JP3964235B2 - Acrylic resin plate manufacturing method - Google Patents
Acrylic resin plate manufacturing method Download PDFInfo
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- JP3964235B2 JP3964235B2 JP2002076133A JP2002076133A JP3964235B2 JP 3964235 B2 JP3964235 B2 JP 3964235B2 JP 2002076133 A JP2002076133 A JP 2002076133A JP 2002076133 A JP2002076133 A JP 2002076133A JP 3964235 B2 JP3964235 B2 JP 3964235B2
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- Prior art keywords
- polymerization
- acrylic resin
- resin plate
- plate
- mass
- 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 - Fee Related
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- 239000004925 Acrylic resin Substances 0.000 title claims description 67
- 229920000178 Acrylic resin Polymers 0.000 title claims description 67
- 238000004519 manufacturing process Methods 0.000 title claims description 16
- 238000006116 polymerization reaction Methods 0.000 claims description 102
- 229920000642 polymer Polymers 0.000 claims description 32
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 29
- 239000002994 raw material Substances 0.000 claims description 25
- -1 acrylic ester Chemical class 0.000 claims description 22
- 238000006243 chemical reaction Methods 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 20
- 239000011347 resin Substances 0.000 claims description 18
- 229920005989 resin Polymers 0.000 claims description 18
- 230000003287 optical effect Effects 0.000 claims description 13
- 230000000379 polymerizing effect Effects 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000012986 chain transfer agent Substances 0.000 claims 1
- 125000002298 terpene group Chemical group 0.000 claims 1
- 230000005540 biological transmission Effects 0.000 description 23
- 239000000463 material Substances 0.000 description 16
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 13
- 239000000203 mixture Substances 0.000 description 13
- 239000000178 monomer Substances 0.000 description 13
- 239000003505 polymerization initiator Substances 0.000 description 9
- 230000007547 defect Effects 0.000 description 7
- 239000006188 syrup Substances 0.000 description 7
- 235000020357 syrup Nutrition 0.000 description 7
- 210000004027 cell Anatomy 0.000 description 6
- 239000004973 liquid crystal related substance Substances 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000000654 additive Substances 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 230000031700 light absorption Effects 0.000 description 5
- 238000005259 measurement Methods 0.000 description 5
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 4
- MOYAFQVGZZPNRA-UHFFFAOYSA-N Terpinolene Chemical compound CC(C)=C1CCC(C)=CC1 MOYAFQVGZZPNRA-UHFFFAOYSA-N 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000005187 foaming Methods 0.000 description 4
- 238000001746 injection moulding Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- NOBYOEQUFMGXBP-UHFFFAOYSA-N (4-tert-butylcyclohexyl) (4-tert-butylcyclohexyl)oxycarbonyloxy carbonate Chemical compound C1CC(C(C)(C)C)CCC1OC(=O)OOC(=O)OC1CCC(C(C)(C)C)CC1 NOBYOEQUFMGXBP-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical class CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 3
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- GRWFGVWFFZKLTI-IUCAKERBSA-N (-)-α-pinene Chemical compound CC1=CC[C@@H]2C(C)(C)[C@H]1C2 GRWFGVWFFZKLTI-IUCAKERBSA-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
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 238000000149 argon plasma sintering Methods 0.000 description 2
- UAHWPYUMFXYFJY-UHFFFAOYSA-N beta-myrcene Chemical compound CC(C)=CCCC(=C)C=C UAHWPYUMFXYFJY-UHFFFAOYSA-N 0.000 description 2
- WQAQPCDUOCURKW-UHFFFAOYSA-N butanethiol Chemical compound CCCCS WQAQPCDUOCURKW-UHFFFAOYSA-N 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- XMGQYMWWDOXHJM-UHFFFAOYSA-N limonene Chemical compound CC(=C)C1CCC(C)=CC1 XMGQYMWWDOXHJM-UHFFFAOYSA-N 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 239000013307 optical fiber Substances 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 2
- 239000004926 polymethyl methacrylate Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- YHQGMYUVUMAZJR-UHFFFAOYSA-N α-terpinene Chemical compound CC(C)C1=CC=C(C)CC1 YHQGMYUVUMAZJR-UHFFFAOYSA-N 0.000 description 2
- YKFLAYDHMOASIY-UHFFFAOYSA-N γ-terpinene Chemical compound CC(C)C1=CCC(C)=CC1 YKFLAYDHMOASIY-UHFFFAOYSA-N 0.000 description 2
- WTARULDDTDQWMU-RKDXNWHRSA-N (+)-β-pinene Chemical compound C1[C@H]2C(C)(C)[C@@H]1CCC2=C WTARULDDTDQWMU-RKDXNWHRSA-N 0.000 description 1
- WTARULDDTDQWMU-IUCAKERBSA-N (-)-Nopinene Natural products C1[C@@H]2C(C)(C)[C@H]1CCC2=C WTARULDDTDQWMU-IUCAKERBSA-N 0.000 description 1
- FVQMJJQUGGVLEP-UHFFFAOYSA-N (2-methylpropan-2-yl)oxy 2-ethylhexaneperoxoate Chemical compound CCCCC(CC)C(=O)OOOC(C)(C)C FVQMJJQUGGVLEP-UHFFFAOYSA-N 0.000 description 1
- KDGNCLDCOVTOCS-UHFFFAOYSA-N (2-methylpropan-2-yl)oxy propan-2-yl carbonate Chemical compound CC(C)OC(=O)OOC(C)(C)C KDGNCLDCOVTOCS-UHFFFAOYSA-N 0.000 description 1
- UICXTANXZJJIBC-UHFFFAOYSA-N 1-(1-hydroperoxycyclohexyl)peroxycyclohexan-1-ol Chemical compound C1CCCCC1(O)OOC1(OO)CCCCC1 UICXTANXZJJIBC-UHFFFAOYSA-N 0.000 description 1
- AYMDJPGTQFHDSA-UHFFFAOYSA-N 1-(2-ethenoxyethoxy)-2-ethoxyethane Chemical compound CCOCCOCCOC=C AYMDJPGTQFHDSA-UHFFFAOYSA-N 0.000 description 1
- CRJIYMRJTJWVLU-UHFFFAOYSA-N 2,4,4-trimethylpentan-2-yl 3-(5,5-dimethylhexyl)dioxirane-3-carboxylate Chemical compound CC(C)(C)CCCCC1(C(=O)OC(C)(C)CC(C)(C)C)OO1 CRJIYMRJTJWVLU-UHFFFAOYSA-N 0.000 description 1
- DMWVYCCGCQPJEA-UHFFFAOYSA-N 2,5-bis(tert-butylperoxy)-2,5-dimethylhexane Chemical compound CC(C)(C)OOC(C)(C)CCC(C)(C)OOC(C)(C)C DMWVYCCGCQPJEA-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
- GOXQRTZXKQZDDN-UHFFFAOYSA-N 2-Ethylhexyl acrylate Chemical compound CCCCC(CC)COC(=O)C=C GOXQRTZXKQZDDN-UHFFFAOYSA-N 0.000 description 1
- PFHOSZAOXCYAGJ-UHFFFAOYSA-N 2-[(2-cyano-4-methoxy-4-methylpentan-2-yl)diazenyl]-4-methoxy-2,4-dimethylpentanenitrile Chemical compound COC(C)(C)CC(C)(C#N)N=NC(C)(C#N)CC(C)(C)OC PFHOSZAOXCYAGJ-UHFFFAOYSA-N 0.000 description 1
- WYGWHHGCAGTUCH-UHFFFAOYSA-N 2-[(2-cyano-4-methylpentan-2-yl)diazenyl]-2,4-dimethylpentanenitrile Chemical compound CC(C)CC(C)(C#N)N=NC(C)(C#N)CC(C)C WYGWHHGCAGTUCH-UHFFFAOYSA-N 0.000 description 1
- WFUGQJXVXHBTEM-UHFFFAOYSA-N 2-hydroperoxy-2-(2-hydroperoxybutan-2-ylperoxy)butane Chemical compound CCC(C)(OO)OOC(C)(CC)OO WFUGQJXVXHBTEM-UHFFFAOYSA-N 0.000 description 1
- 125000000954 2-hydroxyethyl group Chemical group [H]C([*])([H])C([H])([H])O[H] 0.000 description 1
- RTEZVHMDMFEURJ-UHFFFAOYSA-N 2-methylpentan-2-yl 2,2-dimethylpropaneperoxoate Chemical compound CCCC(C)(C)OOC(=O)C(C)(C)C RTEZVHMDMFEURJ-UHFFFAOYSA-N 0.000 description 1
- RPBWMJBZQXCSFW-UHFFFAOYSA-N 2-methylpropanoyl 2-methylpropaneperoxoate Chemical compound CC(C)C(=O)OOC(=O)C(C)C RPBWMJBZQXCSFW-UHFFFAOYSA-N 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 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
- WSTYNZDAOAEEKG-UHFFFAOYSA-N Mayol Natural products CC1=C(O)C(=O)C=C2C(CCC3(C4CC(C(CC4(CCC33C)C)=O)C)C)(C)C3=CC=C21 WSTYNZDAOAEEKG-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical class SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 1
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 1
- WTARULDDTDQWMU-UHFFFAOYSA-N Pseudopinene Natural products C1C2C(C)(C)C1CCC2=C WTARULDDTDQWMU-UHFFFAOYSA-N 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- XCPQUQHBVVXMRQ-UHFFFAOYSA-N alpha-Fenchene Natural products C1CC2C(=C)CC1C2(C)C XCPQUQHBVVXMRQ-UHFFFAOYSA-N 0.000 description 1
- VYBREYKSZAROCT-UHFFFAOYSA-N alpha-myrcene Natural products CC(=C)CCCC(=C)C=C VYBREYKSZAROCT-UHFFFAOYSA-N 0.000 description 1
- MVNCAPSFBDBCGF-UHFFFAOYSA-N alpha-pinene Natural products CC1=CCC23C1CC2C3(C)C MVNCAPSFBDBCGF-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 239000007869 azo polymerization initiator Substances 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 description 1
- 229930006722 beta-pinene Natural products 0.000 description 1
- 229930006974 beta-terpinene Natural products 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 210000002858 crystal cell Anatomy 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 239000012933 diacyl peroxide Substances 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- LCWMKIHBLJLORW-UHFFFAOYSA-N gamma-carene Natural products C1CC(=C)CC2C(C)(C)C21 LCWMKIHBLJLORW-UHFFFAOYSA-N 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229940087305 limonene Drugs 0.000 description 1
- 235000001510 limonene Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- KZCOBXFFBQJQHH-UHFFFAOYSA-N octane-1-thiol Chemical compound CCCCCCCCS KZCOBXFFBQJQHH-UHFFFAOYSA-N 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
- 150000004978 peroxycarbonates Chemical class 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- BWJUFXUULUEGMA-UHFFFAOYSA-N propan-2-yl propan-2-yloxycarbonyloxy carbonate Chemical compound CC(C)OC(=O)OOC(=O)OC(C)C BWJUFXUULUEGMA-UHFFFAOYSA-N 0.000 description 1
- GRWFGVWFFZKLTI-UHFFFAOYSA-N rac-alpha-Pinene Natural products CC1=CCC2C(C)(C)C1C2 GRWFGVWFFZKLTI-UHFFFAOYSA-N 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 125000003011 styrenyl group Chemical class [H]\C(*)=C(/[H])C1=C([H])C([H])=C([H])C([H])=C1[H] 0.000 description 1
- VNJISVYSDHJQFR-UHFFFAOYSA-N tert-butyl 4,4-dimethylpentaneperoxoate Chemical compound CC(C)(C)CCC(=O)OOC(C)(C)C VNJISVYSDHJQFR-UHFFFAOYSA-N 0.000 description 1
- NMOALOSNPWTWRH-UHFFFAOYSA-N tert-butyl 7,7-dimethyloctaneperoxoate Chemical compound CC(C)(C)CCCCCC(=O)OOC(C)(C)C NMOALOSNPWTWRH-UHFFFAOYSA-N 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- DLSMLZRPNPCXGY-UHFFFAOYSA-N tert-butylperoxy 2-ethylhexyl carbonate Chemical compound CCCCC(CC)COC(=O)OOOC(C)(C)C DLSMLZRPNPCXGY-UHFFFAOYSA-N 0.000 description 1
- 238000002834 transmittance Methods 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
- SCWPFSIZUZUCCE-UHFFFAOYSA-N β-terpinene Chemical compound CC(C)C1=CCC(=C)CC1 SCWPFSIZUZUCCE-UHFFFAOYSA-N 0.000 description 1
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Description
【0001】
【発明の属する技術分野】
本発明は、光入射による樹脂内部の白濁現象(チンダル現象)が抑えられたアクリル樹脂板状物の製造方法に関し、特に、液晶表示装置のフロントライトや、各種のディスプレイ用面光源装置、面照明装置などの導光板および光集光装置や、光伝達装置などの光導波板として用いられる光学用アクリル樹脂板状物の製造方法に関する。
【0002】
【従来の技術】
従来より、薄型の看板や表示装置、液晶表示装置の背面光源(バックライト)および前面光源(フロントライト)等に用いられる光源装置として、導光体に光を入射して発光させる面発光装置が知られている。また近年は、サイドライド方式と呼ばれる、導光体の側面に冷陰極管や熱陰極管などの光源を配置し、任意の形状またはパターンで発光させる面発光装置が主流となっている。
【0003】
この種の光源装置には、より輝度が高く、よりコンパクトであること(軽量化および薄肉化)が求められている。また、この光源装置に用いられる導光体は、耐熱性が高く、かつ導光体中における光の吸収、散乱、反射などによる透過損失ができるだけ少ないことが望ましい。このような点から、高い光線透過率を有するアクリル樹脂が用いられている。
【0004】
しかし、アクリル樹脂を用いた場合であっても、例えば、液晶セルの前面にサイドライト型の導光板が配置されるフロントライトタイプの表示装置においては、導光板内部に曇り等の透過損失因子が存在すると、液晶表示の色再現性およびコントラスト等の画像特性の低下が生じ易い。
【0005】
導光体に用いられる透過損失を改良したアクリル樹脂として、例えば、特開平7−331018号公報、特開平9−12822号公報、特開平9−25386号公報には、アクリル樹脂中にホスファイト化合物を特定濃度で含有させることにより、射出成型時の加熱着色による光の吸収を低減したアクリル系樹脂組成物が開示されている。また、特開平8−334626号公報には、可視光の透過損失の少ない導光板用アクリル樹脂として、紫外線吸収剤などの光を吸収する添加剤を含まないアクリル系樹脂製導光体が開示されている。
【0006】
導光板の素板材料であるアクリル樹脂板状物の成形方法としては、例えばキャスト製法、押出製法、射出成形法、加熱プレス成形法などの種々の方法が知られているが、何れの方法においても、サブミクロンからミクロンオーダーの異物が混入していることが多い。そして、アクリル樹脂と異なる屈折率の異物が混入すると、導光板に光を入光させたときに輝度ムラまたは輝点不良が生じる場合があるので、このような異物は極力減少させる必要がある。例えば、特開平8−227004号公報、特開平10−265530号公報、特開平8−248416号公報では、アクリル樹脂中の異物のサイズおよび量と揮発性成分の種類および残存量を特定した導光板用アクリル樹脂組成物が提案されている。また、特開平8−334626号公報では、導光体への入光波長より大きく屈折率を異にする物質を含まないアクリル製導光体が開示されている。
【0007】
しかしながら、これら公報に開示された導光板用アクリル樹脂組成物は、導光板と屈折率が異なる物質に起因する透過損失を、添加剤の有無や物理的な方法によって低減しているものであり、根本的な問題の解決には至っていない。特に、板厚が5mmを超える導光板を使用する対角線長さ457mm以上の液晶表示装置においては、用いられる導光板の透過光路長が長いので、より透過損失の影響を受け易く、面光源の輝度ムラ等が発生し易い。
【0008】
現在、上市されている導光板は、セルキャスト法、押出法、射出成形法、加熱プレス成形法などにより製造されている。しかし、板厚が5mmを超える導光板において、押出法、射出成形法、加熱プレス成形法により製造された導光板は、冷却時に生じる板内部と板表面部の温度差が原因で熱歪みが生じ、これが光学歪みとなり透過損失を生じさせる要因となる場合がある。このような光学歪みは、特にフロントライト用導光板において、像がゆがんで見える不具合を引き起こす。また、成形に必要な時間(成形サイクル)が長時間となるという製造上の問題もある。
【0009】
一方、従来のセルキャスト製板法では、製板される板の厚みが厚くなるに従って、アクリル樹脂内部に不均一な組成分布が生じ易くなり、また、未反応の残存不飽和単量体、開始剤の副生成物、添加剤の未溶解残渣などの基材(ポリメタクリル酸メチル)と屈折率が異なる物質が存在し、それらによる光の吸収や散乱、反射が生じる。そのため得られたアクリル樹脂導光板は、その端部から光を入射すると光の散乱、反射により樹脂内部に白濁が確認される。また特に、フロントライトタイプの表示装置に用いられる導光板または長光路長となる大型の導光板の場合、透過損失が大きい。
【0010】
このような透過損失を引き起こす白濁欠陥が発生する要因に関しては不明な点が多いが、アクリル樹脂内部に不均一な組成分布が生じ、あるいは未反応の残存不飽和単量体、開始剤の副生成物、添加剤の未溶解残渣など、基材(ポリメタクリル酸メチル等)とは屈折率が異なる物質が存在し、そのため光の吸収や散乱、反射が生じ、アクリル樹脂内部で白濁現象が生じるものと考えられる。
【0011】
【発明が解決しようとする課題】
本発明は、上述した従来技術の各課題を解決すべくなされたものである。すなわち、本発明の目的は、アクリル樹脂中の白濁欠陥が低減され、透過損失の少ないアクリル系樹脂板状物の製造方法を提供することにある。
【0012】
【課題を解決するための手段】
本発明者らは、上記目的を達成すべく鋭意検討を行った結果、セルキャスト製板法を特定の重合条件に従って行えば、アクリル樹脂板状物の内部に発生する白濁を低減でき、光学用途に非常に好適なアクリル樹脂板状物が得られることを見い出し、本発明を完成するに至った。
【0013】
すなわち本発明は、メタクリル酸メチルを主成分とする重合性原料をキャスト製板法により重合して板厚10mm以上のアクリル樹脂板状物を製造する方法において、20℃以上60℃未満の重合温度で、少なくとも1段階以上の昇温によりポリマーコンバージョンを30質量%〜60質量%に重合させる工程と、続いて、60℃以上130℃以下の重合温度で、少なくとも1段階以上の昇温により樹脂のポリマーコンバージョンを97質量%以上に重合させる工程とを有し、前記60℃以上130℃以下の重合温度条件下における重合工程開始時から重合発熱ピーク発現までの時間Tが、下記式(1)
T≦0.4×t (1)
[式中、Tは前記60℃以上130℃以下の重合温度条件下における重合工程開始時から重合発熱ピーク発現までの時間(hr)、tはアクリル樹脂板状物の板厚(mm)]
で表した範囲内であることを特徴とするアクリル樹脂板状物の製造方法である。
また本発明は、上述のアクリル樹脂板状物の製造方法において、メタクリル酸メチルを主成分とし、かつアクリル酸エステルを含む重合性原料を用いるアクリル樹脂板状物の製造方法に関する。
【0014】
【発明の実施の形態】
本発明においては、メタクリル酸メチルを主成分とする重合性原料をキャスト製板法により重合して板厚10mm以上のアクリル樹脂板状物を製造する。通常、板厚10mm以上のキャスト製板法では、重合時に発泡させないように重合発熱温度を抑えて重合を行う必要があり、低温度で長時間かけて重合を行う。しかしながら、従来の重合条件のキャスト製板法により得たアクリル樹脂板状物は、内部透過損失が大きく、アクルリ板側面より光を入射したエッジライト観察では、板全体が曇って見える。一方、本発明は、重合初期の温度を20℃以上60℃未満の範囲内にして、樹脂のポリマーコンバージョンを30質量%〜60質量%に重合させて、続いて60℃を超える温度で急速に重合を行うことによって、ポリマーコンバージョンを97質量%以上に重合させる方法であり。このような重合条件によって、板厚10mm以上のアクリル樹脂板の内部透過損失を減少させたアクリル樹脂板状物を得ることができる。
【0015】
20℃以上60℃未満の重合温度で、少なくとも1段階以上の昇温によりポリマーコンバージョンを30質量%〜60質量%に重合させる工程(以下「初期重合工程」と称す)において、重合温度が20℃未満では、重合に長時間を要するので工業的生産に適さず、また60℃以上では、重合発熱温度が高温になり発泡欠陥が発生する恐れがある。
【0016】
初期重合工程においては、温水浴による重合を行うことが好ましい。温水浴による重合は除熱効果が大きいので、重合発熱温度の上昇を抑制でき、特に厚板重合における重合発熱温度の暴走を防止できる。
【0017】
初期重合工程の重合温度の具体的値は、製造しようとするアクリル樹脂板状物のサイズや板厚等に応じて、上述の温度範囲内で適宜決定すればよい。初期重合工程においては、上述の温度範囲内において、少なくとも1段階以上の昇温により重合させることができ、例えば、多段階的に昇温することもできる。多段階に昇温する場合は、短時間で所定のポリマーコンバージョンまで重合することができるので、重合時間を短縮できる。
【0018】
初期重合工程終了時におけるポリマーコンバージョンは、30質量%〜60質量%である。これが60質量%を超えると、アクリル樹脂板状物の内部透過損失が大きくなるので、光学用材料として好ましくない。また、これが30質量%未満では、初期重合工程の後の60℃を超える高温度での重合工程において、重合発熱温度が高温になり過ぎ、発泡欠陥が発生する恐れがある。さらにポリマーコンバージョンの下限値は40質量%以上が好ましく、また上限値は50質量%以下が好ましい。
【0019】
本発明においては、上述した初期重合工程の後、60℃以上130℃以下の重合温度で、少なくとも1段階以上の昇温により樹脂のポリマーコンバージョンを97質量%以上に重合させる工程(以下「高温重合工程」と称す)を行う。この高温重合工程における重合温度が60℃未満では、重合時間が長時間になるだけでなく、アクリル樹脂板状物の内部透過損失が大きくなるので光学用材料として好ましくない。また、130℃を超えると、重合発熱温度が高温になり発泡欠陥が発生し易い。
【0020】
高温重合工程においては、空気浴による重合を行うことが好ましい。空気浴による重合は、除熱効果が小さいので重合発熱温度が上昇しやすく、重合反応が急速に進行するので、ポリマーコンバージョンを急速に上昇できる。
【0021】
高温重合工程の具体的値は、製造しようとするアクリル樹脂板状物のサイズや板厚等に応じて、上述の温度範囲内で適宜決定すればよい。高温重合工程においては、上述の温度範囲内において、少なくとも1段階以上の昇温により重合させることができ、例えば、多段階的に昇温することもできる。多段階に昇温する場合は、例えば厚板の重合では、重合発熱を抑制しながら重合することができるため、発泡欠陥を防止することができる。
【0022】
高温重合工程終了時におけるポリマーコンバージョンは、97質量%以上である。製造したアクリル系樹脂板状物において、未反応単量体の残存量が3質量%未満であれば、未反応モノマーに起因する耐熱性の低下および耐光性の低下を低減することができ、また残存する未反応単量体に起因する光散乱による透過損失の低下を抑えることができる。
【0023】
高温重合工程において、アクリル樹脂板状物のポリマーコンバージョンを97質量%以上に上げるためには、特に、高温重合工程における1段階目昇温パターンに次いで、2段階目の昇温として120℃以上130℃以下の温度で1時間〜20時間の加熱処理を行うことが好ましい。
【0024】
高温重合工程において、その工程開始時から重合発熱ピーク発現までの時間Tは、下記式(1)
T≦0.4×t (1)
[式中、Tは高温重合工程開始時から重合発熱ピーク発現までの時間(hr)、tはアクリル樹脂板状物の板厚(mm)]
で表した範囲内である。
【0025】
高温重合工程開始時から重合発熱ピーク発現までの時間Tが、式(1)で表した時間を超えると、得られるアクリル樹脂板状物の内部透過損失が大きくなり、光学用材料として好ましくない。また、ここで高温重合工程における重合温度条件を多段階に昇温した場合、重合発熱ピーク発現までの時間Tは、1段階目の高温重合工程開始時から最初に発現した重合発熱ピークまでの時間を表す。
【0026】
さらに、この時間Tは下記式(2)
T≦0.25×t (2)
[T、tは式(1)と同意]。
で表した範囲内であることが好ましい。
【0027】
本発明において、メタクリル酸メチルを主成分とする重合性原料は、単量体としてメタクリル酸メチルのみを含む重合性原料であってもよいし、メタクリル酸メチルと共重合可能な他の単量体との単量体混合物からなる重合性原料であってもよい。また、メタクリル酸メチル単独重合体または単量体混合物の重合体と、メタクリル酸メチルまたは単量体混合物とからなるシロップ状の重合性原料であってもよい。重合性原料中のメタクリル酸メチルの含有量(メタクリル酸メチル系重合体を含む場合は重合体中のメタクリル酸メチル単位の含有量も含む)は、50モル%以上であることが好ましい。
【0028】
メタクリル酸メチルと共重合可能な他の単量体としては、従来より知られる種々のビニル系単量体を使用できる。例えば、アクリル酸メチル、(メタ)アクリル酸エチル、(メタ)アクリル酸ブチル、(メタ)アクリル酸シクロヘキシル、(メタ)アクリル酸フェニル、(メタ)アクリル酸ベンジル、(メタ)アクリル酸2−エチルヘキシル、(メタ)アクリル酸2−ヒドロキシエチル等のメタクリル酸メチル以外の(メタ)アクリル酸エステルが挙げられる。ここで「(メタ)アクリル酸」とは、アクリル酸とメタクリル酸の総称である。
【0029】
これらのなかでも、メタクリル酸メチルとアクリル酸エステルからなる重合性原料が更に好ましい。このアクリル酸エステルとしては、アクリル酸メチル、アクリル酸エチル、アクリル酸ブチルおよびアクリル酸2−エチルヘキシルからなる群より選ばれる少なくとも一種を使用することが最も好ましい。重合性原料がアクリル酸エステルとメタクリル酸メチルとを含む場合、アクリル酸エステルの含有量は1〜10質量%が好ましく、この範囲において、3質量%以上がより好ましく、7質量%以下が特に好ましい。メタクリル酸メチルの含有量は90〜99質量%が好ましく、この範囲において、93質量%以上がより好ましく、97質量%以下が特に好ましい。重合性原料がアクリル酸エステルを含むと、透過損失の小さい優れた透明性を有するアクリル樹脂板状物を得ることが容易となる。ただし、アクリル酸エステルの含有量が多過ぎると、得られたアクリル樹脂板状物の耐熱性が低下し、高熱を発する光源ランプと近接する導光板用途においては、樹脂板の融解や変形が生じるおそれがある。
【0030】
また、透明性が損なわれず、所望の特性を持つ板状物が得られる範囲内で、エチレングリコールジ(メタ)アクリレート、ジエチレングリコール(メタ)アクリレート、ネオペンチルグリコールジ(メタ)クリレートなどの多官能(メタ)アクリレート等を添加してもよい。ここで「(メタ)アクリレート」とは、アクリレートとメタクリレートの総称である。
【0031】
本発明においては、必要に応じて重合調節剤を用いることができる。重合調節剤は、重合速度を遅延する作用を有する化合物であればよく、従来より知られる各種のものを使用できる。例えば、n−ブチルメルカプタン、n−オクチルメルカプタンなどのメルカプタン化合物、リモネン、ミルセン、α−テルピネン、β−テルピネン、γ−テルピネン、テルピノレン、β−ピネン、α−ピネンなどのテルペノイド系化合物、α−メチルスチレンダイマーなどが挙げられる。特に、テルペノイド系化合物が好ましい。これら重合調節剤は単独で用いても、2種以上を混合して用いても良い。重合調節剤の添加量は、重合性原料100質量部に対して、0.001〜0.05質量部が好ましい。
【0032】
重合開始剤としては、例えば、重合性原料に可溶なアゾ系化合物および過酸化物系化合物などが好ましく、特に、メタクリル酸メチルに溶解し、あるいはメタクリル酸メチルを含む単量体混合物に溶解するものが好ましい。
【0033】
アゾ系化合物(アゾ系重合開始剤)としては、例えば、2,2'−アゾビスイソブチロニトリル、2,2'−アゾビス(2,4−ジメチルバレロニトリル)、2,2'−アゾビス(2,4−ジメチル−4−メトキシバレロニトリル)等が挙げられる。
【0034】
過酸化物系化合物(過酸化物系重合開始剤)としては、例えば、メチルエチルケトンパーオキサイド、メチルイソブチルケトンパーオキサイド、シクロヘキサノンパーオキサイド等のケトンパーオキサイド類;イソブチリルパーオキサイド、ラウロイルパーオキサイド、ベンゾイルパーオキサイド等のジアシルパーオキサイド類;2,5−ジメチル−2,5−ジ−(t−ブチルパーオキシ)ヘキサン等のジアルキルパーオキサイド類;1,1−ジ(t−ブチルパーオキシ)−3,3,5−トリメチルシクロヘキサン等のパーオキシケタール類;1,1,3,3−テトラメチルブチルパーオキシネオデカノエート、t−ブチルパーオキシネオデカノエート、t−ブチルパーオキシネオヘプタノエート、t−ヘキシルパーオキシピバレート、t−ブチルパーオキシピバレート、t−ブチルパーオキシ−2−エチルヘキサノエート、t−ブチルパーオキシイソブチレート等のアルキルパーエステル類;ジ−3−メトキシブチルパーオキシジカボネート、ジ−2−エチルヘキシルパーオキシジカーボネート、ビス(4−t−ブチルシクロヘキシル)パーオキシジカーボネート、ジ−イソプロピルパーオキシジカーボネート、t−ブチルパーオキシイソプロピルカーボネート、t−ブチルパーオキシ−2−エチルヘキシルカーボネート等のパーオキシカーボネート類;などが挙げられる。
【0035】
これらの重合開始剤は単独で、あるいは二種以上を混合して用いてもよい。その使用量は、重合温度等の重合条件に応じて適宜設定されるが、通常、重合性原料100質量部に対して0.0001〜1質量部である。
【0036】
重合性原料の調製時や、キャストセル組み立て時、セルへの原料注入時において、輝点不良の発生を防止する点から、異物の混入はできるだけ避ける必要がある。また重合性原料は、微細な目の濾過材(メンブレンフィルターや焼結金属フィルター等)で異物を除去した後に重合することが好ましい。
【0037】
アクリル樹脂板状物には、透明性が損なわれず、所望の特性を持つアクリル樹脂板が得られる範囲内で、従来より知られる各種の紫外線吸収剤、酸化防止剤等の安定剤、難燃剤、帯電防止剤、樹脂板の鋳型との剥離を容易にする離型剤等の添加剤を添加してもよい。
【0038】
本発明におけるキャスト製板法は、重合性原料を鋳型内で塊状重合する方法である。鋳型としては、例えば、ガラス板、鏡面研磨されたステンレス鋼板等からなる鋳型を用いることができる。また、内部表面に微小な凹凸形状を有する鋳型を用いても良い。バッチ式のキャスト製板法としては、例えば、2枚の板(ガラス板、鏡面研磨されたステンレス鋼板等)と、塩化ビニール製の無端ガスケットとからなる鋳型の空間部に、重合開始剤を溶解した重合性原料を注入し、この重合性原料を重合硬化させ、板状重合体を鋳型から剥離して取り出す方法が挙げられる。
【0039】
【実施例】
以下、実施例により本発明を、具体的に説明する。なお、各評価は以下の方法に従い行った。
【0040】
(1)輝度の測定:
板状物内部の白濁度合いを評価する為に、以下の様にして輝度を測定した。まず、アクリル樹脂板状物を、平面形状が長方形の300mm×400mm(光路長400mm)に切断し、板状物周辺の4つの側面を電動カンナおよび羽布研磨機にて鏡面研磨を行った。4つの側面のうち光入射面1面を除く3つの側面には、反射率が96%であるリフレクターフィルム((株)ツジデン製、SU119)を配置した。この板状物の背面側には、明度が2.0である黒色板を板状物から10mm離して設置した。また、100Wハロゲンランプを用いた光ファイバー照明装置の光源(三菱レイヨン(株)製光源装置:ELI 100J、光ファイバーライトガイド 幅1mm×長さ200mm、光源の光出射面から50mm離れた場所の照度:100000Lux)を、光入射面における板厚方向での中央部に平行に設置した。
【0041】
そして、クローズアップレンズ(ミノルタ(株)製 No.122)を装着した輝度測定装置(ミノルタ(株)製 LS−110)を、板状物正面から350mm離した位置に設置し、板状物正面中央部における垂直方向の輝度を測定し、板状物内部の白濁度合いの指標を輝度で評価した。すなわち、板状物に光を入射した際、その光は透過および反射によりアクリル樹脂内を導光し、樹脂内部に異物あるいは不均一な組成分布等が存在すると光の吸収・散乱・反射が起き、白濁が確認されるとともに透過損失が生じるので、この輝度の測定により白濁度合いを評価できる。
【0042】
(2)ポリマーコンバージョンの測定:
各工程におけるアクリル樹脂を液体窒素中で凍結粉砕し、得られた樹脂2gをクロロホルム100mlに溶解し、n−ヘキサン3L中に滴下、攪拌してアクリルポリマーを再析出させた。その後、ガラスフィルターNO.2G3(孔径40μm〜100μm)にて溶剤をろ過処理してポリマーを得た。さらに、このポリマーを80℃真空乾燥機中にて一昼夜、溶剤を揮発および乾燥させ、乾燥したポリマーの重量を計測し、初期に溶解したアクリル樹脂から析出したポリマーの比率を算出し、ポリマーコンバージョンの値とした。
【0043】
(3)重合発熱ピーク時間の測定:
鋳型を組む際、坂口電熱(株)製のT35型シース熱伝対(直径1mm、長さ1000mm)を板サイズの中央および板厚の中央部分に先端が来るようにセッティングし、横河電機(株)製のペンレコーダーLR4110に接続して、重合発熱ピーク時間を測定した。
【0044】
<実施例1>
メタクリル酸メチル100質量部に、重合開始剤としてビス(4−t−ブチルシクロヘキシル)−パーオキシジカーボネート0.007質量部、およびテルピノレン0.007質量部を添加して30分間攪拌した。脱気後、縦400mm×500mm、厚み6mmのガラス板2枚を塩化ビニール製の無端チューブを介して構成された鋳型の中に注入し、40℃温水浴にて20時間重合し、続いて70℃の空気浴にて3時間重合し、続いて130℃の空気浴にて2時間かけて重合を完結させて、サイズ350mm×450mm、厚さ10mmのアクリル樹脂板を得た。
【0045】
40℃温水浴での重合後の樹脂のポリマーコンバージョンは44質量%であり、70℃空気浴での重合後のポリマーコンバージョンは85質量%、130℃空気浴での重合後のポリマーコンバージョンは99質量%であった。また、70℃空気浴における高温重合工程開始時から最初の重合発熱ピーク発現までの時間Tは、0.4時間であった。得られたアクリル樹脂板について輝度の測定を行い、表1に示す結果を得た。
【0046】
<実施例2〜8>
表1に記載のように、樹脂板の厚み、原料組成、重合開始剤の量、重合温度および重合時間を変えたこと以外は、実施例1と同様にしてアクリル樹脂板を製造した。ここでメタクリル酸メチルのシロップとは、メタクリル酸メチルの一部を重合させた重合体とメタクリル酸メチルとからなるシロップのことであり、そのシロップ中のポリマーコンバージョンが10質量%、シロップの粘度が500mPa・sのものを用いた。また、実施例6〜8においては、輝度測定におけるサンプルサイズは200mm×200mmとした。各実施例で得られたアクリル樹脂板について輝度の測定を行い、表1に示す結果を得た。
【0047】
<実施例9〜14>
表2に記載のように、樹脂板の厚み、原料組成、重合開始剤の量、重合温度および重合時間に変えたこと以外は、実施例1と同様にしてアクリル樹脂板を製造した。ここでメタクリル酸メチルのシロップとは、メタクリル酸メチルの一部を重合させた重合体とメタクリル酸メチルとからなるシロップのことであり、そのシロップ中の重合体含有率は10質量%、シロップの粘度は500mPa・sのものを用いた。また、実施例11〜14においては、輝度測定におけるサンプルサイズは200mm×200mmとした。各実施例で得られたアクリル樹脂板について輝度の測定を行い、表2に示す結果を得た。
【0048】
<比較例1>
メタクリル酸メチル100質量部に、重合開始剤としてビス(4−t−ブチルシクロヘキシル)−パーオキシジカーボネート0.02質量部を添加して30分間攪拌した。脱気後、縦400mm×横500mm、厚み6mmのガラス板2枚を塩化ビニール製の無端チューブを介して構成されたセルの中に注入し、40℃温水浴にて17時間重合し、続いて130℃の空気浴にて2時間かけて重合を完結させて、サイズ350mm×450mm、厚さ10mmのアクリル樹脂板を得た。40℃温水浴での重合後の樹脂のポリマーコンバージョンは85質量%であり、130℃空気浴での重合後のポリマーコンバージョンは99質量%であった。得られたアクリル樹脂板について輝度の測定を行い、表3に示す結果を得た。
【0049】
<比較例2〜5>
表3に記載のように、樹脂板の厚み、原料組成、重合開始剤の種類と量、重合温度および重合時間を変えたこと以外は、実施例1と同様にしてアクリル樹脂板を製造した。また、比較例4および比較例5は、実施例6〜8と同様のサイズにて樹脂板を得た。得られた樹脂板について輝度の測定を行い、表3に示す結果を得た。
【0050】
【表1】
【0051】
【表2】
【0052】
【表3】
【0053】
【発明の効果】
本発明によれば、アクリル樹脂中の白濁欠陥が低減され、透過損失の少ない光学用に適したアクリル系樹脂板状物の製造方法を提供することができる。このアクリル系樹脂板状物は、特に、薄型の看板や表示装置、液晶表示装置のフロントライト等に用いられる導光板用途に好適である。また特に、樹脂にメタクリル酸メチルとアクリル酸エステルとを含むことによって、さらに透過損失の少ないアクリル樹脂板状物を得ることができる。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for manufacturing an acrylic resin plate-like material in which a white turbidity phenomenon (Tyndall phenomenon) inside a resin due to light incidence is suppressed, and in particular, a front light of a liquid crystal display device, various display surface light source devices, and surface illumination. The present invention relates to a method of manufacturing an optical acrylic resin plate used as a light guide plate such as a device, a light condensing device, or an optical waveguide plate such as a light transmission device.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, as a light source device used for a thin signboard, a display device, a back light source (backlight) and a front light source (front light) of a liquid crystal display device, a surface light emitting device that emits light by being incident on a light guide Are known. In recent years, a surface light-emitting device called a side ride method, in which a light source such as a cold cathode tube or a hot cathode tube is arranged on the side surface of a light guide and emits light in an arbitrary shape or pattern, has become mainstream.
[0003]
This type of light source device is required to have higher brightness and be more compact (light weight and thinner). Further, it is desirable that the light guide used in this light source device has high heat resistance and has as little transmission loss as possible due to light absorption, scattering, and reflection in the light guide. From such a point, an acrylic resin having a high light transmittance is used.
[0004]
However, even when acrylic resin is used, for example, in a front light type display device in which a sidelight type light guide plate is arranged in front of a liquid crystal cell, there is a transmission loss factor such as fogging inside the light guide plate. If present, image characteristics such as color reproducibility and contrast of the liquid crystal display are likely to deteriorate.
[0005]
As an acrylic resin with improved transmission loss used for a light guide, for example, Japanese Patent Application Laid-Open No. 7-33018, Japanese Patent Application Laid-Open No. 9-12822, and Japanese Patent Application Laid-Open No. 9-25386 include a phosphite compound in an acrylic resin. An acrylic resin composition in which the absorption of light due to heating and coloring during injection molding is reduced by containing at a specific concentration is disclosed. Japanese Patent Laid-Open No. 8-334626 discloses an acrylic resin light guide that does not contain an additive that absorbs light, such as an ultraviolet absorber, as an acrylic resin for a light guide plate with little visible light transmission loss. ing.
[0006]
Various methods such as a cast manufacturing method, an extrusion manufacturing method, an injection molding method, and a hot press molding method are known as a molding method of an acrylic resin plate material that is a base material of a light guide plate. In many cases, however, foreign matter of submicron to micron order is mixed. If foreign matter having a refractive index different from that of the acrylic resin is mixed, unevenness of brightness or defective bright spots may occur when light is incident on the light guide plate. Therefore, it is necessary to reduce such foreign matter as much as possible. For example, in JP-A-8-227004, JP-A-10-265530, and JP-A-8-248416, a light guide plate in which the size and amount of foreign matter in the acrylic resin, the type of volatile components, and the residual amount are specified. An acrylic resin composition has been proposed. Japanese Patent Application Laid-Open No. 8-334626 discloses an acrylic light guide that does not contain a substance that has a refractive index greater than the wavelength of light incident on the light guide.
[0007]
However, the acrylic resin composition for a light guide plate disclosed in these publications has reduced transmission loss due to a substance having a refractive index different from that of the light guide plate by the presence or absence of an additive or a physical method. The fundamental problem has not been solved. In particular, in a liquid crystal display device having a diagonal line length of 457 mm or more that uses a light guide plate with a plate thickness exceeding 5 mm, the light guide plate used has a long transmission optical path length, which is more susceptible to transmission loss, and the luminance of the surface light source Unevenness is likely to occur.
[0008]
Currently marketed light guide plates are manufactured by cell casting, extrusion, injection molding, hot press molding, and the like. However, in a light guide plate with a plate thickness exceeding 5 mm, a light guide plate manufactured by an extrusion method, an injection molding method, or a hot press molding method is thermally distorted due to the temperature difference between the inside of the plate and the plate surface portion that occurs during cooling. This may cause optical distortion and cause transmission loss. Such optical distortion causes a problem that an image looks distorted particularly in a light guide plate for a front light. In addition, there is a manufacturing problem that the time required for molding (molding cycle) becomes long.
[0009]
On the other hand, in the conventional cell cast plate making method, as the thickness of the plate to be made increases, a non-uniform composition distribution tends to occur inside the acrylic resin, and unreacted residual unsaturated monomer is started. There are substances having a refractive index different from that of the base material (polymethyl methacrylate), such as a by-product of the agent and an undissolved residue of the additive, and light absorption, scattering, and reflection are caused by them. Therefore, when the obtained acrylic resin light-guide plate injects light from the edge part, white turbidity is confirmed inside resin by light scattering and reflection. In particular, in the case of a light guide plate used in a front light type display device or a large light guide plate having a long optical path length, transmission loss is large.
[0010]
There are many unclear points about the cause of the cloudiness defect that causes such transmission loss, but non-uniform composition distribution occurs inside the acrylic resin, or unreacted residual unsaturated monomer, initiator by-product Substances that have a different refractive index from the base material (polymethyl methacrylate, etc.), such as undissolved residues of materials and additives, which cause light absorption, scattering, and reflection, resulting in white turbidity inside the acrylic resin it is conceivable that.
[0011]
[Problems to be solved by the invention]
The present invention has been made to solve the above-described problems of the prior art. That is, an object of the present invention is to provide a method for producing an acrylic resin plate-like product in which white turbidity defects in an acrylic resin are reduced and transmission loss is small.
[0012]
[Means for Solving the Problems]
As a result of intensive studies to achieve the above object, the present inventors have been able to reduce the white turbidity generated inside the acrylic resin plate-like material by performing the cell casting plate method in accordance with specific polymerization conditions, and for optical applications. The present inventors have found that an acrylic resin plate that is very suitable for the above can be obtained, and have completed the present invention.
[0013]
That is, the present invention provides a polymerization temperature of 20 ° C. or more and less than 60 ° C. in a method for producing an acrylic resin plate having a thickness of 10 mm or more by polymerizing a polymerizable raw material mainly composed of methyl methacrylate by a cast plate method. in the step of polymerizing further polymer conversion of 30% to 60% by weight or more heating at least one stage, followed by the following polymerization temperature 60 ° C. or higher 130 ° C., and more than the heating at least one stage A step of polymerizing the polymer conversion of the resin to 97% by mass or more, and the time T from the start of the polymerization step under the polymerization temperature condition of 60 ° C. to 130 ° C. until the peak of the exothermic polymerization is expressed by the following formula (1 )
T ≦ 0.4 × t (1)
[Wherein, T is the time from the start of the polymerization step under the polymerization temperature condition of 60 ° C. or higher and 130 ° C. or lower until the peak of the exothermic polymerization (hr), t is the thickness of the acrylic resin plate (mm)]
It is in the range represented by (4), The manufacturing method of the acrylic resin plate-shaped object characterized by the above-mentioned.
The present invention also relates to a method for producing an acrylic resin plate using the polymerizable raw material containing methyl methacrylate as a main component and containing an acrylate ester in the method for producing an acrylic resin plate.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, an acrylic resin plate having a thickness of 10 mm or more is produced by polymerizing a polymerizable raw material mainly composed of methyl methacrylate by a cast plate method. Usually, in the cast plate method having a plate thickness of 10 mm or more, it is necessary to carry out the polymerization while suppressing the polymerization exothermic temperature so as not to foam during the polymerization, and the polymerization is carried out at a low temperature for a long time. However, the acrylic resin plate obtained by the cast plate method under the conventional polymerization conditions has a large internal transmission loss, and the whole plate appears cloudy when observed by edge light incident from the side of the acrylic plate. On the other hand, in the present invention, the initial polymerization temperature is set within a range of 20 ° C. or more and less than 60 ° C., and the polymer conversion of the resin is polymerized to 30% by mass to 60% by mass, and then rapidly at a temperature exceeding 60 ° C. It is a method of polymerizing polymer conversion to 97% by mass or more by performing polymerization. Under such polymerization conditions, it is possible to obtain an acrylic resin plate material in which the internal transmission loss of an acrylic resin plate having a thickness of 10 mm or more is reduced.
[0015]
At a polymerization temperature of less than 20 ° C. or higher 60 ° C., in a step of polymerizing the more polymer conversions or more heating at least one step in 30% to 60% by weight (hereinafter referred to as "initial polymerization step"), the polymerization temperature is 20 If it is less than 0 ° C., it takes a long time for the polymerization, so it is not suitable for industrial production, and if it is 60 ° C. or more, the heat of polymerization exotherm becomes high and foaming defects may occur.
[0016]
In the initial polymerization step, it is preferable to perform polymerization using a warm water bath. Since the polymerization in the hot water bath has a large heat removal effect, it is possible to suppress an increase in the polymerization exotherm temperature, and in particular, it is possible to prevent runaway of the polymerization exotherm temperature in the thick plate polymerization.
[0017]
What is necessary is just to determine suitably the specific value of the superposition | polymerization temperature of an initial stage polymerization process within the above-mentioned temperature range according to the size, board thickness, etc. of the acrylic resin plate-shaped material to be manufactured. Initial In the polymerization step, in a temperature range described above, it is possible to further polymerizing the above heating at least one stage, for example, can also be multi-stepwise raised. When the temperature is raised in multiple stages, the polymerization can be carried out in a short time until a predetermined polymer conversion, so that the polymerization time can be shortened.
[0018]
Polymer conversion at the end of the initial polymerization step is 30% by mass to 60% by mass. If this exceeds 60% by mass, the internal transmission loss of the acrylic resin plate is increased, which is not preferable as an optical material. On the other hand, if it is less than 30% by mass, the polymerization exothermic temperature becomes too high in the polymerization step at a high temperature exceeding 60 ° C. after the initial polymerization step, and foaming defects may occur. Furthermore, the lower limit of polymer conversion is preferably 40% by mass or more, and the upper limit is preferably 50% by mass or less.
[0019]
In the present invention, after the above-mentioned initial polymerization step, a polymerization temperature of 60 ° C. or higher 130 ° C. or less, is polymerized further polymer conversion of the resin to less than 97% by mass or more heating at least one step process (hereinafter "hot The polymerization step). When the polymerization temperature in this high-temperature polymerization step is less than 60 ° C., not only the polymerization time becomes long, but also the internal transmission loss of the acrylic resin plate is increased, which is not preferable as an optical material. On the other hand, if it exceeds 130 ° C., the polymerization exotherm temperature becomes high and foaming defects are likely to occur.
[0020]
In the high temperature polymerization step, it is preferable to perform polymerization using an air bath. Polymerization using an air bath has a small heat removal effect, so that the polymerization exotherm temperature is likely to rise and the polymerization reaction proceeds rapidly, so that the polymer conversion can be rapidly increased.
[0021]
What is necessary is just to determine the specific value of a high temperature polymerization process suitably within the above-mentioned temperature range according to the size, board thickness, etc. of the acrylic resin plate to be manufactured. In the high temperature polymerization process, in a temperature range described above, it is possible to further polymerization in the Atsushi Nobori above at least one stage, for example, can also be multi-stepwise raised. When the temperature is raised in multiple stages, for example, in the polymerization of a thick plate, the polymerization can be carried out while suppressing the heat generated by the polymerization, so that foaming defects can be prevented.
[0022]
The polymer conversion at the end of the high temperature polymerization process is 97% by mass or more. In the produced acrylic resin plate-like product, if the remaining amount of the unreacted monomer is less than 3% by mass, the decrease in heat resistance and light resistance due to the unreacted monomer can be reduced, and A decrease in transmission loss due to light scattering caused by the remaining unreacted monomer can be suppressed.
[0023]
In high temperature polymerization process, in order to increase the polymer conversion of the acrylic resin plate was more than 97% by weight, in particular, next to one step MeNoboru temperature pattern in the high temperature polymerization process, 120 ° C. and the Atsushi Nobori of the second stage The heat treatment is preferably performed at a temperature of 130 ° C. or lower for 1 hour to 20 hours.
[0024]
In the high temperature polymerization step, the time T from the start of the step to the occurrence of the polymerization exothermic peak is expressed by the following formula (1).
T ≦ 0.4 × t (1)
[In the formula, T is the time (hr) from the start of the high-temperature polymerization step to the peak of the exothermic polymerization, and t is the thickness of the acrylic resin plate (mm)].
It is within the range expressed by
[0025]
If the time T from the start of the high-temperature polymerization process to the occurrence of the polymerization exothermic peak exceeds the time represented by the formula (1), the internal transmission loss of the resulting acrylic resin plate is increased, which is not preferable as an optical material. In addition, when the polymerization temperature conditions in the high temperature polymerization step are raised in multiple stages, the time T until the polymerization exothermic peak appears is the time from the start of the first stage high temperature polymerization step to the first polymerization exothermic peak. Represents.
[0026]
Furthermore, this time T is expressed by the following formula (2)
T ≦ 0.25 × t (2)
[T and t agree with formula (1)].
It is preferable to be within the range represented by
[0027]
In the present invention, the polymerizable raw material mainly composed of methyl methacrylate may be a polymerizable raw material containing only methyl methacrylate as a monomer, or other monomer copolymerizable with methyl methacrylate. The polymerizable raw material which consists of a monomer mixture with may be sufficient. Further, it may be a syrup-like polymerizable raw material comprising a methyl methacrylate homopolymer or a monomer mixture polymer and methyl methacrylate or a monomer mixture. The content of methyl methacrylate in the polymerizable raw material (including the content of methyl methacrylate units in the polymer when it includes a methyl methacrylate polymer) is preferably 50 mol% or more.
[0028]
As other monomers copolymerizable with methyl methacrylate, various conventionally known vinyl monomers can be used. For example, methyl acrylate, ethyl (meth) acrylate, butyl (meth) acrylate, cyclohexyl (meth) acrylate, phenyl (meth) acrylate, benzyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, Examples include (meth) acrylic acid esters other than methyl methacrylate such as 2-hydroxyethyl (meth) acrylate. Here, “(meth) acrylic acid” is a general term for acrylic acid and methacrylic acid.
[0029]
Among these, a polymerizable raw material composed of methyl methacrylate and an acrylate ester is more preferable. As the acrylate ester, it is most preferable to use at least one selected from the group consisting of methyl acrylate, ethyl acrylate, butyl acrylate, and 2-ethylhexyl acrylate. When the polymerizable raw material includes an acrylic ester and methyl methacrylate, the content of the acrylic ester is preferably 1 to 10% by mass, and in this range, 3% by mass or more is more preferable, and 7% by mass or less is particularly preferable. . The content of methyl methacrylate is preferably 90 to 99% by mass, and in this range, 93% by mass or more is more preferable, and 97% by mass or less is particularly preferable. When the polymerizable raw material contains an acrylate ester, it becomes easy to obtain an acrylic resin plate having excellent transparency with small transmission loss. However, if the content of the acrylate ester is too large, the heat resistance of the resulting acrylic resin plate is lowered, and in the light guide plate application close to the light source lamp that emits high heat, the resin plate is melted or deformed. There is a fear.
[0030]
Moreover, within the range in which transparency is not impaired and a plate-like product having desired characteristics is obtained, polyfunctionality such as ethylene glycol di (meth) acrylate, diethylene glycol (meth) acrylate, neopentyl glycol di (meth) acrylate ( A (meth) acrylate or the like may be added. Here, “(meth) acrylate” is a general term for acrylate and methacrylate.
[0031]
In the present invention, a polymerization regulator can be used as necessary. The polymerization regulator may be a compound having an action of delaying the polymerization rate, and various conventionally known compounds can be used. For example, mercaptan compounds such as n-butyl mercaptan and n-octyl mercaptan, limonene, myrcene, α-terpinene, β-terpinene, γ-terpinene, terpinolene, β-pinene, α-pinene and other terpenoid compounds, α-methyl Examples include styrene dimer. In particular, terpenoid compounds are preferable. These polymerization regulators may be used alone or in combination of two or more. The addition amount of the polymerization regulator is preferably 0.001 to 0.05 parts by mass with respect to 100 parts by mass of the polymerizable raw material.
[0032]
As the polymerization initiator, for example, an azo compound or a peroxide compound that is soluble in the polymerizable raw material is preferable, and particularly, it dissolves in methyl methacrylate or dissolves in a monomer mixture containing methyl methacrylate. Those are preferred.
[0033]
As the azo compound (azo polymerization initiator), for example, 2,2′-azobisisobutyronitrile, 2,2′-azobis (2,4-dimethylvaleronitrile), 2,2′-azobis ( 2,4-dimethyl-4-methoxyvaleronitrile) and the like.
[0034]
Examples of peroxide compounds (peroxide polymerization initiators) include ketone peroxides such as methyl ethyl ketone peroxide, methyl isobutyl ketone peroxide, and cyclohexanone peroxide; isobutyryl peroxide, lauroyl peroxide, and benzoyl peroxide. Diacyl peroxides such as oxide; dialkyl peroxides such as 2,5-dimethyl-2,5-di- (t-butylperoxy) hexane; 1,1-di (t-butylperoxy) -3, Peroxyketals such as 3,5-trimethylcyclohexane; 1,1,3,3-tetramethylbutylperoxyneodecanoate, t-butylperoxyneodecanoate, t-butylperoxyneoheptanoate , T-hexyl peroxypivalate, t-butyl per Alkyl peresters such as xypivalate, t-butylperoxy-2-ethylhexanoate, t-butylperoxyisobutyrate; di-3-methoxybutylperoxydicarbonate, di-2-ethylhexylperoxydicarbonate Peroxycarbonates such as bis (4-t-butylcyclohexyl) peroxydicarbonate, di-isopropylperoxydicarbonate, t-butylperoxyisopropylcarbonate, t-butylperoxy-2-ethylhexylcarbonate; Can be mentioned.
[0035]
These polymerization initiators may be used alone or in admixture of two or more. The amount used is appropriately set according to the polymerization conditions such as the polymerization temperature, but is usually 0.0001 to 1 part by mass with respect to 100 parts by mass of the polymerizable raw material.
[0036]
It is necessary to avoid contamination of foreign matters as much as possible from the viewpoint of preventing the occurrence of defective bright spots during the preparation of the polymerizable raw material, the assembly of the cast cell, and the injection of the raw material into the cell. The polymerizable raw material is preferably polymerized after removing foreign substances with a fine filter medium (membrane filter, sintered metal filter, etc.).
[0037]
In the acrylic resin plate-like material, transparency is not impaired, and within a range where an acrylic resin plate having desired characteristics is obtained, various conventionally known ultraviolet absorbers, stabilizers such as antioxidants, flame retardants, An additive such as an antistatic agent or a release agent that facilitates peeling of the resin plate from the mold may be added.
[0038]
The cast plate making method in the present invention is a method of bulk polymerization of a polymerizable raw material in a mold. As the mold, for example, a mold made of a glass plate, a mirror-polished stainless steel plate, or the like can be used. Moreover, you may use the casting_mold | template which has a micro uneven | corrugated shape on an internal surface. As a batch-type cast plate method, for example, a polymerization initiator is dissolved in a space of a mold composed of two plates (glass plate, mirror-polished stainless steel plate, etc.) and an endless gasket made of vinyl chloride. The polymerizable raw material is injected, the polymerizable raw material is polymerized and cured, and the plate-like polymer is peeled off from the mold and taken out.
[0039]
【Example】
Hereinafter, the present invention will be described specifically by way of examples. Each evaluation was performed according to the following method.
[0040]
(1) Measurement of luminance:
In order to evaluate the degree of white turbidity inside the plate, the luminance was measured as follows. First, the acrylic resin plate was cut into a rectangular shape of 300 mm × 400 mm (optical path length 400 mm), and the four side surfaces around the plate were mirror-polished with an electric plane and a cloth polishing machine. A reflector film (SU119, manufactured by Tsujiden Co., Ltd.) having a reflectance of 96% was disposed on three side surfaces of the four side surfaces excluding one light incident surface. On the back side of the plate-like material, a black plate having a lightness of 2.0 was placed 10 mm away from the plate-like material. Further, a light source of an optical fiber illuminator using a 100 W halogen lamp (light source device manufactured by Mitsubishi Rayon Co., Ltd .: ELI 100J, optical fiber light guide width 1 mm × length 200 mm, illuminance at a location 50 mm away from the light exit surface of the light source: 100000 Lux ) Was installed in parallel to the central portion of the light incident surface in the thickness direction.
[0041]
Then, a luminance measuring device (LS-110 manufactured by Minolta Co., Ltd.) equipped with a close-up lens (No. 122 manufactured by Minolta Co., Ltd.) is installed at a position 350 mm away from the front of the plate-shaped object, and the front of the plate-shaped object is installed. The brightness in the vertical direction at the center was measured, and an index of the degree of white turbidity inside the plate was evaluated by brightness. That is, when light is incident on a plate-like object, the light is guided through the acrylic resin by transmission and reflection, and if there is a foreign substance or a non-uniform composition distribution in the resin, light absorption / scattering / reflection occurs. Since white turbidity is confirmed and transmission loss occurs, the degree of white turbidity can be evaluated by measuring the luminance.
[0042]
(2) Measurement of polymer conversion:
The acrylic resin in each step was freeze-pulverized in liquid nitrogen, and 2 g of the obtained resin was dissolved in 100 ml of chloroform, dropped and stirred in 3 L of n-hexane to reprecipitate the acrylic polymer. Thereafter, the solvent was filtered through a glass filter No. 2G3 (pore diameter: 40 μm to 100 μm) to obtain a polymer. Further, the polymer was volatilized and dried overnight in a vacuum dryer at 80 ° C., the weight of the dried polymer was measured, and the ratio of the polymer precipitated from the acrylic resin that was initially dissolved was calculated. Value.
[0043]
(3) Measurement of polymerization exothermic peak time:
When assembling the mold, set the T35 type sheath thermocouple (diameter 1 mm, length 1000 mm) manufactured by Sakaguchi Electric Heat Co., Ltd. so that the tip comes to the center of the plate size and the center of the plate thickness. It was connected to a pen recorder LR4110 manufactured by Co., Ltd., and the polymerization exothermic peak time was measured.
[0044]
<Example 1>
To 100 parts by mass of methyl methacrylate, 0.007 parts by mass of bis (4-t-butylcyclohexyl) -peroxydicarbonate and 0.007 parts by mass of terpinolene were added as a polymerization initiator and stirred for 30 minutes. After deaeration, two glass plates having a length of 400 mm × 500 mm and a thickness of 6 mm were poured into a mold formed through an endless tube made of vinyl chloride, polymerized for 20 hours in a 40 ° C. hot water bath, and subsequently 70 Polymerization was performed for 3 hours in an air bath at a temperature of 3 ° C., followed by completion of polymerization in an air bath at 130 ° C. for 2 hours to obtain an acrylic resin plate having a size of 350 mm × 450 mm and a thickness of 10 mm.
[0045]
Polymer conversion of the resin after polymerization in a 40 ° C. hot water bath was 44% by mass, polymer conversion after polymerization in a 70 ° C. air bath was 85% by mass, and polymer conversion after polymerization in a 130 ° C. air bath was 99% by mass. %Met. The time T from the start of the high-temperature polymerization process in the 70 ° C. air bath to the first peak of the exothermic polymerization was 0.4 hours. The obtained acrylic resin plate was measured for luminance, and the results shown in Table 1 were obtained.
[0046]
<Examples 2 to 8>
As shown in Table 1, an acrylic resin plate was produced in the same manner as in Example 1 except that the thickness of the resin plate, the raw material composition, the amount of the polymerization initiator, the polymerization temperature, and the polymerization time were changed. Here, the methyl methacrylate syrup is a syrup composed of a polymer obtained by polymerizing a part of methyl methacrylate and methyl methacrylate. The polymer conversion in the syrup is 10% by mass, and the viscosity of the syrup is The thing of 500 mPa * s was used. In Examples 6 to 8, the sample size in the luminance measurement was 200 mm × 200 mm. The luminance was measured for the acrylic resin plate obtained in each example, and the results shown in Table 1 were obtained.
[0047]
<Examples 9 to 14>
As shown in Table 2, an acrylic resin plate was produced in the same manner as in Example 1 except that the thickness of the resin plate, the raw material composition, the amount of the polymerization initiator, the polymerization temperature, and the polymerization time were changed. The methyl methacrylate syrup is a syrup composed of a polymer obtained by polymerizing a part of methyl methacrylate and methyl methacrylate, and the polymer content in the syrup is 10% by mass. A viscosity of 500 mPa · s was used. In Examples 11 to 14, the sample size in the luminance measurement was 200 mm × 200 mm. The acrylic resin plate obtained in each example was measured for luminance, and the results shown in Table 2 were obtained.
[0048]
<Comparative Example 1>
To 100 parts by mass of methyl methacrylate, 0.02 part by mass of bis (4-t-butylcyclohexyl) -peroxydicarbonate was added as a polymerization initiator and stirred for 30 minutes. After deaeration, two glass plates of length 400 mm x width 500 mm and thickness 6 mm are poured into a cell constructed through an endless tube made of vinyl chloride, polymerized in a 40 ° C hot water bath for 17 hours, and subsequently The polymerization was completed in an air bath at 130 ° C. for 2 hours to obtain an acrylic resin plate having a size of 350 mm × 450 mm and a thickness of 10 mm. The polymer conversion of the resin after polymerization in the 40 ° C. hot water bath was 85% by mass, and the polymer conversion after polymerization in the 130 ° C. air bath was 99% by mass. The obtained acrylic resin plate was measured for luminance, and the results shown in Table 3 were obtained.
[0049]
<Comparative Examples 2-5>
As shown in Table 3, an acrylic resin plate was produced in the same manner as in Example 1 except that the thickness of the resin plate, the raw material composition, the type and amount of the polymerization initiator, the polymerization temperature, and the polymerization time were changed. Moreover, the comparative example 4 and the comparative example 5 obtained the resin board in the same size as Examples 6-8. The resulting resin plate was measured for luminance, and the results shown in Table 3 were obtained.
[0050]
[Table 1]
[0051]
[Table 2]
[0052]
[Table 3]
[0053]
【The invention's effect】
ADVANTAGE OF THE INVENTION According to this invention, the cloudiness defect in an acrylic resin is reduced and the manufacturing method of the acrylic resin plate-shaped material suitable for the optical use with little transmission loss can be provided. This acrylic resin plate is particularly suitable for use as a light guide plate used for thin signboards, display devices, front lights of liquid crystal display devices, and the like. In particular, by including methyl methacrylate and acrylic ester in the resin, an acrylic resin plate-like product with further less transmission loss can be obtained.
Claims (4)
20℃以上60℃未満の重合温度で、少なくとも1段階以上の昇温によりポリマーコンバージョンを30質量%〜60質量%に重合させる工程と、
続いて、60℃以上130℃以下の重合温度で、少なくとも1段階以上の昇温により樹脂のポリマーコンバージョンを97質量%以上に重合させる工程とを有し、
前記60℃以上130℃以下の重合温度条件下における重合工程開始時から重合発熱ピーク発現までの時間Tが、下記式(1)
T≦0.4×t (1)
[式中、Tは前記60℃以上130℃以下の重合温度条件下における重合工程開始時から重合発熱ピーク発現までの時間(hr)、tはアクリル樹脂板状物の板厚(mm)]
で表した範囲内であることを特徴とするアクリル樹脂板状物の製造方法。In a method for producing an acrylic resin plate having a thickness of 10 mm or more by polymerizing a polymerizable raw material mainly composed of methyl methacrylate by a cast plate method,
At a polymerization temperature of less than 20 ° C. or higher 60 ° C., a step of polymerizing the more polymer conversions or more heating at least one step in 30% to 60% by weight,
Then, at a polymerization temperature of 60 ° C. or higher 130 ° C. or less, and a step of polymerizing further polymer conversion of the resin to less than 97% by mass or more heating at least one stage,
The time T from the start of the polymerization step under the polymerization temperature condition of 60 ° C. or higher and 130 ° C. or lower until the occurrence of the polymerization exothermic peak is represented by the following formula (1)
T ≦ 0.4 × t (1)
[Wherein, T is the time from the start of the polymerization step under the polymerization temperature condition of 60 ° C. or higher and 130 ° C. or lower until the peak of the exothermic polymerization (hr), t is the thickness of the acrylic resin plate (mm)]
The manufacturing method of the acrylic resin plate-shaped object characterized by being in the range represented by (4).
T≦0.25×t (2)
[T、tは式(1)と同意]。
で表した範囲内である請求項1記載のアクリル樹脂板状物の製造方法。Time T is the following formula (2)
T ≦ 0.25 × t (2)
[T and t agree with formula (1)].
The method for producing an acrylic resin plate according to claim 1, wherein
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