Foams made from interpolymers of ethylene/alpha-olefins
An olefin copolymer and olefin copolymerization technology, applied in the field of foam prepared by ethylene/α-olefin copolymer, can solve the problems of impact foam rupture, tearing and shrinkage properties
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Embodiment 1-4
[0289] Examples 1-4, Comparative Examples A-C
[0290] Typical high throughput parallel polymerization conditions
[0291] Polymerization was performed using a high throughput parallel polymerization reactor (PPR) available from Symyx technologies, Inc. and operated substantially in accordance with U.S. Patent Nos. 6,248,540, 6,030,917, 6,362,309, 6,306,658, and 6,316,663. Ethylene copolymerization was carried out at 130°C at 200 psi (1.4 MPa) with ethylene on demand and using 1.2 equivalents of Cocatalyst 1 (based on total catalyst used) (1.1 equivalents when MMAO was present). A series of polymerization reactions were carried out in a parallel pressure reactor (PPR) containing 48 individual reactor units in 6x8 arrays fitted with pre-weighed glass tubes. The operating volume within each reactor unit was 6000 μL. Each unit controls temperature and pressure, and provides stirring through individual stirring paddles. Monomer gas and quenching gas are directly sent into the...
Embodiment 1
[0299] The DSC curve for the polymer of Example 1 showed a melting point (Tm) of 115.7°C with a heat of fusion of 158.1 J / g. The corresponding CRYSTAF curve shows the highest peak at 34.5°C with a peak area of 52.9%. The difference between DSC Tm and Tcrystaf was 81.2°C.
Embodiment 2
[0300] The DSC curve for the polymer of Example 2 showed a peak with a melting point (Tm) of 109.7°C with a heat of fusion of 214.0 J / g. The corresponding CRYSTAF curve shows the highest peak at 46.2°C with a peak area of 57.0%. The difference between DSC Tm and Tcrystaf was 63.5°C.
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Abstract
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