Ligand compound, catalyst system for olefin oligomerazation, and method for olefin oligomerization using the same
US-2016122371-A1 · May 5, 2016 · US
US10870104B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10870104-B2 |
| Application number | US-201615528576-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 2, 2016 |
| Priority date | Feb 12, 2015 |
| Publication date | Dec 22, 2020 |
| Grant date | Dec 22, 2020 |
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The present invention relates to a method for preparing an oligomerization catalyst system and the method comprises preparing a catalyst composition by mixing a PNP-based ligand compound and a transition metal compound, and mixing and activating a co-catalyst and the catalyst composition at a temperature from −40 to 80° C. The oligomerization catalyst system prepared by the method may maintain the activity thereof during an oligomerization reaction at a high temperature, and the reaction temperature of oligomerization may be easily controlled. Various merits in processing may be obtained.
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The invention claimed is: 1. A method for preparing an oligomerization catalyst system, the method comprising: preparing a catalyst composition by mixing a ligand compound comprising a diphosphine moiety of the following Formula 3, and an organic chromium compound; and activating by mixing a co-catalyst and the catalyst composition for two or more minutes and less than five minutes at a temperature from 20 to 80° C.: wherein in Formula 3: R1 to R4 are each independently a C6 aryl or C7 alkylaryl group; R5 is a methyl group; R6 is a linear C2-C3 alkyl group or a linear C2-C3 alkenyl group; and R7 to R9 are hydrogen. 2. The method for preparing an oligomerization catalyst system of claim 1 , wherein an activating time of the co-catalyst and the catalyst composition is from two minutes or more to three minutes or less. 3. The method for preparing an oligomerization catalyst system of claim 1 , wherein an activating temperature is from 20 to 80° C. 4. The method for preparing an oligomerization catalyst system of claim 1 , wherein R7 to R9 of Formula 3 are hydrogen. 5. The method for preparing an oligomerization catalyst system of claim 1 , wherein the transition metal compound comprises an organic chromium compound, and the organic chromium compound comprises at least one selected from the group consisting of chromium(III) acetyl acetonate, trichlorochromium tris tetrahydrofuran, chromium(III)-2-ethylhexanoate, chromium(III) tris (2,2,6,6-tetramethyl-3,5-heptanedionate), chromium(III) benzoyl acetonate, chromium(III) hexafluoro-2,4-pentanedionate and chromium(III) acetate hydroxide. 6. The method for preparing an oligomerization catalyst system of claim 1 , wherein the co-catalyst is at least one selected from the compounds of the following Formulae 4 to 6: −[Al(R 5 )−O] c — [Formula 4] wherein in the above Formula 4, R 5 is the same or different and is independently a halogen radical, a hydrocarbyl radical having 1 to 20 carbon atoms, or a halogen substituted hydrocarbyl radical having 1 to 20 carbon atoms, and c is an integer of at least 2; D(R 6 ) 3 [Formula 5] wherein in the above Formula 5, D is aluminum or boron, each R 6 is the same or different and is independently hydrogen, halogen, hydrocarbyl having 1 to 20 carbon atoms, or halogen substituted hydrocarbyl having 1 to 20 carbon atoms; [L-H] + [Q(E) 4 ] − [Formula 6] wherein in the above Formula 6, L is a neutral Lewis base, [L-H] + is a brönsted acid, Q is boron or aluminum with an oxidation state of +3, and each E is independently aryl having 6 to 20 carbon atoms or alkyl having 1 to 20 carbon atoms, where at least one hydrogen atom is substituted with halogen, a hydrocarbyl having 1 to 20 carbon atoms, an alkoxy functional group or a phenoxy functional group or is unsubstituted. 7. A method for oligomerizing olefin, the method comprising: performing a oligomerization reaction of olefin in a reaction temperature range of 30 to 150° C. in the presence of the oligomerization catalyst system prepared by the preparation method according to claim 1 . 8. The method for oligomerizing olefin of claim 7 , wherein the reaction temperature is in a range of 60 to 130° C. 9. The method for oligomerizing olefin of claim 7 , wherein an activity of the catalyst system in a whole reaction temperature range is 100,000 kg/molCr/hr or more in a batch type process, and 100,000 kg/molCr or more in a continuous type process. 10. The method for oligomerizing olefin of claim 7 , wherein an activity decreasing ratio of the catalyst system according to temperature increase is less than 6% in a whole reaction temperature range. 11. The method for oligomerizing olefin of claim 7 , wherein selectivity of 1-hexene and 1-octene relative to a total amount of a product is 80 wt % or more in a whole reaction temperature range.
Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title
as phosphines, arsines, stilbines or bismuthines · CPC title
of aluminium · CPC title
Chromium · CPC title
Phosphines · CPC title
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