US2002074691A1PendingUtilityA1

High speed method of making plastic film and nonwoven laminates

30
Priority: Sep 14, 1999Filed: Sep 14, 1999Published: Jun 20, 2002
Est. expirySep 14, 2019(expired)· nominal 20-yr term from priority
Inventors:Robert M. MortelliteThomas G. MushabenPai-Chuan Wu
B29C 48/08B29C 2035/1658B32B 38/1825B32B 37/153B32B 2305/20B32B 2307/7265B32B 2307/724B29C 48/9135B29C 48/914B32B 2305/28B32B 2038/0028B32B 2309/14
30
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Claims

Abstract

Thermoplastic film, microporous film, and laminates thereof, are made at high speeds on the order of about 500 fpm to about 1200 fpm. Bond strengths of film and nonwoven laminates are effectively controlled by air cooling devices which cause the air to flow substantially parallel to the extruded web during drawdown and provide a plurality of cooling air vortices to effectively cool the web. Film gauge control is also achieved by the method.

Claims

exact text as granted — not AI-modified
What is claimed is:  
     
         1 . A high speed method of making a thermoplastic film comprising 
 melting a thermoplastic composition,    extruding a web of said molten thermoplastic composition from a slot die through a cooling zone into a nip of rollers to form a film at a speed on the order of at least about several hundred fpm, and    directing a stream of cooling gas to flow through said zone substantially parallel to the surface of said web to cool the web and form a film without draw resonance.    
     
     
         2 . The method of  claim 1  comprising the further step of enhancing the effectiveness of said cooling gas by creating a plurality of vortices of said gas as the stream moves through said zone to cool the web.  
     
     
         3 . The method of  claim 2  wherein the gas stream moves in the same direction as the web movement.  
     
     
         4 . The method of  claim 2  wherein the gas stream moves in different directions parallel to the movement of the web.  
     
     
         5 . The method of  claim 2  wherein the gas stream moves in a direction opposite to the movement of the web.  
     
     
         6 . The method of  claim 1  comprising introducing a nonwoven fibrous web into said nip of rollers and controlling the temperature and compressive force between the web and the film at the nip to bond the surface of the web to form a laminate d sheet.  
     
     
         7 . The method of  claim 1  wherein the thermoplastic composition is formed by melt blending a thermoplastic polymer and filler particles to form a microporous formable thermoplastic polymer composition, and 
 applying a stretching force to the film at said speed along lines substantially and uniformly across the film and throughout its depth to provide a microporous film.  
 
     
     
         8 . The method of  claim 1  wherein said film is formed at a speed on the order of at least about 500 fpm to about 1200 fpm without draw resonance.  
     
     
         9 . The method of  claim 1  wherein the composition comprises 
 (a) about 30% to about 45% by weight of a linear low density polyethylene,  
 (b) about 1% to about 10% by weight of a low density polyethylene,  
 (c) about 40% to about 60% by weight calcium carbonate filler particles.  
 
     
     
         10 . The method of  claim 9  wherein said melt blended composition consists essentially of about 41% by weight linear low density polyethylene, about 5% by weight low density polyethylene, about 45% by weight calcium carbonate filler particles, and about 5% by weight high density polyethylene.  
     
     
         11 . The method of  claim 10  wherein said melt blended composition further comprises about 3% by weight titanium dioxide and about 1% by weight antioxidant/processing aid.  
     
     
         12 . The method of  claim 1  wherein said nip of rollers comprises a metal embossing roller and a rubber roller and the compresive force between said rollers is controlled to form an embossed film.  
     
     
         13 . The method of  claim 12  comprising introducing a nonwoven fibrous web into said nip of rollers and controlling the compressive force between the web and the film at the nip to bond the surface of the web to the film to form a laminated sheet.  
     
     
         14 . The method of  claim 1  wherein the melt blended composition comprises a thermoplastic polymer containing a dispersed phase of particles selected from the group consisting of an inorganic filler and an organic material and a method comprising the further step of stretching the film to form a laminated microporous sheet.  
     
     
         15 . The method of  claim 1  comprising the further step of stretching a film at said speed to provide a microporous film.  
     
     
         16 . The method of  claim 6  wherein said fibrous web comprises polyolefin fibers.  
     
     
         17 . The method of  claim 16  wherein said fibers are selected from the group consisting of polypropylene, polyethylene, polyesters, cellulose, rayon, nylon, and blends or coextrusions of two or more of such fibers.  
     
     
         18 . The method of  claim 16  wherein the fibrous web has a weight from about 5 to about 70 gms/yd 2  and the microporous film has a thickness on the order of about 0.25 to about 10 mils.  
     
     
         19 . The method of  claim 18  wherein said web is formed from staple fibers or filaments.  
     
     
         20 . The method of  claim 7  wherein said incremental stretching step is conducted at ambient temperature.  
     
     
         21 . The method of  claim 7  wherein said incremental stretching step is conducted at elevated temperature.  
     
     
         22 . The method of  claim 1  wherein said thermoplastic composition is a polymer selected from the group consisting of polyethylene, polypropylene, and copolymers thereof.  
     
     
         23 . The method of  claim 1  wherein said thermoplastic composition is an elastomeric polymer.  
     
     
         24 . The method of  claim 23  wherein said elastomeric polymer is selected from the group consisting of poly(ethylene-butene), poly(ethylene-hexene), poly(ethylene-octene), poly(ethylene-propylene), poly(styrene-butadiene-styrene), poly(styrene-isoprene-styrene), poly(styrene-ethylene-butylene-styrene), poly(ester-ether), poly(ether-amide), poly(ethylene-vinylacetate), poly(ethylene-methylacrylate), poly(ethylene-acrylic acid), poly(ethylene butylacrylate), polyurethane, poly(ethylene-propylene-diene), and ethylene-propylene rubber.  
     
     
         25 . A high speed method of making a microporous thermoplastic film comprising 
 melt blending a composition of 
 (a) about 30% to about 45% by weight of a linear low density polyethylene,  
 (b) about 1% to about 10% by weight of a low density polyethylene,  
 (c) about 40% to about 60% by weight calcium carbonate filler particles,  
   extruding a web of said melt blended composition through a cooling zone into a nip of rollers to form a film at a speed on the order of at least about 500 fpm to about 1200 fpm,    directing a stream of cooling air to flow through said zone substantially parallel to said web surface to cool the web and form a film without draw resonance, and    enhancing the effectiveness of said cooling gas by creating a plurality of vortices of said gas as said stream moves through said zone to cool the web.    
     
     
         26 . The method of  claim 25  comprising the further step of applying an incremental stretching force to said film at said speed along lines substantially and uniformly across said film and throughout its depth to provide a microporous film.  
     
     
         27 . The method of  claim 25  comprising introducing a nonwoven fibrous web into said nip of rollers and controlling the temperature and compressive force between the web and the film at the nip to bond the surface of the web to form a laminated sheet.  
     
     
         28 . The method of  claim 25  wherein said melt composition further contains high density polyethylene and titanium dioxide.  
     
     
         29 . The method of  claim 28  wherein the high density polyethylene is contained in an amount of 5% by weight and the titanium dioxide is contained in an amount of about 3% by weight.  
     
     
         30 . The method of  claim 25  wherein said linear low density polyethylene is selected from the group consisting of poly(ethylene-butene), poly(ethylene-hexene), poly(ethylene-octene), poly(ethylene-propylene), poly(styrene-butadiene-styrene), poly(styrene-isoprene-styrene), poly(styrene-ethylene-butylene-styrene), poly(ester-ether), poly(ether-amide), poly(ethylene-vinylacetate), poly(ethylene-methylacrylate), poly(ethylene-acrylic acid), poly(ethylene butylacrylate), polyurethane, poly(ethylene-propylene-diene), and ethylene-propylene rubber.  
     
     
         31 . The method of  claim 27  wherein said fibers are selected from the group consisting of polypropylene, polyethylene, polyesters, cellulose, rayon, nylon, and blends of coextrusions of two or more such fibers.  
     
     
         32 . The method of  claim 31  wherein the fibrous web has a weight of from about 5 to about 70 grams/yd  2  and the microporous film has a thickness on the order of about 0.25 to about 10 mils.  
     
     
         33 . The method of  claim 25  wherein said incremental stretching step is conducted at ambient temperature.  
     
     
         34 . The method of  claim 25  wherein said incremental stretching step is conducted at an elevated temperature.

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