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US4268652A
Expired / Lapsed
US
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Color styrene-acrylonitrile polymers
Assignee: Dow Chemical Co
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Filing: 1980-01-16
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Granted: 1981-05-19
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Expires: 2000-01-16
Abstract
Abstract A process for reducing the color of styrene-acrylonitrile polymers comprising polymerizing a feedstream of styrene and acrylonitrile monomers, optionally admixed with a diluent, in the presence of an unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane catalyst, said feedstream being substantially oxygen-free and said feedstream being maintained within a polymerization zone for a limited time.
Inventors
- 👤 Raymond W. Kent, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 13:54
CPC Classifications
C; C08; C08F; C08F212/00; C08F212/02; C08F212/04; C08F212/06; C08F212/08; C08F212/10
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
223 words
In a process for the mass polymerization of a feedstream, said feedstream comprising a monomer composition of from about 20 to about 80 parts by weight of acrylonitrile, from about 80 to about 20 parts by weight of styrene, and from about 0 to about 30 parts by weight of a diluent, said feedstream thereafter being passed into a polymerization zone wherein the feedstream is maintained at a temperature of from about 120° C. to about 170° C. under a pressure of from about 10 to about 300 psi whereby at least a portion of the feedstream is polymerized to form a polymer, said polymer thereafter being subjected to heat and vacuum sufficient to remove at least a major portion of any residual unpolymerized components of the feedstream and diluent, the improvement being the incorporation within the feedstream, as a polymerization initiator, from about 80 to about 700 parts per million parts by weight of the feedstream of an unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane, the attaining and maintaining of a level of oxygen within the feedstream as it is passed into the polymerization zone, while said feedstream is being polymerized, of not greater than about 20 parts by weight per million parts by weight of the feedstream, and the residence time of the feedstream within the polymerization zone being from about 0.7 to about 1.4 hours.
Claim 2
Dependent Claim
223 words
In a process for the mass polymerization of a feedstream, said feedstream comprising a monomer composition of from about 20 to about 80 parts by weight of acrylonitrile, from about 80 to about 20 parts by weight of styrene, and from about 0 to about 30 parts by weight of a diluent, said feedstream thereafter being passed into a polymerization zone wherein the feedstream is maintained at a temperature of from about 120° C. to about 170° C. under a pressure of from about 10 to about 300 psi whereby at least a portion of the feedstream is polymerized to form a polymer, said polymer thereafter being subjected to heat and vacuum sufficient to remove at least a major portion of any residual unpolymerized components of the feedstream and diluent, the improvement being the incorporation within the feedstream, as a polymerization initiator, from about 80 to about 700 parts per million parts by weight of the feedstream of an unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane, the attaining and maintaining of a level of oxygen within the feedstream as it is passed into the polymerization zone, while said feedstream is being polymerized, of not greater than about 20 parts by weight per million parts by weight of the feedstream, and the residence time of the feedstream within the polymerization zone being from about 0.7 to about 1.4 hours.
Claim 3
Dependent Claim
11 words
The process of claim 1 wherein the unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane is 1-tertiary-butylazo-1-cyanocyclohexane.
Claim 4
Dependent Claim
11 words
The process of claim 1 wherein the unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane is 1-tertiary-amylazo-1-cyanocyclohexane.
Claim 5
Dependent Claim
56 words
The process of claim 1 wherein the unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane has the formula ##STR2## wherein R is a tertiary-butyl or a tertiary-pentyl radical, R 1 is a methyl radical, R 2 is an alkyl or an alkoxy C 6 radical, and R 1 and R 2 when considered collectively are part of a single, straight-chain pentenylene moiety.
Claim 6
Dependent Claim
11 words
The process of claim 1 wherein the unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane is 2-tertiary-butylazo-2-cyanobutane.
Claim 7
Dependent Claim
11 words
The process of claim 1 wherein the unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane is 2-tertiary-butylazo-2-cyanopropane.
Claim 8
Dependent Claim
36 words
The process of claim 1 wherein the unsymmetrical tertiary-aliphatic-alpha-cyano-azoalkane is incorporated into the feedstream in an amount of from about 200 to about 500 parts per million parts based upon the total weight of the feedstream.
Claim 9
Dependent Claim
10 words
The process of claim 1 wherein the diluent is ethylbenzene.
Claim 10
Dependent Claim
11 words
The process of claim 1 wherein the admixing diluent is N,N-dimethylformamide.
Claim 11
Dependent Claim
25 words
The process of claim 1 wherein the monomer composition is an admixture with from about 15 to about 25 parts by weight of a diluent.
Claim 12
Dependent Claim
18 words
The process of claim 1 wherein the temperature range is from about 135° C. to about 155° C.
Claim 13
Dependent Claim
17 words
The process of claim 1 wherein the pressure range is from about 100 to about 200 psi.
Claim 14
Dependent Claim
21 words
The process of claim 1 wherein the residence time within the polymerization zone is from about 0.9 to about 1.2 hours.
Claim 15
Dependent Claim
43 words
The process of claim 1 wherein the level of oxygen within the feedstream as it is passed into the polymerization zone, while said feedstream is being polymerized, is not greater than 5 parts by weight per million parts by weight of the feedstream.
Claim 16
Dependent Claim
221 words
In a process for the mass polymerization of a feedstream, said feedstream comprising a monomer composition of from about 20 to about 80 parts by weight of acrylonitrile, from about 80 to about 20 parts by weight of styrene, and from about 15 to about 25 parts by weight of ethylbenzene, said feedstream thereafter being passed into a polymerization zone wherein the feedstream is maintained at a temperature of from about 135° C. to about 155° C. under a pressure of from about 100 to about 200 psi whereby at least a portion of the feedstream is polymerized to form a polymer, said polymer thereafter being subjected to heat and vacuum sufficient to remove at least a major portion of any residual unpolymerized components of the feedstream and diluent, the improvement being the incorporation within the feedstream of from about 200 to about 500 parts per million parts by weight of the feedstream of 1-tertiary-butylazo-1-cyanocyclohexane as a polymerization initiator, the attaining and maintaining of a level of oxygen within the feedstream as it is passed into the polymerization zone, while said feedstream is being polymerized, of not greater than about 5 parts by weight per million parts by weight of the feedstream, and the residence time of the feedstream within the polymerization zone being from about 0.9 to about 1.2 hours.
Claim 17
Dependent Claim
221 words
In a process for the mass polymerization of a feedstream, said feedstream comprising a monomer composition of from about 20 to about 80 parts by weight of acrylonitrile, from about 80 to about 20 parts by weight of styrene, and from about 15 to about 25 parts by weight of ethylbenzene, said feedstream thereafter being passed into a polymerization zone wherein the feedstream is maintained at a temperature of from about 135° C. to about 155° C. under a pressure of from about 100 to about 200 psi whereby at least a portion of the feedstream is polymerized to form a polymer, said polymer thereafter being subjected to heat and vacuum sufficient to remove at least a major portion of any residual unpolymerized components of the feedstream and diluent, the improvement being the incorporation within the feedstream of from about 200 to about 500 parts per million parts by weight of the feedstream of 1-tertiary-butylazo-1-cyanocyclohexane as a polymerization initiator, the attaining and maintaining of a level of oxygen within the feedstream as it is passed into the polymerization zone, while said feedstream is being polymerized, of not greater than about 5 parts by weight per million parts by weight of the feedstream, and the residence time of the feedstream within the polymerization zone being from about 0.9 to about 1.2 hours.
References Cited (Backward Citations)
US3931143A
Cited
US3891609A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-05-18 | 1984-11-17 | 1985-05-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-05-18 | 1988-11-17 | 1989-05-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-05-18 | 1992-11-17 | 1993-05-19 | $7700.00 | Window Closed / Lapsed |