Ethene (co)polymer capable of crosslinking, its preparation and crosslinking

Abstract: In the invention was prepared a crosslinkable ethene (co)polymer by copolymerizing first with ethene an unsaturated monomer containing a first hetero group to an ethene (co)polymer having said first hetero group and then by grafting to the obtained ethene (co)polymer a crosslinking agent having an unsaturated crosslinking group and a second hetero group reacting with said first hetero group. Typical reacting hetero group pairs are hydroxyl and carboxyl groups. By the method ethene (co)polymers are obtained, which are easily crosslinkable and have excellent properties.

Description: The object of the invention is a method for the preparation of an ethene (co)polymer, in which a) the ethene is (co)pollymerized to an ethene (co)polymer, and b) to the ethene (co)polymer is grafted a crosslinking agent. The invention also relates to an ethene (co)polymer capable of crosslinking, to which a crosslinking agent has been grafted and the crosslinking of such an ethene (co)polymer by means of ionizing radiation or peroxide treatment. Polyethene can be crosslinked in many different ways. Most usually peroxide crosslinking, radiation crosslinking or silane crosslinking have been used. The methods differ somewhat from each other. The radiation and peroxide crosslinkings are radical reactions. As a result of radiation or the decomposition of peroxides radicals are formed in the polymer chains. When these are combined covalent bonds are formed between the polymer chains i.e. crosslinks. In the silane crosslinking the silanol groups react with each other and form crosslinks. In peroxide crosslinking the polyethene is first mixed with peroxides and additives, after which the mixture is extruded e.g. to cables or pipes. The crosslinking takes place in molten state after the extrusion in a so-called vulcanizing line, at a temperature of about 300°C, usually in nitrogen atmosphere. The peroxides decompose at high temperature and form radicals, which create radicals into the polymer chains. When the polymer radicals are combined covalent bonds are formed between the molecules. After enough bonds have been created the polymer becomes insoluble. The degree of crosslinking is usually measured by solution extraction according to the ASTM standard D 27265. The radiation crosslinking takes place at room temperature after extrusion, generally in a separate stage. Only amorphous parts of a polymer can be crosslinked by radiation. The radiation affects the crystalline parts of a polymer very scarcely. Accordingly, it is easier to crosslink a low density polyethene than a high density polyethene. Electron accelerators or a gamma radiation source are usually used as a radiation source. The energy of an electron accelerator suitable for crosslinking applications varies from 500 KeV to 10 MeV and the power between 10 and 20 kW. With same radiation energy, the electron radiation has a lower penetration depth than the gamma radiation. For this reason gamma radiation is used for the radiation crosslinking of big bodies. Gamma radiation originates from radioactive isotopes, e.g. ⁶⁰Co or ¹³⁷Cs, or it can be produced by an electron accelerator by conducting the electron spray e.g. to a wolfram electrode, whereby obstracting radiation is formed. The gamma radiation source has in both cases a remarkably lower batch velocity than the electron accelerator. The crosslinking of cables by an electron accelerator usually takes only a couple of seconds. Polyethene can be grafted by vinyl silanes and from this grafted copolymer can immediately or later on be prepared a product. The product can afterwards be crosslinked by water vapor (Monosil and Sioplas technique). This technique is also used for the crosslinking of ethene vinyl silane copolymers. To make the crosslinking more effective a catalysator is usually used, e.g. dibutyl tin dilaurate. The silane crosslinking takes place slowly because the reaction rate depends on the diffusion of the water vapor in the polymer. Accordingly, the silane crosslinking is best suitable for thin-walled products, e.g. low voltage cables. The heat resistance and the maximal operation temperature of polyethene can be improved by crosslinking. At high temperatures, as above the melting point of the crystalline part of polyethene, a non-crosslinked polyethene flows but a crosslinked polymer maintains its form, because the polymer chains cannot move in regard to each other. Accordingly, a crosslinked polyethene body better maintains its form than a non-crosslinked body. Irrespective of the crosslinking method the mechanical strength of the polymer at high temperature will improve. In many applications crosslinking is necessary to make the use of a polyethene possible. A non-crosslinked LDPE (a low density polyethene) can be used continuously at 70°C at the most and momentarily at 90°C. A crosslinked polyethene can be used continuously at a temperature of 90°C and momentarily at even a temperature of 250°C. Certain polyethene types, among others HDPE (high density polyethene) endure heat better than LDPE thanks to a higher density and crystallinity. The crosslinking makes the use of polyethene possible at a wider temperature range which is important in many applications (e.g. the cable and hot waterpipe applications). It is very important to reach a degree of crosslinking high enough in the isolation layers of cables and hotwater pipes so as to have a sufficient heat resistance. According to the ASTM standard D-2765 and measured by solution extraction a degree of crosslinking over 70% is needed for cable and pipe applications [Roberts, B.E. and Verne, S., Plastics and Rubber Processing and Applications 4 (1984), p. 135 to 139]. Crosslinked polyethene can also be used for so-called shrink product applications. The polymer is extruded and crosslinked, after which the product is stretched and cooled. The product cools to the streched form and in heating reverts to the same form as before the streching. In this way shrink film, pipes and joints can be prepared. The shrinking of a non-crosslinked product mainly depends on the orientation the polymer has obtained during the extrusion. The crosslinking makes an easy control of the shrinkage possible and, moreover, the shrinking power of a crosslinked polymer is large compared with that of a non-crosslinked one. The shrink product applications, e.g. the shrink film, bag or various kinds of joints, generally need a lower degree of crosslinking than the cables and the hotwater pipes, usually about 30 to 40%. Crosslinked polyethene can also be utilized in the preparation of cellular plastic. The polyethene, foaming agent and the additives are extruded and crosslinked. The crosslinked polymer is foamed whereby the polymer cools down into extended form. The advantage of a crosslinked polyethene foam is a smaller an more even cell size. If the polymer has a high molecular mass a remarkable improvement of the mechanical properties, e.g. in the toughness, the tear strength and the thermal stability of the polymer, would be achieved. A polymer having a high molecular mass can be easily crosslinked because less crosslinks are needed before the polymer becomes insoluble. An easily crosslinked polyethene thus has a high molecular mass. The processing properties, on the other hand, are decreased decisively, when the molecular mass of the polymer increases. The melt index of polyethene is measured by the ASTM D-1238 standard method at a temperature of 190°C. The melt index illustrates the flowability and thus also the processability and the molecular mass of the polymer. In radiation crosslinking, by the gel dose is meant the radiation dose that is necessary for the forming of at least one crosslink/molecule. By this radiation dose the polymer becomes insoluble, when all the polymer chains have been linked to each other. In practice crosslinking takes place incidentally; thus first only a part of the polymer becomes insoluble and when the radiation dose becomes larger the gel content increases (Bradley, R., Radiation Technology Hand-book, Marcel Dekker Inc. 1984). By copolymerizing ethene and diene polymers can be prepared that contain double bonds. Many crosslinking polyethene qualities and ethene propylene rubbers are copolymers or terpolymers of ethene and dienes. These polymers usually have been prepared by coordination polymerization. h many cases 1,4-hexadiene has been used as the comonomer. Other dienes that have conventionally been used as a comonomer are e.g. 5-methyl-1,4-hexadiene, methyl-1,4-hexadiene, 1,6-octadiene, cyclohexadiene, dicyclopentadiene or 5-ethylidene-2-norbornene (JP 59106946-A, JP 57098534-A, JP 570599333-A). Polymers that contain vinyl, vinylidene or vinylene double bonds crosslink by peroxides as much as 50% better than the corresponding saturated polyethenes. These unsaturated polymer qualities are crosslinked by radiation only a little better than the corresponding saturated polyethene qualities. It is prior known that the crosslinking of polymers can be improved by precipitating them with multifunctional acrylate monomers. Hereby 1 to 10% by weight of mono-, di-, or trifunctional allyl monomers, e.g. tetraethyleneglycol diacrylate (TEGDMA), trimethylolpropylenetrimethacrylate (TMPTMA) or triallylcyanurate (TAC) have been used, e.g. (1544804-B). The problem with a mixture of polyethene and an acrylate monomer is that the dispersion of the polar monomer in a non-polar matrix plastic is difficult. The acrylate or allyl monomers precipitated in polyethene have an aptitude to migrate out of the matrix plastic and accumulate on the surface causing so-called sweating. Because of the sweating the body must be crosslinked as soon as possible after the extrusion. In the crosslinking stage the monomers polymerize to homopolymers of the acrylate or allyl monomer concerned. The monomers that are able to form bonds between the various polymer chains of the matrix plastic are thus located in the boundary of the monomer phase and the matrix plastic. It is also prior known that an acrylate double bond is extremely sensitive to react by means of radiation or peroxide. Most varnishes and paints that harden by ultraviolet light (UV) or electron radiation are based on acrylated epoxy, urethane or polyester oligomers. These oligomers usually contain 3-5 acrylate double bonds. A radiation dose of 10 to 30kGy is enough for the hardening of these oligomers for an almost complete polymerization. Oligomers have a relatively high viscosity, for which reason the paints and varnishes are mixtures of oligomers and monomers. The most commonly used monomers are hexanedioldiacrylate (HDDA), tripropyleneglycoldiacrylate (TMPTA) or N-vinylpyrrolidone (NVP) [Holman, R., UV & EB curing formulations for printing inks, coatings & paints, SITA-Technology 1984]. The aim of the present invention is to provide an ethene (co)polymer whose processing properties in non-crosslinked state correspond to the processing properties of the best ethene (co)polymers. Furthermore, it must be possible to process further and crosslink the hardened non-crosslinked product by means of conventional methods. A further aim of the invention is the preparation of an ethene (co)polymer capable of crosslinking that has as high a reactivity as possible when crosslinked by means of radiation or a peroxide. Also the final crosslinked ethene (co)polymer shall be as usable as possible as to its properties. The above-mentioned aims have now been achieved by a method for the preparation of an ethene (co)polymer capable of crosslinking principally characterized by what is stated in the characterizing clause of claim 1. Thus, it has been realized that in a method of the kind mentioned the ethene must in the first phase a) be copolymerized with an unsaturated comonomer containing a first hetero group to an ethene (co)polymer containing said hetero group. After that, in the second phase i.e. in phase b), said ethene (co)polymer having the first hetero group should be crosslinked by a crosslinking agent having an unsaturated crosslinking group and another hetero group capable of reacting with said first hetero group. By hetero group is here meant an organic or inorganic reactive group having some other atom than carbon or hydrogen. The first hetero group i.e. that of the unsaturated comonomer and the other i.e. that of the crosslinking agent thus form a functional pair of groups that forms the bond connecting the crosslinking agent to the comonomer. Such functional pairs of groups are e.g. the following pairs: acid (or its derivative) epoxy amino epoxy hydroxy epoxy mercapto epoxy hydroxy acid (or its derivative) hydroxy isocyanate amino isocyanate acid isocyanate hydroxy ketene urea isocyanate These groups react with each other and they can belong either to the comonomer or the crosslinking agent. According to one embodiment the hetero group of the monomer is a hydroxyl group and the hetero group of the crosslinking agent is a carboxyl group. When such a classic ester-forming pair is in question the said unsaturated monomer preferably is one according to following formula (I): wherein R is H, alkyl or aryl and x is one of the integers 1 to 10. It is still more preferable that R is H or -CH₃ and x is one of the integers 1 to 4, whereby a suitable unsaturated monomer is e.g. hydroxyethyl(meth)acrylate. When a pair of substances suitable for esterification is concerned the crosslinking agent preferably is in accordance with the following formula (II) wherein R is H, alkyl or aryl and R′ is OH, a halogen or the bridge oxygen of an acid anhydride. A very suitable crosslinking agent is acrylic acid or alkacrylic acid such as methacrylic acid. The invention also relates to an ethene (co)polymer capable of crosslinking, to which has been grafted a crosslinking agent. The ethene (co)polymer according to the invention then contains units of ethene and comonomers to which an unsaturated crosslinking agent has been grafted by means of a reaction between the hetero groups of the comonomer and the crosslinking agent. From the reaction between the hetero group of the comonomer, e.g. a hydroxyl group, and the hetero group of the crosslinking agent, e.g. a carboxyl group, a branch is created, formed by the crosslinking agent in the ethene (co)polymer, the graft preferably having the formula (III) wherein R is H, alkyl or aryl and x is one of the integers 1 to 10. R preferably is H or -CH₃ and x preferably is 1, 2, 3, or 4. The ethene (co)polymer according to the invention is particularly capable of crosslinking when it is being crosslinked by means of ionizing radiation or peroxide treatment. This applies particularly when the unsaturated crosslinking group of the crosslinking agent is an acrylic group. Hereby it is worth using doses of ionizing radiation being of the order 10 to 30kGy, because by such radiation doses the crosslinking is improving remarkably compared with the prior art saturated polyetheneacrylate copolymers or ethenediene copolymers. The above-mentioned hetero groups can naturally change place e.g. so that the acid group is in the polymer chain and it is esterified in connection with the grafting to an unsaturated alcohol. The polymer according to the invention can be used e.g. for the following applications: cable or pipe applications where a high crosslinking rate is required, the material can also be used for shrink product applications and for the production of cellular plastic, the polymer can be used in combination products having already a component degrading easily in Gy radiation e.g. in the coating of paper. The thermal stability of the coating can be improved by radiation crosslinking. Thanks to the good crosslinking ability of the polymer the paper does not degrade when it is radiated. the polymer can be used for objects to be coloured or painted, in which chemical bonds can be created between the polymer and the layer of paint, thus to improve the adhesion, the polymer can also be dispersed in polyolefins (e.g. polypropylene) and crosslinked in connection with mixing, whereby thermoplastic elastomer is obtained, or it can be dispersed in technical plastics (e.g. polyamide), whereby their toughness is improved, the polymer can be used to improve the adhesion e.g. to metals and polar plastics. The following examples are presented for the illustration of the invention: For the clarification of the structure of the esterified polymer a Fourier Transform infrared spectrometer (FTIR) has been used as well as a nuclear magnetic resonance spectrometer (NMR). Moreover, a differential scanning calorymetry (DSC) has been used for the clarification of the melting point and the crystallinity of the polymer. In Figure 1 is presented the degree of crosslinking of example 5, in figure 2 the degree of crosslinking of example 6, in figure 3 the degree of crosslinking of example 7 and in figure 4 are presented the degrees of crosslinking of examples 8, 9, and 10. Example 1 The esterification has been carried out in melt state by a Brabender Plasticorder mixer. As raw material has been used an ethene hydroxyethyl methacrylate copolymer, whose hydroxyethyl methacrylate (HEMA) content is 5% by weight and the melt index 2.4g/10min (Pl, see table 1). The polymer has been esterified by 10% by weight of acrylic acid. The conditions were 180°C, the speed of revolution 50rpm and the residence time 10 minutes. Example 2 It was proceeded as in example 1, but as raw material was used ethene hydroxyethyl methacrylate copolymer whose hydroxyethyl methacrylate content is 8% by weight and melt index 2.5g/10 min (P2, see table 1). Example 3 It was proceeded as in example 1, but as raw material was used ethene hydroxyethyl methacrylate copolymer, whose hydroxyethyl methacrylate content is 7% by weight and melt index 11.6g/10 min (P3, see table 1). Example 4 From the polymer prepared in example 1, a film having the thickness of 0.1mm was prepared by compression moulding. The compression time was 5 min., the temperature 150°C and the pressure 100 bars. Example 5 The sample body was crosslinked by radiation using an Energy Sciences Inc. Electrocurtain Lab-Unit electron accelerator. The sample bodies were radiated with 175keV electrons using radiation doses of 10, 30, 50, and 100kGy at an oxygen content of about 120 to 150ppm, O₂. The degree of crosslinking was measured according to ASTM standard D 2765 except that no antioxidant was used and the extraction time had been extended to 24 hours. The degrees of crosslinking achieved by doses of 0, 10, 30, 50, and 100kGy were 0.4%, 50.4%, 63.4%, 69.5% and 71.6%, see figure 1, in which the reference is a non-esterified P1. Example 6 It was proceeded as in examples 4 and 5, but as material was used the material prepared in example 2. The degrees of crosslinking achieved by doses of 0, 10, 30, 50 ja 100kGy were 2.3%, 60.2%, 67.1%, 69.9% and 75.1%, see figure 2, in which the reference is a non-esterified P2. Example 7 It was proceeded as in examples 4 and 5, but as raw material was used the polymer prepared in example 3. The degrees of crosslinking measured by a dose of 0, 10, 30, 50, and 100kGy were 0.5%, 58.6%, 68.8%, 72.7%, and 74.1%, see figure 3, in which the reference is a non-esterified P3. Example 8 A peroxide crosslinking was carried out by a Brabender Plasticorder mixer using 1% by weight of dicumyl peroxide. The conditions were 180°C, 50rpm and 10 minutes. As the degree of crosslinking of the non-esterified copolymer P1, crosslinked in the same manner, 64.3% was achieved. For the crosslinking degree of a crosslinked, non-esterified copolymer P1 was in the same manner achieved 39.4%. Example 9 It was proceeded as in example 8, except that for the crosslinking was used the polymer prepared in example 2, whereby 68.3% was achieved as the degree of crosslinking. As the degree of crosslinking of the non-esterified copolymer P2 crosslinked in the same manner, was achieved 31,3% (see figure 4). Example 10 It was proceeded as in example 1, but for the crosslinking was used the polymer prepared in example 3, whereby 66.3% was achieved as the degree of crosslinking. As the degree of crosslinking of the non-esterified copolymer P3, crosslinked in the same manner, was achieved 29.1% (see figure 4). The melt indices and HEMA-contents of E-HEMA copolymers Material Melt index (2.16kg) (g/10 min) HEMA (% by weight) P1 2.4 5 P2 2.5 8 P3 11.6 7

Claims: Method for the preparation of a crosslinkable ethene (co)polymer, wherein a) the ethene is (co)polymerized to an ethene (co)polymer, and b) to the ethene (co)polymer is grafted a crosslinking agent, characterized in that the ethene, in stage a) is copolymerized with an unsaturated monomer containing a first hetero group, to an ethene (co)polymer having said first hetero group, and, in stage b) the ethene (co)polymer having said first hetero group is grafted by a crosslinking agent having an unsaturated crosslinking group and a second hetero group reacting in the grafting with the first hetero group. Method according to claim 1, characterized in that the first hetero group is a hydroxyl group. Method according to claim 1 or 2, characterized in that the unsaturated monomer has the following formula (I) in which R is H, alkyl or aryl and x is one of the integers 1 to 10. Method according to claim 3, characterized in that R is H or -CH₃ and x is one of the integers 1, 2, 3 or 4. Method according to claim 4, characterized in that the unsaturated monomer is hydroxyethyl methacrylate. Method according to claims 1 or 2, characterized in that the other hetero group is a carboxyl group or its derivative. Method according to any of the preceding claims, characterized in that the crosslinking agent has the following formula (II): wherein R is H, alkyl or aryl and R′ is OH, halogen or a bridge oxygen of an acid anhydride. Method according to claim 7, characterized in that the crosslinking agent is an acrylic acid or methacrylic acid. A crosslinkable ethene (co)polymer, to which has been grafted a crosslinking agent, characterized in that the ethene (co)polymer has units of ethene and a comonomer to which the unsaturated crosslinking agent has been grafted by means of a reaction between the hetero groups of the comonomer and the crosslinking agent. An ethene (co)polymer according to claim 9, characterized in that the hetero group of the comonomer is a hydroxyl group. An ethene (co)polymer according to claim 9 or 10, characterized in that the hetero group of the crosslinking agent is a carboxyl group. An ethene (co)polymer according to any of the claims 9 to 11, characterized in that the formula of the graft formed by the crosslinking agent to the ethene (co)polymer is (III) in which R is H, alkyl or aryl and x is one of the integers 1 to 10. Ethene (co)polymer according to claim 12, characterized in that R is H or CH₃ and x is 1, 2, 3, or 4. Crosslinking of an ethene (co)polymer according to any of the claims 9 to 13 or prepared by a method according to any of the claims 1 to 8 by means of an ionizing radiation or a peroxide treatment. Crosslinking according to claim 14, characterized in that the doses of the ionizing radiation are of the order 10 to 30kGy.

Inventors: BERGSTROEM CHRISTER, ORA MARJA, SJOESTROEM HAEKAN, TURPEINEN VEIJO, BERGSTROEM, CHRISTER, ORA, MARJA, SJOESTROEM, HAEKAN, TURPEINEN, VEIJO, BERGSTRÖM, Christer, Sjöström, Häkan
Applicants: BOREALIS HOLDING AS, BOREALIS HOLDING A/S
Application year: 1991
Main classification: C08F255
IPC codes: C08F8, C08F290