Dispersion stabilizer for suspension polymerization and vinyl resin production method
US-2015329713-A1 · Nov 19, 2015 · US
US9334374B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9334374-B2 |
| Application number | US-201314387141-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 22, 2013 |
| Priority date | Mar 29, 2012 |
| Publication date | May 10, 2016 |
| Grant date | May 10, 2016 |
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Polymer blends of polypropylene homopolymer and propylene-α-olefin interpolymer. Processes for producing polymeric compositions comprising control-cooling heated blends of polypropylene and propylene-α-olefin interpolymer. Such polymeric compositions can be employed in forming coated wires and cables.
Opening claim text (preview).
The invention claimed is: 1. A process for preparing a thermoplastic polymeric composition, said process comprising: (a) heating a polymer blend comprising a polypropylene homopolymer and a propylene-α-olefin interpolymer to a melt temperature of (1) greater than 140° C., (2) at least the melting temperature of the polypropylene homopolymer, or (3) at least the melting temperature of the propylene-α-olefin interpolymer, whichever of (1) through (3) is greatest, for a time sufficient to form a polymer melt blend; and (b) cooling said polymer melt blend from said melt temperature down to ambient temperature, wherein said cooling comprises: (i) non-control-cooling said polymer melt blend from said melt temperature to an initial cooled temperature in the range of from 140 to 125° C., (ii) control-cooling said polymer melt blend at an average cooling rate in the range of from 0.1 to 30° C. per minute from said initial cooled temperature to an intermediate cooled temperature in the range of from 110 to 100° C., and (iii) cooling, by either control-cooling or non-control-cooling, said polymer melt blend from said intermediate cooled temperature to ambient temperature, thereby forming said polymeric composition. 2. The process of claim 1 , wherein said polymeric composition has an alternating current (“AC”) breakdown strength that is at least 5% greater than an otherwise identical but quench-cooled polymeric composition, as measured on 100 micrometer thick films in accordance with ASTM D-149. 3. The process of claim 1 , wherein said polymeric composition has an AC breakdown strength of at least 100 kV/mm, as measured on 100 micrometer thick films in accordance with ASTM D-149. 4. The process of claim 1 , wherein said polypropylene homopolymer and said polypropylene-α-olefin interpolymer are present in said polymer blend in a weight ratio ranging from 4:1 to 1:4. 5. The process of claim 1 , wherein said initial cooled temperature is 125° C., wherein said intermediate cooled temperature is 110° C., wherein said cooling of step (iii) is non-control-cooling. 6. The process of claim 1 , wherein said control-cooling of step (ii) is performed at a rate in the range of from 1 to 10° C. per minute. 7. The process of claim 1 , further comprising, prior to said cooling of step (b), coating said polymer melt blend on a conductive core thereby forming said polymeric coating on said conductive core following said cooling of step (b). 8. The process of claim 7 , wherein said polymeric coating on said conductive core presents a direct current (“DC”) breakdown strength of at least 400 kV when measured at a thickness of 3.5 mm. 9. The process of claim 1 , wherein said polypropylene homopolymer is non-nucleated. 10. The process of claim 1 , wherein the α-olefin component of said polypropylene-α-olefin interpolymer is ethylene.
Polypropene · CPC title
Polypropene · CPC title
Particle-shaped (making granules B29B9/00) · CPC title
Heating, e.g. for cross linking · CPC title
containing two or more polymers of the same C08L -group · CPC title
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