Stretch films containing random copolymer polypropylene resins in adjacent layers of a nanolayer structure
A method of producing a stretch film includes at least: extruding a first random copolymer polypropylene (RCPP) resin from a first extruder at a first temperature to at least one primary channel inside of a feedblock; extruding a second RCPP resin from a second extruder at a second temperature to at least one secondary channel, wherein said second temperature is greater than said first temperature; combining the first RCPP resin and the second RCPP resin to create a layered stream using a combining adapter disposed in communication with the feedblock; passing said layered stream from the combining adapter to a die; and passing the layered stream through said die to a casting unit. A multi-layered stretch film includes at least one nanolayer section, the nanolayer section comprising alternating substantially adjacent layers of a first random copolymer polypropylene (RCPP) resin and a second RCPP resin.
1. A method of producing a multi-layered stretch film, said method comprising:
extruding a first random copolymer polypropylene (RCPP) resin from a first extruder at a first temperature to at least one primary channel inside of a feedblock;
extruding a second RCPP resin from a second extruder at a second temperature to at least one secondary channel inside of the feedblock, wherein said second temperature is greater than said first temperature, thereby creating a relative temperature gradient of at least about 30° F.;
combining the first RCPP resin from the at least one primary channel and the second RCPP resin from the at least one secondary channel to create alternating substantially adjacent nanolayers using a combining adapter disposed in communication with the feedblock;
passing said alternating substantially adjacent nanolayers from the combining adapter to a die; and
passing said alternating substantially adjacent nanolayers through said die to a casting unit, thereby forming a nanolayer section of a film web.
2. The method of claim 1 , further comprising extruding the first RCPP resin and the second RCPP resin at the temperature gradient of at least about 80° F.
3. The method of claim 1 , further comprising extruding the first RCPP resin at the first temperature ranging from about 480° F. to about 560° F. and extruding the second RCPP resin at the second temperature ranging from about 510° F. to about 650° F.
4. The method of claim 3 , further comprising extruding the first RCPP resin at the first temperature of about 500° F. and extruding the second RCPP resin at the second temperature of about 580° F.
5. The method of claim 3 , further comprising extruding the first RCPP resin with a melt flow rate ranging from about 8 g/10 min to about 20 g/10 min (I 2 at 230° C.), and extruding the second RCPP resin with a melt flow rate ranging from about 2 g/10 min to about 12 g/10 min (I 2 at 230° C.); further wherein the melt flow rate of the second RCPP resin is less than the melt flow rate of the first RCPP resin.
6. The method of claim 3 , further comprising extruding the second RCPP resin with an ethylene percentage ranging from about 0.7 weight percent ethylene to about 6.0 weight percent ethylene, and extruding the first RCPP resin with an ethylene percentage ranging from about 0.7 weight percent ethylene to about 6.0 weight percent ethylene.
7. The method of claim 3 , further comprising extruding the second RCPP resin with a melting point ranging from about 152° C. to about 163° C., and extruding the first RCPP resin with a melting point ranging from about 152° C. to about 163° C.
8. The method of claim 1 , further comprising:
extruding a third resin from a third extruder to a third channel disposed in communication with the feedblock; and
combining said alternating substantially adjacent nanolayers and said third resin from the third channel to create a layered stream using said combining adapter;
passing said layered stream from the combining adapter to said die; and
passing said layered stream through said die to a casting unit, thereby forming said film web.
9. The method of claim 8 , further comprising extruding said third resin, said third resin including at least one of: Ziegler Natta (ZN) catalyzed linear low density polyethylene (ZN-LLDPE), metallocene catalyzed linear low density polyethylene (m-LLDPE), polyethylenes, polyethylene copolymers, polyethylene terpolymers, polyethylene blends, polypropylenes, polypropylene copolymers, metallocene catalyzed polypropylenes, metallocene catalyzed polypropylene copolymers, and blends thereof.