Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
  • B29C48/901—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
  • B29C48/903—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies externally
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
  • B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
  • B29C48/901—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
  • B29C48/902—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies internally
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/885—External treatment, e.g. by using air rings for cooling tubular films
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
  • B29C48/904—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article using dry calibration, i.e. no quenching tank, e.g. with water spray for cooling or lubrication
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
  • B29C48/905—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article using wet calibration, i.e. in a quenching tank
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
  • B29C48/907—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article using adjustable calibrators, e.g. the dimensions of the calibrator being changeable
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/911—Cooling
  • B29C48/9115—Cooling of hollow articles
  • B29C48/912—Cooling of hollow articles of tubular films
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/919—Thermal treatment of the stream of extruded material, e.g. cooling using a bath, e.g. extruding into an open bath to coagulate or cool the material

Definitions

• the present invention relates to an apparatus for producing an extruded hollow plastic section in accordance with the preamble of claim 1.
• Such an apparatus for producing an extruded plastic tube is known, for example, from NL 7612518 and NL 1001259.
• the first sealing plug is disposed immediately downstream of the inner mandrel of the die, between the die and the external calibration device, while the second sealing plug is situated downstream of the external cooling device.
• the two sealing plugs together with the extruded tube delimit a cooling water compartment in the inner chamber of the tube.
• a feed line is provided for filling cooling water into said compartment.
• a discharge line and suitable pump means are provided, so that cooling water can be circulated through the cooling water compartment, with the result that the extruded tube is cooled internally.
• the closure obtained by the first sealing plug has to be very reliably liquid-tight , in order to prevent the hot inner mandrel of the die from coming into contact with the cooling water. In practice, such contact leads to considerable disruption or jamming of the extrusion process and may even damage the inner mandrel .
• Another generally accepted advantage of the combination of external and internal cooling of a plastic tube, in particular thick-walled pipe, by comparison with exclusively external cooling, is that the tube coming out of the extruder then quickly acquires a cooled, and hence relatively strong layer, both on the internal circumference and on the external circumference .
• the two cooled layers enclose the warm, soft plastic material between them, thus preventing, or at least counteracting, the possibility of this soft plastic material sagging downwards, resulting in an undesired shape of the tube.
• the extruded mass of plastic material comes out of the die at a speed which is lower than the speed of the tube at the location of the drawing or hauloff machine.
• the wall thickness of the tube decreases and also the diameter of the tube becomes smaller. Since a cold and strong layer is rapidly formed on the inside of the tube if internal cooling is used, this layer will start to become creased as the diameter of the tube is reduced.
• the object of the present invention is to provide an apparatus and a method with which the internal cooling process in the horizontal extrusion of hollow plastic sections can be improved and controlled better, enabling better results to be achieved.
• the present invention provides a apparatus in accordance with the preamble of claim 1 which is charac- terized in that the apparatus defines a path for said extruded plastic section which is such that the compartment which is filled with liquid has a highest point at a predetermined location, and in that the apparatus further comprises vent means for discharging from the liquid filled compartment gas or vapour which collects at the highest point of the said compartment .
• the two sealing plugs bounding said liquid filled compartment are rigidly fixed by suitable attachment means to said inner mandrel of the die, and the rigid assembly of the die and the attached sealing plugs is directed at an incline with respect to the horizontal.
• the external calibration device is vertically offset from the die of the extruder, so that between them an inclined path is formed for the extruded tube and the highest point of the liquid filled compartment can be obtained.
• both the die and the external calibration device can be arranged horizontally as a slight bending of the still soft extruded section is allowable in many cases. It is also envisaged that the die is oriented horizontally and that the two sealing plugs bounding the liquid filled compartment are vertically offset from one another to obtain an inclined path for the extruded section.
• the present invention is based on the insight that, particularly if water is used for internally cooling the extruded plastic section, air bubbles are released from the cooling water when the water heats up as a result of coming into contact with the extruded plastic section which comes out of the extruder at a high temperature.
• the direct contact between the plastic section and the cooling water may also result in the water beginning to boil in certain locations, thus producing steam.
• the air bubbles and the steam accumulate in the top of the inner chamber in the plastic section.
• the plastic section is not in direct contact with the cooling water.
• the cooling of the plastic section is then no longer uniform when viewed in the circumferential direction of the plastic section.
• the present invention provides for the extruded section to be supported and guided by the extrusion apparatus in such a manner that the liquid-filled compartment has a highest point at a predetermined location and that the apparatus has vent means arranged to remove the gas and air bubbles which collect at said location.
• the air bubbles and vapour bubbles rising in the liquid-filled compartment move automatically towards the highest point, where they are discharged through the vent means .
• the measure according to the invention is also advantageous when combined with measuring the wall thickness of the extruded section. It is usual to measure the wall thickness of an extruded section continuously, in order thus to control the gap of the die so as to obtain a wall thickness and shape of the section which are as uniform as possible. It has been found that if internal cooling is used, with a sealing plug which lies inside the plastic section forming the separation between the inner mandrel of the die and a compartment which is filled with cooling medium, it is extremely important that the wall thickness of the section coming out of the die be controlled accurately, in order to ensure the sealing action of the sealing plug. This is the case in particular if the cooling medium is pressurized.
• a liquid-filled compartment in the plastic section to be present at the location of the ultrasonic wall-thickness measuring device, said compartment being formed by a sealing plug upstream and a sealing plug downstream of said measuring device, and for vent means to be provided for discharging from that compartment gas or vapour which accumulates at the highest point of the said compartment .
• the fact that according to the invention the entire compartment is filled with liquid avoids disruption caused by air or vapour which would otherwise be present .
• the present invention also provides for an ultrasonic sound emitted by the wall-thickness measuring device to pass at a location from outside through the wall of the plastic section, resulting in two echoes, and then to propagate through the liquid in the plastic section, after which it again passes through the wall of the plastic section at the diametrically opposite location, resulting in a further two echoes.
• the wall-thickness measuring device can use the four echoes to determine the wall thickness at two locations which are situated diametrically opposite one another.
• Fig. 1 shows a diagrammatic side view, partially in section, of an exemplary embodiment of the apparatus according to the invention.
• Figure 1 shows an extruder 1 with a die 2 for extruding thermoplastic material.
• the die 2 has an inner mandrel 3 and an outer barrel 4, which inner mandrel 3 and outer barrel 4 delimit a die annulus, which the extruded plastic material comes out of in the form of a cylindrical tube 5.
• the device 6 comprises a sleeve (not shown) having an inner diameter corresponding to the desired external diameter of the tube 5.
• Water-feed means 7 are provided on that side of the vacuum calibration device 6 which faces towards the extruder 1, for the purpose of forming a film of water on the outside of the tube 5.
• water-discharge means 8 are disposed between the water-feed means 7 and the die 2, these water-discharge means in the present example taking the form of air-jet nozzles which are directed towards the tube 5 and the vaccum calibration device 6.
• a water-suction device could be provided.
• the vacuum calibration device 6 is arranged displaceably with respect to the die 2 and can be displaced between a position in which it is virtually against the die 2 and a position in which it is situated away from the die 2; the latter position is shown in Figure 1.
• An external cooling device 9 is disposed downstream of the vacuum calibration device 6.
• This external cooling device 9 comprises a plurality of compartments 9a, 9b, 9c, which are situated one behind the other and are filled with cooling water.
• a drawing or hauloff device 10, which engages on the tube 5, is situated downstream of the external cooling device 9.
• Figure 1 furthermore diagrammatically shows an internal cooling device for internally cooling the extruded tube 5.
• the internal cooling device comprises a first sealing plug 12, which is fixed to the inner mandrel 3 of the die 2.
• the first sealing plug 12 lies in the inner chamber of the tube 5 and forms an absolutely liquid-tight seal against the interior surface of the tube 5.
• the internal cooling device furthermore comprises a second sealing plug 13 and a third sealing plug 14. These sealing plugs 13, 14 also form a liquid-tight seal against the interior surface of the tube 5.
• the second sealing plug 13 is preferably designed as described in NL 1001259.
• the third sealing plug 14 is provided with flexible sealing lips engaging on the tube 5.
• the second and third sealing plugs 13, 14 are arranged on a rigid tubular attachment element which lies in the centre of the tube 5, thus forming therewith an elongate and rigid internal cooling member 15 which can be manipulated as a single unit .
• the inner mandrel 3 and the internal cooling member 15 are provided with interacting coupling means e.g a bajonet or screw-thread connection (not shown) , so that the internal cooling member 15 can be attached releaseably to the inner mandrel 3.
• These coupling means are preferably designed in such a way that the internal cooling member 15 can be attached to the inner mandrel 3 by waiting, after starting the extruder 1, until the extrusion process has become stable, then cutting off the tube 5 downstream of the drawing device 10, then pushing the internal cooling member 15 into the tube 5 and subsequently fixing it to the inner mandrel 3.
• the first sealing plug 12 and the second sealing plug 13 lie at a distance axially spaced from one another, when seen in the direction of extrusion, and delimit a first compartment 20 in the inner chamber of the tube 5.
• the second sealing plug 13 and the third sealing plug 14 lie at a distance from one another, when seen in the direction of extrusion, and delimit a second compartment 21 in the inner chamber of the tube 5.
• a set of feed lines and discharge lines for cooling water which are respectively indicated by reference numerals 22a, 22b and 23a, 23b, are present for each of the compartments 20, 21.
• These lines 22a, 22b, 23a, 23b run, via the central tube of the internal cooling member 15, through the inner mandrel 3 of the extruder 1 and are connected to a pump device (not shown) and possibly to a heat exchanger.
• a pump device not shown
• each of the compartments 20, 21 can be filled with cooling water and cooling water can be circulated through each of the compartments 20, 21.
• the die 2, the vacuum calibration device 6, the external cooling device 9, and the internal cooling member 15, which is connected to the inner mandrel 3 of the die 2, are disposed at a slight angle with respect to the horizontal, directed downwards when seen in the direction of extrusion.
• This inclined arrangement means that the compartments 20, 21, which are filled with cooling water, each have a single highest point, which is denoted respectively by A and B in Figure 1, at a predetermined location, in this case close to the sealing plug, respectively 12, 13, which delimits each compartment 20, 21 at the upstream end thereof.
• the apparatus further comprises a vent pipe, respectively 27, 28, with an inlet opening very close to the interior surface of the wall of the tube 5 at the highest point A, B of the compartment 20, 21 in question.
• the gas or vapour which accumulates at the highest point A, B of respectively the compartment 20, 21 can be discharged to the outside via the corresponding vent pipe 27, 28.
• each of the vent pipes 27, 28 is provided with a valve for opening and closing the vent pipe 27, 28. The valve can be actuated on command, but may also operate automatically, so that the valve opens as soon as a specific quantity of gas and vapour have accumulated at the highest point .
• the angle of inclination of the path followed by the tube 5 as it passes each of the compartments 20, 21 only has to be small in order to achieve the effect described above and obtain a highest point at a predetermined location somewhere between the sealing plugs. In practice, it is advantageous if the angle is less than 5%, and a value which is advantageous in practice is approximately 1% (1 centimetre per metre) . It is not necessary for the entire extrusion apparatus, i.e. including, for example, the drawing device 10, to be at an angle to the horizontal in order for each liquid-filled compartment 20, 21 in the tube 5 to have a highest point. This is because it is also possible to allow the tube 5 to run inclined to the horizontal over part of the length of the apparatus, while the tube 5 runs precisely horizontally further on in the apparatus. This is because the tube 5 is still sufficiently LO LO t t H H
• the wall-thickness measuring device 30 is designed to recognize these four echoes, and one head can then be used to determine the wall thickness of the tube 5 at two diametrically opposite locations.
• the central attachement body of the internal cooling member 15 should have a small cross-section.
• the wall-thickness measuring device 30 may have one single transmitting-and-receiving head, which continuously rotates through 360° around the tube 5, or it may have a plurality of heads, for example four heads which are distributed around the circumference of the tube 5 and each perform a reciprocating movement of 90°. If the diameter of the tube 5 is small, provision may be made to arrange the transmitting-and-receiving heads one behind the other, when seen in the direction of extrusion.
• the internal cooling device 15 is designed to circulate cooling liquid in the compartment 21 at a lower temperature than in the compartment 20, which is situated closer to the extruder 1.
• the internal cooling member 15 comprises a fourth sealing plug 40 at a distance downstream of the sealing plug 14 which delimits compartment 21 for cooling water, which fourth sealing plug 40, together with the sealing plug 14, delimits a liquid-suction compartment 41.
• the internal cooling member 15 is provided with a line 42, via which line 42 cooling water which has managed to pass by the third sealing plug 14 can be sucked out.
• the line 42 has a suction opening close to the lowest point of the compartment 41.
• the first sealing plug 12 is situated just downstream of the inner mandrel 3, to which it is attached with the interposition of a thermal insulation member 45, in particular a ring of plastic material, such as Polytetrafluorethylene .
• the first sealing plug 12 has a dimensionally stable sealing surface 46, which during operation of the apparatus bears in a sealing manner against the inside of the extruded tube 5.
• the annular sealing surface 46 is made of metal.
• the sealing surface 46 is kept at a low temperature.
• separate cooling means (not shown) are provided.
• the sealing surface 46 may be provided with one or more peripheral grooves which are connected to a vacuum pump, in order to ensure that the tube 5 bears firmly against the sealing surface 46.
• the extruder 1 is set in operation, with the result that the tube 5 made of thermoplastic material is pushed outwards from the die 2. It should be noted here that it is sometimes desirable during the start-up procedure of an extrusion process for producing plastic tubular sections to use a different plastic material from the plastic which is intended to be used ultimately, this "start-up material" having a better stability at high temperatures.

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• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• Physics & Mathematics (AREA)
• Thermal Sciences (AREA)
• Extrusion Moulding Of Plastics Or The Like (AREA)
• Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
• Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
• Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
• Casting Or Compression Moulding Of Plastics Or The Like (AREA)

Priority Applications (11)

Applications Claiming Priority (2)

Related Child Applications (1)

Publications (1)

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Family Applications (1)

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Cited By (8)

Families Citing this family (10)

Citations (4)

Family Cites Families (6)

• 1997
  • 1997-02-14 NL NL1005282A patent/NL1005282C2/nl not_active IP Right Cessation
• 1998
  • 1998-02-06 NZ NZ337074A patent/NZ337074A/xx not_active IP Right Cessation
  • 1998-02-06 WO PCT/NL1998/000073 patent/WO1998035814A1/en not_active Ceased
  • 1998-02-06 DE DE69808102T patent/DE69808102T2/de not_active Expired - Fee Related
  • 1998-02-06 PL PL98335133A patent/PL185674B1/pl not_active IP Right Cessation
  • 1998-02-06 AU AU58854/98A patent/AU732297B2/en not_active Ceased
  • 1998-02-06 BR BR9807681A patent/BR9807681A/pt not_active IP Right Cessation
  • 1998-02-06 CA CA002280810A patent/CA2280810C/en not_active Expired - Lifetime
  • 1998-02-06 EP EP98902295A patent/EP1007324B1/en not_active Expired - Lifetime
  • 1998-02-06 ES ES98902295T patent/ES2184229T3/es not_active Expired - Lifetime
  • 1998-02-06 PT PT98902295T patent/PT1007324E/pt unknown
  • 1998-02-06 AT AT98902295T patent/ATE224289T1/de not_active IP Right Cessation
  • 1998-02-06 JP JP53560798A patent/JP4110542B2/ja not_active Expired - Fee Related
• 1999
  • 1999-08-04 US US09/366,956 patent/US6368547B1/en not_active Expired - Lifetime
  • 1999-08-11 NO NO993862A patent/NO993862L/no not_active Application Discontinuation

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