Patent US3968059A successfully refreshed from Google Patents.
US3968059A
Expired / Lapsed
US
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Process for producing methyl methacrylate polymers
Assignee: Mitsubishi Chemical Corp
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Filing: 1975-02-04
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Granted: 1976-07-06
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Expires: 1995-02-04
Abstract
Abstract A process of producing methyl methacrylate polymers is provided wherein the monomer are polymerized by a bulk polymerization procedure at 150 DEG to 180 DEG C with a conversion of 50 to 80% and the volatiles predominantly comprised of the unreacted monomer, separated from the polymer product, are cyclically reused as a part of the monomer feed for polymerization. In such a monomer feed cycle system, oligomers are substantially removed from the volatiles and then the volatiles are blended with a virgin monomer feed for polymerization, the content in the volatiles of impurities having boiling points of lower than 200 DEG C at normal pressure is maintained within the range of 5 to 20% by weight.
Inventors
- 👤 Kazushi Shimada
- 👤 Toru Maeda
- 👤 Tamotu Nishizawa
- 👤 Yositaka Sasaki
- 👤 Takehiko Narisada
- 👤 Hisao Anzai
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 19:00
CPC Classifications
C; C08; C08F; C08F20/00; C08F20/02; C08F20/10; C08F20/12; C08F20/14; C08F2/00; C08F2/02
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
192 words
An improvement in the process of producing a methyl methacrylate polymer or a copolymer, said methyl methacrylate polymer or copolymer comprising at least 80% by weight of units derived from methyl methacrylate and at most 20% by weight of units derived from a copolymerizable ethylenically unsaturated compound, by a bulk polymerization procedure wherein the monomer or monomers are polymerized at temperatures of 150° to 180°C with a conversion of 50 to 80% in a polymerization zone and the polymerizaton mixture withdrawn from the polymerizaton zone is introduced into a separation zone where volatiles predominantly comprised of an unreacted monomer or monomers are separated from the polymer product, said separated volatiles being cyclically used as a part of the monomer feed for the polymerization, said improvement comprising substantially removing polymers having molecular weights of 186 to approximately 1,000 from the volatiles and cyclically using the volatiles so treated as a part of the monomer feed for the polymerization while maintaining the content in the volatiles of impurities having boiling points of lower than 200°C at normal pressure within the range from 5 to 20% by weight based on the weight of the volatiles.
Claim 2
Dependent Claim
192 words
An improvement in the process of producing a methyl methacrylate polymer or a copolymer, said methyl methacrylate polymer or copolymer comprising at least 80% by weight of units derived from methyl methacrylate and at most 20% by weight of units derived from a copolymerizable ethylenically unsaturated compound, by a bulk polymerization procedure wherein the monomer or monomers are polymerized at temperatures of 150° to 180°C with a conversion of 50 to 80% in a polymerization zone and the polymerizaton mixture withdrawn from the polymerizaton zone is introduced into a separation zone where volatiles predominantly comprised of an unreacted monomer or monomers are separated from the polymer product, said separated volatiles being cyclically used as a part of the monomer feed for the polymerization, said improvement comprising substantially removing polymers having molecular weights of 186 to approximately 1,000 from the volatiles and cyclically using the volatiles so treated as a part of the monomer feed for the polymerization while maintaining the content in the volatiles of impurities having boiling points of lower than 200°C at normal pressure within the range from 5 to 20% by weight based on the weight of the volatiles.
Claim 3
Dependent Claim
98 words
The process according to claim 1 wherein said maintenance of the content of the impurities in the volatiles is carried out by removing a portion of the separated volatiles, either before or after the substantial removal of the polymers having molecular weight of 186 to approximately 1,000, when the content of the impurities in the volatiles gets near the intended value falling within the range from 5 to 20% by weight with repetition or continuation of the polymerization, and cyclically feeding the remaining portion of the volatiles as a part of the monomer feed to the polymerization zone.
Claim 4
Dependent Claim
33 words
The process according to claim 1 wherein the content of said impurities in the volatiles is maintained within the range from 5 to 15% by weight based on the weight of the volatiles.
Claim 5
Dependent Claim
23 words
The process according to claim 1 wherein said impurities having boiling points of lower than 200°C comprise methyl isobutyrate, methyl α-hydroxyisobutyrate and water.
Claim 6
Dependent Claim
46 words
The process according to claim 1 wherein said volatiles predominantly comprised of the unreacted monomer or monomers are maintained at temperatures of 30° to 150°C and pressures of 5 to 500 mmHg whereby said polymers having molecular weights of 186 to approximately 1,000 are substantially removed.
Claim 7
Dependent Claim
54 words
The process according to claim 1 wherein said substantial removal of the polymers having molecular weights of 186 to approximately 1,000 is effected to an extent such that the resulting volatiles contain less than 2% by weight of dimers formed from methyl methacrylate alone or from methyl methacrylate and the copolymerizable ethylenically unsaturated compound.
Claim 8
Dependent Claim
50 words
The process according to claim 1 wherein said substantial removal of the polymers having molecular weights of 186 to approximately 1,000 is effected to an extent such that the resulting volatiles contain less than 0.01% by weight of the polymer ingredients having molecular weights of approximately 500 to approximately 1,000.
Claim 9
Dependent Claim
33 words
The process according to claim 1 wherein said polymerization is carried out in a continuous manner by employing at least one reactor equipped with a stirring means for completely stirring the polymerization mixture.
Claim 10
Dependent Claim
38 words
The process according to claim 1 wherein said polymerization mixture is heated at 200°C to 290°C under a reduced pressure of 5 to 500 mmHg in the separation zone whereby said volatiles are separated from the polymer product.
Claim 11
Dependent Claim
18 words
The process according to claim 1 wherein said polymerization is carried out at temperatures of 150° to 160°C.
Claim 12
Dependent Claim
22 words
The process according to claim 1 wherein said copolymerizable ethylenically unsaturated compound is selected from methyl acrylate, ethyl acrylate and butyl acrylate.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-07-06 | 1980-01-05 | 1980-07-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-07-06 | 1984-01-05 | 1984-07-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-07-06 | 1988-01-05 | 1988-07-06 | $7700.00 | Window Closed / Lapsed |