Extruded polyolefin foam in thicker grades and plank and process therefor
AssigneeSealed Air Corporation (US)
InventorsShau-Tarng Lee, Natarajan S. Ramesh
Life of this patent
Estimating the term…
Abstract
An extruded polyolefin foam in thicknesses of at least about 12 mm and greater of improved compressive strength, extensional viscosity, and reduced aging time and a process for making the foam are disclosed. The foam is prepared using a propane blowing agent. The beneficial properties imparted to thicker grade and plank foams by a propane blowing agent can be achieved with up to as much as 75% by volume of either normal butane or isobutane or both in the blowing agent, depending on the polyolefin selected.
Claims12
An extruded polyolefin foam having a thickness of at least about 12 mm and a density of from about 20 to 180 kg/m3, wherein said polyolefin is selected from the group consisting of low density polyethylene, polypropylene, and mixtures thereof, wherein said foam has a compressive strength about one hour after extrusion of from about 8 to 45 psig at 25 percent compression by unit volume, and wherein said foam is expanded by a blowing agent comprising from about 25 to 100 percent propane and from about 0 to 75 percent by volume of isobutane, normal butane, or a mixture of isobutane and normal butane.
The foam of claim I wherein said blowing agent is about 70 percent propane and 30 percent by weight of isobutane, normal butane, or a mixture of iso- and normal butane.
An extruded polyolefin foam having a thickness of at least about 12 mm and a density of from about 20 to 65 kg/m3, wherein said polyolefin is selected from the group consisting of low density polyethylene, polypropylene, and mixtures thereof, wherein said foam is expanded by a blowing agent comprising from 25 to 100 percent propane and from 0 to 75 percent isobutane, normal butane, or mixtures thereof, and wherein the force required to cut the foam is at least 10 percent less than that of foams prepared from the same polyolefins using a blowing agent of 100% isobutane, normal butane, or mixtures thereof for foam samples of comparable size and density.
An extruded polyolefin foam having a thickness of at least about 12 mm and a density of from about 20 to 65 kg/m3, wherein said polyolefin is selected from the group consisting of low density polyethylene, polypropylene, and mixtures thereof, wherein said foam is expanded by a blowing agent comprising from 25 to 100 percent propane and from 0 to 75 percent isobutane, normal butane, or mixtures thereof, and wherein the force required to bend the foams is at least 5% higher than that for foams prepared from the same polyolefins using a blowing agent of 100% isobutane, normal butane, or mixtures thereof for foam samples of comparable size and density.
A process for producing an extruded low density polyolefin foam having a thickness of at least about 12 mm, said process comprising the steps of:
- a) mixing a blowing agent with a plasticized polyolefin resin selected from the group consisting of low density polyethylene, polypropylene, and mixtures thereof, wherein the blowing agent is selected from the group consisting of 100 percent by weight of propane and blends of propane with up to about 75% by weight of normal butane, isobutane, or a mixture of normal butane and isobutane;
- and
- b) extruding the mixture of resin and blowing agent so as to produce a foam plank having a compressive strength about one hour after extrusion of from about 8 to 45 psig at 25 percent compression by unit volume.
An extruded polyolefin foam having a nominal thickness of at least about 12 mm and a density of from about 20 to 65 kg/m3, wherein said polyolefin is selected from the group consisting of low density polyethylene, polypropylene, and mixtures thereof, wherein said foam is expanded by a blowing agent comprising from about 25 to 100 percent by weight of propane and from about 0 to 75 percent by weight of isobutane, normal butane, or a mixture of isobutane and normal butane, and wherein said foam has a compressive strength one hour after extrusion of about 8 to 20 psig at about 25 percent compression by unit volume.
Dependencies are inferred from the claim text.