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US4499249A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing tetrafluoroethylene/fluoro(alkyl vinyl ether) copolymer

Assignee: Daikin Industries Ltd
•
Filing: 1983-04-28
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Granted: 1985-02-12
•
Expires: 2003-04-28
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Abstract

Abstract A process for preparing a tetrafluoroethylene/fluoro(alkyl vinyl ether) copolymer comprising polymerizing tetrafluoroethylene and fluoro(alkyl vinyl ether) in an aqueous suspension system which comprises a mixed medium of water and a fluorohydrocarbon or a chlorofluorohydrocarbon in a volume ratio of from 1:1 to 10:1 at a temperature of from 0 DEG to 25 DEG C. in the presence of a polymerization initiator of the formula: [Cl(CF2)n-COO]2 (I) wherein n is an integer of 1 to 10, the copolymer obtained by the process having a small number of unstable terminal groups and excellent flex life.

Inventors

  • 👤 Shinichi Nakagawa
  • 👤 Tsuneo Nakagawa
  • 👤 Sadaatsu Yamaguchi
  • 👤 Kiyohiko Ihara
  • 👤 Toshihiko Amano
  • 👤 Mitsugu Omori
  • 👤 Kohzoh Asano

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 09:12
CPC Classifications
C; C08; C08F; C08F214/00; C08F214/18; C08F214/26; C08F214/262

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 89 words
A process for preparing a tetrafluoroethylene/fluoro(alkyl vinyl ether) copolymer, comprising: polymerizing tetrafluoroethylene and fluoro(alkyl vinyl ether) selected from the group consisting of perfluoro(methyl vinyl ether), perfluoro(ethyl vinyl ether), perfluoro(propyl vinyl ether), ##STR3## in an aqueous suspension system which comprises a mixed medium of water and a fluorohydrocarbon or a chlorofluorohydrocarbon in a volume ratio of from 1:1 to 10:1 at a temperature of from 0° to 25° C. in the presence of a polymerization initiator of the formula: [Cl(CF.sub.2).sub.n --COO].sub.2 wherein n is an integer of 1 to 10.
Claim 2
Dependent Claim 89 words
A process for preparing a tetrafluoroethylene/fluoro(alkyl vinyl ether) copolymer, comprising: polymerizing tetrafluoroethylene and fluoro(alkyl vinyl ether) selected from the group consisting of perfluoro(methyl vinyl ether), perfluoro(ethyl vinyl ether), perfluoro(propyl vinyl ether), ##STR3## in an aqueous suspension system which comprises a mixed medium of water and a fluorohydrocarbon or a chlorofluorohydrocarbon in a volume ratio of from 1:1 to 10:1 at a temperature of from 0° to 25° C. in the presence of a polymerization initiator of the formula: [Cl(CF.sub.2).sub.n --COO].sub.2 wherein n is an integer of 1 to 10.
Claim 3
Dependent Claim 26 words
The process according to claim 1, wherein the polymerization initiator is a compound of the formula (I) wherein n is an integer of 1 to 4.
Claim 4
Dependent Claim 19 words
The process according to claim 1, wherein the polymerization initiator is a compound of the formula: [ClCF.sub.2 CF.sub.2 COO].sub.2.
Claim 5
Dependent Claim 21 words
The process according to claim 1, wherein the weight ratio of tetrafluoroethylene and fluoro(alkyl vinyl ehter) is from 1:1 to 10:1.
Claim 6
Dependent Claim 21 words
The process according to claim 1, wherein the volume ratio of water and fluorohydrocarbon or chlorofluorohydrocarbon is from 1.5:1 to 5:1.
Claim 7
Dependent Claim 25 words
The process according to claim 1, wherein the fluorohydrocarbon or the chlorofluorohydrocarbon is selected from the group consisting of 1,1,2,-trichloro-1,2,2-trifluoroethane, 1,2-dichloro-1,1,2,2-tetrafluoroethane, trichlorofluoromethane, dichlorodifluoromethane and perfluorocyclobutane.
Claim 8
Dependent Claim 16 words
The process according to claim 1, wherein the reaction temperature is from 5° to 15° C.
Claim 9
Dependent Claim 18 words
The process according to claim 1, wherein the reaction pressure is from 0.5 to 15 kg/cm 2 G.
Claim 10
Dependent Claim 26 words
The process according to claim 8, wherein the polymerization initiator is a compound of the formula (I) wherein n is an integer of 1 to 4.
Claim 11
Dependent Claim 21 words
The process according to claim 1, wherein the weight ratio of the produced copolymer to the solvent is 0.4 or more.

References Cited (Backward Citations)

US2684959A Cited
US2877217A Cited
US3528954A Cited
US3671510A Cited
US3642742A Cited
US4078135A Cited
US4262101A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-02-12 1988-08-13 1989-02-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-02-12 1992-08-13 1993-02-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-02-12 1996-08-13 1997-02-12 $7700.00 Window Closed / Lapsed

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