Expandable olefin bead polymers
Abstract
The invention relates to expandable olefin bead polymers which comprise a blowing agent with a boiling point of from −5 to 150° C., selected from the group consisting of alkanes, alkanols, ketones, ethers and esters. The particles are unfoamed and have a bulk density above 500 g/l, and can be foamed to a bulk density below 200 g/l after storage for one hour at room temperature in free contact with the atmosphere. They are prepared by impregnating polyolefin pellets in suspension in a pressure vessel with the blowing agent, cooling the batch below 100° C., reducing the pressure and isolating the particles.
Claims
exact text as granted — not AI-modifiedWe claim:
1 . An expandable olefin bead polymer which may have been blended with up to 50% of a thermoplastic with a glass transition point below 180° C. and comprises from 1 to 40% by weight of an organic blowing agent with a boiling point of from −5 to 150° C., based in each case on the weight of the olefin polymer, wherein the unfoamed beads have a bulk density above 400 g/l and can be foamed to a bulk density below 200 g/l after storage for one hour at room temperature in free contact with the atmosphere by heating above 100° C.
2 . An expandable olefin polymer as claimed in claim 1 , which comprises a halogen-free blowing agent.
3 . An expandable olefin polymer as claimed in claim 1 which is a copolymer of propylene with up to 15% by weight of ethylene and/or 1-butene.
4 . An expandable olefin polymer as claimed in claim 1 , which comprises from 0.001 to 10% by weight of a nucleating agent, based on the weight of the polymer.
5 . An expandable olefin polymer as claimed in claim 1 , which comprises no admixed thermoplastics.
6 . An expandable olefin polymer as claimed in claim 1 which has been blended with from 5 to 40% by weight of a polyamide.
7 . A process for preparing expandable olefin bead polymers by impregnating polyolefin pellets with from 2 to 50% by weight of an organic blowing agent with a boiling point of from −5 to 150° C. in suspension in a pressure vessel at elevated temperature, reducing the pressure on the batch and isolating and washing the impregnated pellets, wherein the batch is cooled below 100° C. before the pressure is reduced.
8 . A process as claimed in claim 7 , wherein a halogen-free blowing agent is used.
9 . A process as claimed in claim 7 , wherein the blowing agent is an alkane, an alkanol, a ketone, an ether, an ester or a mixture of these.
10 . A process as claimed in claim 9 , wherein the blowing agent is a pentane, a hexane, a heptane, 3,3-dimethyl-2-butanone or 4-methyl-2-pentanone.
11 . A process as claimed in claim 7 , wherein the polyolefin pellets comprise from 0.001 to 10% by weight of a nucleating agent.
12 . A process as claimed in claim 11 , wherein the nucleating agent is a wax and/or talc.
13 . The use of expandable olefin bead polymers as claimed in claim 1 for producing foams.Join the waitlist — get patent alerts
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