Improved powdered thermoplastic polyolefin elastomer composition for slush molding
US-2015368391-A1 · Dec 24, 2015 · US
US10053522B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10053522-B2 |
| Application number | US-201214131397-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 6, 2012 |
| Priority date | Jul 8, 2011 |
| Publication date | Aug 21, 2018 |
| Grant date | Aug 21, 2018 |
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wherein the composition distribution breadth index (CDBI) of the polyethylene resin is below 70%, as analyzed by quench TREF (temperature rising elution fractionation) analysis.
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The invention claimed is: 1. A metallocene-catalyzed polyethylene resin having a multimodal molecular weight distribution, comprising: from 45% by weight to 75% by weight of a low density fraction, said low density fraction having a density below or equal to 0.918 g/cm 3 as measured following the method of standard test ISO 1183 at a temperature of 23° C.; wherein the density of the polyethylene resin is from 0.920 to 0.945 g/cm 3 ; wherein the Mw/Mn of the polyethylene resin is from 2.8 to 6; wherein the melt index MI 2 of the polyethylene resin is from 0.1 to 5 g/10 min as measured following the method of standard test ISO 1133 Condition D at a temperature of 190° C. and under a load of 2.16 kg; wherein the composition distribution breadth index (CDBI) of the polyethylene resin is below 70%, as analyzed by quench TREF (temperature rising elution fractionation) analysis; and wherein the polyethylene resin comprises a bimodal composition as measured by quench TREF analysis, wherein the polyethylene resin has a g rheo of less than 0.90 and greater than 0.35, wherein g rheo is determined according to: g rheo ( PE ) = M w ( SEC ) M w ( η 0 , MWD , SCB ) wherein M w (SEC) is the weight average molecular weight obtained from size exclusion chromatography expressed in kDa, and wherein M w (n 0 ,MWD,SCB) is determined according to the following M w (η 0 ,MWD,SCB )=exp(1.7789+0.199769Ln M n +0.209026(Lnη 0 )+0.955(ln ρ)−0.007561(Ln M z (Lnη 0 )+0.02355(ln M z ) 2 wherein density ρ is measured in g/cm 3 and measured according to ISO 1183 at a temperature of 23° C. and wherein zero shear viscosity η 0 in Pa·s is obtained from a frequency sweep experiment combined with a creep experiment, and taking the assumption of equivalence of angular frequency (rad/s) and shear rate, and wherein zero shear viscosity η 0 is estimated by fitting with Carreau-Yasuda flow curve (η−W) at a temperature of 190° C., obtained by oscillatory shear rheology on ARES-G2 equipment in the linear viscoelasticity domain, and wherein circular frequency (W in rad/s) varies from 0.05-0.1 rad/s to 250-500 rad/s, and the shear strain is typically 10%, and wherein the creep experiment is carried out at a temperature of 190° C. under nitrogen atmosphere with a stress level such that after 1200 s the total strain is less than 20%. 2. The metallocene-catalyzed polyethylene resin according to claim 1 , wherein the Mw of the low density fraction is from 80 to 140 kDa. 3. The metallocene-catalyzed polyethylene resin according to claim 1 , wherein the CDBI of the polyethylene resin is in a range of 30-50%, as analyzed by quench TREF analysis. 4. The metallocene-catalyzed polyethylene resin according to claim 1 , wherein the polyethylene resin comprises a higher density fraction having a higher density than the low density fraction, wherein a ratio Mw of the low density fraction/Mw of the higher density fraction is less than 6 and greater than 2.5.
with unsaturated hydrocarbons only containing four or more carbon atoms · CPC title
Homopolymers or copolymers of ethene · CPC title
Manufacture of films or sheets · CPC title
containing two or more polymers of the same C08L -group · CPC title
Metallocene or single site catalysts · CPC title
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