US2008113575A1PendingUtilityA1

Solvent stripping process

38
Assignee: DAVIS MICHAEL CPriority: Nov 9, 2006Filed: Nov 9, 2006Published: May 15, 2008
Est. expiryNov 9, 2026(~0.3 yrs left)· nominal 20-yr term from priority
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-modified
1 . 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.

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