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A high strength, flexible crosslinked polyethylene (PEX) material is provided wherein the base polymer is intermixed with a polymer modifier which affects the amorphous region of the polymer, leaving the crystalline portion of the base polymer virtually unaffected. Consequently, the amorphous region

A high strength, flexible crosslinked polyethylene (PEX) material is provided wherein the base polymer is intermixed with a polymer modifier which affects the amorphous region of the polymer, leaving the crystalline portion of the base polymer virtually unaffected. Consequently, the amorphous region's density is lowered, resulting in a more flexible final product, while the crosslinked molecular structure and/or crystalline portion of the polymer, which controls the strength of the base polymer, remains strong. The polymer modifier can comprise a hydrocarbon fluid such as PAO, Group III basestocks, or a gas-to-liquid hydrocarbon. A method for producing the plastic material is also provided. The plastic material has particular utility in the production of tubing, piping, and conduits for transporting gases, liquids, and the like, as well as wire and cable coatings such as jacketing and insulation.

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1. A composition comprising crosslinked polyethylene (PEX) prepared by the method comprising: blending a polyethylene resin with a flexibilizing amount of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 3000 cSt at 100° C., pour poin

1. A composition comprising crosslinked polyethylene (PEX) prepared by the method comprising: blending a polyethylene resin with a flexibilizing amount of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 3000 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, and flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP;wherein the blend comprises less than 10 wt % of a propylene polymer having a melting point of 40° C. or more, by weight of the blend;processing the blend into a shape of an article;crosslinking the blend in the form of the shape. 2. The composition of claim 1 wherein the polyethylene resin comprises an ethylene based polymer comprising at least 50 mole % ethylene units and having less than 20 mole % propylene units. 3. The composition of claim 2 wherein the polyethylene resin is selected from the group consisting of low density polyethylene, high density polyethylene and combinations thereof. 4. The composition of claim 1 wherein the blend in the processing comprises a continuous, homogeneous matrix phase of a mixture of the polyethylene resin and the NFP. 5. A composition comprising crosslinked polyethylene (PEX) prepared by the method comprising: blending a polyethylene resin with a flexibilizing amount of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 300 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, and flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP;wherein the blend comprises at least 90 weight percent of the polyethylene resin by weight of polymer components of the blend;processing the blend into a shape of an article; andcrosslinking the blend in the form of the shape. 6. The composition of claim 1 wherein the NFP comprises from about 0.5 to about 10 weight percent by weight of the polyethylene resin. 7. The composition of claim 1 wherein the NFP is selected from poly-alpha-olefins (PAOs), Group III basestocks, high purity hydrocarbon fluids derived from a gas-to-liquids process (GTLs) and combinations thereof. 8. The composition of claim 1 wherein the NFP comprises oligomers of C5 to C14 olefins. 9. The composition of claim 1 wherein the NFP comprises a Group III basestock and has a kinematic viscosity at 100° C. of 4 to 50 cSt, a number average molecular weight (Mn) of 400 to 1,000 g/mole, or a combination thereof. 10. The composition of claim 1 wherein the NFP comprises a paraffinic composition derived from Fischer-Tropsch hydrocarbons and/or waxes, including wax isomerate lubricant oil basestocks and gas-to-liquids basestocks, having a kinematic viscosity at 100° C. of about 3 cSt to about 500 cSt. 11. The composition of claim 1 wherein the blending comprises blending in a melt stream. 12. The composition of claim 11 wherein the NFP is added to the polyethylene outside a melt stream. 13. The composition of claim 11 wherein the NFP is added to the polyethylene into the melt stream. 14. The composition of claim 11 wherein the melt blending comprises compounding in a single screw extruder. 15. The composition of claim 1 wherein the blending comprises introducing a cure system to the blend. 16. The composition of claim 15 wherein the cure system comprises an organic peroxide introduced into the blend at a temperature below a decomposition point of the peroxide, and the crosslinking comprises heating the blend to a temperature above the decomposition point of the peroxide. 17. The composition of claim 16 wherein the crosslinking comprises a continuous vulcanization process downstream from an extruder. 18. The composition of claim 16 wherein the crosslinking comprises an Engel process wherein after the peroxide is introduced the blend is rammed through a head maintained above the decomposition temperature of the peroxide to form a crosslinked extrudate. 19. The composition of claim 15 wherein the cure system comprises a moisture-curable silane compound and the blend is cured by exposing the shaped article to moisture. 20. The composition of claim 19 wherein the moisture exposure comprises contacting the shaped article with water at a temperature of 15° C. or less. 21. The composition of claim 19 wherein the silane compound is introduced as a copolymerized comonomer in a reactor copolymer in the polyethylene resin. 22. The composition of claim 21 wherein the blending comprises introducing a masterbatch comprising moisture-curing catalyst into the blend. 23. The composition of claim 19 wherein the silane compound is grafted onto the polyethylene resin by reactive extrusion and the graft resin is mixed with a masterbatch comprising moisture-curing catalyst. 24. The composition of claim 19, the method comprising a one step process wherein the silane compound and a crosslinking catalyst are introduced into the blend in a single extruder. 25. The composition of claim 19, the method comprising a two-step process wherein the silane compound and a crosslinking catalyst are serially introduced into the blend in separate extrusions. 26. The composition of claim 1 wherein the crosslinking comprises electron beam irradiation of the shaped article. 27. A crosslinked polyethylene article comprising the composition prepared by the method comprising: blending a polyethylene resin with a flexibilizing amount of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 3000 cSt at 100° C., pour point less than −20° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP;wherein the blend comprises less than 10 wt % of a propylene polymer having a melting point of 40° C. or more, by weight of the blend;processing the blend into a shape of a tubular article;crosslinking the blend in the form of the shape. 28. The crosslinked polyethylene article of claim 27 wherein the crosslinked polyethylene article is selected from the group consisting of pipes, conduits, tubes, wire jacketing and insulation, and cable jacketing and insulation. 29. The crosslinked polyethylene article of claim 28 comprising an extrudate. 30. A composition consisting essentially of crosslinked polyethylene (PEX) blended with from about 0.1 to about 10 percent by weight of the composition of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 300 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP. 31. A pipe comprising at least one layer comprising a composition consisting essentially of crosslinked polyethylene (PEX) blended with from about 0.1 to about 10 percent by weight of the composition of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 300 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP. 32. The pipe of claim 31 comprising a plurality of layers wherein the PEX composition comprises one layer. 33. Tubing comprising at least one layer comprising a composition consisting essentially of crosslinked polyethylene (PEX) blended with from about 0.1 to about 10 percent by weight of the composition of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 300 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP. 34. Insulation or jacketing for wire or cable comprising at least one layer comprising a composition consisting essentially of crosslinked polyethylene (PEX) blended with from about 0.1 to about 10 percent by weight of the composition of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 300 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP. 35. A tubular present in a structure selected from the group consisting of hot and cold water plumbing systems, drinking water systems, hydronic radiant heating systems, snow melting equipment, ice rink plumbing and wiring and refrigeration warehouse plumbing and wiring, wherein the tubular comprises at least one layer comprising a composition consisting essentially of crosslinked polyethylene (PEX) blended with from about 0.1 to about 10 percent by weight of the composition of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 300 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP. 36. A tubular comprising at least one layer comprising a composition consisting essentially of crosslinked polyethylene (PEX) blended with from about 0.1 to about 10 percent by weight of the composition of a non-functionalized plasticizer (NFP) having a viscosity index greater than 120, kinematic viscosity of from 3 to 300 cSt at 100° C., pour point less than −20° C., specific gravity less than 0.86, flash point greater than 200° C., and wherein the NFP contains less than 5 weight percent of functional groups selected from hydroxide, aryls, substituted aryls, halogens, alkoxys, carboxylates, esters, acrylates, oxygen, nitrogen, and carboxyl, based upon the weight of the NFP, and wherein the number of carbons of the NFP involved in olefinic bonds is less than 5% of the total number of carbon atoms in the NFP, and having a flexibility at least 5 percent greater than a similar tubular comprising the corresponding non-flexibilized composition without the NFP. 37. The composition of claim 30 wherein the NFP comprises oligomers of C5 to C14 olefins. 38. The composition of claim 30 wherein the NFP comprises a Group III basestock and has a kinematic viscosity at 100° C. of 4 to 50 cSt, a number average molecular weight (Mn) of 400 to 1,000 g/mole, or a combination thereof. 39. The composition of claim 30 wherein the NFP comprises a paraffinic composition derived from Fischer-Tropsch hydrocarbons and/or waxes, including wax isomerate lubricant oil basestocks and gas-to-liquids basestocks, having a kinematic viscosity at 100° C. of about 3 cSt to about 500 cSt. 40. The composition of claim 30 wherein the crosslinked polyethylene is obtained by crosslinking a blend of the NFP in a polyethylene resin comprising an ethylene based polymer comprising at least 50 mole % ethylene units and having less than 20 mole % propylene units. 41. The composition of claim 40 wherein the polyethylene resin is selected from the group consisting of low density polyethylene, high density polyethylene and combinations thereof. 42. The composition of claim 40 wherein the blend comprises a continuous, homogeneous matrix phase of a mixture of the polyethylene resin and the NFP. 43. The composition of claim 40 wherein the blend comprises at least 90 weight percent of the polyethylene resin by weight of polymer components of the blend. 44. The composition of claim 40 wherein the blend is crosslinked with an organic peroxide. 45. The composition of claim 40 wherein the blend is crosslinked with a silane compound and moisture curing. 46. The composition of claim 45 wherein the blend comprises an intimate admixture with a masterbatch comprising moisture-curing catalyst. 47. The composition of claim 40 wherein the polyethylene resin comprises a reactor copolymer comprising a copolymerized silane compound. 48. The composition of claim 40 wherein the blend comprises a silane compound grafted onto the polyethylene resin by reactive extrusion and a masterbatch comprising moisture-curing catalyst in intimate admixture therewith. 49. The composition of claim 40 wherein the blend is crosslinked by electron beam irradiation. 50. The composition of claim 43 wherein the composition comprises a flexibility at least 5 percent greater and a stress at yield of not more than 20 percent less than a corresponding non-flexibilized composition without the NFP.