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US4808262A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for devolatilizing polymer solutions

Assignee: General Electric Co
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Filing: 1987-12-07
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Granted: 1989-02-28
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Expires: 2007-12-07
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Abstract

Abstract A method and apparatus for devolatilizing high viscosity polymer solutions are provided wherein high viscosity polymer solutions are heated along a short zone of indirect heat exchange. The residence time within the zone of indirect heat exchange ranges from approximately 5 seconds to 120 seconds.

Inventors

  • 👤 Viney P. Aneja
  • 👤 John P. Skilbeck

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 13:43
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/001; C08F6/003; B; B01; B01D; B01D1/00; B01D1/22; B01D1/221; F; F28; F28D; F28D9/00; F28D9/0012; F28D9/0018; F28F; F28F3/00; F28F3/08; F28F3/086; F28F2250/00; F28F2250/10; F28F2250/102

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 198 words
A method for removing volatile components from a polymer solution comprising at least 25 weight percent polymer, said method comprising: (A) uniformly feeding said solution of polymer through a zone of indirect heat exchange which comprises a plurality of channels, each having a substantially uniform surface to volume ratio in the range of about 4 to 50, height of about 0.05 to 0.5 inches, a width of about 1 to 4 inches, and a length of about 0.5 to 12 inches, wherein the polymer solution is heated in said channels to a temperature above the vaporization temperature of said volatile components and below the boiling point of the polymers within the solution, wherein a uniform pressure of about 2 atmospheres to about 200 atmospheres is applied to the polymer solution in each channel during heating, such that vaporization of the volatile components is substantially prevented while said solution is in the channels; (B) passing the solution from the heat exchange zone into a vaporization chamber at a pressure at which at least 25% of the volatile components of said polymer solution are vaporized upon exiting the zone of indirect heat exchange; and (C) recovering the devolatilized polymer solution.
Claim 2
Independent Claim 198 words
A method for removing volatile components from a polymer solution comprising at least 25 weight percent polymer, said method comprising: (A) uniformly feeding said solution of polymer through a zone of indirect heat exchange which comprises a plurality of channels, each having a substantially uniform surface to volume ratio in the range of about 4 to 50, height of about 0.05 to 0.5 inches, a width of about 1 to 4 inches, and a length of about 0.5 to 12 inches, wherein the polymer solution is heated in said channels to a temperature above the vaporization temperature of said volatile components and below the boiling point of the polymers within the solution, wherein a uniform pressure of about 2 atmospheres to about 200 atmospheres is applied to the polymer solution in each channel during heating, such that vaporization of the volatile components is substantially prevented while said solution is in the channels; (B) passing the solution from the heat exchange zone into a vaporization chamber at a pressure at which at least 25% of the volatile components of said polymer solution are vaporized upon exiting the zone of indirect heat exchange; and (C) recovering the devolatilized polymer solution.
Claim 3
Dependent Claim 29 words
A method as in claim 1 wherein the polymer in solution is selected from the group consisting of polystyrene, polypropylene, polycarbonate, polyphenylene ether, polyetherimide, polyester, polyamide, and blends thereof.
Claim 4
Dependent Claim 29 words
A method as in claim 1 wherein the polymer solution is heated within the zone of indirect heat exchange above the glass transition temperature of the polymers in solution.
Claim 5
Dependent Claim 27 words
A method as in claim 1 wherein the residence time of the polymer solution within said channels falls within the range of about 5 to 120 seconds.
Claim 6
Dependent Claim 18 words
A method as in claim 1 wherein the volatile components are vaporized at a pressure below 50 atmospheres.
Claim 7
Dependent Claim 15 words
A method as in claim 5 wherein the volatile components are vaporized under a vacuum.
Claim 8
Dependent Claim 39 words
A method as in claim 1 wherein each channel has a surface to volume ratio in the range of 5 to 30, a height of from 0.1 to 0.2 inches, and a length of from 3 to 6 inches.
Claim 9
Dependent Claim 22 words
A method as in claim 7 wherein the polymer solution is heated to a temperature in the range of about 150°-350° C.
Claim 10
Dependent Claim 26 words
A method as in claim 8 wherein the residence time of the polymer solution within said channels falls within the range of 5 to 10 seconds.
Claim 11
Dependent Claim 28 words
A method as in claim 1 wherein the polymer in solution is a polystyrene selected from the group consisting of high impact polystyrene, acrylonitrile-butylene-styrene copolymer, and brominated polystyrene.
Claim 12
Dependent Claim 27 words
A method as in claim 10 wherein the solution contains another polymer selected from the group consisting of polyphenylene ether, polycarbonate, polyetherimide, polybutylene terephthalate and polyethylene terephthalate.
Claim 13
Dependent Claim 25 words
A method as in claim 11 wherein the polymer solution is comprised of about 10% to 80% polystyrene and about 10% to 40% polyphenylene ether.
Claim 14
Dependent Claim 18 words
The method of claim 1 wherein substantially all of the volatile components are removed from the polymer solution.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-02-28 1992-08-29 1993-02-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-02-28 1996-08-29 1997-02-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-02-28 2000-08-29 2001-02-28 $7700.00 Window Closed / Lapsed

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