JPH0635498B2 - Method for producing vinyl chloride resin - Google Patents
Method for producing vinyl chloride resinInfo
- Publication number
- JPH0635498B2 JPH0635498B2 JP60175776A JP17577685A JPH0635498B2 JP H0635498 B2 JPH0635498 B2 JP H0635498B2 JP 60175776 A JP60175776 A JP 60175776A JP 17577685 A JP17577685 A JP 17577685A JP H0635498 B2 JPH0635498 B2 JP H0635498B2
- Authority
- JP
- Japan
- Prior art keywords
- vinyl chloride
- weight
- parts
- chloride resin
- alkyl
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 title claims description 36
- 229920005989 resin Polymers 0.000 title claims description 20
- 239000011347 resin Substances 0.000 title claims description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000000178 monomer Substances 0.000 claims description 21
- 125000005250 alkyl acrylate group Chemical group 0.000 claims description 12
- -1 alkyl methacrylate Chemical compound 0.000 claims description 11
- 229920001519 homopolymer Polymers 0.000 claims description 10
- 230000007704 transition Effects 0.000 claims description 9
- 229920001577 copolymer Polymers 0.000 claims description 5
- 150000002825 nitriles Chemical class 0.000 claims description 3
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical compound C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 claims description 3
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 claims description 2
- 238000000034 method Methods 0.000 description 18
- 238000007334 copolymerization reaction Methods 0.000 description 13
- 229920006243 acrylic copolymer Polymers 0.000 description 11
- 238000006116 polymerization reaction Methods 0.000 description 10
- 229920000578 graft copolymer Polymers 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000003505 polymerization initiator Substances 0.000 description 4
- 238000010558 suspension polymerization method Methods 0.000 description 4
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 3
- 239000007900 aqueous suspension Substances 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 3
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- UZKWTJUDCOPSNM-UHFFFAOYSA-N 1-ethenoxybutane Chemical compound CCCCOC=C UZKWTJUDCOPSNM-UHFFFAOYSA-N 0.000 description 2
- LEJBBGNFPAFPKQ-UHFFFAOYSA-N 2-(2-prop-2-enoyloxyethoxy)ethyl prop-2-enoate Chemical compound C=CC(=O)OCCOCCOC(=O)C=C LEJBBGNFPAFPKQ-UHFFFAOYSA-N 0.000 description 2
- XFCMNSHQOZQILR-UHFFFAOYSA-N 2-[2-(2-methylprop-2-enoyloxy)ethoxy]ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCOC(=O)C(C)=C XFCMNSHQOZQILR-UHFFFAOYSA-N 0.000 description 2
- INQDDHNZXOAFFD-UHFFFAOYSA-N 2-[2-(2-prop-2-enoyloxyethoxy)ethoxy]ethyl prop-2-enoate Chemical compound C=CC(=O)OCCOCCOCCOC(=O)C=C INQDDHNZXOAFFD-UHFFFAOYSA-N 0.000 description 2
- KUDUQBURMYMBIJ-UHFFFAOYSA-N 2-prop-2-enoyloxyethyl prop-2-enoate Chemical compound C=CC(=O)OCCOC(=O)C=C KUDUQBURMYMBIJ-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 2
- QYKIQEUNHZKYBP-UHFFFAOYSA-N Vinyl ether Chemical class C=COC=C QYKIQEUNHZKYBP-UHFFFAOYSA-N 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
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- GMSCBRSQMRDRCD-UHFFFAOYSA-N dodecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCOC(=O)C(C)=C GMSCBRSQMRDRCD-UHFFFAOYSA-N 0.000 description 2
- 238000010556 emulsion polymerization method Methods 0.000 description 2
- 238000007720 emulsion polymerization reaction Methods 0.000 description 2
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 2
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 description 2
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 description 2
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 description 2
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 description 2
- OCWMFVJKFWXKNZ-UHFFFAOYSA-L lead(2+);oxygen(2-);sulfate Chemical compound [O-2].[O-2].[O-2].[Pb+2].[Pb+2].[Pb+2].[Pb+2].[O-]S([O-])(=O)=O OCWMFVJKFWXKNZ-UHFFFAOYSA-L 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- SJOCPYUKFOTDAN-ZSOIEALJSA-N methyl (4z)-4-hydroxyimino-6,6-dimethyl-3-methylsulfanyl-5,7-dihydro-2-benzothiophene-1-carboxylate Chemical compound C1C(C)(C)C\C(=N\O)C=2C1=C(C(=O)OC)SC=2SC SJOCPYUKFOTDAN-ZSOIEALJSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000007870 radical polymerization initiator Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- DGVVWUTYPXICAM-UHFFFAOYSA-N β‐Mercaptoethanol Chemical compound OCCS DGVVWUTYPXICAM-UHFFFAOYSA-N 0.000 description 2
- HGXJDMCMYLEZMJ-UHFFFAOYSA-N (2-methylpropan-2-yl)oxy 2,2-dimethylpropaneperoxoate Chemical compound CC(C)(C)OOOC(=O)C(C)(C)C HGXJDMCMYLEZMJ-UHFFFAOYSA-N 0.000 description 1
- LNAZSHAWQACDHT-XIYTZBAFSA-N (2r,3r,4s,5r,6s)-4,5-dimethoxy-2-(methoxymethyl)-3-[(2s,3r,4s,5r,6r)-3,4,5-trimethoxy-6-(methoxymethyl)oxan-2-yl]oxy-6-[(2r,3r,4s,5r,6r)-4,5,6-trimethoxy-2-(methoxymethyl)oxan-3-yl]oxyoxane Chemical compound CO[C@@H]1[C@@H](OC)[C@H](OC)[C@@H](COC)O[C@H]1O[C@H]1[C@H](OC)[C@@H](OC)[C@H](O[C@H]2[C@@H]([C@@H](OC)[C@H](OC)O[C@@H]2COC)OC)O[C@@H]1COC LNAZSHAWQACDHT-XIYTZBAFSA-N 0.000 description 1
- VDYWHVQKENANGY-UHFFFAOYSA-N 1,3-Butyleneglycol dimethacrylate Chemical compound CC(=C)C(=O)OC(C)CCOC(=O)C(C)=C VDYWHVQKENANGY-UHFFFAOYSA-N 0.000 description 1
- LAYAKLSFVAPMEL-UHFFFAOYSA-N 1-ethenoxydodecane Chemical compound CCCCCCCCCCCCOC=C LAYAKLSFVAPMEL-UHFFFAOYSA-N 0.000 description 1
- XXCVIFJHBFNFBO-UHFFFAOYSA-N 1-ethenoxyoctane Chemical compound CCCCCCCCOC=C XXCVIFJHBFNFBO-UHFFFAOYSA-N 0.000 description 1
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 description 1
- ZFFMLCVRJBZUDZ-UHFFFAOYSA-N 2,3-dimethylbutane Chemical group CC(C)C(C)C ZFFMLCVRJBZUDZ-UHFFFAOYSA-N 0.000 description 1
- GOXQRTZXKQZDDN-UHFFFAOYSA-N 2-Ethylhexyl acrylate Chemical compound CCCCC(CC)COC(=O)C=C GOXQRTZXKQZDDN-UHFFFAOYSA-N 0.000 description 1
- HWSSEYVMGDIFMH-UHFFFAOYSA-N 2-[2-[2-(2-methylprop-2-enoyloxy)ethoxy]ethoxy]ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCOCCOC(=O)C(C)=C HWSSEYVMGDIFMH-UHFFFAOYSA-N 0.000 description 1
- CFVWNXQPGQOHRJ-UHFFFAOYSA-N 2-methylpropyl prop-2-enoate Chemical compound CC(C)COC(=O)C=C CFVWNXQPGQOHRJ-UHFFFAOYSA-N 0.000 description 1
- HTWRFCRQSLVESJ-UHFFFAOYSA-N 3-(2-methylprop-2-enoyloxy)propyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCCOC(=O)C(C)=C HTWRFCRQSLVESJ-UHFFFAOYSA-N 0.000 description 1
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 1
- DBCAQXHNJOFNGC-UHFFFAOYSA-N 4-bromo-1,1,1-trifluorobutane Chemical compound FC(F)(F)CCCBr DBCAQXHNJOFNGC-UHFFFAOYSA-N 0.000 description 1
- SJVGFKBLUYAEOK-SFHVURJKSA-N 6-[4-[(3S)-3-(3,5-difluorophenyl)-3,4-dihydropyrazole-2-carbonyl]piperidin-1-yl]pyrimidine-4-carbonitrile Chemical compound FC=1C=C(C=C(C=1)F)[C@@H]1CC=NN1C(=O)C1CCN(CC1)C1=CC(=NC=N1)C#N SJVGFKBLUYAEOK-SFHVURJKSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- WOSHQKYMJRBBMW-UHFFFAOYSA-N C(C=C)(=O)O.C(C(=C)C)(=O)O.C(C(=C)C)(=O)O.C(CCCO)O Chemical compound C(C=C)(=O)O.C(C(=C)C)(=O)O.C(C(=C)C)(=O)O.C(CCCO)O WOSHQKYMJRBBMW-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 239000004641 Diallyl-phthalate Substances 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- DCXXMTOCNZCJGO-UHFFFAOYSA-N Glycerol trioctadecanoate Natural products CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 description 1
- 239000004609 Impact Modifier Substances 0.000 description 1
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 description 1
- GYCMBHHDWRMZGG-UHFFFAOYSA-N Methylacrylonitrile Chemical compound CC(=C)C#N GYCMBHHDWRMZGG-UHFFFAOYSA-N 0.000 description 1
- 239000006057 Non-nutritive feed additive Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- JAWMENYCRQKKJY-UHFFFAOYSA-N [3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-ylmethyl)-1-oxa-2,8-diazaspiro[4.5]dec-2-en-8-yl]-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]methanone Chemical compound N1N=NC=2CN(CCC=21)CC1=NOC2(C1)CCN(CC2)C(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F JAWMENYCRQKKJY-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 1
- 239000012874 anionic emulsifier Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- ZPOLOEWJWXZUSP-AATRIKPKSA-N bis(prop-2-enyl) (e)-but-2-enedioate Chemical compound C=CCOC(=O)\C=C\C(=O)OCC=C ZPOLOEWJWXZUSP-AATRIKPKSA-N 0.000 description 1
- YLTDNYQTDYMOBH-UHFFFAOYSA-N bis(prop-2-enyl) 2-hydroxybutanedioate Chemical compound C=CCOC(=O)C(O)CC(=O)OCC=C YLTDNYQTDYMOBH-UHFFFAOYSA-N 0.000 description 1
- QUDWYFHPNIMBFC-UHFFFAOYSA-N bis(prop-2-enyl) benzene-1,2-dicarboxylate Chemical compound C=CCOC(=O)C1=CC=CC=C1C(=O)OCC=C QUDWYFHPNIMBFC-UHFFFAOYSA-N 0.000 description 1
- HABAXTXIECRCKH-UHFFFAOYSA-N bis(prop-2-enyl) butanedioate Chemical compound C=CCOC(=O)CCC(=O)OCC=C HABAXTXIECRCKH-UHFFFAOYSA-N 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000012986 chain transfer agent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- GTBGXKPAKVYEKJ-UHFFFAOYSA-N decyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCOC(=O)C(C)=C GTBGXKPAKVYEKJ-UHFFFAOYSA-N 0.000 description 1
- FWLDHHJLVGRRHD-UHFFFAOYSA-N decyl prop-2-enoate Chemical compound CCCCCCCCCCOC(=O)C=C FWLDHHJLVGRRHD-UHFFFAOYSA-N 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- UQLDLKMNUJERMK-UHFFFAOYSA-L di(octadecanoyloxy)lead Chemical compound [Pb+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O UQLDLKMNUJERMK-UHFFFAOYSA-L 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- UIWXSTHGICQLQT-UHFFFAOYSA-N ethenyl propanoate Chemical compound CCC(=O)OC=C UIWXSTHGICQLQT-UHFFFAOYSA-N 0.000 description 1
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Substances CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- LNMQRPPRQDGUDR-UHFFFAOYSA-N hexyl prop-2-enoate Chemical compound CCCCCCOC(=O)C=C LNMQRPPRQDGUDR-UHFFFAOYSA-N 0.000 description 1
- 229920003063 hydroxymethyl cellulose Polymers 0.000 description 1
- 229940031574 hydroxymethyl cellulose Drugs 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 150000002734 metacrylic acid derivatives Chemical class 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- VOVZXURTCKPRDQ-CQSZACIVSA-N n-[4-[chloro(difluoro)methoxy]phenyl]-6-[(3r)-3-hydroxypyrrolidin-1-yl]-5-(1h-pyrazol-5-yl)pyridine-3-carboxamide Chemical compound C1[C@H](O)CCN1C1=NC=C(C(=O)NC=2C=CC(OC(F)(F)Cl)=CC=2)C=C1C1=CC=NN1 VOVZXURTCKPRDQ-CQSZACIVSA-N 0.000 description 1
- AMEVLYGGLRIBIO-UHFFFAOYSA-N octoxycarbonyloxy octyl carbonate Chemical compound CCCCCCCCOC(=O)OOC(=O)OCCCCCCCC AMEVLYGGLRIBIO-UHFFFAOYSA-N 0.000 description 1
- NZIDBRBFGPQCRY-UHFFFAOYSA-N octyl 2-methylprop-2-enoate Chemical compound CCCCCCCCOC(=O)C(C)=C NZIDBRBFGPQCRY-UHFFFAOYSA-N 0.000 description 1
- ANISOHQJBAQUQP-UHFFFAOYSA-N octyl prop-2-enoate Chemical compound CCCCCCCCOC(=O)C=C ANISOHQJBAQUQP-UHFFFAOYSA-N 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 1
- NHARPDSAXCBDDR-UHFFFAOYSA-N propyl 2-methylprop-2-enoate Chemical compound CCCOC(=O)C(C)=C NHARPDSAXCBDDR-UHFFFAOYSA-N 0.000 description 1
- PNXMTCDJUBJHQJ-UHFFFAOYSA-N propyl prop-2-enoate Chemical compound CCCOC(=O)C=C PNXMTCDJUBJHQJ-UHFFFAOYSA-N 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007779 soft material Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
Landscapes
- Graft Or Block Polymers (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、塩化ビニル樹脂の製造法に関するものであ
る。更に詳しくは耐衝撃性,耐候性,曲げ弾性率に優れ
た塩化ビニル樹脂を製造する方法に関する。TECHNICAL FIELD The present invention relates to a method for producing a vinyl chloride resin. More specifically, it relates to a method for producing a vinyl chloride resin excellent in impact resistance, weather resistance and flexural modulus.
塩化ビニル樹脂は優れた物理的,機械的性質を有してい
るため、硬質,半硬質,軟質用樹脂として多くの用途が
ある。しかし、硬質用に塩化ビニルホモポリマーを使用
すると、耐衝撃性,耐候性に劣るという欠点を有してい
た。これらの欠点を改良する方法として、塩化ビニルホ
モポリマーと各種の弾性体とのポリマーブレンドが挙げ
られる。この方法によれば確かに耐衝撃性を改良するこ
とができるが、反対に耐候性,曲げ弾性率が低下すると
いう欠陥を有している。Since vinyl chloride resin has excellent physical and mechanical properties, it has many uses as a resin for hard, semi-hard, and soft materials. However, when a vinyl chloride homopolymer is used for hard materials, it has the drawback of being inferior in impact resistance and weather resistance. As a method for improving these drawbacks, a polymer blend of a vinyl chloride homopolymer and various elastic bodies can be mentioned. Although this method can certainly improve the impact resistance, it has a defect that the weather resistance and the flexural modulus are decreased.
アルキルアクリレート重合体に塩化ビニルをグラフト共
重合して得られた塩化ビニルグラフト共重合体が知られ
ており(特公昭39−17067)この塩化ビニルグラ
フト共重合体は、確かに耐衝撃性は向上するが、曲げ弾
性率が充分でないという欠点があつた。以上の如く、現
在までに知られた各方法はいずれも一長一短があり、そ
のため用途もある程度制限されて来た。A vinyl chloride graft copolymer obtained by graft-copolymerizing vinyl chloride with an alkyl acrylate polymer is known (Japanese Patent Publication No. 39-17067). This vinyl chloride graft copolymer is certainly improved in impact resistance. However, there was a drawback that the flexural modulus was not sufficient. As described above, each of the methods known to date has advantages and disadvantages, and therefore the applications have been limited to some extent.
本発明の目的は耐衝撃性,耐候性に優れ、かつ曲げ弾性
率も向上した物性のバランスのとれた塩化ビニル樹脂を
得る方法を提供することにある。An object of the present invention is to provide a method for obtaining a vinyl chloride resin having excellent impact resistance, weather resistance, and improved flexural modulus and well-balanced physical properties.
本発明者らは、前記問題点を解決するため鋭意研究を行
い、本発明を完成するに至つたものである。The inventors of the present invention have conducted intensive studies to solve the above problems and completed the present invention.
すなわち、本発明者らは、耐衝撃性,耐候性に優れかつ
曲げ弾性率に優れた塩化ビニル樹脂を得るための方法に
つき詳細な検討を重ねた結果、ホモポリマーとした時の
二次転移点が−10℃以下であるアルキルアクリレート
および/又はアルキルメタクリレートと、ホモポリマー
とした時の二次転移点が0℃以上の特定のモノマーと多
官能性モノマーとの共重合体に塩化ビニルをグラフト共
重合することにより、耐衝撃性,耐候性に優れかつ、曲
げ弾性率に優れた塩化ビニル樹脂を製造し得ることを見
い出し本発明に至つた。すなわち、本発明はホモポリマ
ーとしたときに、その二次転移点が−10℃以下である
アルキルアクリレートおよび/又はアルキルメタクリレ
ート95〜60重量%とホモポリマーとしたときの二次
転移点が0℃以上でα−メチルスチレン、ビニルトルエ
ン、不飽和ニトリル類、ビニルエーテル類、アルキルア
クリレート類、アルキルメタクリレート類よりなる群よ
り選ばれた少なくとも一つのモノマー5〜39重量%と
多官能性モノマー1〜30重量%とを共重合させて得ら
れた共重合体(以下アクリル系共重合体と記す)1〜3
0重量部に対して塩化ビニル99〜70重量部をグラフ
ト共重合させることを特徴とする耐衝撃性,耐候性に優
れ、かつ曲げ弾性率に優れた塩化ビニル樹脂の製造方法
である。That is, the present inventors have conducted a detailed study on a method for obtaining a vinyl chloride resin excellent in impact resistance, weather resistance and flexural modulus, and as a result, the secondary transition point when a homopolymer is obtained. With a vinyl chloride graft copolymer to a copolymer of an alkyl acrylate and / or an alkyl methacrylate having a temperature of −10 ° C. or lower, and a specific monomer having a secondary transition point of 0 ° C. or higher when formed into a homopolymer and a polyfunctional monomer. It has been found that a vinyl chloride resin having excellent impact resistance and weather resistance and an excellent flexural modulus can be produced by polymerization, and the present invention has been completed. That is, when the present invention is a homopolymer, the secondary transition point of the alkyl acrylate and / or alkyl methacrylate of which the secondary transition point is −10 ° C. or lower is 95 to 60% by weight, and the secondary transition point of the homopolymer is 0 ° C. At least 5 to 39% by weight of at least one monomer selected from the group consisting of α-methylstyrene, vinyltoluene, unsaturated nitriles, vinyl ethers, alkyl acrylates and alkyl methacrylates, and 1 to 30% by weight of polyfunctional monomers. % Copolymers (hereinafter referred to as “acrylic copolymers”) 1-3
A method for producing a vinyl chloride resin excellent in impact resistance, weather resistance and flexural modulus, characterized by graft-copolymerizing 99 to 70 parts by weight of vinyl chloride with respect to 0 part by weight.
本発明に使用されるアルキルアクリレートおよびアルキ
ルメタクリレートとしては、ホモポリマーとしたとき
に、その二次転移点が−10℃以下のもので、例えば、
エチルアクリレート,n−プロピルアクリレート,イソ
−ブチルアクリレート,n−ブチルアクリレート,n−
ヘキシルアクリレート,2−エチルヘキシルアクリレー
ト,n−オクチルアクリレート,n−デシルアクリレー
トおよびn−オクチルメタクリレート,n−デシルメタ
クリレート,n−ドデシルメタクリレート,ラウリルメ
タクリレート等があげられる。これらアルキルアクリレ
ートおよびアルキルメタクリレートは共重合物のソフト
セグメントとして働きすぐれた耐衝撃性を付与するもの
でその使用量は95〜60重量%が好適であり、95重
量%を超えると曲げ弾性率の向上が望めず、60重量%
未満では、耐衝撃性が低下するので好ましくない。The alkyl acrylate and alkyl methacrylate used in the present invention have a secondary transition point of −10 ° C. or lower when formed into a homopolymer, and include, for example,
Ethyl acrylate, n-propyl acrylate, iso-butyl acrylate, n-butyl acrylate, n-
Hexyl acrylate, 2-ethylhexyl acrylate, n-octyl acrylate, n-decyl acrylate and n-octyl methacrylate, n-decyl methacrylate, n-dodecyl methacrylate, lauryl methacrylate and the like can be mentioned. These alkyl acrylates and alkyl methacrylates act as soft segments of the copolymer to impart excellent impact resistance, and the amount used is preferably 95 to 60% by weight, and when it exceeds 95% by weight, the flexural modulus is improved. Can not be expected, 60% by weight
When it is less than 1, the impact resistance is lowered, which is not preferable.
本発明に使用される特定のモノマーとしては、ホモポリ
マーにしたときの二次転移点が0℃以上のもので、α−
メチルスチレン,ビニルトルエンなどの芳香族ビニル
類、アクリロニトリル,メタクリロニトリルなどの不飽
和ニトリル類,酢酸ビニル,プロピオン酸ビニルなどの
ビニルエステル類,ブチルビニルエーテル,オクチルビ
ニルエーテル,ラウリルビニルエーテルなどのビニルエ
ーテル類,メチルアクリレートのごときアルキルアクリ
レート類,メチルメタクリレート,エチルメタクリレー
ト,プロピルメタクリレートなどのアルキルメタクリレ
ート類からなる群から選ばれたモノマーで単独、又は二
種以上の混合で使用される。これらモノマー類は共重合
することによりハードセグメントとして働きその使用量
は、5〜39重量%が好適であり、5重量%未満では、
曲げ弾性率の向上が望めず、又39重量%を超えると、
耐衝撃性が低下するので好ましくない。特に曲げ弾性率
を調整する場合は、メチルメタクリレート,メチルアク
リレート,アクリロニトリルが好適である。The specific monomer used in the present invention has a second-order transition point of 0 ° C. or higher when formed into a homopolymer, and α-
Aromatic vinyls such as methylstyrene and vinyltoluene, unsaturated nitriles such as acrylonitrile and methacrylonitrile, vinyl esters such as vinyl acetate and vinyl propionate, vinyl ethers such as butyl vinyl ether, octyl vinyl ether and lauryl vinyl ether, methyl Monomers selected from the group consisting of alkyl acrylates such as acrylates, alkyl methacrylates such as methyl methacrylate, ethyl methacrylate, and propyl methacrylate are used alone or in combination of two or more. These monomers work as a hard segment by copolymerization, and the amount used is preferably 5 to 39% by weight, and when less than 5% by weight,
If the flexural modulus cannot be improved and if it exceeds 39% by weight,
It is not preferable because the impact resistance is lowered. In particular, when adjusting the flexural modulus, methyl methacrylate, methyl acrylate, and acrylonitrile are suitable.
本発明に使用される多官能性モノマーとは、アルキルア
クリレートおよび/又は、アルキルメタクリレートに架
橋等を生じせしめる多官能性のモノマーであつて、例え
ばエチレングリコールジアクリレート,ジエチレングリ
コールジアクリレート,トリエチレングリコールジアク
リレート、エチレングリコールジメタクリレート,ジエ
チレングリコールジメタクリレート,トリエチレングリ
コールジメタクリレート,1,3−プロピレングリコー
ルジメタクリレート,1,3−ブチレングリコールジメ
タクリレート,1,4−ブチレングリコールジメタクリ
レート等モノもしくはポリアルキレングリコールのアク
リレートもしくは、メタクリレート類、ジアリルフタレ
ート,ジアリルマレート,ジアリルフマレート,ジアリ
ルサクシネート等のジもしくは、トリアリル化合物類お
よびジビニルベンゼン等があげられる。多官能性モノマ
ーの使用量は、1〜30重量%が好適であり1重量%未
満では、曲げ弾性率の向上が望めず、又30重量%を超
えると耐衝撃性が低下するので好ましくない。The polyfunctional monomer used in the present invention is a polyfunctional monomer that causes crosslinking or the like in alkyl acrylate and / or alkyl methacrylate, and examples thereof include ethylene glycol diacrylate, diethylene glycol diacrylate, and triethylene glycol diacrylate. Of mono- or polyalkylene glycols such as acrylate, ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, triethylene glycol dimethacrylate, 1,3-propylene glycol dimethacrylate, 1,3-butylene glycol dimethacrylate, 1,4-butylene glycol dimethacrylate Acrylate or methacrylates, diallyl phthalate, diallyl malate, diallyl fumarate, diallyl succinate, etc. Di- or triallyl compounds and divinylbenzene and the like. The amount of the polyfunctional monomer to be used is preferably 1 to 30% by weight. If it is less than 1% by weight, the flexural modulus cannot be expected to be improved, and if it exceeds 30% by weight, the impact resistance is lowered, which is not preferable.
本発明に使用するアルキルアクリレートおよび/又はア
ルキルメタクリレートと、前記モノマー類とおよび多官
能性モノマー類この共重合体は一般公知の乳化剤,分散
剤,触媒等を使用して乳化重合,懸濁重合,溶液重合又
は塊状重合等の重合方法により得られるが特に乳化重合
が好ましい。一般的な乳化重合法によつて、共重合体を
得る方法としては、例えばジヤケツト付重合反応機内に
純水,アニオン系乳化剤,水溶性重合触媒を入れ、缶内
の空気を排除し、次いでアルキルアクリレートおよび/
又はアルキルメタクリレートと前記モノマー類および多
官能性モノマー類を装入し乳化後缶内をジヤケツト内の
熱媒体により加熱し共重合反応を開始させる。共重合反
応は発熱反応であり、必要に応じてジヤケツト内の熱媒
体により内部温度の制御を行なう。反応終了後未反応の
モノマー類を缶外に除去し、本発明のアクリル系共重合
体を得る。重合反応機への装入方法は特に限定されるも
のではない。又必要に応じてアクリル系共重合体の粒径
調整剤,共重合反応を制御するため触媒の分解促進剤等
を添加しても良い。The alkyl acrylate and / or alkyl methacrylate used in the present invention, the above-mentioned monomers, and polyfunctional monomers are copolymerized by emulsion polymerization, suspension polymerization, using a generally known emulsifier, dispersant, catalyst, etc. It can be obtained by a polymerization method such as solution polymerization or bulk polymerization, but emulsion polymerization is particularly preferable. As a method for obtaining a copolymer by a general emulsion polymerization method, for example, pure water, an anionic emulsifier and a water-soluble polymerization catalyst are put in a polymerization reactor with a jacket, air in the can is eliminated, and then an alkyl Acrylate and /
Alternatively, the alkyl methacrylate, the above-mentioned monomers and polyfunctional monomers are charged, and after emulsification, the inside of the can is heated by the heating medium in the jacket to start the copolymerization reaction. The copolymerization reaction is an exothermic reaction, and if necessary, the internal temperature is controlled by the heat medium in the jacket. After completion of the reaction, unreacted monomers are removed from the can to obtain the acrylic copolymer of the present invention. The charging method into the polymerization reactor is not particularly limited. If necessary, a particle size adjusting agent for the acrylic copolymer and a catalyst decomposition accelerator for controlling the copolymerization reaction may be added.
グラフト共重合の幹ポリマーとして使用するアクリル系
共重合体の使用量は塩化ビニルモノマーの使用量との合
計量100重量部当り1〜30重量部が適当である。ア
クリル系共重合体の使用量が1重量部未満では、耐衝撃
性が充分でなく、又30重量部を超えると、耐衝撃性は
向上するが、曲げ弾性率が低下するので好ましくない。The amount of the acrylic copolymer used as the trunk polymer for the graft copolymerization is appropriately 1 to 30 parts by weight per 100 parts by weight of the total amount including the amount of the vinyl chloride monomer used. If the amount of the acrylic copolymer used is less than 1 part by weight, the impact resistance is insufficient, and if it exceeds 30 parts by weight, the impact resistance is improved but the flexural modulus is lowered, which is not preferable.
本発明のグラフト共重合方法としては水性懸濁重合法、
水性乳化重合法、溶液重合法、無溶媒重合法等があげら
れるが、水性懸濁重合法を採用することが好ましい。As the graft copolymerization method of the present invention, an aqueous suspension polymerization method,
Examples of the aqueous emulsion polymerization method, solution polymerization method, solventless polymerization method and the like are preferable, and the aqueous suspension polymerization method is preferably adopted.
水性懸濁重合法を行う場合、多幹ポリマーのアクリル系
共重合体と塩化ビニルモノマーの合計量と水との重量割
合は1:1〜1:5好ましくは、1:1〜1:8であ
る。一般的な懸濁重合法によつてグラフト共重合共重合
させる方法は、例えばジヤケツト付重合反応機内に、純
水、ヒドロキシプロピルメチルセルローズのような懸濁
安定剤、ラジカル重合開始剤、必要に応じて重合度低下
剤を入れ、これにアクリル系共重合体を入れて懸濁し、
次いで缶内の空気を排除し、次いで塩化ビニルを必要に
応じその他のビニル化合物と共に装入する。その後缶内
をジヤケツト内熱媒体により加熱し、アクリル系共重合
体を塩化ビニル類に溶解し、グラフト共重合を開始させ
る。グラフト共重合は発熱反応であり、必要に応じてジ
ヤケツト内熱媒体により内部温度の制御を行う。反応終
了後、未反応の塩化ビニル類を缶外に除去し、スラリー
状のグラフト共重合させた塩化ビニル樹脂を得る。スラ
リーは常法にしたがい脱水乾燥されグラフト共重合樹脂
が得られる。又重合反応機への装入方法は限定されるも
のではなく、純水、懸濁安定剤、アクリル系共重合体そ
して塩化ビニル等の装入原料のうち、アクリル系共重合
体を塩化ビニルに溶解して装入するという方法も採用さ
れる。When carrying out the aqueous suspension polymerization method, the weight ratio of the total amount of the acrylic copolymer of the multi-stem polymer, the vinyl chloride monomer and water is 1: 1 to 1: 5, preferably 1: 1 to 1: 8. is there. The method of graft copolymerization copolymerization by a general suspension polymerization method is, for example, pure water, a suspension stabilizer such as hydroxypropylmethylcellulose, a radical polymerization initiator, and if necessary, in a polymerization reactor with a jacket. Put a polymerization degree lowering agent, suspend the acrylic copolymer by adding it,
The air in the can is then evacuated and then vinyl chloride is charged, optionally with other vinyl compounds. After that, the inside of the can is heated by the heating medium in the jacket, the acrylic copolymer is dissolved in vinyl chlorides, and the graft copolymerization is started. Graft copolymerization is an exothermic reaction, and the internal temperature is controlled by a heating medium in the jacket, if necessary. After completion of the reaction, unreacted vinyl chloride is removed outside the can to obtain a slurry-like graft copolymerized vinyl chloride resin. The slurry is dehydrated and dried according to a conventional method to obtain a graft copolymer resin. Also, the charging method to the polymerization reactor is not limited, and among the charging materials such as pure water, suspension stabilizer, acrylic copolymer and vinyl chloride, the acrylic copolymer is changed to vinyl chloride. A method of melting and charging is also adopted.
グラフト共重合にあたつては、耐衝撃性,耐候性,曲げ
弾性率を低下させない範囲で、他の単量体を共存させて
もよい。In the graft copolymerization, other monomers may coexist as long as the impact resistance, weather resistance and flexural modulus are not reduced.
本発明を実施するにあたり、グラフト共重合はラジカル
重合法で行うのが有利であり、そのために使用されるラ
ジカル重合開始剤としては、ラウロイルパーオキサイ
ド、ターシヤリーブチルパーオキシピバレート、ジイソ
プロピルパーオキシジカーポネート、ジオクチルパーオ
キシジカーボネート等の有機パーオキサイド類、2,
2′−アゾヒスイソプチロニトリル、2,2′−アゾビ
ス−2,4−ジメチルバレロニトリル等のアゾ化合物の
油溶性重合開始剤、および過硫酸カリウム、過硫酸アン
モニウム等の水溶性重合開始剤があげられる。これらの
重合開始剤の使用量は塩化ビニル樹脂100重量部あた
り0.005〜1.0重量部とするのが好ましい。In carrying out the present invention, the graft copolymerization is advantageously carried out by a radical polymerization method, and as the radical polymerization initiator used for that purpose, lauroyl peroxide, tert-butyl peroxypivalate, diisopropyl peroxydiene is used. Organic peroxides such as carbonate and dioctyl peroxydicarbonate, 2,
Examples thereof include oil-soluble polymerization initiators of azo compounds such as 2'-azohisisobutyronitrile and 2,2'-azobis-2,4-dimethylvaleronitrile, and water-soluble polymerization initiators such as potassium persulfate and ammonium persulfate. To be The amount of these polymerization initiators used is preferably 0.005 to 1.0 part by weight per 100 parts by weight of the vinyl chloride resin.
分散剤としては、メチルセルローズ,エチルセルロー
ズ,ヒドロキシプロピルメチルセルローズヒドロキシメ
チルセルローズ,ポリビニルアルコール及びその部分ケ
ン化物,ゼラチン,ポリビニルピロリドン,デンプン等
の有機物あるいは炭酸マグネシウム,炭酸カルシウム,
燐酸カルシウム等の無機物が単独又は組み合せて使用さ
れ、その添加量は、塩化ビニル100重量部に対して0.
01〜1.0重量部である。Examples of the dispersant include methyl cellulose, ethyl cellulose, hydroxypropyl methyl cellulose, hydroxymethyl cellulose, polyvinyl alcohol and partially saponified products thereof, gelatin, polyvinylpyrrolidone, organic substances such as starch, magnesium carbonate, calcium carbonate,
Inorganic substances such as calcium phosphate are used alone or in combination, and the addition amount thereof is 0. 0 with respect to 100 parts by weight of vinyl chloride.
01-1.0 parts by weight.
さらに本発明は、ビニル単量体を重合する従来の方法に
おいて使用されている連鎖移動剤例えば2メルカプトエ
タノールを塩化ビニル樹脂100重量部に対して0.001
〜1.0重量部添加してもよい。Furthermore, the present invention provides a chain transfer agent, such as 2 mercaptoethanol, used in the conventional method for polymerizing vinyl monomers in an amount of 0.001 per 100 parts by weight of vinyl chloride resin.
~ 1.0 parts by weight may be added.
本発明の方法で得られるグラフト共重合塩化ビニル樹脂
は、従来の塩化ビニル樹脂の成型加工に使用される通常
の熱安定性,滑剤,加工助剤,酸化防止剤,充填剤,紫
外線吸収剤,顔料等を配合することにより、通常の成型
加工を行うことができ、耐衝撃性,耐候性,機械的強度
に優れた特性を生かして建材等に好適に使用される。The graft-copolymerized vinyl chloride resin obtained by the method of the present invention has the usual thermal stability, lubricants, processing aids, antioxidants, fillers, ultraviolet absorbers, used for molding conventional vinyl chloride resins, By adding a pigment or the like, it is possible to carry out a usual molding process, and it is suitably used for a building material or the like by taking advantage of the characteristics excellent in impact resistance, weather resistance and mechanical strength.
以下実施例によつて本発明を具体的に説明するが、実施
例中に示されている部は重量部である。Hereinafter, the present invention will be described in detail with reference to examples, but the parts shown in the examples are parts by weight.
実施例−1〜実施例−6 比較例−1〜−8 撹拌翼を装備した内容積7m3の重合機に、脱イオン水,
第1表に示す組成を有するアクリル系共重合体,分散
剤,重合開始剤等を装入し、内部の空気を真空ポンプで
除去した後、塩化ビニルを装入し、重合を行なつた。そ
の後塩化ビニルを除去し、内容物を瀘過乾燥し白色の粉
末を得た。この粉末の塩化ビニルの成分を測定した。得
られたグラフト共重合樹脂100部に三塩基性硫酸鉛2
部、二塩基性ステアリン酸鉛1部、ステアリン酸鉛1.5
部を均一に混合し、更に180℃の熱ロールで5分間混
練し、180℃で5分間プレスすることによりシートを
作成し、このシートから採取した試料についてシヤルピ
ー衝撃強度,耐候性,曲げ弾性率を下記により測定し
た。結果を第1表および第2表に示す。A polymerizer having an inner volume of 7m 3 equipped with Example 1 through Example -6 Comparative Example -1-8 stirring blades, deionized water,
An acrylic copolymer having the composition shown in Table 1, a dispersant, a polymerization initiator and the like were charged, the air inside was removed by a vacuum pump, and then vinyl chloride was charged to carry out polymerization. Then, vinyl chloride was removed, and the contents were filtered and dried to obtain a white powder. The vinyl chloride component of this powder was measured. Tribasic lead sulfate 2 was added to 100 parts of the obtained graft copolymer resin.
Parts, dibasic lead stearate 1 part, lead stearate 1.5
Parts were mixed uniformly, further kneaded with a hot roll at 180 ° C for 5 minutes, and pressed at 180 ° C for 5 minutes to prepare a sheet, and the samples taken from this sheet were subjected to sheary impact strength, weather resistance, and flexural modulus. Was measured as follows. The results are shown in Tables 1 and 2.
シヤルピー衝撃強:JIS K−6745 曲げ弾性率:JIS K−6740 耐候性:カーボンアークサンシヤインウエザロメーター
(スプレー12/60分,ブラツクパネル63℃)にて
200時間照射,変色比較。Shearpy impact strength: JIS K-6745 Bending elastic modulus: JIS K-6740 Weather resistance: Carbon arc sun shear in weather meter (spray 12/60 minutes, black panel 63 ° C) irradiation for 200 hours, comparison of discoloration.
比較例−9 実施例−1においてアクリル系樹脂の装入を行なわない
以外は、実施例−1と同様にして重合を行ない第2表に
示す結果を得た。このレジン100部にアクリル系耐衝
撃剤(組成n−ブチルアクリレート75%,メチルアク
リレート20%,アクリルニトリル5%)15部,三塩
基性硫酸鉛2部,2塩基性ステアリン酸鉛1部,ステア
リン酸鉛1.5部を均一に混合し、実施例−1と同様にし
てシートを作成し、物性を測定した。結果を第2表に示
す。Comparative Example-9 Polymerization was performed in the same manner as in Example-1 except that the acrylic resin was not charged in Example-1, and the results shown in Table 2 were obtained. To 100 parts of this resin, 15 parts of acrylic impact modifier (composition n-butyl acrylate 75%, methyl acrylate 20%, acrylonitrile 5%), tribasic lead sulfate 2 parts, dibasic lead stearate 1 part, stearin 1.5 parts of lead acid was uniformly mixed, a sheet was prepared in the same manner as in Example-1, and the physical properties were measured. The results are shown in Table 2.
以上の結果本発明のグラフト共重合による塩化ビニル樹
脂は、耐衝撃性,耐候性,機械的強度に極めて優れてい
ることが明らかである。From the above results, it is clear that the vinyl chloride resin by graft copolymerization of the present invention is extremely excellent in impact resistance, weather resistance and mechanical strength.
〔発明の効果〕 以上詳細に説明したように、本発明の方法によれば、耐
衝撃性・耐候性に優れ、かつ曲げ弾性率も向上した、物
性バランスのとれた塩化ビニル樹脂を得ることができ
る。 [Effects of the Invention] As described in detail above, according to the method of the present invention, it is possible to obtain a vinyl chloride resin having excellent physical properties and excellent impact resistance and weather resistance, and improved flexural modulus. it can.
Claims (1)
0℃以下であるアルキルアクリレートおよび/又はアル
キルメタクリレート60〜95重量%と、ホモポリマー
とした時の二次転移点が0℃以上で、α−メチルスチレ
ン、ビニルトルエン、不飽和ニトリル類、ビニルエーテ
ル類、アルキルアクリレート類、アルキルメタクリレー
ト類よりなる群より選ばれた少なくとも一つのモノマー
5〜39重量%と、多官能性モノマー1〜30重量%と
の共重合体1〜30重量部に塩化ビニル70〜99重量
部をグラフト共重合させることを特徴とする塩化ビニル
樹脂の製造方法。1. A homopolymer having a second-order transition point of -1.
Alkyl acrylate and / or alkyl methacrylate having a temperature of 0 ° C. or lower and 60 to 95% by weight and a secondary transition point of a homopolymer of 0 ° C. or higher, α-methylstyrene, vinyltoluene, unsaturated nitriles, vinyl ethers Copolymer of 5 to 39% by weight of at least one monomer selected from the group consisting of alkyl acrylates and alkyl methacrylates and 1 to 30% by weight of a polyfunctional monomer and 1 to 30 parts by weight of vinyl chloride and 70 to 50% of vinyl chloride. A method for producing a vinyl chloride resin, which comprises graft-copolymerizing 99 parts by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60175776A JPH0635498B2 (en) | 1985-08-12 | 1985-08-12 | Method for producing vinyl chloride resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60175776A JPH0635498B2 (en) | 1985-08-12 | 1985-08-12 | Method for producing vinyl chloride resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6236412A JPS6236412A (en) | 1987-02-17 |
JPH0635498B2 true JPH0635498B2 (en) | 1994-05-11 |
Family
ID=16002064
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60175776A Expired - Lifetime JPH0635498B2 (en) | 1985-08-12 | 1985-08-12 | Method for producing vinyl chloride resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0635498B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2910774B2 (en) * | 1989-12-28 | 1999-06-23 | 三井化学株式会社 | Method for producing vinyl chloride resin |
JP2002327103A (en) * | 2001-02-27 | 2002-11-15 | Sekisui Chem Co Ltd | Vinyl chloride resin |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IL47035A (en) * | 1974-07-01 | 1978-04-30 | Stauffer Chemical Co | Process for the preparation of interpolymer particles containing an acrylic elastomer and vinyl chloride |
JPS6035231A (en) * | 1983-08-05 | 1985-02-23 | Nippon Steel Corp | Method for measuring temperature distribution inside a substance |
-
1985
- 1985-08-12 JP JP60175776A patent/JPH0635498B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS6236412A (en) | 1987-02-17 |
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