JPH0315648B2 - - Google Patents
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- Publication number
- JPH0315648B2 JPH0315648B2 JP22777782A JP22777782A JPH0315648B2 JP H0315648 B2 JPH0315648 B2 JP H0315648B2 JP 22777782 A JP22777782 A JP 22777782A JP 22777782 A JP22777782 A JP 22777782A JP H0315648 B2 JPH0315648 B2 JP H0315648B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- polymer
- multilayer structure
- monomer
- 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
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- 229920000642 polymer Polymers 0.000 claims description 101
- 239000000178 monomer Substances 0.000 claims description 29
- 238000004519 manufacturing process Methods 0.000 claims description 18
- -1 Alkyl methacrylate Chemical compound 0.000 claims description 14
- 125000000217 alkyl group Chemical group 0.000 claims description 13
- 125000004432 carbon atom Chemical group C* 0.000 claims description 11
- 239000003795 chemical substances by application Substances 0.000 claims description 11
- 125000005250 alkyl acrylate group Chemical group 0.000 claims description 9
- 230000009477 glass transition Effects 0.000 claims description 9
- 230000000379 polymerizing effect Effects 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 238000006116 polymerization reaction Methods 0.000 description 19
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 18
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 17
- 238000006243 chemical reaction Methods 0.000 description 12
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 239000000203 mixture Substances 0.000 description 10
- 229920005989 resin Polymers 0.000 description 9
- 239000011347 resin Substances 0.000 description 9
- 230000008961 swelling Effects 0.000 description 8
- 230000007423 decrease Effects 0.000 description 7
- 238000003756 stirring Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 230000002087 whitening effect Effects 0.000 description 5
- 239000003995 emulsifying agent Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000002834 transmittance Methods 0.000 description 4
- BJELTSYBAHKXRW-UHFFFAOYSA-N 2,4,6-triallyloxy-1,3,5-triazine Chemical compound C=CCOC1=NC(OCC=C)=NC(OCC=C)=N1 BJELTSYBAHKXRW-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 3
- 210000000988 bone and bone Anatomy 0.000 description 3
- 150000002148 esters Chemical class 0.000 description 3
- 239000004816 latex Substances 0.000 description 3
- 229920000126 latex Polymers 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 239000011342 resin composition Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 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 2
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 description 2
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical compound COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical group C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- 239000003945 anionic surfactant Substances 0.000 description 2
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 238000010556 emulsion polymerization method Methods 0.000 description 2
- 238000007720 emulsion polymerization reaction Methods 0.000 description 2
- 125000005394 methallyl group Chemical group 0.000 description 2
- 229920002959 polymer blend Polymers 0.000 description 2
- FBCQUCJYYPMKRO-UHFFFAOYSA-N prop-2-enyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC=C FBCQUCJYYPMKRO-UHFFFAOYSA-N 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- WVAFEFUPWRPQSY-UHFFFAOYSA-N 1,2,3-tris(ethenyl)benzene Chemical compound C=CC1=CC=CC(C=C)=C1C=C WVAFEFUPWRPQSY-UHFFFAOYSA-N 0.000 description 1
- KOMNUTZXSVSERR-UHFFFAOYSA-N 1,3,5-tris(prop-2-enyl)-1,3,5-triazinane-2,4,6-trione Chemical compound C=CCN1C(=O)N(CC=C)C(=O)N(CC=C)C1=O KOMNUTZXSVSERR-UHFFFAOYSA-N 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
- JJBFVQSGPLGDNX-UHFFFAOYSA-N 2-(2-methylprop-2-enoyloxy)propyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC(C)COC(=O)C(C)=C JJBFVQSGPLGDNX-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
- AEPWOCLBLLCOGZ-UHFFFAOYSA-N 2-cyanoethyl prop-2-enoate Chemical compound C=CC(=O)OCCC#N AEPWOCLBLLCOGZ-UHFFFAOYSA-N 0.000 description 1
- XOJWAAUYNWGQAU-UHFFFAOYSA-N 4-(2-methylprop-2-enoyloxy)butyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCCCOC(=O)C(C)=C XOJWAAUYNWGQAU-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
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical class C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- GYCMBHHDWRMZGG-UHFFFAOYSA-N Methylacrylonitrile Chemical class CC(=C)C#N GYCMBHHDWRMZGG-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- RXPKAZWARAPDMU-UHFFFAOYSA-M [Na+].O=C.[O-]O.OSO.CC(C)C1=CC=CC=C1 Chemical compound [Na+].O=C.[O-]O.OSO.CC(C)C1=CC=CC=C1 RXPKAZWARAPDMU-UHFFFAOYSA-M 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 229920000800 acrylic rubber Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 125000000751 azo group Chemical group [*]N=N[*] 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 235000011148 calcium chloride Nutrition 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000012986 chain transfer agent Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 125000002573 ethenylidene group Chemical group [*]=C=C([H])[H] 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
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 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
- 238000001125 extrusion Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 125000003709 fluoroalkyl group Chemical group 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 description 1
- 125000000896 monocarboxylic acid group Chemical group 0.000 description 1
- KZCOBXFFBQJQHH-UHFFFAOYSA-N octane-1-thiol Chemical compound CCCCCCCCS KZCOBXFFBQJQHH-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
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pentâ4âenâ2âone Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920005668 polycarbonate resin Polymers 0.000 description 1
- 239000004431 polycarbonate resin Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920001447 polyvinyl benzene Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 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
- 239000012966 redox initiator Substances 0.000 description 1
- XWGJFPHUCFXLBL-UHFFFAOYSA-M rongalite Chemical compound [Na+].OCS([O-])=O XWGJFPHUCFXLBL-UHFFFAOYSA-M 0.000 description 1
- 238000005185 salting out Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 150000008054 sulfonate salts Chemical class 0.000 description 1
- 238000010558 suspension polymerization method Methods 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 239000006097 ultraviolet radiation absorber Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Graft Or Block Polymers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
ãçºæã®è©³çŽ°ãªèª¬æã
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å€å±€æ§é éåäœã®è£œé æ¹æ³ã«é¢ãããDETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a multilayer polymer, and more particularly, to a method for producing a multilayer polymer with excellent flexibility, transparency, and weather resistance.
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çšéã«ã¯çšããããšãåºæ¥ãªãã€ãã Acrylic resins, particularly methyl methacrylate polymers, are known as resins that have both excellent transparency and weather resistance, and are widely used in cast molded products, extrusion molded products, and the like. however,
Since these methyl methacrylate polymers are generally hard and brittle, they cannot be used in applications that require flexibility, such as films, coatings, or soft tubes.
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ã«å¯ãã ã¢ã¯ãªã«ç³»çŽ æã¯éçºã§ããªãã€ãã For this reason, attempts have been made to introduce certain rubber components into methyl methacrylate-based polymers in order to impart toughness and flexibility, but these efforts have resulted in significantly lower weather resistance and lower transparency. In many cases, the excellent characteristics of methyl methacrylate polymers have been sacrificed, such as a significant decrease in the properties of methyl methacrylate polymers.Moreover, they have not been able to provide enough flexibility and toughness to handle them as materials for films and sheets. However, it has not been possible to develop an acrylic material that is highly flexible and can be used in applications such as soft tubes that require even greater flexibility.
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ã®è£œé æ¹æ³ãæäŸããããšãç®çãšããã An object of the present invention is to eliminate the above-mentioned drawbacks and provide a method for producing an acrylic multilayer structure polymer having excellent flexibility, transparency, and weather resistance.
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ç¹åŸŽãšããå€å±€æ§é éåäœã®è£œé æ³ã§ããã The method for producing a multilayer structure polymer of the present invention includes: (A) 60 to 100 parts by weight of an alkyl acrylate (A 1 ) having an alkyl group having 8 or less carbon atoms; 0 to 40 parts by weight of a copolymerizable double bond; (A 2 ), 0 to 10 parts by weight of a polyfunctional monomer (A 3 ), and 100 parts by weight of the total amount of (A 1 ) to (A 3 ).
polymerizing 0.1 to 5 parts by weight of a graft cross-agent;
Form an innermost layer polymer (A) having a gel content of 60% by weight or more and a glass transition temperature of 0°C or less, and (B) having 60 to 100 parts by weight of an alkyl group having 4 or less carbon atoms. Alkyl methacrylate (B 1 ) and 0 to 40 parts by weight of a monomer having a copolymerizable double bond (B 2 ) are graft-polymerized to the innermost layer polymer (A), and the glass transition temperature is 60°C or higher. The proportion of the innermost layer polymer (A) in the thus obtained multilayer structure polymer is 51 to 90% by weight, and the outermost layer polymer (B) is This is a method for producing a multilayer structure polymer, characterized in that the proportion of B) is 10 to 49% by weight.
以äžãæ¬çºæãæŽã«è©³çŽ°ã«èª¬æããã The present invention will be explained in more detail below.
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ãã®æåã§ããã The innermost layer polymer (A) constituting the polymer produced by the production method of the present invention is a component for imparting flexibility to the polymer.
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ç¯å²ã§çšããããã Alkyl acrylate (A 1 ) having an alkyl group having 1 to 8 carbon atoms constituting the innermost layer polymer (A)
may be linear or branched, and methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, n-octyl acrylate, etc. are used alone or in combination, but the glass transition temperature ( Those with a low Tg (hereinafter abbreviated as Tg) are more preferable. These alkyl acrylates (A 1 )
is used in a range of 60 to 100 parts by weight (hereinafter, parts by weight are abbreviated as parts).
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ãªã«çã䜿çšå¯èœã§ããã Further, the monomer (A 2 ) having a copolymerizable double bond is preferably an acrylic monomer other than the above, such as alkyl acrylate, lower alkoxy acrylate, cyanoethyl acrylate, acrylamide, acrylic acid, or methacrylic acid. It is used in a range of 0 to 40 parts. As other (A 2 ) ingredients
Styrene, alkyl-substituted styrene, acrylonitrile, methacrylonitrile, etc. can be used within a range not exceeding 40% by weight.
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ãã Furthermore, the polyfunctional monomer (A 3 ) is preferably an alkylene glycol dimethacrylate such as ethylene glycol dimethacrylate, 1,3-butylene glycol dimethacrylate, 1,4-butylene glycol dimethacrylate, and propylene glycol dimethacrylate, and divinyl Polyvinylbenzenes such as benzene and trivinylbenzene and alkylene glycol diacrylates can also be used. These monomers work effectively to crosslink the layer in which they are contained, but do not work on bonding between layers with other layers. These polyfunctional monomers (A 3 ) can be used to form the polymer (A), provided that the gel content is 60% by weight or more depending on the polymerization conditions or the use of a grafting agent. , there is no need to use 10
It may be used as long as it is within this range. When the polyfunctional monomer (A 3 ) is used in an amount exceeding 10 parts, the flexibility of the polymer (A) decreases.
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ãã The grafting agent is an essential component for forming an effective chemical bond with the outermost resin layer or intermediate layer, and is present in an amount of 0.1 to 5 parts per 100 parts of the total amount of (A 1 ) to (A 3 ). It is preferably used within the range of 0.5 to 2 parts. If the amount of graft cross-agent used is less than 0.1 part, the amount of effective graft bonding will be too small, and layer destruction will easily occur during molding, resulting in a significant decrease in transparency, etc. On the other hand, if more than 5 parts is used, the elasticity decreases. As a grafting agent,
Copolymerizable α,β-unsaturated monocarboxylic acid or dicarboxylic acid allyl ester, methalyl ester, crotyl ester, triallyl cyanurate, triallyl isocyanurate, etc. are used, but allyl methacrylate and triallyl cyanurate are used. Particularly preferred. In such a graft cross-agent, the conjugated unsaturated bond of the ester reacts much faster than the allyl group, methallyl group, or crotyl group, and is chemically bonded. During this time, a substantial portion of the allyl group, methallyl group, or crotyl group effectively acts on the polymerization of the next layer polymer (B) and provides a graft bond between the two adjacent layers.
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ã30ã®å Žåã«ç¹ã«å¥œãŸããçµæãåŸãããã The innermost layer polymer A as described above needs to be an elastic body that has been crosslinked to some extent and has a glass transition temperature (Tg) of 0°C or less, and also has a gel content of
60% by weight or more, preferably 80% by weight, swelling degree 5
Particularly favorable results are obtained in the case of Ë30.
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é ã«ããããšãåºæ¥ãã The amount of the polymer (A) in the acrylic multilayer structure polymer is 51 to 90% by weight. If the amount is less than 51% by weight, the desired excellent flexibility cannot be imparted to the acrylic multilayer structure polymer. vice versa
If the amount exceeds 90% by weight, the entire polymer becomes rubbery and becomes difficult to handle, and various physical properties such as weather resistance are also significantly reduced. The innermost layer polymer (A) made of a crosslinked elastic body of acrylic rubber can also have a two-tiered structure or a three-tiered structure depending on the need.
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ãã The outermost layer polymer (B) constituting the acrylic multilayer structure polymer is essentially a resin layer, and it not only gives the polymer ease of handling as a resin, but also provides various properties such as weather resistance. It is the responsibility of
Therefore, the Tg of the outermost layer polymer (B) needs to be 60°C or higher, preferably 80°C or higher.
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ãŸããã The alkyl methacrylate (B 1 ) having an alkyl group having 4 or less carbon atoms forming the outermost layer polymer (B) includes at least one of methyl methacrylate, ethyl methacrylate, propyl methacrylate, butyl methacrylate, etc. in an amount of 60 to 100 parts. Methyl methacrylate is particularly preferred.
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åŸãããªãã Monomer with copolymerizable double bond (B 2 )
In addition to the alkyl acrylate having an alkyl group having 8 or less carbon atoms, those shown in the above component (A 2 ) are used in a range of 0 to 40 parts. The amount of the outermost layer polymer (B) in the acrylic multilayer structure polymer is 10 to 49% by weight. If the amount is less than 10%, a stable polymer cannot be obtained from the viewpoint of polymerization and coagulation operations. Moreover, if the amount exceeds 49%, the content of the innermost layer polymer (A) becomes too small to obtain the desired flexibility.
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ããããã奜ãŸããå Žåãå€ãã Incidentally, during the polymerization of the outermost layer polymer (B), it is also possible to adjust the degree of polymerization using a chain transfer agent or the like, and this is often preferable.
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ããããã The acrylic multilayer structure polymer produced in the present invention is the innermost layer polymer (A) and the outermost layer polymer (B).
is the basic structural unit, but if necessary, after forming the polymer (A) layer, between the polymer (B) layers, 10 to 90 parts of an alkyl group having 4 or less carbon atoms are added. Alkyl methacrylate (C 1 ) having 10 to 90 parts of an alkyl group having 8 or less carbon atoms (C 2 ), 0 to 20 parts of a monomer having a copolymerizable double bond (C 3 ), 0 to 10 parts of a polyfunctional monomer (C 4 ), and 0.1 to 5 parts of a grafting agent to 100 parts of the total amount of (C 1 ) to (C 4 ) to the innermost layer polymer (A ) can be graft-polymerized to form one or more intermediate layers. Here, each of the components (C 1 ) to (C 4 ) and the grafting agent are the same as those used in the polymer (A) and polymer (B).
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ååã«çºæ®ãããããã«ãªãã This intermediate layer is arranged to achieve more effective bonding between the innermost crosslinked elastic layer and the outermost resin layer, which not only further improves transparency but also increases flexibility. The characteristics of the crosslinked elastic layer and the resin layer, such as hardness and weather resistance, are fully exhibited as a whole.
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ãªãã The amount of the intermediate layer (C) in the acrylic multilayer structure polymer is suitably 5 to 30%, and if it exceeds 30%, it is not preferable because the overall balance of the polymer will be lost.
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ã©ããããŠããããšã奜ãŸããã Furthermore, each layer of the acrylic multilayer structure polymer produced in the present invention must be organically bonded, and the total amount of the outermost layer (B) and the middle layer (C), or the amount of the middle layer (C) If not, it is preferable that at least one third of the outermost layer (B) is grafted onto the innermost layer.
å°ãæ¬çºæã®è£œé æ³ã«ããéåäœã®åå±€ã®ã²ã«
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å€ãããã Note that the gel content and degree of swelling of each layer of the polymer produced by the production method of the present invention refer to values measured as follows.
JIS â6388ã«æºãåœè©²éåäœãæå®éæ¡å
ãã25âã§48æéã¡ãã«ãšãã«ã±ãã³ïŒMEKïŒ
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é€å»ããæéåŸã®çµ¶ä¹Ÿééãèªã¿ãšãã A predetermined amount of the polymer was collected according to JIS K-6388, and methyl ethyl ketone (MEK) was stored at 25°C for 48 hours.
immerse in it. After immersion, pull out the swollen sample, wipe off the adhered MEK, and measure its weight. Next, MEK is removed by drying in a vacuum dryer, and the absolute dry weight after constant weight is read.
èšç®ã¯æ¬¡åŒã«åŸãã The calculation follows the following formula.
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ããã Swelling degree = Weight after MEK swelling - Bone dry weight / Bone dry weight Gel content (%) = Bone dry weight / Weight of collected sample x
100 However, the gel content of the entire multilayer polymer is calculated by preparing a 1% by weight MEK solution of the polymer,
After standing overnight at â, use a centrifuge at 16000r.pm.
This refers to the weight percent of insoluble matter after centrifugation for 90 minutes.
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ãééåçãè¡šããã Further, the glass transition temperature (Tg) as used in the present invention is calculated from the commonly known FOX equation: 1/Tg=a 1 /Tg 1 +a 2 /Tg 2 . In the formula, a 1 and
a 2 each represents a weight fraction.
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æ¹æ³ã«ããå€å±€æ§é éåäœãåŸãããã The multilayer structure polymer produced by the production method of the present invention is usually obtained by a sequential multistage polymerization method using an emulsion polymerization method. When the intermediate layer (C) is multilayered, multistage polymerization may be carried out while gradually decreasing the amount of alkyl acrylate (C 2 ).
When carrying out a sequential multi-stage polymerization method using emulsion polymerization method, a predetermined amount of an emulsifier, a catalyst, a monomer, etc. are added to an aqueous solvent and reacted, and after each reaction, the monomers and monomers forming the upper layer are added. By sequentially adding a polymerization initiator to the reaction system, a multilayer structure polymer can be obtained by the production method of the present invention.
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ãšããŠãããããšãã§ããã There are no particular limitations on the emulsifier, catalyst, etc. used in the production of the multilayer structure polymer, and emulsifiers, catalysts, etc. used in ordinary emulsion polymerization can be used. As emulsifiers, long chain fatty acid salts, sulfonate salts, sulfosuccinic acid ester salts, phosphate ester salts,
Representative examples include anionic surfactants such as acid amide type anionic surfactants. Typical examples of catalysts include inorganic peroxides such as potassium persulfate, organic peroxides such as cumene hydroperoxide and lauroyl peroxide, and azo initiators such as azobisisobutyronitrile. Preferred examples include redox initiators such as cumene hydroperoxide-sodium formaldehyde sulfoxylate.
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éåã¯æ¯èŒç枩床ã®æ¹ã奜ãŸããå Žåãå€ãã The temperature conditions and polymerization time for the polymerization of the multilayer structure polymer depend on the catalyst used, etc., and any conditions are possible as long as the polymerization proceeds smoothly to the final stage. Usually 30â
Polymerization is carried out within the temperature range of ~95â, and the polymerization time is 3~
It is 20 hours. In many cases, the crosslinked elastic body portion of the polymer is polymerized at a relatively high temperature.
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åæ³ã«ãã€ãŠãåŸãããšãã§ããã Furthermore, the production method of the present invention is not particularly limited to the above-mentioned method; for example, it can also be obtained by an emulsion suspension polymerization method in which after emulsion polymerization, the outermost layer polymer is converted to suspension polymerization. can.
å°ãå€å±€æ§é éåäœã®æçµéåäœã«ããããšã
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800ã2000â«çšåºŠã®ç¯å²ãæã奜ãŸããã There is no particular restriction on the emulsion particle size in the final polymer of the multilayer structure polymer;
The most preferable range is about 800 to 2000 Ã
.
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ãã Multilayer polymer latex is processed by salting out by adding additives such as antioxidants, lubricants, coagulants, etc. as necessary, and then filtered, washed with water, dehydrated, and dried to form a powder. It is said to be a polymer with a shape.
å°ãæ¬çºæã®è£œé æ¹æ³ã«ããå€å±€æ§é éåäœ
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ãããªãã Incidentally, the multilayer structure polymer produced by the production method of the present invention can be easily molded into a molded article such as a tube by a conventional method. Furthermore, during molding, ultraviolet absorbers, pigments, etc. may be added as necessary.
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ã«ããå€å±€æ§é éåäœããåŸãããšãåºæ¥ãã The tubes obtained in this way are extremely flexible, have excellent weather resistance and transparency, and are free from the problem of plasticity oozing, which has been a problem with soft PVC, etc., which have traditionally been widely used as soft tubes. Therefore, it has extremely high commercial value. Furthermore, molded articles suitable for applications requiring flexibility and weather resistance, such as automobile moldings, can also be obtained from the multilayer structure polymer produced by the production method of the present invention.
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ãŠãå€å±€æ§é éåäœã補é ããããšãã§ããã Further, the multilayer structure polymer obtained by the production method of the present invention is mixed with 1 to 99% by weight of at least one thermoplastic resin selected from the following groups (a) and (b) to produce a multilayer structure polymer. You can also.
(a) 次åŒïŒ
ïŒåŒäžãåã³ïŒ¹ã¯åäžã§ãç°ãªã€ãŠããŠãã
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ãïŒClïŒBrïŒïŒŠïŒCH3ïŒCOOHïŒ
COOCH3ïŒCNïŒOCOCH3ïŒCOCH3ïŒC6H5ïŒ
SO3Håã¯OR1ãè¡šãããäœããR1ã¯äœçŽã¢ã«ã
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ïŒa2ïŒ CF2ïŒCFZ
ïŒåŒäžãã¯ïŒšïŒClïŒïŒŠåã¯CF3ãè¡šããïŒ
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ææ§ã«åªããæš¹èçµæç©ãšããããšãã§ããã(a) The following formula: (In the formula, X and Y may be the same or different, and each represents H, Cl, Br, F, CH 3 , COOH,
COOCH 3 , CN, OCOCH 3 , COCH 3 , C 6 H 5 ,
Represents SO 3 H or OR 1 . However, R 1 is a lower alkyl group) (a 2 ) CF 2 = CFZ (in the formula, Z represents H, Cl, F or CF 3 ) (In the formula, R 2 represents a fluoroalkyl group) Homopolymers of vinyl monomers or vinylidene monomers or copolymers of these monomers (b) Polycarbonates, thermoplastic polyesters, and polyamides Also, the production method of the present invention It has excellent transparency even when mixed with other thermoplastic resins that have different refractive indexes but are compatible.
A resin composition having no or very little stress whitening property can be obtained. In particular, when blended with a methyl methacrylate resin, a resin composition can be obtained that has excellent transparency, stress whitening resistance, weather resistance, and impact resistance.
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ãæ¹æ³ããã¯äºæž¬ãåŸãªããã®ã§ããã It is surprising that stress whitening properties are extremely low even in polymer blend systems. This is based on the effect of the special structure of the multilayer polymer, and cannot be predicted from conventional methods of introducing rubber components.
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ãªåäžãããããã To explain the polymer blend system in more detail, for example, when mixed with vinyl chloride resin, polystyrene, AS resin, or polycarbonate resin, the multilayer structure polymer produced by the production method of the present invention has a type of weather resistance and impact resistance. Acts as a modifier and significantly improves weather resistance and impact resistance.
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ã«ã æ圢çšçŽ æãšããŠãåªããŠãããéæã§åŒ·é
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åå䟡å€ã®é«ããã®ã§ããã In addition, blend compositions containing polyvinylidene fluoride have excellent properties such as weather resistance, transparency, stress whitening resistance, chemical resistance, toughness, and moldability. A resin composition comprising 50 to 99 parts of a multilayer structure polymer is also excellent as a material for film molding, and provides a transparent, tough film with excellent weather resistance, stress whitening resistance, chemical resistance, etc. Such a film can easily impart weather resistance and a design effect by laminating it on the surface of an ordinary molded article, and has extremely high commercial value.
以äžå®æœäŸã«ããæ¬çºæãå ·äœçã«èª¬æããã The present invention will be specifically explained below using Examples.
å®æœäŸäžã®éšæ°ã¯ãã¹ãŠééåºæºã§ããã All parts in the examples are by weight.
ãªãå®æœäŸäžã®ç¥èªã¯äžèšã®éãã§ããã In addition, the abbreviations in the examples are as follows.
MMA ã¡ãã«ã¡ã¿ã¯ãªã¬ãŒã
BuA ããã«ã¢ã¯ãªã¬ãŒã
AMA ã¢ãªã«ã¡ã¿ã¯ãªã¬ãŒã
TAC ããªã¢ãªã«ã·ã¢ãã¬ãŒã
CHP ã¯ã¡ã³ããããã«ãªãã·ã
SFS ãœãžãŠã ãã«ã ã¢ã«ãããã¹ã«ããã·ã¬
ãŒã
ïœâOSH ïœâãªã¯ãã«ã¡ã«ã«ãã¿ã³
BD ïŒïŒïŒâããã¬ã³ã°ãªã³ãŒã«ãžã¡ã¿ã¯ãª
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éšãä»èŸŒã¿ãçªçŽ æ°æµäžã§æ¹æåŸã65éšã®BuAã
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å±€ã®ã¬ã©ã¹è»¢ç§»æž©åºŠïŒTgïŒã¯â40âã§ãã€ãã MMA Methyl methacrylate BuA Butyl acrylate AMA Allyl methacrylate TAC Triallyl cyanurate CHP Cumene hydroperoxide SFS Sodium formaldehyde sulfoxylate n-OSH n-Octyl mercaptan BD 1,3-Butylene glycol dimethacrylate Example 1 Inside a reaction vessel with a condenser 250 parts of ion exchange water,
Sulfosuccinic acid ester soda salt 1.5 parts, SFS0.05
After stirring under a nitrogen stream, 65 parts of BuA,
I prepared 0.65 copies of AMA. 0.1% CHP was dissolved in BuA. Furthermore, for all monomers added in subsequent steps, 0.1% of each monomer is added unless otherwise specified.
Contains CHP. Next, under a nitrogen stream,
The temperature was raised to 50°C while stirring at a rotation speed of 200 rpm.
The mixture was stirred for 180 minutes to complete polymerization of the innermost layer polymer (A). The polymerization rate was 97% or more. The resulting innermost layer polymer (A) had a particle diameter of approximately 0.1 Ό, a gel content of 92.5% by weight, and a degree of swelling of 7.5. Also, (A)
The glass transition temperature (Tg) of the layer was -40°C.
次ã«éå枩床ã75âã«ææž©ããå°éã®æ°Žã«ãšã
ãã0.05éšã®SFSãæ·»å ããã®ã¡ãïŒéšã®MMAã
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å±€ïŒïŒ£ïŒã®éåãè¡ãªã€ãã Next, the polymerization temperature was raised to 75â, and after adding 0.05 parts of SFS dissolved in a small amount of water, 5 parts of MMA,
A mixture of 5 parts of BuA and 0.05 parts of AMA was added dropwise to the reaction system over 30 minutes, and the mixture was maintained for an additional 60 minutes to polymerize the intermediate layer (C).
æŽã«åŒãã€ã¥ãã25éšã®MMAåã³0.025éšã®
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ããïŒïŒ¢ïŒå±€ã®Tgã¯100âã§ãã€ãã Subsequently, a mixture consisting of 25 parts of MMA and 0.025 parts of n-OSH was added dropwise to the reaction system over a period of 60 minutes, and the reaction system was maintained at that temperature with stirring for an additional 60 minutes to form the outermost layer polymer (B). ) was completed. The Tg of layer (B) was 100°C.
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也ç²ãåŸãã The obtained latex was salted out using 5 parts of CaCl2 , coagulated and solidified, filtered, washed with water, and dried to obtain a dry powder.
åŸãããå€å±€æ§é éåäœã®ã²ã«å«æéã¯80ïŒ
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ãã€ãã The gel content of the obtained multilayer polymer was 80%.
å€å±€æ§é éåäœã®ä¹Ÿç²100éééšã«å¯ŸããŠ1.5éš
ã®çŽ«å€ç·åžåå€ãæ·»å æ··åããçŽåŸ40mmã®ã¹ã¯ãª
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ããåæããŠãã¬ãããšããã 1.5 parts of an ultraviolet absorber was added to 100 parts by weight of the dry powder of the multilayer structure polymer, and the mixture was extruded at 200°C using an extruder with a screw of 40 mm in diameter, and the pellets were cut into pellets.
åŸããããã¬ãããååã«ä¹Ÿç¥ããã®ã¡ãå°åº
æåæ©ãçšããŠïŒmmåã®å¹³æ¿ãæåããã After the obtained pellets were sufficiently dried, they were molded into a 2 mm thick flat plate using an injection molding machine.
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2.5ã§ãããéææ§ã¯æ¥µããŠè¯å¥œã§ãã€ãã The total light transmittance of the obtained flat plate was 91%, and the haze value was
2.5, and the transparency was extremely good.
åããã®æš¹èæ¿ã®ã·ãšã¢ïŒ€ç¡¬åºŠã¯42ãæ²ã匟æ§
ç2000KgïŒcm2ã§ãã€ãã Further, the shore D hardness of this resin plate was 42, and the flexural modulus was 2000 Kg/cm 2 .
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ãšã»ãšãã©äœäžããŠããªãã€ãã Furthermore, this plate was subjected to a 2000-hour accelerated exposure test using a Sunshine Weather-Ometer.
Even after the test, no coloring was observed, and the total light transmittance was also low.
There was almost no decline at 86%.
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å«ããã®ãšãããExample 2 250 parts of ion-exchanged water was placed in a reaction vessel equipped with a condenser.
Sulfosuccinic acid ester soda salt 1.5 parts, SFS0.05
After stirring under a nitrogen stream and replacing the inside of the container with nitrogen, add 70 parts of BuA and 0.35 parts of BuA.
A monomer mixture consisting of 0.1% CHP to TAC and BuA was charged. It should be noted that all monomers added in the subsequent steps also contain 0.1% CHP, unless otherwise specified.
次ãã§åå¿å®¹åšãçªçŽ æ°æµäžã«200rpmã®å転
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ãèšæœ€åºŠã¯19ã§ãã€ãã Next, the temperature of the reaction vessel was raised to 50° C. under a nitrogen stream while stirring at a rotation speed of 200 rpm, and polymerization was continued while stirring for 180 minutes to complete polymerization of the innermost layer polymer (A). The resulting innermost layer polymer (A) had a particle size of about 0.13ÎŒ, a Tg of -40°C, and a gel content of
The content was 89% by weight, and the degree of swelling was 19.
次ãã§åå¿ç³»ã80âã«ææž©ããå°éã®æ°Žã«ãšã
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ãããã Next, the reaction system was heated to 80°C, and 0.05 parts of SFS dissolved in a small amount of water was added, followed by 5 parts of MMA,
A monomer mixture consisting of 5 parts BuA and 0.05 parts TAC was added dropwise to the reaction system over a period of 30 minutes.
The intermediate layer (C) was polymerized by maintaining the temperature at 80° C. while stirring for a minute. Next, 20 parts of MMA was added dropwise to the reaction system over 60 minutes, and the reaction system was maintained at that temperature for an additional 60 minutes to complete polymerization of the outermost layer polymer (B).
åŸãããã©ããã¯ã¹ãïŒéšã®CaCl2ãçšããŠå¡©
æããåéã»åºåããã®ã¡ãéïŒæ°ŽæŽïŒä¹Ÿç¥ã
ãŠä¹Ÿç²ãåŸããåŸãããå€å±€æ§é éåäœã®Tgã¯
100âãã²ã«å«æéã¯85ïŒ
ã§ãã€ãã The obtained latex was salted out using 5 parts of CaCl 2 to coagulate and solidify, and then filtered, washed with water, and dried to obtain a dry powder. The Tg of the obtained multilayer structure polymer is
At 100°C, the gel content was 85%.
å®æœäŸ ïŒ
å®æœäŸïŒãšåæ§ã«ããŠã50éšã®BuAãïŒéšã®
MMAãïŒéšã®BDåã³0.275éšã®AMAãããªã
æå
å±€ã7.5éšã®BuAã7.5éšã®MMAåã³0.1éšã®
AMAãããªãäžéå±€åã³27éšã®MMAãïŒéšã®
BuAã0.03éšã®ïœâOSHãããªãæå€å±€ãæã
ãå€å±€æ§é éåäœãéåããã該éåäœã®æå
å±€
ïŒïŒ¡ïŒã®Tgã¯â25âãã²ã«å«æéã¯95ééïŒ
ãèš
最床ã¯ïŒã§ããããŸãæå€å±€ïŒïŒ¢ïŒã®Tgã¯80â
ã§ãã€ãŠã該éåäœå
šäœã®ã²ã«å«æéã¯75ééïŒ
ã§ãã€ããExample 3 In the same manner as in Example 1, 50 parts of BuA, 3 parts of
Innermost layer consisting of MMA, 2 parts BD and 0.275 parts AMA, 7.5 parts BuA, 7.5 parts MMA and 0.1 parts
Intermediate layer consisting of AMA and 27 divisions of MMA, 3 divisions of
A multilayered polymer was polymerized with the outermost layer consisting of BuA and 0.03 parts of n-OSH. The Tg of the innermost layer (A) of the polymer is -25°C, the gel content is 95% by weight, and the degree of swelling is 6, and the Tg of the outermost layer (B) is 80°C.
and the gel content of the entire polymer is 75% by weight
It was hot.
å€å±€æ§é éåäœãçšãå®æœäŸïŒãšåæ§ã«å¹³æ¿ã
æ圢ãè©äŸ¡ããããã®å¹³æ¿ã®å
šå
ç·ééçã¯93
ïŒ
ãæ䟡ã¯2.0ã§ãããã·ãšã¢ïŒ€ç¡¬åºŠã¯47ã§ãã€
ããåãã®å¹³æ¿ã¯ããµã³ã·ã€ã€ã³ãŠãšã¶ãªã¡ãŒã¿
ãŒã«ãã2000æéã®å éæé²è©ŠéšåŸãå€è²åã³é
ææ§ã®äœäžãããããŠããããèåæ§ã«ãããã
ããã®ã§ãã€ãã A flat plate was molded using the multilayer structure polymer in the same manner as in Example 1 and evaluated. The total light transmittance of this flat plate is 93
%, haze value was 2.0, and shore D hardness was 47. Furthermore, this flat plate showed no discoloration or decrease in transparency even after a 2000 hour accelerated exposure test using a Sunshine Weather-Ometer, and had excellent weather resistance.
æŽã«å€å±€æ§é éåäœãçšããŠãã€ã³ãã¬ãŒã·ãš
ã³æ³ã«ããã190âã§åã¿50ÎŒã®ãã€ã«ã ãæè
ããããã®ãã€ã«ã ã¯æ¥µããŠæè»ã§ããã€éææ§
ã«ãããããæè»æ§ãèŠæ±ãããçšéã§ã®ãªãŒã
ãŒã¬ã€ãã€ã«ã ãšããŠæé©ãªãã®ã§ãã€ãã Furthermore, using the multilayer structure polymer, a film with a thickness of 50 ÎŒm was formed at 190° C. by an inflation method. This film was extremely flexible and had excellent transparency, making it ideal as an overlay film for applications requiring flexibility.
å®æœäŸ ïŒ
å®æœäŸïŒãšåæ§ã«ããŠäžèšã®åŠãçµæã®äºå±€æ§
é éåäœã補é ãããExample 4 A two-layer structure polymer having the following composition was produced in the same manner as in Example 1.
æå
å±€ïŒïŒ¡ïŒïŒBuA 70éšïŒTAC 0.525éš
æå€å±€ïŒïŒ¢ïŒïŒMMA 27éšïŒBuA ïŒéšïŒïœâ
OSH 0.03éš
該éåäœã®æå
å±€ïŒïŒ¡ïŒã®ç²ååŸã¯çŽ0.12ÎŒã
ã²ã«å«æéã¯90ééïŒ
ãèšæœ€åºŠã¯23ã§ãã€ããå
æå€å±€ïŒïŒ¢ïŒã®TgïŒèšç®å€ïŒã¯çŽ80âã§ãããæ
çµéåäœã®ã²ã«å«æéã¯83ïŒ
ã§ãã€ãã Innermost layer (A); BuA 70 parts, TAC 0.525 parts Outermost layer (B); MMA 27 parts, BuA 3 parts, n-
OSH 0.03 part The particle size of the innermost layer (A) of the polymer is approximately 0.12Ό,
The gel content was 90% by weight and the degree of swelling was 23. The Tg (calculated value) of the outermost layer (B) was about 80°C, and the gel content of the final polymer was 83%.
ãã®å€å±€æ§é éåäœãçšããå®æœäŸïŒãšåæ§ã«
å¹³æ¿ã«æ圢ãè©äŸ¡ãããåŸãããå¹³æ¿ã®å
šå
ç·é
éçã¯87ïŒ
ãæ䟡ã¯3.5ã§ããããŸãæ²ã匟æ§ç
ã¯2000KgïŒcm2ãã·ãšã¢ïŒ€ç¡¬åºŠã¯41ã§ãã€ãã Using this multilayer structure polymer, it was molded into a flat plate and evaluated in the same manner as in Example 1. The obtained flat plate had a total light transmittance of 87%, a haze value of 3.5, a flexural modulus of 2000 Kg/cm 2 and a Shore D hardness of 41.
æŽã«ãµã³ã·ã€ã€ã³ãŠãšã¶ãªã¡ãŒã¿ãŒã«ãã2000
æéã®å éæé²è©ŠéšåŸãçè²ãéææ§ã®å€§å·Ÿãªäœ
äžã¯èªããããªãã€ãã Furthermore, 2000 by Sunshine Weather Ometer
Even after the accelerated exposure test, no significant decrease in coloration or transparency was observed.
Claims (1)
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ãåéäœïŒA2ïŒã ïŒã10éééšã®å€å®èœæ§åéäœïŒA3ïŒã åã³ ïŒA1ïŒãïŒA3ïŒã®åèšé100éééšã«å¯Ÿã
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ãã (B) 次ã«ã60ã100éééšã®ççŽ æ°ïŒä»¥äžã®ã¢ã«
ãã«åºãæããã¢ã«ãã«ã¡ã¿ã¯ãªã¬ãŒã
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ïŒïŒ¢ïŒã圢æããã ãããŠãã®ããã«ããŠåŸãããå€å±€æ§é éåäœ
äžã«å ããæå å±€éåäœïŒïŒ¡ïŒã®å²åã51ã90é
éïŒ ã§ãããæå€å±€éåäœïŒïŒ¢ïŒã®å²åã10ã49
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ãåéäœïŒC3ïŒã ïŒã10ééã®å€å®èœæ§åéäœïŒC4ïŒãåã³ ïŒC1ïŒãïŒC4ïŒã®åèšé100éééšã«å¯Ÿã0.1
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ãã«åºãæããã¢ã«ãã«ã¡ã¿ã¯ãªã¬ãŒã
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äžã«å ããæå å±€éåäœïŒïŒ¡ïŒã®å²åã51ã85é
éïŒ ã§ãããäžéå±€ïŒïŒ£ïŒã®å²åãïŒã30ééïŒ
ã§ãããæå€å±€éåäœïŒïŒ¢ïŒã®å²åã10ã44éé
ïŒ ã§ããããšãç¹åŸŽãšããå€å±€æ§é éåäœã®è£œé
æ¹æ³ã[Scope of Claims] 1 (A) 60 to 100 parts by weight of an alkyl acrylate (A 1 ) having an alkyl group having 8 or less carbon atoms, and 0 to 40 parts by weight of a monomer having a copolymerizable double bond. (A 2 ), 0 to 10 parts by weight of polyfunctional monomer (A 3 ), and 100 parts by weight of the total amount of (A 1 ) to (A 3 )
polymerizing 0.1 to 5 parts by weight of a graft cross-agent;
Form an innermost layer polymer (A) having a gel content of 60% by weight or more and a glass transition temperature of 0°C or less, and (B) having 60 to 100 parts by weight of an alkyl group having 4 or less carbon atoms. Alkyl methacrylate (B 1 ) and 0 to 40 parts by weight of a monomer having a copolymerizable double bond (B 2 ) are graft-polymerized to the innermost layer polymer (A), and the glass transition temperature is 60°C or higher. The proportion of the innermost layer polymer (A) in the thus obtained multilayer structure polymer is 51 to 90% by weight, and the outermost layer polymer ( B) ratio is 10-49
A method for producing a multilayer polymer characterized by the following: 2 (A) 60 to 100 parts by weight of an alkyl acrylate (A 1 ) having an alkyl group having 8 or less carbon atoms, 0 to 40 parts by weight of a monomer (A 2 ) having a copolymerizable double bond, 0 ~10 parts by weight of polyfunctional monomer (A 3 ) and 100 parts by weight of the total amount of (A 1 ) to (A 3 )
polymerizing 0.1 to 5 parts by weight of a graft cross-agent;
forming an innermost layer polymer (A) having a gel content of 60% by weight or more and a glass transition temperature of 0°C or less; Alkyl methacrylate (C 1 ), 10 to 90 parts by weight of alkyl acrylate (C 2 ) having an alkyl group having 8 or less carbon atoms, 0 to 20 parts by weight of a monomer having a copolymerizable double bond (C 3 ), 0 to 10 parts by weight of polyfunctional monomer (C 4 ), and 0.1 parts by weight per 100 parts by weight of the total amount of (C 1 ) to (C 4 ).
~5 parts by weight of a graft cross-agent is graft-polymerized to the innermost layer polymer (A) to form at least one intermediate layer (C), and (B) 60 to 100 parts by weight of a carbon number of 4 or less An alkyl methacrylate (B 1 ) having an alkyl group of The outermost layer polymer (B) having a temperature of 60°C or higher is formed, and the proportion of the innermost layer polymer (A) in the multilayer structure polymer thus obtained is 51 to 85% by weight, and the middle layer is The proportion of (C) is 5 to 30% by weight
A method for producing a multilayer structure polymer, characterized in that the proportion of the outermost layer polymer (B) is 10 to 44% by weight.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22777782A JPS59122513A (en) | 1982-12-28 | 1982-12-28 | Polymer having multi-layered structure |
JP20520090A JPH03163153A (en) | 1982-12-28 | 1990-08-03 | Multilayered polymer resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22777782A JPS59122513A (en) | 1982-12-28 | 1982-12-28 | Polymer having multi-layered structure |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20520090A Division JPH03163153A (en) | 1982-12-28 | 1990-08-03 | Multilayered polymer resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59122513A JPS59122513A (en) | 1984-07-16 |
JPH0315648B2 true JPH0315648B2 (en) | 1991-03-01 |
Family
ID=16866215
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22777782A Granted JPS59122513A (en) | 1982-12-28 | 1982-12-28 | Polymer having multi-layered structure |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59122513A (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59152856A (en) * | 1983-02-21 | 1984-08-31 | äžè±ã¬ã€ãšã³æ ªåŒäŒç€Ÿ | Multilayer structure polymer |
US4916171A (en) * | 1984-07-25 | 1990-04-10 | Rohm And Haas Company | Polymers comprising alkali-insoluble core/alkali-soluble shell and copositions thereof |
CA1332992C (en) * | 1986-08-27 | 1994-11-08 | Susan Marie Liwak | Impact-strength modifiers for thermoplastic polymers |
FR2610328B1 (en) * | 1987-01-30 | 1989-08-25 | Charbonnages Ste Chimique | INTERPOLYMER STRENGTHENING MATERIAL OF RIGID THERMOPLASTIC MATRICES, PREPARATION THEREOF AND CORRESPONDING REINFORCED COMPOSITIONS |
FR2610327B1 (en) * | 1987-01-30 | 1989-08-25 | Charbonnages Ste Chimique | MULTI-LAYER COMPOSITE INTERPOLYMER, PREPARATION METHOD THEREOF, APPLICATION TO REINFORCEMENT OF RIGID THERMOPLASTIC MATRICES AND REINFORCED COMPOSITIONS THEREOF |
JP2004339350A (en) * | 2003-05-15 | 2004-12-02 | Mitsubishi Rayon Co Ltd | Acrylic soft resin, acrylic soft resin composition and manufacturing process of the composition |
KR100548626B1 (en) * | 2003-10-29 | 2006-01-31 | 죌ìíì¬ ìì§íí | Rubber Latex and Manufacturing Method thereof |
CN103703076A (en) * | 2011-05-31 | 2014-04-02 | äžè±äžœé³æ ªåŒäŒç€Ÿ | Acrylic resin composition, molded object thereof, process for producing film, and acrylic resin film |
EP3774956A1 (en) * | 2018-03-29 | 2021-02-17 | Rohm and Haas Company | Three-stage polymer particle |
WO2019190703A1 (en) * | 2018-03-29 | 2019-10-03 | Rohm And Haas Company | Modified styrene-acrylonitrile |
-
1982
- 1982-12-28 JP JP22777782A patent/JPS59122513A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS59122513A (en) | 1984-07-16 |
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