US4011284A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the manufacture of impact-resistant polyvinyl aromatic compound
Assignee: Shell USA Inc
•
Filing: 1975-06-25
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Granted: 1977-03-08
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Expires: 1995-06-25
Abstract
Abstract A continuous process is described for the manufacture of impact-resistant polyvinyl-aromatic compounds by the bulk polymerization of a vinyl-aromatic monomer in admixture with an elastomeric polymer and in the optional presence of up to 20% by weight of hydrocarbon diluent, calculated on starting vinyl-aromatic monomer. The resulting polyvinyl-aromatic compounds are also described.
Inventors
- 👤 George Gawne
- 👤 Cornelis Ouwerkerk
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 13:34
CPC Classifications
C; C08; C08F; C08F279/00; C08F279/02; C08F291/00; C08F291/02
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
187 words
In the continuous process for the manufacture of an impact-resistant polyvinyl-aromatic compound by the bulk polymerization of a solution of a vinyl-aromatic monomer in admixture with an elastomeric polymer and in the optional presence of up to 20% by weight of hydrocarbon diluent, calculated on the starting vinyl-aromatic monomer, where said solution is successively passed through an agitated pre-polymerication zone, a backmixed intermediate polymerization zone and an unstirred final polymerization zone, the improvement which comprises reacting said solution in an intermediate zone having from 2 to 4 reactors, inclusive, wherein the reaction mixture is maintained in each reactor in substantially homogeneous condition by agitation, and heat of polymerization is removed from each reactor by evaporation of vaporizable components of the mixture, and wherein the monomer conversion in said intermediate zone is advanced from a range of about 20% to about 35% entering the first intermediate reactor to a range of about 65% to about 85% leaving the last intermediate reactor, and controlling the conversion in said intermediate zone so that the difference in the percent of conversion in successive reactors in said zone does not exceed 25%.
Claim 2
Dependent Claim
187 words
In the continuous process for the manufacture of an impact-resistant polyvinyl-aromatic compound by the bulk polymerization of a solution of a vinyl-aromatic monomer in admixture with an elastomeric polymer and in the optional presence of up to 20% by weight of hydrocarbon diluent, calculated on the starting vinyl-aromatic monomer, where said solution is successively passed through an agitated pre-polymerication zone, a backmixed intermediate polymerization zone and an unstirred final polymerization zone, the improvement which comprises reacting said solution in an intermediate zone having from 2 to 4 reactors, inclusive, wherein the reaction mixture is maintained in each reactor in substantially homogeneous condition by agitation, and heat of polymerization is removed from each reactor by evaporation of vaporizable components of the mixture, and wherein the monomer conversion in said intermediate zone is advanced from a range of about 20% to about 35% entering the first intermediate reactor to a range of about 65% to about 85% leaving the last intermediate reactor, and controlling the conversion in said intermediate zone so that the difference in the percent of conversion in successive reactors in said zone does not exceed 25%.
Claim 3
Dependent Claim
12 words
The process of claim 1 where the intermediate zone comprises 3 reactors.
Claim 4
Dependent Claim
12 words
The process of claim 1 where the intermediate zone comprises 2 reactors.
Claim 5
Dependent Claim
11 words
The process of claim 3 where the vinyl-aromatic monomer is styrene.
Claim 6
Dependent Claim
21 words
The process of claim 4 where the elastomeric polymer is a polybutadiene having a cis content of greater than about 40%.
Claim 7
Dependent Claim
11 words
The process of claim 5 where the hydrocarbon diluent is toluene.
Claim 8
Dependent Claim
26 words
The process of claim 6 where the temperatures of the reactors of the intermediate zone are maintained by evaporation between about 140° and about 160° C.
References Cited (Backward Citations)
US3311675A
Cited
US3513145A
Cited
GB1175262A
Cited
US3658946A
Cited
US3639372A
Cited
US3664977A
Cited
US3903202A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-03-07 | 1980-09-06 | 1981-03-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-03-07 | 1984-09-06 | 1985-03-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-03-07 | 1988-09-06 | 1989-03-08 | $7700.00 | Window Closed / Lapsed |