Process for making crosslinked cable insulation using high melt strength ethylene-based polymer made in a tubular reactor and optionally modified with a branching agent
US-11912852-B2 · Feb 27, 2024 · US
US9890231B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9890231-B2 |
| Application number | US-201615161663-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 23, 2016 |
| Priority date | Nov 20, 2008 |
| Publication date | Feb 13, 2018 |
| Grant date | Feb 13, 2018 |
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To provide an industrially useful α-olefin•((meth)acrylic acid)-based olefin copolymer having both a high molecular weight and a high comonomer content, a catalyst component capable of realizing a production of two different kinds of α-olefin•((meth)acrylic acid)-based olefin copolymers, and a production process using the catalyst. An α-olefin•((meth)acrylic acid)-based olefin copolymer is produced by using a metal complex complexed with a ligand represented by the following formula (Y is phosphorus or arsenic) for a catalyst composition.
Opening claim text (preview).
The invention claimed is: 1. A ternary copolymer of an ethylene, an α-olefin having a carbon number of 3 to 10 and a (meth)acrylic acid or ester represented by CH 2 ═C(R 18 )CO 2 (R 19 ), wherein R 18 is a hydrogen atom or an alkyl group having a carbon number of 1 to 10, and R 19 is a hydrogen atom or an alkyl group having a carbon number of 1 to 30, which may contain a hydroxyl group, an alkoxy group or an epoxy group on an arbitrary position, the ternary copolymer satisfying the following requirements (a) and (b): (a) the ratio Mw/Mn of the weight average molecular weight (Mw) to the number average molecular weight (Mn) satisfies the following relationship: 1.5≦Mw/Mn≦3 (b) the melting point Tm (° C.), the α-olefin content [C] (mol %) and the polar group-containing vinyl monomer content [X] (mol %) from the (meth)acrylic acid or ester satisfy the following relationship: 60 ≦Tm≦ 135−6.4×([ C ]+[ X ]) wherein Tm is a peak temperature of a melting curve obtained by the measurement using a differential scanning calorimeter (DSC), and when a plurality of melting peaks are detected, Tm is the temperature of the maximum peak out of detected peaks. 2. The ternary copolymer as claimed in claim 1 , wherein a phase angle δ(G*=0.1 MPa at G*−0.1 MPa) as measured by a rotary rheometer is from 40 to 75°. 3. The ternary copolymer as claimed in claim 1 , wherein a difference T90−T10 (° C.) between a temperature T10 (° C.) allowing 10 wt % of the total to elute in an integrated elution curve as determined by a continuous temperature rising elution fractionation method (TREF) and a temperature T90 (° C.) allowing 90 wt % of the total to elute, and a weight average elution temperature Tw (° C.) satisfy the following relationship: 28−0.3 ×Tw≦T 90− T 10≦41−0.3× Tw. 4. The ternary copolymer as claimed in claim 1 , wherein the carbon number of the α-olefin is any of 4 to 8.
Nickel compounds · CPC title
Narrow molecular weight distribution, i.e. Mw/Mn < 3 · CPC title
the oxygen atom being part of a five-membered ring · CPC title
Ethene · CPC title
Monomers containing five or more carbon atoms · CPC title
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