Patent Publication Number: US-2017355175-A1

Title: Layered structure with copper passivator

Description:
FIELD OF INVENTION 
     The present invention relates to a layered structure comprising a copper conductor and a polymer layer adjacent to the copper conductor, more specific to a wire or cable insulation layer that can preserve the copper conductor from discolouration. The polymer layer adjacent to the copper conductor comprises a polymer composition comprising a benzotriazole compound. This prevents discoloration of the copper conductor. 
     BACKGROUND OF INVENTION 
     A typical electrical power cable or wire generally comprises one or more conductors in a cable core, which is surrounded by one or more insulation layers or sheaths of polymeric material. The core typically is copper or aluminium, surrounded by a number of different polymeric layers, each serving a specific function, e.g. semiconducting layer (shielding layer), insulation layer, metallic tape shield layer and polymeric jacket. Each layer can provide more than one function. A low voltage wire or cable are often surrounded by a single polymeric layer that serves as insulating, a metallic shield and polymeric jacketing layer. A medium to extra-high voltage cable may for example be surrounded by a first polymeric semiconducting layer, a polymeric insulating layer, a second polymeric semiconducting layer, a metallic tape shield, and a polymeric jacket. 
     A wide variety of polymeric materials have been utilized as electrical insulating and semiconducting materials for power cables. Such polymeric materials in addition to having suitable dielectric properties must also be enduring and must substantially retain their initial properties for effective and safe performance over many years of service. Such materials have also to meet stringent safety requirements as laid down in international standards. 
     Power cables typically use stranded copper or aluminium conductors, although small power cables may use solid conductors. 
     Despite competition from other materials, copper remains the preferred electrical conductor in many electrical cable constructions with the major exception being overhead electric power transmission where aluminium is often preferred. Copper wire is used in power generation, power transmission, power distribution, telecommunications, electronics circuitry, and countless types of electrical equipment. Electrical wiring is the most important market for the copper industry. This includes building wire, communications cable, power distribution cable, appliance wire, automotive wire and cable, and magnet wire. Roughly half of all copper mined is used to manufacture electrical wire and cable conductors. Many electrical devices rely on copper wiring because of its multitude of inherent beneficial properties, such as its high electrical conductivity, tensile strength, ductility, creep (deformation) resistance, corrosion resistance, low thermal expansion, high thermal conductivity, solderability, and ease of installation. 
     Copper slowly react with atmospheric oxygen to forming a layer of brown-black copper oxide which, unlike the rust which forms when iron is exposed to moist air, protects the underlying copper from more extensive corrosion. A green layer of verdigris (copper carbonate) can often be seen on old copper constructions. Further is copper sensitive to sulphur containing substances that contribute to discoloration as well as fingerprints, since perspiration is corrosive. 
     Discolouration of the copper conductor is a common problem. This impairs the esthetical properties of the copper conductor. When connecting copper conductor are the polymeric layers removed in order to get an undiscoloured part of the copper conductor. Many copper conductors are installed underground in presence of water that increases the discolouration. 
     U.S. Pat. No. 6,262,151 disclose the use of phenolic derivate including a benzotriazole group as UV absorbing agent for polyolefines. 
     Benzotriazole compound (including its derivates) reduce Copper discolouration on the Copper surface. It is sold for that purpose. If benzotriazole compound is applied onto a copper surface it will protect the surface from discolouration. It will form a protective benzotriazole-copper polymeric network. The protective layer will physically protect the copper from discolouration. The copper conductor can easily be scratched and the protective surface of benzotriazole compound be destroyed with a resulting of discoloured surface. This can happen when the cable insulation is extruded onto the copper conductor or during installation or use of the cable. Commonly are copper passivators e.g. benzotriazole compound added to the copper conductor drawing oil prior to cable extrusion, thereby forming a thin layer of copper passivator on the copper conductor surface. This method does however not lead to a satisfactory protection against copper discolouration when copper conductor comes in contact with moisture after cable extrusion. 
     Benzotriazole compound and its derivate are commonly used in insulation oils for transformators. It works as a corrosion inhibitor and protects the copper. There is a positive correlation between the thickness of the copper passivator layer and the efficiency of preventing corrosion. 
     BRIEF SUMMARY OF INVENTION 
     The invention is a layered structure comprising a copper conductor and a polymer layer adjacent to the copper conductor, wherein the polymer layer comprises a polymer composition comprising a benzotriazole compound. 
     A conductor can carry electricity along its length. It can be a power or signal current. Polymers are defined to have more than at least 1000 repeating units. 
     It has surprisingly been found that a polymer layer, comprising of a polymer composition which comprises the benzotriazole compound, adjacent to a copper conductor, will form a protective layer on the copper conductor and prevent discolouration of the copper conductor. Instead of applying the benzotriazole compound first on the copper conductor surface and thereby risking to scratch or damage the surface during applying the adjacent polymer layer, the benzotriazole compound, which is present in the polymer composition of the invention, surprisingly migrates from the polymer composition to the surface of the copper conductor and forms a protective layer after the copper conductor is covered by the polymer layer comprising the polymer composition comprising the benzotriazole compound. Some unreacted benzotriazole compound will remain in the polymer layer and will migrate when needed. The polymer layer will work as a reservoir for the benzotriazole compound, which prolong the discolouration effect compared to applying it directly onto the copper conductor surface. The protective layer will be self-healing and the polymer layer will work as a reservoir. 
     The benzotriazole is a compound with an active site of benzotriazole. It can be substituted or non-substituted. 
     Polymer layer means that the conductor is partly sheeted or more suitably surrounding the conductor, i.e. the conductor is coated with a polymer layer. The polymer layer can be an insulation layer, a semiconducting layer, a combined insulation and jacketing layer. The decisive is that the polymer layer shall be adjacent to the conductor, i.e. in direct contact. The polymer layer suitably is an insulation layer or a combined insulation and jacketing layer, most suitably only an insulation layer. The insulation layer can be used in many applications that include copper conductors, most suitably in a cable. 
     The layered structure of the invention is suitably a cable or wire, suitably a cable. Accordingly, said cable comprises a copper conductor and a polymer layer adjacent to the copper conductor, wherein the polymer layer comprises a polymer composition comprising the benzotriazole compound. Suitably the polymer layer of the cable is an insulation layer, a semiconducting layer, jacketing layer or a combined insulation and jacketing layer more suitably an insulation layer or a combined insulation and jacketing layer. Most suitably the polymer layer is an insulation layer which is suitably covered with a jacketing layer. 
    
    
     THE DETAILED DESCRIPTION OF THE INVENTION 
     The benzotriazole compound can be substituted or unsubstituted, and is suitably a compound of formula (I) (hereinafter benzotriazole compound): 
     
       
         
         
             
             
         
       
     
     wherein
 
R1 is a hydrogen atom, an alkyl group comprising at least 6 carbon atoms, suitably at least 12 carbon atoms, and suitably less than 100 carbon atoms, more suitably from 12 to 100 carbon atoms, or an alkyl group comprising at least one amine group, and
 
R2 is a hydrogen atom or an alkyl group, suitably a methyl group.
 
     By substituting the benzotriazole compound the balance between exudation and compatibility between the polymer composition and the benzotriazole compound can be controlled. Improved solubility of the benzotriazole compound means that a higher loading of benzotriazole compound can be added into the polymer composition. 
     Examples of commercial benzotriazole compounds are Irgamet 30, Irgamet 39, Irgamet 42, Irgamet BTA, Irgamet BTZ &amp; Irgamet TTZ supplied by Basell. 
     In a further embodiment the benzotriazole compound is substituted with at least one amine. Suitably the benzotriazole compound is Irgamet 39, which is a mixture of 2 isomers: N,N-bis(2-ethylehexyl)-4-methyl-1H-benzotriazol-1-methylammine (CAS no: 80584-90-3) and N,N-bis(2-ethylehexyl)-5-methyl-1H-benzotriazol-1-methylamine (CAS no: 80595-74-0). 
     In one embodiment the amount of benzotriazole compound in the polymer composition is from 50 ppm to 1000 ppm, suitably 50 ppm to 500 ppm or more suitably 100 ppm to 400 ppm. 
     In another embodiment the polymer composition comprise a polyolefin, suitably a polymer of ethylene. The polymer of ethylene is suitably at least 70 wt % or more suitably more than 90 wt % of the polymer composition. The polymer of ethylene suitably has an MFR 2  of 0.1 to 40 g/10 min, suitably 0.5 to 15 g/10 min and most suitably 0.75 to 4 g/10 min. 
     The definition of polymer of ethylene is a polymer with more than 50 wt % of ethylene monomer, suitably more than 90 wt % of ethylene monomer. The polymer of ethylene can further comprise of alfa-olefines and comonomers with vinyl groups and functional groups such as polar comonomers. 
     The polymer of ethylene suitably comprises a comonomer with silane groups containing units that are hydrolysable. 
     Silane groups that are hydrolysable mean that a silanol condensation reaction can form covalent bonds with other silane groups. The silane groups can make covalent bonds with other silane groups of the polymer of ethylene with a comonomer with silane groups containing units and form a network. The network degree can for example be measured by gel content or hot set. 
     The polymer of ethylene with silane groups containing units suitably has silane content of 0.1 to 10 wt %, suitably 1 to 5 wt % 20 and most suitably 1.5 to 3 wt %. 
     The polymer of ethylene with silane groups containing units can be made by several conventional processes. The silane is hydrolysable, i.e. crosslinkable. The hydrolysable silane groups may be introduced into the polymer of ethylene by copolymerisation of e.g. ethylene monomers with silane group containing comonomer(s) or by grafting, i.e. by chemical modification of the polymer of ethylene by addition of silane groups mostly in a radical reaction, as well known in the art. Benefits of copolymerisation are that no polar peroxide residues or unreacted vinyl silanes are present in the final article. This will make the final product more uniform, better consistency and improve quality. Storage stability of the copolymerised ethylene with vinyl triethoxy silane and/or vinyl trimethoxy silane made in a high pressure radical process is greatly improved compared to grafted solutions. Another benefit is less handling liquid vinyl silanes which are flammable and have a strong odour. Further benefits are less scrape, less scorch (premature crosslinking in extruder) and longer production runs (less cleaning of extruders). Copolymerisation is the preferred production process of the polymer of ethylene with silane groups containing units. The amount of silane groups can be decreased compared to grafting. The reason for this is that all silane groups are copolymerised while grafted polymer usually contains unreacted silane with peroxide residues. The polymer of ethylene with silane groups containing units is suitably a low density polymer of ethylene containing silane groups containing units. 
     The polymer of ethylene of the invention is produced by polymerising ethylene suitably with a comonomer with silane groups containing units as defined above in a high pressure (HP) radical polymerisation process using free radical polymerization in the presence of one or more initiator(s) and optionally using a chain transfer agent (CTA) to control the MFR of the polymer. 
     The HP reactor can be e.g. a well-known tubular or autoclave reactor or a mixture thereof, suitably a tubular reactor. The high pressure (HP) polymerisation and the adjustment of process conditions for further tailoring the other properties of the polyolefin depending on the desired end application are well known and described in the literature, and can readily be used by a skilled person. Suitable polymerisation temperatures range up to 400° C., preferably from 80 to 350° C. and pressure from 70 MPa, preferably 100 to 400 MPa, more preferably from 100 to 350 MPa. The high pressure polymerization is generally performed at pressures of 100 to 400 MPa and at temperatures of 80 to 350° C. Such processes are well known and well documented in the literature. 
     The incorporation of the comonomer with silane groups containing units (as well as optional other comonomer(s)) and the control of the comonomer feed to obtain the desired final content of said (hydrolysable) comonomer with silane groups containing units can be carried out in a well-known manner and is within the skills of a skilled person. 
     Further details of the production of ethylene (co)polymers by high pressure radical polymerization can be found i.a. in the Encyclopedia of Polymer Science and Engineering, Vol. 6 (1986), pp 383-410 and Encyclopedia of Materials: Science and Technology, 2001 Elsevier Science Ltd.: “Polyethylene: High-pressure, R. Klimesch, D. Littmann and F.-O. Mähling pp. 7181-7184. 
     The silane groups containing comonomer for copolymerising silane groups or the silane groups containing compound for grafting silane groups to produce polymer of ethylene is suitably a vinyl silane compound represented by the formula: 
       R 1 SiR 2   q Y 3-q   (II) wherein
 
     R 1  is an ethylenically unsaturated hydrocarbyl, hydrocarbyloxy or (meth)acryloxy hydrocarbyl group, each R 2  is independently 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. 
     Special examples of the unsaturated silane compound 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. Most suitable is vinyl triethoxysilane (VTES) or vinyl trimethoxy silane (VTMS). 
     One embodiment of the invention is copolymerising the ethylene monomer with vinyl triethoxy silane or vinyl trimethoxy silane comonomer in a high pressure radical process to produce the copolymer of ethylene with a copolymer with silane groups containing units. 
     The polymer of ethylene with silane groups containing units may contain further comonomer(s) which are other than silane groups containing comonomer. Moreover, the polymer of ethylene with silane groups containing units may contain further polar groups other than silane groups (referred herein as polar groups). In one embodiment the polymer of ethylene with silane groups containing units contains also polar groups, which may be introduced by grafting a polar groups containing compound or by copolymerising a polar groups containing comonomer (herein referred as polar comonomer). In this embodiment, the polymer of ethylene is produced by polymerising ethylene monomer with silane groups containing comonomer and with at least one, suitably one, polar comonomer. 
     In one embodiment the polymer of ethylene with silane groups containing units is selected from a polymer consisting of ethylene monomer, silane groups containing comonomer and one or more, suitably one, polar comonomer. Typical polar comonomers are a) vinyl carboxylate esters, such as vinyl acetate and vinyl pivalate, (b) (meth)acrylates, such as methyl(meth)acrylate, ethyl(meth)acrylate, butyl(meth)acrylate and hydroxyethyl(meth)acrylate, (c) olefinically unsaturated carboxylic acids, such as (meth)acrylic acid, maelic acid and fumaric acid, (d) (meth)acrylic acid derivatives, such as (meth)acrylonitrile and (meth)acrylic amide, and (e) vinyl ethers, such as vinyl methyl ether and vinyl phenyl ether. The polymer of ethylene is produced by a high pressure polymerisation with free radical initiation. 
     Typical polar comonomers can be hydroxyl group(s), alkoxy group(s), carbonyl group(s), carboxyl group(s), ether group(s) or ester group(s), or a mixture thereof, can be used. More suitably, polar comonomer(s) containing carboxyl and/or ester group(s) can be used as said polar comonomer. Still more suitably the polar comonomer(s) is selected from the groups of acrylate(s), methacrylate(s) or acetate(s), or any mixtures thereof. Even more suitably selected from the group of alkyl acrylates, alkyl methacrylates or vinyl acetate, or a mixture thereof. Further preferably, said optional polar comonomers can be selected from C1- to C6-alkyl acrylates, C1- to C6-alkyl methacrylates or vinyl acetate. 
     Especially suitable polar comonomers are vinyl acetate (EVA), methyl (meth)acrylate, (EMA &amp; EMMA), ethyl acrylate (EEA), and/or butyl acrylate (EBA), most suitably from EBA, EMA and EEA. Two or more such olefinically unsaturated compounds may be used in combination. The term “(meth)acrylic acid” is intended to embrace both acrylic acid and methacrylic acid. The copolymer ethylene is produced by a high pressure polymerisation with free radical initiation. 
     In one embodiment of the invention the polymer layer is an insulation layer crosslinked by a condensation reaction of the polymer of ethylene with a comonomer with silane groups containing units. Suitably condensation reaction is catalysed by a condensation reaction catalyst. Typical cables with the insulation layer adjacent to the copper conductor are commonly thin and used in applications exposed to weather and wind. The cables are crosslinked to withstand the demanding environment. A protective self-healing layer of benzotriazole compound is especially suitable for such cables. 
     The condensation reaction catalyst is suitably selected from carboxylates of metals, such as tin, zinc, iron, lead and cobalt; from a titanium compound bearing a group hydrolysable to a Brönsted acid, from organic bases; from inorganic acids; and from organic acids; more suitably from carboxylates of metals, such as tin, zinc, iron, lead and cobalt, from titanium compound bearing a group hydrolysable to a Brönsted acid as defined above or from organic acids. The condensation reaction catalyst is suitably acidic, more suitably a Brönsted acid. In an even more suitable embodiment the condensation reaction catalyst is a sulphonic acid, even more suitable an aromatic organic sulphonic acid, which is an organic sulphonic acid which comprises the structural element: 
       Ar(SO3H) x   (III) wherein
 
     Ar is an aryl group which may be substituted or non-substituted, and if substituted, then suitably with at least one hydrocarbyl group up to 50 carbon atoms, and x is at least 1; or a precursor of the sulphonic acid of formula (III) including an acid anhydride thereof or a sulphonic acid of formula (III) that has been provided with a hydrolysable protective groups, e.g. an acetyl group that is removable by hydrolysis. Such organic sulphonic acids are described e.g. in EP736065, or alternatively, in EP1309631, EP1309632. 
     In one embodiment the condensation reaction catalyst is an aromatic sulphonic acid, more suitably the aromatic organic sulphonic acid of formula (III). Said sulphonic acid of formula (III) as the condensation reaction catalyst may comprise the structural unit according to formula (III) one or several times, e.g. two or three times (as a repeating unit (II)). For example, two structural units according to formula (III) may be linked to each other via a bridging group such as an alkylene group. 
     Suitably the organic aromatic sulphonic acid of formula (III) has from 6 to 200 C-atoms, more suitably from 7 to 100 C-atoms. 
     Suitably x is 1, 2 or 3, and more suitably x is 1 or 2. Most suitably, Ar is a phenyl group, a naphthalene group or an aromatic group comprising three fused rings such as phenantrene and anthracene. 
     Non-limiting examples of the even more suitable sulphonic acid compounds of formula (II) are p-toluene sulphonic acid, 1-naphtalene sulfonic acid, 2-naphtalene sulfonic acid, acetyl p-toluene sulfonate, acetylmethane-sulfonate, dodecyl benzene sulphonic acid, octadecanoyl-methanesulfonate and tetrapropyl benzene sulphonic acid; which each independently can be further substituted. 
     Even more suitable sulphonic acid of formula (III) is substituted, i.e. Ar is an aryl group which is substituted with at least one C1 to C30-hydrocarbyl group. In this more suitable subgroup of the sulphonic acid of formula (III), it is furthermore suitable that Ar is a phenyl group and x is at least one (i.e. phenyl is substituted with at least one —S(═O)2OH), more suitably x is 1, 2 or 3; and more suitably x is 1 or 2 and Ar is phenyl which is substituted with at least one C3-20-hydrocarbyl group. Most suitable sulphonic acid (III) as the condensation reaction catalyst is tetrapropyl benzene sulphonic acid and dodecyl benzene sulphonic acid, more suitably dodecyl benzene sulphonic acid. 
     The amount of the condensation reaction catalyst is typically 0.00001 to 0.1 mol/kg polymer composition suitably 0.0001 to 0.01 mol/kg polymer composition, more suitably 0.0005 to 0.005 mol/kg polymer composition. The choice of the condensation reaction catalyst and the feasible amount thereof depends on the end application and is well within the skills of a skilled person. 
     In one embedment the cable comprising the polymer layer is an insulation layer comprising the polymer composition. The polymer composition is suitably crosslinked by condensation reaction, suitably with a condensation reaction catalyst as in any above described embodiments. The hotset of the crosslinked polymer composition is suitably less than 175% after 7 days ambient condition, RH50, more suitably less than 100%. The hot set is measured as described in in the test methods. One object of the invention is good discolouration properties while maintaining good crosslinking properties, even for acidic condensation reaction catalyst such as sulphonic acids. 
     In one embodiment the condensation reaction is carried out using a condensation reaction catalyst which is acidic, or more suitable sulphonic acid, the amount of benzotriazole compound in the polymer composition is suitably from 50 ppm to 500 ppm in the polymer composition, more suitably 50 ppm to 400 ppm or most suitably 100 ppm to 300 ppm. It is surprising that such good crosslinking properties can be maintained with such high loading of the benzotriazole compound due to its basic nature. 
     The polymer composition may contain further component(s), such as further polymer component(s), like miscible thermoplastic(s); additive(s), such as antioxidant(s), further stabilizer(s), e.g. water treeing retardant(s); lubricant(s), foaming agent(s) or colorant(s); filler(s), such as conductive filler. 
     The total amount of further polymer component(s), if present, is typically up to 30 wt %, suitably up 20 wt %, suitably up 10 wt %, more suitably from 0.5 to 7 wt %, based on the total amount of the polymer composition. 
     The total amount of additive(s), if present, is generally from 0.01 to 10 wt %, suitably from 0.05 to 7 wt %, more suitably from 0.2 to 5 wt %, based on the total amount of the polymer composition. 
     Suitably the polymer composition comprises, suitably consists of, a polyolefin, a benzotriazole compound of formula (I) and optionally, and suitably, further additives. 
     Suitably the benzotriazole compound is added to the polymer composition in a form of a Master Batch (MB), which comprises the benzotriazole compound together with a carrier medium. Alternatively, the benzotriazole compound can be soaked into the polymer composition or in the condensation reaction catalyst master batch. More suitably the benzotriazole compound is added as master batch, since this make dosing more accurate. This reduces the risk of overdosing and consequently reduces risk for impairing crosslinking Suitably the benzotriazole compound is added in the condensation reaction catalyst master batch. 
     In one embodiment of the invention the insulation layer is covered with a jacketing layer. Such layer is a sheeting layer that covers and protects the insulation layer mechanically. The object of such layer are to be tough and resistant to mechanical damage, both short term during installation and long term after installation. 
     Suitably, the cable is a power cable, more suitable the cable is a low voltage (LV) or medium voltage (MV) power cable, most suitably a low voltage power cable. Power cable is defined to be a cable transferring energy operating at any voltage level. LV power cable typically operates at voltages of below 6 kV, typically above 400V. MV power cables operate at higher voltage levels and in different applications than LV cables. A typical MV power cable usually operates at voltages from 6 to 36 kV. LV power cable and in some embodiment medium voltage (MV) power cables comprises an electric conductor which is coated with an insulation layer or a combined insulation and jacketing layer, suitable an insulation layer. Typically MV power cables comprise of a conductor surrounded at least by an inner semiconductive layer, an insulation layer and an outer semiconductive layer, in that order. Suitably the cable insulation is extruded on the copper conductor. 
     The invention further relates to a process for passivating a copper conductor of a cable by migration, wherein the process comprises the steps of producing a cable layer according to any previous embodiments for adding a copper passivator in a cable, suitably an insulation layer. The copper conductor should suitably be cleaned. The polymer composition should be applied directly on copper conductor, suitably by extrusion. The copper passivator migrates from the insulation layer onto the copper conductor. Copper passivator is an additive that prevents the degradation of copper, i.e. discolouration. The passivator is forming a polymeric layer on the surface of and thereby protects the copper from degradation. Suitably the copper passivator is a benzotriazole compound as described in any embodiment above. 
     Test Methods 
     a) Melt Flow Rate 
     The melt flow rate MFR 2  was measured in accordance with ISO 1133 at 190° C. and a load of 2.16 kg for ethylene homo and copolymers. 
     b) Density: The density was measured according to ISO 1183D and ISO1872-2 for sample preparation.
 
c) The content (wt % and mol %) of polar comonomer present in the polymer and the content (wt % and mol %) of silane groups containing units (preferably comonomer) present in the polymer composition (preferably in the polymer):
 
     Quantitative nuclear-magnetic resonance (NMR) spectroscopy was used to quantify the comonomer content of the polymer in the polymer composition. 
     Quantitative 1H NMR spectra recorded in the solution-state using a Bruker Advance III 400 NMR spectrometer operating at 400.15 MHz. All spectra were recorded using a standard broad-band inverse 5 mm probehead at 100° C. using nitrogen gas for all pneumatics. Approximately 200 mg of material was dissolved in 1,2-tetrachloroethane-d2 (TCE-d2) using ditertiarybutylhydroxytoluen (BHT) (CAS 128-37-0) as stabiliser Standard single-pulse excitation was employed utilising a 30 degree pulse, a relaxation delay of 3 s and no sample rotation. A total of 16 transients were acquired per spectra using 2 dummy scans. A total of 32 k data points were collected per FID with a dwell time of 60 μs, which corresponded to a spectral window of approx. 20 ppm. The FID was then zero filled to 64 k data points and an exponential window function applied with 0.3 Hz line-broadening. This setup was chosen primarily for the ability to resolve the quantitative signals resulting from methylacrylate and vinyltrimethylsiloxane copolymerisation when present in the same polymer. 
     Quantitative 1H NMR spectra were processed, integrated and quantitative properties determined using custom spectral analysis automation programs. All chemical shifts were internally referenced to the residual protonated solvent signal at 5.95 ppm. 
     When present characteristic signals resulting from the incorporation of vinylacytate (VA), methyl acrylate (MA), butylacrylate (BA) and vinyltrimethylsiloxane (VTMS), in various comonomer sequences, were observed (Randel189). All comonomer contents calculated with respect to all other monomers present in the polymer. 
     The vinylacytate (VA) incorporation was quantified using the integral of the signal at 4.84 ppm assigned to the *VA sites, accounting for the number of reporting nuclie per comonomer and correcting for the overlap of the OH protons from BHT when present: 
       VA=( I *VA−(IArBHT)/2)/1
 
     The methylacrylate (MA) incorporation was quantified using the integral of the signal at 3.65 ppm assigned to the 1MA sites, accounting for the number of reporting nuclie per comonomer: 
       MA= I 1MA/3 
     The butylacrylate (BA) incorporation was quantified using the integral of the signal at 4.08 ppm assigned to the 4BA sites, accounting for the number of reporting nuclie per comonomer: 
       BA= I 4BA/2 
     The vinyltrimethylsiloxane incorporation was quantified using the integral of the signal at 3.56 ppm assigned to the 1VTMS sites, accounting for the number of reporting nuclei per comonomer: 
       VTMS= I 1VTMS/9 
     Characteristic signals resulting from the additional use of BHT as stabiliser, were observed. The BHT content was quantified using the integral of the signal at 6.93 ppm assigned to the ArBHT sites, accounting for the number of reporting nuclei per molecule: 
       BHT=IArBHT/2 
     The ethylene comonomer content was quantified using the integral of the bulk aliphatic (bulk) signal between 0.00-3.00 ppm. This integral may include the 1VA (3) and αVA (2) sites from isolated vinylacetate incorporation, *MA and αMA sites from isolated methylacrylate incorporation, 1BA (3), 2BA (2), 3BA (2), *BA (1) and αBA (2) sites from isolated butylacrylate incorporation, the *VTMS and αVTMS sites from isolated vinylsilane incorporation and the aliphatic sites from BHT as well as the sites from polyethylene sequences. The total ethylene comonomer content was calculated based on the bulk integral and compensating for the observed comonomer sequences and BHT: 
         E =(¼)*[ I bulk−5*VA−3*MA−10*BA−3*VTMS−21*BHT]
 
     It should be noted that half of the a signals in the bulk signal represent ethylene and not comonomer and that an insignificant error is introduced due to the inability to compensate for the two saturated chain ends (S) without associated branch sites. The total mole fractions of a given monomer (M) in the polymer was calculated as: 
         fM=M /( E +VA+MA+BA+VTMS) 
     The total comonomer incorporation of a given monomer (M) in mole percent was calculated from the mole fractions in the standard manner: 
         M  [mol %]=100* fM    
     The total comonomer incorporation of a given monomer (M) in weight percent (wt %) was calculated from the mole fractions and molecular weight of the monomer (MW) in the standard manner: 
         M  [wt %]=100*( fM *MW)/(( f VA*86.09)+( f MA*86.09)+( f BA*128.17)+( f VTMS*148.23)+((1− f VA− f MA− f BA− f VTMS)*28.05))
 
     Randal189 
     J. Randall, Macromol. Sci., Rev. Macromol. Chem. Phys. 1989, C29, 201. 
     It is evident for a skilled person that the above principle can be adapted similarly to quantify content of any further polar comonomer(s) which is other than MA BA and VA, if within the definition of the polar comonomer as given in the present application, and to quantify content of any further silane groups containing units which is other than VTMS, if within the definition of silane groups containing units as given in the present application, by using the integral of the respective characteristic signal. 
     d) Gel content (wt %): is measured according to ASTM D2765-90 using a sample consisting of said silane-crosslinked polyolefin polymer composition of the invention (Method A, decaline extraction). Ambient condition is 23° C., 50% room humidity (RH). The RH at 50° C. to 100° C. was about 10%, if not otherwise specified.
 
e) Hot set elongation
 
     Tape preparation: the mixtures are extruded at 190° C. Then, cross-linking is performed in a water bath at temperatures of 90° C. for 24 hours. After, the samples are placed in a constant room set up at 23° C. and 50% humidity for 24 h (defined as ambient condition). Then tapes of desired length are cut out. 
     The above described tapes are used to determine the hot set properties. Three dumb-bells samples, taken out along extrusion direction are prepared according to ISO527 5A from the 1.8+/−0.1 mm thick crosslinked tape. The hot set tests are made according to EN60811-2-1 (hot set test) by measuring the thermal deformation. Reference lines are marked 20 mm apart on the dumb-bells. Each test sample is fixed vertically from upper end thereof in the oven and the load of 0.2 MPa is attached to the lower end of each test sample. After 15 min, 200° C. in oven the distance between the pre-marked lines is measured and the percentage hot set elongation calculated, elongation %. For permanent set %, the tensile force (weight) is removed from the test samples and after, recovered in 200° C. for 5 minutes and then let to cool at room temperature. 
     The permanent set % reported in Table 3 is calculated from the distance between the marked lines. The average of the three tests is reported. 
     Materials 
     LE4423, VTMS-ethylene copolymer is made in a high pressure radical process, where ethylene monomers were reacted with vinyl trimethoxy silane (VTMS) amounts so as to yield 1.35 wt % silane content in the copolymer. The MFR 2  is 1 g/10 min. LE4423 is described in EP2562768. 
     CatMB SA, Condensation reaction catalyst master batch with a carrier of low density polymer of ethylene (MFR 2  is 7.5 g/10 min) containing 1.5 wt % dodecyl benzene sulphonic acid as condensation reaction catalyst and 2% Irganox 1010 as stabiliser was dry blended into the silane copolymers. 
     CATMB SB, Condensation reaction catalyst master batch with a carrier of low density polymer of ethylene (MFR 2  is 7.5 g/10 min) containing 4 wt % Nacure CD-2180, supplied by King Industries as condensation reaction catalyst and 2% Irganox 1010 as stabiliser was dry blended into the silane copolymers. 
     CATMB Tin, Condensation reaction catalyst master batch with a carrier of low density polymer of ethylene (MFR 2  is 7.5 g/10 min) containing 3 wt % dioctyl tin dilaurate DOTL as condensation reaction catalyst and 2% Irganox 1010 as stabiliser was dry blended into the silane copolymers. 
     Irgamet 39 supplied by Basell, Cas 80584-90-3 
     
       
         
         
             
             
         
       
     
     Sample Preparation 
     Prior to extrusion the copper conductors were cleaned with a cloth soaked in isopropanol. The appearance of the copper conductor surface was shiny without any defects or discolouration. The insulations were extruded onto stranded copper conductors on a mini cable line using a temperature profile of 150° C./160° C./170° C. and 50 rpm. The diameter of the copper conductor was 5 mm and the insulation layer thickness was 0.7 mm. Furthermore, the copper conductor was preheated to 110° C. prior to extrusion. 
     All examples have 5 wt % of condensation reaction catalyst master batch (CatMB) and 95 wt % of LE4423. The Irgamet 39 was added in the CatMB. The final amount of Irgamet 39 in the polymer composition is indicated in each example. 
     The cables were inspected after treatment in 90° C. waterbath for 24 h by peeling of 5 cm of the insulation. In general there was some discoloration visible after treatment in hot waterbath. After treatment in ambient conditions for 24 h (23° C., 50% RH) there was no sign of discolouration for any of the samples. 
     
       
         
           
               
             
               
                 TABLE 1 
               
             
            
               
                   
               
               
                 Discoloration appearance of copper conductor 
               
            
           
           
               
               
               
            
               
                 Rating 
                 Appearance 
                 Comment 
               
               
                   
               
               
                 1 
                 Dark discolouration 
                 The copper has a dark skin 
               
               
                 2 
                 Clearly discoloured 
               
               
                 3 
                 Slight discolouration 
                 Grey clearly visible skin 
               
               
                   
                   
                 covering most of copper 
               
               
                   
                   
                 conductor 
               
               
                 4 
                 Faint discolouration 
                 Some grey spots 
               
               
                 5 
                 Shiny copper 
                 Nothing 
               
               
                   
               
            
           
         
       
     
     
       
         
           
               
             
               
                 TABLE 2 
               
             
            
               
                   
               
               
                 Copper discolouration on cables after 90° C. waterbath for 24 h 
               
            
           
           
               
               
               
               
            
               
                   
                 Sample 
                 Irgamet 39 content 
                 Rating 
               
               
                   
                   
               
               
                   
                 Naked Wire 
                   
                 5 
               
               
                   
                 LE4423 
                  0 ppm 
                 3 
               
               
                   
                 LE4423 + CATMB Tin 
                 600 ppm 
                 5 
               
               
                   
                 LE4423 + CATMB Tin 
                  0 ppm 
                 3 
               
               
                   
                 LE4423 + CatMB SA 
                  0 ppm 
                 3 
               
               
                   
                 LE4423 + CatMB SB 
                  0 ppm 
                 3 
               
               
                   
                 LE4423 + Cat MB SA 
                 600 ppm 
                 4 
               
               
                   
                 LE4423 + CatMB SB 
                 600 ppm 
                 4 
               
               
                   
                 LE4423 + Cat MB SA 
                 200 ppm 
                 4 
               
               
                   
                 LE4423 + Cat MB SB 
                 200 ppm 
                 4 
               
               
                   
                   
               
            
           
         
       
     
     From Table 2 it can be seen that addition of the copper passivator Irgamet 39 will reduce the copper conductor discolouration after treatment in hot waterbath. The same rating for copper discolouration was obtained both for 200 ppm and 600 ppm total concentration of Irgamet 39 in the insulation. Addition of Irgamet 39 to a tin-catalysed system works very well in terms of reducing copper discolouration. This is due to minor or no interaction between the copper passivator and the tin condensation reaction catalyst. Further is it seen that that Irgamet 39 maintains its copper passivating properties even after addition to a strong acid condensation reaction catalyst, such a sulphonic acid, which will interact with the alkaline copper passivator. 
     
       
         
           
               
             
               
                 TABLE 3 
               
             
            
               
                   
               
               
                 Hotset results on cables with 600 ppm Irgamet 39. 
               
            
           
           
               
               
               
               
               
            
               
                   
                   
                   
                 LE4423 + 
                 LE4423 + 
               
               
                   
                 LE4423 + 
                   
                 Cat MB SA 
                 Cat MB SB 
               
               
                   
                 CatMB 
                 LE4423 + 
                 with 600 ppm 
                 with 600 ppm 
               
               
                 Hotset 
                 SA 
                 CatMB SB 
                 Irgamet 39 
                 Irgamet 39 
               
               
                   
               
               
                 24 h, 90° C. 
                 57% 
                 21% 
                 50% 
                 22% (2 min) 
               
               
                 water-bath 
                   
                   
                   
                 Snap Break 
               
               
                 7 days, 
                 51% 
                 74% 
                 Strain Break 
                 157% 
               
               
                 ambient 
               
               
                 14 days, 
                 55% 
                 61% 
                 Strain Break 
                 73% (2 min) 
               
               
                 ambient 
                   
                   
                   
                 Snap Break 
               
               
                   
               
            
           
         
       
     
     In Table 3 it can be seen that addition of 600 ppm Irgamet 39 to the current condensation reaction catalyst concentration fails to give sufficient crosslinking reactions in ambient conditions. When lowering the concentration of Irgamet 39 to 200 ppm, satisfactory crosslinking is achieved in ambient conditions as is shown in Table 4. 
     
       
         
           
               
             
               
                 TABLE 4 
               
             
            
               
                   
               
               
                 Hotset results on cables. 
               
            
           
           
               
               
               
               
               
            
               
                   
                   
                   
                 LE4423 + 
                 LE4423 + 
               
               
                   
                 LE4423 + 
                   
                 Cat MB SA 
                 Cat MB SB 
               
               
                   
                 CatMB 
                 LE4423 + 
                 with 200 ppm 
                 with 200 ppm 
               
               
                 Hotset 
                 SA 
                 CatMB SB 
                 Irgamet 39 
                 Irgamet 39 
               
               
                   
               
               
                 24 h 90° C. 
                 57% 
                 21% 
                 31% 
                 38% 
               
               
                 waterbath 
               
               
                 7 d ambient 
                 51% 
                 74% 
                 Snap Break 
                 52% (2 min) 
               
               
                   
                   
                   
                   
                 Snap Break 
               
               
                 14 d ambient 
                 55% 
                 61% 
                 Snap Break 
                 63% 
               
               
                 Gel content 
                 72% 
                   
                 70% 
                 77% 
               
               
                 after 24 h 
               
               
                 waterbath 
               
               
                 90° C. 
               
               
                 Gel content 
                 70% 
                   
                 60% 
                 69% 
               
               
                 after 4 weeks 
               
               
                 ambient 
               
               
                   
               
            
           
         
       
     
     To conclude on the ambient crosslinking adding 200 ppm Irgamet 39 to a sulphonic acid based condensation reaction catalyst, also gel content measurements are presented in Table 4. The results clearly show that sufficient crosslinking levels are achieved both after treatment in hot waterbath and ambient conditions. 
     Pellets of Cat MB SA with 4000 ppm Irgamet 39 were sealed in aluminium bag and stored in oven at 50° C. for 7 days. It is evident that the Irgamet 39 has not been migrating to the pellet surfaces, since the pellets are free flowing (no sticky surface). This enables a proper mixing of base-resin pellets and condensation reaction catalyst masterbatch pellets prior to cable extrusion.