← Back to Patent Explorer
US4027086A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing elastomeric copolymers of vinylidene fluoride and the elastomeric copolymers obtained thereby

Assignee: Montedison SpA
•
Filing: 1975-08-07
•
Granted: 1977-05-31
•
Expires: 1995-08-07
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for preparing new elastomeric copolymers of vinylidene fluoride having exceptionally valuable properties is disclosed. Monomeric mixtures containing vinylidene fluoride in such quantities as to yield elastomeric products are polymerized in solution, emulsion or suspension, or in the absence of solvents and/or dispersants (mass or bulk) in the presence of radical polymerization initiators, at temperatures of -30 DEG C to =200 DEG C, preferably at 0 DEG C to 120 DEG C, and at a pressure of from autonomous pressure to 300 atmospheres. In this process, vinylidene fluoride is fed into the reaction mixture during the polymerization and in a quantity such that the ratio between the added vinylidene fluoride and the vinylidene fluoride of the monomeric mixture subjected to polymerization varies between 0.1 and 1.5.

Inventors

  • 👤 Ernesto Lo Valvo
  • 👤 Gianfranco Diotallevi
  • 👤 Carlo Lagana

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 16:35
CPC Classifications
C; C08; C08F; C08F214/00; C08F214/18; C08F214/22; Y; Y10; Y10S; Y10S526/00; Y10S526/916

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 204 words
A process for preparing elastomeric vinylidene fluoride/tetrafluorethylene/1-hydropentafluoroethylene terpolymers containing between about 68% and about 80% in moles of vinylidene fluoride, by polymerizing the three comonomers in solution, emulsion or suspension, or in the absence of solvents and or dispersants (mass or bulk), in the presence of radical initiators, at a temperature of from -30° C. to +200° C. and under a pressure from the autogenous pressure to 300 atms., said process being characterized in that the feeding of the monomeric mixture to the zone in which the terpolymerization is effected is interrupted intermittently, the monomeric mixture is left to polymerize in said zone until the pressure reaches a value comprised between 1/100 and 9/10 of the pre-fixed, normal polymerization pressure, vinylidene fluoride is then fed into said zone until a pressure value comprised between 11/10 and 19/10 of the pre-fixed normal pressure is reached, the monomers mixture thus obtained is left to polymerize in said zone until the normal pressure is reached, and thereafter feeding of the monomers mixture is resumed, the ratio between the vinylidene fluoride fed to the reaction zone alone, as separate monomer, to the vinylidene fluoride fed in the mixture with tetrafluoroethylene and 1-hydropentafluoroethylene being comprised between 0.1 and 1.5.
Claim 2
Dependent Claim 204 words
A process for preparing elastomeric vinylidene fluoride/tetrafluorethylene/1-hydropentafluoroethylene terpolymers containing between about 68% and about 80% in moles of vinylidene fluoride, by polymerizing the three comonomers in solution, emulsion or suspension, or in the absence of solvents and or dispersants (mass or bulk), in the presence of radical initiators, at a temperature of from -30° C. to +200° C. and under a pressure from the autogenous pressure to 300 atms., said process being characterized in that the feeding of the monomeric mixture to the zone in which the terpolymerization is effected is interrupted intermittently, the monomeric mixture is left to polymerize in said zone until the pressure reaches a value comprised between 1/100 and 9/10 of the pre-fixed, normal polymerization pressure, vinylidene fluoride is then fed into said zone until a pressure value comprised between 11/10 and 19/10 of the pre-fixed normal pressure is reached, the monomers mixture thus obtained is left to polymerize in said zone until the normal pressure is reached, and thereafter feeding of the monomers mixture is resumed, the ratio between the vinylidene fluoride fed to the reaction zone alone, as separate monomer, to the vinylidene fluoride fed in the mixture with tetrafluoroethylene and 1-hydropentafluoroethylene being comprised between 0.1 and 1.5.
Claim 3
Dependent Claim 22 words
The process of claim 1, in which the polymerization is carried out at a temperature of from 0° C. to 120° C.
Claim 4
Dependent Claim 15 words
The process of claim 1, in which the immissions of vinylidene fluoride have periodical frequency.
Claim 5
Dependent Claim 18 words
The process of claim 3, in which the number of vinylidene fluoride immissions varies from 2 to 9.
Claim 6
Dependent Claim 68 words
The process of claim 1 in which, after feeding of the monomeric mixture is interrupted, the remaining monomeric mixture is left to polymerize until the pressure reaches a value comprised between 3/100 and 8/10 of the normal polymerization pressure, after which vinylidene fluoride in the gaseous state is fed into the reactor until the pressure reaches a value comprised between 12/10 and 16/10 of the normal gaseous pressure.
Claim 7
Dependent Claim 80 words
Elastomeric terpolymers of tetrafluoroethylene/1-hydro-pentafluoropropene/vinylidene fluoride, containing from about 68% to about 80% in moles of chemically combined vinylidene fluoride, prepared by the process of claim 1 and characterized by a high frequency of polymeric sequences, essentially consisting of polymerized vinylidene fluoride, the ratio between the frequency of the polymerized vinylidene fluoride sequences determined experimentally by NMR analysis and the theoretical value of the same frequency calculated on the basis of the mean composition of the terpolymer, being greater than 1.
Claim 8
Dependent Claim 21 words
Vulcanizable compositions based on the elastomeric terpolymers of vinylidene fluoride of claim 6 and containing, as vulcanizing agents, aromatic polynucleophil compounds.
Claim 9
Dependent Claim 10 words
Vulcanized products prepared from the vulcanizable compositions of claim 7.

References Cited (Backward Citations)

US3622549A Cited
US3876654A Cited
US3845024A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-05-30 1980-11-29 1981-05-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-05-30 1984-11-29 1985-05-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-05-30 1988-11-29 1989-05-31 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag