Apparatus, Methods, and Compositions for Producing Oriented Stretch Film In-Process
Apparatus and methods for producing folded edges in a film in-process, and compositions of such film are provided. A method of folding edges includes: separating a first idler roll and a second idler roll by a first distance; positioning a plurality of folding guides between the first idler roll and the second idler roll; separating adjacent sections of film having a majority layer comprising a Ziegler Natta catalyzed linear low density polyethylene copolymer resin having molecules that inherently lack long chain branching, wherein a majority of said molecules are oriented in a substantially longitudinal direction due to an induced strain, and inducing two folds with each folding guide, thereby causing an edge of each section of film to turn under 180° and cling to a bottom surface of the section of film; and moving the adjacent sections of film from the folding guides to the second idler roll.
1 . An apparatus for producing folded edges in a film in-process, the apparatus comprising:
a first idler roll;
a second idler roll separated from the first idler roll by a first distance; and
a plurality of folding guides that are positioned between the first idler roll and the second idler roll, wherein each folding guide separates adjacent sections of film and induces two folds, thereby causing an edge of each section of film to turn under 180° and cling to a bottom surface of the section of the film, as the film travels from the folding guides to the second idler roll;
wherein the film comprises a majority layer comprising a Ziegler Natta catalyzed linear low density polyethylene (LLDPE) copolymer resin having molecules that inherently lack long chain branching, wherein a majority of said molecules are oriented in a substantially longitudinal direction due to an induced strain.
2 . The apparatus of claim 1 , the film further comprising LLDPE copolymer resin blended with other resins chosen from the group consisting of Ziegler Natta catalyzed LLDPE, metallocene catalyzed linear low density polyethylene (m-LLDPE), polyethylenes, polyethylene copolymers, polyethylene terpolymers, polyethylene blends, polypropylenes, polypropylene copolymers, and blends thereof.
3 . The apparatus of claim 1 , the film further comprising a plurality of minority layers and a total film thickness.
4 . The apparatus of claim 3 , further wherein the minority layers comprise resins chosen from the group consisting of Ziegler Natta catalyzed LLDPE, metallocene catalyzed linear low density polyethylene (m-LLDPE), polyethylenes, polyethylene copolymers, polyethylene terpolymers, polyethylene blends, polypropylenes, polypropylene copolymers, and blends thereof.
5 . The apparatus of claim 3 , wherein the minority layers have a thickness ranging from about 0 to about 49 percent of the total film thickness.
6 . The apparatus of claim 5 , wherein the minority layers have a thickness of about 16 percent of the total film thickness.
7 . The apparatus of claim 4 , further wherein the resins comprising the minority layers have a melt index ranging from about 0.5 g/10 min. @ 190° C./2.16 kg to about 12 g/10 min. @ 190° C./2.16 kg.
8 . The apparatus of claim 7 , further wherein the resins comprising the minority layers have a melt index ranging from about 3 g/10 min. @ 190° C./2.16 kg to about 5 g/10 min. @ 190° C./2.16 kg.
9 . The apparatus of claim 4 , further wherein the resins comprising the minority layers have a density ranging from about 0.850 g/cm 3 to about 0.969 g/cm 3 .
10 . The apparatus of claim 9 , further wherein the resins comprising the minority layers have a density of about 0.917 g/cm 3 .
11 . The apparatus of claim 1 , further wherein the majority layer comprises a higher density alpha-olefin LLDPE resin.
12 . The apparatus of claim 1 , further wherein the resin comprising the majority layer has a melt index ranging from about 0.5 g/10 min. @ 190° C. 12.16 kg to about 4 g/10 min. @ 190° C./2.16 kg.
13 . The apparatus of claim 12 , further wherein the resin comprising the majority layer has a melt index ranging from about 0.8 g/10 min. @ 190° C./2.16 kg to about 1.2 g/10 min. @ 190° C./2.16 kg.
14 . The apparatus of claim 1 , further wherein the resin comprising the majority layer has a density ranging from about 0.900 g/cm 3 to about 0.960 g/cm 3 .
15 . The apparatus of claim 14 , further wherein the resin comprising the majority layer has a density of about 0.920 g/cm 3 .
16 . The apparatus of claim 1 , further wherein the Ziegler Natta catalyzed LLDPE copolymer resin has a composition depth breadth index of about less than 70 percent.
17 . The apparatus of claim 16 , further wherein the Ziegler Natta catalyzed LLDPE copolymer resin has a composition depth breadth index of about 30 percent to about 60 percent.
18 . The apparatus of claim 1 , further wherein at least 20 percent of the majority layer comprises the Ziegler Natta catalyzed LLDPE copolymer resin having molecules that inherently lack long chain branching.
19 . A method of folding edges of film in-process, said method comprising:
separating a first idler roll and a second idler roll by a first distance;
positioning a plurality of folding guides between the first idler roll and the second idler roll;
separating adjacent sections of film comprising a majority layer comprising a Ziegler Natta catalyzed linear low density polyethylene (LLDPE) copolymer resin having molecules that inherently lack long chain branching, wherein a majority of said molecules are oriented in a substantially longitudinal direction due to an induced strain, and inducing two folds in the film with each folding guide, thereby causing an edge of each section of film to turn under 180° and cling to a bottom surface of the section of film; and
moving the adjacent sections of film from the folding guides to the second idler roll.
20 . The method of claim 19 , the film further comprising LLDPE copolymer resin blended with other resins chosen from the group consisting of Ziegler Natta catalyzed LLDPE, metallocene catalyzed linear low density polyethylene (m-LLDPE), polyethylenes, polyethylene copolymers, polyethylene terpolymers, polyethylene blends, polypropylenes, polypropylene copolymers, and blends thereof.
21 . The method of claim 19 , the film further comprising a plurality of minority layers and a total film thickness.
22 . The method of claim 21 , further wherein the minority layers comprise resins chosen from the group consisting of Ziegler Natta catalyzed LLDPE, metallocene catalyzed linear low density polyethylene (m-LLDPE), polyethylenes, polyethylene copolymers, polyethylene terpolymers, polyethylene blends, polypropylenes, polypropylene copolymers, and blends thereof.
23 . The method of claim 21 , wherein the minority layers have a thickness ranging from about 0 to about 49 percent of the total film thickness.
24 . The method of claim 23 , wherein the minority layers have a thickness of about 16 percent of the total film thickness.
25 . The method of claim 22 , further wherein the resins comprising the minority layers have a melt index ranging from about 0.5 g/10 min. @ 190° C./2.16 kg to about 12 g/10 min. @ 190° C./2.16 kg.
26 . The method of claim 25 , further wherein the resins comprising the minority layers have a melt index ranging from about 3 g/10 min. @ 190° C./2.16 kg to about 5 g/10 min. @ 190° C./2.16 kg.
27 . The method of claim 22 , further wherein the resins comprising the minority layers have a density ranging from about 0.850 g/cm 3 to about 0.969 g/cm 3 .
28 . The method of claim 27 , further wherein the resins comprising the minority layers have a density of about 0.917 g/cm 3 .
29 . The method of claim 19 , further wherein the majority layer comprises a higher density alpha-olefin LLDPE resin.
30 . The method of claim 19 , further wherein the resin comprising the majority layer has a melt index ranging from about 0.5 g/10 min. @ 190° C.12.16 kg to about 4 g/10 min. @ 190° C./2.16 kg.
31 . The method of claim 30 , further wherein the resin comprising the majority layer has a melt index ranging from about 0.8 g/10 min. @ 190° C./2.16 kg to about 1.2 g/10 min. @ to 190° C./2.16 kg.
32 . The method of claim 19 , further wherein the resin comprising the majority layer has a density ranging from about 0.900 g/cm 3 to about 0.960 g/cm 3 .
33 . The method of claim 32 , further wherein the resin comprising the majority layer has a density of about 0.920 g/cm 3 .
34 . The method of claim 19 , further wherein the Ziegler Natta catalyzed LLDPE copolymer resin has a composition depth breadth index of about less than 70 percent.
35 . The method of claim 34 , further wherein the Ziegler Natta catalyzed LLDPE copolymer resin has a composition depth breadth index of about 30 percent to about 60 percent.
36 . The method of claim 19 , further wherein at least 20 percent of the majority layer comprises the Ziegler Natta catalyzed LLDPE copolymer resin having molecules that inherently lack long chain branching.