Process for producing polyethylene
AssigneeBorealis AG
InventorsVictor SUMERIN, Joseph THORMAN, Jani AHO, Markku VAHTERI, Ravindra TUPE, Jarmo KELA
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AssigneeBorealis AG
InventorsVictor SUMERIN, Joseph THORMAN, Jani AHO, Markku VAHTERI, Ravindra TUPE, Jarmo KELA
Estimating the term…
The present invention relates to a process for producing ethylene copolymers in a multistage process comprising at least one slurry phase polymerization stage and at least one gas phase polymerization stage in the presence of Ziegler Natta catalyst comprising a solid catalyst component, a cocatalyst of a compound of group 13 metal and an external additive selected from alkoxysilanes of formula (1) R1nSi(OR2)4-n, (I) where n is an integer 0 to 3, each R1 are equal or different and are selected among H, halogen, alkyl groups of 1 to 6 10 carbon atoms optionally substituted with one or more halogen atoms, alkenyl groups of 2 to 6 carbon atoms optionally substituted with one or more halogen atoms, and aryl groups of 6 to 12 carbon atoms optionally substituted with one or more halogen atoms, or the R1 groups can form with the Si atom they are linked to a ring of 3 to 8 ring atoms, provided that all R1 are not hydrogen, R2 are equal or different and are selected among alkyl groups of 1 to 6 carbon atoms optionally substituted with one or more halogen atoms, alkenyl groups of 2 to 6 carbon atoms optionally substituted with one or more halogen atoms, and aryl groups of 6 to 12 carbon atoms optionally substituted with one or more halogen atoms, or the OR2 groups can form with the Si atom they are linked to a ring of 3 to 8 ring atoms, halogen is Br, Cl or F. The invention further relates to the catalysts and use thereof in said multistage process r for producing ethylene copolymers having melt flow rate ratio FRR21/5 at least 40 and/or polydispersity index PDI of at least 27.
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The Ziegler-Natta catalyst according to claim 14, wherein in the formula (I) n is an integer 1 to 3, all R1 groups are the same or different and are hydrogen or alkyl groups of 1 to 6 carbon atoms or aryl groups of 6 to 12 carbon atoms, provided that all R1 are not hydrogen, and all R2 groups are the same and are alkyl groups of 1 to 3 carbon atoms.
The Ziegler-Natta catalyst according to claim 14, wherein each R1 is independently hydrogen, methyl or ethyl, R2 is methyl or ethyl, provided that at least one R1 is methyl or ethyl, and n is 1 or 2.
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The Ziegler-Natta catalyst according to claim 14, wherein the solid Ziegler-Natta catalyst component comprises a titanium compound, an aluminum compound, and an internal organic compound of formula (II).
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The Ziegler-Natta catalyst according to claim 14, wherein the solid Ziegler-Natta catalyst component comprises a solid MgCl2 supported component which is prepared by a method comprising the steps:
The Ziegler-Natta catalyst according to claim 14, wherein the external additive is selected from the group consisting of dimethoxydimethylsilane, trimethoxymethylsilane, diethoxydimethylsilane, dimethoxydiethyl silane, dimethoxydi-n-propylsilane, dimethoxy(methyl)silane, vinylmethyldimethoxysilane, chloromethyl(methyl)dimethoxysilane, dimethoxymethylphenylsilane, 3-chloropropyldimethoxymethylsilane, trimethoxy(3,3,3-trifluoropropyl)silane, and 3-chloropropyltrimethoxysilane.
The Ziegler-Natta catalyst according to claim 14, wherein the cocatalyst is an organoaluminium compound.
A Ziegler-Natta catalyst comprising:
Dependencies are inferred from the claim text.