Emulsion polymerization of dipolymers of tetrafluoroethylene and 3,3,3-trifluoropropene

Information

  • Patent Application
  • 20070232769
  • Publication Number
    20070232769
  • Date Filed
    February 27, 2007
    17 years ago
  • Date Published
    October 04, 2007
    16 years ago
Abstract
An aqueous semi-batch polymerization process is disclosed for the manufacture of dipolymers of tetrafluoroethylene and 3,3,3-trifluoropropene that contain between 45 and 95 mole percent tetrafluoroethylene and between 5 and 55 mole percent 3,3,3-trifluoropropene.
Description
Claims
  • 1. A semi-batch polymerization process for the manufacture of a dipolymer of tetrafluoroethylene and 3,3,3-trifluoropropene, said process comprising: A) charging a reactor with a quantity of an aqueous solution;B) pressurizing said reactor to a pressure between 0.3 and 10.0 MPa with a first gaseous monomer mixture consisting of between 100 and 95 mole percent tetrafluoroethylene and between 0 and 5 mole percent 3,3,3-trifluoropropene to form a reaction mixture;C) polymerizing said reaction mixture in the presence of a free radical initiator to form a polymer dispersion while maintaining said reactor at said pressure and at a temperature between 25° C. and 130° C.; andD) feeding to said reactor a quantity of a second gaseous monomer mixture at a rate so as to maintain said pressure in said reactor, said second gaseous monomer mixture consisting of between 45 and 95 mole percent tetrafluoroethylene and between 5 and 55 mole percent 3,3,3-trifluoropropene to form a dispersed dipolymer of tetrafluoroethylene and 3,3,3-trifluoropropene.
  • 2. The process of claim 1 wherein said aqueous solution comprises a fluorosurfactant.
  • 3. The process of claim 2 wherein said fluorosurfactant is selected from the group consisting of ammonium perfluorooctanoate, perfluorohexylethylsulfonic acid and ammonium 3,3,4,4-tetrahydrotridecafluorooctanoate.
  • 4. The process of claim 1 further comprising feeding a chain transfer agent to the reactor.
  • 5. The process of claim 1 wherein said pressure is maintained between 0.3 and 3 MPa.
  • 6. The process of claim 1 wherein said temperature is maintained between 30° and 90° C.
  • 7. The process of claim 1 wherein said second gaseous monomer mixture consists of 70 to 85 mole percent tetrafluoroethylene and 15 to 30 mole percent 3,3,3-trifluoropropene.
Provisional Applications (1)
Number Date Country
60788854 Apr 2006 US