2010
DOI: 10.1002/cctc.201000087
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Immobilized Chromium Catalyst System for Selective Ethene Trimerization to 1‐Hexene with a PNPNH Ligand

Abstract: Tie me catalyst down, support: A selective homogeneous chromium‐based ethene trimerization catalyst is heterogenized by immobilization on a functionalized polymer support. The immobilized catalyst displays good selectivity towards 1‐hexene, and retains high activity for long times on‐stream, combining advantages of homogeneous and heterogeneous catalyst systems.

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Cited by 27 publications
(29 citation statements)
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“…While there have been numerous ethylene trimerisation studies with 1 previously reported in the literature, [21][22][23][32][33][34][35][36]38,40 it was of interest to optimise the ligand under our conditions in order to determine a series of conditions with which to benchmark the novel ligand systems. The results of catalytic testing of 1/Cr in conjunction with triethylaluminium are shown in Table 1.…”
Section: Methodsmentioning
confidence: 99%
“…While there have been numerous ethylene trimerisation studies with 1 previously reported in the literature, [21][22][23][32][33][34][35][36]38,40 it was of interest to optimise the ligand under our conditions in order to determine a series of conditions with which to benchmark the novel ligand systems. The results of catalytic testing of 1/Cr in conjunction with triethylaluminium are shown in Table 1.…”
Section: Methodsmentioning
confidence: 99%
“…Nowadays it is attempted to immobilize active sites for ethene oligomerization on a heterogeneous support, hence, avoiding further catalyst separation. These active sites could be based on, e.g., nickel [5,6] or chromium [7,8]. The use of zeolites or silica-alumina as support could additionally lead to an increase in product flexibility due to the presence of both active metal ion and acid sites on such catalysts.…”
Section: Introductionmentioning
confidence: 98%
“…22 Furthermore, the tethering of chromium-based catalysts on polymeric supports has been described. 23,24 However, none of the authors comment on the morphology of the polymeric side product, catalyst leaching or reactor fouling during the oligomerization process. 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 4 Here we report the immobilization of the Mitsui ethylene trimerization pre-catalyst 1 (Scheme 1), with the aim to prevent reactor fouling by homogeneous polymer formation while retaining the high trimerization activity and selectivity.…”
Section: Introductionmentioning
confidence: 98%