Patent classifications
C08F2500/03
Production method for polar olefin polymer and copolymer
An object of the present invention is to provide a novel method of producing a nonpolar olefin polymer (e.g., a copolymer of a nonpolar olefin and a polar olefin). The present invention provides a method of producing a polar olefin polymer or copolymer, the method including the polymerization step of polymerizing a polar olefin monomer using, as a catalyst, a polymerization catalyst composition containing: 1) a metallocene complex represented by Formula (I), which contains a central metal M that is scandium (Sc) or yttrium (Y), a ligand Cp* containing a cyclopentadienyl derivative and being bound to the central metal, monoanionic ligands Q.sup.1 and Q.sup.2, and W neutral Lewis bases L wherein W is an integer of 0 to 3; and 2) an ionic compound composed of a non-coordinating anion and a cation. ##STR00001## ##STR00002##
ETHYLENE-RICH DIENE BLOCK POLYMER HAVING A RANDOM BLOCK AND A POLYETHYLENE BLOCK
A diblock polymer composed of a first block and a second block is provided. The first block is a statistical copolymer comprising units of a 1,3-diene and more than 50 mol % of ethylene units. The second block is a polyethylene with a melting point above 90° C. and a number-average molar mass greater than or equal to 2000 g/mol and less than or equal to 10 000 g/mol. Such a diblock polymer has improved rheology compared to a statistical copolymer of the same microstructure and of the same macrostructure as the first block of the diblock polymer.
ETHYLENE-RICH DIENE BLOCK POLYMER HAVING A RANDOM BLOCK AND A POLYETHYLENE BLOCK
A diblock polymer composed of a first block and a second block is provided. The first block is a statistical copolymer comprising units of a 1,3-diene and more than 50 mol % of ethylene units. The second block is a polyethylene with a melting point above 90° C. and a number-average molar mass greater than or equal to 2000 g/mol and less than or equal to 10 000 g/mol. Such a diblock polymer has improved rheology compared to a statistical copolymer of the same microstructure and of the same macrostructure as the first block of the diblock polymer.
BIS(PHOSPHINO)-PHENOXY NICKEL(II) CATALYSTS FOR THE COPOLYMERIZATION OF ETHYLENE AND ACRYLATE MONOMERS
Processes of polymerizing olefin monomers using catalyst systems and catalysts systems that include a procatalyst having a structure according to formula (I): (I).
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BIS(PHOSPHINO)-PHENOXY NICKEL(II) CATALYSTS FOR THE COPOLYMERIZATION OF ETHYLENE AND ACRYLATE MONOMERS
Processes of polymerizing olefin monomers using catalyst systems and catalysts systems that include a procatalyst having a structure according to formula (I): (I).
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Polymerization of Purge Stream Containing 1-Octene
The present disclosure provides a process. In an embodiment, the process includes providing a purge stream containing octene monomer. The process includes contacting, under polymerization conditions, the purge stream with a bis-biphenylphenoxy catalyst, and forming an octene polymer having an absolute weight average molecular weight (Mw(Abs)) greater than 1,300,000 g/mol and a Mw(Abs)/Mn(Abs) from 1.3 to 3.0.
Polymerization of Purge Stream Containing 1-Octene
The present disclosure provides a process. In an embodiment, the process includes providing a purge stream containing octene monomer. The process includes contacting, under polymerization conditions, the purge stream with a bis-biphenylphenoxy catalyst, and forming an octene polymer having an absolute weight average molecular weight (Mw(Abs)) greater than 1,300,000 g/mol and a Mw(Abs)/Mn(Abs) from 1.3 to 3.0.
Polymerization of C6-C14 a-Olefin Monomers and Polymers Thereof
The present disclosure provides a process. In an embodiment, the process includes contacting, under polymerization conditions, one or more C.sub.6-C.sub.14 α-olefin monomers with a bis-biphenylphenoxy catalyst. The process includes forming a polymer composed of one or more C.sub.6-C.sub.14 α-olefin monomers, and having an absolute weight average molecular weight (Mw.sub.(abs)) greater than 1,300,000 g/mol and a Mw.sub.(abs)/Mn.sub.(abs) from 1.3 to 3.0.
Polymerization of C6-C14 a-Olefin Monomers and Polymers Thereof
The present disclosure provides a process. In an embodiment, the process includes contacting, under polymerization conditions, one or more C.sub.6-C.sub.14 α-olefin monomers with a bis-biphenylphenoxy catalyst. The process includes forming a polymer composed of one or more C.sub.6-C.sub.14 α-olefin monomers, and having an absolute weight average molecular weight (Mw.sub.(abs)) greater than 1,300,000 g/mol and a Mw.sub.(abs)/Mn.sub.(abs) from 1.3 to 3.0.
STERICALLY HINDERED PHOSPHINO-UREA SUPPORTED NICKEL (II) OR PALLADIUM (II) CATALYSTS FOR THE COPOLYMERIZATION OF ETHYLENE AND POLAR COMONOMERS
Processes of polymerizing olefin monomers using catalyst systems and catalysts systems that include a procatalyst having a structure according to formula (I):
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