CN108467463A - A kind of water proof type aqueous coating polyurethane-polyacrylate composite emulsion and preparation method thereof - Google Patents
A kind of water proof type aqueous coating polyurethane-polyacrylate composite emulsion and preparation method thereof Download PDFInfo
- Publication number
- CN108467463A CN108467463A CN201810285332.7A CN201810285332A CN108467463A CN 108467463 A CN108467463 A CN 108467463A CN 201810285332 A CN201810285332 A CN 201810285332A CN 108467463 A CN108467463 A CN 108467463A
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- CN
- China
- Prior art keywords
- water
- aqueous coating
- proof type
- polyurethane
- water proof
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 82
- 239000000839 emulsion Substances 0.000 title claims abstract description 74
- 229920000058 polyacrylate Polymers 0.000 title claims abstract description 42
- 238000000576 coating method Methods 0.000 title claims abstract description 36
- 239000011248 coating agent Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
- 239000002131 composite material Substances 0.000 title claims description 21
- 238000004945 emulsification Methods 0.000 title claims description 9
- 239000004814 polyurethane Substances 0.000 claims abstract description 46
- 229920002635 polyurethane Polymers 0.000 claims abstract description 43
- -1 polysiloxanes Polymers 0.000 claims abstract description 37
- 239000000178 monomer Substances 0.000 claims abstract description 34
- 239000004970 Chain extender Substances 0.000 claims abstract description 28
- 229920001296 polysiloxane Polymers 0.000 claims abstract description 22
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 19
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 18
- 150000003384 small molecules Chemical group 0.000 claims abstract description 14
- 239000002245 particle Substances 0.000 claims abstract description 12
- 229920005862 polyol Polymers 0.000 claims abstract description 12
- 150000003077 polyols Chemical class 0.000 claims abstract description 12
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 11
- 229920000570 polyether Polymers 0.000 claims abstract description 11
- 150000003839 salts Chemical class 0.000 claims abstract description 4
- 239000006210 lotion Substances 0.000 claims abstract 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 32
- 238000006243 chemical reaction Methods 0.000 claims description 31
- 238000003756 stirring Methods 0.000 claims description 31
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims description 21
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 18
- 229910052757 nitrogen Inorganic materials 0.000 claims description 17
- 239000003995 emulsifying agent Substances 0.000 claims description 16
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 13
- 239000003999 initiator Substances 0.000 claims description 12
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims description 10
- 229920001228 polyisocyanate Polymers 0.000 claims description 10
- 239000005056 polyisocyanate Substances 0.000 claims description 10
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 9
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 9
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical group CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims description 8
- 239000008367 deionised water Substances 0.000 claims description 8
- 229910021641 deionized water Inorganic materials 0.000 claims description 8
- 238000006116 polymerization reaction Methods 0.000 claims description 5
- 229920000909 polytetrahydrofuran Polymers 0.000 claims description 5
- 239000005057 Hexamethylene diisocyanate Substances 0.000 claims description 4
- 125000000129 anionic group Chemical group 0.000 claims description 4
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 claims description 4
- CRVGTESFCCXCTH-UHFFFAOYSA-N methyl diethanolamine Chemical compound OCCN(C)CCO CRVGTESFCCXCTH-UHFFFAOYSA-N 0.000 claims description 4
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 claims description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 3
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 claims description 3
- 150000002148 esters Chemical class 0.000 claims description 3
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 claims description 3
- 239000012948 isocyanate Substances 0.000 claims description 3
- 229920001451 polypropylene glycol Polymers 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 2
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims 3
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims 2
- HJOVHMDZYOCNQW-UHFFFAOYSA-N isophorone Chemical compound CC1=CC(=O)CC(C)(C)C1 HJOVHMDZYOCNQW-UHFFFAOYSA-N 0.000 claims 2
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims 1
- 239000002202 Polyethylene glycol Substances 0.000 claims 1
- 239000000908 ammonium hydroxide Substances 0.000 claims 1
- XLJMAIOERFSOGZ-UHFFFAOYSA-M cyanate Chemical compound [O-]C#N XLJMAIOERFSOGZ-UHFFFAOYSA-M 0.000 claims 1
- QDPMLKBAQOZXEF-UHFFFAOYSA-N ethanesulfonic acid;sodium Chemical compound [Na].CCS(O)(=O)=O QDPMLKBAQOZXEF-UHFFFAOYSA-N 0.000 claims 1
- 125000002768 hydroxyalkyl group Chemical group 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 229920001223 polyethylene glycol Polymers 0.000 claims 1
- 235000019260 propionic acid Nutrition 0.000 claims 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 claims 1
- DCKVNWZUADLDEH-UHFFFAOYSA-N sec-butyl acetate Chemical compound CCC(C)OC(C)=O DCKVNWZUADLDEH-UHFFFAOYSA-N 0.000 claims 1
- 238000010521 absorption reaction Methods 0.000 abstract description 4
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 239000003973 paint Substances 0.000 abstract 3
- 239000005871 repellent Substances 0.000 abstract 2
- UHESRSKEBRADOO-UHFFFAOYSA-N ethyl carbamate;prop-2-enoic acid Chemical compound OC(=O)C=C.CCOC(N)=O UHESRSKEBRADOO-UHFFFAOYSA-N 0.000 abstract 1
- 239000004922 lacquer Substances 0.000 abstract 1
- 230000008961 swelling Effects 0.000 description 19
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 5
- 150000002009 diols Chemical class 0.000 description 5
- 239000012528 membrane Substances 0.000 description 5
- 229910052710 silicon Inorganic materials 0.000 description 5
- 239000010703 silicon Substances 0.000 description 5
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 4
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 description 4
- 239000012975 dibutyltin dilaurate Substances 0.000 description 4
- 238000010907 mechanical stirring Methods 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 235000019333 sodium laurylsulphate Nutrition 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
- QWGRWMMWNDWRQN-UHFFFAOYSA-N 2-methylpropane-1,3-diol Chemical compound OCC(C)CO QWGRWMMWNDWRQN-UHFFFAOYSA-N 0.000 description 3
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 description 3
- 239000004205 dimethyl polysiloxane Substances 0.000 description 3
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 3
- 238000012712 reversible addition−fragmentation chain-transfer polymerization Methods 0.000 description 3
- JVYDLYGCSIHCMR-UHFFFAOYSA-N 2,2-bis(hydroxymethyl)butanoic acid Chemical compound CCC(CO)(CO)C(O)=O JVYDLYGCSIHCMR-UHFFFAOYSA-N 0.000 description 2
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 description 2
- 239000004342 Benzoyl peroxide Substances 0.000 description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 2
- 102100026735 Coagulation factor VIII Human genes 0.000 description 2
- 101000911390 Homo sapiens Coagulation factor VIII Proteins 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 239000005058 Isophorone diisocyanate Substances 0.000 description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 239000011258 core-shell material Substances 0.000 description 2
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 2
- 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 2
- 229920000056 polyoxyethylene ether Polymers 0.000 description 2
- 229940051841 polyoxyethylene ether Drugs 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 2
- DAJSVUQLFFJUSX-UHFFFAOYSA-M sodium;dodecane-1-sulfonate Chemical compound [Na+].CCCCCCCCCCCCS([O-])(=O)=O DAJSVUQLFFJUSX-UHFFFAOYSA-M 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- KSBAEPSJVUENNK-UHFFFAOYSA-L tin(ii) 2-ethylhexanoate Chemical compound [Sn+2].CCCCC(CC)C([O-])=O.CCCCC(CC)C([O-])=O KSBAEPSJVUENNK-UHFFFAOYSA-L 0.000 description 2
- 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 2
- 238000004383 yellowing Methods 0.000 description 2
- 229920002818 (Hydroxyethyl)methacrylate Polymers 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- SVYKKECYCPFKGB-UHFFFAOYSA-N N,N-dimethylcyclohexylamine Chemical group CN(C)C1CCCCC1 SVYKKECYCPFKGB-UHFFFAOYSA-N 0.000 description 1
- UEEJHVSXFDXPFK-UHFFFAOYSA-N N-dimethylaminoethanol Chemical compound CN(C)CCO UEEJHVSXFDXPFK-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000000354 decomposition reaction Methods 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
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 230000002522 swelling effect Effects 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F283/00—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
- C08F283/006—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polymers provided for in C08G18/00
-
- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/30—Low-molecular-weight compounds
- C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
- C08G18/3203—Polyhydroxy compounds
- C08G18/3206—Polyhydroxy compounds aliphatic
-
- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/30—Low-molecular-weight compounds
- C08G18/34—Carboxylic acids; Esters thereof with monohydroxyl compounds
- C08G18/348—Hydroxycarboxylic acids
-
- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
-
- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4854—Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
-
- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/61—Polysiloxanes
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- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/6505—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen the low-molecular compounds being compounds of group C08G18/32 or polyamines of C08G18/38
- C08G18/6511—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen the low-molecular compounds being compounds of group C08G18/32 or polyamines of C08G18/38 compounds of group C08G18/3203
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- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/6541—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen the low-molecular compounds being compounds of group C08G18/34
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- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
- C08G18/6666—Compounds of group C08G18/48 or C08G18/52
- C08G18/667—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
- C08G18/6674—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
-
- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
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Abstract
Description
技术领域technical field
本发明属于涂料技术领域,具体涉及一种防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液及其制备方法。The invention belongs to the technical field of coatings, and in particular relates to a water-based polyurethane-polyacrylate composite emulsion for waterproof coatings and a preparation method thereof.
背景技术Background technique
在当今社会,人们追求以经济,效率,生态和能源为原则来发展涂料工业,应安全环保的要求,水性聚氨酯将逐步代替传统的溶剂型聚氨酯的应用。相较于传统的溶剂型聚氨酯,水性聚氨酯具有无毒、不易燃、耐低温等优点。但水性聚氨酯也有其固有缺点,如耐水性差,力学性能不佳,耐光性差、原材料相对昂贵等。而聚丙烯酸酯类具有许多突出的优点,如优异的耐光性、耐候性、耐酸碱性以及力学性能,但其低温易变脆,高温易变粘。利用聚氨酯核聚丙烯酸酯性能上的互补,通过丙烯酸酯对聚氨酯进行改性,可获得性能优异的聚氨酯-聚丙烯酸酯复合材料。In today's society, people pursue the principles of economy, efficiency, ecology and energy to develop the coatings industry. In response to the requirements of safety and environmental protection, water-based polyurethane will gradually replace the application of traditional solvent-based polyurethane. Compared with traditional solvent-based polyurethane, water-based polyurethane has the advantages of non-toxic, non-flammable, and low temperature resistance. However, water-based polyurethane also has its inherent disadvantages, such as poor water resistance, poor mechanical properties, poor light resistance, and relatively expensive raw materials. Polyacrylates have many outstanding advantages, such as excellent light resistance, weather resistance, acid and alkali resistance, and mechanical properties, but they tend to become brittle at low temperature and sticky at high temperature. Utilizing the complementary properties of polyurethane core and polyacrylate, the polyurethane-polyacrylate composite material with excellent performance can be obtained by modifying polyurethane through acrylate.
公开号为CN105482060的中国专利公开了一种通过RAFT(可逆加成-断裂链转移聚合)方法,制备了化学键合核壳的水性聚氨酯-丙烯酸酯共聚乳液,虽然获得了核壳组成可控的聚氨酯-丙烯酸酯乳液,但是RAFT链转移试剂可能会使聚合物带有一定的颜色和气味,而且它们的去除和转换也比较困难。The Chinese patent with the publication number CN105482060 discloses a method of RAFT (reversible addition-fragmentation chain transfer polymerization) to prepare a chemically bonded core-shell aqueous polyurethane-acrylate copolymer emulsion, although a polyurethane with a controllable core-shell composition has been obtained. - Acrylate emulsions, but RAFT chain transfer agents may impart some color and odor to the polymer, and their removal and conversion are more difficult.
发明内容Contents of the invention
本发明目的是为了解决现有的水性聚氨酯-丙烯酸酯乳液产品的耐水性差、低温成膜性差的问题,而提供一种防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液及其制备方法。The purpose of the present invention is to provide a water-based polyurethane-polyacrylate composite emulsion for waterproof coatings and a preparation method thereof in order to solve the problems of poor water resistance and low-temperature film-forming properties of existing water-based polyurethane-acrylate emulsion products.
本发明首先提供一种防水型涂料用水性聚氨酯-聚丙烯酸酯乳液,该乳液是经过自乳化法合成出阴离子型水性聚氨酯乳液,然后通过预溶胀的方式将丙烯酸酯单体分散到聚氨酯体系中聚合得到的,所制备的乳液粒子为semi-IPN结构;该乳液按照重量份数计,包括如下:The present invention firstly provides a water-based polyurethane-polyacrylate emulsion for waterproof coatings, the emulsion is an anionic water-based polyurethane emulsion synthesized by a self-emulsification method, and then the acrylate monomer is dispersed into the polyurethane system by pre-swelling for polymerization Obtained, the prepared emulsion particle is semi-IPN structure; The emulsion includes as follows in parts by weight:
优选的是,所述的聚醚多元醇选自聚氧化乙烯醚二醇、聚四氢呋喃醚二醇、聚氧化丙烯二醇中的一种或几种。Preferably, the polyether polyol is selected from one or more of polyoxyethylene ether diol, polytetrahydrofuran ether diol, and polyoxypropylene ether diol.
优选的是,所述的多异氰酸酯类单体选自二苯基甲烷二异氰酸酯、甲苯二异氰酸酯、异佛尔酮二异氰酸酯或六亚甲基二异氰酸酯中的一种或几种。Preferably, the polyisocyanate monomer is selected from one or more of diphenylmethane diisocyanate, toluene diisocyanate, isophorone diisocyanate or hexamethylene diisocyanate.
优选的是,所述的聚硅氧烷选自羟基封端聚硅氧烷、羟烷基封端聚硅氧烷或氨基封端聚硅氧烷中的一种或几种。Preferably, the polysiloxane is selected from one or more of hydroxyl-terminated polysiloxanes, hydroxyalkyl-terminated polysiloxanes, or amino-terminated polysiloxanes.
优选的是,所述的丙烯酸酯类单体选自丙烯酸丁酯、甲基丙烯酸甲酯、甲基丙烯酸乙酯或甲基丙烯酸丁酯中的一种或几种。Preferably, the acrylate monomer is selected from one or more of butyl acrylate, methyl methacrylate, ethyl methacrylate or butyl methacrylate.
优选的是,所述的小分子扩链剂选自乙二醇、新戊二醇、1,4-丁二醇或2-甲基-1,3-丙二醇中的一种或几种。Preferably, the small molecule chain extender is selected from one or more of ethylene glycol, neopentyl glycol, 1,4-butanediol or 2-methyl-1,3-propanediol.
优选的是,所述的亲水扩链剂选自二羟甲基丙酸、二羟基半酯、乙二胺基乙磺酸钠、二乙烯三胺或甲基二乙醇胺中的一种或几种。Preferably, the hydrophilic chain extender is selected from one or more of dimethylolpropionic acid, dihydroxy half ester, sodium ethylenediaminoethanesulfonate, diethylenetriamine or methyldiethanolamine. kind.
优选的是,所述的成盐剂选自三乙胺、氨水或氢氧化钠中的一种。Preferably, the salt-forming agent is selected from one of triethylamine, ammonia water or sodium hydroxide.
本发明还提供一种防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液的制备方法,包括如下步骤:The present invention also provides a preparation method of water-based polyurethane-polyacrylate composite emulsion for waterproof coating, comprising the steps of:
步骤一:在反应容器中加入聚醚多元醇、多异氰酸酯、聚硅氧烷、小分子扩链剂、亲水扩链剂和催化剂,在75~95℃反应2~4小时,得到预聚物;Step 1: Add polyether polyol, polyisocyanate, polysiloxane, small molecule chain extender, hydrophilic chain extender and catalyst into the reaction vessel, and react at 75-95°C for 2-4 hours to obtain a prepolymer ;
步骤二:将反应容器内温度降至30~40℃,加入丙酮降粘,继续反应20~40分钟,然后加入成盐剂,反应5~10分钟,在室温下加入去离子水搅拌,得到水性聚氨酯乳液;Step 2: Lower the temperature in the reaction vessel to 30-40°C, add acetone to reduce viscosity, continue to react for 20-40 minutes, then add salt-forming agent, react for 5-10 minutes, add deionized water at room temperature and stir to obtain aqueous polyurethane emulsion;
步骤三:在得到的水性聚氨酯乳液中加入丙烯酸酯类单体,25℃下预溶胀12~24小时,同时加入1/3乳化剂,待预溶胀结束后,将反应温度升至65~80℃,加入引发剂及剩余乳化剂,氮气保护,搅拌反应3~7小时,得到防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液。Step 3: Add acrylate monomers to the obtained water-based polyurethane emulsion, pre-swell at 25°C for 12-24 hours, and add 1/3 emulsifier at the same time, after the pre-swelling is completed, raise the reaction temperature to 65-80°C , adding initiator and remaining emulsifier, nitrogen protection, stirring and reacting for 3-7 hours to obtain water-based polyurethane-polyacrylate composite emulsion for waterproof coating.
优选的是,所述的步骤三的搅拌速度为250~300转/分钟。Preferably, the stirring speed in the third step is 250-300 rpm.
本发明的有益效果Beneficial effects of the present invention
本发明提供一种防水型涂料用水性聚氨酯-聚丙烯酸酯乳液,由于采用脂肪族异氰酸酯为原料,所制备的乳液具有耐黄变性和稳定的特点;其在聚氨酯分子主链上引入有机硅链段,降低了膜表面能,改善了膜的耐水性;同时,本发明通过预溶胀的方式加入丙烯酸酯类单体,获得一种半网络互穿结构(semi-IPN结构)双改性的水性聚氨酯乳液,该特殊结构可以使膜耐水性提高。所述的水性聚氨酯-聚丙烯酸酯乳液固含量为30%~40%,粒径为80~140nm,储存稳定性在6个月以上,具有乳液粘度适中,粒度均一,稳定性好等优点。实验结果表明:涂饰成膜后,耐水性突出,接触角≥88°,吸水率≤10%,力学性能良好,综合性能优异。The invention provides a water-based polyurethane-polyacrylate emulsion for waterproof coatings. Since aliphatic isocyanate is used as a raw material, the prepared emulsion has the characteristics of yellowing resistance and stability; it introduces organic silicon segments into the main chain of polyurethane molecules , which reduces the surface energy of the membrane and improves the water resistance of the membrane; at the same time, the present invention adds acrylic monomers through pre-swelling to obtain a double-modified water-based polyurethane with a semi-interpenetrating network structure (semi-IPN structure) Emulsion, this special structure can improve the water resistance of the film. The water-based polyurethane-polyacrylate emulsion has a solid content of 30%-40%, a particle size of 80-140nm, a storage stability of more than 6 months, and has the advantages of moderate emulsion viscosity, uniform particle size and good stability. The experimental results show that after coating and forming a film, the water resistance is outstanding, the contact angle is ≥88°, the water absorption rate is ≤10%, the mechanical properties are good, and the comprehensive performance is excellent.
本发明还提供了一种防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液的制备方法,该方法为将多异氰酸酯单体、聚醚型多元醇、亲水扩链剂及有机硅按照比例进行逐步聚合,首先制备预聚物,经过自乳化法合成出阴离子型水性聚氨酯乳液,然后通过预溶胀的方式将丙烯酸酯单体分散到聚氨酯体系中,继续聚合,制备出双改性的水性聚氨酯乳液。该方法所制备的乳液粒子为semi-IPN(半-网络互穿)结构。该制备方法简单,原料易得,制备得到的产品具有优异的综合性能。The present invention also provides a method for preparing a water-based polyurethane-polyacrylate composite emulsion for waterproof coatings. The method is to gradually prepare polyisocyanate monomers, polyether polyols, hydrophilic chain extenders and organic silicon according to the proportion. Polymerization, first prepare a prepolymer, synthesize an anionic water-based polyurethane emulsion through self-emulsification, then disperse the acrylate monomer into the polyurethane system by pre-swelling, continue polymerization, and prepare a double-modified water-based polyurethane emulsion. The emulsion particles prepared by the method have a semi-IPN (semi-interpenetrating network) structure. The preparation method is simple, the raw materials are easy to obtain, and the prepared product has excellent comprehensive properties.
附图说明Description of drawings
图1为本发明实施例1制备的一种防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液粒子的透射电镜图;Fig. 1 is the transmission electron microscope picture of a kind of waterproof coating water-based polyurethane-polyacrylate composite emulsion particle prepared in Example 1 of the present invention;
图2为本发明实施例1制备的防水型涂料用一种水性聚氨酯-聚丙烯酸酯复合乳液的水接触角和吸水率图。Fig. 2 is a water contact angle and water absorption diagram of a water-based polyurethane-polyacrylate composite emulsion for a waterproof coating prepared in Example 1 of the present invention.
具体实施方式Detailed ways
为了进一步了解本发明,下面结合具体实施例对本发明的优选实施方案进行描述,但是应该理解,这些描述只是为进一步说明本发明的特征和优点而不是对本发明专利要求的限制。In order to further understand the present invention, the preferred embodiments of the present invention are described below in conjunction with specific examples, but it should be understood that these descriptions are only for further illustrating the features and advantages of the present invention rather than limiting the patent requirements of the present invention.
本发明首先提供一种防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液,该乳液是经过自乳化法合成出阴离子型水性聚氨酯乳液,然后通过预溶胀的方式将丙烯酸酯单体分散到聚氨酯体系中聚合得到的,所制备的乳液粒子为semi-IPN结构;该乳液按照重量份数计,包括:The present invention firstly provides a water-based polyurethane-polyacrylate composite emulsion for waterproof coatings. The anionic water-based polyurethane emulsion is synthesized through a self-emulsification method, and then the acrylate monomer is dispersed into the polyurethane system by pre-swelling. Obtained by polymerization, the prepared emulsion particles have a semi-IPN structure; the emulsion includes in parts by weight:
聚醚多元醇50~100,多异氰酸酯30~80,丙烯酸酯类单体30~70份,聚硅氧烷6~17份,小分子扩链剂4~10份,亲水扩链剂5~15份,成盐剂3~10份。优选为:聚醚多元醇60~90,多异氰酸酯40~70,聚硅氧烷7~15份,小分子扩链剂5~8份,亲水扩链剂7~10份,成盐剂7~10份,丙烯酸酯类单体30~60份。Polyether polyol 50-100, polyisocyanate 30-80, acrylate monomer 30-70, polysiloxane 6-17, small molecule chain extender 4-10, hydrophilic chain extender 5- 15 parts, 3 to 10 parts of salt forming agent. Preferably: polyether polyol 60-90, polyisocyanate 40-70, polysiloxane 7-15 parts, small molecule chain extender 5-8 parts, hydrophilic chain extender 7-10 parts, salt-forming agent 7 parts ~10 parts, 30~60 parts of acrylate monomer.
本发明所述的聚醚多元醇选自聚氧化乙烯醚二醇、聚四氢呋喃醚二醇、聚氧化丙烯二醇中的一种或几种,所述的多元醇的数均分子量优选为1000~3000。The polyether polyol of the present invention is selected from one or more of polyoxyethylene ether diol, polytetrahydrofuran ether diol, and polyoxypropylene diol, and the number average molecular weight of the polyol is preferably 1000~ 3000.
本发明所述的多异氰酸酯类单体选自二苯基甲烷二异氰酸酯、甲苯二异氰酸酯、异佛尔酮二异氰酸酯或六亚甲基二异氰酸酯中的一种或几种,本发明采用的脂肪族异氰酸酯为原料,制备的乳液具有耐黄变性和稳定的特点。The polyisocyanate monomers described in the present invention are selected from one or more of diphenylmethane diisocyanate, toluene diisocyanate, isophorone diisocyanate or hexamethylene diisocyanate, and the aliphatic diisocyanate used in the present invention Using isocyanate as raw material, the prepared emulsion has the characteristics of yellowing resistance and stability.
本发明所述的聚硅氧烷选自羟基封端聚硅氧烷、羟烷基封端聚硅氧烷或氨基封端聚硅氧烷中的一种或几种,所述的聚硅氧烷的数均分子量优选为500~2000,在聚氨酯分子主链上引入聚硅氧烷,降低了膜的表面性能,改善了膜的耐水性。The polysiloxane of the present invention is selected from one or more of hydroxyl-terminated polysiloxane, hydroxyalkyl-terminated polysiloxane or amino-terminated polysiloxane, and the polysiloxane The number-average molecular weight of the alkane is preferably 500-2000, and polysiloxane is introduced into the main chain of the polyurethane molecule, which reduces the surface properties of the film and improves the water resistance of the film.
本发明所述的丙烯酸酯类单体选自丙烯酸丁酯、甲基丙烯酸甲酯、甲基丙烯酸乙酯或甲基丙烯酸丁酯中的一种或几种,优选为甲基丙烯酸甲酯和丙烯酸丁酯的混合物,且甲基丙烯酸甲酯和丙烯酸丁酯的质量比为1:1。本发明通过预溶胀的方式将丙烯酸酯单体加入到反应体系中,这种预溶胀的方式可以获得一种半网络互穿结构(semi-IPN结构),semi-IPN结构会赋予膜优异的耐水性。The acrylate monomers described in the present invention are selected from one or more of butyl acrylate, methyl methacrylate, ethyl methacrylate or butyl methacrylate, preferably methyl methacrylate and acrylic acid A mixture of butyl esters, and the mass ratio of methyl methacrylate to butyl acrylate is 1:1. In the present invention, the acrylate monomer is added to the reaction system by pre-swelling, and this pre-swelling method can obtain a semi-network interpenetrating structure (semi-IPN structure), and the semi-IPN structure will endow the film with excellent water resistance sex.
本发明所述的小分子扩链剂选自乙二醇、新戊二醇、1,4-丁二醇或2-甲基-1,3-丙二醇中的一种或几种。The small molecule chain extender in the present invention is selected from one or more of ethylene glycol, neopentyl glycol, 1,4-butanediol or 2-methyl-1,3-propanediol.
本发明所述的亲水扩链剂选自二羟甲基丙酸、二羟基半酯、乙二胺基乙磺酸钠、二乙烯三胺或甲基二乙醇胺中的一种或几种。The hydrophilic chain extender in the present invention is selected from one or more of dimethylolpropionic acid, dihydroxy half ester, sodium ethylenediaminoethanesulfonate, diethylenetriamine or methyldiethanolamine.
本发明所述的成盐剂选自三乙胺、氨水或氢氧化钠中的一种。The salt-forming agent described in the present invention is selected from one of triethylamine, ammonia water or sodium hydroxide.
本发明还提供一种防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液的制备方法,包括如下:The present invention also provides a method for preparing a water-based polyurethane-polyacrylate composite emulsion for waterproof coatings, comprising the following steps:
步骤一:在反应容器中加入聚醚多元醇、多异氰酸酯、聚硅氧烷、小分子扩链剂、亲水扩链剂和催化剂,在75~95℃反应2~4小时,得到预聚物;Step 1: Add polyether polyol, polyisocyanate, polysiloxane, small molecule chain extender, hydrophilic chain extender and catalyst into the reaction vessel, and react at 75-95°C for 2-4 hours to obtain a prepolymer ;
步骤二:将反应容器内温度降至30~40℃,加入丙酮降粘,继续反应20~40分钟,然后加入成盐剂,反应5~10分钟,在室温(25℃)下加入去离子水搅拌,得到水性聚氨酯乳液;Step 2: Lower the temperature in the reaction vessel to 30-40°C, add acetone to reduce the viscosity, continue the reaction for 20-40 minutes, then add the salt-forming agent, react for 5-10 minutes, add deionized water at room temperature (25°C) Stir to obtain aqueous polyurethane emulsion;
步骤三:在得到的水性聚氨酯乳液中加入丙烯酸酯类单体,25℃下预溶胀12~24小时,同时加入1/3乳化剂,待预溶胀结束后,将反应温度升至65~80℃,加入引发剂及剩余乳化剂,氮气保护,搅拌反应3~7小时,得到防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液。本发明步骤一中:先将用于反应的聚醚多元醇置于80~100℃的真空烘箱中真空下除水1~2小时,脱水结束后物料降温,再将多异氰酸酯、聚硅氧烷、小分子扩链剂、亲水扩链剂和催化剂加入到反应釜中,开启搅拌装置及加热装置至75~95℃反应2~4小时,搅拌速度优选为300~400转/分钟,全程通氮气保护,待-NCO值达到理论值,制得预聚物;所述的催化剂选自N,N-二甲基环已胺、N,N-二甲基乙醇胺、N,N-二甲基吡啶、辛酸亚锡和二月桂酸二丁基锡中的一种。催化剂按照重量分数计,优选0.01~0.1份。Step 3: Add acrylate monomers to the obtained water-based polyurethane emulsion, pre-swell at 25°C for 12-24 hours, and add 1/3 emulsifier at the same time, after the pre-swelling is completed, raise the reaction temperature to 65-80°C , adding initiator and remaining emulsifier, nitrogen protection, stirring and reacting for 3-7 hours to obtain water-based polyurethane-polyacrylate composite emulsion for waterproof coating. In step 1 of the present invention: first place the polyether polyol used for the reaction in a vacuum oven at 80-100°C to remove water under vacuum for 1-2 hours, after the dehydration is completed, the material is cooled, and then polyisocyanate, polysiloxane , small molecule chain extender, hydrophilic chain extender and catalyst are added to the reaction kettle, and the stirring device and heating device are turned on to react at 75-95°C for 2-4 hours. The stirring speed is preferably 300-400 rpm Nitrogen protection, when the -NCO value reaches the theoretical value, a prepolymer is prepared; the catalyst is selected from N, N-dimethylcyclohexylamine, N, N-dimethylethanolamine, N, N-dimethyl One of pyridine, stannous octoate and dibutyltin dilaurate. The catalyst is preferably 0.01-0.1 part by weight fraction.
本发明步骤二中:将反应容器内温度降至30~40℃,然后加入30~60ml的丙酮降粘20~40分钟,接着加入成盐剂,反应5~10分钟,再加入去离子水,常温下高速搅拌30~50分钟,搅拌速度优选为1000~2000转/分钟,得到水性聚氨酯乳液。In the second step of the present invention: the temperature in the reaction vessel is lowered to 30-40°C, then 30-60ml of acetone is added to reduce the viscosity for 20-40 minutes, then a salt-forming agent is added, reacted for 5-10 minutes, and then deionized water is added, Stir at a high speed at room temperature for 30-50 minutes, preferably at a stirring speed of 1000-2000 rpm, to obtain an aqueous polyurethane emulsion.
本发明步骤三中:在得到的水性聚氨酯乳液中加入丙烯酸酯类单体,25℃下预溶胀12~24小时,即常温下机械搅拌12~24小时,优选预溶胀时间为14~16小时,同时加入1/3乳化剂,待预溶胀14~16小时后,将反应温度升至65~80℃,加入引发剂及剩余乳化剂,氮气保护,搅拌反应3~7小时,搅拌速度优选为250~300转/分钟,通过减压蒸馏的方式除去丙酮,得到水性聚氨酯-聚丙烯酸酯复合乳液。In the third step of the present invention: add acrylate monomers to the obtained water-based polyurethane emulsion, pre-swell for 12-24 hours at 25°C, that is, mechanically stir for 12-24 hours at room temperature, preferably the pre-swelling time is 14-16 hours, Add 1/3 of the emulsifier at the same time, after pre-swelling for 14-16 hours, raise the reaction temperature to 65-80°C, add the initiator and the remaining emulsifier, under nitrogen protection, stir for 3-7 hours, the stirring speed is preferably 250 ~300 rev/min, remove acetone by vacuum distillation to obtain water-based polyurethane-polyacrylate composite emulsion.
按照本发明,步骤三预溶胀的时间及预溶胀结束后的反应温度、时间等都是控制该反应的关键参数,本发明所述的预溶胀时间为12-24h,如果时间太短,单体是以一种大液滴的形式存在,在机械搅拌下,会使单体液滴适当变小,影响预溶胀效果;如果时间太长,会影响聚氨酯水分散体系的稳定性。所述的反应温度为65-80℃,如果温度太低,没有达到引发剂的分解温度,反应效果差,如果温度过高,会使水部分蒸发,会对固含量有影响。According to the present invention, the pre-swelling time of step 3 and the reaction temperature and time after the pre-swelling are all key parameters to control the reaction. The pre-swelling time of the present invention is 12-24h. If the time is too short, the monomer It exists in the form of large droplets. Under mechanical stirring, the monomer droplets will become smaller and affect the pre-swelling effect; if the time is too long, it will affect the stability of the polyurethane water dispersion system. The reaction temperature is 65-80°C. If the temperature is too low, the decomposition temperature of the initiator will not be reached, and the reaction effect will be poor. If the temperature is too high, part of the water will evaporate, which will affect the solid content.
本发明的防水型涂料用水性聚氨酯-聚丙烯酸酯复合乳液的制备方法,是先合成聚氨酯并用水分散成水性聚氨酯,再进行预溶胀,预溶胀的目的就是将单体分散在整个水性聚氨酯这个体系中,由于丙烯酸酯类单体自身具有一定的疏水性,会使大多数单体溶胀进入到聚氨酯胶束粒子中,仍有少部分单体仍游离在水相中。待第二部分丙烯酸酯单体的自由基聚合,加了引发剂之后,大部分单体在PU内部进行聚合,而PU之外游离在水相中的单体也会和内部产生的长链继续进行反应形成互相渗透的网络结构,因为没有引入官能化单体(例如甲基丙烯酸羟乙酯HEMA,其一端带有-OH,一端带有不饱和双键,-OH与聚氨酯反应,生成带有端不饱和双键的预聚物,)HEMA可以作为桥梁,将丙烯酸酯单体接在PU链上,这样就形成具有化学键的聚氨酯-聚丙烯酸酯共聚结构。同时在本发明的这个体系中,还加了有机硅(聚硅氧烷),有机硅的特点是表面能低,在乳液成膜的过程中,硅链段会向膜表面迁移,会降低膜表面的表面能,也就使得膜表面耐水性提高。这里硅链段迁移会受结构的影响,它没有化学键这种强分子作用力,分子链易活动和形变,这样硅链段容易迁移到膜表面,使得膜表面耐水性提高。The preparation method of the water-based polyurethane-polyacrylate composite emulsion of the waterproof coating of the present invention is to first synthesize polyurethane and disperse it with water to form water-based polyurethane, and then perform pre-swelling. The purpose of pre-swelling is to disperse monomers in the entire water-based polyurethane system In the process, due to the certain hydrophobicity of the acrylate monomer itself, most of the monomers will swell and enter the polyurethane micelle particles, and a small part of the monomers are still free in the water phase. After the free radical polymerization of the second part of the acrylate monomer, after adding the initiator, most of the monomers are polymerized inside the PU, and the monomers free in the water phase outside the PU will also continue with the long chain generated inside. The reaction forms an interpenetrating network structure, because there is no introduction of functional monomers (such as hydroxyethyl methacrylate HEMA, which has -OH at one end and unsaturated double bonds at one end, and -OH reacts with polyurethane to form a The prepolymer with unsaturated double bonds at the end,) HEMA can be used as a bridge to connect the acrylate monomer to the PU chain, thus forming a polyurethane-polyacrylate copolymer structure with chemical bonds. Simultaneously in this system of the present invention, also added organosilicon (polysiloxane), the characteristic of organosilicon is that surface energy is low, and in the process of emulsion film formation, silicon segment can migrate to film surface, can reduce film The surface energy of the surface also improves the water resistance of the membrane surface. Here, the migration of the silicon segment will be affected by the structure. It has no strong molecular force such as chemical bonds, and the molecular chain is easy to move and deform. In this way, the silicon segment is easy to migrate to the surface of the membrane, which improves the water resistance of the membrane surface.
本发明所述引发剂选自过硫酸钾、过硫酸铵、偶氮二异丁氰、过氧化苯甲酰中的一种。引发剂的用量为丙烯酸酯类单体重量的0.5%~2%,优选为1%。The initiator described in the present invention is selected from one of potassium persulfate, ammonium persulfate, azobisisobutylcyanide and benzoyl peroxide. The dosage of the initiator is 0.5%-2% of the weight of the acrylate monomer, preferably 1%.
本发明所述的乳化剂选自十二烷基硫酸钠(SDS),十二烷基磺酸钠或十二烷基苯磺酸钠(SDBS)中的一种。乳化剂的总用量为丙烯酸酯类单体重量的1%~4%,优选为3%。The emulsifier in the present invention is selected from sodium dodecyl sulfate (SDS), sodium dodecylsulfonate or sodium dodecylbenzenesulfonate (SDBS). The total amount of the emulsifier is 1%-4% of the weight of the acrylate monomer, preferably 3%.
下面结合实施例对本发明做进一步详细的描述。The present invention will be further described in detail below in conjunction with the examples.
实施例1Example 1
在装有搅拌装置、冷凝管、温度计并通有氮气的四口烧瓶中,加入聚四氢呋喃醚二醇(数均分子量为2000)80g,在100℃下抽真空脱水2小时,之后加入异佛尔酮二异氰酸酯60g,亲水扩链剂二羟甲基丙酸10g,小分子扩链剂1,4-丁二醇8g,双羟基封端聚二甲基硅氧烷(数均分子量为1000)10g和催化剂二月桂酸二丁基锡0.1g,全程氮气保护,油浴锅温度控制在80℃,搅拌速度为380转/分钟,反应3小时至-NCO达到理论值,得到预聚物;In a four-necked flask equipped with a stirring device, a condenser, a thermometer and nitrogen, add 80 g of polytetrahydrofuran ether diol (number average molecular weight: 2000), vacuumize and dehydrate at 100°C for 2 hours, and then add isophor Ketone diisocyanate 60g, hydrophilic chain extender dimethylol propionic acid 10g, small molecule chain extender 1,4-butanediol 8g, dihydroxyl-terminated polydimethylsiloxane (number average molecular weight is 1000) 10g and catalyst dibutyltin dilaurate 0.1g, under nitrogen protection throughout the process, the temperature of the oil bath was controlled at 80°C, the stirring speed was 380 rpm, and the reaction was carried out for 3 hours until -NCO reached the theoretical value to obtain a prepolymer;
将反应器内温度降至40度,加入50ml丙酮降粘30分钟,然后将温度降至25℃,加入成盐剂三乙胺3g,反应10分钟,再加入去离子水,在1200转/分钟的转速下高速搅拌30分钟进行乳化,得到水性聚氨酯乳液;Lower the temperature in the reactor to 40°C, add 50ml of acetone to reduce the viscosity for 30 minutes, then lower the temperature to 25°C, add 3g of salt-forming agent triethylamine, react for 10 minutes, then add deionized water, at 1200 rpm High-speed stirring under the rotating speed of 30 minutes carries out emulsification, obtains water-based polyurethane emulsion;
在得到的水性聚氨酯乳液中加入甲基丙烯酸甲酯和丙烯酸丁酯的混合物50g(其质量比为1:1),同时加入0.5g乳化剂十二烷基硫酸钠(SDS),25℃下预溶胀14小时(即常温下机械搅拌14小时),搅拌速度为300转/分钟,待预溶胀14小时后,将反应温度升至70℃,加入引发剂偶氮二异丁氰0.5g及剩余乳化剂1g,氮气保护下,搅拌反应5小时,得到水性聚氨酯-聚丙烯酸酯复合乳液。In the aqueous polyurethane emulsion obtained, add 50g (its mass ratio is 1:1) of the mixture of methyl methacrylate and butyl acrylate, add 0.5g emulsifier sodium dodecyl sulfate (SDS) simultaneously, under 25 ℃, pre- Swell for 14 hours (that is, mechanically stir for 14 hours at room temperature), and the stirring speed is 300 rpm. After 14 hours of pre-swelling, the reaction temperature is raised to 70 ° C, and 0.5 g of initiator azobisisobutylcyanide and remaining emulsified Agent 1g, under the protection of nitrogen, stirred and reacted for 5 hours to obtain a water-based polyurethane-polyacrylate composite emulsion.
将得到的水性聚氨酯-聚丙烯酸酯乳液和涂膜进行测试与表征,结果如表1所示。The obtained aqueous polyurethane-polyacrylate emulsion and coating film were tested and characterized, and the results are shown in Table 1.
图1为本发明实施例1制备的一种水性聚氨酯-聚丙烯酸酯乳液的透射电镜照片。从图1中可以看出,乳液粒子分布较均一,粒径在合理的范围内,且该粒子的结构为semi-IPN(半-网络互穿)结构。Fig. 1 is a transmission electron microscope photograph of a kind of water-based polyurethane-polyacrylate emulsion prepared in Example 1 of the present invention. It can be seen from Figure 1 that the distribution of emulsion particles is relatively uniform, the particle size is within a reasonable range, and the structure of the particles is a semi-IPN (semi-interpenetrating network) structure.
图2为本发明实施例1制备的一种水性聚氨酯-聚丙烯酸酯乳液的涂膜的吸水性和水接触角测试,从图2中可以看出,其接触角达到93.1°,吸水率为9.61%,涂膜耐水性较好。Fig. 2 is the water absorbency and the water contact angle test of the coating film of a kind of aqueous polyurethane-polyacrylate emulsion prepared in the embodiment of the present invention 1, as can be seen from Fig. 2, its contact angle reaches 93.1 °, and water absorption rate is 9.61 %, the water resistance of the coating film is better.
实施例2Example 2
在装有搅拌装置、冷凝管、温度计并通有氮气的四口烧瓶中,加入聚氧化乙烯二醇(数均分子量为1000)60g,在100℃下抽真空脱水2小时,之后加入六亚甲基二异氰酸酯40g,亲水扩链剂甲基二乙醇胺8g,小分子扩链剂新戊二醇6g,氨基封端聚二甲基硅氧烷(数均分子量为1000)8g和催化剂辛酸亚锡0.05g,全程氮气保护,油浴锅温度控制在80℃,搅拌速度为380转/分钟,反应3小时至-NCO达到理论值,得到预聚物;In a four-necked flask equipped with a stirring device, a condenser, a thermometer and nitrogen, add 60 g of polyoxyethylene diol (number average molecular weight: 1000), vacuumize and dehydrate at 100 ° C for 2 hours, and then add hexamethylene Diisocyanate 40g, hydrophilic chain extender methyldiethanolamine 8g, small molecule chain extender neopentyl glycol 6g, amodimethicone (number average molecular weight is 1000) 8g and catalyst stannous octoate 0.05g, nitrogen protection throughout the whole process, the temperature of the oil bath is controlled at 80°C, the stirring speed is 380 rpm, and the reaction is carried out for 3 hours until -NCO reaches the theoretical value to obtain the prepolymer;
将反应器内温度降至40度,加入30ml丙酮降粘30分钟,然后将温度降至25℃,加入成盐剂三乙胺2g,反应10分钟,再加入去离子水,在1200转/分钟的转速下高速搅拌30分钟进行乳化,得到水性聚氨酯;Lower the temperature in the reactor to 40°C, add 30ml of acetone to reduce the viscosity for 30 minutes, then lower the temperature to 25°C, add 2g of salt-forming agent triethylamine, react for 10 minutes, then add deionized water, at 1200 rpm Stir at a high speed under the rotating speed of 30 minutes and carry out emulsification, obtain water-based polyurethane;
在得到的水性聚氨酯乳液中加入甲基丙烯酸甲酯和丙烯酸丁酯的混合物30g(其质量比为1:1),同时加入0.3g乳化剂十二烷基磺酸钠,25℃下预溶胀14小时(即常温下机械搅拌14小时),搅拌速度为300转/分钟,待预溶胀14小时后,将反应温度升至70℃,加入引发剂过硫酸钾0.3g及剩余乳化剂0.6g,氮气保护下,搅拌反应5小时,得到水性聚氨酯-聚丙烯酸酯复合乳液。Add 30 g of a mixture of methyl methacrylate and butyl acrylate (its mass ratio is 1:1) to the obtained aqueous polyurethane emulsion, and add 0.3 g of emulsifier sodium dodecyl sulfonate at the same time, and pre-swell for 14 at 25 ° C. hours (that is, mechanical stirring at room temperature for 14 hours), the stirring speed is 300 rpm, after pre-swelling for 14 hours, the reaction temperature is raised to 70 ° C, and 0.3 g of initiator potassium persulfate and 0.6 g of remaining emulsifier are added, nitrogen Under protection, stirring and reacting for 5 hours, an aqueous polyurethane-polyacrylate composite emulsion was obtained.
将得到的水性聚氨酯-聚丙烯酸酯乳液和涂膜进行测试与表征,结果如表1所示。The obtained aqueous polyurethane-polyacrylate emulsion and coating film were tested and characterized, and the results are shown in Table 1.
实施例3Example 3
在装有搅拌装置、冷凝管、温度计并通有氮气的四口烧瓶中,加入聚氧化乙烯二醇(数均分子量为2000)100g,在100℃下抽真空脱水2小时,之后加入异佛尔酮二异氰酸酯75g,亲水扩链剂二羟甲基丁酸15g,小分子扩链剂2-甲基-1,3-丙二醇10g,双羟基封端聚二甲基硅氧烷(数均分子量为2000)15g和催化剂二月桂酸二丁基锡0.1g,全程氮气保护,油浴锅温度控制在80℃,搅拌速度为380转/分钟,反应3小时至-NCO达到理论值,得到预聚物;In a four-necked flask equipped with a stirring device, a condenser, a thermometer and nitrogen, add 100 g of polyoxyethylene diol (number average molecular weight: 2000), vacuumize and dehydrate at 100°C for 2 hours, and then add Isophor Ketone diisocyanate 75g, hydrophilic chain extender dimethylol butyric acid 15g, small molecule chain extender 2-methyl-1,3-propanediol 10g, dihydroxy-terminated polydimethylsiloxane (number average molecular weight 2000) 15g and catalyst dibutyltin dilaurate 0.1g, under nitrogen protection throughout the process, the temperature of the oil bath was controlled at 80°C, the stirring speed was 380 rpm, and the reaction was carried out for 3 hours until -NCO reached the theoretical value to obtain a prepolymer;
将反应器内温度降至40度,加入60ml丙酮降粘30分钟,然后将温度降至25℃,加入成盐剂三乙胺4g,反应10分钟,再加入去离子水,在1200转/分钟的转速下高速搅拌30分钟进行乳化,得到水性聚氨酯;Lower the temperature in the reactor to 40°C, add 60ml of acetone to reduce the viscosity for 30 minutes, then lower the temperature to 25°C, add 4g of salt-forming agent triethylamine, react for 10 minutes, then add deionized water, at 1200 rpm Stir at a high speed under the rotating speed of 30 minutes and carry out emulsification, obtain water-based polyurethane;
在得到的水性聚氨酯乳液中加入甲基丙烯酸甲酯和丙烯酸丁酯的混合物60g(其质量比为1:1),同时加入0.6g乳化剂十二烷基硫酸钠,25℃下预溶胀14小时(即常温下机械搅拌14小时),搅拌速度为300转/分钟,待预溶胀14小时后,将反应温度升至70℃,加入引发剂过过氧化苯甲酰0.6g及剩余乳化剂1.2g,氮气保护下,搅拌反应5小时,得到水性聚氨酯-聚丙烯酸酯复合乳液。Add 60 g of a mixture of methyl methacrylate and butyl acrylate (the mass ratio is 1:1) to the obtained aqueous polyurethane emulsion, and add 0.6 g of emulsifier sodium lauryl sulfate at the same time, pre-swell at 25 ° C for 14 hours (i.e. mechanical stirring at room temperature for 14 hours), the stirring speed is 300 rpm, after pre-swelling for 14 hours, the reaction temperature is raised to 70°C, and the initiator benzoyl peroxide 0.6g and the remaining emulsifier 1.2g are added , under the protection of nitrogen, stirred and reacted for 5 hours to obtain an aqueous polyurethane-polyacrylate composite emulsion.
将得到的水性聚氨酯-聚丙烯酸酯乳液和涂膜进行测试与表征,结果如表1所示。The obtained aqueous polyurethane-polyacrylate emulsion and coating film were tested and characterized, and the results are shown in Table 1.
实施例4Example 4
在装有搅拌装置、冷凝管、温度计并通有氮气的四口烧瓶中,加入聚四氢呋喃醚二醇(数均分子量为2000)70g,在100℃下抽真空脱水2小时,之后加入异佛尔酮二异氰酸酯50g,亲水扩链剂二羟甲基丁酸9g,小分子扩链剂1,4-丁二醇7g,羟基封端聚二甲基硅氧烷(数均分子量为1000)8g和催化剂二月桂酸二丁基锡0.1g,全程氮气保护,油浴锅温度控制在80℃,搅拌速度为380转/分钟,反应3小时至-NCO达到理论值,得到预聚物;In a four-necked flask equipped with a stirring device, a condenser, a thermometer and nitrogen, add 70 g of polytetrahydrofuran ether diol (number average molecular weight: 2000), vacuum dehydrate at 100 ° C for 2 hours, and then add isophor Ketone diisocyanate 50g, hydrophilic chain extender dimethylol butyric acid 9g, small molecule chain extender 1,4-butanediol 7g, hydroxyl-terminated polydimethylsiloxane (number average molecular weight: 1000) 8g and the catalyst dibutyltin dilaurate 0.1g, under nitrogen protection throughout the process, the temperature of the oil bath was controlled at 80°C, the stirring speed was 380 rpm, and the reaction was carried out for 3 hours until -NCO reached the theoretical value to obtain a prepolymer;
将反应器内温度降至40度,加入40ml丙酮降粘30分钟,然后将温度降至25℃,加入成盐剂三乙胺3g,反应10分钟,再加入去离子水,在1200转/分钟的转速下高速搅拌30分钟进行乳化,得到水性聚氨酯;Lower the temperature in the reactor to 40°C, add 40ml of acetone to reduce the viscosity for 30 minutes, then lower the temperature to 25°C, add 3g of salt-forming agent triethylamine, react for 10 minutes, then add deionized water, at 1200 rpm Stir at a high speed under the rotating speed of 30 minutes and carry out emulsification, obtain water-based polyurethane;
在得到的水性聚氨酯乳液中加入甲基丙烯酸甲酯和丙烯酸丁酯的混合物40g(其质量比为1:1),同时加入0.4g乳化剂十二烷基硫酸钠,25℃下预溶胀14小时(即常温下机械搅拌14小时),搅拌速度为300转/分钟,待预溶胀14小时后,将反应温度升至70℃,加入引发剂过硫酸钾0.4g及剩余乳化剂0.8g,氮气保护下,搅拌反应5小时,得到水性聚氨酯-聚丙烯酸酯复合乳液。Add 40 g of a mixture of methyl methacrylate and butyl acrylate (the mass ratio is 1:1) to the obtained aqueous polyurethane emulsion, and add 0.4 g of emulsifier sodium lauryl sulfate at the same time, pre-swell for 14 hours at 25 ° C (that is, mechanical stirring at room temperature for 14 hours), the stirring speed is 300 rpm, and after 14 hours of pre-swelling, the reaction temperature is raised to 70 ° C, and 0.4 g of initiator potassium persulfate and 0.8 g of remaining emulsifier are added. Under stirring reaction for 5 hours, water-based polyurethane-polyacrylate composite emulsion was obtained.
将得到的水性聚氨酯-聚丙烯酸酯乳液和涂膜进行测试与表征,结果如表1所示。The obtained aqueous polyurethane-polyacrylate emulsion and coating film were tested and characterized, and the results are shown in Table 1.
表1Table 1
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