WO2009056407A1 - Compositions polyoléfiniques fonctionnalisées avec des silanes, produits associés et procédés de préparation associés pour fils & câbles - Google Patents

Compositions polyoléfiniques fonctionnalisées avec des silanes, produits associés et procédés de préparation associés pour fils & câbles Download PDF

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WO2009056407A1
WO2009056407A1 PCT/EP2008/062735 EP2008062735W WO2009056407A1 WO 2009056407 A1 WO2009056407 A1 WO 2009056407A1 EP 2008062735 W EP2008062735 W EP 2008062735W WO 2009056407 A1 WO2009056407 A1 WO 2009056407A1
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silane
composition
polymer
polyolefin composition
component
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PCT/EP2008/062735
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English (en)
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Ola Fagrell
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Borealis Technology Oy
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Publication of WO2009056407A1 publication Critical patent/WO2009056407A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F255/00—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
    • C08F255/02—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F255/00—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00—Chemical modification by after-treatment
    • C08F8/42—Introducing metal atoms or metal-containing groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L101/00—Compositions of unspecified macromolecular compounds
    • C08L101/02—Compositions of unspecified macromolecular compounds characterised by the presence of specified groups, e.g. terminal or pendant functional groups
    • C08L101/10—Compositions of unspecified macromolecular compounds characterised by the presence of specified groups, e.g. terminal or pendant functional groups containing hydrolysable silane groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00—Compositions 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
    • C08L51/06—Compositions 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
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
    • H01B1/20—Conductive material dispersed in non-conductive organic material
    • H01B1/24—Conductive material dispersed in non-conductive organic material the conductive material comprising carbon-silicon compounds, carbon or silicon
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B3/00—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
    • H01B3/002—Inhomogeneous material in general
    • H01B3/004—Inhomogeneous material in general with conductive additives or conductive layers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions 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
    • C08L23/10—Homopolymers or copolymers of propene

Definitions

  • Silane-functionalised polyolef ⁇ n compositions, products thereof and preparation processes thereof for wire and cable applications Silane-functionalised polyolef ⁇ n compositions, products thereof and preparation processes thereof for wire and cable applications
  • the invention relates to silane-functionalised polyolef ⁇ n compositions, to silane- crosslinkable polyolef ⁇ n compositions and to silane-crosslinked polyolefin compositions, to a preparation process thereof, to their use for producing products and to the obtained products, to their use for W&C applications, preferably for producing one or more layers of a cable comprising said silane-functionalised polyolefin composition, as well as to silane-crosslinked cables comprising polyolefin compositions.
  • Crosslinking of polymers is one well known modification method in many end applications of polymers.
  • Crosslinking of polymers such as polyolef ⁇ ns, substantially contributes i.a. to heat and deformation resistance, creep properties, mechanical strength, as well as to chemical and abrasion resistance of a polymer.
  • crosslinked polymers such as crosslinked polyethylenes, are commonly used as a layer material, e.g. in insulating, semi-conducting and/or jacketing layers.
  • a typical cable comprises at least one conductor surrounded by one or more layers of polymeric materials.
  • said conductor is surrounded by several layers including an inner semiconductive layer, an insulation layer and an outer semiconductive layer, in that order.
  • the cables are commonly produced by extruding the layers on a conductor. One or more of said layers are then typically crosslinked to achieve the desired properties to the end product cable.
  • Crosslinking can be effected i.a. by radical reaction using radiation or free radical generating agents, also called crosslinking agents.
  • free radical generating agents are peroxides including inorganic and organic peroxides.
  • Crosslinking using peroxide is known as peroxide technology.
  • a further well known crosslinking method is crosslinking functional groups, e.g. by hydrolysing hydrolysable silane groups, which are linked to a polymer, and subsequently condensing the formed silanol groups using a silanol condensation catalyst, for instance carboxylates of metals, such as tin, zinc, iron, lead and cobalt; organic bases; inorganic acids; and organic acids.
  • a silanol condensation catalyst for instance carboxylates of metals, such as tin, zinc, iron, lead and cobalt
  • organic bases such as tin, zinc, iron, lead and cobalt
  • organic bases such as tin, zinc, iron, lead and cobalt
  • organic bases such as tin, zinc, iron, lead and cobalt
  • organic bases such as tin, zinc, iron, lead and cobalt
  • organic bases such as tin, zinc, iron, lead and cobalt
  • organic bases such as tin, zinc, iron, lead and cobalt
  • Silane groups can be introduced into the polymer structure 1) by copolymerisation of monomers, such as olefin monomers, with silane-moiety bearing comonomers, or 2) by grafting crosslinkable silane -moieties bearing compounds, such as unsaturated silane compounds with hydrolysable silane group(s), onto a polymer. Both methods are well known in the art. Grafting is usually performed by radical reaction using free radical generating agents.
  • Free radical generation using free radical generating agents is thus conventionally used e.g. (a) for crosslinking a polymer, i.a. for forming primarily interpolymer crosslinks (bridges) by radical reaction, (b) for grafting a polymer, i.e. for introducing compounds, such as said silane compounds, to a polymer chain (to backbone and/or side chains) by radical reaction, and also (c) for visbreaking a polymer, e.g. for modifying the rheological properties, such as melt flow rate (MFR), by radical reaction.
  • MFR melt flow rate
  • the crosslinking side -reaction brings therefore limitation to the amount of silane groups to be grafted, since the more silane groups is added the more free radical generating agent is needed, whereby also more crosslinking side -reactions take place resulting in increased viscosity (decreased MFR) of the polymer. Accordingly, in order to enable the sufficient processability the amount of crosslinkable silane groups and thus the resulting degree of crosslinking of the silane-grafted polyethylene must usually be kept relatively low.
  • Said crosslinking degree can be expressed i.a. as gel content of the crosslinked polymer material.
  • said degree of crosslinking of silane-grafted and silane-crosslinked polymers has conventionally been kept at a level which, when defined being the gel content of a crosslinked polymer, corresponds to a gel content of 25-30 wt%, when measured according to ASTM D2765- 95 using a crosslinked polymer sample.
  • the storage period, i.e. self life, of the grafted PE material is typically limited to 3-4 months due to undesired gel formation
  • semiconductive layer materials have typically a high filler content, whereby said filler, usually carbon black, also increases the viscosity of the polymer material.
  • crosslinkable silane-grafted polymers of prior art has been limited, if used at all, in applications, such as in crosslinkable semiconductive layer materials. Accordingly, there is a continuous need for alternative polymer compositions suitable for different application areas of polymers and suitable for meeting the increasing demands of the end users.
  • One of the objects of the present invention is to provide an alternative silane- functionalised polyolefin composition, which exhibits i.a. an excellent storage stability.
  • the present polyolefin composition preferably may also provide a superior balance between mechanical and processing properties, when desired.
  • a further object of the present invention is to provide a process for preparing said polyolefin composition of the invention.
  • the invention also provides a silane-crosslinkable polyolefin composition which has an excellent storage stability, and, if desired, enables to obtain silane-crosslinkable polymers that provide i.a. high degree of crosslinking, however, without sacrificing processability. Moreover, a process for silane-crosslinking said polyolefin composition is provided, as well as a silane-crosslinked polyolefin composition which has excellent mechanical, i.a. hot set elongation, properties.
  • the use of polyolefin composition of the invention for wire and cable, W&C, applications, preferably use as a cable layer material, is also provided.
  • the invention also provides silane-crosslinkable and silane-crosslinked products, preferably silane-crosslinkable and silane-crosslinked cables, comprising said silane- crosslinkable and, respectively, silane-crosslinked, preferably silane-grafted, polyolefin composition, which products are feasibly producible and have good mechanical properties.
  • Said crosslinked product may further provide an excellent peeling property, also known as low strip force, when desired.
  • polyolefin composition of the invention provides a polyolefin composition which comprises:
  • polymer component (i) which is a polymer (A) bearing silane -moieties, and is referred herein also as “polymer component (i)"
  • polyolefin component (ii) which is a polymer of olefin having at least 3 carbon atoms, and is referred herein also as “polyolefin component (ii)"
  • polyolefin component (ii) and, optionally,
  • the base polymer (A) of said component (i) is an ethylene homopolymer or copolymer (Al), which bears said silane-moieties,.
  • silane-moieties or "silane-functionalised” etc. as used herein interchangeably all mean that silane-moieties have been introduced into a polymer structure i.a. by means of grafting or copolymerising, preferably by grafting, using a compound or, respectively, a comonomer, which bears a functional silane-moiety as part of said compound or said comonomer, as described later below.
  • Said functional silane- moiety can be subjected to said desired functional chemical reaction for providing a desired effect to said polymer, preferably crosslinkability.
  • Said silane, (Y)3_ q Si, -moiety is referred herein also as "(functional) silane-group”.
  • Such “functional silane-group” is preferably a hydrolysable silane-group which is crosslinkable by hydrolysation and subsequent condensation reaction in the presence of a silanol condensation catalyst and water, as known in the art, to form Si-O-Si links between other hydrolysable silane-groups present in said (i) polymer component of the polyolefin composition of the invention.
  • silane compound Said functional silane-moiety bearing compound or comonomer used for introducing said silane-groups to polymer of said polymer component (i) is referred herein as silane compound and, respectively, silane comonomer.
  • silane compound Said functional silane-moiety bearing compound or comonomer used for introducing said silane-groups to polymer of said polymer component (i) is referred herein as silane compound and, respectively, silane comonomer.
  • crosslinkable or silane-crosslinkable polyolefln composition etc. used interchangeably are well known and mean also herein that the polyolefin composition of the invention can be crosslinked to form bridges i.a.
  • the polyolefin composition of the invention is crosslinkable at least via said functional silane-groups present at least in said silane- functionalised compounds of said polymer component (i) by a silane-crosslinking reaction as explained above and further below.
  • silane-crosslinkable crosslinkable polyolefin composition of the invention and/or crosslinkable component (i) thereof is shortly referred herein as "silane-crosslinkable”.
  • Crosslinked polyolefin composition or “silane-crosslinked polyolefin composition”, as used interchangeably above and below, mean herein that said polyolefin composition of the invention contains said bridges at least between said silane-groups which bridges are formed during above-said silane-crosslinking reaction explained above.
  • Silane-crosslinking conditions mean herein conditions that enable the crosslinking reaction to occur, which is most preferably the above mentioned hydrolysis and subsequent condensation reaction. All these expressions are well known in the art.
  • Base “polymer (A)” is the base polymer (backbone), wherein the silane-moieties are incorporated in the “final” polymer (A) component (i) and wherein said silane-moieties are introduced during the preparation of said polymer (A) component (i).
  • "Free radical generating agent” is shortly referred herein also as “initiator”.
  • Said polyolefin composition may comprise independently one or more of each of said polymer component (i), polyolefin component (ii) and optional filler (iii) component. It is also evident that said polyolefin composition may comprise further polymer components or further components, such as additives.
  • Said polyolefin composition of the invention is also referred herein shortly as polyolefin composition.
  • said polyolefin composition has preferably an excellent storage stability, even when said silane moieties of polymer component (i) have been introduced by silane- grafting as later further described.
  • the undesired MFR decrease during the preparation process of said polyolefin composition of the invention and/or during the storage thereof, can be markedly reduced or even avoided with said polyolefin composition.
  • the storage life of said polyolefin composition may be prolonged considerably.
  • the present combination of components (i) and (ii) is believed to contribute to said improved stability.
  • said polyolefin composition has a melt flow ratio, MFR21, of at least 0.01 g/10 min and further (i) the MFR of said polyolefin composition, when measured according to ISO 1133 at 19O 0 C using a load of 2.16 kg or of 21.6 kg, is changed of less than ⁇ 60%, preferably of less than ⁇ 30 %, more preferably of less than ⁇ 27 %, in some embodiments even of less than ⁇ 15%, from the initial MFR thereof, after a storage period of 3 months, preferably of 6 months, when stored in a sealed container in a room which has an atmospheric pressure, temperature of 23 0 C and relative humidity of 55%.
  • MFR21 melt flow ratio
  • the sealed container was a plastic bag made of film structure which had a WVTR less than 0.5 g H2 ⁇ /m 2 /24h, when measured in an atmosphere having a temperature of 38 0 C and a relative humidity of 90% (standard pressure).
  • said bag was made from Al-laminated polyethylene film.
  • said filler (iii) is present, as preferred, the typically MFR21 with a load of 21.6 kg is measured.
  • said MFR of said polyolefin composition is changed of less than ⁇ 30 %, more preferably of less than ⁇ 27 %, in some embodiments even of less than ⁇ 15%, from the initial MFR thereof, after a storage period of 9 months, when stored as defined above.
  • said polyolefin composition comprises a filler (iii) and said
  • the MFR of said polyolefin composition can be measured from a sample which can be any of pellets, granules, powder or similar consisting of said polyolefin composition of the invention.
  • the sample is taken from an outlet of a production line, e.g. a mixer or pelletising extruder of the preparation process of said polyolefin composition, which outlet is evident for as skilled person.
  • a production line e.g. a mixer or pelletising extruder of the preparation process of said polyolefin composition, which outlet is evident for as skilled person.
  • the obtained sample is put to an above given storage conditions within 5 hours after said sampling and said initial MFR is determined from such stored sample within 24 to 48 hours after said sampling from said outlet.
  • silane crosslinkable embodiments of said polyolefin composition as discussed later below, an unexpectedly high degree of crosslinking can be achieved to said polyolefin composition, and at the same time an excellent processability.
  • the combination of said polyolefin component (ii) and said polymer component (i) is believed to contribute to said unexpected property.
  • the degree of crosslinking is expressed herein as a gel content of a crosslinked polyolefin composition, when measured according to ASTM D2765-95 using a sample consisting of said crosslinked polyolefin composition.
  • the present combination of the invention enables to increase the crosslinking level of a silane -moieties bearing polymer composition without sacrificing processability thereof, even when said silane-moieties of said polymer component (i) are introduced by grafting using an initiator. Moreover, said increased degree of crosslinking and, at the same time, also advantageous processability, can be achieved even with high filler (iii) content.
  • Said polyolefin composition of the invention enables to broaden the industrially usable range of the silane-functionalised polymer applications and is highly suitable i.a. for wire and cable (W&C) applications, and particularly in providing semiconductive layers that comprise carbon black as said filler (iii).
  • such high degree of crosslinking can be provided after silane-crosslinking said polyolefin composition that i.a. a hot set elongation thereof can surprisingly be measured.
  • Said polyolefin composition of the invention provides also feasible deformation resistance in silane-crosslinking applications.
  • the combination of said polymer component (i) and said polyolefin component (ii), as defined above and below, provides also an excellent peeling property, i.e. low strip force, which enables to make e.g. strippable semiconductive layers i.a. for medium voltage cable applications.
  • the excellent strippability property of said polyolefin composition of the invention enables to minimize or even avoid the use of additional polar polymer components, e.g. so called NBR which is copolymer of acrylonitrile and butadiene, also known as nitrile butyl rubber or nitrile rubber, and which is often needed in strippable semiconductive layer materials for decreasing the adhesion of said layer onto adjacent layer(s), such as an insulation layer.
  • NBR is copolymer of acrylonitrile and butadiene, also known as nitrile butyl rubber or nitrile rubber
  • the preferred polyolefin composition of the invention for use as a semiconductive layer material comprises no added NBR component.
  • said polyolefin composition has a strip force of less than 9.0 kN/m, preferably of from 0.5 to 9.0 kN/m, more preferably of from 0.8 to 7.0 kN/m, more preferably of from 1.0 to 5.0 kN/m, when measured at 90° peeling angle from an outer layer of a test three-layer cable, wherein said outer layer has a thickness of 1.0 mm and consists of said polyolefin composition.
  • the strip force method and the test cable sample used in said determination were as described below under "Determination methods".
  • said polyolefin composition can be uncrosslinked or crosslinked. Most preferably said polyolefin composition is crosslinkable and meets the above strip force property in a crosslinked form, when measured as defined above from a test cable consisting of said crosslinked polyolefin composition.
  • Said silane-moieties of base polymer (A) of component (i) of polyolefin composition are preferably silane-crosslinkable.
  • Said polyolefin composition as defined above or below comprises preferably - 20 to 98 wt% of said polymer component (i) bearing silane-moieties, - 2 to 50 wt% of said polyolefin component (ii) of olefins with 3 or higher carbon atoms, and - 0 to 50 wt% of said optional filler (iii), based on the total amount of said polyolefin composition.
  • total amount or “amount” of said polyolefin composition as used herein above and below is 100 wt%.
  • the amount of said polymer component (i) bearing silane-moieties is typically between 40 to 98 wt%, preferably between 50 to 97 wt%, such as between 55 to 95 wt%, more preferably 80 to 95 wt%, of the amount of said polyolefin composition of the invention. If said filler (iii) is not present, then the amount of said polyolefin component (ii) is typically between 2 to 60 wt%, preferably between 3 to 50 wt%, such as between 5 to 45 wt%, more preferably between 5 to 20 wt%, of the amount of said polyolefin composition.
  • said filler (iii) is present, whereby the amount of said polymer component (i) is typically between 20 to 90 wt%, preferably 30 to 80 wt%, more preferably 40 to 70 wt%, or it may be even 45 to 60 wt%, of the amount of said polyolefin composition.
  • the amount of said polyolefin component (ii) is typically 2 to 45 wt%, preferably between 2 to 40 wt%, more preferably between 3 to 30 wt%, more preferably between 5 to 20 wt%, of the amount of said polyolefin composition.
  • the amount of said filler (iii) is not limited and can vary within a wide range depending on the filler, as well as the effect desired to said polyolefin composition or to an end product thereof, as well known in the art.
  • the amount of said filler (iii) is between 5 to 50 wt%, typically between 10 to 45 wt%, such as between 15 to 45 wt%, or in some embodiments it may be preferable to have even 20 to 45 wt%, preferably 25 to 45 wt%, more preferably 30 to 45 wt%, of the amount of said polyolefin composition.
  • Said polyolefin composition contains of from 0.001 to 12 mol%, preferably of from 0.01 to 4 mol%, most preferably of from 0.1 to 1.6 mol%, of said functional silane-moieties, i.e. Si(Y)3_q, based on the amount of the two polymer components, i.e. polymer component (i) and polyolefin component (ii), present in said polyolefin composition.
  • said polyolefln composition contains preferably of from 0.2 to 1.6 mol%, and even as high as of from 0.3 to 1.6 mol%, of said functional silane-moieties, i.e.
  • the amount of functional silane-groups as defined above and present in said polyolefin composition of the invention is not limited and depends on the effect of said functional silane-groups desired to said polyolefin composition and/or to an end product thereof. More preferably said functional silane-groups are those introduced to said polyolefin composition during the preparation of said polymer component (i), optionally in the presence of other components of said polyolefin composition of the invention, preferably in the presence of said polyolefin component (ii) as described later below.
  • the melt flow ratio, MFR, of said polyolefin composition of the invention is also not limited and can vary within a broad range depending on the end application.
  • said polyolefin composition comprises said filler (iii) and the lower limit OfMFR 2I of said polyolefin composition is of at least 0.01 g/10 min, such as of at least 0.1 g/10 min, suitably of at least 0.5 g/10 min, preferably of at least 1.0 g/10 min, more preferably of at least 1.5 g/10 min, and the upper limit can be selected depending on the desired application and may be e.g. of up to 200 g/10 min, e.g.
  • up to 100 g/10 min more preferably is within the ranges of from 2.0 to 50 g/10 min, more preferably of from 2.0 to 20 g/10 min, and more preferably of 2.5 to 17 g/10 min, when measured according to ISO 1133 at 19O 0 C using 21.6 kg load.
  • the density of said polyolefin composition of the invention is not limited and can vary depending on the end application.
  • Said polyolefin composition for W&C applications may preferably have a density of less than 970 kg/m 3 , preferably between 870 to 90 kg/m 3 , when said filler (iii) is not present.
  • said filler (iii) is present, whereby said polyolefin composition has a density of at least 950 kg/m , and more preferably up to 1150 kg/m 3 .
  • Polymer component (i) Said (i) polymer (A) component bearing silane-moieties of the polyolefin composition of the invention a silane-functionalised ethylene polymer (Al) as defined above and in claims below.
  • the amount of functional silane-groups in said polymer component (i) is not limited and depends on the desired effect provided by said functional silane-groups.
  • said functional silane-groups that are present in the final polyolefin composition are introduced during the preparation process of said polymer component (i) to provide the above defined amount of functional silane-groups to said polyolefin composition of the invention.
  • Said polymer component (i) may be obtainable by any suitable means.
  • said polymer component (i) of said polyolefin composition of the invention is obtainable by silane-grafting or silane-copolymerisation, most preferably by silane- grafting, as described further below including said further preferred subgroups thereof.
  • Said ethylene homopolymer or ethylene copolymer (Al) as said base polymer (A) of said polymer component (i), which bears said silane-moieties is preferably, a branched low density polyethylene homo- or copolymer produced in high pressure by radical polymerisation and referred herein as LDPE homo- or copolymer (Ai i), more preferably an LDPE copolymer (Ai i b), even more preferably an LDPE copolymer of ethylene with at least polar comonomer(s) (A2), which bears silane-moieties and which is further described later below by means of preferred subgroups thereof.
  • LDPE homo- or copolymer a branched low density polyethylene homo- or copolymer produced in high pressure by radical polymerisation and referred herein as LDPE homo- or copolymer (Ai i), more preferably an LDPE copolymer (Ai i b), even more preferably
  • silane-functionalised polymer (A) component (i) which bears said silane-moieties, are referred herein also as silane- functionalised polymer (A) component (i), and said preferable subgroups thereof, in increasing preference order, as silane-functionalised polymer (Al), (Ai i), (Ai i b), and most preferably (A2) component (i).
  • said polymer (A) or a preferable subgroup thereof, as mentioned above, is actually a copolymer obtainable by copolymerising said monomer units of said base polymer, preferably olefin units, more preferably ethylene units, with silane comonomer units, and in case of preferred base copolymers (Al), (Ai i) and (A2)/(A3) with other comonomer units of said base polymer.
  • said copolymers are referred herein according to base polymer as silane-functionalised copolymer (A), (Al), (Ai i) and, respectively, (A2) component (i).
  • polar comonomer is other than “silane comonomer”.
  • Said polar groups of said polar comonomer are preferably selected from siloxane, amide, anhydride, carboxylic, carbonyl, hydroxyl, ester and epoxy groups.
  • the content of said polar comonomer(s) is not limited and may be e.g. up to 70 wt%, preferably 0.5 to 35 wt%, more preferably 1.0 to 30 wt%, of the amount of said base polymer (A) of said polymer component (i).
  • said (i) copolymer component comprises polar comonomer units in an amount: (a) of at least 7.0 mol%, preferably of at least 7.5 mol% , more preferably of from 8 to 15 mol%, based on the total moles of polymerisable monomers of said base LDPE copolymer (A2), or,
  • LDPE copolymer (b) in an amount of at least 20 wt%, such as at least 25 wt%, preferably at least 26 wt% more preferably from 27 to 35 wt%, based on said base LDPE copolymer (A), and is referred herein as silane-functionalised LDPE copolymer of ethylene with at least polar comonomer(s) (A3). Both mol% and wt% can be used for defining the preferable embodiment of high comonomer content.
  • polyolefln composition comprising said silane-functionalised LDPE copolymer of ethylene and at least polar comonomer(s) (A2) component (i), more preferably said silane-functionalised LDPE copolymer of ethylene and at least polar comonomer(s) (A3) component (i) is preferable in cable, such as in semiconductive cable, applications and particularly in case of such high polar comonomer contents, in strippable semiconductive layers, as described further below including said further preferred subgroups thereof.
  • said polymer component (i) consists of one polymer (A) which bears silane - moieties.
  • said polyolefin composition comprises said silane-functionalised polymer (A) component (i), wherein said functional silane-groups are incorporated by grafting silane compounds to said base polymer (A) as described further below including said further preferred subgroups thereof, and referred herein as silane-grafted polymer component (i).
  • silane-moieties are introduced by grafting silane moieties to said base polymer (A), i.e. to said ethylene homopolymer or copolymer (Al), more preferably to said LDPE homo- or copolymer (Ai i), more preferably to said LDPE copolymer (Ai i b), more preferably to said LDPE copolymer of ethylene with at least polar comonomer(s) (A2), more preferably to said LDPE copolymer of ethylene with at least polar comonomer(s) (A3), as defined above and further below including said further preferred subgroups thereof and which are referred herein also as silane-grafted ethylene homopolymer or copolymer (Al) component (i), and as preferable, in increasing preference order, LDPE homo- or copolymer (Ai i),
  • Said silane-grafted polymer component (i) is preferably obtainable by grafting via radical reaction silane compounds (B) to said base polymer (A).
  • the "grafting" or “silane-grafting" of a polymer as used herein is thus a well known modification method and means introducing compounds to the polymer chain (backbone and/or side chain) by radical reaction, i.e. by reacting a polymer with a silane compound(s).
  • radical reaction i.e. by reacting a polymer with a silane compound(s).
  • silane-grafted polymer component (i) is obtainable by radical reaction using one or both of an irradiation or a free radical generating agent including any conventional inorganic or organic free radical generating agents.
  • silane-grafted polymer component (i) as defined above is preferably prepared using a silane-graftable polymer composition (C) which also forms part of the invention and which comprises - at least one base polymer (A) component, which is referred also as "polymer (A)", which is ethylene homopolymer of copolymer (Al),
  • composition (C) is referred herein as “composition (C)”.
  • said compostion (C) further comprises said polyolefin component (ii) as defined above and further below including said further preferred subgroups thereof, which preferred composition (C) is referred herein as silane-graftable polymer composition (Cl), and also as “composition (Cl)".
  • Said silane-graftable polymer composition (C), preferably, said preferred composition (Cl), is highly feasible for producing said silane-grafted polymer component (i) of said polyolefin composition as defined above including said further preferred subgroups thereof.
  • a preparation process for producing said silane-grafted polymer component (i) as defined above comprises a step of mixing at least said base polymer (A), said silane compound (B) and said initiator together to form a silane - graftable polymer composition (C), preferably mixing at least said base polymer (A), said silane compound (B), said polyolefin component (ii) and said initiator together to form a silane-graftable polymer composition (Cl), and a step of grafting the obtained composition (C), preferably the obtained composition (Cl), and recovering the obtained silane-grafted polymer (A) component (i).
  • the grafting step is carried out under silane - grafting conditions. Grafting naturally occurs due to reaction of said base polymer (A) and silane compound (B) initiated by said initiator, and when grafting said preferable composition (Cl), in the presence of said polyolefin component (ii). Also further component(s) may be present during said grafting step.
  • Said silane-grafting step can be effected according or analogously to grafting processes and conditions that are well known in the art and include i.a. melt mixing in any compounding equipment, i.e. mixing device, such as a conventional single or twin screw extruder or a kneader, e.g. supplied by Buss.
  • the grafting is typically effected above the melting point of the polymer components and below the undesired decomposition temperature of the polymer material and/or further components present in said mixture during said grafting process.
  • the grafting step is preferably carried out under mixing and at a temperature of above 100 0 C, preferably of above 15O 0 C, and e.g. below 23O 0 C , preferably in the range of 150 to 19O 0 C, depending on the used polymer material and optional further components.
  • Said base polymer (A) of composition (C), preferably of composition (Cl), and above and below preferable subgroups thereof, is highly preferable for preparing said silane- grafted polymer component (i), of said polyolefin composition, but it is also to be understood to be preferable polymer (A) for any of said polymer component (i) bearing silane -moieties that is usable in the present invention.
  • said polymers (A) that are suitable for said composition (C), preferably for said composition (Cl), and thus for producing said silane-grafted polymer component (i) of said polyolefin composition are referred herein shortly "preferable for C/Cl/polymer component (i)" and include any suitable polymers that are e.g. commercially available polymers or they can be prepared in a known manner according to or analogously to polymerisation process described in the literature.
  • the properties of said polymer (A) for C/Cl/polymer component (i) may vary considerably depending on the end application of said polyolefin composition.
  • Melt flow ratio, MFR 2 of said polymer (A) may typically be of at least 0.01 g/10 min, suitably of at least 0.5 g/10 min, preferably of at least 1.0 g/10 min, more preferably of at least 2.0 g/10 min, even more preferably of at least 3.0 g/10 min, when measured according to ISOl 133, 2.16 kg load, 19O 0 C.
  • the upper limit MFR 2 of said polymer (A) is not limited and may be e.g. of up 50 g/10 min , such as of up to 30 g/10 min, preferably up of to 20 g/10 min, more preferably of up to 15 g/10 min, when determined as defined above.
  • the density of preferable polymer (A) for C/Cl/polymer component (i) may typically be e.g. less than 980 kg/m , preferably from 900 to 960 kg/m , more preferably between 910 to 958 kg/m 3 .
  • Said polymer (A) for C/Cl/polymer component (i) thus is a homopolymer of ethylene or copolymer of ethylene with one or more comonomers, which is referred above also as polyethylene (Al) and is preferably selected from 1) a branched polyethylene homo- or copolymer produced in high pressure by radical polymerisation and well known as low density polyethylene (LDPE) homopolymer or copolymer, which is referred herein as LDPE homo- or copolymer (Ai i), or 2) a linear polyethylene homo- or copolymer produced by low pressure polymerisation using a coordination catalyst, such as well known linear very low density polyethylene, linear low density polyethylene (LLDPE), medium density polyethylene (MDPE) or high density polyethylene (HDPE), which is referred herein as linear PE homo- or copolymer (Ai 2).
  • LDPE low density polyethylene
  • MDPE medium density polyethylene
  • HDPE high density polyethylene
  • said polyethylene (Al) as defined above suitable as said polymer (A) for producing said silane-grafted polymer component (i) of the invention can be said linear PE homo- or copolymer (Ai 2 ), which is preferably VLDPE, LLDPE, MDPE or HDPE polymer. They can be produced in a known manner in a single or multistage processes e.g. as slurry polymerisation, a solution polymerisation, a gas phase polymerisation, and in case of multistage process in any combination(s) thereof, in any order, using one or more of e.g. Ziegler-Natta catalysts, single site catalysts, including metallocenes and non- metallocenes, and Cr-catalysts.
  • the preparation of linear ethylene polymer is and the used catalysts are very well known in the field, and as an example only, reference is made i.a. to a multistage process described in EP517868.
  • a chain transfer agent such as propylene.
  • Such polymers are well known and described e.g. in WO 93/08222, EP1695996 or WO2006/131266.
  • said unsaturated polyolefins have a double bond content of more than 0.1 double bonds/1000 C-atoms.
  • Said preferable LDPE homo or copolymer (Ai i) subgroup of said ethylene polymers (Al), as defined above as preferred for C/Cl /polymer component (i), is more preferably an LDPE copolymer of ethylene with one or more comonomers which are preferably selected from a) C3 or higher olefin comonomer(s), preferably (C3-C30)alpha-olefin comonomer(s), more preferably (C3-C12)alpha-olefin comonomer(s), b) polar comonomer(s), c) silane comonomer(s) or d) polyunsaturated comonomer(s), e.g.
  • LDPE copolymer a comonomer with at least two double bonds, such as diene comonomers, or a mixture of said (a)-(d) comonomers, and which LDPE copolymer may optionally have a further unsaturation provided by using a chain transfer agent, such as propylene, and which LDPE copolymer is referred herein as LDPE copolymer (Ai i b).
  • chain transfer agent such as propylene
  • Most preferred polymer (A) for C/Cl/polymer component (i) is said LDPE copolymer (Ai i b), more preferably is a LDPE copolymer (Ai i b), wherein the comonomer is selected from one or more of b) polar comonomer(s) and may optionally comprise an unsaturation provided preferably by copolymerising ethylene with at least one (d) polyunsaturated comonomer(s) and/or by using a chain transfer agent, such as propylene, as defined above, which LDPE copolymer is referred herein as LDPE copolymer of ethylene with at least polar comonomer(s) (A2), and is most preferably an LDPE copolymer of ethylene and at least (b) polar comonomer(s).
  • said polar (b) comonomer(s) in said LDPE copolymer of ethylene with at least polar comonomer(s) (A2) for C/Cl/polymer component (i) is/are selected from: (a) vinyl carboxylate esters, such as vinyl acetate and vinyl pivalate, (b) (meth)acrylates, such as methyl(meth)acrylate, ethyl(meth) aery late, butyl(meth)acrylate and hydroxyethyl(meth)acrylate, (c) olefinically unsaturated carboxylic acids, such as (meth)acrylic acid, maleic acid and fumaric acid, (d) (meth)acrylic acid derivatives, such as (meth)acrylonitrile and (meth)acrylic amide, or (e) vinyl ethers, such as vinyl methyl ether and vinyl phenyl ether.
  • vinyl carboxylate esters such as vinyl acetate and vinyl pivalate
  • said LDPE copolymer of ethylene with at least polar comonomer(s) (A2) for C/Cl/polymer component (i) is a LDPE copolymer of ethylene with one or more of vinyl esters of monocarboxylic acids having 1 to 4 carbon atoms, such as vinyl acetate, or of (meth)acrylates of alcohols having 1 to 4 carbon atoms, or of a mixture thereof, preferably of vinyl acetate, methyl (meth)acrylate, ethyl (meth)acrylate or butyl (meth)acrylate.
  • the preferred subgroup of said LDPE copolymer of ethylene with at least polar comonomer(s) (A2) of C/Cl/polymer component (i) is a LDPE copolymer of ethylene with at least vinyl acetate, LDPE copolymer of ethylene with at least methyl acrylate, a LDPE copolymer of ethylene with at least ethyl acrylate or a LDPE copolymer of ethylene with at least butyl acrylate, or any mixture thereof.
  • (meth)acrylic acid and “(meth)acrylate” are intended to embrace both acrylic acid and methacrylic acid and, respectively “methacrylate” and “acrylate”.
  • the content of polar comonomer in said LDPE copolymer of ethylene with at least polar comonomer(s) (A2) as defined above, that is most preferable as said polymer (A) for C/Cl/polymer component (i), is not limited and may be of up to 70 wt%, preferably of 0.5 to 35 wt%, more preferably of 1.0 to 35 wt%, of the total amount of said LDPE copolymer.
  • high polar comonomer content is preferred, whereby the content of polar comonomer units can be of at least 20 wt%, such as at least 25 wt%, preferably at least 26 wt% more preferably from 27 to 35 wt%, based on said LDPE copolymer (A2).
  • Said preferred high polar comonomer content when expressed using mol-%, present in said LDPE copolymer of ethylene with at least polar comonomer(s) (A2) can then be of at least 7.0 mol%, preferably of at least 7.5 mol% , more preferably of from 8 to 15 mol%, polar comonomer units based on the total moles of polymerisable monomers of said LDPE copolymer (A2).
  • High pressure polymerisation for producing said LDPE homo or copolymer (Ai i) and the subgroups (Ai i b), (A2) and, respectively, (A3) thereof, as defined above, is a well known technology in the polymer field and can be effected in a tubular or an autoclave reactor, preferably, in a tubular reactor. Further details about high pressure radical polymerisation are given in WO 93/08222.
  • the polymerisation of the high pressure process is generally performed at pressures of from 1200 to 3500 bar and temperatures of from 150 to 35O 0 C.
  • composition (C), preferably said composition (Cl), and polymer component (i) of the invention comprises, preferably consists of one polymer (A) which bears silane-moieties.
  • Said unsaturated silane compound (B) that is preferable for C/Cl/polymer component (i), as defined above, is preferably a vinyl-functional silane compound, most preferably an unsaturated silane compound represented by the formula
  • R 1 is an ethylenically unsaturated hydrocarbyl, hydro carbyloxy or (meth)acryloxy hydrocarbyl group,
  • R 2 is an aliphatic saturated hydrocarbyl group, Y which may be the same or different, is a hydrolysable organic group and q is 0, 1 or 2.
  • unsaturated silane compound (I) are those wherein R is vinyl, allyl, isopropenyl, butenyl, cyclohexanyl or gamma-(meth)acryloxy propyl; Y is methoxy, ethoxy, formyloxy, acetoxy, propionyloxy or an alkyl-or arylamino group; and R 2 , if present, is a methyl, ethyl, propyl, decyl or phenyl group.
  • a preferred unsaturated silane compound (I) is represented by the formula
  • CH 2 CHSi(OA) 3 (Ia) wherein A is a hydrocarbyl group having 1-8 carbon atoms, preferably 1-4 carbon atoms.
  • the preferred compounds of formula (Ia) as said silane compound (B) for the present invention are vinyl trimethoxysilane, vinyl bismethoxyethoxysilane, vinyl triethoxysilane, gamma-(meth)acryloxypropyltrimethoxysilane, gamma(meth)acryloxypropyltriethoxysilane, and vinyl triacetoxysilane, more preferably vinyl trimethoxysilane or vinyl triethoxysilane.
  • Said base polymer component (A), said silane compound (B) and said optional polyolefin component (ii) in said composition (C), preferably in said composition (Cl), as defined above, preferably for producing said silane-grafted polymer component (i), correspond to and can be calculated by a skilled person based on the amounts of polymer component (i), polyolefin component (ii) and on the amount of silane-moieties that are to be provided for the final polyolefin composition as defined above and below including said further preferred subgroups thereof.
  • silane compound (B) is added in amount of 0.001 to 15 wt%, more preferably of from 0.01 to 5.0 wt%, most preferably of from 0.1 to 2.0 wt%, most preferably of from 0.4 to 2.0 wt%, most preferably of from 0.6 to 2.0 wt%, based on the weight of polymer component (A).
  • Said initiator of said silane-graftable polymer composition (C), preferably of composition (Cl), of the invention preferable for producing said silane-grafted polymer component (i) for said polyolefin composition can be any suitable agent for initiating the grafting reaction.
  • Non-limiting examples of preferable initiator are organic peroxides, such as di-tert-amylperoxide, 2,5-di(tert-butylperoxy)-2,5-dimethyl-3-hexyne, 2,5-di(tert- butylperoxy)-2,5-dimethylhexane, tert-butylcumylperoxide, di(tert-butyl)peroxide, dicumylperoxide, bis(tert-butylperoxyisopropyl)benzene, butyl-4,4-bis(tert-butylperoxy)- valerate, l,l-bis(tert-butylperoxy)-3,3,5-trimethylcyclohexane, tert-butylperoxybenzoate, dibenzoylperoxide, 2,5-dimethyl-2,5-di(benzoylperoxy)hexane, l,l-di(tert- but
  • the amount of said initiator used in said composition (C), preferably in said composition (Cl), as defined above, preferably for producing said silane-grafted polymer component (i) for said polyolefin composition depends on the amount of said silane compound (B) desired to be incorporated to said silane-grafted polymer component (i) and, respectively, to said polyolefin composition of the invention, and can be determined by a skilled person.
  • the amount of said initiator may preferably vary in the range of 0.05 to 0.5 mol% based on the total polymerisable monomers of said base polymer (A) and total moles of said silane compound (B).
  • said polyolefin composition includes also i.a. an embodiment, wherein said (i) polymer component bearing silane -moieties is a copolymer of monomer with at least one silane comonomer and optionally with one or more further comonomer.
  • Said (i) polymer component of this further embodiment is referred herein as silane-copolymer component (i).
  • Said silane - copolymer component (i) is preferably said base polymer (A), as defined above and below including said further preferred subgroups thereof, which comprises additionally one or more silane comonomer(s).
  • Said silane comonomer is preferably said silane compound (B), preferably said unsaturated compound of formula I, more preferably of formula Ia, as defined above including said further preferred subgroups thereof.
  • said silane-copolymer component (i) is as said silane-functionalised polymer (A) component (i) as defined above including said preferable subgroups thereof, which comprises further said silane comonomers as defined above including said further preferred subgroups thereof.
  • Said silane-copolymer component (i) as said polymer component (i) of said polyolefin composition is obtainable by polymerising monomer units, such as an olefin, more preferably ethylene, preferably with one or more (b) polar comonomer(s), as defined above for polymer (A) and preferred subgroups thereof for preferred C/C 1/polymer component (i), and with at least one silane comonomer, which is preferably said silane compound (B), preferably said unsaturated silane -compound of formula I, more preferably of formula Ia, under "Preparation of said silane-grafted polymer component (i)"as defined above including said further preferred subgroups thereof, and in amounts of said silane comonomer(s) and any polar comonomer(s), if present, which correspond to and can be calculated based on the amounts given therein.
  • monomer units such as an olefin, more preferably ethylene, preferably with one
  • Said (ii) polymer of olefin having at least 3 carbon atoms of said polyolefin composition of the invention as defined above is an olefin homopolymer or copolymer, wherein said olefin has at least three carbon atoms.
  • Said polyolefin component (ii) can be a linear, straight or branched chain, olefin or a cyclic olefin, and which can have at least one unsaturated bond, such as a double bond, or which can be polyunsaturated, such as a diene or polyene, olefin, preferably a linear, straight or branched chain, (C3-C50)alpha- olefin, preferably (C3- C20)alpha-olefin, more preferably an alpha-olefin having 3 to 12 carbon atoms.
  • said C3 or higher olefin may be copolymerised with one or more comonomer(s) other than said C3 or higher olefin, which can be linear, straight or branched chain, comonomer(s) or cyclic comonomer(s), and which can have at least one unsaturated bond, such as double bond, or which can be polyunsaturated, such as a diene or polyene, comonomer(s).
  • said comonomer(s) are olefins, preferably ethylene or (C3-C50)olefins, such as ethylene or (C3-C20)alpha-olefins, more preferably ethylene or (C3-C12)alpha-olefins, such as ethylene, butene, hexene, heptene, octene or decene.
  • olefins preferably ethylene or (C3-C50)olefins, such as ethylene or (C3-C20)alpha-olefins, more preferably ethylene or (C3-C12)alpha-olefins, such as ethylene, butene, hexene, heptene, octene or decene.
  • Preferred polyolefin component (ii) of said polyolefin composition include homopolymers of propylene, random copolymers of propylene or heterophasic copolymers of propylene, as well as homo- or copolymers of butene, which all are very well known in the polymer field.
  • said polyolefin component (ii) is selected from propylene homopolymers, random propylene copolymers or heterophasic propylene copolymers, or from mixtures thereof.
  • Said heterophasic propylene copolymer comprises a matrix phase which can be a propylene homopolymer or a propylene copolymer, and an elastomeric phase of propylene copolymer, also known as rubber part, which is dispersed in said matrix phase.
  • the comonomer used in said random propylene copolymer and in said elastomeric propylene copolymer phase, and optionally in said random propylene copolymer matrix, of a heterophasic propylene copolymer as polyolefin component (i) is preferably ethylene or (C4-C20)olefin, even more preferably ethylene or (C4-C12)alpha- olefin, such as ethylene, butene, pentene, hexene, heptene, octene, of decene, or any mixture thereof, preferably ethylene and/or butene.
  • Said random propylene copolymer as said polyolefin component (ii) of the invention contains preferably conventionally used amounts of comonomer, for example up to 30 wt% of the amount of said polyolefin component (ii), e.g. between 0.5 to 20wt%, preferably 1.0 to 10 wt%, more preferably between 2.0 to 7 wt%, even more preferably 2.5 to 5 wt%, based on the amount of said polyolefin component (ii).
  • the xylene solubles content (wt%) of said random propylene copolymer as said polyolefln component (ii) is preferably of up to 20 wt%, preferably of up to 15 wt%, e.g. 0.5 to 10 wt%, based on the amount of said polyolefln component(ii).
  • Said homopropylene component as said polyolef ⁇ n component (ii) of said polyolef ⁇ n composition of the invention has typically a XS (in wt%) e.g. of below 5 wt%, such as 0.1 to 3 wt%, based on the amount of said polyolefin component (ii).
  • Said heterophasic propylene copolymer as said polyolefin component (ii) comprises said matrix phase of propylene homo- or copolymer of up to 95 wt%, preferably of from 20 to 90 wt%, said elastomeric propylene copolymer phase of up to 80 wt%, preferably of from 10 to 40wt%, based on the amount of said heterophasic propylene copolymer.
  • said matrix phase of said heterophasic propylene copolymer is a random propylene copolymer
  • the comonomer content and XS (wt%) content of said matrix phase is preferably as defined above for said random copolymer as said polyolefin component (ii).
  • said matrix phase is a propylene homopolymer
  • said XS (wt%) content is preferably as defined above for said propylene homopolymer component as said polyolefin component (ii).
  • Said heterophasic propylene copolymer as said polyolefin component (ii) has typically a total xylene solubles (wt%) of up to 50 wt%, preferably of up to 30 wt%, based on the amount of said polyolefin component (ii).
  • Suitable homo, random and heterophasic polymers of propylene (PP) as said polyolefin component (ii) of said polyolefin composition of the invention are e.g. well known and commercially available or, alternatively, may be produced using e.g conventional polymerisation processes which are well documented in the literature. Accordingly also the polypropylene polymer usable in the present invention may be produced in a single - or multistage process e.g. as bulk polymerisation, gas phase polymerisation, slurry polymerisation, solution polymerisation, and in case of a multistage process in any combination(s) thereof, in any order, using conventional catalysts including Ziegler-Natta and single site, such as metallocene catalysts.
  • the matrix of propylene homopolymer or random copolymer can be produced e.g. in a single stage or as a multistage process described above and the elastomeric (rubber) part of the propylene copolymer can be produced as an in-situ polymerisation e.g. in a separate reactor, e.g. gas phase reactor in the presence of the matrix polymer produced in the previous stage.
  • the elastomeric copolymer of propylene part can be mechanically compounded to the matrix phase material, as well known in the art.
  • suitable polypropylenes as said (ii) component and the preparation processes thereof reference is made to e.g. Nello Pasquini (Ed.) Polypropylene Handbook, Hanser, Kunststoff, 2005, pages 15 - 141.
  • said polyolefin composition of the invention may comprise more than one said polyolefin component (ii) as defined above, preferably comprises one polyolefin component (ii) which comprises, preferably consists of, one or more, preferably one of a propylene homopolymer, random propylene copolymer or a heterophasic propylene copolymer, as defined above.
  • said polyolefin of the invention includes also an embodiment wherein said polyolefin component (ii) is treated by radical reaction after polymerisation process thereof, preferably using a free radical generating agent(s) for further modifying the properties, such as rheological properties, thereof.
  • said polyolefin, preferably said polypropylene as defined above, component (ii) of said polyolefin composition has a melting temperature of at least 65 0 C, such as of at least 8O 0 C, preferably of at least 100 0 C, more preferably of at least 12O 0 C, e.g. of up to 200 0 C, preferably of between 13O 0 C to 19O 0 C.
  • component (ii) of said polyolefin composition is typically of at least 2.0 g/10 min, preferably of at least 3.0 g/10 min and of up to 150 g/10 min, preferably of from 3.0 to 50 g/10 min, more preferably of from 3.0 to 30 g/10 min.
  • Optional filler (iii) of the invention Said polyolefin composition of the invention may optionally comprise one or more filler(s) (iii) including any organic and inorganic solid compound which are understood and conventionally used in prior art within the meaning of "filler".
  • said filler (iii) is at least, preferably consists of, a carbon black (CB).
  • high filler content can be incorporated into the polyolefin composition due to the highly beneficial rheological properties of said combination of said components (i) and (ii).
  • said filler (iii) is present and is a carbon black.
  • the type and amount of said CB as said filler (iii) of the invention are not limited and can be selected depending on the end application of said polyolefin composition.
  • Preferably said carbon black is electrically conductive.
  • Said carbon black as said filler (iii) of polyolefin composition has a surface area of up to 300 m 2 /g, preferably of up to 140 m 2 /g, more preferably of up to 80 m 2 /g, even more preferably of from 30 to 70 m 2 /g, most preferably of from 40 to 65 m 2 /g, when measured according to ASTM D 4820-99 (BET, N 2 adsorption).
  • this preferable carbon black (iii) with specific surface area is believed to have an advantageous effect in preventing and thus decreasing scorch, i.a. premature crosslinking, which is a well known undesired phenomenon during e.g. a cable preparation process.
  • said polyolefin composition of the invention which is suitable i.a. for a semiconductive layer material of a cable
  • said polyolefin composition comprises a (iii) carbon black as defined above in an amount that provides a volume resistivity of less than 500000 ⁇ cm, preferably of less than 100000 ⁇ cm, when measured at 23 and/or 90 0 C, to said polyolefin composition.
  • said polyolefin composition comprises said (iii) CB in an amount that provides a volume resistivity of less than 5000 ⁇ cm, preferably of less than 1000 ⁇ cm, such as of less than 500 ⁇ cm, more preferably of less than 100 ⁇ cm, when measured at 23 0 C, or of less than 50000 ⁇ cm, preferably of less than 10000 ⁇ cm, such as of less than 5000 ⁇ cm, more preferably of less than 1000 ⁇ cm, when measured at 90 0 C, to said polyolefin composition.
  • the carbon black as said filler (iii) of the invention may have an arithmethic mean primary particle size of at least 20 nanometers, preferably at least 29 nanometers, up to 70 nanometers, when measured using transmission electron microscopy as described in ASTM D 3849-95a, dispersion procedure D.
  • said carbon black as said filler (iii) of the invention has a DBP (dibutyl phthalate) absorption number of from 80 to 300 cm /10Og, preferably less than 180 cm 3 /100g, when measured according to ASTM D 2414-06a.
  • DBP dibutyl phthalate
  • Non-limiting examples of carbon blacks as said filler (iii) of the invention are e.g. carbon blacks grades described with ASTM Nxxx codes, Ensaco black, supplied e.g. by Timcal, Timcal acetylene black, furnace black and Ketjen black.
  • Preferable carbon blacks as said filler (iii) of the invention are Ensaco black supplied e.g. by Timcal, furnace carbon black.
  • Other suitable carbon blacks for the present invention are also those described e.g. EP1065672.
  • Said polyolefin composition of the invention may additionally comprise further components such as further polymers or, preferably, additives, such as at least antioxidant(s).
  • Said antioxidant is preferably a compound, or a mixture of such compounds, which compound is neutral or acidic, and can be a diphenyl amine compound, a quinoline compound, a compound which comprises a sterically hindered phenol group or a compound which comprises aliphatic or aromatic sulphur group(s).
  • Particularly suitable antioxidants for said polyolefln composition of the invention are disclosed i.a. in WO2005003199A1 and EP 1 254 923.
  • additives such as one or more of stabilisers, e.g. voltage stabilisers, processing aids, scorch retardants, crosslinking boosters or water tree retardants, lubricants or any mixtures thereof, can be mentioned.
  • stabilisers e.g. voltage stabilisers, processing aids, scorch retardants, crosslinking boosters or water tree retardants, lubricants or any mixtures thereof.
  • the additives can be used i.a. in conventional amounts and in a manner well known in the art.
  • the antioxidant is preferably present in the composition in an amount of from 0.01 to 3 wt%, more preferably 0.05 to 2 wt%, and most preferably 0.08 to 1.5 wt%, based on the amount of said polyolefln composition of the invention.
  • said polyolefln composition of the invention is avoid of, i.e. does not contain, any metal hydroxide comprising additives, such as flame retardants which comprise a metal hydroxide.
  • polymer components present in said polyolefln composition consist of said polymer component (i) and polyolefln component (ii) as polymer components, i.e. no other polymer components are present, and further comprises said optional filler (iii) and optional additives, preferably further comprises said filler (iii) and at least an antioxidant.
  • the invention provides a process for producing said polyolefin composition as defined above or below in claims, wherein said process comprises a step of mixing -said polymer component (i) which is a polyethylene (Al) bearing silane-moieties,
  • polyolefin component (ii) which is a polymer of olefin having at least 3 carbon atoms
  • At least said polymer component (i) is added first to said mixing step of the invention.
  • This addition step is referred herein as a "first mixing step”.
  • At least said polymer component (i) and said polyolefin component (ii) are added together at said first mixing step of said mixing step of PROCESS.
  • Said mixing step can be carried out in any mixer, i.e. compounding device, such as a conventional extruder or mixer as described above in relation to preparation of said silane-graftable polymer composition (C), as defined above including said further preferred subgroups thereof.
  • the mixing is effected in an elevated temperature which is above the melting temperature of the polymer components present in said polyolefin composition of the invention and preferably below an undesired decomposition of any of said polyolefin composition of the invention.
  • the preferable mixing temperature is of above 100 0 C, preferably of above 15O 0 C, typically of below 23O 0 C, more preferably of from 150 to 19O 0 C.
  • the polymer component (i) and polyolefin component (ii) can independently be prepared before the mixing step of PROCESS, or during PROCESS.
  • said silane-moieties present in the final polyolefln composition of the invention are introduced during PROCESS by producing said polymer component (i), more preferably by silane-grafting said functional silane-moieties to said base polymer (A) of the polymer component (i) as defined above, in situ during PROCESS.
  • PROCESS comprises a step of producing said polymer component (i) at said first mixing step or at said subsequent mixing step(s) during the mixing step of PROCESS, and optionally in the presence of one or both of said polyolefin component (ii) and said filler (iii).
  • said polyolefin composition is produced, which comprises said silane-grafted polymer component (i) as defined above including said further preferred subgroups thereof. More preferably, said silane-grafted polymer component (i) is produced during the mixing step of said PROCESS by adding the components of said silane-graftable polymer composition (C), as defined above, at said first mixing step and by silane-grafting under mixing said silane compound (B) to said polymer (A) in the presence of said initiator, more preferably by adding the components of said silane-graftable composition (Cl) as defined above and silane-grafting said silane compound (B) to said polymer (A) in the presence of said initiator and in the presence of said polyolefin component (ii).
  • composition (Cl) visbreaking and/or grafting of said polyolefin component (ii) may also occur due to action of said initiator and said polyolefin component (ii), as known in the art.
  • Said polyolefin component (ii) is preferably a propylene homopolymer, a random copolymer of propylene or a heterophasic copolymer of propylene, or any mixture thereof, as defined above including said further preferred subgroups thereof.
  • Said optional filler (iii) is preferably present in said polyolefin composition of the invention, and it is preferably added at said subsequent mixing step(s) during said mixing step of PROCESS.
  • the obtained polyolefin composition of the invention is recovered in a known manner and preferably pelletised in a subsequent well known pelletsing step as a part of said preparation process.
  • the obtained pellets comprising said polyolefin composition are recovered for further use in various end applications, preferable in cable production.
  • Said pelletising step may be carried out e.g. in conventional pelletising equipment, such as extruder, as well known.
  • the invention further provides pellets comprising said polyolefin composition of the invention.
  • pellets is well known and includes herein any powder, granule or pellet form of any shape of said polyolefin composition of the invention, and thus such powders, granules and pellets of said polyolefin composition of the invention are also covered by the present invention. Said pellets of the invention have excellent storage stability.
  • PROCESS may be carried out batch wise or in a continuous manner.
  • PROCESS may be integrated directly to a production line of a product which is produced using said polyolefin composition of the invention.
  • Said production line is preferably a cable production line.
  • PROCESS and equipment of the invention is naturally preceded the production step and production line of said intermediate and/or end product, whereby after said mixing step the obtained polyolefin composition is further processed to an end product, such as a cable layer.
  • said polyolefin composition is silane-crosslinkable and referred herein as silane-crosslinkable polyolefin composition.
  • silane-crosslinkable polyolefin composition said functional silane- group(s), i.e. silane-moieties, of said polymer component (i) are silane-crosslinkable, more preferably are silane-crosslinkable hydrolysable silane group(s). Accordingly, a silane-crosslinkable polyolefin composition is provided which comprises said silane-crosslinkable polymer (A) component (i), said polyolefin component (ii) and said optional filler (iii).
  • said silane-crosslinkable polymer (A) component (i) of said silane-crosslinkable polyolefin composition comprises, preferably consists of, said silane-grafted polymer (A) component (i) which is said silane-grafted ethylene homopolymer or copolymer (Al) component (i), preferably said silane-grafted LDPE homo- or copolymer (Ai i) component (i), more preferably said silane-grafted LDPE copolymer (Ai i b) component (i), even more preferably said silane-grafted LDPE copolymer with at least polar comonomer(s) (A2) component (i), even more preferably said LDPE copolymer of ethylene and at least polar comonomer(s) (A3), as defined above including said further preferred subgroups thereof, which is silane-crosslinkable, and referred herein as silane-crosslinkable silane-grafted polymer (Al) component (i),
  • the preferred hydrolysable silane-groups of said crosslinkable polyolefin composition of the invention comprise, preferably consist of, hydrolysable silane-groups that are provided by said silane compound (B) during the preparation of said silane-graftable polymer component (i) of said polyolefin composition, more preferably using said silane-graftable composition polymer (C), more preferably using said silane-graftable polymer composition (Cl), preferably during said PROCESS, as defined above including said further preferred subgroups thereof.
  • the degree of crosslinking depends on and can be controlled by the amount of said compound (B) which provides said crosslinkable silane-groups.
  • the amount of said silane compound (B) is thus not limited and can be varied depending i.a. on the degree of crosslinking which is desired for the final crosslinked polyolefin composition of the invention.
  • silane-crosslinkable pellets which contain said silane- crosslinkable polyolefin composition which comprises said silane-crosslinkable, preferably, silane-grafted polymer (A) component (i) as defined above, which is said silane-crosslinkable silane-grafted ethylene homopolymer or copolymer (Al) component (i), more preferably said silane-crosslinkable silane-grafted LDPE homo- or copolymer (Ai i) component (i), even more preferably said silane-crosslinkable silane-grafted copolymer (Ai i b) component (i), most preferably said silane-crosslinkable silane-grafted copolymer with at least polar comonomer(s) (A2) component (i), even more preferably said silane-crosslinkable silane-grafted LDPE copolymer of ethylene and at least polar comonomer(s) (A3) component (i), as defined above including said further preferred subgroups thereof
  • Said silane-crosslinkable polyolefin composition may further comprise a silane- crosslinking agent for silane-crosslinking said composition in a subsequent crosslinking step as described below.
  • said crosslinkable polyolefin composition of the invention which is recovered for further use, e.g. for producing products comprising said polyolefin composition, comprises no added silane- crosslinking agent, i.e. no silane-crosslinking agent is added to said composition before said recovery step, e.g. said pelletising step.
  • said pellets of said crosslinkable polyolefin composition do not comprise, i.e. are avoid of, any silane- crosslinking agent.
  • the crosslinkable polyolefin composition of the invention is preferably brought to a silane-crosslinking contact with said silane-crosslinking agent during the actual silane-crosslinking step of said polymer composition as described later below.
  • the invention also independently provides a polyolefin composition (SG), which comprises - a polymer component (i) which is a silane-grafted polymer (A)
  • polyolefin component (ii) which is a polymer of olefin having at least 3 carbon atoms , and, optionally,
  • the base polymer (A) of said component (i) is an ethylene homopolymer or copolymer (Al) which is silane-grafted, and wherein said polyolefin composition has a melt flow ratio, MFR 21 of at least 0.01 g/10 min when measured according to ISO 1133 at 19O 0 C using 21.6 kg load, and wherein
  • melt fow ratio, MFR, of said polyolefin composition when measured according to ISO 1133 at 19O 0 C with a load of 2.16 kg or 21.6 kg, is changed of less than ⁇ 60 %, preferably less than ⁇ 30 %, more preferably of less than ⁇ 27 %, in some embodiments even of less than ⁇ 15%, from the initial MFR thereof, after a storage period of 9 months, when stored in a sealed container in a room which has an atmospheric pressure, temperature of 23 0 C and relative humidity of 55% as defined above.
  • said polyolefin composition (SG) comprises said filler (iii) and the MFR definition of property (i) above is measured for MFR 21 with 21.6 kg load.
  • Said polyolefin composition (SG) is preferably as defined above for said silane-grafted polyolefin composition including the preferable subgroups thereof and, preferably produced as defined above for the preparation of the silane-grafted polyolefin composition including preferable subgroups thereof. Moreover, the below crosslinking methods and end applications described below for said polyolefin composition apply similarly for said polyolefin composition (SG).
  • the invention further provides a silane-crosslinking process for preparing a silane- crosslinked polyolefin composition of the invention, which process comprises a step of silane-crosslinking of said silane-crosslinkable polyolefin composition of the invention as defined above including said further preferred subgroups thereof, in the presence of silane-crosslinking agent.
  • said crosslinkable silane-groups that are present in said polyolefln composition are hydro lysable silane-groups which are crosslinked by hydrolysis and subsequent condensation in the presence of a silanol-condensation catalyst and water in a manner known in the art.
  • Said silane-crosslinking agent suitable for silane-crosslinkable polyolefin composition of the invention is preferably a silanol condensation catalyst selected from carboxylates of metals, such as tin, zinc, iron, lead and cobalt; organic bases; inorganic acids; and organic acids, more preferably carboxylates of metals, such as tin, zinc, iron, lead and cobalt, or an organic acid , which is prefereably an organic sulphonic acid, more preferably, an organic sulphonic acid comprising 10 C-atoms or more, more preferably 12 C-atoms or more, and most preferably 14 C-atoms or more, the sulphonic acid further comprising at least one aromatic group which may e.g.
  • Preferred sulphonic acid is the aromatic organic sulphonic acid which comprises the structural element: Ar(SO 3 H) x (II) with Ar being an aryl group which may be substituted or non- substituted, and x being at least 1, or a precursor of the sulphonic acid of formula (II) including an acid anhydride thereof or a sulphonic acid of formula (II) that has been provided with a hydrolysable protective group(s), e.g. an acetyl group that is removable by hydrolysis.
  • the preferred silanol condensation catalyst may comprise the structural unit according to formula (II) one or several times, e.g. two or three times.
  • two structural units according to formula (II) may be linked to each other via a bridging group such as an alkylene group.
  • Ar is a aryl group which is substituted with at least one C 4 - to C30- hydrocarbyl group, more preferably C 4 - to C3o-alkyl group.
  • Aryl group Ar preferably is a phenyl group, a naphthalene group or an aromatic group comprising three fused rings such as phenantrene and anthracene.
  • x is 1 , 2 or 3, and more preferably x is 1 or 2.
  • the compound used as organic aromatic sulphonic acid silanol condensation catalyst has from 10 to 200 C-atoms, more preferably from 14 to 100 C- atoms.
  • the currently most preferred compounds are dodecyl benzene sulphonic acid and tetrapropyl benzene sulphonic acid.
  • Preferable silanol-condensation catalyst for use in the present invention are described e.g. in those mentioned in EP736065.
  • sulphonic acid catalyst as described in EP 1 309 631 and EP 1 309 632 may be used.
  • the amount of said silanol condensation catalyst used in said silane-crosslinking process of the invention is typically of from 0.0001 to 6.0 wt%, more preferably of from 0.001 to 2.0 wt%, and more preferably of from 0.02 to 0.5 wt%, based on the amount of the crosslinkable polymer material.
  • the crosslinking step is effected in an elevated temperature.
  • the preferable silane- crosslinking step is typically carried out below 100 0 C, preferably below 80 0 C, more preferably between 60 to 8O 0 C. If said preferable silanol condensation catalyst as defined above is used, the said crosslinking step is carried out in the presence of liquid water or steam, i.e. water vapour, or both, preferably at least water vapour, as well known in the art.
  • Said silane-crosslinking can be effected in a conventional manner using a conventional equipment.
  • the invention thus further provides said silane-crosslinked polyolefin composition which comprises said silane crosslinked polymer component (i), as defined above or below including said further preferred subgroups thereof, and which is preferably obtainable by said silane-crosslinking process of the invention as defined above.
  • said polyolefin composition of the invention it is possible to incorporate a high amount of hydro lysable silane-groups into said (i) polymer component bearing silane-moieties during said preparation process of said hydrolysable silane-groups bearing polymer component (i), preferably of said silane-grafted polymer component (i), more preferably using said silane-graftable polymer composition (Cl), as defined above including said further preferred subgroups thereof, whereby a high degree of crosslinking can be obtained, whereby said hot set elongation property of said crosslinked polyolefin composition can be measured.
  • silane-crosslinked polyolefin composition of the invention has one or more of the following properties:
  • - feature (a) has a gel content of more than 35.0 wt%, preferably of from 37.0 wt% to 80 wt%, more preferably of less than 70 wt%, even preferably of less than 60 wt%, most preferably of between from 40.0 wt% to 50.0 wt%, when measured as defined below under "Determination methods" using a sample consisting of said silane-crosslinked polyolefin composition,
  • feature (b) has a hot set elongation of less than 200%, preferably of less than 175%, preferably of less than 100%, in some embodiment may have even as low as of less than 60%, e.g. from 1 to 60%, when measured according to IEC 60811-2-1 at 200 0 C with a load of 0.1 MPa, more preferably with a load of 0.2 MPa, using a cable layer sample which has a thickness of 1.0 mm and consists of said silane-crosslinked polyolefin composition of the invention, as described below under "Determination methods", or feature (c) comprises a silane crosslinked polymer component (i), wherein said base polymer (A) is silane-crosslinkable silane-functionalised, preferably silane-grafted, ethylene homopolymer or copolymer (Al), as defined above including said further preferred subgroups thereof, which is silane-crosslinked, and referred herein as silane- crosslinked silane-grafted polymer (Al) component (i), and said
  • said crosslinked polyolefin composition of the invention is according to said (1) first alternative, said (2) second alternative or said (3) third alternative, preferably according to said (1), (2) and (3) alternative, of said polyolefln composition of the invention, as defined above, which is crosslinked preferably according to said crosslinking process of the invention as defined above.
  • the polyolefln composition of this embodiment is very advantageous for W&C applications, particularly for semiconductive cable applications.
  • Said polyolefin composition of the invention is highly feasible in wide variety of end applications of polymers. Accordingly, the invention further provides a product which comprises the polyolefin composition of the invention as defined above and below.
  • the present polyolefin of the invention is also highly advantageous for forming end products with high filler content.
  • said product of the invention is a cable comprising a conductor surrounded with one or more layers, wherein at least one layer comprises said polyolefin composition of the invention as defined above, preferably at least one silane- crosslinkable layer which comprises said silane-crosslinkable polyolefin composition, as defined above or in claims below including said further preferred subgroups thereof.
  • conductor means herein above and below that the conductor comprises one or more wires. Moreover, the cable may comprise one or more such conductors. Preferably the conductor is an electrical conductor.
  • the cable of the invention comprises a jacketing layer and optionally one or more layers selected from an insulation layer or semiconductive layer surrounded by said jacketing layer, wherein said jacketing layer comprises said polyolefin composition as defined above, preferably said silane-crosslinkable polyolefin composition as defined above including said further preferred subgroups thereof.
  • a low voltage cable which comprises an insulation layer and optionally a jacketing layer, wherein at least said insulation layer comprises said polyolefin composition as defined above, preferably said silane-crosslinkable polyolefin composition, as defined above or in claims below including said further preferred subgroups thereof.
  • said cable is a semiconductive power cable which comprises a conductor surrounded by at least an inner semiconductive layer, an insulation layer and an outer semiconductive layer, in that order, wherein at least one of said inner and outer semiconductive layers, preferably at least said outer semiconductive layer, comprises said said silane-crosslinkable polyolefin composition as defined above or in claims below including said further preferred subgroups thereof, wherein said filler (iii) is present and is said electrically conductive carbon black, as defined above including said further preferred subgroups thereof.
  • Said power cable may optionally be surrounded by a jacketing layer.
  • At least said outer semiconductive layer of said power cable comprises said silane-crosslinkable polyolefin composition with filler (iii), wherein said (i) polymer (A) component bearing said silane- moieties is said silane-crosslinkable silane-grafted ethylene homopolymer or copolymer (Al) component (i), more preferably said silane-crosslinkable silane-grafted LDPE homo- or copolymer (Ai i) component (i), more preferably said silane-crosslinkable silane-grafted LDPE copolymer (Ai i b) component (i), even more preferably said silane- crosslinkable silane-grafted LDPE copolymer with at least polar comonomer(s) (A2) component (i), most preferably said silane-crosslinkable silane-grafted copolymer (A3) component (i) as defined above including said further preferred subgroups thereof.
  • a low voltage (LV) cable is a cable operating in voltages from 500 V to 3.6 kV.
  • a power cable is defined herein to be a cable transferring energy operating at any voltage, typically operating at voltages higher than 3.6 kV.
  • the voltage applied to the power cable can be alternating (AC), direct (DC), or transient
  • the power cable prepared according to the present invention is operating at voltages from 3.6 kV to 36 kV and known as medium voltage (MV) power cables.
  • Said polyolefin composition of the invention is preferably used for said LV or MV, more preferably for MV, cable applications.
  • the present invention thus further provides a process for producing a product by using said polyolefin composition as defined above or below in claims, more preferably said silane-crosslinked polyolefin composition as defined above.
  • a process for producing a cable comprises steps of applying on a conductor, preferably by (co)extrusion, one or more layers comprising a polymer composition, wherein at least one layer comprises said polyolefin composition as defined above including said further preferred subgroups thereof, which most preferably comprises said silane-grafted polymer (A) component (i) as defined above including said further preferred subgroups thereof.
  • (co)extrusion means herein that in case of two or more layers, said layers can be extruded in separate steps, or at least two or all of said layers can be coextruded in a same extrusion step, as well known in the art.
  • the components of a layer material can be mixed in a separate mixer before introducing to the extruder for producing said layers or added directly to an extruder and mixed therein before forming to a layer.
  • Further components such as additives, preferably as defined above including said further preferred subgroups thereof, can be added during the mixing step.
  • Said mixing step is carried out at elevated temperature, which is typically above the melting point of the polymer components of the layer material, e.g. of at least 2O 0 C, preferably of at least 25 0 C, above the melting point of said polymer components of the layer material, and preferably said mixing temperature is kept below 200 0 C.
  • Said meltmixed layer material is then (co)extruded on a conductor in a manner very well known in the field.
  • Conventional extruders and mixers may be used in the process of the invention.
  • said silane-crosslinkable polyolefin composition which comprises preferably said silane- crosslinkable silane-grafted polyethylene (1), more preferably, in increasing preference order, (Ai i), (Ai it,), (A2), most preferably (A3), component (i), as defined above, is applied on a conductor for producing at least one of the one or more cable layer(s), more preferably for producing one or more of layers selected from a semiconductive layer, an insulation layer and a jacketing layer, more preferably, for producing at least said semiconductive layer, even more preferably for producing at least said outer semiconductive layer, which is preferably strippable, of a silane-crosslinkabale power cable of the invention comprising a conductor, an inner semiconductive layer, an insulation layer and an outer semiconductive layer, in that order, as defined above under "1.1 Cable".
  • the obtained preferred silane-crosslinkable product is typically crosslinked before use in the end application thereof. Accordingly, a process for crosslinking a silane-crosslinkable product is provided, wherein said product comprising said silane-crosslinkable, polyolefin composition as defined above including said further preferred subgroups thereof, is crosslinked in the presence of a silane-crosslinking agent, preferably a silanol crosslinking agent, more preferably said crosslinking agent of formula (II), as defined above.
  • a silane-crosslinking agent preferably a silanol crosslinking agent, more preferably said crosslinking agent of formula (II), as defined above.
  • a process for crosslinking said silane-crosslinkable cable as defined above and under "1.1 Cable” including said further preferred subgroups thereof, and preferably obtainable by cable preparation process as defined under, wherein said process comprises a step of silane-crosslinking said silane-crosslinkable polyolefin composition, as defined above including said further preferred subgroups thereof, which is present in said one or more layers of said silane-crosslinkable cable, in the presence of a silane-crosslinking agent, preferably a silanol condensation catalyst as defined above, and water.
  • Preferred process for crosslinking is a process for crosslinking said silane-crosslinkable semiconductive cable as defined above under "1.1. Cable” and “Preparation of said 1.1. Cable”.
  • Said Crosslinking step of the invention can be carried out in a manner known in the art for silane-crosslinking of cable layers using e.g. a conventional silane-crosslinking equipment, e.g. a water or a steam bath.
  • a conventional silane-crosslinking equipment e.g. a water or a steam bath.
  • silane-crosslinking is carried out in elevated temperatures, preferably in a temperature of below 100 0 C, more preferably of from 60 to 8O 0 C, as defined above.
  • the cable silane-crosslinking agent is typically provided by the insulation layer, if present and preferably the insulation layer is present, wherein the silane-crosslinking agent is present in said insulation layer in an amount of from 0.0001 to 6.0 wt%, preferably of from 0.001 to 2.0 wt%, more preferably of from 0.02 to 0.5 wt%, based on the amount of the insulation layer material.
  • the invention also provides said silane-crosslinked cable comprising at least one layer comprising said silane-crosslinked polyolefin composition, as defined above including said further preferred subgroups thereof.
  • said silane- crosslinked cable is a silane-crosslinked semiconductive cable surrounded by at least one semiconductive layer comprising said silane-crosslinked polyolefin composition of the invention which comprises said silane-crosslinked silane-grafted polymer component (i), as defined above, preferably under "1.1 Cable", including said further preferred subgroups thereof, and is preferably obtainable by said crosslinking process of the invention as defined above under this title. Determination methods
  • MFR 2 was determined for ethylene homo- and copolymers and for polyolefin composition according to ISO 1133 at 19O 0 C using 2.16 kg load and for propylene homo- and copolymers according to ISO 1133 at 23O 0 C, 2.16 kg load.
  • MFR 2 i for polyethylene according to ISOl 133 at 190 0 C at a load of 21.6 kg
  • Xylene cold solubles were determined for propylene homo- and copolymers at 23 0 C according ISO 6427. Xylene solubles are defined as the percent by weight that stays in solution after the polymer sample is dissolved in hot xylene and the solution is allowed to cool to 23 0 C.
  • - WVTR Water vapour transmission rate was measured at 90 % relative humidity and 38 0 C temperature according to the method ASTM E96.
  • - Volume resistivity The volume resistivity of the semiconductive material is measured on crosslinked polyethylene cables according to ISO 3915 (1981). Cable specimens having a length of 13.5 cm are conditioned at 1 atm and 60 ⁇ 2°C for 5 ⁇ 0.5 hours before measurement. The resistance of the outer semiconductive layer is measured using a four- terminal system using metal wires pressed against the semiconductive layer. To measure the resistance of the inner semiconductive layer, it is necessary to cut the cable in two halves, removing the metallic conductor. The resistance between the conductive silver paste applied onto the specimen ends is then used to determine the volume resistivity of the inner semiconductive layer.
  • Iodine number of the carbon black samples was measured in accordance with ASTM D1510-07.
  • Tm melting temperature
  • Tcr crystallization temperature
  • degree of crystallinity The melting temperature Tm of the used polymers was measured in accordance with ASTM D3418. Tm and Tcr were measured with Mettler TA820 differential scanning calorimetry (DSC) on 3 ⁇ 0.5 mg samples. Both crystallization and melting curves were obtained during 10°C/min cooling and heating scans between -10 to 200 0 C. Melting and crystallization temperatures were taken as the peaks of endotherms and exotherms. The degree of crystallinity was calculated by comparison with heat of fusion of a perfectly crystalline polymer of the same polymer type, e.g. for polyethylene, 290 J/g.
  • comonomer content The comonomer content(s) of polymer component (i), such as polar comonomer contents of polymer component (i), were calculated based on the polymer component (i) content, and the comonomer content(s) of polyolefln component (ii) were calculated based on the polyolefin component (ii) content, as evident for a skilled person.
  • the silane content was determined based on the combined amount of polymer component (i) and polyolefin component (ii) as described in the description using the below methodology.
  • Si-atom content was analysed by wavelength dispersive XRF (AXS S4 Pioneer Sequential X-ray Spectrometer supplied by Bruker).
  • the pellet sample was pressed to a 3 mm thick plaque (150 0 C for 2 minutes, under pressure of 5 bar and cooled to room temperature).
  • XRF- method the sample is irradiated by electromagnetic waves with wavelengths 0.01-10 nm.
  • the elements present in the sample will then emit fluorescent X-ray radiation with discrete energies that are characteristic for each element.
  • quantitative analysis can be performed.
  • the quantitative methods are calibrated with compounds with known concentrations of the element of interest e.g. prepared in a Brabender compounder.
  • the XRF results show the total content (wt%) of Si and are then calculated and expressed herein as MoI %-Content of functional silane-moieties (Si(Y)3_ q ).
  • Comonomer content (wt%) of the polar comonomer was determined in a known manner based on Fourier transform infrared spectroscopy (FTIR) determination calibrated with C-NMR as described in Haslam J, Willis HA, Squirrel DC. Identification and analysis of plastics, 2 n ed. London Iliffe books; 1972. FTIR instrument was a Perkin Elmer 2000, lscann, resolution 4cm " . For determination of the comonomers, films with thickness 0.1 mm were prepared. The peak for the used comonomer was compared to the peak of polyethylene as evident for a skilled person (e.g. the peak for butyl acrylate at 3450 cm " was compared to the peak of polyethylene at 2020 cm “1 ). The weight-% was converted to mol-% by calculation based on the total moles of polymerisable monomers.
  • FTIR Fourier transform infrared spectroscopy
  • the peak height for methyl acrylate at 3457 cm “1 with base point at 3510 cm “1 was compared to the peak height of polyethylene at 2670 cm “ with base point 2450cm " .
  • the peak height for vinyl acetate at 610 cm “1 with base point at 580 cm “1 was compared to the peak height of polyethylene at 2670 cm “1 with base point 2450 cm “1 .
  • the weight-% was converted to mol-% by calculation based on the total moles of polymerisable monomers.
  • NMR Comonomer Content
  • the comonomer content was determined by using C -NMR.
  • the C -NMR spectra were recorded on Bruker 400 MHz spectrometer at 130 0 C from samples dissolved in l,2,4-trichlorobenzene/benzene-d6 (90/10 w/w).
  • the relevant peak for content determination is taken according to the compound or comonomer under measurement as known and within the skills of the skilled person.
  • polyolef ⁇ n component (ii) such as ethylene content in random copolymer of propylene of up to 5 wt, e.g. 3.0-4.0 wt%
  • the following determination can be used: Content (wt% and mol%) of C2 in polyolefin, such as polypropylene, component (ii): C2 content (wt%) of the polyolefin component was determined in a known manner based on Fourier transform infrared spectroscopy (FTIR) determination calibrated with C- NMR as described in Haslam J, Willis HA, Squirrel DC. Identification and analysis of plastics, 2 n ed. London Iliffe books; 1972.
  • FTIR Fourier transform infrared spectroscopy
  • FTIR instrument was a Perkin Elmer 2000, 2 scans, resolution 4 cm “1 .
  • the peak for C2 was compared to the peak of polypropylene as evident for a skilled person.
  • films with thickness 0.3-0.5 mm were prepared.
  • the peak area for C2 at 730 cm “ with base line at 760-700 cm " was compared to the peak height of polypropylene at 4323 cm “1 with base point at 4700 cm “1 .
  • the weight-% was converted to mol-% by calculation based on the total moles of polymerisable monomers.
  • C2 content Olefin content, e.g. alpha-olefin content, such as ethylene or butene Content (NMR):
  • NMR butene Content
  • the C2 or C4 content was determined by using 13 C -NMR and relevant peaks for C2 or, respectively, for C4.
  • the 13 C -NMR spectra were recorded on Bruker 400 MHz spectrometer at 130 0 C from samples dissolved in 1,2,4- trichlorobenzene/benzene-d6 (90/10 w/w).
  • NMR -method would give comparable results to above FTIR method for C2 content determination from polyolefin, such as polypropylene, component (ii).
  • Gel content (wt%) is measured according to ASTM D2765-90 using a sample consisting of said silane-crosslinked polyolefin composition of the invention.
  • - Hot set elongation (%) To determine that the different layers in the cable constructions are properly cured the hot set elongation and permanent set are determined according to IEC 60811 -2-1 , by measuring thermal deformation at 200 0 C and at a load of 0.1 MPa using a cable layer sample consisting of said silane-crosslinked polyolefin composition of the invention. In the preferred embodiment of the invention a load of 0.2 MPa is used.
  • dumb-bell test samples are prepared from a crosslinked cable layer consisting of a polyolefin composition to be tested by cutting a 1.0 mm thick layer sample from the test cable layer in the direction along the cable axis. The other dimensions were according to said standard.
  • the test layer sample is taken from the outer semiconductive layer of the test cable by peeling said outer layer having a layer thickness of 1.0 mm from the insulation layer.
  • Each test sample is fixed vertically from upper end thereof in the oven and the load of 0.1 MPa or, preferably, 0.2 MPa are attached to the lower end of each test layer sample.
  • the distance between the premarked lines is measured and the percentage hot set elongation calculated, elongation %.
  • the tensile force weight is removed from the test samples and after recovered in 200 0 C for 5 minutes and then let to cool in room temperature to ambient temperature. The permanent set % is calculated from the distance between the marked lines.
  • the peeling was carried out using a peeling angle of 90° and peeling speed of 500 mm/min.
  • the force required to peel said outer semiconductive layer from the insulation is recorded and the test was repeated at least ten times for each test layer sample.
  • the average force divided by the width (10 mm) of th sample was taken as said strip force and the given values represent the average strip force of the test results obtained from said minimum ten tests.
  • test cables of three layer surrounding a conductor and consisting of an inner semiconductive layer, insulating layer and outer semiconductive layer were prepared using the following layer compositions.
  • Test cables consisted of Insulation layer, IL, composition:
  • base polymer conventional copolymer of ethylene and vinyltrimethoxy silane (VTMS)produced in high pressure by radical polymerisation having a density of 923 kg/m 3 , a MFR 2 of 0.9 g/10 min and a silane copolymer content of 1.3 wt.%, and - 5 wt% Master batch (MB) of condensation catalyst:
  • VTMS vinyltrimethoxy silane
  • a matrix resin a conventional ethylene butylacrylate copolymer produced in high pressure by radical polymerisation having a density of
  • a silanol condensation catalyst conventional dibutyl tin dilaurate (DBTL); - 1.7 wt% of stabilizer 1: pentaerythrityl-tetrakis(3-(3',5'-di-ter. butyl-4- hydroxyphenyl)-propionate (CAS-no. 6683-19-8)
  • Pellets of the IL components i.e. base polymer and the MB, were dry blended just before cable extrusion to yield the composition for the insulating layer of a test cable.
  • Inner semiconductive layer, IS composition:
  • LDPE low density polyethylene
  • CBl carbon black
  • EnsacoMS210 - 1 wt% of commercial stabiliser Polymer of 2,2,4-trimethyl-l ,2-dihydroquinoline (CAS- no. 26780-96-1)
  • Preparation, i.e. compounding, of said IS layer composition was done in a conventional manner in a Buss mixer before extrusion to a test cable as described later below under preparation of test cable.
  • Components of the OS composition consisted of the polyolefin composition under test.
  • the test polyolefin compositions used in the present experimental part were polyolefin compositions of inventive examples 1-4 and the polymer compositions of reference examples 1- 2 as listed in tables below.
  • Preparation of OS composition was effected by compounding the components in a Buss mixer.
  • the polymer (i) was grafted during said preparation of the OS composition.
  • the grafting and compounding operations were made in a 46 mm continuous Buss mixer.
  • the polymer (i) and polyolefin (ii), if present, were feeded in the first hopper of the mixer.
  • the initiator and silane compound were injected into the mixer from an injection point which located just after the first hopper.
  • the blend was mixed together and grafted at about 190 0 C.
  • filler (iii) was used like carbon black it was added in the subsequent second hopper together with the additive(s) and the mixing was continued at 190 0 C.
  • test cables were prepared using so called 1 plus 2 extruder set-up, Mailerfer extruder, supplied by Mailerfer. That means that the inner semiconductive layer was extruded on the conductor first in an own head, and then the insulation and outer semiconductive layer are jointly extruded together and on the inner semiconductive in a double extruder head.
  • the inner and outer semiconductive extruder screw had a diameter of 45 mm and the insulation screw had a diameter of 60 mm.
  • test cable When producing the test cable, 1.6 m/min production rate was used for each test cable using the same conventional production conditions.
  • Each test cable had the following properties:
  • the MB was only added to the insulation layer.
  • the catalyst then during crosslinking migrates from the insulation layer out to the semiconductive layer and catalyses the crosslinking reaction.
  • test cables of 30 cm were done in water bath having 90 0 C for 50 hours and then used for experimental testings as described below.
  • the polyolefin composition of the invention has high storage stability.
  • Table 2 shows the superior storge stability obtained with the combination of components of polymer (i) and polyolefin (ii) over the reference.
  • the concept of using the combination of polymer (i) and polyolefin (ii) can be seen from the results of table 2 and table 3.
  • the MFR in these tests was measured from pellets of silane-grafted polyolefin compositions of inventive examples and of reference examples before and after storage according to procedure and storage conditions as defined above in the description part. The pellets are thus as obtained from the PROCESS, i.e. non-crosslinked and do not contain any added crosslinking agent.
  • compositions in table 2 do not contain any filler (iii).
  • compositions in table 3 contain carbon black as said filler(iii).
  • Results show that superior storage stability can be achieved with and without CB, with different types of polyolefin components (ii) and, moreover, using polyolefin compositions with different initial MFR. Moreover, compositions of Inv 1- Inv 6 are easy to process, as indicated by high MFR values, compared to Ref 1.
  • Table 3 Measurements from pellets of silane-grafted polyolefin composition containing filler (iii) of Inv and Ref examples

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Dispersion Chemistry (AREA)
  • Spectroscopy & Molecular Physics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

L'invention concerne des compositions polyoléfiniques fonctionnalisées avec des silanes, des compositions polyoléfiniques réticulables au moyen de silanes et des compositions polyoléfiniques réticulées au moyen de silanes, un procédé de préparation desdites compositions, leur utilisation dans l'élaboration de produits et les produits obtenus, leur utilisation dans les fils & câbles, de préférence pour réaliser une ou plusieurs couches d'un câble comprenant ladite composition polyoléfinique fonctionnalisée avec des silanes, ainsi que des câbles réticulés au moyen de silanes comprenant des compositions polyoléfiniques.
PCT/EP2008/062735 2007-10-31 2008-09-24 Compositions polyoléfiniques fonctionnalisées avec des silanes, produits associés et procédés de préparation associés pour fils & câbles WO2009056407A1 (fr)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2363267A1 (fr) * 2010-03-03 2011-09-07 Borealis AG Composition en polyoléfine réticulable comportant deux types de groupes de silane
EP2580274B1 (fr) * 2010-06-10 2018-10-24 Borealis AG Composition semiconductrice pour enrobage de cable et usage correspondant
WO2018229191A1 (fr) 2017-06-16 2018-12-20 Borealis Ag Composition de polymère pour applications photovoltaïques
WO2018229182A1 (fr) 2017-06-16 2018-12-20 Borealis Ag Composition polymère pour applications photovoltaïques
CN110998752A (zh) * 2017-08-18 2020-04-10 瑞士新集团有限公司 绝缘组合物
WO2023234980A1 (fr) * 2022-05-31 2023-12-07 Dow Global Technologies Llc Procédé de fonctionnalisation par fusion d'hydrure de silicium contenant une polyoléfine et produit

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GB2116986A (en) * 1982-03-18 1983-10-05 Exxon Research Engineering Co Method for producing polymer mouldings
WO1997019965A1 (fr) * 1995-11-30 1997-06-05 The Dow Chemical Company Copolymeres mono-olefines/polyenes, procede de preparation, compositions les contenant et articles realises a partir de ceux-ci
US5948865A (en) * 1996-10-14 1999-09-07 Hitachi Cable, Ltd. Method of manufacturing a crosslinking formed body
WO2002073630A2 (fr) * 2001-03-08 2002-09-19 Union Carbide Chemicals & Plastics Technology Corporation Compositions de blindage semiconductrices
WO2005005532A1 (fr) * 2003-07-10 2005-01-20 Carmel Olefins Ltd. Procede de fabrication de vulcanisats thermoplastiques

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Publication number Priority date Publication date Assignee Title
GB2116986A (en) * 1982-03-18 1983-10-05 Exxon Research Engineering Co Method for producing polymer mouldings
WO1997019965A1 (fr) * 1995-11-30 1997-06-05 The Dow Chemical Company Copolymeres mono-olefines/polyenes, procede de preparation, compositions les contenant et articles realises a partir de ceux-ci
US5948865A (en) * 1996-10-14 1999-09-07 Hitachi Cable, Ltd. Method of manufacturing a crosslinking formed body
WO2002073630A2 (fr) * 2001-03-08 2002-09-19 Union Carbide Chemicals & Plastics Technology Corporation Compositions de blindage semiconductrices
WO2005005532A1 (fr) * 2003-07-10 2005-01-20 Carmel Olefins Ltd. Procede de fabrication de vulcanisats thermoplastiques

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2363267A1 (fr) * 2010-03-03 2011-09-07 Borealis AG Composition en polyoléfine réticulable comportant deux types de groupes de silane
EP2580274B1 (fr) * 2010-06-10 2018-10-24 Borealis AG Composition semiconductrice pour enrobage de cable et usage correspondant
WO2018229191A1 (fr) 2017-06-16 2018-12-20 Borealis Ag Composition de polymère pour applications photovoltaïques
WO2018229182A1 (fr) 2017-06-16 2018-12-20 Borealis Ag Composition polymère pour applications photovoltaïques
US11552210B2 (en) 2017-06-16 2023-01-10 Borealis Ag Polymer composition for photovoltaic applications
CN110998752A (zh) * 2017-08-18 2020-04-10 瑞士新集团有限公司 绝缘组合物
US11795257B2 (en) 2017-08-18 2023-10-24 Si Group, Inc. Insulation composition
CN110998752B (zh) * 2017-08-18 2023-10-27 盛瑞士集团有限责任公司 绝缘组合物
WO2023234980A1 (fr) * 2022-05-31 2023-12-07 Dow Global Technologies Llc Procédé de fonctionnalisation par fusion d'hydrure de silicium contenant une polyoléfine et produit

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