUUDNSNPN-UHFFFAOYSA-N Trimethylolpropane triacrylate Chemical group C=CC(=O)OCC(CC)(COC(=O)C=C)COC(=O)C=C DAKWPKUUDNSNPN-UHFFFAOYSA-N 0.000 claims description 2
- MQDJYUACMFCOFT-UHFFFAOYSA-N bis[2-(1-hydroxycyclohexyl)phenyl]methanone Chemical compound C=1C=CC=C(C(=O)C=2C(=CC=CC=2)C2(O)CCCCC2)C=1C1(O)CCCCC1 MQDJYUACMFCOFT-UHFFFAOYSA-N 0.000 claims description 2
- -1 butyl catechols Chemical class 0.000 claims description 2
- 238000004821 distillation Methods 0.000 claims description 2
- AUHZEENZYGFFBQ-UHFFFAOYSA-N 1,3,5-trimethylbenzene Chemical group CC1=CC(C)=CC(C)=C1 AUHZEENZYGFFBQ-UHFFFAOYSA-N 0.000 claims 2
- VFZKVQVQOMDJEG-UHFFFAOYSA-N 2-prop-2-enoyloxypropyl prop-2-enoate Chemical compound C=CC(=O)OC(C)COC(=O)C=C VFZKVQVQOMDJEG-UHFFFAOYSA-N 0.000 claims 1
- 239000012752 auxiliary agent Substances 0.000 claims 1
- UQRKXZOISAAYQQ-UHFFFAOYSA-N diphenylphosphorylformaldehyde Chemical compound C=1C=CC=CC=1P(=O)(C=O)C1=CC=CC=C1 UQRKXZOISAAYQQ-UHFFFAOYSA-N 0.000 claims 1
- 125000000687 hydroquinonyl group Chemical group C1(O)=C(C=C(O)C=C1)* 0.000 claims 1
- 229920000728 polyester Polymers 0.000 abstract description 19
- 239000007787 solid Substances 0.000 abstract description 13
- 229920006305 unsaturated polyester Polymers 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 4
- 238000007142 ring opening reaction Methods 0.000 abstract description 2
- 238000003756 stirring Methods 0.000 abstract description 2
- 238000005292 vacuum distillation Methods 0.000 abstract description 2
- 229920001577 copolymer Polymers 0.000 abstract 1
- 150000002118 epoxides Chemical class 0.000 abstract 1
- 230000007928 solubilization Effects 0.000 abstract 1
- 238000005063 solubilization Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 24
- 229920001225 polyester resin Polymers 0.000 description 19
- 239000004645 polyester resin Substances 0.000 description 19
- 238000003848 UV Light-Curing Methods 0.000 description 13
- 238000005516 engineering process Methods 0.000 description 12
- 239000000047 product Substances 0.000 description 12
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- 125000001931 aliphatic group Chemical group 0.000 description 9
- 229920003232 aliphatic polyester Polymers 0.000 description 9
- 229920005989 resin Polymers 0.000 description 9
- 239000011347 resin Substances 0.000 description 9
- 239000004744 fabric Substances 0.000 description 8
- 239000011521 glass Substances 0.000 description 8
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 4
- 238000004132 cross linking Methods 0.000 description 4
- 125000003700 epoxy group Chemical group 0.000 description 4
- JIGUICYYOYEXFS-UHFFFAOYSA-N 3-tert-butylbenzene-1,2-diol Chemical compound CC(C)(C)C1=CC=CC(O)=C1O JIGUICYYOYEXFS-UHFFFAOYSA-N 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 3
- 239000004925 Acrylic resin Substances 0.000 description 3
- 229920000178 Acrylic resin Polymers 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 150000008064 anhydrides Chemical class 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000005886 esterification reaction Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 2
- 238000001723 curing Methods 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 2
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- RSWGJHLUYNHPMX-UHFFFAOYSA-N 1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylic acid Chemical compound C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 1
- ZDQNWDNMNKSMHI-UHFFFAOYSA-N 1-[2-(2-prop-2-enoyloxypropoxy)propoxy]propan-2-yl prop-2-enoate Chemical compound C=CC(=O)OC(C)COC(C)COCC(C)OC(=O)C=C ZDQNWDNMNKSMHI-UHFFFAOYSA-N 0.000 description 1
- FQXGHZNSUOHCLO-UHFFFAOYSA-N 2,2,4,4-tetramethyl-1,3-cyclobutanediol Chemical compound CC1(C)C(O)C(C)(C)C1O FQXGHZNSUOHCLO-UHFFFAOYSA-N 0.000 description 1
- RIWRBSMFKVOJMN-UHFFFAOYSA-N 2-methyl-1-phenylpropan-2-ol Chemical compound CC(C)(O)CC1=CC=CC=C1 RIWRBSMFKVOJMN-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- PODOEQVNFJSWIK-UHFFFAOYSA-N diphenylphosphoryl-(2,4,6-trimethoxyphenyl)methanone Chemical compound COC1=CC(OC)=CC(OC)=C1C(=O)P(=O)(C=1C=CC=CC=1)C1=CC=CC=C1 PODOEQVNFJSWIK-UHFFFAOYSA-N 0.000 description 1
- VFHVQBAGLAREND-UHFFFAOYSA-N diphenylphosphoryl-(2,4,6-trimethylphenyl)methanone Chemical compound CC1=CC(C)=CC(C)=C1C(=O)P(=O)(C=1C=CC=CC=1)C1=CC=CC=C1 VFHVQBAGLAREND-UHFFFAOYSA-N 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- RPQRDASANLAFCM-UHFFFAOYSA-N oxiran-2-ylmethyl prop-2-enoate Chemical compound C=CC(=O)OCC1CO1 RPQRDASANLAFCM-UHFFFAOYSA-N 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 238000003847 radiation curing Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/24—Preparation of carboxylic acid esters by reacting carboxylic acids or derivatives thereof with a carbon-to-oxygen ether bond, e.g. acetal, tetrahydrofuran
- C07C67/26—Preparation of carboxylic acid esters by reacting carboxylic acids or derivatives thereof with a carbon-to-oxygen ether bond, e.g. acetal, tetrahydrofuran with an oxirane ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/76—Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring
- C07C69/80—Phthalic acid esters
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
- C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
- C08G63/52—Polycarboxylic acids or polyhydroxy compounds in which at least one of the two components contains aliphatic unsaturation
- C08G63/56—Polyesters derived from ester-forming derivatives of polycarboxylic acids or of polyhydroxy compounds other than from esters thereof
- C08G63/58—Cyclic ethers; Cyclic carbonates; Cyclic sulfites ; Cyclic orthoesters
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
- C08G63/81—Preparation processes using solvents
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D167/00—Coating compositions based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Coating compositions based on derivatives of such polymers
- C09D167/06—Unsaturated polyesters having carbon-to-carbon unsaturation
- C09D167/07—Unsaturated polyesters having carbon-to-carbon unsaturation having terminal carbon-to-carbon unsaturated bonds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D4/00—Coating compositions, e.g. paints, varnishes or lacquers, based on organic non-macromolecular compounds having at least one polymerisable carbon-to-carbon unsaturated bond ; Coating compositions, based on monomers of macromolecular compounds of groups C09D183/00 - C09D183/16
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Macromonomer-Based Addition Polymer (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种聚酯树脂,特别涉及一种可紫外光固化的不饱和聚酯树脂及其制备方法与应用,属于精细化工领域。The invention relates to a polyester resin, in particular to an ultraviolet-curable unsaturated polyester resin and a preparation method and application thereof, belonging to the field of fine chemicals.
背景技术Background technique
UV固化涂料是指UV光照射使得光引发剂裂解成为自由基或阴阳离子,进一步引发含活性基团的单体发生聚合反应,聚合成不溶不熔的固体涂膜。与传统的固化技术相比,UV固化技术节约能源、固化速度快、涂膜性能好、适用于大规模工业化生产。常用的聚酯丙烯酸酯的制备是在羟基聚酯树脂分子链上,通过酯化反应将丙烯酸引入到聚酯链上,需要160-200℃酯化反应,作为脱水溶剂的苯及其同系物有毒,不易从树脂中脱除。如中国发明专利申请CN105061738A通过将对苯二甲酸与2,2,4,4-四甲基-1,3-环丁二醇以及乙二醇在催化剂的作用下发生缩聚反应,反应温度200-260℃,得到缩聚产物,而后向上述反应后的体系中加入丙烯酸或丙烯酸酯,反应制得聚酯型丙烯酸UV固化单体。中国发明专利申请CN105504245A先制备含羧基的聚酯树脂,其酯化反应温度在200℃,然后与丙烯酸缩水甘油醚或甲基丙烯酸缩水甘油醚反应制备乙烯基聚酯树脂,原料成本高,且耗能高,不利于大规模工业生产。文献报道可UV固化聚酯树脂的制备需要在较高温度(180℃以上)酯化,引入乙烯基或丙烯酸单体工艺复杂,成本较高。UV curable coating means that UV light irradiation makes the photoinitiator crack into free radicals or anions and cations, further triggers the polymerization reaction of monomers containing active groups, and polymerizes into an insoluble and infusible solid coating film. Compared with traditional curing technology, UV curing technology saves energy, has fast curing speed, good coating performance, and is suitable for large-scale industrial production. The preparation of commonly used polyester acrylate is to introduce acrylic acid into the polyester chain through esterification reaction on the molecular chain of hydroxyl polyester resin, which requires an esterification reaction at 160-200 ° C. As a dehydration solvent, benzene and its homologues are poisonous , not easily removed from the resin. For example, the Chinese invention patent application CN105061738A undergoes a polycondensation reaction of terephthalic acid, 2,2,4,4-tetramethyl-1,3-cyclobutanediol and ethylene glycol under the action of a catalyst, and the reaction temperature is 200- 260°C to obtain a polycondensation product, and then add acrylic acid or acrylate to the above-mentioned reacted system to react to obtain a polyester-type acrylic UV-curable monomer. Chinese invention patent application CN105504245A first prepares carboxyl-containing polyester resin, and its esterification reaction temperature is 200 ° C, and then reacts with glycidyl acrylate or glycidyl methacrylate to prepare vinyl polyester resin, the cost of raw materials is high, and consumption High energy, not conducive to large-scale industrial production. It is reported in the literature that the preparation of UV-curable polyester resin needs to be esterified at a relatively high temperature (above 180°C), and the process of introducing vinyl or acrylic monomer is complicated and the cost is high.
中国发明专利申请2016111382348(CN106748765A,2017.5.31)公开了一种可UV固化聚酯及其制备方法与应用。其制备方法是:1)按摩尔分数计,将1份三缩水甘油醚和3-4份的丙烯酸单体混合于反应釜中,并加入季铵盐类催化剂、阻聚剂有机溶剂于105-125℃下反应至酸值低于10mgKOH/g;2)在步骤1)制备的基质中加入酸酐、阻聚剂和对甲苯磺酸,于105-130℃下反应2-4h,然后加入酸酐摩尔数的0.9-1.2倍的环氧化合物,并加入季铵盐类催化剂和有机溶剂反应至酸值小于10mgKOH/g,减压蒸馏脱除溶剂,降温出料;该树脂固体分达到100%以上,黏度为3000-30000mPa·s。采用该聚酯制备的UV固化涂料,涂膜性能优异且成本较低。但该技术制备的聚酯丙烯酸树脂的乙烯基含量少,因一份三缩水甘油醚与丙烯酸反应,最多可在树脂分子链上引入3个乙烯基,即产物树脂的乙烯基官能度为3,UV固化后期涂膜的交联密度低,降低涂膜的耐化学品性。起始物三缩水甘油醚大多价格昂贵,提高了可UV固化聚酯丙烯酸树脂的成本。Chinese invention patent application 2016111382348 (CN106748765A, 2017.5.31) discloses a UV curable polyester and its preparation method and application. Its preparation method is: 1) In terms of mole fraction, mix 1 part of triglycidyl ether and 3-4 parts of acrylic acid monomer in a reaction kettle, and add quaternary ammonium salt catalyst, polymerization inhibitor organic solvent in 105- React at 125°C until the acid value is lower than 10mgKOH/g; 2) Add acid anhydride, polymerization inhibitor and p-toluenesulfonic acid to the matrix prepared in step 1), react at 105-130°C for 2-4h, and then add moles of acid anhydride 0.9-1.2 times the number of epoxy compounds, and add a quaternary ammonium salt catalyst and an organic solvent to react until the acid value is less than 10mgKOH/g, remove the solvent by distillation under reduced pressure, cool down and discharge the material; the solid content of the resin reaches more than 100%, The viscosity is 3000-30000mPa·s. The UV curable coating prepared by the polyester has excellent film performance and low cost. However, the vinyl content of the polyester acrylic resin prepared by this technology is small, because a part of triglycidyl ether reacts with acrylic acid, and at most 3 vinyl groups can be introduced on the resin molecular chain, that is, the vinyl functionality of the product resin is 3, The crosslinking density of the coating film in the later stage of UV curing is low, which reduces the chemical resistance of the coating film. The starting triglycidyl ethers are mostly expensive, increasing the cost of UV-curable polyester acrylic resins.
发明内容Contents of the invention
本发明的首要目的在于提供一种成本相对较低,交联密度高,耐化学品性能好,且节能的高乙烯基官能度的可UV固化不饱和聚酯树脂及其制备方法;本发明可获得固含为85wt%以上,黏度为2000~6000mPa·s(25℃)的UV固化聚酯。The primary purpose of the present invention is to provide a relatively low cost, high cross-linking density, good chemical resistance, and energy-saving UV-curable unsaturated polyester resin with high vinyl functionality and a preparation method thereof; A UV curable polyester with a solid content of more than 85 wt % and a viscosity of 2000-6000 mPa·s (25° C.) is obtained.
本发明的另一目的在于提供由上述方法制备得到的UV固化树脂在涂料中的应用。采用本发明可UV固化树脂制备的涂膜性能优异,其涂膜硬度可达2H。Another object of the present invention is to provide the application of the UV curable resin prepared by the above method in coatings. The coating film prepared by adopting the UV curable resin of the invention has excellent performance, and the coating film hardness can reach 2H.
本发明的目的通过以下技术方案实现:The object of the present invention is achieved through the following technical solutions:
高乙烯基官能度可UV固化不饱和聚酯树脂的制备方法,其质量百分比组成为:酸酐:33~42%,乙烯基缩水甘油醚:11~24%,环氧化合物:18~34%,阻聚剂0.1~0.5%,有机溶剂10~20%。其制备步骤如下:在氮气保护下,向装有搅拌器、温度计的三口烧瓶中加入酸酐、环氧化合物、催化剂和溶剂,搅拌并加热到90~120℃并保温1-3h;然后在1-2h内逐滴加入溶有阻聚剂的乙烯基缩水甘油醚,在90~120℃下开环共聚反应4-6h,测定反应体系酸值至15mg KOH/g以下,减压蒸馏脱除未反应的单体和溶剂,得到浅黄色透明不饱和聚酯。The invention discloses a method for preparing a UV-curable unsaturated polyester resin with high vinyl functionality. The mass percentage consists of: acid anhydride: 33-42%, vinyl glycidyl ether: 11-24%, epoxy compound: 18-34%, Inhibitor 0.1-0.5%, organic solvent 10-20%. The preparation steps are as follows: under the protection of nitrogen, add acid anhydride, epoxy compound, catalyst and solvent into a three-necked flask equipped with a stirrer and a thermometer, stir and heat to 90-120°C and keep it warm for 1-3h; Add vinyl glycidyl ether dissolved in a polymerization inhibitor dropwise within 2 hours, conduct ring-opening copolymerization reaction at 90-120°C for 4-6 hours, measure the acid value of the reaction system to below 15mg KOH/g, and remove unreacted by vacuum distillation monomer and solvent to obtain light yellow transparent unsaturated polyester.
所述的酸酐包括邻苯二甲酸酐、偏苯三酸酐、六氢苯酐、甲基六氢苯酐及均苯四甲酸二酐等的一种或两种以上。The acid anhydrides include one or more of phthalic anhydride, trimellitic anhydride, hexahydrophthalic anhydride, methylhexahydrophthalic anhydride and pyromellitic dianhydride.
所述的环氧化合物包括环氧氯丙烷、正丁基缩水甘油醚、辛基缩水甘油醚、苄基缩水甘油醚、叔碳酸缩水甘油酯及C12~14缩水甘油醚中的一种或两种以上。The epoxy compound includes one or both of epichlorohydrin, n-butyl glycidyl ether, octyl glycidyl ether, benzyl glycidyl ether, glycidyl tert-carbonate and C12 ~14 glycidyl ether. more than one species.
所述的乙烯基缩水甘油醚包括甲基丙烯酸缩水甘油酯、烯丙基缩水甘油醚、4-乙烯基苄基缩水甘油醚及4-羟基丁基丙烯酸酯缩水甘油醚中的一种或两种以上。The vinyl glycidyl ether includes one or both of glycidyl methacrylate, allyl glycidyl ether, 4-vinylbenzyl glycidyl ether and 4-hydroxybutyl acrylate glycidyl ether above.
所述的溶剂包括乙酸乙酯、乙酸丁酯、丁酮及环己酮中的一种或两种以上。The solvent includes one or more of ethyl acetate, butyl acetate, butanone and cyclohexanone.
所述的催化剂包括四乙基溴化铵、四丁基溴化铵、四辛基溴化铵及醋酸锌中的一种或两种以上。所述的催化剂用量为酸酐质量的1%~5%。The catalyst includes one or more of tetraethylammonium bromide, tetrabutylammonium bromide, tetraoctylammonium bromide and zinc acetate. The dosage of the catalyst is 1%-5% of the mass of the acid anhydride.
所述的阻聚剂包括对苯二酚、对羟基苯甲醚及叔丁基邻苯二酚中的一种或两种以上。The polymerization inhibitor includes one or more of hydroquinone, p-hydroxyanisole and tert-butylcatechol.
一种高乙烯基官能度可UV固化不饱和聚酯树脂,由上述的制备方法制得,25℃下黏度为2000~6000mPa·s。A UV-curable unsaturated polyester resin with high vinyl functionality, prepared by the above preparation method, has a viscosity of 2000-6000mPa·s at 25°C.
所述的高乙烯基官能度可UV固化不饱和聚酯树脂在涂料中的应用,在聚酯中添加活性稀释剂和光引发剂,质量百分比组成为:聚酯树脂65~75%,活性稀释剂20~35%,光引发剂2~5%,其他助剂0.1~0.5%,经UV固化成膜。所述活性稀释剂包括三羟甲基丙烷三丙烯酸酯、三丙二醇二丙烯酸酯、己二醇二丙烯酸酯、甲基丙烯酸羟乙酯、甲基丙烯酸羟丙酯和丙烯酰吗啉等的一种或两种以上;The application of the UV-curable unsaturated polyester resin with high vinyl functionality in coatings includes adding a reactive diluent and a photoinitiator to the polyester, and the mass percentage is composed of: polyester resin 65% to 75%, reactive diluent 20-35%, photoinitiator 2-5%, other additives 0.1-0.5%, film-forming by UV curing. The active diluent includes trimethylolpropane triacrylate, tripropylene glycol diacrylate, hexanediol diacrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate and acryloyl morpholine, etc. or two or more;
所述光引发剂包括2,4,6-三甲基苯甲酰基-二苯基氧化膦(Lucirin TPO)、2-羟基-2-甲基-1-苯基-1-丙酮(Darocur 1173)及1-羟基环己基苯基甲酮等的一种或两种以上;The photoinitiators include 2,4,6-trimethylbenzoyl-diphenylphosphine oxide (Lucirin TPO), 2-hydroxy-2-methyl-1-phenyl-1-propanone (Darocur 1173) One or more of 1-hydroxycyclohexyl phenyl ketone, etc.;
所述的其他助剂包括流平剂、基材润湿剂及消泡剂中的一种或两种以上。The other additives include one or more of leveling agent, substrate wetting agent and defoamer.
所述的流平剂包括德国BYK 358N、BYK 306及BYK 371中的一种或两种以上;The leveling agent includes one or more of German BYK 358N, BYK 306 and BYK 371;
所述的消泡剂包括德国毕克公司的BYK 024、BYK 028及BYK 141中的一种或两种以上;The defoamer includes one or more of BYK 024, BYK 028 and BYK 141 of BYK, Germany;
所述的基材润湿剂包括赢创德固赛公司的TEGO 2250、TEGO 270及TEGO245中的一种或两种以上。其UV固化涂膜铅笔硬度达2H,具有优异的耐水性和耐醇性。The substrate wetting agent includes one or more of TEGO 2250, TEGO 270 and TEGO 245 from Evonik Degussa. Its UV curable coating has a pencil hardness of 2H and has excellent water resistance and alcohol resistance.
本发明的技术原理如下:Technical principle of the present invention is as follows:
本发明通过酸酐与乙烯基缩水甘油醚的环氧基团开环聚合制备出不饱和脂肪族聚酯;在聚合反应体系中,酸酐首先和催化剂配位、活化、开环,生成酯基阴离子,阴离子进攻被催化剂配位、活化的环氧基团,导致环氧基团开环插入到聚合物主链,酸酐和乙烯基缩水甘油醚交替插入聚合物增长链生成含大量乙烯基的聚酯,该聚酯分子链上含有大量的乙烯基缩水甘油醚,乙烯基的官能度很高,可进行UV固化;为了调控不饱和聚酯的乙烯基官能度,采用不含乙烯基的环氧化合物参与聚合反应,降低乙烯基缩水甘油醚的添加量,同时也降低树脂的黏度和成本。The present invention prepares the unsaturated aliphatic polyester through the ring-opening polymerization of the epoxy group of the acid anhydride and vinyl glycidyl ether; in the polymerization reaction system, the acid anhydride first coordinates with the catalyst, activates, and opens the ring to generate an ester group anion, The anion attacks the epoxy group coordinated and activated by the catalyst, causing the epoxy group to open and insert into the polymer main chain, and the acid anhydride and vinyl glycidyl ether are alternately inserted into the polymer chain to form a polyester containing a large number of vinyl groups. The polyester molecular chain contains a large amount of vinyl glycidyl ether, the vinyl functionality is very high, and can be cured by UV; in order to regulate the vinyl functionality of the unsaturated polyester, an epoxy compound without vinyl is used to participate Polymerization reaction reduces the amount of vinyl glycidyl ether added, and also reduces the viscosity and cost of the resin.
与现有技术相比,本发明具有如下优点:Compared with prior art, the present invention has following advantage:
1.本发明通过酸酐与乙烯基缩水甘油醚的开环聚合制备出高乙烯基官能度的不饱和聚酯,用于可UV固化涂料;该方法所用原料来源广、价格低,反应步骤少,配方简单,工业上操作难度低,与现有技术相比可节约大量成本,十分适合工业大规模生产;1. The present invention prepares the unsaturated polyester of high vinyl functionality by the ring-opening polymerization of acid anhydride and vinyl glycidyl ether, which is used for UV-curable coatings; the method uses wide sources of raw materials, low price, and few reaction steps. The formula is simple, the difficulty of industrial operation is low, and compared with the existing technology, it can save a lot of cost, and is very suitable for industrial mass production;
2.相比传统酸与醇生成聚酯的反应,本反应不产生副产物水,不需要苯类物质做带水剂和溶剂,且反应温度不超过120℃,工艺更加简单、节能降耗和安全环保;2. Compared with the traditional reaction of acid and alcohol to produce polyester, this reaction does not produce by-product water, does not need benzene substances as water-carrying agents and solvents, and the reaction temperature does not exceed 120 ° C, the process is simpler, energy saving and consumption reduction. Safety and environmental protection;
3.本发明制备的聚酯树脂,经UV固化成膜后,涂膜硬度高,附着力优异,此外涂膜具有高光泽以及良好的耐介质性能。3. The polyester resin prepared by the present invention has high coating film hardness and excellent adhesion after UV curing to form a film. In addition, the coating film has high gloss and good medium resistance.
附图说明Description of drawings
图1为实施例1中产物可UV固化聚酯的红外光谱图。Fig. 1 is the infrared spectrogram of the product UV curable polyester in Example 1.
图2实施例1制备的可UV固化聚酯的结构图。其中结构式1为邻苯二甲酸酐与甲基丙烯酸缩水甘油醚反应的产物聚合物结构式;结构式2为在实施例1反应中添加正丁基缩水甘油醚的产物结构式。FIG. 2 is a structural diagram of the UV-curable polyester prepared in Example 1. FIG. Wherein, structural formula 1 is the product polymer structural formula of the reaction between phthalic anhydride and methacrylic acid glycidyl ether; structural formula 2 is the product structural formula of adding n-butyl glycidyl ether in the reaction of Example 1.
具体实施方式Detailed ways
为更好理解本发明,下面结合附图和实施例对本发明作进一步的描述,但本发明的实施方式不限如此。In order to better understand the present invention, the present invention will be further described below in conjunction with the accompanying drawings and examples, but the embodiments of the present invention are not limited thereto.
实施例中对比的巴斯夫Laromer LR 9004是由德国巴斯夫公司生产,主要用于纸、PVC、木材和木产品辐射固化光油和印刷油墨生产用途的弹性聚酯丙烯酸酯,有良好的稳定性和低温柔韧性,属于市场占有率较大的一类聚酯丙烯酸树脂。The BASF Laromer LR 9004 compared in the embodiment is produced by BASF, Germany, and is mainly used in the elastic polyester acrylate of paper, PVC, wood and wood products radiation curing varnish and printing ink production purposes, with good stability and low temperature Flexibility, belongs to a class of polyester acrylic resin with a large market share.
下面实施例中,UV固化聚酯树脂和光固化涂料的性能按照以下方法检测:根据GB/T 21059-2007使用NDJ-1型旋转黏度计测定树脂黏度;根据GB/T 6743-2008测定树脂酸值;根据GB/T 6739-2006测定涂膜硬度;根据GB/T 9286-1998测定涂膜附着力;根据GB/T9754-2007采用60°角WGG60-E4型光泽度计测定涂膜光泽;根据GB/T 5209-1985采用室温浸泡法测定涂膜耐水性;根据GB/T 4893.1-2005测定涂膜耐醇性。In the following examples, the performance of UV-curable polyester resin and light-curable coating is detected according to the following methods: use NDJ-1 type rotational viscometer to measure resin viscosity according to GB/T 21059-2007; measure resin acid value according to GB/T 6743-2008 ; Measure the hardness of the coating film according to GB/T 6739-2006; measure the adhesion of the coating film according to GB/T 9286-1998; /T 5209-1985 uses room temperature immersion method to measure the water resistance of the coating film; according to GB/T 4893.1-2005, the alcohol resistance of the coating film is measured.
实施例1Example 1
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表1(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is as shown in Table 1 (catalyst is not included):
表1Table 1
2)高乙烯基官能度的可UV固化不饱和聚酯树脂的制备工艺包括以下步骤:2) The preparation technology of UV-curable unsaturated polyester resin with high vinyl functionality comprises the following steps:
图2中分子结构式1为邻苯二甲酸酐与甲基丙烯酸缩水甘油醚反应的产物聚合物结构式,其中n为重复链节的个数,一般大于6;通过调整苯酐与甲基丙烯酸缩水甘油醚的物质的量的比例来调控产物分子量一般在2000以上,即n值在6-10。图2中结构式2为在上述反应中添加正丁基缩水甘油醚的产物结构式,其主要作用是调控不饱和聚酯中乙烯基的官能度,即乙烯基含量,从而调控涂膜的交联密度,进而调控涂膜硬度和耐化学品性及成本。Molecular structural formula 1 in Fig. 2 is the product polymer structural formula of phthalic anhydride and methacrylic acid glycidyl ether reaction, and wherein n is the number of repeating chain link, generally greater than 6; By adjusting phthalic anhydride and methacrylic acid glycidyl ether The ratio of the amount of the substance to control the molecular weight of the product is generally above 2000, that is, the n value is 6-10. Structural formula 2 in Figure 2 is the product structural formula of adding n-butyl glycidyl ether in the above reaction, and its main function is to regulate the functionality of the vinyl group in the unsaturated polyester, that is, the vinyl content, thereby regulating the crosslinking density of the coating film , and then control the hardness of the coating film, chemical resistance and cost.
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入邻苯二甲酸酐、正丁基缩水甘油醚、乙酸乙酯和四乙基溴化铵(酸酐质量分数的1.0%)混合均匀,升温至90℃保温1h,然后逐滴加入溶有对苯二酚的甲基丙烯酸缩水甘油酯,1.5h滴完,在100℃下开环共聚反应4h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under nitrogen protection, add phthalic anhydride, n-butyl glycidyl ether, ethyl acetate and tetraethylammonium bromide (1.0% of the mass fraction of anhydride) to a flask equipped with a stirrer and a thermometer according to a given mass. ) mix evenly, raise the temperature to 90°C and keep it warm for 1h, then add glycidyl methacrylate dissolved in hydroquinone drop by drop, finish dripping in 1.5h, perform ring-opening copolymerization reaction at 100°C for 4h until the acid value drops to 15mgKOH/ g, lower the temperature and discharge to obtain UV curable unsaturated aliphatic polyester.
3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:淡黄色透明;固含:88.41%;酸值:8.5mgKOH/g,黏度(25℃):4075mPa·s。3) Physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: Appearance: pale yellow and transparent; solid content: 88.41%; acid value: 8.5mgKOH/g, viscosity (25°C): 4075mPa·s.
4)UV固化涂料的制备及性能4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表2:In parts by mass, the composition of the UV curable coating is as follows in Table 2:
表2Table 2
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表3所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 3 below:
表3table 3
表3说明本实施例制备的UV固化聚酯树脂涂膜光泽度高、硬度高且耐水性优异。Table 3 shows that the UV curable polyester resin coating film prepared in this example has high gloss, high hardness and excellent water resistance.
图1为所制备的UV固化聚酯树脂红外光谱图,图中没有出现邻苯二甲酸酐在1760cm-1、1850cm-1处的酸酐羰基振动吸收峰,证明酸酐在开环共聚期间反应;在905、913cm-1处左右不存在环氧基的特征吸收峰,证明环氧化合物和酸酐发生了开环反应,生成图2结构式2所示的结构;在1726cm-1处出现强且尖锐的酯羰基峰,1640cm-1处出现-C=C-的特征吸收峰,证明可UV固化不饱和聚酯的生成。图2中分子结构式1为邻苯二甲酸酐与甲基丙烯酸缩水甘油醚反应的产物聚合物结构式,其中n为重复链节的个数,一般大于6;通过调整苯酐与甲基丙烯酸缩水甘油醚的物质的量的比例来调控产物分子量一般在2000以上,即n值在6-10。图2中结构式2为在上述反应中添加正丁基缩水甘油醚的产物结构式,其主要作用是调控不饱和聚酯中乙烯基的官能度,即乙烯基含量,从而调控涂膜的交联密度,进而调控涂膜硬度和耐化学品性及成本。Figure 1 is the infrared spectrogram of the prepared UV curable polyester resin, in which there is no carbonyl vibration absorption peak of phthalic anhydride at 1760cm -1 and 1850cm- 1 , which proves that the acid anhydride reacts during the ring-opening copolymerization; There are no characteristic absorption peaks of epoxy groups at around 905 and 913 cm -1 , which proves that epoxy compounds and acid anhydrides undergo a ring-opening reaction to form the structure shown in Figure 2 Structural Formula 2; a strong and sharp ester appears at 1726 cm -1 The carbonyl peak and the characteristic absorption peak of -C=C- appear at 1640cm -1 , which proves the generation of UV-curable unsaturated polyester. Molecular structural formula 1 in Fig. 2 is the product polymer structural formula of phthalic anhydride and methacrylic acid glycidyl ether reaction, and wherein n is the number of repeating chain link, generally greater than 6; By adjusting phthalic anhydride and methacrylic acid glycidyl ether The ratio of the amount of the substance to control the molecular weight of the product is generally above 2000, that is, the n value is 6-10. Structural formula 2 in Figure 2 is the product structural formula of adding n-butyl glycidyl ether in the above reaction, and its main function is to regulate the functionality of the vinyl group in the unsaturated polyester, that is, the vinyl content, thereby regulating the crosslinking density of the coating film , and then control the hardness of the coating film, chemical resistance and cost.
与中国发明专利申请2016111382348(CN106748765A,2017.5.31)相比,本实施例乙烯基官能度从3个增大到6个以上,制备工艺从两步法工艺变为一步法工艺,不需使用价格昂贵的三缩水甘油醚为起始物;通过改变环氧单体的种类和比例,可有效调控不饱和聚酯的乙烯基官能度、黏度和性能,制备出高固含量,低黏度的UV固化聚酯。因此,本实施例具有可UV固化不饱和树脂乙烯基官能度高,UV固化涂膜硬度高,耐化学品性好,工艺简单,成本低。与传统醇和酸生成聚酯的反应(CN105061738A和CN105504245A),本发明不需在180-240℃下反应,反应温度较低,不超过120℃,不产生副产物水,不需要苯类物质做带水剂,更加绿色环保,工艺简单,节能省耗。Compared with the Chinese invention patent application 2016111382348 (CN106748765A, 2017.5.31), the vinyl functionality in this example increases from 3 to more than 6, and the preparation process changes from a two-step process to a one-step process without using the price Expensive triglycidyl ether is used as the starting material; by changing the type and proportion of epoxy monomers, the vinyl functionality, viscosity and performance of unsaturated polyester can be effectively regulated, and high solid content, low viscosity UV curing can be prepared polyester. Therefore, this embodiment has UV curable unsaturated resin with high vinyl functionality, high hardness of UV curable coating film, good chemical resistance, simple process and low cost. For the reaction of polyester with traditional alcohol and acid (CN105061738A and CN105504245A), the present invention does not need to react at 180-240°C, the reaction temperature is relatively low, no more than 120°C, no by-product water is produced, and benzene is not required as a belt Water agent, more green and environmental protection, simple process, energy saving and consumption saving.
实施例2Example 2
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表4(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is as shown in Table 4 (catalyst is not included):
表4Table 4
2)高乙烯基官能度的可UV固化不饱和聚酯树脂的制备工艺,包括以下步骤:2) The preparation technology of UV-curable unsaturated polyester resin with high vinyl functionality, comprising the following steps:
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入邻苯二甲酸酐、辛基缩水甘油醚、乙酸丁酯和四丁基溴化铵(酸酐质量分数的1.2%)混合均匀,升温至100℃保温2.5h,然后逐滴加入溶有对苯二酚的甲基丙烯酸缩水甘油酯,1h滴完,在110℃下开环共聚反应4.5h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under the protection of nitrogen, add phthalic anhydride, octyl glycidyl ether, butyl acetate and tetrabutylammonium bromide (1.2% of the mass fraction of anhydride) in a flask equipped with a stirrer and a thermometer according to a given mass Mix evenly, raise the temperature to 100°C and keep it warm for 2.5h, then add glycidyl methacrylate dissolved in hydroquinone dropwise, drop it in 1h, and perform ring-opening copolymerization reaction at 110°C for 4.5h until the acid value drops to 15mgKOH/ g, lower the temperature and discharge to obtain UV curable unsaturated aliphatic polyester.
3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:浅黄色透明;固含:89.25%;酸值:9.6mgKOH/g,黏度(25℃):3560mPa·s。3) Physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: appearance: light yellow and transparent; solid content: 89.25%; acid value: 9.6mgKOH/g, viscosity (25°C): 3560mPa·s.
4)UV固化涂料的制备及性能4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表5:In parts by mass, the composition of the UV curable coating is as follows in Table 5:
表5table 5
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表6所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 6 below:
表6Table 6
实施例3Example 3
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表7(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is shown in Table 7 (catalyst is not included):
表7Table 7
2)高乙烯基官能度的可UV固化不饱和聚酯树脂的制备工艺包括以下步骤:2) The preparation technology of UV-curable unsaturated polyester resin with high vinyl functionality comprises the following steps:
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入六氢苯酐、苄基缩水甘油醚、乙酸丁酯和四丁基溴化铵(酸酐质量分数的1.5%)混合均匀,升温至110℃保温3h,然后逐滴加入溶有叔丁基邻苯二酚的烯丙基缩水甘油醚,1h滴完,在110℃下开环共聚反应6h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under the protection of nitrogen, add hexahydrophthalic anhydride, benzyl glycidyl ether, butyl acetate and tetrabutylammonium bromide (1.5% of the mass fraction of acid anhydride) according to a given mass into a flask equipped with a stirrer and a thermometer, and mix well , heat up to 110°C for 3 hours, then add allyl glycidyl ether dissolved in tert-butyl catechol dropwise, drop after 1 hour, and perform ring-opening copolymerization reaction at 110°C for 6 hours until the acid value drops to 15mgKOH/g, Cool down and discharge to obtain UV curable unsaturated aliphatic polyester.
3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:浅黄色透明;固含:87.92%;酸值:9.5mgKOH/g,黏度(25℃):4580mPa·s。3) Physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: appearance: light yellow and transparent; solid content: 87.92%; acid value: 9.5mgKOH/g, viscosity (25°C): 4580mPa·s.
4)UV固化涂料的制备及性能4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表8:In terms of parts by mass, the composition of the UV curable coating is as follows in Table 8:
表8Table 8
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表9所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 9 below:
表9Table 9
实施例4Example 4
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表10(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is shown in Table 10 (catalyst is not included):
表10Table 10
2)该UV固化聚酯树脂的制备工艺,包括以下步骤:2) the preparation technology of this UV curable polyester resin, comprises the following steps:
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入丁二酸酐、正丁基缩水甘油醚、丁酮和醋酸锌(酸酐质量分数的1.5%)混合均匀,升温至90℃保温3h,然后逐滴加入溶有对羟基苯甲醚的4-乙烯基苄基缩水甘油醚,2h滴完,在100℃下开环共聚反应4h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under nitrogen protection, add succinic anhydride, n-butyl glycidyl ether, methyl ethyl ketone and zinc acetate (1.5% of the mass fraction of acid anhydride) by given mass in the flask equipped with a stirrer and a thermometer, mix well, and heat up to 90 Insulate at ℃ for 3 hours, then add 4-vinylbenzyl glycidyl ether dissolved in p-hydroxyanisole drop by drop, finish dropping in 2 hours, perform ring-opening copolymerization reaction at 100℃ for 4 hours until the acid value drops to 15mgKOH/g, then cool down Discharging to obtain UV curable unsaturated aliphatic polyester.
(3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:浅黄色透明;固含:86.98%;酸值:11.3mgKOH/g,黏度(25℃):2750mPa·s。(3) The physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: appearance: light yellow and transparent; solid content: 86.98%; acid value: 11.3mgKOH/g, viscosity (25°C): 2750mPa·s.
(4)UV固化涂料的制备及性能(4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表11:In parts by mass, the composition of the UV curable coating is as follows in Table 11:
表11Table 11
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表12所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 12 below:
表12Table 12
实施例5Example 5
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表13(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is shown in Table 13 (catalyst is not included):
表13Table 13
2)高乙烯基官能度的可UV固化不饱和聚酯树脂的制备工艺,包括以下步骤:2) The preparation technology of UV-curable unsaturated polyester resin with high vinyl functionality, comprising the following steps:
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入领苯二甲酸酐、正丁基缩水甘油醚、叔碳酸缩水甘油酯、乙酸乙酯和四丁基溴化铵(酸酐质量分数的3.0%)混合均匀,升温至110℃保温2h,然后逐滴加入溶有对羟基苯甲醚的4-羟基丁基丙烯酸酯缩水甘油醚,1h滴完,在110℃下开环共聚反应5h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under nitrogen protection, add phthalic anhydride, n-butyl glycidyl ether, glycidyl tert-carbonate, ethyl acetate and tetrabutylammonium bromide ( 3.0% of the mass fraction of acid anhydride) and mix evenly, raise the temperature to 110°C and keep it warm for 2h, then add 4-hydroxybutyl acrylate glycidyl ether dissolved in p-hydroxyanisole dropwise, drop it for 1h, and open the ring at 110°C Copolymerize for 5 hours until the acid value drops to 15 mgKOH/g, then cool down and discharge to obtain UV-curable unsaturated aliphatic polyester.
3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:浅黄色透明;固含:88.86%;酸值:8.4mgKOH/g,黏度(25℃):3925mPa·s。3) Physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: appearance: light yellow and transparent; solid content: 88.86%; acid value: 8.4mgKOH/g, viscosity (25°C): 3925mPa·s.
4)UV固化涂料的制备及性能4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表14:In parts by mass, the composition of the UV curable coating is as follows in Table 14:
表14Table 14
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表15所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 15 below:
表15Table 15
实施例6Example 6
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表16(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is shown in Table 16 (catalyst is not included):
表16Table 16
2)高乙烯基官能度的可UV固化不饱和聚酯树脂的制备工艺,包括以下步骤:2) The preparation technology of UV-curable unsaturated polyester resin with high vinyl functionality, comprising the following steps:
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入丁二酸酐、苄基缩水甘油醚、环氧氯丙烷、乙酸乙酯和醋酸锌(酸酐质量分数的2.5%)混合均匀,升温至90℃保温2h,然后逐滴加入溶有对苯二酚的甲基丙烯酸缩水甘油酯,1h滴完,在90℃下开环共聚反应6h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under the protection of nitrogen, add succinic anhydride, benzyl glycidyl ether, epichlorohydrin, ethyl acetate and zinc acetate (2.5% of the mass fraction of acid anhydride) according to a given mass in a flask equipped with a stirrer and a thermometer. Evenly, heat up to 90°C and keep it warm for 2 hours, then add glycidyl methacrylate dissolved in hydroquinone drop by drop, drop after 1 hour, and perform ring-opening copolymerization reaction at 90°C for 6 hours until the acid value drops to 15mgKOH/g, Cool down and discharge to obtain UV curable unsaturated aliphatic polyester.
(3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:浅黄色透明;固含:90.32%;酸值:9.7mgKOH/g,黏度(25℃):2855mPa·s。(3) The physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: appearance: light yellow and transparent; solid content: 90.32%; acid value: 9.7mgKOH/g, viscosity (25°C): 2855mPa·s.
(4)UV固化涂料的制备及性能(4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表17:In parts by mass, the composition of the UV curable coating is as follows in Table 17:
表17Table 17
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表18所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 18 below:
表18Table 18
实施例7Example 7
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表19(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is shown in Table 19 (catalyst is not included):
表19Table 19
2)高乙烯基官能度的可UV固化不饱和聚酯树脂的制备工艺,包括以下步骤:2) The preparation technology of UV-curable unsaturated polyester resin with high vinyl functionality, comprising the following steps:
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入甲基六氢苯酐、苄基缩水甘油醚、C12~14缩水甘油醚、丁酮和四丁基溴化铵(酸酐质量分数的1.2%)混合均匀,升温至100℃保温2.5h,然后逐滴加入溶有对苯二酚的烯丙基缩水甘油醚,1h滴完,在100℃下开环共聚反应6h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under nitrogen protection, add methyl hexahydrophthalic anhydride, benzyl glycidyl ether, C12-14 glycidyl ether, butanone and tetrabutylammonium bromide ( 1.2% of the mass fraction of acid anhydride) and mix evenly, raise the temperature to 100°C and keep it warm for 2.5h, then add allyl glycidyl ether dissolved in hydroquinone dropwise, drop it in 1h, and perform the ring-opening copolymerization reaction at 100°C for 6h to When the acid value drops to 15 mgKOH/g, the temperature is lowered and the material is discharged to obtain a UV-curable unsaturated aliphatic polyester.
3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:浅黄色透明;固含:90.02%;酸值:10.5mgKOH/g,黏度(25℃):3365mPa·s。3) Physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: appearance: light yellow and transparent; solid content: 90.02%; acid value: 10.5mgKOH/g, viscosity (25°C): 3365mPa·s.
4)UV固化涂料的制备及性能4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表20:In parts by mass, the composition of the UV curable coating is as follows in Table 20:
表20Table 20
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表21所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 21 below:
表21Table 21
实施例8Example 8
1)一种高乙烯基官能度的可UV固化不饱和聚酯树脂,原料配方质量百分比组成如表22(不包括催化剂):1) A UV-curable unsaturated polyester resin with high vinyl functionality, the mass percentage composition of the raw material formula is shown in Table 22 (catalyst is not included):
表22Table 22
2)高乙烯基官能度的可UV固化不饱和聚酯树脂的制备工艺包括以下步骤:2) The preparation technology of UV-curable unsaturated polyester resin with high vinyl functionality comprises the following steps:
在氮气保护下,向装有搅拌器、温度计的烧瓶中按给定质量加入偏苯三酸酐、正丁基缩水甘油醚、C12~14缩水甘油醚、环己酮和四辛基溴化铵(酸酐量分数的4.0%)混合均匀,升温至120℃保温3h,然后逐滴加入溶有叔丁基邻苯二酚的甲基丙烯酸缩水甘油酯,1h滴完,在120℃下开环共聚反应6h至酸值降到15mgKOH/g时,降温出料,得到可UV固化不饱和脂肪族聚酯。Under nitrogen protection, add trimellitic anhydride, n-butyl glycidyl ether, C 12-14 glycidyl ether, cyclohexanone and tetraoctyl ammonium bromide according to the given mass to the flask equipped with a stirrer and a thermometer (the amount of anhydride 4.0% of the fraction) mix evenly, raise the temperature to 120°C and keep it warm for 3h, then add glycidyl methacrylate dissolved in tert-butyl catechol drop by drop, finish dropping in 1h, and perform ring-opening copolymerization reaction at 120°C for 6h to reach the acid value When the temperature drops to 15mgKOH/g, the temperature is lowered and the material is discharged to obtain a UV-curable unsaturated aliphatic polyester.
(3)上述制备方法得到的可UV固化聚酯树脂的物化性能:外观:浅黄色透明;固含:90.25%;酸值:7.8mgKOH/g,黏度(25℃):5275mPa·s。(3) Physical and chemical properties of the UV-curable polyester resin obtained by the above preparation method: appearance: light yellow and transparent; solid content: 90.25%; acid value: 7.8mgKOH/g, viscosity (25°C): 5275mPa·s.
(4)UV固化涂料的制备及性能(4) Preparation and properties of UV curable coatings
以质量份计,UV固化涂料的配制组成情况如下表23:In terms of parts by mass, the composition of the UV curable coating is as follows in Table 23:
表23Table 23
将上述配方物质加入容器中,在600r/min的转速下低速分散10~15min,经300目滤布过滤得到UV固化涂料。将该涂料分别在木板和玻璃板上进行涂膜于能量为600mJ/cm2的UV固化机下固化。Add the above-mentioned formula substances into the container, disperse at a low speed of 600r/min for 10-15min, and filter through a 300-mesh filter cloth to obtain a UV-curable coating. The coating was cured under a UV curing machine with an energy of 600mJ/cm 2 on a wooden board and a glass board respectively.
测定涂膜性能,与巴斯夫Laromer LR 9004性能进行比较,如下表24所示:The performance of the coating film was measured and compared with the performance of BASF Laromer LR 9004, as shown in Table 24 below:
表24Table 24
本发明制备的可UV固化聚酯具有制备工艺简单、低VOC排放、节能环保的特点,所制备涂膜具有光泽度高、耐水性好、硬度高等优点。The UV curable polyester prepared by the invention has the characteristics of simple preparation process, low VOC emission, energy saving and environmental protection, and the prepared coating film has the advantages of high gloss, good water resistance, high hardness and the like.
需要说明的是,本发明不受上述实施例约束,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的替代方式,都包含在本发明的保护范围之内。It should be noted that the present invention is not restricted by the above-mentioned embodiments, and any other changes, modifications, substitutions, combinations, and simplifications that do not deviate from the spirit and principles of the present invention should be equivalent alternatives, including Within the protection scope of the present invention.
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CN110684176A (en) * | 2019-10-17 | 2020-01-14 | 嘉宝莉化工集团股份有限公司 | Polyester modified epoxy acrylate resin and its preparation method and application |
CN113174207A (en) * | 2021-06-15 | 2021-07-27 | 安徽熙泰智能科技有限公司 | Plant-based quick-drying optical transparent adhesive, preparation method thereof and application of semiconductor package |
WO2022133680A1 (en) * | 2020-12-21 | 2022-06-30 | 张佩嫦 | Uv-curable low-viscosity polyester and method for preparation thereof |
CN117466840A (en) * | 2023-09-28 | 2024-01-30 | 华南理工大学 | UV-curable modified epoxy vegetable oil acrylate and its preparation method and coating |
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CN110684176A (en) * | 2019-10-17 | 2020-01-14 | 嘉宝莉化工集团股份有限公司 | Polyester modified epoxy acrylate resin and its preparation method and application |
WO2022133680A1 (en) * | 2020-12-21 | 2022-06-30 | 张佩嫦 | Uv-curable low-viscosity polyester and method for preparation thereof |
CN113174207A (en) * | 2021-06-15 | 2021-07-27 | 安徽熙泰智能科技有限公司 | Plant-based quick-drying optical transparent adhesive, preparation method thereof and application of semiconductor package |
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CN117736420B (en) * | 2024-02-05 | 2024-05-10 | 中山大学 | A long-chain branched polyester copolymer for plasticizing polyvinyl chloride and preparation method thereof |
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