US2009264684A1PendingUtilityA1
Fluoroelastomers
Est. expiryJul 30, 2024(expired)· nominal 20-yr term from priority
C07C 21/18C07C 41/54C07C 43/313C07C 68/00C07C 41/48C08F 14/18
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Claims
Abstract
VDF-based curable fluoroelastomers having glass transition temperature lower than −35° C. and an amount of —COF end groups in the polymer lower than the sensitivity limit of the method using the FT-IR spectroscopy described in the present application.
Claims
exact text as granted — not AI-modified1 . A process to obtain the monomer CF 3 OCF 2 OCF═CF 2 comprising the following steps:
I obtainment of the fluoroformate CF 3 OCOF; II reaction of the fluoroformate CF 3 OCOF with elemental fluorine and olefinic compounds having formula:
CAF═CA′F (IV)
for obtaining the fluorohalogenether of formula
CF 3 OCF 2 OCFACF 2 A′ (V)
wherein A and A′, equal to or different the one from the other, are H, Cl or Br, with the proviso that both are not H;
the temperature being between −120° C. and −20° C.;
III removal of the substituents A and A′ from the fluorohalogenether (V).
2 . A process according to claim 1 , wherein in step I the fluoroformate CF 3 OCOF is prepared by reaction of CF 3 OF with CO at temperatures between 80° C. and 250° C.
3 . A process according to claim 1 , wherein in step I the temperature ranges from 120° C. to 230° C.
4 . A process according to claim 1 , wherein in step I the temperature ranges from 150° C. to 200° C.
5 . A process according to claim 1 , wherein in step I the molar ratio CF 3 OF/CO is between 0.1 and 10.
6 . A process according to claim 1 , wherein in step I the molar ratio CF 3 OF/CO is between 0.2 and 5.
7 . A process according to claim 1 , wherein in step I the molar ratio CF 3 OF/CO is between 0.5 and 2.
8 . A process according to claim 1 , wherein in step II it is operated in the presence of a perhalogenated solvent, liquid and inert under the reaction conditions.
9 . A process according to claim 8 , wherein the perhalogenated solvent is an organic compound containing fluorine and/or chlorine.
10 . A process according to claim 8 , wherein the perhalogenated solvent contains one or more oxygen atoms in the chain and/or aminic groups as end group.
11 . A process according to claim 8 , wherein the perhalogenated solvent is perfluorinated.
12 . A process according to claim 11 , wherein the perfluorinated solvent is selected from perfluorocarbons, perfluoroethers, perfluoropolyethers or perfluoroamines, and mixtures thereof.
13 . A process according to claim 1 , wherein in step II fluorine is diluted with an inert gas.
14 . A process according to claim 13 , wherein the inert gas is selected from nitrogen or helium.
15 . A process according to claim 1 , wherein in step I the reaction mixture containing CF 3 OCOF is directly fed, without separation of the mixture components, into the reactor of step II.
16 . A process according to claim 1 , wherein the reactor used in step I is made of glass, inert perfluorinated plastics, or of metal alloys coated inside with glass or with perfluorinated plastics.
17 . A process according to claim 16 , wherein the perfluorinated plastics are selected from PTFE, PFA.Join the waitlist — get patent alerts
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