US2008113575A1PendingUtilityA1
Solvent stripping process
Est. expiryNov 9, 2026(~0.3 yrs left)· nominal 20-yr term from priority
Inventors:Michael C. Davis
Y10T442/626D01D 10/06D01F 13/04D04H 3/16D01D 10/02Y02P70/62
38
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Claims
Abstract
A process for stripping spinning solvent from a solution-spun nonwoven web by transporting a nonwoven web comprising solvent-laden polymeric fibers having average fiber diameters of less than about 1 micrometer through a solvent stripping zone wherein a solvent stripping fluid heated to at least about 70° C. impinges on the nonwoven web in order to reduce the solvent concentration of the fibers to less than about 10,000 ppmw.
Claims
exact text as granted — not AI-modified1 . A process for stripping chemically bonded spinning solvent from a solution-spun nonwoven web comprising the steps of:
providing a nonwoven web comprising solvent-laden polymeric fibers having average fiber diameters of less than about 1 micrometer, and transporting the nonwoven web through a solvent stripping zone wherein a solvent stripping fluid heated to at least about 70° C. impinges on the nonwoven web in order to reduce the solvent concentration of the fibers to less than about 10,000 ppmw.
2 . The process according to claim 1 wherein the average fiber diameter is less than 0.8 micrometer.
3 . The process according to claim 1 , wherein the solvent stripping fluid is heated to between about 70° C. and the melting point of the fiber polymer.
4 . The process according to claim 1 , wherein the solvent stripping fluid is heated to between about 70° C. and the decomposition point of the fiber polymer.
5 . The process according to claim 1 , wherein the solvent stripping fluid is selected from the group of air, nitrogen, argon, helium, carbon dioxide, hydrocarbons, halocarbons, halohydrocarbons, and mixtures thereof.
6 . The process according to claim 5 , wherein the solvent stripping fluid is air.
7 . The process according to claim 2 , wherein the average fiber diameter is less than 0.5 micrometer.
8 . The process according to claim 1 , wherein the solvent concentration is reduced to less than 1,000 ppmw.
9 . The process according to claim 8 , wherein the solvent concentration is reduced to less than 300 ppmw.
10 . The process according to claim 1 , further comprising transporting the web through the solvent stripping zone by pinning the nonwoven web to a moving porous belt with a vacuum source located on the side of the porous belt opposite the nonwoven web, and passing fresh solvent stripping fluid through the web.
11 . The process according to claim 1 , wherein the nonwoven web is transported through the solvent stripping zone on top of a scrim.
12 . The process according to claim 1 , further comprising passing the nonwoven web through at least one additional solvent stripping zone.
13 . A solution-spun nonwoven web comprising polymeric fibers having average fiber diameters of less than about 1 micrometer and containing less than about 10,000 ppmw of spinning solvent which bonds with the fiber polymer.
14 . The solution-spun nonwoven web of claim 13 , wherein said fibers contain less than about 1000 ppmw of said spinning solvent.
15 . The solution-spun nonwoven web of claim 12 , wherein said fibers contain less than about 300 ppmw of said spinning solvent.
16 . The solution-spun nonwoven web of claim 13 , wherein said polymeric fibers have average fiber diameters of less than 0.5 micrometer.Cited by (0)
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