US2004158015A1PendingUtilityA1
Process for the high-pressure polymerization of 1,1-difluoroethylene
Priority: Sep 26, 2000Filed: Feb 4, 2004Published: Aug 12, 2004
Est. expirySep 26, 2020(expired)· nominal 20-yr term from priority
Inventors:Thierry Senninger
C08F 14/22
44
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Claims
Abstract
The invention relates to a continuous process for the manufacture of PVDF homopolymer or copolymer. The optional comonomer comprises a vinyl group polymerized by free radicals, and comprises at least one fluorine atom, a fluoroalkyl group or a fluoroalkoxy group, directly attached to this vinyl group. The invention also relates to PVDF homopolymers made by processes of the invention. The invention further relates to a process for deoxygenating a flow.
Claims
exact text as granted — not AI-modified1 . A process for deoxygenating a flow comprising at least one fluoro monomer selected from VF2 and monomers comprising a vinyl group polymerizable by free radicals and at least one fluorine atom, a fluoroalkyl group or a fluoroalkoxy group, directly attached to this vinyl group, said process comprising placing this flow in contact with (i) a sufficient amount of a catalyst whose active sites are elements belonging to groups 8 to 11 of the Periodic Table of the Elements and (ii) for a period which is sufficient to obtain the desired oxygen content.
2 . A process according to claim 1 , wherein the support for the active sites is a mineral of alumina, silica, a zeolite or an aluminosilicate.
3 . A process according to claim 2 , wherein the catalyst comprises 0.05-5% by weight of the active element.
4 . A process according to claim 1 , wherein the temperature is 0-200° C.
5 . A process according to claim 1 , wherein the temperature is 50° C.-100° C.
6 . A process according to claim 1 , wherein the active element is copper or palladium.
7 . A process according to claim 1 , wherein the flow of deoxygenated VF2 and of optional comonomer comprises less than 5 ppm of oxygen.
8 . A process according to claim 1 , wherein the oxygen content is less than 1 ppm.
9 . A flow comprising less than 5 ppm of oxygen, and at least one fluoro monomer selected from VF2 and monomers comprising a vinyl group self polymerizable by free radicals, wherein the monomer comprises at least one fluorine atom, a fluoroalkyl group or a fluoroalkoxy group directly attached to this vinyl group.
10 . A flow according to claim 9 , comprising less than 1 ppm of oxygen.
11 . A PVDF, optionally comprising from 0 to 50% of comonomers, having a melt flow index, measured at 230° C. under a 5 kg load, of greater than 50 g/10 min according to ASTM D-1238.
12 . A PVDF according to claim 11 , having a melt flow index, of greater than 100 g/10 min according to ASTM D-1238.
13 . A PVDF according to claim 11 , having a melt flow index, of greater than 200 g/l 0 min according to ASTM D-1238.
14 . A PVDF according to claim 11 , having a melt flow index, of greater than 400 g/10 min according to ASTM D-1238.
15 . A PVDF homopolymer with a level of defects, measured by fluorine NMR, of greater than 6%.
16 . A PVDF homopolymer according to claim 15 , with a level of defects, measured by fluorine NMR, of greater than 7%.
17 . A PVDF homopolymer with an elastic modulus (at 23° C., according to ASTM D-1708) of between 1020 and 650 MPa.
18 . A PVDF homopolymer according to claim 17 , with an elastic modulus (at 23° C., according to ASTM D-1708) of less than 1000 MPa.
19 . A PVDF homopolymer according to claim 17 , with an elastic modulus (at 23° C., according to ASTM D-1708) of less than 900 MPa.
20 . A PVDF homopolymer according to claim 17 , with an elastic modulus (at 23° C., according to ASTM D-1708) of less than 800 MPa.
21 . A PVDF homopolymer according to claim 17 , with an elastic modulus (at 23° C., according to ASTM D-1708) of less than 700 MPa.
22 . A PVDF with an Mw/Mn ratio of 1.5-1.9.Join the waitlist — get patent alerts
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