Fluoropolymer Dispersion Treatment Employing High pH and Oxygen Source to Reduce Fluoropolymer Resin Discoloration
Process for reducing thermally induced discoloration of fluoropolymer resin produced by polymerizing fluoromonomer in an aqueous dispersion medium to form aqueous fluoropolymer dispersion and isolating said fluoropolymer from said aqueous medium to obtain said fluoropolymer resin. The process comprises: adjusting the pH of the aqueous medium of the aqueous fluoropolymer dispersion to greater than about 8.5; and exposing said aqueous fluoropolymer dispersion to an oxygen source.
1 . Process for reducing thermally induced discoloration of fluoropolymer resin, said fluoropolymer resin produced by polymerizing fluoromonomer in an aqueous dispersion medium to form aqueous fluoropolymer dispersion and isolating said fluoropolymer from said aqueous medium to obtain said fluoropolymer resin, said process comprising:
adjusting the pH of the aqueous medium of the aqueous fluoropolymer dispersion to greater than about 8.5; and
exposing said aqueous fluoropolymer dispersion to an oxygen source.
2 . The process of claim 1 wherein said process reduces thermally induced discoloration by at least about 10% as measured by % change in L* on the CIELAB color scale.
3 . The process of claim 1 wherein said aqueous fluoropolymer dispersion contains hydrocarbon surfactant which causes said thermally induced discoloration.
4 . The process of claim 2 wherein said aqueous fluoropolymer dispersion is polymerized in the presence of hydrocarbon surfactant.
5 . The process of claim 1 wherein the pH of the aqueous medium of the aqueous fluoropolymer dispersion is adjusted to about 8.5 to about 11.
6 . The process of claim 1 wherein the pH of the aqueous medium of the aqueous fluoropolymer dispersion is adjusted to about 9.5 to about 10.
7 . The process of claim 1 wherein the pH of the aqueous medium is adjusted by adding an alkali metal hydroxide.
8 . The process of claim 1 wherein said oxygen source is selected from the group consisting of air, oxygen rich gas, ozone containing gas and hydrogen peroxide.
9 . The process of claim 1 wherein the solids content of said dispersion during said exposing to oxygen source is about 2 weight % to about 30 weight %.
10 . The process of claim 1 wherein said exposing the aqueous fluoropolymer dispersion to oxygen source is carried out at a temperature of about 10° C. to about 95° C.
11 . The process of claim 1 wherein said exposing to oxygen source is carried out for a time period of about 5 minutes to about 24 hours.
12 . The process of claim 1 wherein the fluoropolymer resin has an initial thermally induced discoloration value (L*i) at least about 4 L units on the CIELAB color scale below the L* value of equivalent fluoropolymer resin of commercial quality manufactured using ammonium perfluorooctanoate fluorosurfactant.