Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US10246527B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10246527-B2 |
| Application number | US-201013509257-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 3, 2010 |
| Priority date | Nov 11, 2009 |
| Publication date | Apr 2, 2019 |
| Grant date | Apr 2, 2019 |
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A power cable includes a conductor surrounded by one or more layers. At least one of the layers can include a polymer composition having an electric conductivity of 0.50×10 −15 S/m or less when measured according to DC conductivity method using a tape sample. The polymer composition can include a polyolefin which is obtainable by a high pressure polymerization process. This process includes: compressing one or more monomers under pressure in a compressor, in which a compressor lubricant, such as mineral oil is used for lubrication; polymerizing a monomer optionally together with one or more comonomers in a polymerization zone; and separating the obtained polyolefin from the unreacted products and recovering the separated polyolefin in a recovery zone.
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What is claimed is: 1. A direct current (DC) power cable comprising a conductor surrounded by at least an inner semiconductive layer, an insulation layer and an outer semiconductive layer, in that order, wherein the insulation layer comprises a polymer composition having an electric conductivity of 0.50×10 −15 S/m or less, when measured according to DC conductivity method using a tape sample consisting of the polymer composition as described under “Determination Methods”, the polymer composition comprising a polyolefin which is a low density polyethylene (LDPE) copolymer of ethylene with a polyunsaturated comonomer obtained by a high pressure polymerization process comprising: (a) compressing ethylene with the polyunsaturated comonomer under pressure in a compressor, wherein a compressor lubricant is used for lubrication, (b) polymerizing ethylene with the polyunsaturated comonomer in a polymerization zone, (c) separating the obtained polyolefin from the unreacted products and recovering the separated polyolefin in a recovery zone, wherein the compressor lubricant comprises a mineral oil. 2. The direct current (DC) power cable according to claim 1 , wherein the polymer composition has an electrical conductivity of 0.48×10 −15 S/m or less, when measured according to DC conductivity method using a tape sample consisting of the polymer composition, as described under “Determination Methods”. 3. The direct current (DC) power cable according to claim 1 , wherein the LDPE copolymer of ethylene is unsaturated. 4. The direct current (DC) power cable of claim 1 , wherein in step a), the compressor lubricant comprises white oil as the mineral oil and is suitable for production of polymers for food or medical industry; and wherein the polymerization step b) is operated at a pressure up to 4000 bar, and at a temperature of up to 400° C. 5. The direct current (DC) power cable of claim 1 , wherein the mineral oil has a viscosity of at least 8.5×10-6 m2/s at 100° C. 6. A process for producing the direct current (DC) power cable according to claim 1 , comprising; applying at least the inner semiconductive layer, the insulation layer and the outer semiconductive layer on the conductor in that order wherein the insulation layer comprises the polymer composition; and optionally crosslinking at least the obtained layer of the power cable. 7. The direct current (DC) power cable of claim 1 , wherein the mineral oil is a white mineral oil. 8. The direct current (DC) power cable of claim 1 , wherein the mineral oil comprises 5% or less by weight of a hydrocarbon having less than 25 carbon atoms. 9. The direct current (DC) power cable of claim 1 , wherein the mineral oil comprises a hydrocarbon having an average molecular weight of 480 or more.
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