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US4246382A Expired / Lapsed US ⏱️ 0.0 years remaining

Solvent resistent acrylic resin and process for producing the same

Assignee: Asahi Kasei Corp
•
Filing: 1978-11-06
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Granted: 1981-01-20
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Expires: 1998-11-06
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Abstract

Abstract An acrylic resin having resistance to crazing or crack formation when brought into contact with an organic solvent may be prepared by polymerizing or copolymerizing a monomer or monomers comprising (1) 50 to 100 wt. % of methyl methacrylate and (2) 0 to 50 wt. % of at least one monomer selected from the group consisting of an acrylic ester and a methacrylic acid ester, and adding a chain transfer agent after initiation and prior to completion of the polymerization. The acrylic resins have an intrinsic viscosity of 0.028 to 0.117 liters per gram, and a ratio of weight-average molecular weight to number-average molecular weight of 2.3 to 6.0.

Inventors

  • 👤 Makoto Honda
  • 👤 Kohe Ozawa
  • 👤 Kazuhiro Hosoya
  • 👤 Jiro Kurita

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 20:52
CPC Classifications
C; C08; C08F; C08F20/00; C08F20/02; C08F20/10; C08F20/12; C08F20/14; C08F2/00; C08F2/38

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 215 words
A process for producing an acrylic resin having an intrinsic viscosity of about 0.028 to about 0.117 l/g and a weight-average molecular weight to number-average molecular weight ratio, measured by gel permeation chromatography, of about 2.3 to about 6.0, which process comprises polymerizing at a temperature range of from 40° C. to 170° C., using a polymerization initiator: A. about 50 to 100 wt. % of methyl methacrylate, and B. 0 to about 50 wt. % of at least one monomer selected from the group consisting of acrylic ester monomer and methacrylic ester monomer, said acrylic ester monomer comprising the reaction product of an alkyl alcohol having 1 to 8 carbon atoms and acrylic acid and said methacrylic ester comprising the reaction product of an alkyl alcohol having 2 to 12 carbon atoms and methacrylic acid; and adding, after initiation of polymerization, about 0.01 to about 5 wt. %, based on the weight of monomer, of a chain transfer agent comprising at least one compound selected from the group consisting of alkylmercaptans containing 4 to 18 carbon atoms; esters of thioglycolic acid and an alkyl alcohol having 1 to 12 carbon atoms; said chain transfer agent being added at a stage where the degree of conversion to the polymer is about 10 to about 60%.
Claim 2
Dependent Claim 215 words
A process for producing an acrylic resin having an intrinsic viscosity of about 0.028 to about 0.117 l/g and a weight-average molecular weight to number-average molecular weight ratio, measured by gel permeation chromatography, of about 2.3 to about 6.0, which process comprises polymerizing at a temperature range of from 40° C. to 170° C., using a polymerization initiator: A. about 50 to 100 wt. % of methyl methacrylate, and B. 0 to about 50 wt. % of at least one monomer selected from the group consisting of acrylic ester monomer and methacrylic ester monomer, said acrylic ester monomer comprising the reaction product of an alkyl alcohol having 1 to 8 carbon atoms and acrylic acid and said methacrylic ester comprising the reaction product of an alkyl alcohol having 2 to 12 carbon atoms and methacrylic acid; and adding, after initiation of polymerization, about 0.01 to about 5 wt. %, based on the weight of monomer, of a chain transfer agent comprising at least one compound selected from the group consisting of alkylmercaptans containing 4 to 18 carbon atoms; esters of thioglycolic acid and an alkyl alcohol having 1 to 12 carbon atoms; said chain transfer agent being added at a stage where the degree of conversion to the polymer is about 10 to about 60%.
Claim 3
Dependent Claim 30 words
The process of claim 1 wherein up to 1 wt. %, based on the weight of monomer of chain transfer agent is present with the monomer at initiation of polymerization.
Claim 4
Dependent Claim 11 words
The process of claim 1 wherein said polymerization is suspension polymerization.
Claim 5
Dependent Claim 11 words
The process of claim 1 wherein said polymerization is bulk polymerization.
Claim 6
Dependent Claim 11 words
The process of claim 1 wherein said polymerization is solution polymerization.
Claim 7
Dependent Claim 13 words
The process of claim 1 wherein said chain transfer agent is added batchwise.
Claim 8
Dependent Claim 13 words
The process of claim 1 wherein said chain transfer agent is added continuously.
Claim 9
Dependent Claim 13 words
The process of claim 1 wherein said chain transfer agent is added intermittently.
Claim 10
Dependent Claim 10 words
An acrylic resin produced by the process of claim 1.

References Cited (Backward Citations)

US3272786A Cited
US3198775A Cited
US3960824A Cited
US4145494A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-01-20 1984-07-21 1985-01-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-01-20 1988-07-21 1989-01-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-01-20 1992-07-21 1993-01-20 $7700.00 Window Closed / Lapsed

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