Continuous ethylene tetramerization process
US-2015284303-A1 · Oct 8, 2015 · US
US11623209B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11623209-B2 |
| Application number | US-202217669558-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 11, 2022 |
| Priority date | Mar 13, 2015 |
| Publication date | Apr 11, 2023 |
| Grant date | Apr 11, 2023 |
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The invention relates to oligomerization of olefins, such as ethylene, to higher olefins, such as a mixture of 1-hexene and 1-octene, using a catalyst system that comprises a) a source of chromium b) one or more activators and c) a phosphacycle-containing ligating compound. Additionally, the invention relates to a phosphacycle-containing ligating compound and a process for making said compound.
Opening claim text (preview).
What is claimed is: 1. A process for oligomerizing an olefin comprising: contacting at least one olefin with a catalyst system under olefin oligomerization conditions sufficient to convert at least a portion of the at least one olefin to a product comprising at least one oligomer of the at least one olefin, the catalyst system comprising: a) a source of chromium; b) one or more activators; and, c) at least one phosphacycle-containing ligating compound of the formula: or wherein: P is phosphorus; L is C; q is 1 or 2; p is 1 or 2; wherein when p is 1 L 1 is Si; and when p is 2: a first of L 1 is Si and a second of L 1 is Si; or the first of L 1 is N and q is 0 or 1 to give and the second of L 1 is Si and q is 1 or 2 to give or the first of L 1 is N and q is 0 or 1 to give and the second of L 1 is C and q is 1 or 2 to give or the first of L 1 is C and q is 0 or 1 to give and the second of L 1 is Si and q is 1 or 2 to give R 5 attached to L 1 is independently H, C 1-40 substituted or unsubstituted alkyl, C 1-40 substituted or unsubstituted aryl; each R 5 attached to the C or L group is independently H, halogen, C 1-40 substituted or unsubstituted alkyl, C 1-40 substituted or unsubstituted aryl; each R 3 and R 4 is independently an alkyl, substituted alkyl, phenyl, substituted phenyl, furanyl, substituted furanyl, thienyl, substituted thienyl, pyrrolyl, substituted pyrrolyl, pyridinyl, and substituted pyridinyl; and two or more R 3 , R 4 or R 5 groups are optionally linked together to form cyclic structures containing 4 to 10 ring atoms; two or more R 5 groups linked to separate L atoms in a phosphacycle moiety are optionally linked together to form a cyclic structure that contains from 3 to 10 ring atoms; and two R 5 groups attached to the same L atom may be optionally linked together to form a cyclic structure that contains from 3 to 10 ring atoms. 2. The process of claim 1 wherein the olefin comprises ethylene and the product comprises a mixture of 1-octene and 1-hexene in a weight fraction ranging from 85 percent by weight to 100 percent by weight of total product formed. 3. The process of claim 1 wherein the catalyst system is prepared by combining a) the source of chromium, b) one or more activators, and c) at least one phosphacycle-containing ligating compound together in any order. 4. The process of claim 1 comprising contacting a feed stream with the catalyst system wherein the feed stream comprises the olefin. 5. The process of claim 1 , wherein the source of chromium is selected from the group consisting of trichlorotris(tetrahydrofuran)chromium, chromium (III) acetylacetonate, chromium (III) 2-ethylhexanoate, and chromium (III) acetate. 6. The process of claim 1 , wherein the source of chromium and the ligating compound are contacted in proportions to provide Cr:ligating compound ratios from 1000:1 to 1:1000. 7. The process of claim 1 , wherein the catalyst system further includes an activator selected from the group consisting of (hydrocarbyl)aluminum compounds, (hydrocarbyl)gallium compounds, (hydrocarbyl)boron compounds, (hydrocarbyl)zinc compounds, non-coordinating, ion-forming compounds, an organic salt, an inorganic acid and salt. 8. The process of claim 7 , wherein the activator is an alkylaluminoxane. 9. The process of claim 8 , wherein the source of chromium and the aluminoxane are combined in proportions to provide chromium:activator molar ratios from 1:1 to 1:10,000. 10. The process of claim 1 wherein the product comprises polymer byproduct having a total mass fraction with respect to the total mass of products within a range of zero percent by weight to 10 percent by weight. 11. The process of claim 1 , wherein the at least one phosphacycle-containing ligating compound is selected from the group consisting of:
Chromium · CPC title
Nitrile groups · CPC title
comprising aliphatic or saturated rings, e.g. Xantphos · CPC title
comprising perfluoroalkyl groups or moieties · CPC title
the ring phosphorus atom being part of a phosphine oxide or thioxide · CPC title
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