US4362852A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Devolatilizing molten polymer with a rotary disk processor
Assignee: Honeywell International Inc
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Filing: 1981-09-16
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Granted: 1982-12-07
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Expires: 2001-09-16
Abstract
Abstract This invention is an improved process to remove volatiles from molten synthetic, preferably fiber forming relatively high viscosity polymers which comprises passing molten polymer through a rotary disk polymer processor at a temperature of between 260° C. and 300° C. at a rate of between about 10 and 75 pounds (4.5 and 34 kg) per hour per square foot (0.093 m 2 ) of processor filming area, at a rotational rate of between about 5 and 75 rpm for the disks, and a processor having between 1 and 20 stages.
Inventors
- 👤 David Pendlebury
- 👤 Hugh H. Rowan
- 👤 Edward J. Buyalos
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 20:11
CPC Classifications
C; C08; C08G; C08G69/00; C08G69/02; C08G69/26; C08G69/28; C08G63/00; C08G63/88; C08G69/46
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
86 words
In a process to remove volatiles from molten synthetic, relatively high viscosity polymers the improvement comprising passing the molten polymer through a rotary disc polymer processor at a temperature of between about 260° C. and 300° C., at a rate of between about 10 and 75 pounds per hour per square foot (48.9 to 367 kg/hr/m 2 ) of processor filming area, at a rotational rate of between about 5 and 75 rpm of the disks, and said processor having between about one and twenty stages.
Claim 2
Dependent Claim
86 words
In a process to remove volatiles from molten synthetic, relatively high viscosity polymers the improvement comprising passing the molten polymer through a rotary disc polymer processor at a temperature of between about 260° C. and 300° C., at a rate of between about 10 and 75 pounds per hour per square foot (48.9 to 367 kg/hr/m 2 ) of processor filming area, at a rotational rate of between about 5 and 75 rpm of the disks, and said processor having between about one and twenty stages.
Claim 3
Dependent Claim
19 words
The process of claim 1 wherein the polymer is selected from the group consisting of fiber-forming nylon and polyester.
Claim 4
Dependent Claim
91 words
The process of claim 2 wherein the polyester is polyethylene terephthalate having an intrinsic viscosity above 0.72 and containing about 15 to 30 carboxyls per million grams of polymer before processing, the pressure in the processor is between about 5 and 10 Torr (5 and 10 mm Hg), the film thickness of the polyester in the processor is between about 0.025 and 0.050 inch (0.0625 and 0.125 cm) and additional reactive materials are also fed into the processor with the polyester in order to lower the carboxyl level of the polymer.
Claim 5
Dependent Claim
91 words
The process of claim 3 wherein the reactive additive is ethylene carbonate with a catalyst, added in excess so that the carboxyl content of the polyester is lowered to between about 2 and 5, the reaction by-product carbon dioxide gas is removed by the processor, the excess of ethylene carbonate is vaporized and removed by the processor so the residual amount of ethylene carbonate in the polyester is between about 75 and 125 ppm and the residual amount of carbon dioxide in the polyester is between about 25 and 75 ppm.
Claim 6
Dependent Claim
41 words
The process of claim 4 wherein the viscosity of the feed polymer to the processor is between about 0.94 to about 0.97 intrinsic viscosity, and the viscosity of the polymer exiting the processor is between about 0.90 to 0.92 intrinsic viscosity.
Claim 7
Dependent Claim
54 words
The process of claim 5 wherein the processor feeds into a spinning apparatus to spin the polyester into fiber and said processor is located within a few feet of said spinning apparatus so that the low carboxyl level is maintained at below 10 per 10 6 grams in the fiber spun from the polyester.
Claim 8
Dependent Claim
100 words
The process of claim 2 wherein the nylon is poly-epsilon-caprolactam fed to the processor containing between about 6 to 12 percent by weight of monomer and oligomers, having a relative viscosity of above 35, the pressure in the processor is between 2 and 100 Torr (2 and 100 mm Hg), the thickness of the polymer film in the processor is between about 0.005 and 0.15 inch (0.0125 and 0.375 cm), and said monomers and oligomers are vaporized and removed by the processor so that only between about 2 to 5 percent by weight remain in the polymer exiting the processor.
Claim 9
Dependent Claim
38 words
The method of claim 7 wherein the processor is multistaged and the pressure is about 100 Torr (100 mm Hg) at the initial stage of the processor and about 5 Torr at the final stage of the processor.
Claim 10
Dependent Claim
97 words
The method of claim 7 wherein the feed temperature is between about 265° and 275° C., the feed rate is between about 25 and 35 pounds per hour per square foot (122.3 to 171.2 kg/hr/m 2 ) of processor filming area, the processor temperature is maintained at between about 265° C. and 275° C., the overall low pressure is between about 4 and 7 Torr (4 and 7 mm Hg), the processor disk rotation is between about 15 and 25 rpm and the processor film thickness is between about 0.02 and 0.03 inch (0.05 and 0.75 cm).
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-12-06 | 1986-06-07 | 1986-12-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-12-06 | 1990-06-07 | 1990-12-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-12-06 | 1994-06-07 | 1994-12-07 | $7700.00 | Window Closed / Lapsed |