Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US12486346B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12486346-B2 |
| Application number | US-202418647691-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 26, 2024 |
| Priority date | Feb 12, 2018 |
| Publication date | Dec 2, 2025 |
| Grant date | Dec 2, 2025 |
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In at least one embodiment, a process to produce a poly alpha-olefin (PAO) includes introducing a first alpha-olefin to a first catalyst system comprising activator and a metallocene compound into a continuous stirred tank reactor or a continuous tubular reactor under first reactor conditions to form a first reactor effluent. The first alpha-olefin is introduced to the reactor at a flow rate of about 100 g/hr or more. The first reactor effluent includes at least 60 wt % of PAO dimer and 40 wt % or less of higher oligomers, where the higher oligomers are oligomers that have a degree of polymerization of 3 or more. The process includes introducing the first reactor effluent and a second alpha-olefin to a second catalyst composition including an acid catalyst in a second reactor to form a second reactor effluent comprising PAO trimer.
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What is claimed is: 1 . A composition, comprising: a plurality of poly-alpha olefins (PAOs), wherein the plurality of PAOs comprise; about 80 weight percent (wt %) or more of PAO trimers based on a total amount of PAO dimer, PAO trimer, PAO tetramer, and higher oligomers, wherein the composition comprises a kinematic viscosity @ 100° C. of about 4.5 cSt or less, wherein the PAOs are derived from an unsaturated poly alpha-olefin product comprising: greater than or equal to about 80 mol % vinylidenes, based on total moles of vinyls, vinylidenes, di-substituted vinylenes, and tri-substituted vinylenes contained therein; 0.1 mol % to 3.5 mol % of tri-substituted vinylenes; 3.0 mol % or less of di-substituted vinylenes; 3.0 mol % or less of vinyl groups; based on total moles of vinylidenes, tri-substituted vinylenes, di-substituted vinylenes, and vinyls contained therein; and having an Mn of less than 5000 g/mol as determined by 1H NMR. 2 . The composition of claim 1 , wherein the composition comprises a kinematic viscosity @40° C. of about 25 cSt or less. 3 . The composition of claim 1 , wherein the plurality of PAOs comprise 10 wt % or less of PAO dimers. 4 . The composition of claim 1 , wherein the plurality of PAOs comprise 30 wt % or less of the PAO dimer, the PAO tetramer, the higher oligomers, or a combination thereof. 5 . The composition of claim 1 , wherein the plurality of PAOs comprise 20 wt % or less of the PAO dimer, the PAO tetramer, the higher oligomers, or a combination thereof. 6 . The composition of claim 1 , wherein the plurality of PAOs comprise: 80 wt % or more of the PAO trimer; 10 wt % or less of the PAO tetramer, the higher oligomers, or a combination thereof; and 10 wt % or less of PAO dimer. 7 . A lubricant comprising the composition of claim 1 . 8 . The composition of claim 1 , comprising a kinematic viscosity @ 100° C. from about 2.8 cSt to about 4.5 cSt. 9 . The composition of claim 1 , wherein the composition further comprises PAOs functionalized with an amine, sulfur, a halogen, or a combination thereof. 10 . The composition of claim 1 , wherein the plurality of PAOs comprise hybrid trimers. 11 . The composition of claim 1 , comprising a Brookfield viscosity at 40° C. of about 2,000 cP or less. 12 . The composition of claim 1 , comprising a cold crank simulator value (CCS) at −35° C. of about 1,000 cP or less. 13 . The composition of claim 1 , comprising a CCS at −35° C. of about 900 cP or less. 14 . The composition of claim 1 , comprising a viscosity index of about 135 or greater. 15 . A lubricant composition, comprising: one or more additives; and a plurality of poly-alpha olefins (PAOs), wherein the plurality of PAOs comprise about wt % or more of PAO trimers, wherein the lubricant composition comprises a kinematic viscosity @ 100° C. of about 10 cSt or less and a kinematic viscosity @ 40° C. of about 25 cSt or less, wherein the PAOs are derived from an unsaturated poly alpha-olefin product comprising: greater than or equal to about 80 mol % vinylidenes, based on total moles of vinyls, vinylidenes, di-substituted vinylenes, and tri-substituted vinylenes contained therein; 0.1 mol % to 3.5 mol % of tri-substituted vinylenes; 3.0 mol % or less of di-substituted vinylenes; 3.0 mol % or less of vinyl groups; based on total moles of vinylidenes, tri-substituted vinylenes, di-substituted vinylenes, and vinyls contained therein; and having an Mn of less than 5000 g/mol as determined by 1H NMR. 16 . The lubricant composition of claim 15 , wherein the additives comprise viscosity index improvers, corrosion inhibitor, oxidation inhibitor, dispersant, lube oil flow improver, detergents, demulsifiers, rust inhibitors, pour point depressant, anti-foaming agents, antiwear agents, seal swellant, friction modifiers, or a combination thereof. 17 . The lubricant composition of claim 15 , wherein the composition further comprises PAOs functionalized with an amine, sulfur, a halogen, or a combination thereof. 18 . The lubricant composition of claim 15 , wherein the plurality of PAOs is derivatized. 19 . The lubricant composition of claim 15 , wherein the lubricant composition comprises about 25 to about 60 wt % of the one or more additives. 20 . The lubricant composition of claim 15 , wherein the lubricant comprises about 10 wt % of additives.
Preparation of halogenated hydrocarbons · CPC title
as complexes, e.g. acetyl-acetonates {(complexes of salts of acids of halogen C07C2/20)} · CPC title
containing metal-to-carbon bond; Metal hydrides · CPC title
containing at least two cyclopentadienyl rings, fused or not · CPC title
in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+ · CPC title
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