JPH1087706A5 - - Google Patents

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Publication number
JPH1087706A5
JPH1087706A5 JP1996249821A JP24982196A JPH1087706A5 JP H1087706 A5 JPH1087706 A5 JP H1087706A5 JP 1996249821 A JP1996249821 A JP 1996249821A JP 24982196 A JP24982196 A JP 24982196A JP H1087706 A5 JPH1087706 A5 JP H1087706A5
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JP
Japan
Prior art keywords
polymerization
solvent
monomer
polymerized
methyl methacrylate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP1996249821A
Other languages
Japanese (ja)
Other versions
JP3779777B2 (en
JPH1087706A (en
Filing date
Publication date
Application filed filed Critical
Priority to JP24982196A priority Critical patent/JP3779777B2/en
Priority claimed from JP24982196A external-priority patent/JP3779777B2/en
Publication of JPH1087706A publication Critical patent/JPH1087706A/en
Publication of JPH1087706A5 publication Critical patent/JPH1087706A5/ja
Application granted granted Critical
Publication of JP3779777B2 publication Critical patent/JP3779777B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【0019】
メタクリル系樹脂の重合温度としては、一般的な120−160℃の範囲内の温度が好ましい。重合温度が120℃未満であれば、重合が遅すぎ、また160℃を越えると転化率の調整が困難となるため好ましくない。
本発明の連続溶液重合プロセスの一例を図1で説明する。
(A)新たなメタクリル酸メチルを主成分とする単量体1と重合後の未反応メタクリル酸メチルを主成分とする単量体及び溶媒を含むリサイクル液9とを連続して蒸留塔2へ供給し、蒸留された単量体及び溶剤、更に重合開始剤、分子量調整剤を連続して重合反応機5に供給、重合し、次いで重合液を脱揮タンク8で脱揮して重合物10を取り出すと同時に未反応のビニル単量体及び溶媒をリサイクル使用して連続溶液重合する。又は(B)重合後の未反応メタクリル酸メチルを主成分とする単量体及び溶媒を含むリサイクル液9を連続して蒸留塔2へ供給し、蒸留されたメタクリル酸メチルを主成分とする単量体及び溶剤と新たなメタクリル酸メチルを主成分とする単量体1及び溶剤、更に重合開始剤、分子量調整剤を連続して重合反応機5に供給、重合し、次いで重合液を脱揮タンク8で脱揮して重合物を取り出すと同時に未反応のビニル単量体及び溶媒をリサイクル使用して連続溶液重合する。
[0019]
The polymerization temperature of the methacrylic resin is preferably a temperature in the general range of 120 to 160° C. If the polymerization temperature is less than 120° C., the polymerization is too slow, and if it exceeds 160° C., it is difficult to adjust the conversion rate, which is not preferable.
An example of the continuous solution polymerization process of the present invention is illustrated in FIG.
(A) Fresh monomer 1 containing methyl methacrylate as the main component and a recycled liquid 9 containing unreacted methyl methacrylate-based monomer and solvent after polymerization are continuously fed to distillation column 2, the distilled monomer and solvent, as well as a polymerization initiator and a molecular weight modifier, are continuously fed to polymerization reactor 5 and polymerized, the polymerized liquid is then devolatilized in devolatilization tank 8, polymerized product 10 is taken out, and at the same time, the unreacted vinyl monomer and solvent are recycled for continuous solution polymerization. Or (B) Fresh monomer 1 containing methyl methacrylate as the main component and solvent after polymerization are continuously fed to distillation column 2, the distilled monomer and solvent, fresh monomer 1 containing methyl methacrylate as the main component and solvent, as well as a polymerization initiator and a molecular weight modifier are continuously fed to polymerization reactor 5 and polymerized, the polymerized liquid is then devolatilized in devolatilization tank 8, polymerized product is taken out, and at the same time, the unreacted vinyl monomer and solvent are recycled for continuous solution polymerization.

JP24982196A 1996-09-20 1996-09-20 Method for producing methacrylic resin Expired - Lifetime JP3779777B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24982196A JP3779777B2 (en) 1996-09-20 1996-09-20 Method for producing methacrylic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24982196A JP3779777B2 (en) 1996-09-20 1996-09-20 Method for producing methacrylic resin

Publications (3)

Publication Number Publication Date
JPH1087706A JPH1087706A (en) 1998-04-07
JPH1087706A5 true JPH1087706A5 (en) 2004-09-30
JP3779777B2 JP3779777B2 (en) 2006-05-31

Family

ID=17198695

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24982196A Expired - Lifetime JP3779777B2 (en) 1996-09-20 1996-09-20 Method for producing methacrylic resin

Country Status (1)

Country Link
JP (1) JP3779777B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5568841B2 (en) 2008-04-08 2014-08-13 住友化学株式会社 Methacrylic resin composition for hot plate fusion
JP7642908B1 (en) * 2024-05-10 2025-03-10 住友化学株式会社 Composition, polymer, cured product, molded product, and method for producing polymethyl methacrylate

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