USE OF CROSS-LINKED POLYOLEFINS MATERIAL IN PRESSURE PIPES

Abstract: Use of at least partly cross-linked polyolefin plastic, which is oriented biaxially, as material for pressure pipes, is described. The pressure pipe is produced by extrusion with subsequent axial and peripheral orientation of the pipe, the pipe being at least partly cross-linked before the biaxial orientation. Preferably, the pipe is cross-linked to about 20-50 % before orientation. By the at least partial cross-linking before orientation, this can be carried out at temperatures above the crystalline melting point of the plastic material.

Description: USE OF CROSS-LINKED POLYOLEFINS MATERIAL IN PRESSURE PIPES The present invention relates to use of at least partly cross-linked, biaxially oriented polyolefin plastic as material for pressure pipes. By pressure pipe is meant a pipe which, when used, is subjected to a positive pressure, i.e. the pressure side or outside the pipe is higher than the pressure outside and inside the pipe, respectively. Nowadays, pipes of polymer material are frequently used for various purposes, such as fluid transport, i.e. transport of liquid or gas, e.g. water or natural gas, during which the fluid can be pressurised. Moreover, the transported fluid may have varying temperatures, usually not outside the temperature range from about -40°C to about 100°C. Such pipes are now preferably made of poly- olefm plastic, such as ethylene plastic (HDPE, MDPE) , or of polyvinyl chloride (PVC) or alternatively of other materials that are not necessarily based on polymer. It is known that the physical and mechanical proper¬ ties of many polymer materials can be improved by onent- mg the material and its structure. It is also known that the properties which by orientation are improved in the direction of orientation m most cases become lower in a direction perpendicular to the direction of orientation, in many cases on the same level as the properties of an unoriented material or worse. In many cases, it is not satisfactory to have so different properties in two dif¬ ferent directions, and a biaxial orientation of the mate¬ rial may then be applied. The biaxial orientation means that the polymer material is oriented in two directions, perpendicular to one another. By this technique, the physical and mechanical material properties can thus be adapted in the two main directions in dependence on load, requirements as to function, pipe manufacturing process etc. For a pipe construction of the type involved having an internal positive pressure, the load in the pipe wall is, in the normal case, greatest in the circumferential or peripheral direction and lower n the axial direction. In conventional manufacture of plastic pipes by ex¬ trusion, preferably a uniaxial orientation of the polymer material is obtained in the axial direction of the pipe owing to the shear, elongation etc., to which the molten mass of polymer is subjected on its way from the ex- truder, through the nozzle and by calibration and coolmg to a ready-formed pipe in solid state. Thus, pipes manufactured by conventional extrusion usually have better physical and mechanical properties n the axial direction of the pipe compared with its peri- pheral direction, at the same time as the load or tension in the pipe wall is greater in the peripheral direction than in the axial direction. The properties of such conventional plastic pipes are quite sufficient for many purposes, but not satisfac- tory m some cases, for instance in applications requir¬ ing high pressure resistance, i.e. pipes that are sub¬ jected to an internal fluid pressure for a long and/or short period. For such pipes, improved compressive strength is desired. With a view to reducing the restrictions with pres¬ surised plastic pipes, it is known that the physical and mechanical properties can be improved by biaxial orienta¬ tion of the pipe, i.e. the polymer material in the pipe is oriented in two directions which are perpendicular to one another. One of these two directions is the axial direction of orientation, i.e. the direction (direction of extrusion) m which the pipe is manufactured in the normal case, whereas the other direction s the circum¬ ferential or peripheral direction of the pipe. Thanks to biaxial orientation, a plurality of the properties of the pipe can be improved to a considerable extent, and espe- cially the compressive strength, both for shorter and longer periods, should be mentioned. The improved compressive strength means that with corresponding dimensions of the pipe material, it is possible to subject the pipe to higher internal pressure compared with a pipe that is not biaxially oriented. Al¬ ternatively, it is possible to use, w th the same pres- surisation, a smaller thickness of material in a biaxi¬ ally oriented plastic pipe. Other mechanical properties that can be improved by orientation is, for instance, rigidity (modulus of elas¬ ticity) , strength (tensile strength) as well as impact toughness. Increased rigidity and strength result in im¬ provement of the short-term strength of the material. The improved impact toughness means that the pipe is less sensitive to external influence in the form of impacts, i.e. the handling of the pipe is rendered more easy. Im¬ provements of properties can also be achieved, for instance, in the form of improved chemical resistance, improved weather resistance and lower coefficient of thermal expansion. As examples of known methods for biaxial orientation of plastic pipes, reference can be made to an article by W. E. Gloor, "Why biaxially oriented pipe?", Modern Plastics, November I960, pp. 111-114, 212, 214, an article by K. Richard, G Diedrich and E. Gaube, "Strengthened pipes from Ziegler Polythene", Plastics, December 1961, pp. 111-114, and PCT Application WO 93/19924. As mentioned above, plastic pipes are generally manufactured by extrusion, or, to a smaller extent, by injection moulding. A conventional plant for extrusion of plastic pipes comprises an extruder, a nozzle, a cali¬ brating device, cooling equipment, a pulling device, and a device for cutting or for coilmg-up the pipe. By the molten mass of polymer on its way from the extruder through the nozzle and up to calibration, cooling and finished p pe being subjected to shear and elongation etc. in the axial direction of the pipe, an essentially uniaxial orientation of the pipe its axial direction will be obtained. A further reason that contributes to the orientation of the polymer material in the direction of material flow is that the pipe can be subjected to tension in connection with the manufacture. To achieve biaxial orientation, the above-described plant can be supplemented, downstream of the pulling device, with a device for temperature control of the pipe to a temperature that is suitable for biaxial orientation of the pipe, an orienting device, a calibrating device, a cool g device, and a pulling device which supplies the biaxially oriented pipe to a cutting device or coiler. The biaxial orientation can also be carried out direct connection with the first calibration after extru¬ sion, m which case the above-described supplementary equipment succeeds the first calibrating device. The biaxial orientation of the pipe can be carried out m various ways, for instance mechanically by means of an internal mandrel, or by an internal pressurised fluid, such as air or water or the like. A further method is the orienting of the pipe by means of rollers, for in¬ stance by arranging the pipe on a mandrel and rotating the mandrel and the pipe relative to one or more pressure rollers engaging the pipe, or via internally arranged pressure rollers that are rotated relative to the pipe against an externally arranged mould or calibrating device. To sum up, there are several prior art methods for biaxial orientation of plastic pipes, and all these methods can be used in the present invention. For all prior art methods for biaxial orientation of crystalline and uncross-linked plastic materials, such as polyolefin plastic, the orientation must be carried out with a given, restricted temperature range, and the pipe must be cooled withm a limited period of time to prevent the material from quickly returning to an unori¬ ented state (relaxation) . Moreover, the requirements for temperature accuracy m the pipe/pipe wall are great in order to obtain a uniform orientation both along the pipe and in the peripheral direction of the pipe, and to ob¬ tain satisfactory dimensional tolerances for the final product. The upper limit of the restricted temperature range at which the process can be performed is determined by the crystalline melting point (7 m ) of the material, which for instance for HDPE is about 128-135°C. Orientation above this temperature normally causes no increased strength of the material and is usually of no value. The lower limit of the temperature range is deter- mined by the properties of the plastic material when sub¬ jected to a deformation procedure, which occurs, for in¬ stance, in conventional tensile testmg of plastic mate¬ rials. When, for instance, polyethylene is subjected to tensile stress in this manner at low temperatures, in the order of room temperature (about 20°C), the stress-strain curve has a marked maximum even at a low elongation of about 5-20% (see the above-mentioned literature refer¬ ences) . For the case where the orientation procedure of a pipe takes place by utilising an inflation technique with pressurised internal fluid, this means that if a certain tensile stress is exceeded, there occurs a transition from a homogeneous deformation of the material to a local plast cising (flow) of the material involving necking, a locally thinned wall and a behaviour where the pipe is locally inflated like a balloon, either along the entire circumference of the pipe or very locally like a blister the pipe wall as the visual result. The same also applies at higher temperatures, but the marked maximum of the stress-strain curve decreases more and more with increasing temperature so as to finally disappear completely at a temperature ust below the crystalline melting point. When the maximum of the stress-strain curve has disappeared, also the local plasticising is eliminated, and the pipe can expand in an even and uniform manner for accomplishing a biaxial orientation. For other types of orientation procedures which are useable for pipe constructions, temperature and material effects of the equivalent type usually arise, with a local or, alternatively, uniform deformation behaviour. When orienting by means of drawing over a mandrel, the lower limit of the temperature range is in the normal case determined by the fact that the force that is neces¬ sary for the drawing is far too great, and that the pipe relaxes after drawing. Experiments have shown that the temperature range which is restricted by the risk of the local plasticismg behaviour of the material on one hand and the crystalline melting point of the material on the other hand, and within which temperature range the material can be ori¬ ented biaxially, is very narrow and lies between the crystalline melting point (T m ) and about 10°C below that. In practice, the temperature range can be still narrower and, for instance, in the order of one or a few degrees centigrade. To achieve a uniform orientation as mentioned above and satisfactory dimensional tolerances, also the differences in temperature of the pipe material involved should not exceed in the order of one or alternatively a few degrees centigrade. It will be appreciated that it is difficult in ac¬ tual practice to control the temperature of the plastic materials so exactly that it lies in the narrow tempera¬ ture range, within which biaxial orientation is possible, and also so uniformly that the entire plastic material has the same temperature. Such a precise temperature con¬ trol requires complicated and expensive temperature con- trol equipment for adjusting the temperature of the pipe to the desired value. Since plastic as a rule has poor thermal conductiv¬ ity, and plastic pipes frequently have a relatively great wall thickness, which in many cases amounts to about 1/10 of the pipe diameter or more, i.e. about 25 mm or more at a diameter of 250 mm, the above-mentioned, accurate tem¬ perature controllmg process requires considerable time, which results in a time-consuming process and a low pro¬ duction speed. The tension that is required in the pipe wall for achieving the orientation usually has a strong tempera¬ ture dependence in polyolefin plastics, which, according to the method of orientation, can also result in more complicated and expensive equipment for force/tension control . A further drawback the context is that, when the temperature of the pipe has once been adjusted to the correct value and the biaxial orientation has been effected, the temperature of the pipe must be lowered at such a speed as to prevent or minimise a relaxation of the biaxial orientation, i.e. basically as quickly as possible. The demands for a high speed of temperature de¬ crease are thus greater at temperatures close to the orientation temperature than at lower temperatures. With a view to maintaining the orientation, it may for m- stance be necessary to use rapid coolmg processes which utilise direct contact with a coolmg agent of the fluid nitrogen type or the like. It may also be necessary to use both internal and external cooling. With regard to the above-mentioned poor thermal conductivity of plastic materials, it may be difficult m practice to achieve such rapid cooling of the plastic pipe as to maintain the orientation to a sufficient extent. All the above-mentioned drawbacks and limitations mean that a biaxial or peripheral orientation can only take place withm narrow process conditions, by using expensive production equipment and at a low production rate, which has resulted m the method not becoming com¬ mercially interesting on a large scale. The object of the present invention is to reduce or eliminate the above-described drawbacks of pressure pipes made of polyolefin plastic. According to the invention, this is achieved by the pipe being oriented in the axial and peripheral direction, the polyolefin plastic of the pipe being at least partly cross-linked before the pe¬ ripheral orientation. The further features of the invention are apparent from the appended claims. It should be mentioned in this context that it is known, in a completely different field of the technique, to produce a so-called shrink film and a heat-shrinkable sleeve; see e.g. WO 89/07077 and US 3,265,790. When pro¬ ducmg shrink film, the film is stretched for biaxial orientation, and before that the film has been cross- linked to give the film a "mechanical memory", i.e. to make the film, when heated above the orientation tempera- ture, shrink and return to its original size. There is a fundamental difference between the inven¬ tion and shrink film owing to the fact that while the actual purpose of shrink film is as extensive return or shrinkage as possible when later re-heat g the film, no return or shrinkage at all is desired according to the mvention, but mstead an improvement of the pressure resistance. This is also obvious from the fact that according to the invention, it s possible to carry out an subsequent cross-linking order to "lock" the structure. Such subsequent cross-linking is excluded in a shrink film, since this counteracts the desired shrinkage. There being an essential difference between shrink film and the present mvention is also apparent from the fact that although shrink film has been known and used for a very long time, it has not been possible to overcome the above-described drawbacks in biaxial orientation of plastic pressure pipes. Even if there may thus be similarities between the shrink film technique and the invention in respect of the steps involving cross-linking and biaxial orientation, there is no further similarity. Above all, it is not previously known to use the technique of cross-lmking and biaxial orientation when manufacturing pressure pipes of plastic. It should be emphasised that the mvention eliminates an old and very inconvenient problem in the manufacture of pressure pipes of plastic and involves great progress in the art. By using in the biaxial orientation a partly cross- linked polyolefin plastic, the temperature for the peri¬ pheral orientation is limited not by the crystalline melting point (T m ) of the material, but also higher tem- peratures can be used to carry out the orientation. The condition that the temperature range for carrying out the biaxial orientation according to the mvention is consid¬ erably extended in relation to prior art means a great advantage smce at the higher temperatures, less force is necessary to orient the material, i.e. less complicated equipment can be used and the cost for the orientation will be lower. Moreover, the adjustment of the tempera¬ ture of the plastic material for the orientation proce¬ dure need not be as accurate as in prior art technique. This is due to the forces required for the orientation procedure being less temperature-dependent if the degree of cross-linking and temperature levels are selected in a suitable fashion and thus the orientation takes place uniformly the pipe construction, which means that the orientation can be made more rapid and simpler while using less complicated and less expensive equipment. Owing to the cross-lmk g of the material, which con¬ tributes to a locking of the structure, the subsequent coolmg after the biaxial orientation can also be made less critical than in prior art technique. This means that the subsequent coolmg of the material need not be as rapid as before, which in turn implies that the cooling can be made simpler and thus less expensive. As mentioned above, the present invention is limited to polyolefin plastic. By this is meant homopolymers of olefins, preferably alpha-olefins, or copolymers thereof having at least one further, copolymerisable ethyleni¬ cally unsaturated monomer. By copolymers are thus meant also polymers which in addition to ethylene contain two (terpolymers) or several other comonomers. By polyolefin plastic is also meant polymer mixtures, in which the major part, i.e. at least 50% by weight, consists of polyolefin plastic, while the remainder of the polymer mixture consists of another polymer, such as a thermo¬ plastic material. The polyolefin plastic is preferably selected among ethylene plastic, i.e. plastic based on polyethylene or on copolymers of ethylene, in which the ethylene monomer constitutes the greatest part of the mass; propylene plastic, and butene plastic (said plas¬ tics being defined in a manner correspondmg to that of ethylene plastic) . The currently most preferred poly¬ olefin plastic is ethylene plastic and, in particular, ethylene plastic of the MDPE and HDPE type. Such plastics are per se known, and neither they nor their manufacture constitute part of the present invention. It is also per se known to cross-link polyolefin plastics, such as ethylene plastic. Such cross-linking can be accomplished in various ways, such as radiation cross-linking, peroxide cross-linking, cross-linking with cross-linkable groups, ionomer cross-linking, or combina- tions of such procedures. In radiation cross-linking, the cross-linking takes place by the plastic being irradiated with high-energy radiation, such as electron radiation, while in peroxide cross-linking, the cross-linking takes place by the addition of peroxide compounds, such as dicumyl peroxide, which form free radicals. In cross¬ linking with cross-linkable groups, reactive groups are inserted in the plastic, said groups reacting with each other while developing covalent bonds. A special example of such reactive groups is silane groups, which are in¬ serted in the plastic by graft polymerisation or, prefer¬ ably, copolymeπsation and, in the presence of water and a silanol condensation catalyst, are hydrolysed while separating alcohol and forming silanol groups, which then react with each other by a condensation reaction while separating water. In ionomer cross-linking, the plastic contains ionisable groups, which react with polyvalent, ionic cross-linking reagents while developing ionic bonds . The invention is not limited to a special type of cross-linking, but any suitable process which results in cross-linking of the polyolefin plastic can be used. According to the invention, it is important that the plastic pipe is at least partly cross-linked before the biaxial orientation is effected. If the pipe is not cross-linked when the biaxial orientation is performed, this must take place under the same conditions as m prior art, i.e. within the narrow temperature range as indicated above, and no advantages of the invention would be achieved. If, on the other hand, the pipe is cross- linked in the orientation, the cross-linking contributes to the structure of the material that otherwise is mam- tamed by above all the crystals of the material. Owing to the cross-linking, the crystalline melting point of the material thus no longer constitutes a critical upper limit of the orientation, but the orientation can be carried out at temperatures above the crystalline melting point. This means that the temperature range is extended upwards, which results in easier temperature control of the orientation procedure, and also that the material is able to offer less resistance to the orientation, i.e. less force is required for the orientation. The cross- linking also counteracts the local deformation behaviour as mentioned above, exemplified as necking and local inflation of the pipe an orientation procedure based on internal fluid pressure, at temperatures below the crystalline melting point, thereby extending the tem¬ perature range downwards as well. The cross-linking also makes the requirements for accurate temperature control decrease on the one hand above the crystalline melting point when the force required for the orientation pro¬ cedure usually has a smaller temperature dependence and, on the other hand, below the crystalline melting point when the local plasticismg and deformation behaviour as mentioned above is suppressed. The extension of the temperature range, i.e. the increase in temperature above the crystalline melting point and the decrease m temperature below the crystal¬ line melting point, which is possible m the orientation depends on the cross-lmkmg of the plastic material. The extension of the temperature range increases with an in¬ creased degree of cross-linking up to the melting point of the cross-linked plastic material, while the extension of the temperature range above that is relatively mde- pendent of the degree of cross-linking provided that the degree of cross-lmkmg has exceeded a specific level which is dependent on the type of material, the technique of cross-lmkmg etc. The degree of cross-lmkmg is de¬ fmed as the portion of insoluble material m the plastic material (excluding filler, if any) measured by extrac¬ tion with decahydronaphthalene according to the ASTM D 2765 method, except that the extraction with decahydro¬ naphthalene after 6 h is continued one more hour m pure, boiling decahydronaphthalene. Basically, the plastic material can be cross-linked to the highest possible degree of cross-lmkmg of the material during the orien¬ tation, but this may imply that the material becomes more brittle (lower elongation at break) or that it possibly affords undesired high resistance to the orientation. Thus, it is necessary that the material has a certain minimum elongation at break to make it possible to orient the material to the desired level. For this and other reasons, it is preferred that the plastic material is only partly cross-linked in the orientation. A suitable degree of orientation, by which is meant the elongation deformation (elongation/original length) , m the peripheral direction, for achieving relevant im¬ provements of properties for pipe applications, is pre¬ ferably about 25-300%, more preferred 50-200%, and most preferred 75-150%. Therefore the material should have an elongation at break at the temperature of orientation which is at least equal to the selected degree of orien¬ tation. In the axial direction, the same degree of orien¬ tation is normally not required since the load owing to an internal positive pressure is normally lower in the axial direction of the pipe. The axial level of orienta- tion thus is determined such manner that the physical and mechanical properties m the axial direction are not limiting compared with the reinforcement in the periphe¬ ral direction, taking the current case of load and the type of orienting process mto consideration. Before orientation, the plastic material suitably has a degree of cross-linking of at least about 10% and also suitably a degree of cross-lmkmg of at most about 90%. In this range, i.e. about 10-90%, preferably about 20-50% degree of cross-lmkmg, a suitable degree of cross-lmkmg is selected on the one hand on the basis of the appearance of the stress-strain curve in the peri¬ pheral direction and, if applicable, in the axial direc¬ tion, thereby avoiding a marked maximum and, on the other hand, so as to obtain an elongation at break which is sufficient for the orientation procedure. When the plastic pipe has been oriented biaxially, the biaxially oriented structure is "locked" by cooling the pipe. Since the cross-lmkmg contributes to the locking of the structure, the cool g need not be as rapid as accordmg to prior art technique after orienting under equivalent conditions. Thus, the cooling accordmg to the invention can be varied from quick coolmg, for instance by means of a flow of compressed air and water spray, to natural coolmg in air without the different cooling procedures resulting m any noticeable differ¬ ences in terms of reinforcement of the material. In order to obtain a reinforcement of the pipe, it is assumed that the biaxially oriented pipe is prevented from returning completely to the state existing before the orientation procedure. For additional locking of the structure and counteracting any risk of relaxation of the orientation, for instance when heating the plastic pipe, it is espec¬ ially preferred according to the invention to cross-link the pipe additionally after the biaxial orientation. As a rule, the subsequent cross-linking can proceed to the maximum degree of cross-lmkmg of the material involved. Preferably, the subsequent cross-lmkmg results in the pipe being cross-linked to at least the degree of cross- lmkmg stated m DIN 16 892, i.e. for peroxide-cross- linked pipes 75%, for silane-cross-lmked pipes 65%, for radiation-cross-l ked pipes 60%, and for azo-cross- linked pipes 60%. The cross-lmkmg of the plastic pipe thus is begun before the biaxial orientation and suitably after the extrusion of the pipe, preferably immediately before the peripheral orientation. A cross-lmkmg station for accomplishing cross-lmkmg one of the ways previously described thus is arranged between the extruder and the device for peripheral orientation of the pipe. If subsequent cross-linking of the pipe is carried out in order to achieve additional locking of the structure, as is especially preferred n the invention, a subsequent cross-lmkmg station is arranged after the device for peripheral orientation of the pipe and preferably after, or in connection with, the subsequent cool g device. It is emphasised that the cross-linking can also be carried out as a continuous process, in which case the cross-lmkmg is begun before the orientation of the pipe and continues during the actual orientation procedure so as to be completed only after completing the orientation. It should be mentioned in the context that the in¬ ventive method can be carried out as a discontinuous or batchwise method, but preferably is carried out as a con¬ tinuous method. The above stated extension of the temperature range m the biaxial orientation according to the mvention is, as mentioned above, dependent on the degree of cross- linking of the plastic material. The biaxial orientation temperature in the mvention generally amounts to about 20°C below, and about 40°C or more above the crystalline melting point (Tm) of the material. Preferably, the orientation in the invention is carried out withm a temperature range of from about 15°C below Tm and up to about 30°C above Tm, more preferred from about 10°C below Tm and up to about 20°C above Tm, and most preferred from about 5°C below Tm and up to about 10°C above Tm. Orien¬ tation at temperatures above Tm, i.e. about 0-40°C, pre- ferably about 0-30°C, more preferred about 0-20°C, and most preferred about 0-10°C above Tm, constitutes a spe¬ cial aspect of the present invention. In the above description of the mvention it has been assumed that the plastic pipe is homogeneous, i.e. m ts entirety consists of one and the same material. However, it is also possible to apply the invention 1) to composite pipes, i.e. pipes having a multilayer composi¬ tion and consisting of two or more layers of different plastic materials, at least one of the layers being partly cross-linked polyolefin plastic as stated above, and 2) to pipes made of a mixed material, in which the ma part of the material is polyolefin plastic, or al¬ ternatively 3) to combinations of 1) and 2) . With a view to further facilitating the understand- ing of the invention, some Examples follow below, in which all parts relate to weight, unless otherwise stated. It will be appreciated that the Examples are merely intended to elucidate the invention and not to restrict the scope thereof in any way whatever. Example 1 Pipes having an outer diameter of 63 mm and a wall thickness of 12.3 mm were produced in conventional manner from high-density polyethylene (HDPE, density 940- 950 kg/m^) by means of an extruder. By utilising various, known cross-lmkmg methods, the pipes were cross-linked to a different degree of cross-lmkmg, which was deter- mined according to the modified ASTM method D2765, as stated above. The different cross-linking methods are defined in more detail in conjunction with Table 1. After cross-linking, the pipes were oriented biaxially at 140°C by an inflation procedure in the followmg manner: each pipe was mounted in one fixed and one movable pipe coup¬ ling. The pipe was inflated by means of an internal positive pressure against an external supporting pipe of metal. This resulted in peripheral orientation. At the same time, the movable coupling was fed away from the fixed pipe coupling, thereby increasing the length of the pipe. After a certain distance, the movable pipe coupling was stopped. This resulted in both peripheral and axial orientation of the pipe. Immediately after orientation, compressed air of room temperature (25°C) was flushed through the pipe, and an aqueous mist having a tempera¬ ture of 10°C was sprayed over the external supporting pipe. The degree of orientation in the peripheral direc¬ tion of the pipe was 107% and the degree of orientation in the axial direction of the pipe was 18%. The resulting improvement of strength was analysed by tensile testmg at 23°C in the peripheral direction of the pipe (testmg method ASTM D2290) and in the axial direction of the pipe (testmg method ISO 527-2) . The resulting maximum stress on the tensile test curve was noted and the improvement of strength relation to unoriented state was calcu¬ lated. The results are stated in Table 1. Table 1 Resulting improvement of strength Mate- Cross-lmkmg process Degree Peri- Longi¬ rial of cross- pherally tudinally lm .kmg (%) (%) (%) HDPE 0.3% silane di 38 15 -1 HDPE 0.4% silane d. 50 55 13 HDPE 0.23% peroxide < 2 . 30 22 0 HDPE 0.27% peroxide d! 42 35 8 HDPE 0.35% peroxide di 60 108 25 HDPE 50 kGy radiation d! 37 18 -3 HDPE 75 kGy radiation d. 42 37 5 HDPE 105 kGy radiation d! 49 45 10 HDPE 210 kGy radiation d ) 56 132 27 (1) The silane cross-lmkmg and its different degrees of cross-lmkmg were obtained by grafting different amounts of vinyl tπmethoxy silane, VTMS, on the material before extrusion. After extrusion, the pipes were cross-linked in a water bath. (2) The peroxide cross-lmkmg and its different degrees of cross-lmkmg were obtained by addmg to the material different amounts of dicumyl peroxide before extrusion. After extrusion, the pipes were cross-linked in a furnace. (3) The radiation cross-lmkmg and its various degrees of cross-lmkmg were obtained by irradiating the pipes with different doses of beta radiation after extrusion. Example 2 Pipes having an outer diameter of 32 mm and a wall thickness of 5 mm were produced m a manner equivalent to Example 1, but by using an HDPE/ionomer polymer mixture (70% by weight HDPE, density 945 kg/m 3 and 30% by weight ethylene methacrylic acid ionomer, density 930 kg/m 3 ) . The pipes were oriented biaxially in the same way as m Example 1, the orientation in the peripheral direction being 90% and the orientation in the axial direction being 20%. The improvement of strength was analysed by tensile testing at 23°C in the same way as in Example 1 and was measured the peripheral direction to be 35% and in the axial direction to be 6%. Example 3 Test samples of four different pipe materials were examined in respect of power demand in the orientation at different temperatures. The test samples were obtained from the following pipe materials: 1) Test sample of a p pe of uncross-lmked HDPE (density 945 kg/m 3 ) having an outer diameter of 63 mm and a wall thickness of 12.3 mm. 2) Test sample of a pipe of radiation-cross-lmked HDPE having a degree of cross-lmkmg of 49%, measured according to the above-mentioned, modified ASTM method D2765. The outer diameter of the pipe was 63 mm and the wall thickness 12.3 mm. 3) Test sample of a pipe of radiation-cross-linked HDPE having a degree of cross-lmkmg of 56%, measured according to the above-mentioned, modified ASTM method D2765. The outer diameter of the pipe was 63 mm and the wall thickness 12.3 mm. 4) Test sample of a pipe of HDPE/ionomer polymer mixture (70% by weight HDPE, density 945 kg/m 3 , and 30% by weight ethylene methacrylic acid ionomer, density 930 kg/m 3 ) . The outer diameter of the pipe was 63 mm and the wall thickness was 12.3 mm. The test samples were oriented uniaxially by using a tensile testing apparatus and the power demand as a func ¬ tion of the orientation temperature at an orienting speed of about 0.01 s ~ 1 was recorded. Fig. 1 represents the result in the form of the maximum power as a function of the orientation temperature that was noted up to 100% elongation. It should be mentioned that the power scale has been normalised with respect to the properties of the uncross-lmked material at 120°C, i.e. under these condi¬ tions, the power is set to be 1. As appears from Fig. 1, it is possible in cross-lmked polymer materials accord¬ ing to the invention to orient the material at higher temperatures than are possible in uncross-lmked mate¬ rials, and the orientation can besides take place by using a smaller amount of power. As is also evident from Fig. 1, only the cross-linking of the polymer material affects, at a specific deformation speed, the power demand when orienting above the crystalline melting point of the polymer material. Example 4 Test samples were taken from an unoriented pipe of HDPE (density 945 kg/m 3 ) , which had been radiation-cross- linked to a degree of cross-lmkmg of 49%. By means of a tensile testing apparatus, the test samples were oriented uniaxially at 140°C and a speed of orientation of about 0.01 s-l to different degrees of orientation which were 78%, 138% and 222%. An unoriented test sample constituted the reference. The improvement of strength, measured ac¬ cordmg to ISO 527-2, was then determined and the results are shown m Table 2. As can be noted from Fig. 2, low degrees of orientation result in lower yield stress and higher breaking stress. Above a certain degree of orien¬ tation, both yield stress and breaking stress mcrease. Equivalent tests carried out with test samples of the same HDPE but having a degree of cross-linking of 56% indicated a similar behaviour, a degree of orientation of 244% yielding an improvement of strength of 151%. Example 5 Test samples were taken from an unoriented pipe of HDPE (density 945 kg/m 3 ) , which had been radiat on-cross- linked to a degree of cross-lmkmg of 49%. By means of a tensile testmg apparatus, the test samples were oriented uniaxially at different temperatures to a degree of on- entation of 100%, and the resulting improvement of strength was determined (testmg method ISO 527-2) . The speed of orientation was about 0.01 s ~ l. The results are stated in Table 2. As appears from the results in Table 2, the orientation can be carried out with a wide tem¬ perature range. This demonstrates the difference between the invention and the prior art technique, which bi¬ axial orientation of plastic pipes has been carried out withm a very narrow temperature range. Moreover, Table 2 shows that the improvement of strength is relatively independent of the orientation temperature. Table 2 Temperature of orientation (°C) Improvement of strength (' 130 61 140 62 150 63 160 61 170 59 Example 6 Test samples were taken from an uncross-lmked and unoriented pipe of HDPE material (density 945 kg/m 3 ) having an outer diameter of 63 mm and a wall thickness of 12.3 mm. The test samples were designated A and B. The test samples were radiation-cross-lmked to a degree of cross-linking of 55%. By means of a tensile testmg appa¬ ratus, the test samples were then oriented uniaxially at 140°C to a degree of orientation of 120%. The speed of orientation was about 0.01 s ~ l. After orientation, the test samples B were additionally cross-lmked to a total degree of cross-lmkmg of 80%. The length of the test samples before orientation was 50 mm and after orienta¬ tion 110 mm. The shrinkage of the test samples was then determined by placing them on a bed of talc at 140°C for 15 mm., whereupon the length of the test samples was measured. Moreover, the improvement of strength was ana¬ lysed by tensile testing at 23°C according to ISO 527-2, the tensile testing being effected on test samples that had not been tested for shrinkage. The improvement of strength was calculated on the basis of the obtained maximum tensile stress on the stress-strain curve in relation to the oriented material. Table 3 indicates the result of the testing for shrinkage and the improvement of strength. Table 3 Degree Length before Length after Improve- Length after of cross- orientation orientation ment of testing for linking strength shrinkage A 55% 50 mm 110 mm 128% 51 mm B 80% 50 mm 110 mm 127% 109 mm The results m Table 3 indicate the improved dimen¬ sional stability at an increased temperature obtained when using subsequent cross-linking. It should, however, be emphasised that 140°C is not an example of a normal tem¬ perature of use, but is an exceptionally high temperature.

Claims: CLAIMS 1. Use of at least partly cross-lmked polyolefin plastic, which is oriented biaxially, as material for pressure pipes. 2. Use according to claim 1, c h a r a c t e r ¬ i s e d in that the pressure pipe is of a multilayered composition, at least one of the layers being the at least partly cross-l ked polyolefin plastic. 3. Use according to claim 1 or 2, c h a r a c ¬ t e r i s e d that the at least partly cross-l ked polyolefin plastic is selected among ethylene plastic and propylene plastic. 4. Use according to any one of claims 1-3, c h a r a c t e r i s e d in that the polyolefin plastic is completely cross-lmked. 5. Use according to any one of the preceding claims, c h a r a c t e r i s e d m that the polyolefin plastic has been formed mto a pipe, has been temperature- controlled, has been oriented in the axial and peripheral direction and cooled, and that the polyolefin plastic of the pipe has been at least partly cross-lmked before the peripheral orientation. 6. Use according to claim 5, c h a r a c t e r ¬ i s e d in that the peripheral orientation has taken place in a temperature range, the upper limit of which is above the crystalline melting point of the polymer mate¬ rial. 7. Use according to claim 5 or 6, c h a r a c ¬ t e r i s e d in that the polyolefin plastic of the pipe has been additionally cross-linked after the peripheral orientation. 8. Use according to claim 7, c h a r a c t e r - l s e d in that the polyolefin plastic of the pipe has been additionally cross-lmked at a temperature above the crystalline melting point of the polymer material after the peripheral orientation. 9. Use according to any one of the preceding claims, c h a r a c t e r i s e d in that the pressure pipe is intended for transporting a pressurised fluid. 10. Use according to claim 9, c h a r a c t e r ¬ i s e d in that the fluid is water.

Inventors: EK CARL-GUSTAF, HOEJER LARS, EK, CARL-GUSTAF, HOEJER, LARS
Applicants: BOREALIS AS, EK CARL GUSTAF, HOEJER LARS, BOREALIS A/S, EK, CARL-GUSTAF, HOEJER, LARS
Application year: 1996
Main classification: B29D23
IPC codes: B29C55, F16L9