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This disclosure relates to a process for extracting a perfluoropolyether. The process involves: (a) contacting a solvent comprising a liquid or supercritical carbon dioxide with a lubricating grease comprising a thickener, an extraction aid material, and the perfluoropolyether in an extraction zone

This disclosure relates to a process for extracting a perfluoropolyether. The process involves: (a) contacting a solvent comprising a liquid or supercritical carbon dioxide with a lubricating grease comprising a thickener, an extraction aid material, and the perfluoropolyether in an extraction zone to form an extraction solution comprising an extracted perfluoropolyether; and (b) recovering the extracted perfluoropolyether from the extraction solution; wherein the recovered extracted perfluoropolyether comprises no more than about 2 wt % of the thickener.

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1. A process for extracting a perfluoropolyether from lubricating grease, comprising: (a) contacting a solvent comprising a liquid or supercritical carbon dioxide with the lubricating grease, wherein the lubricating grease comprises a thickener, extraction aid material, and the perfluoropolyether in

1. A process for extracting a perfluoropolyether from lubricating grease, comprising: (a) contacting a solvent comprising a liquid or supercritical carbon dioxide with the lubricating grease, wherein the lubricating grease comprises a thickener, extraction aid material, and the perfluoropolyether in an extraction zone to form an extraction solution comprising an extracted perfluoropolyether and wherein the extracted perfluoropolyether comprises unfunctionalized perfluoropolyether and optionally functionalized perfluoropolyether, the functionalized perfluoropolyether if present being present in an amount of no more than 10 wt % based on the total amount of perfluoropolyether; and(b) recovering the extracted perfluoropolyether from the extraction solution; wherein the recovered extracted perfluoropolyether comprises no more than about 2 wt % of the thickener;wherein the yield of the extracted perfluoropolyether is at least about 75 wt %. 2. The process of claim 1, wherein the recovered extracted perfluoropolyether comprises no more than about 0.1 wt % of the thickener. 3. The process of claim 1, wherein the thickener is selected from the group consisting of PTFE, FEP, PFA, MFA, ETFE, PCTFE, ECTFE, PVDF, and combinations thereof. 4. The process of claim 3, wherein the thickener is PTFE. 5. The process of claim 1, wherein the thickener is selected from the group consisting of talc, silica, clay, boron nitride, titanium dioxide, silicon nitride, and combinations thereof. 6. The process of claim 1, wherein the thickener is selected from the group consisting of metal soaps, melamine cyanurate, urea, polyureas, polyurethanes, polyolefins, and combinations thereof. 7. The process of claim 6, wherein the metal soap is selected from the group consisting of lithium soaps, sodium soaps, lithium complex soaps, calcium sulfonates, aluminum soaps, and combinations thereof. 8. The process of claim 1, wherein the weight ratio of the solvent to the lubricating grease is no more than about 50. 9. The process of claim 1, wherein the solvent comprises supercritical carbon dioxide. 10. The process of claim 9, wherein the extraction zone has a temperature and wherein the temperature in the extraction zone is from about 40° C. to about 110° C. 11. The process of claim 9, wherein the extraction zone has a temperature and wherein the temperature in the extraction zone is from about 70° C. to about 90° C. 12. The process of claim 9, wherein the extraction zone has a pressure and wherein the pressure in the extraction zone is from about 1500 psig to about 6000 psig. 13. The process of claim 9, wherein the extraction zone has a pressure and wherein the pressure in the extraction zone is from about 4000 psig to about 5000 psig. 14. The process of claim 1, wherein the solvent comprises liquid carbon dioxide. 15. The process of claim 14, wherein the extraction zone has a temperature and wherein the temperature in the extraction zone is from about 25° C. to less than 31.1° C. 16. The process of claim 1, wherein the yield of the extracted perfluoropolyether is at least about 90 wt %. 17. The process of claim 1, wherein the recovered extracted perfluoropolyether is further purified by an adsorbing agent. 18. The process of claim 1, wherein the extraction aid material comprises a material selected from the group consisting of diatomaceous earth, perlite, and cellulose materials. 19. The process of claim 1, wherein the extraction aid material is selected from the group consisting of particles, powders, fibers, fibrils, filaments, string, thread, wire and yarn. 20. The process of claim 1, wherein the weight ratio of the lubricating grease to the extraction aid material is from about 10:1 to about 1:10.