US2008161435A1PendingUtilityA1
Extrusion of a Foamable Fluoropolymer
Est. expiryDec 21, 2026(~0.4 yrs left)· nominal 20-yr term from priority
C08J 9/0066C08J 2201/03C08J 2327/12H01B 3/445
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Claims
Abstract
A process for making an extruded foamable composition is disclosed where the foamable composition includes a partially-crystalline melt processable perfluoropolymer and a foam nucleating package. The process makes a foamed product having uniform foam cell size at high speeds without loss of product quality.
Claims
exact text as granted — not AI-modified1 . An extrusion process comprising:
a) extruding a foamable composition comprising foamed cells wherein 90% of the foamed cells are 50 micrometers in diameter or less, and said foamable composition comprises:
i) a partially-crystalline melt-processible perfluoropolymer, and
ii) a foam nucleating agent ranging from 0.1-10 wt % of the combined weight of said perfluoropolymer and said foam nucleating agent.
2 . The process according to claim 1 , wherein said foam nucleating agent has a foam nucleating effective amount of at least one thermally stable compound which is selected from the group consisting of sulfonic and phosphonic acids and salts thereof.
3 . The process according to claim 1 , wherein said foamable composition is extruded at a speed of greater than 500 ft/m in (150 m/min).
4 . The process according to claim 1 , wherein said perfluoropolymer has a melt flow rate of from about 25 to 35 g/10 min.
5 . The process according to claim 1 , wherein said perfluoropolymer is made by polymerizing monomers selected from the group consisting of tetrafluoroethylene, hexafluoropropylene and perfluoro(alkyl vinyl ether).
6 . The process according to claim 1 , wherein said perfluoropolymer is substantially free of metal ions.
7 . The process according to claim 1 , wherein said perfluoropolymer is polymerized and isolated without the use of metal-ion containing reagents.
8 . The process according to claim 1 , wherein said foamed insulation has a tensile strength of at least 2000 psi and an elongation of at least 200%.
9 . The process according to claim 1 , wherein said perfluoropolymer comprises from about 0.5 to 10 by weight of at least one perfluoro(alkyl vinyl ether).
10 . The process according to claim 1 , wherein said extruded foamable composition has a capacitance coefficient of variation (COV) of no greater than 1%.
11 . The A process according to claim 1 , further comprising providing a self-skinning foamable composition.
12 . The process according to claim 12 , wherein said foamable composition has a void content of 10-50%.
13 . The process according to claim 1 , wherein said foamable composition has a spark resistance of less than 1 spark per 1000 feet (300 m) when tested at 1.5 kV.
14 . The process according to claim 1 , further comprising creating a foamed covering for a substrate.
15 . The process according to claim 1 , further comprising creating a foamed device.
16 . The process according to claim 15 , wherein said foamed device comprises a tube or a sheet.
17 . An extrusion foaming process comprising extruding a foamable composition comprising:
a) a partially-crystalline melt-processible perfluoropolymer, wherein said perfluoropolymer is fluorinated in the melt and b) a foam nucleating package comprising
i) boron nitride,
ii) a synergistic amount of at least one inorganic salt that is thermally stable at the fluoropolymer extrusion temperature, and consists of a metal cation and a polyatomic anion, and satisfies the relationship
0.36×[14-pKa]−0.52≧[ r −0.2 q] 2>0.11×[14−pKa]−0.28
where
R=crystal ionic radius of the cation, in Angstroms
Q=valence of the cation
pKa=−log of Ka for the following reaction
HA −(n−1) <=>H + +A −n
where A is the salt anion, H is hydrogen, and n=absolute value of the valence of the anion; and
iii) a foam nucleating agent of the formula
[Z(CF 2 ) x (CF 2 CFX) p (R′) y (CH 2 ) z RO 3 ] n M
wherein:
Z is selected from CCl 3 , CCl 2 H, H, F, Cl or Br;
each X, independently, is selected from H, F or Cl;
R is selected from sulfur or phosphorus; M is selected from H or a metallic, ammonium, substituted ammonium or quaternary ammonium cation;
x is an integer and is 0 to 10;
p is an integer and is 0 to 6;
y is 0 or 1;
z is an integer and is 0 to 10;
x+y+z+p is a positive integer or, if x+y+z+p is 0, Z is CCl 3 or CCl 2 H;
n is the valence of M; and
R′ is selected from
a C 5-6 perfluorinated alicyclic ring diradical;
a C 1-16 perfluorinated aliphatic polyether diradical with repeat units selected from [CF 2 O], [CF 2 CF 2 O], and [CF 2 CF(CF 3 )O]; and
a substituted or unsubstituted aromatic diradical, in which case, Z is H;
and said foam nucleating package ranges from 0.1-5 wt % of the combined weight of said perfluoropolymer and said foam nucleating package.
18 . The process according to claim 17 , wherein said perfluoropolymer is made by polymerizing monomers selected from the group consisting of tetrafluoroethylene, hexafluoropropylene and perfluoro(alkyl vinyl ether).
19 . The process according to claim 17 , wherein said perfluoropolymer is made by polymerizing monomers selected from the group consisting of tetrafluoroethylene and perfluoro(alkyl vinyl ether).
20 . The process according to claim 16 , wherein said at least one inorganic salt of the foam nucleating package comprises calcium tetraborate.
21 . The process according to claim 16 , wherein said foam nucleating agent of the foam nucleating package comprises Zonyl® BAS.
22 . The process according to claim 16 , wherein said foam nucleating package comprises 91.1±0.5 weight percent boron nitride, 2.5±0.2 weight percent calcium tetraborate, and 6.4±0.2 weight percent Zonyl® BAS of the total weight percent of the foam nucleating package.Cited by (0)
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