Multilayer blown films for shrink applications

1. A process for producing a multilayer blown film, the process comprising:

(i) introducing into a blown film coextrusion die:

(a) a core layer flow having a first side and a second side, the core layer flow comprising an ethylene polymer characterized by:

a MI in a range from about 0.01 to about 2 g/10 min;

a ratio of HLMI/MI in a range from about 50 to about 300; and

a ratio of Mw/Mn in a range from about 5 to about 30;

(b) an inner layer flow positioned on the first side of the core layer flow, the inner layer flow comprising a first conjugated diene monovinylarene block copolymer; and

(c) an outer layer flow positioned on the second side of the core layer flow, the outer layer flow comprising a second conjugated diene monovinylarene block copolymer; and

(ii) blowing a coextruded flow exiting the die at a blow-up ratio in a range from about 1.5 to about 4 to produce the multilayer blown film;

wherein the multilayer blown film has a MD shrink greater than about 60% and a CD shrink in a range from 0% to about 15% at 150° C.

2. The process of claim 1 , wherein the blow-up ratio is in a range from about 2 to about 3.

3. The process of claim 1 , wherein the process does not comprise a double-bubble orientation step, a machine direction orientation step, or a tenter frame orientation step.

4. The process of claim 1 , wherein the multilayer blown film has a MD shrink in a range from about 65% to about 90% and a CD shrink in a range from about 1% to about 10% at 150° C.

5. The process of claim 1 , wherein the multilayer blown film has a MD:CD shrink ratio in a range from about 4:1 to about 30:1 at 150° C.

6. The process of claim 1 , wherein the ethylene polymer is an ethylene/α-olefin copolymer.

7. The process of claim 6 , wherein the ethylene/α-olefin copolymer is characterized by:

a MI in a range from about 0.1 to about 0.5 g/10 min;

a ratio of HLMI/MI in a range from about 60 to about 140;

a Mw in a range from about 75,000 to about 500,000 g/mol;

a ratio of Mw/Mn in a range from about 7 to about 15; and

a density in a range from about 0.88 to about 0.94 g/cm 3 .

8. The process of claim 1 , wherein:

the first conjugated diene monovinylarene block copolymer has from about 55 to about 95 weight percent monovinylarene monomer content, based on the total weight of the block copolymer; and

the second conjugated diene monovinylarene block copolymer has from about 55 to about 95 weight percent monovinylarene monomer content, based on the total weight of the block copolymer.

9. The process of claim 8 , wherein:

the first conjugated diene monovinylarene block copolymer comprises a first styrene butadiene block copolymer; and

the second conjugated diene monovinylarene block copolymer comprises a second styrene butadiene block copolymer.

10. The process of claim 1 , wherein:

the inner layer flow further comprises a general purpose polystyrene, a high impact polystyrene, a cyclic olefin copolymer, a styrene isoprene styrene copolymer, a styrene ethylene-butylene styrene polymer, or any combination thereof;

the outer layer flow further comprises a general purpose polystyrene, a high impact polystyrene, a cyclic olefin copolymer, a styrene isoprene styrene copolymer, a styrene ethylene-butylene styrene polymer, or any combination thereof;

or both.

11. The process of claim 1 , wherein the multilayer blown film further comprises an additive selected from an antioxidant, an acid scavenger, an antiblock additive, a slip additive, a colorant, a filler, a polymer processing aid, a UV inhibitor, or any combination thereof.

12. The process of claim 1 , wherein the inner layer flow and the outer layer flow comprise different polymers or blends of polymers.

13. A process for producing a multilayer blown film, the process comprising:

(i) introducing into a blown film coextrusion die:

(a) a core layer flow having a first side and a second side, the core layer flow comprising an ethylene polymer, wherein the ethylene polymer is an ethylene/1-butene, ethylene/1-hexene, or ethylene/1-octene copolymer characterized by:

a MI in a range from about 0.01 to about 2 g/10 min;

a ratio of HLMI/MI in a range from about 50 to about 300; and

a ratio of Mw/Mn in a range from about 5 to about 30;

(b) an inner layer flow positioned on the first side of the core layer flow, the inner layer flow comprising a first conjugated diene monovinylarene block copolymer; and

(c) an outer layer flow positioned on the second side of the core layer flow, the outer layer flow comprising a second conjugated diene monovinylarene block copolymer; and

(ii) blowing a coextruded flow exiting the die at a blow-up ratio in a range from about 1.5 to about 4 to produce the multilayer blown film;

wherein the multilayer blown film has a MD shrink greater than about 60% and a CD shrink in a range from 0% to about 15% at 150° C.

14. The process of claim 13 , wherein the multilayer blown film has a MD:CD shrink ratio in a range from about 4:1 to about 30:1 at 150° C.

15. The process of claim 13 , wherein the blow-up ratio is in a range from about 2 to about 3.

16. The process of claim 13 , wherein the process does not comprise a double-bubble orientation step, a machine direction orientation step, or a tenter frame orientation step.

17. The process of claim 13 , wherein the ethylene/1-butene, ethylene/1-hexene, or ethylene/1-octene copolymer is characterized by:

a MI in a range from about 0.1 to about 0.5 g/10 min;

a ratio of HLMI/MI in a range from about 60 to about 140; and

a ratio of Mw/Mn in a range from about 7 to about 15.

18. The process of claim 13 , wherein the ethylene/1-butene, ethylene/1-hexene, or ethylene/1-octene copolymer is characterized by:

a MI in a range from about 0.1 to about 0.5 g/10 min;

a ratio of HLMI/MI in a range from about 60 to about 140;

a Mw in a range from about 75,000 to about 500,000 g/mol;

a ratio of Mw/Mn in a range from about 7 to about 15; and

a density in a range from about 0.88 to about 0.94 g/cm 3 .

19. The process of claim 13 , wherein the multilayer blown film has:

a MD shrink in a range from about 65% to about 90%;

a CD shrink in a range from 1% to about 10%;

an average film thickness in a range from about 0.5 to about 5 mils;

a haze of less than about 10%;

a 60° gloss of greater than about 100%; and

a 1% MD secant modulus greater than about 50,000 psi.

20. The process of claim 13 , wherein:

the first conjugated diene monovinylarene block copolymer has from about 55 to about 95 weight percent monovinylarene monomer content, based on the total weight of the block copolymer, and the first conjugated diene monovinylarene block copolymer comprises a first styrene butadiene block copolymer; and

the second conjugated diene monovinylarene block copolymer has from about 55 to about 95 weight percent monovinylarene monomer content, based on the total weight of the block copolymer, and the second conjugated diene monovinylarene block copolymer comprises a second styrene butadiene block copolymer.