Catalysts and methods for polymer synthesis
US-9505878-B2 · Nov 29, 2016 · US
US9527933B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9527933-B2 |
| Application number | US-201314031348-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 19, 2013 |
| Priority date | Sep 24, 2012 |
| Publication date | Dec 27, 2016 |
| Grant date | Dec 27, 2016 |
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This invention relates to blends of polyalphaolefins (PAOs) and polyhydrosilane-modified polyolefins, methods to prepare the blends and methods to prepare polyhydrosilane-modified polyolefins.
Opening claim text (preview).
What is claimed is: 1. A process to prepare a modified polyolefin comprising the steps of: (i) contacting a non-metallocene catalyst, a hydrosilylation modifier, and one or more vinyl terminated polyolefins selected from a vinyl terminated polyalphaolefin and a vinyl terminated macromonomer; wherein when the vinyl terminated polyolefin is a vinyl terminated macromonomer, the hydrosilylation modifier is represented by one of more of the formulae: and wherein when the vinyl terminated polyolefin is a vinyl terminated polyalphaolefin, the hydrosilylation modifier is represented by the formula: wherein R 1 is hydrogen, Z′, or a C 1 to a C 20 substituted or unsubstituted hydrocarbyl group; and wherein Z′ is a group represented by the formula: each R 2 , R 3 , R 4 , and R 5 , independently, is a H, or a C 1 to a C 20 substituted or unsubstituted hydrocarbyl group, where R 2 and R 3 and/or R 4 and R 5 may form a cyclic structure with Si; each L, L 1 , L 2 , and L 3 , independently, is a bond or a linking group; m is 1 to 1000; n is 1 to 1000; o is 0 to 1000; each of X 1 and X 2 , independently, is hydrogen or a C 1 to a C 20 substituted or unsubstituted hydrocarbyl group; wherein the vinyl terminated polyolefin is a substituted or unsubstituted hydrocarbyl group having from 20 to about 10,000 carbon atoms and at least 5% allyl chain ends; and (ii) obtaining a modified polyolefin; (iii) adding a polymer; and (iv) obtaining a blend comprising the modified polyolefin; wherein the amount of modified polyolefin is from about 0.5 wt % to about 10 wt %, based on the total weight of the blend. 2. The process of claim 1 , wherein the polymer from step (iii) is added during step (i). 3. The process of claim 1 , wherein the vinyl terminated macromonomer has the following properties: a Mn of at least 200 g/mol, measured by 1 H NMR, comprising of one or more C 4 to C 40 higher olefin derived units, where the higher olefin polymer comprises substantially no propylene derived units; and wherein the higher olefin polymer has at least 5% allyl chain ends. 4. The process of claim 1 , wherein each L 1 , L 2 , and L 3 , independently, is O, S, NR A , PR B , SiR C 2 , or a C 1 to a C 20 substituted or unsubstituted hydrocarbyl group; wherein each R A , R B , and R C , independently, is hydrogen, or a C 1 to a C 20 substituted or unsubstituted hydrocarbyl group. 5. The process of claim 1 , wherein each L 1 , L 2 , and L 3 , independently, is O. 6. The process of claim 1 , wherein the process is carried out in the melt phase. 7. The process of claim 1 , wherein the non-metallocene catalyst is one or more of: chloroplatinic acid, platinum complexes, rhodium complexes, peroxides, Ziegler Natta catalysts, and iridium, cobalt, ruthenium, osmium, nickel, and palladium complexes. 8. The process of claim 1 , wherein the vinyl terminated polyalphaolefin of step (i) is ethylene-based. 9. The process of claim 8 , wherein the vinyl terminated ethylene-based polyalphaolefin is made using a metallocene catalyst system comprising an ionizing activator and a metallocene compound represented by the following structure: 10. The process of claim 9 , wherein the ionizing activator is dimethylaniliniumtetrakis(perfluoronaphthyl)borate. 11. The process of claim 1 , wherein the vinyl terminated polyalphaolefin of step (i) is vinyl terminated polyethylene.
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