WO2006101754A1 - Moisture crosslinkable polymeric composition-improved heat aging performance - Google Patents

Moisture crosslinkable polymeric composition-improved heat aging performance Download PDF

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Publication number
WO2006101754A1
WO2006101754A1 PCT/US2006/008368 US2006008368W WO2006101754A1 WO 2006101754 A1 WO2006101754 A1 WO 2006101754A1 US 2006008368 W US2006008368 W US 2006008368W WO 2006101754 A1 WO2006101754 A1 WO 2006101754A1
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Prior art keywords
antioxidant
polymeric composition
crosslinkable polymeric
moisture crosslinkable
silane
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PCT/US2006/008368
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English (en)
French (fr)
Inventor
Michael B. Biscoglio
Mohamed Esseghir
Kenneth T. Devlin
David P. Wright
Yimsan Gau
Salvatore P. Shurott
Joseph Mehalick
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Dow Global Technologies LLC
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Dow Global Technologies LLC
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Priority to US11/817,245 priority Critical patent/US20080176981A1/en
Priority to MX2007011437A priority patent/MX2007011437A/es
Priority to EP06737532.9A priority patent/EP1863873B1/en
Priority to CA2599793A priority patent/CA2599793C/en
Priority to JP2008501917A priority patent/JP5415754B2/ja
Publication of WO2006101754A1 publication Critical patent/WO2006101754A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F255/00Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/0008Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/0008Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • C08K5/005Stabilisers against oxidation, heat, light, ozone
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L51/06Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D123/00Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers
    • C09D123/02Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B3/00Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
    • H01B3/18Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances
    • H01B3/30Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes
    • H01B3/44Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes vinyl resins; acrylic resins
    • H01B3/441Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes vinyl resins; acrylic resins from alkenes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/22Compounds containing nitrogen bound to another nitrogen atom
    • C08K5/24Derivatives of hydrazine
    • C08K5/25Carboxylic acid hydrazides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/36Sulfur-, selenium-, or tellurium-containing compounds
    • C08K5/41Compounds containing sulfur bound to oxygen
    • C08K5/42Sulfonic acids; Derivatives thereof

Definitions

  • This invention relates to a moisture-crosslinkable polymeric composition.
  • the polymeric composition is particularly useful as an insulation layer for low to high voltage wire-and-cable applications.
  • acidic silanol condensation catalysts enhances the cure rates of moisture-crosslinkable polymeric compositions.
  • the acidic catalysts also promote the decomposition of olefinic polymers. Therefore, these acid-containing polymeric compositions have required the use of antioxidants at very high concentrations to achieve heat stabilization.
  • the invented moisture-crosslinkable polymeric composition comprises (a) a silane-functionalized olefinic polymer, (b) an acidic silanol condensation catalyst, and (c) an antioxidant, being a secondary amine substituted with two aromatic groups.
  • Suitable silane-functionalized olefinic polymers include silane-functionalized polyethylene polymers, silane-functionalized polypropylene polymers, and blends thereof.
  • the silane-functionalized olefinic polymer is selected from the group consisting of (i) a copolymer of ethylene and a hydrolyzable silane, (ii) a copolymer of ethylene, a hydrolyzable silane, and one or more C3 or higher alpha- olefins and unsaturated esters, (iii) a homopolymer of ethylene, having a hydrolyzable silane grafted to its backbone, and (iv) a copolymer of ethylene and one or more C3 or higher alpha-olefins and unsaturated esters, having a hydrolyzable silane grafted to its backbone.
  • Polyethylene polymer is a homopolymer of ethylene or a copolymer of ethylene and a minor proportion of one or more alpha- olefins having 3 to 12 carbon atoms, and preferably 4 to 8 carbon atoms, and, optionally, a diene, or a mixture or blend of such homopolymers and copolymers.
  • the mixture can be a mechanical blend or an in situ blend.
  • alpha- olefins are propylene, 1-butene, 1-hexene, 4-methyl-l-pentene, and 1-octene.
  • the polyethylene can also be a copolymer of ethylene and an unsaturated ester such as a vinyl ester (e.g., vinyl acetate or an acrylic or methacrylic acid ester).
  • the polyethylene can be homogeneous or heterogeneous.
  • the homogeneous polyethylenes usually have a polydispersity (Mw/Mn) in the range of about 1.5 to about 3.5 and an essentially uniform comonomer distribution, and are characterized by a single and relatively low melting point as measured by a differential scanning calorimeter.
  • the heterogeneous polyethylenes usually have a polydispersity (Mw/Mn) greater than 3.5 and lack a uniform comonomer distribution.
  • Mw is defined as weight average molecular weight
  • Mn is defined as number average molecular weight.
  • the polyethylenes can have a density in the range of 0.860 to 0.970 gram per cubic centimeter, and preferably have a density in the range of 0.870 to about 0.930 gram per cubic centimeter. They also can have a melt index in the range of about 0.1 to about 50 grams per 10 minutes. If the polyethylene is a homopolymer, its melt index is preferably in the range of about 0.75 to about 3 grams per 10 minutes. Melt index is determined under ASTM D- 1238, Condition E and measured at 190 degrees Celsius and 2160 grams.
  • Low- or high-pressure processes can produce the polyethylenes. They can be produced in gas phase processes or in liquid phase processes (i.e., solution or slurry processes) by conventional techniques. Low-pressure processes are typically run at pressures below 1000 pounds per square inch (“psi”) whereas high-pressure processes are typically run at pressures above 15,000 psi.
  • psi pounds per square inch
  • Typical catalyst systems for preparing these polyethylenes include magnesium/titanium-based catalyst systems, vanadium-based catalyst systems, chromium-based catalyst systems, metallocene catalyst systems, and other transition metal catalyst systems. Many of these catalyst systems are often referred to as Ziegler-Natta catalyst systems or Phillips catalyst systems.
  • Useful catalyst systems include catalysts using chromium or molybdenum oxides on silica-alumina supports.
  • Useful polyethylenes include low density homopolymers of ethylene made by high pressure processes (HP-LDPEs), linear low density polyethylenes (LLDPEs), very low density polyethylenes (VLDPEs), ultra low density polyethylenes (ULDPEs), medium density polyethylenes (MDPEs), high density polyethylene (HDPE), and metallocene copolymers.
  • High-pressure processes are typically free radical initiated polymerizations and conducted in a tubular reactor or a stirred autoclave. In the tubular reactor, the pressure is within the range of about 25,000 to about 45,000 psi and the temperature is in the range of about 200 degrees Celsius to about 350 degrees Celsius. In the stirred autoclave, the pressure is in the range of about 10,000 to 30,000 psi and the temperature is in the range of about 175 degrees Celsius to about 250 degrees Celsius.
  • Copolymers comprised of ethylene and unsaturated esters are well known and can be prepared by conventional high-pressure techniques.
  • the unsaturated esters can be alkyl acrylates, alkyl methacrylates, or vinyl carboxylates.
  • the alkyl groups can have 1 to 8 carbon atoms and preferably have 1 to 4 carbon atoms.
  • the carboxylate groups can have 2 to 8 carbon atoms and preferably have 2 to 5 carbon atoms.
  • the portion of the copolymer attributed to the ester comonomer can be in the range of about 5 to about 50 percent by weight based on the weight of the copolymer, and is preferably in the range of about 15 to about 40 percent by weight.
  • acrylates and methacrylates are ethyl acrylate, methyl acrylate, methyl methacrylate, t-butyl acrylate, n-butyl acrylate, n-butyl methacrylate, and 2-ethylhexyl acrylate.
  • vinyl carboxylates are vinyl acetate, vinyl propionate, and vinyl butanoate.
  • the melt index of the ethylene/unsaturated ester copolymers can be in the range of about 0.5 to about 50 grams per 10 minutes, and is preferably in the range of about 2 to about 25 grams per 10 minutes.
  • Copolymers of ethylene and vinyl silanes may also be used.
  • suitable silanes are vinyltrimethoxysilane and vinyltriethoxysilane.
  • Such polymers are typically made using a high-pressure process.
  • Use of such ethylene vinylsilane copolymers is desirable when a moisture crosslmkable composition is desired.
  • the VLDPE or ULDPE can be a copolymer of ethylene and one or more alpha-olefins having 3 to 12 carbon atoms and preferably 3 to 8 carbon atoms.
  • the density of the VLDPE or ULDPE can be in the range of 0.870 to 0.915 gram per cubic centimeter.
  • the melt index of the VLDPE or ULDPE can be in the range of about 0.1 to about 20 grams per 10 minutes and is preferably in the range of about 0.3 to about 5 grams per 10 minutes.
  • the portion of the VLDPE or ULDPE attributed to the comonomer(s), other than ethylene, can be in the range of about 1 to about 49 percent by weight based on the weight of the copolymer and is preferably in the range of about 15 to about 40 percent by weight.
  • a third comonomer can be included, e.g., another alpha-olefin or a diene such as ethylidene norbornene, butadiene, 1,4-hexadiene, or a dicyclopentadiene.
  • Ethylene/propylene copolymers are generally referred to as EPRs and ethylene/propylene/diene terpolymers are generally referred to as an EPDM.
  • the third comonomer can be present in an amount of about 1 to 15 percent by weight based on the weight of the copolymer and is preferably present in an amount of about 1 to about 10 percent by weight. It is preferred that the copolymer contains two or three comonomers inclusive of ethylene.
  • the LLDPE can include VLDPE, ULDPE, and MDPE, which are also linear, but, generally, has a density in the range of 0.916 to 0.925 gram per cubic centimeter. It can be a copolymer of ethylene and one or more alpha-olefins having 3 to 12 carbon atoms, and preferably 3 to 8 carbon atoms.
  • the melt index can be in the range of about 1 to about 20 grams per 10 minutes, and is preferably in the range of about 3 to about 8 grams per 10 minutes. Any polypropylene may be used in these compositions.
  • polypropylenes examples include homopolymers of propylene, copolymers of propylene and other olefins, and terpolymers of propylene, ethylene, and dienes (e.g. norbornadiene and decadiene). Additionally, the polypropylenes may be dispersed or blended with other polymers such as EPR or EPDM. Suitable polypropylenes include TPEs, TPOs and TPVs. Examples of polypropylenes are described in POLYPROPYLENE HANDBOOK: POLYMERIZATION, CHARACTERIZATION, PROPERTIES, PROCESSING, APPLICATIONS 3- 14, 113-176 (E. Moore, Jr. ed., 1996).
  • Vinyl alkoxysilanes e.g., vinyltrimethoxysilane and vinyltriethoxysilane are suitable silane compound for grafting or copolymerization to form the silane- functionalized olefinic polymer.
  • Suitable acidic silanol condensation catalysts include (a) organic sulfonic acids and hydrolyzable precursors thereof, (b) organic phosphonic acids and hydrolyzable precursors thereof, and (c) halogen acids.
  • the acidic silanol condensation catalyst is an organic sulfonic acid. More preferably, the acidic silanol condensation catalyst is selected from the group consisting of alkylaryl sulfonic acids, arylalkyl sulfonic acids, and alkylated aryl disulfonic acids. Even more preferably, the acidic silanol condensation catalyst is selected from the group consisting of substituted benzene sulfonic acids and substituted naphthalene sulfonic acid. Most preferably, the acidic silanol condensation catalyst is dodecylbenzyl sulfonic acid or dinonylnapthyl sulfonic acid.
  • Suitable secondary amine antioxidant substituted with two aromatic groups include 4,4'-bis (alpha, alpha - dimethylbenzyl) diphenylamine, phenyl-a- naphthylamine, other diaryl amines, and diaryl sulfonamides.
  • the substituted aromatic groups will be benzyl groups or naphthyl groups.
  • the acid silanol condensation catalyst achieves about the same catalytic performance as achievable in the absence of the secondary amine antioxidant.
  • the silane-functionalized olefinic polymer is curable at about the same rate as achievable in the absence of the secondary amine antioxidant.
  • the composition may contain other additives such as colorants, corrosion inhibitors, lubricants, anti-blocking agents, flame retardants, processing aids, and a second antioxidant, being a secondary amine substituted with at least one aromatic group.
  • a second antioxidant is present, it is present in an amount less than or equal to about 25 weight percent of the total amount of antioxidants. More preferably, it is present in an amount between about 1 weight percent and less than about 25 weight percent of the total amount of antioxidants. Even more preferably, it is present in amount between about 2.5 weight percent and 10 weight percent of the total amount of antioxidants.
  • the present invention is a moisture-crosslinkable polymeric composition
  • a moisture-crosslinkable polymeric composition comprising (a) a silane-functionalized olefinic polymer, (b) an acidic silanol condensation catalyst, (c) a first antioxidant, and (d) a second antioxidant, being a secondary amine substituted with at least one aromatic group.
  • the previously-described silane- functionalized olefinic polymer and acidic silanol condensation catalyst are suitable for the present embodiment.
  • the composition may contain other additives such as colorants, corrosion inhibitors, lubricants, anti-blocking agents, flame retardants, and processing aids.
  • Suitable first antioxidants include (a) phenolic antioxidants, (b) thio-based antioxidants, (c) phosphate-based antioxidants, and (d) hydrazine-based metal deactivators.
  • Suitable phenolic antioxidants include methyl-substituted phenols. Other phenols, having substituents with primary or secondary carbonyls, are suitable antioxidants.
  • a preferred phenolic antioxidant is isobutylidenebis(4,6- dimethylphenol).
  • a preferred hydrazine-based metal deactivator is oxalyl bis(benzylidiene hydrazide).
  • the antioxidant is present in amount between about 0.05 weight percent to about 10 weight percent of the polymeric composition.
  • Suitable second antioxidants with at least one aromatic groups include 4,4'-bis
  • the second antioxidant is present in an amount less than or equal to about
  • 25 weight percent of the total amount of antioxidants More preferably, it is present in an amount between about 1 weight percent and less than about 25 weight percent of the total amount of antioxidants. Even more preferably, it is present in amount between about 2.5 weight percent and 10 weight percent of the total amount of antioxidants.
  • the acid silanol condensation catalyst achieves about the same catalytic performance as achievable in the absence of the second antioxidant.
  • the silane-functionalized olefinic polymer is curable at about the same rate as achievable in the absence of the second antioxidant.
  • the invention is wire or cable construction prepared by applying the previously-described polymeric composition over a wire or cable.
  • test Methods The following test methods were used to evaluate the non-limiting examples:
  • Hot set is a measurement of elongation according to IEC-60502-1. A test specimen fails the hot set test if the elongation is greater than 175 percent.
  • the tensile properties of strength and elongation are measured according to
  • coated wire specimens were used to evaluate the cure rate and heat aging performance of the compositions.
  • DFH-2065 is a linear low density polyethylene, having a melt index of 0.65 grams/10 minutes and a density of 0.920 grams/cubic centimeter, and being available from The Dow Chemical Company.
  • DPDA-6182 is an ethylene/ ethyl acrylate copolymer, having a melt index of 1.5 grams/10 minutes and a density of 0.930 grams/cubic centimeter, and being available from The Dow Chemical Company.
  • Agerite MA polymerized l,2-dihydro-2,2,4-trimethylquinoline is commercially available from R. T. Vanderbilt Company.
  • Irganox 1010TM tetrakismethylene (3,5-di-t-butyl-4-hydroxylhydrocinnamate) methane is a hindered phenolic antioxidant, available from Ciba Specialty
  • Irganox 1024TMl 2-bis(3,5-di-t-butyl-4-hydroxyhydrocinnamoyl)hydrazine is available from Ciba Specialty Chemicals Inc.
  • NACURE B201 alkyl aromatic sulfonic acid is available from King Industries, Inc.
  • Naugard 445 4,4'-bis (alpha, alpha - dimethylbenzyl) diphenylamine is available from Crompton Corporation.
  • OABH oxalyl bis (benzylidiene hydrazide), a metal deactivator available from Eastman Chemical Company.
  • Super QTM polymerized l,2-dihydro-2,2,4-trimethylquinoline is available from
  • TBM6 is 4,4-thiobis(2-t-butyl-5-methyl ⁇ henol) available from Great Lakes Chemical Corporation.
  • Comparatives 1 — 3 and 6 and Examples 4 and 5 were maintained at a temperature of 23 degrees Celsius and a relative humidity of 70 percent for two days. Comparative Examples 1 - 3 failed to cure within two days. As such, those comparative examples were not evaluated for hot set. Examples 4 and 5 and Comparative Example 6 were evaluated for hot set after one and two days.
  • Comparative Examples 10, 11, and 13 and Examples 12 and 14 were maintained at a temperature of 23 degrees Celsius and a relative humidity of 70 percent for three days. The hot set measurements were taken after one, two, and three days.
  • Comparative Examples 10, 11, and 13 and Examples 12 and 14 were evaluated for heat aging performance. The performance was measured after 5 days, 7 days, and 10 days of subjecting the test specimens to 135 degrees Celsius.
  • Examples and Comparative Examples were prepared with the described antioxidants, 4 weight percent of NACURETM B201 alkyl aromatic sulfonic acid, and the balance of the composition being DFH-2065 and DPDA-6182 in a 1:1 ratio.

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  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
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PCT/US2006/008368 2005-03-18 2006-03-09 Moisture crosslinkable polymeric composition-improved heat aging performance Ceased WO2006101754A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
US11/817,245 US20080176981A1 (en) 2005-03-18 2006-03-09 Moisture Crosslinkable Polymeric Composition-Improved Heat Aging Performance
MX2007011437A MX2007011437A (es) 2005-03-18 2006-03-09 Composicion polimerica reticulable por humedad - desempeno de envejecimiento por calor mejorado.
EP06737532.9A EP1863873B1 (en) 2005-03-18 2006-03-09 Moisture crosslinkable polymeric composition having improved heat aging performance
CA2599793A CA2599793C (en) 2005-03-18 2006-03-09 Moisture crosslinkable polymeric composition-improved heat aging performance
JP2008501917A JP5415754B2 (ja) 2005-03-18 2006-03-09 水分架橋性ポリマー組成物−改良された耐熱老化性能

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US66313305P 2005-03-18 2005-03-18
US60/663,133 2005-03-18

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EP (1) EP1863873B1 (enExample)
JP (1) JP5415754B2 (enExample)
CN (1) CN101142270A (enExample)
CA (1) CA2599793C (enExample)
MX (1) MX2007011437A (enExample)
TW (1) TW200641053A (enExample)
WO (1) WO2006101754A1 (enExample)

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EP2562768A1 (en) 2011-08-26 2013-02-27 Borealis AG Cable comprising a silane crosslinkable polymer composition
JP2015071776A (ja) * 2007-06-27 2015-04-16 ダウ グローバル テクノロジーズ エルエルシー 柔軟性が増大したケーブルの絶縁のためのポリオレフィンエラストマー及びシランコポリマーの架橋可能なブレンド配合物
WO2017100049A1 (en) * 2015-12-09 2017-06-15 Dow Global Technologies Llc Stabilized moisture-curable polymeric compositions
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PL2251365T3 (pl) * 2009-05-14 2019-09-30 Borealis Ag Sieciowalna kompozycja poliolefinowa zawierająca grupy silanowe tworzące kwas lub zasadę w wyniku hydrolizy
WO2010130457A1 (en) * 2009-05-14 2010-11-18 Borealis Ag Cross-linkable polyolefin composition comprising two types of silane groups
WO2015091707A1 (en) * 2013-12-18 2015-06-25 Borealis Ag A polymer composition comprising a polyolefin composition and a at least one silanol condensation catalyst
US10233310B2 (en) * 2013-12-18 2019-03-19 Borealis Ag Polymer composition comprising a crosslinkable polyolefin with hydrolysable silane groups, catalyst and a surfactant interacting additive
BR112016029739B1 (pt) 2014-06-27 2021-08-10 Dow Global Technologies Llc Composição polimérica reticulável por silano, condutor revestido e processo para preparar uma composição polimérica reticulável por silano
KR102396101B1 (ko) * 2014-06-27 2022-05-11 다우 글로벌 테크놀로지스 엘엘씨 안정화된 수분-경화성 폴리머성 조성물
US10723108B2 (en) 2014-10-30 2020-07-28 Dow Global Technologies Llc Multilayer film and related materials and methods
EP3240686B1 (en) 2014-12-31 2022-08-03 Dow Global Technologies LLC Multilayer films and related uses thereof
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US20080176981A1 (en) 2008-07-24
CA2599793C (en) 2013-08-13
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