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US4028302A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing concentrated acrylonitrile polymer solutions

Assignee: EIDP Inc
•
Filing: 1975-10-07
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Granted: 1977-06-07
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Expires: 1995-10-07
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Abstract

Abstract Clear, bubble-free acrylonitrile polymer solutions of high polymer concentration are rapidly prepared by feeding powdered acrylonitrile polymer to a cool zone of a twin-screw machine and injecting solvent to form a slurry at a temperature below 40° C., advancing the cool slurry to a heated zone and converting the slurry into a concentrated solution at 110° to 150° C. while intermittently squeezing it in directions transverse to the axes of the screws, and discharging the hot solution continuously from the machine. A zone of reduced pressure is provided to remove gases trapped in the slurry. A twin-screw machine for carrying out the process is disclosed.

Inventors

  • 👤 Daniel Gregory Tynan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 13:36
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/02; C08J3/09; C08J3/11; C08J2333/00; C08J2333/18; C08J2333/20

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 190 words
In the preparation of acrylonitrile polymer solutions from polymer powder and an organic solvent selected from the group consisting of dimethylformamide, dimethylacetamide, dimethylsulfoxide and tetramethylenesulfone in a twin-screw machine having temperature-control jackets for providing a cool zone followed by a heated zone; the process for preparing concentrated, clear, bubble-free, acrylonitrile polymer solutions of satisfactory color which comprises continuously feeding the powdered polymer into the cool zone of the twin-screw machine, injecting the organic solvent in a subsequent part of the cool zone at a rate of one to two parts solvent per one part of polymer, mixing the polymer and solvent to form a slurry at a temperature below 40°C., continuously advancing the slurry to the heated zone of the machine, advancing the slurry through a zone of reduced pressure and removing gas released from the slurry, heating the slurry at 110° to 150°C. while intermittently squeezing the slurry in directions transverse to the axes of the screws to provide sharply accelerated flow in directions of the axes, continuing the heating and intermittent squeezing to form a solution at 110° to 150°C., and finally discharging the solution from the machine.
Claim 2
Dependent Claim 190 words
In the preparation of acrylonitrile polymer solutions from polymer powder and an organic solvent selected from the group consisting of dimethylformamide, dimethylacetamide, dimethylsulfoxide and tetramethylenesulfone in a twin-screw machine having temperature-control jackets for providing a cool zone followed by a heated zone; the process for preparing concentrated, clear, bubble-free, acrylonitrile polymer solutions of satisfactory color which comprises continuously feeding the powdered polymer into the cool zone of the twin-screw machine, injecting the organic solvent in a subsequent part of the cool zone at a rate of one to two parts solvent per one part of polymer, mixing the polymer and solvent to form a slurry at a temperature below 40°C., continuously advancing the slurry to the heated zone of the machine, advancing the slurry through a zone of reduced pressure and removing gas released from the slurry, heating the slurry at 110° to 150°C. while intermittently squeezing the slurry in directions transverse to the axes of the screws to provide sharply accelerated flow in directions of the axes, continuing the heating and intermittent squeezing to form a solution at 110° to 150°C., and finally discharging the solution from the machine.
Claim 3
Dependent Claim 23 words
The process defined in claim 1 wherein the slurry is maintained at a temperature below 30°C. in the cool zone of the machine.
Claim 4
Dependent Claim 37 words
The process defined in claim 1 wherein the polymer powder has a mean particle size on the order of 100 microns, with less than 1% of the powder having a particle size of 1 millimeter or greater.
Claim 5
Dependent Claim 11 words
The process defined in claim 1 wherein the solvent is dimethylformamide.

References Cited (Backward Citations)

US3010932A Cited
US3635917A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-06-06 1980-12-06 1981-06-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-06 1984-12-06 1985-06-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-06 1988-12-06 1989-06-07 $7700.00 Window Closed / Lapsed

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