Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US10072111B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10072111-B2 |
| Application number | US-201815876532-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 22, 2018 |
| Priority date | Dec 15, 2014 |
| Publication date | Sep 11, 2018 |
| Grant date | Sep 11, 2018 |
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A solid, spheroidal polymerization catalyst having a particle size distribution characterized by a Dm*/Dn of less than 3.0, the catalyst comprising a phosphinimine catalyst, a cocatalyst and a magnesium chloride support. A process for the polymerization of ethylene with one or more alpha olefin catalyzed by a solid, spheroidal polymerization catalyst having a particle size distribution characterized by a Dm*/Dn of less than 3.0, the catalyst comprising a phosphinimine catalyst, a cocatalyst and a magnesium chloride support.
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The invention claimed is: 1. A method of making a spheroidal olefin polymerization catalyst having a particle size distribution characterized by a Dm*/Dn of less than 3.0, wherein said method comprises: i) combining a dialkylmagnesium compound with a non-protic ether, ii) combining the product of step i) with a source of chloride anion, iii) treating the product of step ii) to substantially remove to provide a MgCl 2 support containing less than about 2.5 wt. % of the non-protic ether, iv) combining the product of step iii) with a phosphinimine catalyst and a cocatalyst. 2. The method of claim 1 wherein treating the product of step ii) to remove the non-protic ether comprises heating the product of step ii). 3. The method of claim 1 wherein treating the product of step ii) to remove the non-protic ether comprises adding an alkylaluminumchloride compound. 4. The method of claim 1 wherein the phosphinimine catalyst has the formula: (L)(PI)MX 2 , where M is Ti, Zr or Hf; PI is a phosphinimine ligand having the formula R 3 P═N—, where R is independently selected from the group consisting of hydrogen, halogen, and C 1 -C 20 hydrocarbyl; L is a ligand selected from the group consisting of cyclopentadienyl, substituted cyclopentadienyl, indenyl, substituted indenyl, fluorenyl, and substituted fluorenyl; and X is an activatable ligand. 5. The method of claim 1 wherein the phosphinimine catalyst has the formula: (L)((t-Bu) 3 P═N)TiX 2 , where L is a cyclopentadienyl ligand, a substituted cyclopentadienyl ligand, an indenyl ligand, or a substituted indenyl ligand; and X is an activatable ligand. 6. The method of claim 1 wherein the phosphinimine catalyst has the formula: (L)((t-Bu) 3 P═N)TiX 2 , where L is a substituted cyclopentadienyl ligand, or a substituted indenyl ligand; and X is an activatable ligand. 7. The method of claim 1 wherein the cocatalyst is selected from the group consisting of ionic activators, alkylaluminoxanes and mixtures thereof.
organic · CPC title
supported on a carrier, e.g. silica, MgCl2, polymer · CPC title
Magnesium halide as support anhydrous or hydrated or complexed by means of a Lewis base for Ziegler-type catalysts · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Cp or analog not bridged to a non-Cp X ancillary anionic donor · CPC title
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