Polymer blends of cycloolefin polymers and polyolefins
First Claim
1. A process for preparing a polymer blend comprising (i) combining at least one of (A) a finely particulate cycloolefin polymer, and (B) a finely particulate polyolefin, with (C) at least one block copolymer, to form a mixture;
- and (ii) processing the mixture at an elevated temperature, under the action of shear forces, to form the polymer blend, wherein;
in the polymer blend, (A) is present in an amount of 0 to 95 parts by weight, (B) is present in an amount of 0 to 95 parts by weight, (C) is present in an amount of 0.1 to 99 parts by weight and, the sum of the amounts of (A), (B) and (C) present is 100 parts by weight;
the finely particulate cycloolefin polymer (A) comprises at least one monomer of formula I, II, III, IV, V and VI and at least one monomer of formula VII and VIII, but said cycloolefin polymer is not a block copolymer;
the block copolymer (C) is obtained by polymerizing;
a) 0.1 to 95% by weight, with respect to the total amount of monomers employed, of at least one monomer of the formula I, II, III, IV, V and VI,b) 0 to 95% by weight, with respect to the total amount of monomers employed, of a cycloolefin of the formula VII, andc) 0 to 99% by weight, with respect to the total amount of monomers employed, of at least one acyclic olefin of the formula VIII,at a temperature of -78°
to 150°
C. and a pressure 0.01 to 64 bar, in the presence of a catalyst comprising a cocatalyst and a metallocene, and at a molecular weight distribution Mw /Mn of less than 2, always with respect to the polymer block forming, the reaction conditions are changed one or more times in such a way that the monomer/comonomer ratio changes by at least 10% or a further polymerizable monomer of the formulae I-VIII is metered into the monomer or the monomers; and
the monomers of the formula I, II, III, IV, V, VI, VII and VIII are;
##STR12## in which R1, R2, R3, R4, R5, R6, R7, R8, R9, R10, R11, and R12 are identical or different and are a hydrogen atom or a C1 -C8 -alkyl radical and n is a number from 2 to 10.
1 Assignment
0 Petitions
Accused Products
Abstract
For producing 100 parts by weight of a polymer blend 0 to 95 parts by weight of a finely divided polyolefin, 0 to 95 parts by weight of finely divided cycloolefin polymer and 0.1 to 99 parts by weight of a blockpolymer (which consists of monomeric units derived from norbornen and monomeric units derived from aliphatic monocycloolefins Cn H2n and/or aliphatic 1-olefin, such as ethylene or propylene, are mixed and the mixture is processed under heat and shear forces. The block copolymer acts as phase mediator and contains in different blocks different proportions of the monomer units used.
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Citations
17 Claims
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1. A process for preparing a polymer blend comprising (i) combining at least one of (A) a finely particulate cycloolefin polymer, and (B) a finely particulate polyolefin, with (C) at least one block copolymer, to form a mixture;
- and (ii) processing the mixture at an elevated temperature, under the action of shear forces, to form the polymer blend, wherein;
in the polymer blend, (A) is present in an amount of 0 to 95 parts by weight, (B) is present in an amount of 0 to 95 parts by weight, (C) is present in an amount of 0.1 to 99 parts by weight and, the sum of the amounts of (A), (B) and (C) present is 100 parts by weight; the finely particulate cycloolefin polymer (A) comprises at least one monomer of formula I, II, III, IV, V and VI and at least one monomer of formula VII and VIII, but said cycloolefin polymer is not a block copolymer; the block copolymer (C) is obtained by polymerizing; a) 0.1 to 95% by weight, with respect to the total amount of monomers employed, of at least one monomer of the formula I, II, III, IV, V and VI, b) 0 to 95% by weight, with respect to the total amount of monomers employed, of a cycloolefin of the formula VII, and c) 0 to 99% by weight, with respect to the total amount of monomers employed, of at least one acyclic olefin of the formula VIII, at a temperature of -78°
to 150°
C. and a pressure 0.01 to 64 bar, in the presence of a catalyst comprising a cocatalyst and a metallocene, and at a molecular weight distribution Mw /Mn of less than 2, always with respect to the polymer block forming, the reaction conditions are changed one or more times in such a way that the monomer/comonomer ratio changes by at least 10% or a further polymerizable monomer of the formulae I-VIII is metered into the monomer or the monomers; andthe monomers of the formula I, II, III, IV, V, VI, VII and VIII are;
##STR12## in which R1, R2, R3, R4, R5, R6, R7, R8, R9, R10, R11, and R12 are identical or different and are a hydrogen atom or a C1 -C8 -alkyl radical and n is a number from 2 to 10. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17)
- and (ii) processing the mixture at an elevated temperature, under the action of shear forces, to form the polymer blend, wherein;
Specification