US4487857A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing thermoplastic resin
Assignee: Mitsubishi Chemical Corp
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Filing: 1983-07-20
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Granted: 1984-12-11
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Expires: 2003-07-20
Abstract
Abstract A process for producing a thermoplastic resin capable of giving a molded article having a very good appearance, by coagulating a thermoplastic resin latex prepared by an emulsion polymerization method which comprises making the latex into a coagulated slurry by carrying out the coagulation procedure in a range of temperatures lower than the solidifying point of the thermoplastic resin, adding an alkaline substance to said coagulated slurry in a range of temperatures lower than the aforesaid solidifying point so that the pH of said coagulated slurry is adjusted to a pH 0.1 or more higher than its pH at the time of the coagulation and that the pH of the whole coagulated slurry after the addition of the alkaline substance is adjusted to 7.0 or lower, and then raising the temperature of said coagulated slurry to solidify the coagulated particles.
Inventors
- 👤 Teruhiko Sugimori
- 👤 Noriyuki Tajiri
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 12:27
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/14; C08F6/22
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
90 words
A process for producing a thermoplastic resin by coagulating a thermoplastic resin latex prepared by emulsion polymerization comprising coagulating the latex in a range of temperature lower than the solidifying point of the thermoplastic resin, thereby forming a slurry; adding an alkaline substance to the thus obtained slurry at temperatures lower than said solidifying point to adjust the pH 0.1 or more higher than at the time of coagulation and to a pH to 7 or less, and then raising the temperature of said slurry to solidify the coagulated particles.
Claim 2
Dependent Claim
90 words
A process for producing a thermoplastic resin by coagulating a thermoplastic resin latex prepared by emulsion polymerization comprising coagulating the latex in a range of temperature lower than the solidifying point of the thermoplastic resin, thereby forming a slurry; adding an alkaline substance to the thus obtained slurry at temperatures lower than said solidifying point to adjust the pH 0.1 or more higher than at the time of coagulation and to a pH to 7 or less, and then raising the temperature of said slurry to solidify the coagulated particles.
Claim 3
Dependent Claim
63 words
A process for producing a thermoplastic resin according to claim 1, wherein the thermoplastic resin latex is a polymer latex comprising, as monomer components, butadiene, acrylonitrile and styrene in a total amount of 90% by weight or more, and both the temperature range at the coagulation procedure and the temperature range at the addition of the alkaline substance are 0° to 88° C.
Claim 4
Dependent Claim
64 words
A process for producing a thermoplastic resin according to claim 1, wherein the thermoplastic resin latex is a polymer latex comprising, as monomer components, butadiene, methyl methacrylate and styrene in a total amount of 90% by weight or more, and both the temperature range at the coagulation procedure and the temperature range at the addition of the alkaline substance are 0° to 80° C.
Claim 5
Dependent Claim
95 words
A process for producing a thermoplastic resin according to claim 1, wherein the thermoplastic resin latex is a polymer latex comprising, as monomer components, ethyl acrylate, butyl acrylate or a mixture thereof in an amount of more than 0% by weight and 25% by weight or less and methyl methacrylate, styrene or a mixture thereof in an amount of 75% by weight or more and less than 100% by weight, and both the temperature range at the coagulation procedure and the temperature range at the addition of the alkaline substance are 0° to 92° C.
Claim 6
Dependent Claim
71 words
A process for producing a thermoplastic resin according to claim 1, wherein the thermoplastic resin latex is a polymer latex comprising as monomer components 35 to 45% by weight of butyl acrylate and 65 to 55% by weight of methyl methacrylate, styrene or a mixture thereof, and both the temperature range at the coagulation procedure and the temperature range at the addition of the alkaline substance are 0° to 83° C.
Claim 7
Dependent Claim
75 words
A process for producing a thermoplastic resin according to claim 1, wherein the thermoplastic resin latex comprises a polymer latex obtained by polymerizing 50 to 30% by weight of methyl methacrylate with 50 to 70% by weight of a copolymer latex (solid) comprising butyl acrylate and styrene as monomer components, and both the temperature range at the coagulation procedure and the temperature range at the addition of the alkaline substance are 0° to 92° C.
Claim 8
Dependent Claim
74 words
A process for producing a thermoplastic resin according to claim 1, wherein the thermoplastic resin latex is a polymer latex comprising as monomer components 40 to 60% by weight of butyl acrylate, 10 to 20 parts by weight of acrylonitrile and 30 to 40 parts by weight of styrene, and both the temperature range at the coagulation procedure and the temperature range at the addition of the alkaline substance are 0° to 88° C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-12-11 | 1988-06-11 | 1988-12-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-12-11 | 1992-06-11 | 1992-12-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-12-11 | 1996-06-11 | 1996-12-11 | $7700.00 | Window Closed / Lapsed |