Process for making liquid composition of perfluorinated ion exchange polymer, and product thereof
AssigneeE. I. Du Pont de Nemours and Company
InventorWalther G. Grot
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AssigneeE. I. Du Pont de Nemours and Company
InventorWalther G. Grot
Estimating the term…
A process is provided for making a liquid composition of a perfluorinated polymer having sulfonic acid or sulfonate groups in a liquid medium by contacting the polymer with a mixture of 25 to 100% by weight of water and 0 to 75% by weight of a second liquid component such as a lower alcohol, e.g., propanol or methanol, at a temperature of at least 180.degree. C. (at least 240.degree. C. when about 90% to 100% water is used), in a closed system. The liquid composition made by this process, or modified liquid products prepared therefrom, are used in coating various substrates, in casting films, and in repairing perfluorinated ion exchange films and membranes. The process is also useful in recovering perfluorinated polymer having sulfonic acid or sulfonate groups from scrap and used articles made of such polymer or containing such polymer as a component part thereof.
A process for making a liquid composition of a perfluorinated ion exchange polymer having --SO.sub.3 M functional groups wherein M is H, Na, K or NR.sub.4, and each R is separately H, CH.sub.3 or C.sub.2 H.sub.5, in a liquid medium, said liquid composition being liquid at room temperature, said process comprising contacting a said polymer having an equivalent weight in the range of 1025 to 1500 with a mixture comprising 20 to 90% by weight of water and 10 to 80% by weight of at least one member of the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, 2-butanol, 2-methoxyethanol, 2-ethoxyethanol, ethylene glycol dimethyl ether, ehtylene glycol diethyl ether, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, dioxane and acetonitrile at a temperature in the range of about 180.degree. to 300.degree. C. and below the critical temperature(s) of said member(s) employed, for at least 0.5 hour in a closed vessel, and separating from said liquid composition any lower density liquid phase present.
A process for making a liquid composition of a perfluorinated ion exchange polymer having --SO.sub.3 M functional groups, wherein M is H, Na, K or NR.sub.4 where each R separately is H, CH.sub.3 or C.sub.2 H.sub.5, in a liquid medium, said liquid composition being liquid at room temperature, said process comprising contacting a said polymer having an equivalent weight in the range of 1025 to 1500, with a mixture consisting essentially of about 90 to 99% by weight water and about 1 to 10% by weight of at least one member of the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, 2-butanol, 2-methoxyethanol, 2-ethoxyethanol, ethylene glycol dimethyl ether, ethylene glycol diethyl ether, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, dioxane and acetonitrile at a temperature in the range of about 240.degree. to 300.degree. C. for at least 0.5 hour in a closed vessel, and separating from said liquid composition any lower density liquid phase present.
A process for making a liquid composition of a perfluorinated ion exchange polymer having --SO.sub.3 M functional groups wherein M is H, Na, K or NR.sub.4 where each R separately is H, CH.sub.3 or C.sub.2 H.sub.5, in water, said liquid composition being liquid at room temperature, said process comprising contacting a said polymer having an equivalent weight in the range of 1025 to 1500, with water at a temperature in the range of about 240.degree. to 300.degree. C. for at least 0.5 hour in a closed vessel.
A process for separating a first perfluorinated ion exchange polymer having --SO.sub.3 M functional groups wherein M is H, Na, K or NR.sub.4, and each R is separately H, CH.sub.3 or C.sub.2 H.sub.5, said first polymer having an equivalent weight in the range of 1025 to 1250, from a second perfluorinated ion exchange polymer having --COOQ functional groups wherein Q is H, lower alkyl, Na, K or NR.sub.4 where each R is separately H, CH.sub.3 or C.sub.2 H.sub.5, said second polymer having an equivalent weight in the range of 600 to 2000, which process comprises contacting material which contains both said first and second polymers with a liquid consisting essentially of 20 to 100% by weight of water and 0 to 80% by weight of at least one member of the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, 2-butanol, 2-methoxyethanol, 2-ethoxyethanol, ethylene glycol dimethyl ether, ethylene glycol diethyl ether, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, dioxane and acetonitrile at a temperature in the range of about 180.degree. to 300.degree. C. and below the critical temperature of each component member of said liquid, for at least 0.5 hour in a closed vessel, and separating a liquid composition containing said first polymer from remaining solids by filtration or centrifugation.
A process for making a second liquid composition of a perfluorinated ion exchange polymer having --SO.sub.3 H functional groups in a liquid medium, said second liquid composition being liquid at room temperature, said process comprising contacting a perfluorinated ion exchange polymer having --SO.sub.3 M' functional groups, wherein M' is Na, K or NR.sub.4 where each R separately is H, CH.sub.3, or C.sub.2 H.sub.5, and having an equivalent weight in the range of 1025 to 1500, with a mixture consisting essentially of about 20 to 100% by weight water and 0 to about 80% by weight of at least one member of the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, 2-butanol, 2-methoxyethanol, 2-ethyoxyethanol, ethylene glycol dimethyl ether, ethylene glycol diethyl ether, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, dioxane and acetonitrile at a temperature in the range of about 180.degree. to 300.degree. C. and below the critical temperature(s) of said member(s) employed, for at least 0.5 hour in a closed vessel to form a first liquid composition, and then contacting said first liquid composition with a cation exchange resin in acid form to convert said first liquid composition to said second liquid composition.
Dependencies are inferred from the claim text.