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US3980596A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for reducing filler loss

Assignee: EIDP Inc
•
Filing: 1975-04-11
•
Granted: 1976-09-14
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Expires: 1995-04-11
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Abstract

Abstract The agglomeration of finely-divided granular tetrafluoroethylene polymer particles to produce agglomerated particles having improved flow properties is carried out by agitating the finely-divided particles in an aqueous dispersion containing a substantially water-immiscible organic liquid. The finely-divided particles can first be blended with particulate metal filler material and the blend agglomerated. The presence of a fatty acid or its salt while agitating the aqueous dispersion of the blend of the filler material and the finely-divided tetrafluoroethylene polymer effectively reduces loss of filler during the agglomeration procedure.

Inventors

  • 👤 Glenn Frederick Leverett

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 16:45
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/12; C08J2327/00; C08J2327/02; C08J2327/12

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 231 words
In the process for preparing filled agglomerated granules of non-melt-fabricable granular tetrafluoroethylene polymer in which the filler is a particulate metal-containing filler present in an amount of between about 5 and 40% by volume of the total volume, by agitating a finely-divided blend of said polymer and said filler in which the particle size of the finely-divided tetrafluoroethylene polymer averages numerically between about 5 microns and about 200 microns and in which the filler is present in an amount of between about 5 and 40% by volume, in a two-phase liquid medium consisting essentially of water and an organic liquid which is soluble in water up to at most 15% by weight at the operating temperature of the process and which has a surface tension no greater than about 40 dynes/cm. at 25°C., and in which the organic liquid is present in an amount of 0.1 to 0.5 cc per gram of said blend, followed by separating the resulting agglomerated granules from the liquid medium; the improvement wherein said liquid medium contains an additive selected from a monocarboxylic hydrocarbon acid containing between about 12 and about 20 carbon atoms or its salt in which the cation of the salt is a Group II metal of the Periodic Table, said acid or salt being present in an amount of between 0.01 and 1 part per 1000 parts by weight of water present.
Claim 2
Dependent Claim 231 words
In the process for preparing filled agglomerated granules of non-melt-fabricable granular tetrafluoroethylene polymer in which the filler is a particulate metal-containing filler present in an amount of between about 5 and 40% by volume of the total volume, by agitating a finely-divided blend of said polymer and said filler in which the particle size of the finely-divided tetrafluoroethylene polymer averages numerically between about 5 microns and about 200 microns and in which the filler is present in an amount of between about 5 and 40% by volume, in a two-phase liquid medium consisting essentially of water and an organic liquid which is soluble in water up to at most 15% by weight at the operating temperature of the process and which has a surface tension no greater than about 40 dynes/cm. at 25°C., and in which the organic liquid is present in an amount of 0.1 to 0.5 cc per gram of said blend, followed by separating the resulting agglomerated granules from the liquid medium; the improvement wherein said liquid medium contains an additive selected from a monocarboxylic hydrocarbon acid containing between about 12 and about 20 carbon atoms or its salt in which the cation of the salt is a Group II metal of the Periodic Table, said acid or salt being present in an amount of between 0.01 and 1 part per 1000 parts by weight of water present.
Claim 3
Dependent Claim 12 words
The process of claim 1 wherein the filler is a bronze-containing filler.
Claim 4
Dependent Claim 33 words
The process of claim 2 wherein the agitation is carried out at a temperature of between 0° and 90°C., provided the temperature is not high enough to cause boiling of the liquid medium.
Claim 5
Dependent Claim 14 words
The process of claim 2 wherein the additive is the hydrocarbon acid defined therein.
Claim 6
Dependent Claim 11 words
The process of claim 4 wherein the acid is lauric acid.
Claim 7
Dependent Claim 17 words
The process of claim 2 wherein the additive is the salt of the hydrocarbon acid defined therein.
Claim 8
Dependent Claim 11 words
The process of claim 6 wherein the salt is zinc stearate.

References Cited (Backward Citations)

US3781258A Cited
GB1277808A Cited
US3838064A Cited
US3915916A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-09-14 1980-03-15 1980-09-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-09-14 1984-03-15 1984-09-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-09-14 1988-03-15 1988-09-14 $7700.00 Window Closed / Lapsed

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