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Draw a polymer composition by providing a polymer composition containing an orientable polymer having a softening temperature and a filler; conditioning the temperature of the polymer composition at or below its softening temperature; and drawing the polymer composition at a draw rate of at least 12

Draw a polymer composition by providing a polymer composition containing an orientable polymer having a softening temperature and a filler; conditioning the temperature of the polymer composition at or below its softening temperature; and drawing the polymer composition at a draw rate of at least 127 centimeters per minute in order to achieve an oriented filled polymer composition demonstrating a stable extent of cavitation with draw rate.

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1. A process for solid state die drawing a polymer composition comprising: (a) providing a polymer composition comprising a filler and an orientable polymer, the polymer composition having a softening temperature, wherein the filler is organic, inorganic or a combination of organic and inorganic;(b)

1. A process for solid state die drawing a polymer composition comprising: (a) providing a polymer composition comprising a filler and an orientable polymer, the polymer composition having a softening temperature, wherein the filler is organic, inorganic or a combination of organic and inorganic;(b) forming a billet from the polymer composition;(c) conditioning the temperature of the polymer composition to within an average drawing temperature, wherein the average drawing temperature is the average of the highest and lowest temperature along the cross sectional dimension and is at least 20° C. below the softening temperature and less than or equal to 40° C. below the softening temperature;(d) providing the billet to a drawing die, wherein the cross sectional dimensions of the billet before entering the drawing die and an exit of the drawing die correspond to a nominal draw ratio in the range of 1.2-8;(e) initiating drawing of the polymer composition while the polymer composition remains at the average drawing temperature;(f) drawing the conditioned polymer composition at the average drawing temperature through the drawing die at a minimum drawing rate of at least 127 centimeters (50 inches) per minute and a maximum drawing rate representative of a drawing force less than a tensile strength of the die drawn polymer composition; and(g) maintaining, during drawing, the temperature of the polymer composition at two different points along a cross sectional dimension of the polymer composition so that the temperature at the two different points differs by 10% or less from the average drawing temperature to reach a cavitation plateau in which a density of the die drawn polymer composition at the cavitation plateau differs by 10% or less from an average density calculated from the density of the polymer composition resulting from drawing at a rate above the minimum drawing rate for drawing rates differing by at least 10 centimeters per minute at a given average drawing temperature, wherein all cross sectional dimensions of the die drawn polymer are greater than 1.5 millimeters. 2. The process of claim 1, wherein the drawing die induces proportional drawing of the polymer composition. 3. The process of claim 1, wherein the polymer composition remains at the average drawing temperature as it draws. 4. The process of claim 1, wherein the filler is an inert inorganic filler. 5. The process of claim 1, wherein the filler is selected from a group consisting of talc, fly ash, clay or calcium carbonate. 6. The process of claim 1, wherein the orientable polymer is one or more than one semi-crystalline polymer. 7. The process of claim 1, wherein the orientable polymer is a polyolefin. 8. The process of claim 1, wherein the orientable polymer is selected from a polypropylene-based polymer or high density polyethylene. 9. The process of claim 1, wherein the drawing rate is at least 150 centimeters (60 inches) per minute. 10. The process of claim 1, wherein the drawing rate is at least 254 centimeters (100 inches) per minute. 11. The process of claim 1, wherein the filler is present at a concentration of 20 percent by weight or more relative to polymer composition weight before drawing. 12. The process of claim 1, wherein the process induces at least 30 percent by volume of void space into the polymer composition. 13. The process of claim 1, wherein the nominal draw ratio is in the range of 1.2 to 3.