US4714756A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for preparing melt processible tetrafluoroethylene copolymer granules
Assignee: EIDP Inc
•
Filing: 1985-10-23
•
Granted: 1987-12-22
•
Expires: 2005-10-23
Abstract
Abstract This invention relates to a process for preparing melt-processible tetrafluoroethylene perfluoro(alkyl vinyl ether) (TFE/PAVE) copolymer granules having good particle flow characteristics and thermal stability, and to the product of the process.
Inventors
- 👤 Marlin D. Buckmaster
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 04:01
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/12; C08F; C08F6/00; C08F6/24; C08J2327/00; C08J2327/02; C08J2327/12; C08J2327/18
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
274 words
A process for treating a slurry of a melt-processible, substantially nonelastomeric copolymer consisting of units of tetrafluoroethylene and perfluoro(alkyl vinyl ether) where the alkyl group is of 1-8 carbon atoms and the ether is present in amounts of between 1 and 10 weight %, which copolymer may contain from between zero to about 5% by weight of at least one additional comonomer represented by the formula: ##STR2## wherein R 1 is --R f or --R f --X in which --R f is perfluoroalkyl radical of 1-12 carbon atoms, --R f -- is a perfluoroalkylene diradical of 1-12 carbon atoms in which the attaching valences are at each end of the chain, and X is H or Cl; and R 2 is --Rf or --R f --X, that was obtained by polymerizing tetrafluoroethylene and perfluoro(alkyl vinyl ether) and any other above-mentioned monomers that may be present in a halocarbon solvent until the copolymer is present in an amount of 5 to 15% by weight, which comprises A. contacting the slurry with water until the slurry water ratio is 1/10 to 2/1 by volume, while agitating the mixture and heating at 20° to 100° C., B. venting the halocarbon solvent while maintaining heat and agitation, C. removing water from the water/copolymer mixture obtained in B and drying the copolymer, D. hardening the copolymer by heating the dried copolymer at a temperature between 25° C. below the differential scanning calorimeter melt onset temperature of the copolymer and the initial melt endotherm peak temperature of the copolymer, until a requisite degree of hardening is obtained as determined by an attrition factor of less than 30 in the copolymer.
Claim 2
Dependent Claim
274 words
A process for treating a slurry of a melt-processible, substantially nonelastomeric copolymer consisting of units of tetrafluoroethylene and perfluoro(alkyl vinyl ether) where the alkyl group is of 1-8 carbon atoms and the ether is present in amounts of between 1 and 10 weight %, which copolymer may contain from between zero to about 5% by weight of at least one additional comonomer represented by the formula: ##STR2## wherein R 1 is --R f or --R f --X in which --R f is perfluoroalkyl radical of 1-12 carbon atoms, --R f -- is a perfluoroalkylene diradical of 1-12 carbon atoms in which the attaching valences are at each end of the chain, and X is H or Cl; and R 2 is --Rf or --R f --X, that was obtained by polymerizing tetrafluoroethylene and perfluoro(alkyl vinyl ether) and any other above-mentioned monomers that may be present in a halocarbon solvent until the copolymer is present in an amount of 5 to 15% by weight, which comprises A. contacting the slurry with water until the slurry water ratio is 1/10 to 2/1 by volume, while agitating the mixture and heating at 20° to 100° C., B. venting the halocarbon solvent while maintaining heat and agitation, C. removing water from the water/copolymer mixture obtained in B and drying the copolymer, D. hardening the copolymer by heating the dried copolymer at a temperature between 25° C. below the differential scanning calorimeter melt onset temperature of the copolymer and the initial melt endotherm peak temperature of the copolymer, until a requisite degree of hardening is obtained as determined by an attrition factor of less than 30 in the copolymer.
Claim 3
Dependent Claim
13 words
The process of claim 1 wherein the copolymerizable comonomer is perfluoro(propyl vinyl ether).
References Cited (Backward Citations)
US3245972A
Cited
US3331822A
Cited
GB1116210A
Cited
US3644319A
Cited
US3553186A
Cited
JPS5017230A
Cited
US4262101A
Cited
US4499249A
Cited
US4675380A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-12-21 | 1991-06-22 | 1991-12-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-12-21 | 1995-06-22 | 1995-12-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-12-21 | 1999-06-22 | 1999-12-22 | $7700.00 | Window Closed / Lapsed |