Ethylene polymerization
AssigneeBorealis Technology Oy
InventorsVidar Almquist, Paul Allemeersch, Roger Goris, Ann Kristin Lindahl
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AssigneeBorealis Technology Oy
InventorsVidar Almquist, Paul Allemeersch, Roger Goris, Ann Kristin Lindahl
Estimating the term…
Ths invention provides a process for the preparation of a polyethylene, in particular an HDPE suitable for blow moulding of HIC, which comprises polymerizing ethylene and, optionally an ethylenically unsaturated comonomer copolymerizable therewith, in the presence of a catalyst comprising a first silica-supported chromium catalyst having a pore volume of at least 2 mL/g, a surface area of at least 350 m2/g and a chromium content of 0.1 to 1.0% by weight and a second silica-supported chromium catalyst having a pore volume of at least 2 mL/g, a surface area of at least 450 m2/g and a chromium content of 0.1 to 1.0% by weight, wherein the silica support of said first catalyst also comprises alumina and the silica support of said second catalyst also comprises titanium, and preferably a co-catalyst.
A process for the preparation of a polyethylene which comprises polymerizing ethylene and, optionally, an ethylenically unsaturated comonomer copolymerizable therewith, in the presence of a catalyst comprising a first silica-supported chromium catalyst having a pore volume of at least 2 mL/g, a surface area of at least 350 m2/g and a chromium content of 0.1 to 1.0% by weight and a second silica-supported chromium catalyst having a pore volume of at least 2 mL/g, a surface area of at least 450 m2/g and a chromium content of 0.1 to 1.0% by weight, wherein the silica support of said first catalyst also comprises alumina and the silica support of said second catalyst also comprises titania, wherein no co-catalyst is used.
A process for the preparation of a polyethylene which comprises polymerizing ethylene and, optionally, an ethylenically unsaturated comonomer copolymerizable therewith, in the presence of a catalyst comprising a first silica-supported chromium catalyst having a pore volume of at least 2 mL/g, a surface area of at least 350 m2/g and a chromium content of 0.1 to 1.0% by weight and a second silica-supported chromium catalyst having a pore volume of at least 2 mL/g, a surface area of at least 450 m2/g and a chromium content of 0.1 to 1.0% by weight, wherein the silica support of said first catalyst also comprises alumina and the silica support of said second catalyst also comprises titania wherein a trialkylboron co-catalyst is also used.
A process for ethylene polymerization in which ethylene is copolymerized with a C3-10 α-olefin comonomer in the presence of a first ethylene polymerization catalyst wherein a second catalyst which is a titania:silica supported chromium catalyst is used to reduce the quantity of comonomer used and wherein no co-catalysts are used.
A process for ethylene polymerization in which ethylene is copolymerized with a C3-10 α-olefin comonomer in the presence of a first ethylene polymerization catalyst wherein a second catalyst which is a titania:silica supported chromium catalyst is used to reduce the quantity of comonomer used and wherein said first and second catalysts are used together with a trialkylboron co-catalyst.
A process for the preparation of a high density polyethylene containing catalyst residues of titanium, chromium, aluminum, silicon and optionally also boron, having a MFR2 of at least 0.2 g/10 min, an MFR21 of at least 20 g/10 min and a bottle ESCR f50 of at least 280 hours, said process comprising polymerizing ethylene and, optionally, an ethylenically unsaturated comonomer copolymerizable therewith, in the presence of a catalyst comprising an alumina:silica supported chromium catalyst and a titanium:silica supported chromium catalyst having a pore volume of at least 2 mL/g, a surface area of at least 350 ma first silica ethylene polymerization in which ethylene is copolymerized with a C3-10 α-olefin comonomer in the presence of a first ethylene polymerization catalyst wherein a second catalyst which is a titania:silica supported chromium catalyst is used to reduce the quantity of comonomer used.
Dependencies are inferred from the claim text.