Continuous ethylene oligomerization with in-situ catalyst preparation
US-2016303551-A1 · Oct 20, 2016 · US
US2018229226A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018229226-A1 |
| Application number | US-201615751938-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 21, 2016 |
| Priority date | Sep 23, 2015 |
| Publication date | Aug 16, 2018 |
| Grant date | — |
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The present invention relates to a catalyst system for olefin oligomerization, and a method for oligomerizing olefins using the same. The catalyst system for olefin oligomerization according to the present invention exhibits high selectivity to 1-hexene and 1-octene while having excellent catalytic activity, thereby enabling more efficient preparation of alpha-olefins.
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1 . A catalyst system for olefin oligomerization comprising: a ligand compound represented by Chemical Formula 1 below; a transition metal source; and a cocatalyst: in the above Chemical Formula 1, E 1 and E 2 are each independently an element selected from the group consisting of boron (B), nitrogen (N), oxygen (O), silicon (Si), phosphorus (P), and sulfur (S), and R 1 to R 6 each independently represent hydrogen, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, an alkylsilyl group having 1 to 20 carbon atoms, a haloalkyl group having 1 to 20 carbon atoms, an aryl group having 6 to 40 carbon atoms, an arylalkyl group having 7 to 20 carbon atoms, an arylsilyl group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, an alkylsiloxy group having 1 to 20 carbon atoms, an aryloxy group having 6 to 20 carbon atoms, a halogen group, or an amino group. 2 . The catalyst system for olefin oligomerization of claim 1 , wherein at least one of E 1 and E 2 in Chemical Formula 1 is nitrogen (N) or oxygen (O). 3 . The catalyst system for olefin oligomerization of claim 1 , wherein at least one of R 1 and R 4 in Chemical Formula 1 is an alkyl group, a cycloalkyl group, or an aryl group having 1 to 20 carbon atoms. 4 . The catalyst system for olefin oligomerization of claim 1 , wherein the ligand compound includes piperazine substituted with one or more functional groups selected from the group consisting of an alkyl group having 1 to 5 carbon atoms and a cycloalkyl group having 4 to 10 carbon atoms. 5 . The catalyst system for olefin oligomerization of claim 1 , wherein the ligand compound is selected from the group consisting of: 6 . The catalyst system for olefin oligomerization of claim 1 , wherein the transition metal source includes one or more compounds selected from the group consisting of chromium(III) 2,2,6,6-tetramethylheptanedionate, chromium(III) 2-ethylhexanoate, chromium(III) tris(2-ethylhexanoate), chromium(III) naphthenate [Cr(NP) 3 ], chromium(III) chloride, chromium(III) bromide, chromium(III) fluoride, chromium(III) acetylacetonate, chromium(III) acetate, chromium(III) butyrate, chromium(III) neopentanoate, chromium(III) laurate, chromium(III) stearate, chromium(III) oxalate, chromium bromide, chromium fluoride, chromium chloride, chromium(II) bis(2-ethylhexanoate), chromium(II) acetate, chromium(II) butyrate, chromium(II) neopentanoate, chromium(II) laurate, chromium(II) stearate, and chromium(II) oxalate. 7 . The catalyst system for olefin oligomerization of claim 1 , wherein the cocatalyst one or more alkyl aluminum compounds selected from the group consisting of triethyl aluminum, tripropyl aluminum, tributyl aluminum, diethyl aluminum chloride, diethyl aluminum bromide, diethyl aluminum ethoxide, diethyl aluminum phenoxide, ethyl aluminum dichloride, and ethyl aluminum sesquichloride. 8 . The catalyst system for olefin oligomerization of claim 1 , wherein the molar ratio of the ligand compound to the transition metal source to the cocatalyst is in the range of 0.5:1:1 to 10:1:10,000. 9 . A method for oligomerizing olefins comprising a step of subjecting an olefin to a multimerization reaction in the presence of the catalyst system for olefin oligomerization of claim 1 . 10 . The method for oligomerizing of claim 9 , wherein the multimerization reaction temperature is 0 to 250° C. 11 . The method for oligomerizing of claim 9 , wherein the multimerization reaction pressure is 1 to 200 bar.
as complexes, e.g. acetyl-acetonates {(complexes of salts of acids of halogen C07C2/20)} · CPC title
Chromium · CPC title
Organic complexes · CPC title
of aluminium · CPC title
Cyclic ligands, including e.g. non-condensed polycyclic ligands, comprising at least one complexing nitrogen atom as ring member, e.g. pyridine · CPC title
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