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Process for the continuous polymerization of polyethylene terephthalate in the solid phase

Assignee: EIDP Inc
•
Filing: 1980-07-28
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Granted: 1981-06-02
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Expires: 2000-07-28
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Abstract

Abstract Amorphous polyethylene terephthalate can be polycondensed in the solid phase to a higher molecular weight product by a continuous process involving preheating the polymer under forced motion, at least partially crystallizing the preheated polymer in a fixed bed, and polycondensing the polymer in a forced motion reactor at temperatures in the range of 220° to 245° C.

Inventors

  • 👤 Nipun M. Shah

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 02:06
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/78; C08G63/80; B; B01; B01J; B01J8/00; B01J8/08; B01J8/10; B01J2219/00; B01J2219/18; B01J2219/182

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 251 words
In a process for the continuous production of high molecular weight polyethylene terephthalate by polycondensation in the solid phase from a dried granulated polyethylene terephthalate in which the granulated polyethylene terephthalate is first at least partially crystallized following which the partially crystallized material is subjected to polycondensation, the improvement which comprises: (A) first preheating said polymer under forced motion to a temperature in the range of about 180° C. to 200° C. without substantial increase in the intrinsic viscosity of said polymer and while maintaining the crystallinity below about 40%; (B) at least partially crystallizing said preheated polymer in a fixed bed crystallizer by feeding said polymer into said fixed bed at a temperature in the range of about 180° to 200° C., maintaining it in said bed for a time sufficient to raise the crystallization to a value in the range of 40 to 60% while maintaining the intrinsic viscosity of the polymer below about 0.75, and thereafter removing it from said bed at a temperature in the range of about 195° to 215° C.; and (C) effecting said polycondensation under forced motion in an agitated reactor by introducing the product of step (B) into said agitator reactor and raising the temperature thereof to a value in the range of about 220° to 245° for a period of time sufficient to raise the intrinsic viscosity of the polymer to a value of at least 0.70 up to about 1.4, steps (B) and (C) being conducted under a non-reactive gas atmosphere.
Claim 2
Dependent Claim 251 words
In a process for the continuous production of high molecular weight polyethylene terephthalate by polycondensation in the solid phase from a dried granulated polyethylene terephthalate in which the granulated polyethylene terephthalate is first at least partially crystallized following which the partially crystallized material is subjected to polycondensation, the improvement which comprises: (A) first preheating said polymer under forced motion to a temperature in the range of about 180° C. to 200° C. without substantial increase in the intrinsic viscosity of said polymer and while maintaining the crystallinity below about 40%; (B) at least partially crystallizing said preheated polymer in a fixed bed crystallizer by feeding said polymer into said fixed bed at a temperature in the range of about 180° to 200° C., maintaining it in said bed for a time sufficient to raise the crystallization to a value in the range of 40 to 60% while maintaining the intrinsic viscosity of the polymer below about 0.75, and thereafter removing it from said bed at a temperature in the range of about 195° to 215° C.; and (C) effecting said polycondensation under forced motion in an agitated reactor by introducing the product of step (B) into said agitator reactor and raising the temperature thereof to a value in the range of about 220° to 245° for a period of time sufficient to raise the intrinsic viscosity of the polymer to a value of at least 0.70 up to about 1.4, steps (B) and (C) being conducted under a non-reactive gas atmosphere.
Claim 3
Dependent Claim 36 words
A process in accordance with claim 1 in which said polymer in step (A) is amorphous polyethylene terephthalate chip characterized by less than 25% crystallinity and an intrinsic viscosity in the range of 0.40 to 0.70.
Claim 4
Dependent Claim 38 words
A process in accordance with claim 1 in which the residence time of said polymer in said crystallizer in step (B) is at least 10 hours and in which said polymer is crystallized to at least 50% crystallinity.
Claim 5
Dependent Claim 24 words
A process in accordance with claim 1 in which the polymer residence time in the agitator reactor of step (C) is about 4 hours.

References Cited (Backward Citations)

US4064112A Cited
US4064112B1 Cited
US4161578A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-06-01 1984-12-01 1985-06-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-06-01 1988-12-01 1989-06-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-06-01 1992-12-01 1993-06-02 $7700.00 Window Closed / Lapsed

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