Olefin polymerization catalyst and method for producing olefin oligomer
US-2018016367-A1 · Jan 18, 2018 · US
US12473387B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12473387-B2 |
| Application number | US-202318304743-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 21, 2023 |
| Priority date | Oct 24, 2017 |
| Publication date | Nov 18, 2025 |
| Grant date | Nov 18, 2025 |
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A preparation method for a copolymer includes the step(s) of contacting an olefin and an unsaturated carboxylic acid shown in Formula II or a derivative of the unsaturated carboxylic acid shown in Formula II with a catalyst and optionally a chain transfer agent for reaction in the presence of an alkane solvent to obtain the copolymer. The copolymer is a spherical and/or spherical-like copolymer.
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The invention claimed is: 1 . A preparation method for a copolymer, comprising: in a reaction system, contacting a C 2 -C 16 α-olefin and an unsaturated carboxylic acid of Formula II or a derivative of the unsaturated carboxylic acid of Formula II with a catalyst and optionally a chain transfer agent for reaction in the presence of an alkane solvent to obtain the copolymer, wherein in the Formula II, each of L 1 , L 2 , and L 3 is independently selected from the group consisting of H and C 1 -C 30 alkyl, and L 4 is a C 1 -C 30 alkylene having a side group selected from the group consisting of C 6 -C 20 aryl, C 1 -C 20 alkyl, and C 1 -C 20 alkoxy, and wherein the catalyst comprises a main catalyst and a co-catalyst, and the main catalyst is selected from at least one metal complex of Formula V: wherein in the Formula V, R 7 -R 10 are H, and R 1 -R 6 are identical to or different from each other and each independently selected from the group consisting of H and C 1 -C 6 alkyl, M is nickel, X is a halogen, n is 2, wherein the reaction is carried out at a reaction temperature in a range from 0° C. to 50° C., wherein the co-catalyst is selected from the group consisting of an organic aluminum compound and an organic boron compound, and wherein the produced copolymer is in the form of spherical and/or spherical-like particles, at least part of the spherical and/or spherical-like particles of the copolymer have a cavity therein. 2 . The preparation method according to claim 1 , wherein in Formula V, R 7 -R 10 are H, and R 1 -R 6 are identical to or different from each other and each is independently selected from the group consisting of H and C 1 -C 3 alkyl. 3 . The preparation method according to claim 1 , wherein the organic aluminum compound is one or more selected from the group consisting of alkyl aluminoxane, alkylaluminum, and alkylaluminum halides; and the organic boron compound is selected from the group consisting of aryl boron and borate. 4 . The preparation method according to claim 1 , wherein a concentration of the main catalyst in a reaction system is 0.00001-100 mmol/L; when the co-catalyst is the organic aluminum compound, a molar ratio of aluminum in the co-catalyst and M in the main catalyst is (10-10000000):1; and when the co-catalyst is the organic boron compound, a molar ratio of boron in the co-catalyst and M in the main catalyst is (0.1-1000):1. 5 . The preparation method according to claim 1 , wherein the chain transfer agent is present in the reaction system and is one or more selected from the group consisting of aluminum alkyl, magnesium alkyl, and zinc alkyl, and a molar ratio of the chain transfer agent and M in the main catalyst is (0.1-2000):1. 6 . The preparation method according to claim 1 , wherein a concentration of the unsaturated carboxylic acid of Formula II or the unsaturated carboxylic acid derivative of Formula II in the reaction system is 0.01-6000 mmol/L. 7 . The preparation method according to claim 1 , wherein the reaction is carried out for 10-200 min. 8 . The preparation method according to claim 1 , wherein the copolymer has a number-average molecular weight of 5000-200000. 9 . The preparation method according to claim 1 , wherein a volume of the cavity in the number of the spherical and/or spherical-like particles of the copolymer having a cavity therein is 5-99% of a volume of the spherical and/or spherical-like particles of the copolymer. 10 . The preparation method according to claim 9 , wherein the spherical and/or spherical-like particles of the copolymer have a density of 0.3000-0.8500 g/cm 3 , measured according to GB/T6343-2009. 11 . The preparation method according to claim 9 , wherein an average particle size of the spherical and/or spherical-like particles of the copolymer is 0.1-50.0 mm. 12 . The preparation method according to claim 9 , wherein the produced copolymer comprises a structural unit derived from the C 2 -C 16 α-olefin and a structural unit of Formula I or a structural unit of a derivative of the Formula I, wherein, in the Formula I, each of L 1 , L 2 , and L 3 is independently selected from the group consisting of H and C 1 -C 30 alkyl, and L 4 is a C 1 -C 30 alkylene having a side group selected from the group consisting of C 6 -C 20 aryl, C 1 -C 20 alkyl, and C 1 -C 20 alkoxy, and the derivative of the Formula I is a IIA, IIIA or IIB Group metal salt of the Formula I. 13 . The preparation method according to claim 12 , wherein, in the copolymer, a content of the structural unit of Formula I or the structural unit of the derivative of Formula I is 0.2-15.0 mol %. 14 . The preparation method according to claim 12 , wherein, in Formula I, L 1 and L 2 are H, L 3 is selected from the group consisting of H and C 1 -C 10 alkyl and L 4 is a C 1 -C 10 alkylene having a side group selected from the group consisting of C 6 -C 10 aryl and C 1 -C 10 alkyl.
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