US4725644A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Tetrafluoroethylene fine powder and preparation thereof
Assignee: EIDP Inc
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Filing: 1986-05-06
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Granted: 1988-02-16
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Expires: 2006-05-06
Abstract
Abstract Tetrafluoroethylene fine powder resins are described which have surprisingly high extrusion pressures and molecular weights which make them useful in post-paste extruded stretching operations. The resins are made by using a permanganate polymerization initiator and controlling its rate of addition.
Inventors
- 👤 Satish C. Malhotra
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 19:49
CPC Classifications
C; C08; C08F; C08F14/00; C08F14/18; C08F14/26; C08F114/00; C08F114/18; C08F114/26
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
158 words
A process for obtaining a tetrafluoroethylene resin which comprises polymerizing tetrafluoroethylene in an aqueous medium in the presence of a substantially non-telogenic anionic surfactant present in an amount which maintains colloidal particles of polymerization product in dispersed form, said process being carried out by contacting tetrafluoroethylene in said aqueous medium in the presence of at least one polymerization initiator defined by the formula XMnO 4 , wherein x is a cation selected from hydrogen, ammonium, alkali metal and alkaline earth metal and wherein the XMnO 4 is added optionally as a precharge, and intermittently or continuously, and where the XMnO 4 last addition occurs so that the reaction slows down and the end point is at least 5% longer in comparison with a reaction where initiator addition is continued to the end of the polymerization; said process being carried out at a temperature of between 50°-125° C., and a pressure of between 15 and 40 kg/cm 2 .
Claim 2
Dependent Claim
158 words
A process for obtaining a tetrafluoroethylene resin which comprises polymerizing tetrafluoroethylene in an aqueous medium in the presence of a substantially non-telogenic anionic surfactant present in an amount which maintains colloidal particles of polymerization product in dispersed form, said process being carried out by contacting tetrafluoroethylene in said aqueous medium in the presence of at least one polymerization initiator defined by the formula XMnO 4 , wherein x is a cation selected from hydrogen, ammonium, alkali metal and alkaline earth metal and wherein the XMnO 4 is added optionally as a precharge, and intermittently or continuously, and where the XMnO 4 last addition occurs so that the reaction slows down and the end point is at least 5% longer in comparison with a reaction where initiator addition is continued to the end of the polymerization; said process being carried out at a temperature of between 50°-125° C., and a pressure of between 15 and 40 kg/cm 2 .
Claim 3
Dependent Claim
10 words
The process of claim 1 wherein no comonomer is present.
Claim 4
Dependent Claim
121 words
The process of claim 1 wherein a comonomer is present and is of the formula ##STR4## wherein R 1 is --R f , --R f --X', or --O--R f or --O--R f --X' in which --R f is a perfluoroalkyl radical of 1-10 carbon atoms, --R f -- is a linear perfluoroalkylenediradical of 1-10 carbon atoms in which the attaching valences are at each end of the linear chain, and X' is H or Cl; R 2 is F, --R f or --R f --X' and R 3 is H or F; or of the formula ##STR5## where Y is ##STR6## X and X' are F or Cl and Z and Z' are each alkyl or fluorinated alkyl of 1-6 carbons.
Claim 5
Dependent Claim
17 words
The process of claim 1, 2 or 3 wherein the initiator XMnO 4 is KMnO 4 .
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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) | 1991-02-15 | 1991-08-17 | 1992-02-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-02-15 | 1995-08-17 | 1996-02-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-02-15 | 1999-08-17 | 2000-02-16 | $7700.00 | Window Closed / Lapsed |