Mesoporous silica supported multiple single-site catalysts and polyethylene reactor blends with tailor-made trimodal and ultra-broad molecular weight distributions
A ternary blend of the bisiminopyridine chromium (III) (Cr-1) with the bisiminopyridine iron (II) (Fe-2) post-metallocenes with the quinolylsilylcyclopentadienyl chromium (III) halfsandwich complex (Cr-3) was supported on mesoporous silica to produce novel multiple single-site catalysts and polyethy...
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| Hauptverfasser: | , , , , |
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| Dokumenttyp: | Article (Journal) |
| Sprache: | Englisch |
| Veröffentlicht: |
2010
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| In: |
Macromolecular rapid communications
Year: 2010, Jahrgang: 31, Heft: 15, Pages: 1359-1363 |
| ISSN: | 1521-3927 |
| DOI: | 10.1002/marc.201000074 |
| Online-Zugang: | Verlag, lizenzpflichtig, Volltext: https://doi.org/10.1002/marc.201000074 Verlag, lizenzpflichtig, Volltext: https://onlinelibrary.wiley.com/doi/abs/10.1002/marc.201000074 |
| Verfasserangaben: | Alexander Kurek, Stefan Mark, Markus Enders, Marc O. Kristen, Rolf Mülhaupt |
MARC
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| 245 | 1 | 0 | |a Mesoporous silica supported multiple single-site catalysts and polyethylene reactor blends with tailor-made trimodal and ultra-broad molecular weight distributions |c Alexander Kurek, Stefan Mark, Markus Enders, Marc O. Kristen, Rolf Mülhaupt |
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| 520 | |a A ternary blend of the bisiminopyridine chromium (III) (Cr-1) with the bisiminopyridine iron (II) (Fe-2) post-metallocenes with the quinolylsilylcyclopentadienyl chromium (III) halfsandwich complex (Cr-3) was supported on mesoporous silica to produce novel multiple single-site catalysts and polyethylene reactor blends with tailor-made molecular weight distributions (MWDs). The preferred cosupporting sequence of this ternary blend on MAO-treated silica was Fe-2 followed by Cr-1 and Cr-3. Cosupporting does not impair the single-site nature of the blend components producing polyethylene fractions with $øverline M _\rm w$ = 104 g · mol−1 on Cr-1, $øverline M _\rm w$ = 3 × 105 g · mol−1 on Fe-2, and $øverline M _\rm w$ = 3 × 106 g · mol−1 on Cr-3. As a function of the Fe-2/Cr-1/Cr-2 mixing ratio it is possible to control the weight ratio of these three polyethylenes without affecting the individual average molecular weights and narrow polydispersities of the three polyethylene fractions. Tailor-made polyethylene reactor blends with ultra-broad MWD and polydispersities varying between 10 and 420 were obtained. When the molar ratio of Fe-2/Cr-1 was constant, the ultra-high molecular polyethylene (UHMWPE, $øverline M _\rm w$ > 106 g · mol−1) content was varied between 8 and 16 wt.-% as a function of the Cr-3 content without impairing the blend ratio of the other two polyethylene fractions and without sacrificing melt processability. When the molar ratio Fe-2/Cr-3 was constant, it was possible to selectively increase the content of the low molecular weight fraction by additional cosupporting of Cr-1. Due to the intimate mixing of low and ultra-high molecular weight polyethylenes (UHMPEs) produced on cosupported single-site catalysts a wide range of melt processable polyethylene reactor blends was obtained. | ||
| 650 | 4 | |a polyethylene | |
| 650 | 4 | |a post-metallocene catalysts | |
| 650 | 4 | |a reactor blends | |
| 650 | 4 | |a Ziegler-Natta polymerization | |
| 700 | 1 | |a Mark, Stefan |e VerfasserIn |0 (DE-588)143621696 |0 (DE-627)647706539 |0 (DE-576)338022341 |4 aut | |
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| 700 | 1 | |a Kristen, Marc O. |e VerfasserIn |4 aut | |
| 700 | 1 | |a Mülhaupt, Rolf |e VerfasserIn |4 aut | |
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