US2011189916A1PendingUtilityA1

Biocomponent fibers with an exterior component comprising polypropylene

Assignee: TOTAL PETROCHEMICALS RES FELUYPriority: Jul 29, 2008Filed: Jul 29, 2009Published: Aug 4, 2011
Est. expiryJul 29, 2028(~2 yrs left)· nominal 20-yr term from priority
D04H 1/5412D04H 3/007D04H 3/16Y10T442/641D01F 8/06D04H 1/544Y10T428/2929D04H 1/54D04H 13/00D01D 5/30
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Claims

Abstract

The present invention relates to bicomponent fibers with improved bonding properties. In particular, the present invention relates to bicomponent fibers comprising an exterior component, which in turn comprises a polypropylene that has been degraded from a first melt flow index MFI 1 (measured according to ISO 1133, condition L, 230° C., 2.16 kg) to a second melt flow index MFI 2 (measured according to ISO 1133, condition L, 230° C., 2.16 kg), such that the degradation ratio MFI 1 /MFI 2 is within a well-defined range and such that the second melt flow index MFI 2 is in the range from 50 dg/min to 300 dg/min. Further, the present invention relates to nonwovens, composites and laminates comprising said bicomponent fibers. The present invention also relates to a process for making such bicomponent fibers, nonwovens, composites and laminates.

Claims

exact text as granted — not AI-modified
1 . Bicomponent fiber comprising
 a) an exterior component covering at least 50% of the surface of the bicomponent fiber, and   b) an interior component comprising a thermoplastic polymer,   wherein the exterior component comprises a polypropylene, which has been degraded chemically or thermally from a first melt flow index MFI 1  (measured according to ISO 1133, condition L, 230° C., 2.16 kg) to a second melt flow index MFI 2  (measured according to ISO 1133, condition L, 230° C., 2.16 kg), such that the second melt flow index MFI 2  is in the range from 50 dg/min to 300 dg/min and such that the degradation ratio MFI 1 /MFI 2  is at least 0.10 and at most 0.80.   
     
     
         2 . Bicomponent fiber according to  claim 1 , wherein the exterior component comprises said polypropylene in at least 50 wt % relative to the total weight of the exterior component. 
     
     
         3 . Bicomponent fiber according to  claim 1 , wherein the exterior component comprises a polypropylene, said polypropylene comprising at least 200 ppm, relative to the weight of said polypropylene, of a primary antioxidant. 
     
     
         4 . Bicomponent fiber according to  claim 3 , wherein the exterior component comprises a polypropylene, said polypropylene comprising at least 200 ppm, relative to the total weight of said polypropylene, of a primary antioxidant and at least 500 ppm, relative to the total weight of said polypropylene, of a secondary antioxidant. 
     
     
         5 . Bicomponent fiber according to  claim 1 , wherein the thermoplastic polymer of the interior component is a polypropylene different from the polypropylene of the exterior component. 
     
     
         6 . Nonwoven comprising the bicomponent fiber of  claim 1 . 
     
     
         7 . Composite and laminate comprising the nonwoven of  claim 6 . 
     
     
         8 . Process for the production of bicomponent fibers comprising the steps of
 a) polymerizing propylene and one or more optional comonomers with a polymerization catalyst to produce a polypropylene having a first melt flow index MFI 1  (measured according to ISO 1133, condition L, 230° C., 2.16 kg),   b) thermally or chemically degrading the polypropylene obtained in step (a) to a second melt flow index MFI 2  (measured according to ISO 1133, condition L, 230° C., 2.16 kg),   c) melting a polypropylene composition comprising the polypropylene obtained in step (b) in a first extruder to form a molten polypropylene composition,   d) melting a thermoplastic polymer composition comprising a thermoplastic polymer in a second extruder to form a molten thermoplastic polymer composition,   e) extruding the molten thermoplastic polymer composition from a number of fine, usually circular, capillaries of a spinneret,   f) extruding the molten polypropylene composition of step (c) from a number of fine openings surrounding said capillaries of step (e), and   g) combining the extrudates of steps (e) and (f) to form a single filament of an intermediate diameter, such that the extrudates of step (f) form an exterior component covering at least 50% of the surface of the so-produced filament,   wherein the polypropylene obtained in step (b) has a second melt flow index MFI 2  (measured according to ISO 1133, condition L, 230° C., 2.16 kg) in the range from 50 dg/min to 300 dg/min and wherein the degradation ratio MFI 1 /MFI 2  is at least 0.10 and at most 0.80.   
     
     
         9 . Process according to  claim 8 , wherein the polypropylene in step (a) is produced by a Ziegler-Natta polymerization catalyst. 
     
     
         10 . Process according to  claim 8 , wherein the exterior component and the interior component are further defined according to  claims 2  to  5 . 
     
     
         11 . Process according to  claim 8 , wherein the process further comprises the step of
 (h) rapidly reducing the intermediate diameter of the filaments extruded in the previous step to a final diameter.   
     
     
         12 . Process according to  claim 8 , wherein the process further comprises the step of
 (i) collecting the filaments obtained in step (g) or (h) on a support, and   (k) subsequently bonding the collected filaments to form a bonded nonwoven.   
     
     
         13 . Process according to  claim 8 , further comprising the step of
 (1-1) laminating a film to the bonded nonwoven obtained in step (k) to form a laminate   
     
     
         14 . Process according to  claim 8 , further comprising the step of
 (1-2) applying a spunbond and/or a meltblown nonwoven to the bonded nonwoven obtained in step (k).   
     
     
         15 . Process according to  claim 8 , wherein the bonded nonwoven is a spunbond nonwoven.

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