Process for the production of polyvinylidene fluoride copolymers
AssigneeArkema Inc.
InventorsAndrew KAHN, Brian PETERSON, Yuanqin LIU, Francois BEAUME
Life of this patent
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Abstract
The present application relates to a copolymer comprising recurring units derived from vinylidene fluoride and recurring units derived from a fluorinated monomer M1; said copolymer having a melting temperature Tm defined by the relationship: (154.45−1.9472*x)−3<Tm (° C.)<(154.45−1.9472*x)+3 wherein x is the weight content of said fluorinated monomer MI expressed as percent based on the total weight of said copolymer; the melting temperature being measured by DSC according to the ASTM E794-06 standard test method. The present application also relates to the use of said composition in various technical fields.
Claims25
A copolymer comprising recurring units derived from vinylidene fluoride and recurring units derived from a fluorinated monomer M1;
- said copolymer having a melting temperature Tm defined by the relationship:
- (154.45−1.9472*x)−3<Tm (° C.)<(154.45−1.9472*x)+3
- wherein x is the weight content expressed as percent of said fluorinated monomer M1 based on the total weight of said copolymer;
- the melting temperature being measured by DSC according to the ASTM E794-06 (2018) standard test method;
- wherein the fluorinated monomer M1 is hexafluoropropene and wherein the weight content of hexafluoropropene based on the total weight of said copolymer is lower than 11 wt %.
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A process for preparing a copolymer, comprising the steps of:
- a) Charging to a reactor an initial charge comprising water, surfactant, a fluorinated monomer M1 and adding vinylidene fluoride to the reactor until the operating pressure is reached;
- b) Initiating the polymerization by adding an initiator;
- c) Continuously feeding vinylidene fluoride and optionally the initiator until all the vinylidene fluoride has been added to the reactor to form the copolymer;
- d) Removing the copolymer from the reactor;
- e) Optionally drying the copolymer to form a powder;
- wherein the weight content of said fluorinated monomer M1 introduced in the reactor throughout the process is lower than 11 wt % based on the total weight of vinylidene fluoride and said fluorinated monomer M1 introduced in the reactor throughout the process;
- and wherein the whole amount of said fluorinated monomer M1 used in the process is added to the reactor prior to step b).
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A copolymer comprising recurring units derived from vinylidene fluoride and recurring units derived from a fluorinated monomer M1;
- said copolymer having a melting temperature Tm defined by the relationship:
- (154.45−1.9472*x)−3<Tm (° C.)<(154.45−1.9472*x)+3
- wherein x is the weight content of said fluorinated monomer M1 expressed as percent based on the total weight of said copolymer;
- the melting temperature being measured by DSC according to the ASTM E794-06 (2018) standard test method;
- wherein the fluorinated monomer M1 is hexafluoropropene and wherein the weight content of hexafluoropropene based on the total weight of said copolymer is greater than 17 wt %.
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Dependencies are inferred from the claim text.