Olefin Polymerization Catalyst Systems and Methods for Making the Same
US-2018155459-A1 · Jun 7, 2018 · US
US12312368B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12312368-B2 |
| Application number | US-202017614747-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 20, 2020 |
| Priority date | May 29, 2019 |
| Publication date | May 27, 2025 |
| Grant date | May 27, 2025 |
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Improved preparation process for silica supported catalyst systems, which comprise a specific class of metallocene complexes in combination with a boron containing cocatalyst and an aluminoxane cocatalyst and use of the new, improved catalyst system.
Opening claim text (preview).
The invention claimed is: 1. A process for the preparation of a supported catalyst system, wherein the catalyst system comprises: (i) a metallocene complex; (ii) a cocatalyst system comprising a boron containing cocatalyst and an aluminoxane cocatalyst; and (iii) a porous inorganic support; whereby the process comprises the steps of: a) reacting the porous inorganic support with a first portion of the aluminoxane cocatalyst in a first hydrocarbon solvent to obtain an aluminoxane cocatalyst treated support; b) reacting the metallocene complex with a second portion of the aluminoxane cocatalyst in a second hydrocarbon solvent, wherein the first portion of the aluminoxane cocatalyst added in step a) is from 75.0 to 97.0 wt % of the total amount of the aluminoxane cocatalyst and the second portion of the aluminoxane cocatalyst added in step b) is from 3.0 to 25.0 wt % of the total amount of aluminoxane cocatalyst; c) adding the boron containing cocatalyst to the solution obtained in step b) to obtain a solution of the metallocene complex, boron containing cocatalyst, and aluminoxane cocatalyst, wherein the metallocene complex includes a metal ion M and whereby the boron containing cocatalyst is added in an amount such that the molar ratio of boron/M is in the range of from 0.1:1 to 10:1; d) adding the solution obtained in step c) to the aluminoxane cocatalyst treated support obtained in step a) to form the supported catalyst system; and optionally e) drying the so obtained supported catalyst system. 2. The process as claimed in claim 1 , wherein the metallocene complex is of formula (I)-(III): wherein each X independently is a sigma-donor ligand; M is Ti, Zr, Hf, Y, Sc, La, or an element from the lanthanides; each Cp independently is an unsubstituted or substituted cyclopentadienyl containing ligand or an unsubstituted or substituted fused cyclopentadienyl containing ligand; Q is —O or —NW or —PW; W is an organic group or H; L is a carbon, silicon or germanium based bridge in which one to four backbone atoms link the ligands; and r is an integer such that the oxidation state of the metal is satisfied. 3. The process as claimed in claim 1 , wherein the metallocene complex is of formula (VI): wherein each X independently is a sigma-donor ligand; M is a group 4 metal; L is a carbon, silicon, or germanium based bridge in which one to four backbone atoms link the ligands; and each Ind is a substituted or unsubstituted indenyl, or a substituted or unsubstituted fused indenyl. 4. The process as claimed in claim 1 , wherein the metallocene complex is of formula (IV): wherein each X independently is a sigma-donor ligand; M is Zr or Hf, L is a carbon, silicon, or germanium based divalent bridge in which one or two backbone atoms link the ligands; each Ar is an aryl or heteroaryl group having 3 to 20 carbon atoms; each R 1 independently is hydrogen, a linear or branched C 1 -C 6 -alkyl group, a C 7-20 -arylalkyl group, a C 7-20 -alkylaryl group, a C 6-20 -aryl group, or an OY group, wherein Y is a C 1-10 -hydrocarbyl group, or wherein two adjacent R 1 groups taken together with the phenyl carbons to which they are bonded form a ring; each R 2 independently is a CHR 8′ —R 8 group, with R 8 being H, a linear or branched C 1-6 -alkyl group, a C 3-8 -cycloalkyl group, a C 6-10 -aryl group, or a heteroaryl group having 3 to 20 carbon atoms optionally substituted by one to three groups R 11 , and R 8′ is H or a C 1-6 alkyl; R 3 is a linear or branched C 1 -C 6 -alkyl group, a C 7-20 -arylalkyl group, a C 7-20 -alkylaryl group, or C 6 -C 20 -aryl group; R 4 is a C(R 9 ) 3 group, with each R 9 independently being a linear or branched C 1 -C 6 -alkyl group; R 5 and R 6 are each independently hydrogen or an aliphatic C 1 -C 20 -hydrocarbyl group optionally containing one or more heteroatoms from groups 14-16 of the periodic table of elements, or wherein R 5 and R 6 taken together form a 5 membered saturated carbon ring which is optionally substituted by n groups R 10 , n being from 0 to 4, and each R 10 independently is a C 1 -C 20 -hydrocarbyl group, or a C 1 -C 20 -hydrocarbyl radical optionally containing one or more heteroatoms belonging to groups 14-16 of the periodic table of elements; R 7 is H, a linear or branched C 1 -C 6 -alkyl group, or an aryl or heteroaryl group having 3 to 20 carbon atoms optionally substituted by one to three groups R 11 ; and each R 11 independently is hydrogen, a linear or branched C 1 -C 6 -alkyl group, a C 7-20 -arylalkyl group, a C 7-20 -alkylaryl group, a C 6-20 -aryl group, or an OY group, wherein Y is a C 1-10 -hydrocarbyl group. 5. The process as claimed in claim 1 , wherein the metallocene complex is of formula (IX): wherein each X independently is a sigma-donor ligand; M is a group 4 metal; L is a carbon, silicon, or germanium based divalent bridge in which one or two backbone atoms link the ligands; R 2 and R 2′ are, independently from each other, H, —OSi(C 1-10 -hydrocarbyl) 3 , or CHR 8′ —R 8 group; R 8 being H, a linear or branched C 1-6 -alkyl group, a C 3-8 -cycloalkyl group, a C 6-10 -aryl group, or an optionally substituted heteroaryl group having 3 to 20 carbon atoms; R 8′ is H or a C 1-6 alkyl; R 5 -R 6 are each independently hydrogen or a C 1 -C 20 -hydrocarbyl group optionally containing one or more heteroatoms from groups 14-16 of the periodic table of elements, or R 5 and R 6 taken together form a 5 membered saturated carbon ring which is optionally substituted by n groups R 10 , n being from 0 to 4; R 5′ —R 6′ are each independently hydrogen or a C 1 -C 20 -hydrocarbyl group optionally containing one or more heteroatoms from groups 14-16 of the periodic table of elements, or R 5′ and R 6′ taken together form a 5 membered saturated carbon ring which is optionally substituted by n groups R 10 , n being from 0 to 4; each R 10 is independently a C 1 -C 20 -hydrocarbyl group, or a C 1 -C 20 -hydrocarbyl radical optionally containing one or more heteroatoms belonging to groups 14-16 of the periodic table of elements; Ar and Ar′ are independently phenyl, naphthyl, anthracenyl, pyridyl, thiophenyl, 2-alkylthiophenyl, benzothiophenyl, pyrrolyl, furanyl, or 2-alkylfuranyl optionally substituted by up to 5 groups R 1 ; and each R 1 independently is hydrogen, a linear or branched C 1 -C 6 -alkyl group, a C 7-20 -arylalkyl group, a C 7-20 -alkylaryl group, C 6-20 -aryl group, or an OY group, wherein Y is a C 1-10 -hydrocarbyl group. 6. The process as claimed in claim 1 wherein the porous inorganic support is a silica support and the metallocene complex is of formula (V): wherein M is Zr or Hf; each X independently is a sigma-donor ligand; L is a divalent bridge selected from —R′ 2 C—, —R′ 2 C—CR′ 2 -, —R′ 2 Si—, —R′ 2 Si—SiR′ 2 —, and —R′ 2 Ge—, wherein each R′ is independently a hydrogen atom or a C 1 -C 20 -hydrocarbyl group optionally containing one or
as molar percentages · CPC title
Viscosity · CPC title
Melt flow index or melt flow ratio · CPC title
Propene · CPC title
two cyclopentadienyl rings being mutually bridged · CPC title
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