EP1775376B1 - Method and device for obtaining wood fibers from wood chips - Google Patents

Method and device for obtaining wood fibers from wood chips Download PDF

Info

Publication number
EP1775376B1
EP1775376B1 EP06021281A EP06021281A EP1775376B1 EP 1775376 B1 EP1775376 B1 EP 1775376B1 EP 06021281 A EP06021281 A EP 06021281A EP 06021281 A EP06021281 A EP 06021281A EP 1775376 B1 EP1775376 B1 EP 1775376B1
Authority
EP
European Patent Office
Prior art keywords
wood chips
wood
conductivity
chips
plug
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Not-in-force
Application number
EP06021281A
Other languages
German (de)
French (fr)
Other versions
EP1775376A3 (en
EP1775376A2 (en
Inventor
Wolfgang Dr. Stahl
Klaus Schug
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Glunz AG
Original Assignee
Glunz AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Glunz AG filed Critical Glunz AG
Priority to PL06021281T priority Critical patent/PL1775376T3/en
Publication of EP1775376A2 publication Critical patent/EP1775376A2/en
Publication of EP1775376A3 publication Critical patent/EP1775376A3/en
Application granted granted Critical
Publication of EP1775376B1 publication Critical patent/EP1775376B1/en
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/36Explosive disintegration by sudden pressure reduction
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C7/00Digesters
    • D21C7/06Feeding devices

Definitions

  • the invention relates to a method for recovering wood fibers from wood chips, the wood chips are fed with a plug screw a stove in which they are exposed to elevated pressure and elevated temperature, and wherein the wood chips discharged under rapid release of pressure from the digester and thereby dissolved in the wood fibers. Furthermore, the invention relates to a device for obtaining wood fibers from wood chips with a plug screw, a digester and a discharge device, wherein the plug screw feeds the wood chips to the digester, the wood chips are exposed in the digester elevated pressure and elevated temperature and wherein the discharge device the woodchips discharges from the cooker with rapid release of pressure so that they dissolve into the wood fibers.
  • the pressure in the digester is suddenly relaxed, dismantle the wood chips into the individual wood fibers.
  • These wood fibers are conveyed through a blown duct by a steam stream produced by the expansion in which they can already be glued with binder before they then enter a dryer in which they are adjusted in a stream of dry hot gas to a desired fiber moisture.
  • the enriched by the excess water vapor gas stream is separated in a separator from the wood fibers, from which the wood fibers are then discharged for the formation of a fiber mat.
  • the invention has for its object to provide a method and apparatus of the type described above such that the fiber moisture content of the wood fibers obtained within narrow limits can be kept constant to date, the average fiber moisture content in the production of wood fiber boards without the risk of too high To be able to increase fiber moisture significantly.
  • the conductivity of the wood chips in the region of a plug from the wood chips at the outlet of the screw plug is measured and used as a control parameter for controlling the further processing of wood chips and / or wood fibers.
  • the conductivity of the wood chips represents a measure of the fiber moisture of the wood fibers, which are still related to the individual wood chips.
  • this measure of the fiber moisture content of the wood fibers in the wood chips in the plug from the wood chips at the outlet of the plug screw can be obtained with sufficient accuracy for subsequent use as a control parameter in the control of further processing of wood chips and / or wood fibers it's a relevant statement in terms of the This is especially true when the plug screw in the region of the graft applies a substantially constant pressure on the woodchips or when measured by the plug screw in the region of the graft on the wood chips measured pressure and at the Use of the measured conductivity of the wood chips as a measure of their fiber moisture in terms of calibration is taken into account. At a certain pressure in the region of the graft, the fiber moisture can be determined relatively accurately from the conductivity of the wood chips in the graft.
  • the new process provides meaningful information about the wood fibers in the wood chips, which determine the fiber moisture content of the wood chips despite their extensive treatment until after the woodchips have been dissolved into the individual wood fibers.
  • this crucial starting point for the fiber moisture of the wood fiber obtained very early in the new process it can be used as a control parameter for all subsequent treatments of the woodchips and the wood fibers in order ultimately to achieve a constant fiber moisture content.
  • a feedforward control is realized, with which the fiber moisture content can be kept within narrower limits with fluctuating input parameters than with the feedback control system known from the prior art.
  • the measured conductivity of the wood chips in the area of a plug from the wood chips can also be used in the sense of a feedback control for the control of preceding steps of the treatment of wood chips.
  • the special feature of the present invention is the feedforward control of the further processing of wood chips and / or wood fibers.
  • the conductivity of the wood chips can be used in the new method of controlling a dryer, with which the fiber moisture content of the wood fibers is set, for example, to a desired level for the production of fiberboard.
  • the dryer can continue to be controlled in response to a measured at its output fiber moisture content of the wood fibers, as was previously the case exclusively in the prior art.
  • the pressure applied by the plug screw in the region of the plug to the wood chips is also measured in order to calibrate the measured conductivity with regard to the fiber moisture corresponding thereto, it is of course possible to monitor the sealing function of the screw plug directly by following this pressure.
  • the conductivity of wood chips can be measured in the new method by directly contacting the plug from the woodchips with measuring electrodes.
  • an indirect conductivity measurement is also possible in which the inductive or capacitive properties of the plug, which depend on the conductivity of the wood chips, are recorded.
  • the plug can be part of a dielectric of a capacitor arrangement or part of the core of a coil arrangement whose alternating current resistance changes with each change in the conductivity of the woodchips.
  • the conductivity is determined as for a single direct measurement via measuring electrodes only for a local area of the circumference of the plug, it is preferred that the Conductivity of the wood chips is measured in several peripheral regions of the graft from the wood chips. Even with a constant fiber moisture content of the wood fibers in the wood chips, it is not to be expected that the fiber moisture of interest can be measured as a constant value which is not subject to fluctuations. Rather, the value measured in each case is also dependent on the electrical contacting of the woodchips and structural inhomogeneities of the graft from the woodchips. It therefore makes sense to obtain as many conductivity measurements as possible for the amount of wood chips each forming a graft. The same applies if this is additionally carried out with regard to the measurement of the pressure in the graft.
  • the device according to the invention has at the outlet of the plug screw a conductivity measuring device for measuring the conductivity of the wood chips in the region of a plug from the wood chips.
  • a conductivity measuring device for measuring the conductivity of the wood chips in the region of a plug from the wood chips.
  • the conductivity measuring device is provided for a direct measurement of the conductivity of the wood chips, a housing of the screw plug having at least one transverse bore, which receives a sealed relative to the housing measuring electrode sealingly.
  • the measuring electrode contacts the plug on the inner circumference of the housing. Any abrasion of the housing affects equally on the measuring electrode.
  • the measuring arrangement thus remains always the same despite an unavoidable abrasion on the inner circumference of the housing.
  • the conductivity measuring device can measure the conductivity between the already mentioned measuring electrode and the housing and / or at least one further measuring electrode. It is important to ensure that the current flowing through the measuring arrangement at a certain voltage actually depends essentially on the conductivity of the wood chips.
  • Preference is given to conductivity measuring devices in the new device, which have a plurality of at least three measuring electrodes distributed over the circumference of the screwing plug in order to also detect the homogeneity of the distribution of the fiber moisture over the respective plug from the woodchips.
  • a pressure measuring device For an additional measurement of a pressure applied by the plug screw in the region of the plug on the wood chips, a pressure measuring device may be provided which has at least one, preferably a plurality of pressure sensors distributed over the circumference thereof at the outlet of the screw plug.
  • a stuffing screw 1 is shown in cross section.
  • a screw conveyor 3 runs around an axis 4, so that a screw spiral 5 of the screw conveyor 3 woodchips 6, which are supplied to the plug screw 2 at its inlet 7 and are not shown here individually, promotes to the right and compressed into a compact plug.
  • the plug from the wood chips 6 serves primarily to seal a cooker 9, the wood chips 6 are fed. In the cooker 9 prevails not only an elevated temperature, but also an increased pressure, which should not escape via the plug screw 2 and against the wood chips 6 must be pressed into the stove 9.
  • a counter-pressure body not shown here for the wood chips 6 is provided, which ensures that the desired plug from the wood chips 6 in the plug screw 2 builds up.
  • excess water with which the woodchips 6 can be watered in a storage container 10 is pressed, so that only the water bound in the wood fibers of the woodchips 6 is present in the region of the graft.
  • This water content, ie the moisture content of the wood chips forming the wood chips 6, is measured by a conductivity measuring device 11.
  • the conductivity meter 11 measures the conductivity of the plug of the woodchips 6 between two electrodes 12 and 13 contacting the plug on the inner periphery 17 of the housing 2 at two spaced apart points.
  • the measured conductivity can be used as a control parameter 14 not only for the cooker 9 as shown here but also for all subsequent devices for further processing
  • a long-term observation of the conductivity of the wood chips 6 in the region of the plug can be used to determine to what extent, despite an inevitable wear of the plug screw 1 both on its housing 2 as well as their screw conveyor 3 is still a complete Abpressung the excess and not bound in the wood fibers water from the wood chips. If this pressure is no longer guaranteed, it is time to replace at least the screw conveyor 3, because then the seal of the stove 9 is no longer ensured.
  • Fig. 1 The measuring arrangement of the conductivity measuring device 11 according to Fig. 1 in which two electrodes 12 and 13 sealingly penetrate the housing 2 in the radial direction, it is necessary that at least the associated portion 15 of the housing is made of electrically non-conductive material or is coated electrically insulating on its inner circumference 17, because otherwise the measuring distance between the Electrodes 12 and 13 would be short-circuited by the housing 2 itself.
  • Fig. 2 outlines another training a measuring distance, which as well as the measuring distance in Fig. 1 remains the same at occurring wear of the housing 2, but does not require a portion 15 of the housing 12 of electrically non-conductive material.
  • the electrically conductive housing 2 wherein the electrode 12 is electrically insulated from the housing 2 by a cylinder jacket insulation 16, which together with the electrode 12 a radially extending to the axis 4 transverse bore 30 in the housing 2 seals.
  • a plurality of electrodes 12, which are distributed over the circumference of the housing 2 of the screw conveyor 1, may be connected to the conductivity measuring device 11.
  • the portion 15 of the housing 2, in which the electrodes 12 are arranged consist of electrically non-conductive material or be provided on its inner circumference 17 with an insulating coating, or for each of the electrodes 12, the measuring arrangement according to Fig. 2 be provided.
  • the conductivity measuring device 11 can scan the individual electrodes 12 or the respective electrodes 12 and / or the associated counterelectrodes, which may be other electrodes 12, in parallel or else sequentially.
  • the conductivity measuring device 11 is according to FIG Fig. 3 also connected to pressure sensors 31.
  • the pressure sensors measure a pressure exerted by the screw conveyor 1 on the wood chips in the region of the electrodes to calibrate the measurement of their fiber moisture based on their conductivity to this pressure.
  • the relationship between the electrical conductivity of woodchips and their fiber moisture is pressure dependent. With a determination of the fiber moisture content from the conductivity Therefore, without consideration of the associated pressure, errors are associated which remain small only at a largely constant pressure of the wood chips in the area of the electrodes 12. On the other hand, taking into account the associated pressure, it is possible to deduce from the measured conductivity very precisely the actual fiber moisture content of the wood fibers in the woodchips.
  • Fig. 4 outlines the production of glued wood fibers 18 for the production 19 of wood fiber boards.
  • the woodchips 6 from the cooker 9 according to Fig. 1 discharged with a discharge device 20, in which the pressure in the interior of the digester 9 is abruptly reduced, so that the woodchips 6 dissolve into individual wood fibers.
  • These wood fibers pass through a blowing passage 21 in a dryer 22. Previously, they are sprayed within the blowing passage 21 with binder 23.
  • the moisture of the wood fibers is adjusted by a stream of hot dry gas.
  • the hot dry gas is prepared in a burner 24 by burning fuel gas 25.
  • the control of the burner 24 is indicated here by a valve 26 which adjusts the amount of hot gas 25 supplied to the burner 24.
  • the adjustment of the valve 26 takes place as a function of the control parameter 14, which is derived from the conductivity of the woodchip chips determined by the conductivity measuring device 11.
  • the control parameter 14 is derived from the conductivity of the woodchip chips determined by the conductivity measuring device 11.
  • the running time of the wood fibers is taken into account by the graft from the woodchips, at which the conductivity is measured, until they enter the dryer 22.
  • the wood fibers pass into a separator 27, where they are separated from the gas flow of the dryer 22 and the excess moisture absorbed by this.
  • the fiber moisture content of the glued wood fibers 18 is measured with a measuring device 28, and from this a further control parameter 29 is determined, which is also used to control the dryer 22.

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Dry Formation Of Fiberboard And The Like (AREA)
  • Debarking, Splitting, And Disintegration Of Timber (AREA)
  • Preliminary Treatment Of Fibers (AREA)

Abstract

Making wood fibers from wood chips by feeding the chips through a tamping screw into a boiler, where they are exposed to high pressure and temperature, and discharging the chips under rapid expansion so that they separate into fibers, comprises measuring the conductivity of a plug of chips leaving the screw and using the result as a control parameter for controlling downstream processing of the chips and/or fibers. An independent claim is also included for apparatus for making wood fibers from wood chips, comprising a tamping screw (1) for feeding the wood chips into a boiler, where they are exposed to high pressure and temperature, and a discharge device for discharging the chips under rapid expansion so that they separate into fibers, comprises a sensor (11) for measuring the conductivity of a plug of chips leaving the screw.

Description

Die Erfindung bezieht sich auf ein Verfahren zum Gewinnen von Holzfasern aus Holzhackschnitzeln, wobei die Holzhackschnitzel mit einer Stopfschnecke einem Kocher zugeführt werden, in dem sie erhöhtem Druck und erhöhter Temperatur ausgesetzt werden, und wobei die Holzhackschnitzel unter schnellem Entspannen des Drucks aus dem Kocher ausgetragen und dadurch in die Holzfasern aufgelöst werden. Weiterhin bezieht sich die Erfindung auf eine Vorrichtung zum Gewinnen von Holzfasern aus Holzhackschnitzeln mit einer Stopfschnecke, einem Kocher und einer Austrageinrichtung, wobei die Stopfschnecke die Holzhackschnitzel dem Kocher zuführt, wobei die Holzhackschnitzel in dem Kocher erhöhtem Druck und erhöhter Temperatur ausgesetzt werden und wobei die Austrageinrichtung die Holzhackschnitzel unter schneller Entspannung des Drucks aus dem Kocher austrägt, so dass sie sich in die Holzfasern auflösen.The invention relates to a method for recovering wood fibers from wood chips, the wood chips are fed with a plug screw a stove in which they are exposed to elevated pressure and elevated temperature, and wherein the wood chips discharged under rapid release of pressure from the digester and thereby dissolved in the wood fibers. Furthermore, the invention relates to a device for obtaining wood fibers from wood chips with a plug screw, a digester and a discharge device, wherein the plug screw feeds the wood chips to the digester, the wood chips are exposed in the digester elevated pressure and elevated temperature and wherein the discharge device the woodchips discharges from the cooker with rapid release of pressure so that they dissolve into the wood fibers.

STAND DER TECHNIKSTATE OF THE ART

Verfahren und Vorrichtungen der eingangs beschriebenen Art finden in der Holzwerkstoff-, Zellstoff- und Papierindustrie Anwendung (vgl. z.B. US 5 262 003 A ). Im Folgenden wird zur Beschreibung der Erfindung auf ihre Anwendung in der Holzwerkstoffindustrie abgestellt. Hierdurch soll die Reichweite der Erfindung jedoch in keiner Weise beschnitten werden.Processes and devices of the type described above are used in the wood-based materials, pulp and paper industry (cf., for example US 5 262 003 A ). In the following, the description of the invention will be based on its application in the wood-based material industry. As a result, the scope of the invention, however, should be curtailed in any way.

Bei der Herstellung von Holzwerkstoffplatten in Form so genannter Faserplatten, wie beispielsweise mitteldichter Faserplatten (MDF), ist es bekannt, Holz in Holzhackschnitzel zu zerkleinern, die Holzhackschnitzel in einem Vorlagebehälter zu wässern und mit einer Stopfschnecke vom Grund des Vorlagebehälters abzuziehen und einem Kocher zuzuführen. Die Zuführung der Holzhackschnitzel über eine Stopfschnecke ist erforderlich, um die Holzhackschnitzel gegen einen erhöhten Innendruck des Kochers in den Kocher hinein zu fördern und dabei auch den Kocher gegen einen Druckverlust abzudichten. In der Stopfschnecke werden die Holzhackschnitzel zu einem massiven Pfropf verdichtet, wobei überschüssiges Wasser von der Wässerung der Holzhackschnitzel abgepresst wird. In dem Kocher werden die Holzhackschnitzel dem erhöhten Druck und erhöhter Temperatur ausgesetzt, um die Bindung zwischen den Holzfasern zu lockern. Wenn die Holzhackschnitzel nach einer gewissen Verweildauer in dem Kocher durch eine Austrageinrichtung aus dem Kocher herausgefördert werden, wobei der Druck in dem Kocher schlagartig entspannt wird, zerlegen sich die Holzhackschnitzel in die einzelnen Holzfasern. Diese Holzfasern werden von einem durch die Entspannung hervorgerufenen Wasserdampfstrom durch einen Blasgang gefördert, in dem sie bereits mit Bindemittel beleimt werden können, bevor sie dann in einen Trockner eintreten, in dem sie in einem Strom von trockenem heißen Gas auf eine gewünschte Faserfeuchtigkeit eingestellt werden. Der durch den überschüssigen Wasserdampf angereicherte Gasstrom wird in einem Abscheider von den Holzfasern abgeschieden, aus dem die Holzfasern dann für die Ausformung einer Fasermatte ausgetragen werden. Falls keine Beleimung der Holzfasern in dem Blasgang erfolgte, ist diese noch vor oder während der Ausformung der Fasermatte vorzunehmen, die anschließend bei erhöhter Temperatur und in der Regel auch unter erhöhtem Druck zu der gewünschten Faserplatte ausgeformt wird, wobei das Bindemittel aushärtet. Um die Holzfasern auf der gewünschten Faserfeuchte zu halten, wird derzeit eine Messung der Faserfeuchte an den Holzfasern am Ausgang des Abscheiders durchgeführt. Wenn hier Abweichungen zwischen der gewünschten Faserfeuchte und der tatsächlichen Faserfeuchte registriert werden, wird die Einstellung des Trockners z. B. bezüglich der Temperatur und/oder des Volumens des Gases, mit dem die Fasern getrocknet werden, modifiziert. Dabei erfolgt die Modifikation anhand von Erfahrungswerten bezüglich des Einflusses der Einstellungen des Trockners auf die damit erreichte Faserfeuchte. Bei dieser Art der Feedback-Regelung des Trockners, um die Faserfeuchte konstant zu halten, sind Schwankungen der Faserfeuchte von wenigen Prozentpunkten einzuhalten, sie sind jedoch über schwankende Zusammensetzungen der Holzhackschnitzel nicht weiter zu reduzieren. Grundsätzlich ist eine möglichst hohe, aber nicht zu hohe Faserfeuchte der Holzfasern bei der Herstellung von Faserplatten von Interesse. Während eine zu hohe Faserfeuchte zu einer die Holzfaserplatten zerstörenden Spaltbildung beim heißen Verpressen führt und daher unbedingt zu vermeiden ist, resultiert eine niedrige Faserfeuchte in schwankende Dichteprofile und andere Qualitätsmängel bei den Holzfaserplatten. Durch eine maximal hohe, aber nicht zu hohe Faserfeuchte wird einerseits Energie sowohl durch weniger weitgehendes Trocknen der Holzfasern als auch durch eine besser Wärmeleitfähigkeit der Matten beim heißen Verpressen zu der Holzfaserplatte eingespart und damit andererseits auch eine maximale Kapazitätsausnutzung einer Holzfaserplattenherstellungsanlage erreicht. Je größer aber die Schwankungen bei der Faserfeuchte der Holzfasern sind, desto geringer muss die Faserfeuchte im Mittel eingestellt werden, um die mit einer zu hohen Faserfeuchte verbundenen Probleme zuverlässig zu verhindern.In the production of wood-based panels in the form of so-called fiberboard, such as medium-density fiberboard (MDF), it is known to crush wood in wood chips, to water the wood chips in a storage tank and deduct with a plug screw from the bottom of the storage container and feed it to a digester. The feeding of the wood chips via a plug screw is required to the To promote wood chips against increased internal pressure of the digester into the digester into it while also sealing the digester against a pressure loss. The wood chips are compacted into a massive plug in the plug screw, with excess water being pressed out from the washing of the wood chips. In the digester, the wood chips are exposed to the increased pressure and elevated temperature to loosen the bond between the wood fibers. If the wood chips are conveyed out after a certain residence time in the digester by a discharge device from the digester, the pressure in the digester is suddenly relaxed, dismantle the wood chips into the individual wood fibers. These wood fibers are conveyed through a blown duct by a steam stream produced by the expansion in which they can already be glued with binder before they then enter a dryer in which they are adjusted in a stream of dry hot gas to a desired fiber moisture. The enriched by the excess water vapor gas stream is separated in a separator from the wood fibers, from which the wood fibers are then discharged for the formation of a fiber mat. If no gluing of the wood fibers took place in the blown duct, this should be carried out before or during the shaping of the fiber mat, which is then shaped at elevated temperature and usually also under elevated pressure to the desired fiberboard, whereby the binder hardens. In order to keep the wood fibers at the desired fiber moisture content, a measurement of the fiber moisture content at the wood fibers at the outlet of the separator is currently being carried out. If deviations between the desired fiber moisture and the actual fiber moisture are registered here, the setting of the dryer z. B. with respect to the temperature and / or the volume of the gas with which the fibers are dried modified. The modification is based on empirical values regarding the influence of the settings of the dryer on the fiber moisture content achieved thereby. In this type of feedback control of the dryer, in order to keep the fiber moisture constant, fluctuations in the fiber moisture of a few percentage points are to be observed, but they are not further reduced by fluctuating compositions of the woodchips. In principle, the highest possible, but not too high fiber moisture content of the wood fibers in the production of fiberboard is of interest. While excessively high fiber moisture leads to cracking of the fibreboard during hot pressing and therefore must be avoided, low fiber moisture results in fluctuating density profiles and other quality deficiencies in fiberboard. Due to a maximum high, but not too high fiber moisture on the one hand energy by less extensive drying of the Wood fibers and saved by a better thermal conductivity of the mats during hot pressing to the wood fiber board and thus on the other hand also achieved a maximum capacity utilization of a wood fiber board manufacturing plant. However, the greater the fluctuations in the fiber moisture of the wood fibers, the lower the fiber moisture must be adjusted on average in order to reliably prevent the problems associated with excessively high fiber moisture.

AUFGABE DER ERFINDUNGOBJECT OF THE INVENTION

Der Erfindung liegt die Aufgabe zugrunde, ein Verfahren und eine Vorrichtung der eingangs beschriebenen Art derart weiterzuentwickeln, dass die Faserfeuchte der gewonnenen Holzfasern in engeren Grenzen als bisher konstant gehalten werden kann, um die mittlere Faserfeuchte bei der Herstellung von Holzfaserplatten ohne das Risiko einer zu hohen Faserfeuchte signifikant anheben zu können.The invention has for its object to provide a method and apparatus of the type described above such that the fiber moisture content of the wood fibers obtained within narrow limits can be kept constant to date, the average fiber moisture content in the production of wood fiber boards without the risk of too high To be able to increase fiber moisture significantly.

LÖSUNGSOLUTION

Diese Aufgabe wird erfindungsgemäß durch ein Verfahren mit den Merkmalen des Patentanspruchs 1 und durch eine Vorrichtung mit den Merkmalen des Patentanspruchs 6 gelöst. Bevorzugte Ausführungsformen des neuen Verfahrens sind in den Unteransprüchen 2 bis 5 beschrieben. Die Unteransprüche 7 bis 10 betreffen bevorzugte Ausführungsformen der neuen Vorrichtung.This object is achieved by a method having the features of claim 1 and by a device having the features of claim 6. Preferred embodiments of the new method are described in the subclaims 2 to 5. The dependent claims 7 to 10 relate to preferred embodiments of the new device.

BESCHREIBUNG DER ERFINDUNGDESCRIPTION OF THE INVENTION

Bei dem neuen Verfahren wird die Leitfähigkeit der Holzhackschnitzel im Bereich eines Pfropfs aus den Holzhackschnitzeln am Ausgang der Stopfschnecke gemessen und als Steuerparameter für die Steuerung der weiteren Verarbeitung der Holzhackschnitzel und/oder der Holzfasern verwendet. Die Leitfähigkeit der Holzhackschnitzel stellt ein Maß für die Faserfeuchte der Holzfasern dar, die bei den einzelnen Holzhackschnitzeln noch zusammenhängen. Überraschender Weise kann dieses Maß für die Faserfeuchte der Holzfasern in den Holzhackschnitzeln in dem Pfropf aus den Holzhackschnitzeln am Ausgang der Stopfschnecke mit ausreichender Genauigkeit für eine anschließende Verwendung als Steuerparameter bei der Steuerung der weiteren Verarbeitung der Holzhackschnitzel und/oder der Holzfasern gewonnen werden, und stellt es eine relevante Aussage in Bezug auf die spätere Faserfeuchte der aus den Holzhackschnitzeln vereinzelten Holzfasern dar. Dies gilt insbesondere dann, wenn die Stopfschnecke im Bereich des Pfropfs einen im Wesentlichen konstanten Druck auf die Holzhackschnitzel aufbringt oder wenn ein von der Stopfschnecke im Bereich des Pfropfs auf die Holzhackschnitzel aufgebrachter Druck gemessen und bei der Verwendung der gemessenen Leitfähigkeit der Holzhackschnitzel als Maß für deren Faserfeuchte im Sinne einer Kalibrierung berücksichtigt wird. Bei einem bestimmten Druck im Bereich des Pfropfs ist die Faserfeuchte relativ genau aus der Leitfähigkeit der Holzhackschnitzel in dem Pfropf bestimmbar.In the new method, the conductivity of the wood chips in the region of a plug from the wood chips at the outlet of the screw plug is measured and used as a control parameter for controlling the further processing of wood chips and / or wood fibers. The conductivity of the wood chips represents a measure of the fiber moisture of the wood fibers, which are still related to the individual wood chips. Surprisingly, this measure of the fiber moisture content of the wood fibers in the wood chips in the plug from the wood chips at the outlet of the plug screw can be obtained with sufficient accuracy for subsequent use as a control parameter in the control of further processing of wood chips and / or wood fibers it's a relevant statement in terms of the This is especially true when the plug screw in the region of the graft applies a substantially constant pressure on the woodchips or when measured by the plug screw in the region of the graft on the wood chips measured pressure and at the Use of the measured conductivity of the wood chips as a measure of their fiber moisture in terms of calibration is taken into account. At a certain pressure in the region of the graft, the fiber moisture can be determined relatively accurately from the conductivity of the wood chips in the graft.

Tatsächlich lassen sich mit dem neuen Verfahren aussagekräftige Informationen über die Holzfasern in den Holzhackschnitzeln gewinnen, die die Faserfeuchte der Holzhackschnitzel trotz ihrer umfangreichen Behandlung bis nach der Auflösung der Holzhackschnitzel in die einzelnen Holzfasern bestimmen. Indem dieser entscheidende Ausgangswert für die Faserfeuchte der gewonnenen Holzfaser bei dem neuen Verfahren sehr früh bestimmt wird, kann er für alle nachfolgenden Behandlungen der Holzhackschnitzel und der Holzfasern als Steuerparameter verwendet werden, um letztlich eine konstante Faserfeuchte zu erreichen. Bei dem neuen Verfahren wird damit eine Feedforward-Steuerung realisiert, mit der bei schwankenden Eingangsparametern die Faserfeuchte in engeren Grenzen gehalten werden kann als bei der aus dem Stand der Technik bekannten Feedback-Regelung.In fact, the new process provides meaningful information about the wood fibers in the wood chips, which determine the fiber moisture content of the wood chips despite their extensive treatment until after the woodchips have been dissolved into the individual wood fibers. By determining this crucial starting point for the fiber moisture of the wood fiber obtained very early in the new process, it can be used as a control parameter for all subsequent treatments of the woodchips and the wood fibers in order ultimately to achieve a constant fiber moisture content. In the new method, a feedforward control is realized, with which the fiber moisture content can be kept within narrower limits with fluctuating input parameters than with the feedback control system known from the prior art.

Natürlich kann bei dem neuen Verfahren die gemessene Leitfähigkeit der Holzhackschnitzel im Bereich eines Pfropfs aus den Holzhackschnitzeln auch im Sinne einer Feedback-Regelung für die Steuerung von davor liegenden Schritten der Behandlung der Holzhackschnitzel genutzt werden. Das Besondere an der vorliegenden Erfindung ist aber die Feedforward-Steuerung der weiteren Verarbeitung der Holzhackschnitzel und/oder der Holzfasern.Of course, in the new method, the measured conductivity of the wood chips in the area of a plug from the wood chips can also be used in the sense of a feedback control for the control of preceding steps of the treatment of wood chips. The special feature of the present invention, however, is the feedforward control of the further processing of wood chips and / or wood fibers.

Konkret kann die Leitfähigkeit der Holzhackschnitzel bei dem neuen Verfahren zur Steuerung eines Trockners verwendet werden, mit dem die Faserfeuchte der Holzfasern beispielsweise auf ein für die Herstellung von Faserplatten gewünschtes Maß eingestellt wird.Specifically, the conductivity of the wood chips can be used in the new method of controlling a dryer, with which the fiber moisture content of the wood fibers is set, for example, to a desired level for the production of fiberboard.

Dabei kann der Trockner weiterhin in Abhängigkeit von einer an seinem Ausgang gemessenen Faserfeuchte der Holzfasern gesteuert werden, wie dies im Stand der Technik bislang ausschließlich der Fall war.In this case, the dryer can continue to be controlled in response to a measured at its output fiber moisture content of the wood fibers, as was previously the case exclusively in the prior art.

Es versteht sich, dass beim Steuern des Trockners die Laufzeit der Holzhackschnitzel und der aus ihnen gewonnenen Holzfasern von der Stopfschnecke bis zu dem Trockner zu berücksichtigen ist.It is understood that when controlling the dryer, the running time of the wood chips and the wood fibers obtained from them from the screw conveyor to the dryer must be taken into account.

Wenn die Holzhackschnitzel bei dem neuen Verfahren vor dem Zuführen in dem Kocher gewässert werden, wird überschüssiges Wasser in der Stopfpresse von den Holzhackschnitzeln abgepresst, bevor die Leitfähigkeit der Holzhackschnitzel gemessen wird. Die Leitfähigkeit der Holzhackschnitzel hängt damit nicht von zuvor zugesetztem freiem Wasser, sondern ausschließlich von der Faserfeuchte der die Holzhackschnitzel ausbildenden Holzfasern ab.When the woodchips are watered in the digester before being fed into the digester, excess water in the stuffing press is squeezed from the wood chips before the conductivity of the woodchips is measured. The conductivity of the wood chips does not depend on previously added free water, but only on the fiber moisture content of wood chips forming wood chips.

Dies gilt zumindest solange, wie die Stopfschnecke in der Lage ist, das überschüssige Wasser vollständig abzupressen. Diese Fähigkeit der Stopfschnecke wiederum geht einher mit ihrer Fähigkeit, den Kocher durch den Pfropf aus den Holzhackschnitzeln bezüglich des in ihm herrschenden Drucks abzudichten. So kann die Abdichtung des Kochers durch die Stopfschnecke bei dem neuen Verfahren durch Beobachten des Langzeitverlaufs der Leitfähigkeit der Holzhackschnitzel überwacht werden. Kommt es dabei zu einem anhaltenden Anstieg der Leitfähigkeit, weist dies auf nicht mehr vollständig abgepresste Anteile des überschüssigen Wassers und damit einem Verschleiß der Stopfschnecke hin. Wenn neben der Leitfähigkeit auch der von der Stopfschnecke im Bereich des Pfropfs auf die Holzhackschnitzel aufgebrachte Druck gemessen wird, um die gemessene Leitfähigkeit im Hinblick auf die ihr entsprechende Faserfeuchte zu kalibrieren, kann natürlich direkt durch Verfolgen dieses Drucks die Abdichtfunktion der Stopfschnecke überwacht werden.This is true at least as long as the plug screw is able to completely squeeze out the excess water. This ability of the screw conveyor, in turn, goes hand in hand with its ability to seal the cooker by the plug from the woodchips with respect to the pressure prevailing in it. Thus, the sealing of the digester by the plug screw in the new method can be monitored by observing the long-term history of the conductivity of the wood chips. If there is a sustained increase in conductivity, this indicates no longer completely depressed portions of the excess water and thus wear of the screw conveyor. If, in addition to the conductivity, the pressure applied by the plug screw in the region of the plug to the wood chips is also measured in order to calibrate the measured conductivity with regard to the fiber moisture corresponding thereto, it is of course possible to monitor the sealing function of the screw plug directly by following this pressure.

Die Leitfähigkeit der Holzhackschnitzel kann bei dem neuen Verfahren durch direktes Kontaktieren des Pfropfs aus den Holzhackschnitzeln mit Messelektroden gemessen werden. Es ist aber auch eine indirekte Leitfähigkeitsmessung möglich bei der die von der Leitfähigkeit der Holzhackschnitzel abhängigen induktiven oder kapazitiven Eigenschaften des Pfropfs erfasst werden. Beispielsweise kann der Pfropf Teil eines Dielektrikums einer Kondensatoranordnung oder Teil des Kerns einer Spulenanordnung sein, deren Wechselstromwiderstand sich mit jeder Änderung der Leitfähigkeit der Holzhackschnitzel ändert.The conductivity of wood chips can be measured in the new method by directly contacting the plug from the woodchips with measuring electrodes. However, an indirect conductivity measurement is also possible in which the inductive or capacitive properties of the plug, which depend on the conductivity of the wood chips, are recorded. For example, the plug can be part of a dielectric of a capacitor arrangement or part of the core of a coil arrangement whose alternating current resistance changes with each change in the conductivity of the woodchips.

Wenn die Leitfähigkeit wie bei einer einzelnen direkten Messung über Messelektroden nur für einen lokalen Bereich des Umfangs des Pfropfs bestimmt wird, ist es bevorzugt, wenn die Leitfähigkeit der Holzhackschnitzel in mehreren Umfangsbereichen des Pfropfs aus den Holzhackschnitzeln gemessen wird. Es ist selbst bei konstanter Faserfeuchte der Holzfasern in den Holzhackschnitzeln nicht zu erwarten, dass die interessierende Faserfeuchte als keinen Schwankungen unterworfener konstanter Wert gemessen werden kann. Vielmehr ist der jeweils gemessene Wert auch von der elektrischen Kontaktierung der Holzhackschnitzel und Strukturinhomogenitäten des Pfropfs aus den Holzhackschnitzeln abhängig. Es macht daher Sinn, möglichst mehrere Leitfähigkeitsmesswerte für die jeweils einen Pfropf ausbildende Menge an Holzhackschnitzeln zu gewinnen. Dasselbe gilt, falls diese zusätzlich durchgeführt wird, in Hinblick auf die Messung des Drucks in dem Pfropfs.If the conductivity is determined as for a single direct measurement via measuring electrodes only for a local area of the circumference of the plug, it is preferred that the Conductivity of the wood chips is measured in several peripheral regions of the graft from the wood chips. Even with a constant fiber moisture content of the wood fibers in the wood chips, it is not to be expected that the fiber moisture of interest can be measured as a constant value which is not subject to fluctuations. Rather, the value measured in each case is also dependent on the electrical contacting of the woodchips and structural inhomogeneities of the graft from the woodchips. It therefore makes sense to obtain as many conductivity measurements as possible for the amount of wood chips each forming a graft. The same applies if this is additionally carried out with regard to the measurement of the pressure in the graft.

Die erfindungsgemäße Vorrichtung, mit der das neue Verfahren umgesetzt werden kann, weist am Ausgang der Stopfschnecke eine Leitfähigkeitsmesseinrichtung für das Messen der Leitfähigkeit der Holzhackschnitzel im Bereich eine Pfropfs aus den Holzhackschnitzeln auf. Dabei kann, wenn die Leitfähigkeitsmesseinrichtung für eine direkte Messung der Leitfähigkeit der Holzhackschnitzel vorgesehen ist, ein Gehäuse der Stopfschnecke mindestens eine Querbohrung aufweisen, die eine gegenüber dem Gehäuse isolierte Messelektrode dichtend aufnimmt. Die Messelektrode kontaktiert den Pfropf am Innenumfang des Gehäuses. Jeder Abrieb des Gehäuses wirkt sich gleichermaßen auf die Messelektrode auf. Die Messanordnung bleibt also trotz eines nicht vermeidbaren Abriebs am Innenumfang des Gehäuses immer dieselbe. Die Leitfähigkeitsmesseinrichtung kann die Leitfähigkeit zwischen der bereits erwähnten Messelektrode und dem Gehäuse und/oder mindestens einer weiteren Messelektrode messen. Dabei ist wichtig darauf zu achten, dass der bei einer bestimmten Spannung durch die Messanordnung fließende Strom tatsächlich im Wesentlichen von der Leitfähigkeit der Holzhackschnitzel abhängt.The device according to the invention, with which the new method can be implemented, has at the outlet of the plug screw a conductivity measuring device for measuring the conductivity of the wood chips in the region of a plug from the wood chips. In this case, if the conductivity measuring device is provided for a direct measurement of the conductivity of the wood chips, a housing of the screw plug having at least one transverse bore, which receives a sealed relative to the housing measuring electrode sealingly. The measuring electrode contacts the plug on the inner circumference of the housing. Any abrasion of the housing affects equally on the measuring electrode. The measuring arrangement thus remains always the same despite an unavoidable abrasion on the inner circumference of the housing. The conductivity measuring device can measure the conductivity between the already mentioned measuring electrode and the housing and / or at least one further measuring electrode. It is important to ensure that the current flowing through the measuring arrangement at a certain voltage actually depends essentially on the conductivity of the wood chips.

Bevorzugt sind Leitfähigkeitsmesseinrichtungen bei der neuen Vorrichtung, die über den Umfang der Stopfschnecke verteilt eine Mehrzahl von mindestens drei Messelektroden aufweisen, um auch die Homogenität der Verteilung der Faserfeuchte über den jeweiligen Pfropf aus den Holzhackschnitzeln zu erfassen.Preference is given to conductivity measuring devices in the new device, which have a plurality of at least three measuring electrodes distributed over the circumference of the screwing plug in order to also detect the homogeneity of the distribution of the fiber moisture over the respective plug from the woodchips.

Für eine zusätzliche Messung eines von der Stopfschnecke im Bereich des Pfropfs auf die Holzhackschnitzel aufgebrachten Drucks kann eine Druckmesseinrichtung vorgesehen sein, die mindestens einen, vorzugsweise mehrere über deren Umfang verteilte Drucksensoren am Ausgang der Stopfschnecke aufweist.For an additional measurement of a pressure applied by the plug screw in the region of the plug on the wood chips, a pressure measuring device may be provided which has at least one, preferably a plurality of pressure sensors distributed over the circumference thereof at the outlet of the screw plug.

Vorteilhafte Weiterbildungen der Erfindung ergeben sich aus den Patentansprüchen, der Beschreibung und den ZeichnungenAdvantageous developments of the invention will become apparent from the claims, the description and the drawings

KURZBESCHREIBUNG DER FIGURENBRIEF DESCRIPTION OF THE FIGURES

Im Folgenden wird die Erfindung unter Bezugnahme auf die beigefügten Zeichnungen anhand von einzelnen Ausführungsbeispielen näher erläutert und beschrieben.

Fig. 1
zeigt einen Querschnitt durch eine Stopfschnecke als zentrales Element eines Flussdiagramms zum Gewinnen von Holzfasern aus Holzhackschnitzeln.
Fig. 2
zeigt die Leitfähigkeitsmesseinrichtung an einer Stopfschnecke in einer gegenüber Fig. 1 abgewandelten Ausführungsform.
Fig. 3
zeigt eine weitere Ausführungsform der Leitfähigkeitsmesseinrichtung; und
Fig. 4
zeigt ein Ablaufdiagramm zur Gewinnung von Holzfasern aus Holzhackschnitzeln für die Herstellung von Holzfaserplatten.
In the following the invention will be explained and described in more detail with reference to the accompanying drawings with reference to individual embodiments.
Fig. 1
shows a cross section through a plug screw as a central element of a flow chart for obtaining wood fibers from wood chips.
Fig. 2
shows the conductivity measuring device on a plug screw in a opposite Fig. 1 modified embodiment.
Fig. 3
shows a further embodiment of the conductivity measuring device; and
Fig. 4
shows a flow diagram for the production of wood fibers from wood chips for the production of wood fiber boards.

FIGURENBESCHREIBUNGDESCRIPTION OF THE FIGURES

In Fig. 1 ist eine Stopfschnecke 1 im Querschnitt wiedergegeben. In einem Gehäuse 2 der Stopfschnecke 1 läuft eine Förderschnecke 3 um eine Achse 4 um, so dass eine Schneckenwendel 5 der Förderschnecke 3 Holzhackschnitzel 6, die der Stopfschnecke 2 an ihrem Einlass 7 zugeführt werden und hier nicht einzeln dargestellt sind, nach rechts fördert und dabei zu einem kompakten Pfropf zusammenpresst. Für den Antrieb der Förderschnecke 3 ist ein in Fig. 1 nur schematisch wiedergegebener Antriebsmotor 8 vorgesehen. Der Pfropf aus den Holzhackschnitzeln 6 dient primär dazu, einen Kocher 9 abzudichten, dem die Holzhackschnitzel 6 zugeführt werden. In dem Kocher 9 herrscht nicht nur eine erhöhte Temperatur, sondern auch ein erhöhter Druck, der über die Stopfschnecke 2 nicht entweichen soll und gegen den die Holzhackschnitzel 6 in den Kocher 9 hineingedrückt werden müssen. Dabei ist am Eingang des Kochers 9 in der Regel ein hier nicht dargestellter Gegendruckkörper für die Holzhackschnitzel 6 vorgesehen, der sicherstellt, dass sich der gewünschte Pfropf aus den Holzhackschnitzeln 6 in der Stopfschnecke 2 aufbaut. Beim Aufbauen des Pfropfs aus den Holzhackschnitzeln wird überschüssiges Wasser, mit dem die Holzhackschnitzel 6 in einem Vorlagebehälter 10 gewässert sein können, abgepresst, so dass im Bereich des Pfropfs nur das in den Holzfasern der Holzhackschnitzel 6 gebundene Wasser vorliegt. Dieser Wassergehalt, d. h. die Faserfeuchte der die Holzhackschnitzel 6 ausbildenden Holzfasern wird durch eine Leitfähigkeitsmesseinrichtung 11 gemessen. Konkret misst die Leitfähigkeitsmesseinrichtung 11 die Leitfähigkeit des Pfropfs aus den Holzhackschnitzeln 6 zwischen zwei Elektroden 12 und 13, die den Pfropf am Innenumfang 17 des Gehäuses 2 an zwei voneinander beabstandeten Punkten kontaktieren. Je größer die Faserfeuchte ist, desto größer ist die von der Leitfähigkeitsmesseinrichtung 11 registrierte Leitfähigkeit zwischen den Elektroden 12 und 13. Die gemessene Leitfähigkeit kann als Steuerparameter 14 nicht nur wie hier dargestellt für den Kocher 9 sondern auch für alle sich daran anschließenden Einrichtungen zur weiteren Aufbereitung der Holzhackschnitzel 6 bzw. daraus gewonnener Holzfasern verwendet werden, aber auch für den Vorlagebehälter 10. Weiterhin kann eine Langzeitbeobachtung der Leitfähigkeit der Holzhackschnitzel 6 im Bereich des Pfropfs genutzt werden, um festzustellen, in wieweit trotz einer unvermeidbaren Abnutzung der Stopfschnecke 1 sowohl an ihrem Gehäuse 2 als auch ihrer Förderschnecke 3 noch eine vollständige Abpressung des überschüssigen und nicht in den Holzfasern gebundenen Wassers von den Holzhackschnitzeln erfolgt. Wenn diese Abpressung nicht mehr gewährleistet ist, ist es an der Zeit, zumindest die Förderschnecke 3 auszutauschen, weil dann auch die Abdichtung des Kochers 9 nicht mehr sichergestellt ist.In Fig. 1 a stuffing screw 1 is shown in cross section. In a housing 2 of the screw conveyor 1, a screw conveyor 3 runs around an axis 4, so that a screw spiral 5 of the screw conveyor 3 woodchips 6, which are supplied to the plug screw 2 at its inlet 7 and are not shown here individually, promotes to the right and compressed into a compact plug. For the drive of the screw conveyor 3 is an in Fig. 1 only schematically reproduced drive motor 8 is provided. The plug from the wood chips 6 serves primarily to seal a cooker 9, the wood chips 6 are fed. In the cooker 9 prevails not only an elevated temperature, but also an increased pressure, which should not escape via the plug screw 2 and against the wood chips 6 must be pressed into the stove 9. In this case, at the entrance of the digester 9 usually a counter-pressure body not shown here for the wood chips 6 is provided, which ensures that the desired plug from the wood chips 6 in the plug screw 2 builds up. When building up the graft from the wood chips, excess water with which the woodchips 6 can be watered in a storage container 10 is pressed, so that only the water bound in the wood fibers of the woodchips 6 is present in the region of the graft. This water content, ie the moisture content of the wood chips forming the wood chips 6, is measured by a conductivity measuring device 11. Concretely, the conductivity meter 11 measures the conductivity of the plug of the woodchips 6 between two electrodes 12 and 13 contacting the plug on the inner periphery 17 of the housing 2 at two spaced apart points. The greater the fiber moisture content, the greater the conductivity recorded between the electrodes 12 and 13 by the conductivity measuring device 11. The measured conductivity can be used as a control parameter 14 not only for the cooker 9 as shown here but also for all subsequent devices for further processing Furthermore, a long-term observation of the conductivity of the wood chips 6 in the region of the plug can be used to determine to what extent, despite an inevitable wear of the plug screw 1 both on its housing 2 as well as their screw conveyor 3 is still a complete Abpressung the excess and not bound in the wood fibers water from the wood chips. If this pressure is no longer guaranteed, it is time to replace at least the screw conveyor 3, because then the seal of the stove 9 is no longer ensured.

Die Messanordnung der Leitfähigkeitsmesseinrichtung 11 gemäß Fig. 1, bei der zwei Elektroden 12 und 13 das Gehäuse 2 in radialer Richtung dichtend durchsetzten, erfordert es, dass zumindest der zugehörige Abschnitt 15 des Gehäuses aus elektrisch nicht leitfähigem Material besteht oder an seinem Innenumfang 17 elektrisch isolierend beschichtet ist, weil sonst die Messstrecke zwischen den Elektroden 12 und 13 durch das Gehäuse 2 selbst kurzgeschlossen würde. Fig. 2 skizziert eine andere Ausbildung einer Messstrecke, die ebenso wie die Messstrecke in Fig. 1 bei auftretendem Verschleiß des Gehäuses 2 gleich bleibt, aber keinen Abschnitt 15 des Gehäuses 12 aus elektrisch nicht leitfähigem Material erfordert. Bei dieser Messanordnung wird als Gegenelektrode zu der Elektrode 12 das elektrisch leitfähige Gehäuse 2 verwendet, wobei die Elektrode 12 gegenüber dem Gehäuse 2 durch eine zylindermantelförmige Isolierung 16 elektrisch isoliert ist, die gemeinsam mit der Elektrode 12 eine radial zu der Achse 4 verlaufende Querbohrung 30 in dem Gehäuse 2 abdichtet.The measuring arrangement of the conductivity measuring device 11 according to Fig. 1 in which two electrodes 12 and 13 sealingly penetrate the housing 2 in the radial direction, it is necessary that at least the associated portion 15 of the housing is made of electrically non-conductive material or is coated electrically insulating on its inner circumference 17, because otherwise the measuring distance between the Electrodes 12 and 13 would be short-circuited by the housing 2 itself. Fig. 2 outlines another training a measuring distance, which as well as the measuring distance in Fig. 1 remains the same at occurring wear of the housing 2, but does not require a portion 15 of the housing 12 of electrically non-conductive material. In this measuring arrangement is used as a counter electrode to the electrode 12, the electrically conductive housing 2, wherein the electrode 12 is electrically insulated from the housing 2 by a cylinder jacket insulation 16, which together with the electrode 12 a radially extending to the axis 4 transverse bore 30 in the housing 2 seals.

In Fig. 3 ist für eine andere Ausführungsform der neuen Vorrichtung skizziert, dass eine Vielzahl von Elektroden 12, die über den Umfang des Gehäuses 2 der Stopfschnecke 1 verteilt sind, an die Leitfähigkeitsmesseinrichtung 11 angeschlossen sein kann. Dabei kann der Abschnitt 15 des Gehäuses 2, in dem die Elektroden 12 angeordnet sind, aus elektrisch nicht leitfähigem Material bestehen oder an seinem Innenumfang 17 mit einer isolierenden Beschichtung versehen sein, oder für jede der Elektroden 12 kann die Messanordnung gemäß Fig. 2 vorgesehen sein. In jedem Fall ist es mit der Vielzahl der Elektroden 12 möglich, die Leitfähigkeit der Holzhackschnitzel in dem sich in dem Abschnitt 15 des Gehäuses 2 ausbildenden Pfropf an mehreren Stellen gleichzeitig oder hintereinander zu messen, um mehr Informationen über die Faserfeuchte der Holzfasern in den Holzhackschnitzeln zu gewinnen, um beispielsweise die Homogenität der Verteilung der Faserfeuchte zu erfassen. Darüber hinaus können bei der Messanordnung gemäß Fig. 3 einzelne Elektroden 12 ausfallen, ohne dass die Vorrichtung insgesamt ihre Funktion verliert. Die Leitfähigkeitsmesseinrichtung 11 kann die einzelnen Elektroden 12 bzw. die aus diesen und zugehörigen Gegenelektroden, bei denen es sich um andere Elektroden 12 handeln kann, parallel zueinander oder auch sequenziell abfragt. Zusätzlich zu den Elektroden 12 ist die Leitfähigkeitsmesseinrichtung 11 gemäß Fig. 3 auch mit Drucksensoren 31 verbunden. Die Drucksensoren messen einen von der Stopfschnecke 1 auf die Holzhackschnitzel im Bereich der Elektroden ausgeübten Druck, um die Messung deren Faserfeuchte anhand ihrer Leitfähigkeit auf diesen Druck zu kalibrieren. Die Beziehung zwischen der elektrischen Leitfähigkeit der Holzhackschnitzel und Ihrer Faserfeuchte ist druckabhängig. Mit einer Bestimmung der Faserfeuchte aus der Leitfähigkeit ohne Berücksichtigung des zugehörigen Drucks sind daher Fehler verbunden, die nur bei einem weitgehend konstanten Druck der Holzhackschnitzel im Bereich der Elektroden 12 klein bleiben. Unter Berücksichtigung des zugehörigen Drucks kann hingegen aus der gemessenen Leitfähigkeit sehr genau auf die tatsächliche Faserfeuchte der Holzfasern in den Holzhackschnitzeln geschlossen werden.In Fig. 3 is sketched for another embodiment of the new device, that a plurality of electrodes 12, which are distributed over the circumference of the housing 2 of the screw conveyor 1, may be connected to the conductivity measuring device 11. In this case, the portion 15 of the housing 2, in which the electrodes 12 are arranged, consist of electrically non-conductive material or be provided on its inner circumference 17 with an insulating coating, or for each of the electrodes 12, the measuring arrangement according to Fig. 2 be provided. In any case, with the plurality of electrodes 12, it is possible to measure the conductivity of the woodchips in the graft forming in the section 15 of the housing 2 at several points simultaneously or in succession to provide more information about the fiber moisture of the wood fibers in the woodchips win, for example, to capture the homogeneity of the distribution of fiber moisture. In addition, in the measuring arrangement according to Fig. 3 individual electrodes 12 fail, without the device loses its overall function. The conductivity measuring device 11 can scan the individual electrodes 12 or the respective electrodes 12 and / or the associated counterelectrodes, which may be other electrodes 12, in parallel or else sequentially. In addition to the electrodes 12, the conductivity measuring device 11 is according to FIG Fig. 3 also connected to pressure sensors 31. The pressure sensors measure a pressure exerted by the screw conveyor 1 on the wood chips in the region of the electrodes to calibrate the measurement of their fiber moisture based on their conductivity to this pressure. The relationship between the electrical conductivity of woodchips and their fiber moisture is pressure dependent. With a determination of the fiber moisture content from the conductivity Therefore, without consideration of the associated pressure, errors are associated which remain small only at a largely constant pressure of the wood chips in the area of the electrodes 12. On the other hand, taking into account the associated pressure, it is possible to deduce from the measured conductivity very precisely the actual fiber moisture content of the wood fibers in the woodchips.

Fig. 4 skizziert die Gewinnung von beleimten Holzfasern 18 für die Herstellung 19 von Holzfaserplatten. Hierzu werden die Holzhackschnitzel 6 aus dem Kocher 9 gemäß Fig. 1 mit einer Austrageinrichtung 20 ausgetragen, in der der Druck im Inneren des Kochers 9 schlagartig abgebaut wird, so dass sich die Holzhackschnitzel 6 in einzelne Holzfasern auflösen. Diese Holzfasern gelangen durch einen Blasgang 21 in einen Trockner 22. Zuvor werden sie innerhalb des Blasgangs 21 mit Bindemittel 23 besprüht. In dem Trockner 22 wird die Feuchtigkeit der Holzfasern durch einen Strom von heißem trockenen Gas eingestellt. Das heiße trockene Gas wird in einem Brenner 24 durch Verbrennen von Heizgas 25 zubereitet. Die Steuerung des Brenners 24 ist hier durch ein Ventil 26 angedeutet, das die Menge des dem Brenner 24 zugeführten Heizgases 25 einstellt. Die Einstellung des Ventils 26 erfolgt dabei in Abhängigkeit von dem Steuerparameter 14, der aus der von der Leitfähigkeitsmesseinrichtung 11 ermittelten Leitfähigkeit der Holzhackschnitzel abgeleitet wird. Dabei wird für die Steuerung des Brenners 24 die Laufzeit der Holzfasern von dem Pfropf aus den Holzhackschnitzeln, an dem die Leitfähigkeit gemessen wird, bis zu ihrem Eintritt in den Trockner 22 berücksichtigt. Aus dem Trockner 22 gelangen die Holzfasern in einen Abscheider 27, wo sie von dem Gasstrom des Trockners 22 und der von diesem aufgenommenen überschüssigen Feuchtigkeit getrennt werden. Am Ausgang des Abscheiders 27 wird mit einer Messeinrichtung 28 die Faserfeuchte der beleimten Holzfasern 18 gemessen, und hieraus wird ein weiterer Steuerparameter 29 ermittelt, der ebenfalls zur Steuerung des Trockners 22 verwendet wird. Durch die Feedforward-Steuerung des Brenners 22 mit Hilfe der durch die Leitfähigkeitsmesseinrichtung 11 bestimmten Faserfeuchte in den Holzhackschnitzeln 6 erlaubt das in Fig. 4 skizzierte Verfahren zur Gewinnung von Holzfasern 18 aus Holzhackschnitzeln 6 insgesamt, die Faserfeuchte der Holzfasern 18 in einem sehr kleinen Fenster zu halten. Damit kann die Faserfeuchte gegen die Grenze, bei der die Gefahr einer Spaltbildung besteht, erhöht werden, um Energie einzusparen und die Kapazität einer Holzfaserplattenherstellungsanlage voll auszunutzen. Fig. 4 outlines the production of glued wood fibers 18 for the production 19 of wood fiber boards. For this purpose, the woodchips 6 from the cooker 9 according to Fig. 1 discharged with a discharge device 20, in which the pressure in the interior of the digester 9 is abruptly reduced, so that the woodchips 6 dissolve into individual wood fibers. These wood fibers pass through a blowing passage 21 in a dryer 22. Previously, they are sprayed within the blowing passage 21 with binder 23. In the dryer 22, the moisture of the wood fibers is adjusted by a stream of hot dry gas. The hot dry gas is prepared in a burner 24 by burning fuel gas 25. The control of the burner 24 is indicated here by a valve 26 which adjusts the amount of hot gas 25 supplied to the burner 24. The adjustment of the valve 26 takes place as a function of the control parameter 14, which is derived from the conductivity of the woodchip chips determined by the conductivity measuring device 11. In this case, for the control of the burner 24, the running time of the wood fibers is taken into account by the graft from the woodchips, at which the conductivity is measured, until they enter the dryer 22. From the dryer 22, the wood fibers pass into a separator 27, where they are separated from the gas flow of the dryer 22 and the excess moisture absorbed by this. At the output of the separator 27, the fiber moisture content of the glued wood fibers 18 is measured with a measuring device 28, and from this a further control parameter 29 is determined, which is also used to control the dryer 22. By the feedforward control of the burner 22 with the aid of the determined by the conductivity measuring device 11 fiber moisture in the wood chips 6 allows in Fig. 4 sketched method for obtaining wood fibers 18 from wood chips 6 total to keep the fiber moisture of the wood fibers 18 in a very small window. Thus, the fiber moisture can be increased to the limit at which there is a risk of a gap, to save energy and fully exploit the capacity of a wood fiber board manufacturing plant.

BEZUGSZEICHENLISTELIST OF REFERENCE NUMBERS

11
Stopfschneckestuffing screw
22
Gehäusecasing
33
FörderschneckeAuger
44
Achseaxis
55
Schneckenwendelscrew spiral
66
Holzhackschnitzelwood chips
77
Einlassinlet
88th
Antriebsmotordrive motor
99
KocherStove
1010
Vorlagebehälterstorage container
1111
LeitfähigkeitsmesseinrichtungConductivity measuring device
1212
Elektrodeelectrode
1313
Elektrodeelectrode
1414
Steuerparametercontrol parameters
1515
Abschnittsection
1616
Isolierunginsulation
1717
Innenumfanginner circumference
1818
Holzfasernwood fibers
1919
Herstellung von HolzfaserplattenProduction of wood fiber boards
2020
Austrageinrichtungdischarge
2121
Blasgangblow line
2222
Trocknerdryer
2323
Bindemittelbinder
2424
Brennerburner
2525
Heizgasheating gas
2626
VentilValve
2727
Abscheiderseparators
2828
Messeinrichtungmeasuring device
2929
Steuerparametercontrol parameters
3030
Querbohrungcross hole
3131
Drucksensorpressure sensor

Claims (10)

  1. A method of obtaining wood fibres from wood chips, wherein the wood chips are supplied to a digester, in which they are subjected to increased pressure and increased temperature, by means of a feed screw, and wherein the wood chips are discharged from the digester while quickly removing the pressure, and are thus digested in the wood fibres,
    characterized in that an electric conductivity of the wood chips (6) is measured in the area of a plug of the wood chips (6) at the outlet of the feed screw (1), and is used as a control parameter (14) for controlling the further processing of the wood chips (6) and/or the wood fibres (18).
  2. The method of claim 1, characterized in that a pressure applied by the feed screw (1) in the area of the plug onto the wood chips (6) is measured and considered in using the conductivity of the wood chip (6) for controlling the further processing of the wood chips (6) and/or of the wood fibres (18).
  3. The method of claim 1 or 2, characterized in that the conductivity of the wood chips (6) is used for controlling a dryer (22) by which the fibre moisture content of the wood fibres (18) is adjusted.
  4. The method of any of the claims 1 to 3, characterized in that the wood chips (6) are watered prior to being supplied to the digester (9), and that excess water is pressed from the wood chips in the feed screw (1) prior to measuring the conductivity of the wood chips (6).
  5. The method of any of the claims 1 to 4, characterized in that the conductivity of the wood chips (6) is measured in a plurality of circumferential areas of the plug.
  6. An apparatus for obtaining wood fibres from wood chips, the apparatus comprising a feed screw, a digester and a discharge unit, wherein the feed screw supplies the wood chips to the digester, wherein the wood chips are subjected to increased pressure and increased temperature in the digester, and wherein the discharge unit discharges the wood chips with a quick relief of the pressure out of the digester so that they are digested into the wood fibres,
    characterized in that a conductivity measuring unit (11) for measuring an electric conductivity of the wood chips (6) in the area of a plug of the wood chips (6) is provided at the outlet of the feed screw (1).
  7. The apparatus of claim 6, characterized in that a housing (2) of the feed screw (1) comprises at least one cross-hole which, in a sealed way, accepts a measurement electrode of the conductivity measuring unit (11), which is isolated with regard to the housing (2).
  8. The apparatus according to claim 7, characterized in that the conductivity measuring unit (11) measures the conductivity between the electrode (12) and the housing (2) and/or at least one further electrode (12, 13).
  9. The apparatus according to claim 7 or 8, characterized in that the conductivity measuring unit (11) comprises a plurality of at least three electrodes (12) over the circumference of the feed screw (1).
  10. The apparatus according to any of the claims 6 to 9, characterized in that a pressure measuring unit (31) for measuring a pressure, which is applied by the feed screw onto the wood chips (6) in the area of the plug, is provided at the outlet of the feed screw (1).
EP06021281A 2005-10-13 2006-10-11 Method and device for obtaining wood fibers from wood chips Not-in-force EP1775376B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL06021281T PL1775376T3 (en) 2005-10-13 2006-10-11 Method and device for obtaining wood fibers from wood chips

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102005048958A DE102005048958B4 (en) 2005-10-13 2005-10-13 Method and device for obtaining wood fibers from wood chips

Publications (3)

Publication Number Publication Date
EP1775376A2 EP1775376A2 (en) 2007-04-18
EP1775376A3 EP1775376A3 (en) 2007-09-05
EP1775376B1 true EP1775376B1 (en) 2010-05-12

Family

ID=37708214

Family Applications (1)

Application Number Title Priority Date Filing Date
EP06021281A Not-in-force EP1775376B1 (en) 2005-10-13 2006-10-11 Method and device for obtaining wood fibers from wood chips

Country Status (5)

Country Link
EP (1) EP1775376B1 (en)
AT (1) ATE467714T1 (en)
DE (2) DE102005048958B4 (en)
PL (1) PL1775376T3 (en)
PT (1) PT1775376E (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102962876A (en) * 2012-11-30 2013-03-13 濮阳龙丰纸业有限公司 Steam device of wood chip tearing machine

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008022841B4 (en) 2008-05-08 2010-03-04 Kronotec Ag Process and plant for the production of chipboard
CN101463570B (en) * 2009-01-12 2012-01-04 广州华新科实业有限公司 Screw rod injection type plant fibre steam blasting device and method
DK2398958T3 (en) 2009-01-13 2013-05-21 Biogasol Aps Plant and process for the production of bio-products
CN103451985B (en) * 2013-08-23 2016-10-05 华南理工大学 Multistage single screw rod continuous steam explosion device of Plant fiber
TR201909593T4 (en) * 2014-09-19 2019-07-22 Versalis Spa Continuous process for processing a lignocellulosic biomass.
TR201908377T4 (en) 2014-09-19 2019-06-21 Versalis Spa Continuous process for processing a lignocellulosic biomass.
PL3192626T3 (en) * 2016-01-12 2018-11-30 SWISS KRONO Tec AG Method for the treatment of wood dust and assembly for the same

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5262003A (en) * 1991-09-18 1993-11-16 The Black Clawson Company Method and system for defibering paper making materials
AT398587B (en) * 1992-02-04 1994-12-27 Oesterreichische Homogenholz A INPUT PROCEDURE
DE19653530C1 (en) * 1996-12-20 1998-07-23 Siemens Ag Process and device for process control and process optimization in the production of pulp
WO1999028548A1 (en) * 1997-11-26 1999-06-10 Siemens Aktiengesellschaft Control device for a continuos digester for the production of cellulose

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102962876A (en) * 2012-11-30 2013-03-13 濮阳龙丰纸业有限公司 Steam device of wood chip tearing machine

Also Published As

Publication number Publication date
PT1775376E (en) 2010-07-06
PL1775376T3 (en) 2010-10-29
EP1775376A3 (en) 2007-09-05
ATE467714T1 (en) 2010-05-15
DE502006006929D1 (en) 2010-06-24
EP1775376A2 (en) 2007-04-18
DE102005048958A1 (en) 2007-04-19
DE102005048958B4 (en) 2007-08-09

Similar Documents

Publication Publication Date Title
EP1775376B1 (en) Method and device for obtaining wood fibers from wood chips
EP0054015B1 (en) Process and apparatus for producing cellulose
WO2009112163A2 (en) Biomass transport installation for introduction into a pressurised container
WO1996029465A2 (en) Method and device for process control in cellulose and paper manufacture
DE2442627A1 (en) METHOD OF TREATING A FIBER MATERIAL
AT412787B (en) METHOD AND DEVICE FOR TRANSFERRING LIGNOCELLULOUS RAW MATERIAL FROM A COOKER AND PROMOTING THE RAW MATERIAL TO A REFINER
DE3114712A1 (en) "TOBACCO DRYING DEVICE"
DE102014214363A1 (en) Method and device for influencing and regulating a gluing process
EP1834747A2 (en) Method and apparatus for producing moulded articles, in particular boards from lignocellulosic fibres
EP0065019A1 (en) Method for the determination of the degree of saturation of a drying-cartridge, suitable for the drying of humid gases, and devices for carrying out the method
EP1358464B1 (en) Method for producing sample from filter or fly ash
DE102019125408A1 (en) Control and / or regulation of a process air system
DE2745463C3 (en) Method for testing and monitoring the dry density of an insulating panel made of, in particular, perlite or slag wool, produced by a wet molding process
DE202012008077U1 (en) Press screw separator for separating solids from a solid-liquid mixture
EP3827670A1 (en) Process line for producing chocolate with different process stages
DE102008026677B3 (en) Drying lignocellulose fibers, for fiberboard production, has a separator to detach fibers from a steam flow for drying with recovered steam for heating the wood chip start material
AT386427B (en) Method and device for controlling the covering thickness on a Yankee cylinder
WO1996011284A1 (en) Process for controlling a drying plant and arrangement therefor
DE102007002687A1 (en) High pressure molding for tobacco material
DE102005062953B4 (en) Method and device for the production of shaped articles, in particular sheets, from lignocellulose-containing fibers with fiber analysis
WO2015014451A1 (en) System and method for processing fibrous materials
EP1359250B1 (en) Process for dispersing pulp
DE4445203C1 (en) Method and appliance for checking ceramic materials for shaping properties
DE2703016C2 (en) Process for the targeted influencing of the ratio of DBP number / DBP number after pressing pearl black
DE102020113622A1 (en) Method and device for extracting oil from seeds

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA HR MK YU

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA HR MK YU

17P Request for examination filed

Effective date: 20071008

AKX Designation fees paid

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REF Corresponds to:

Ref document number: 502006006929

Country of ref document: DE

Date of ref document: 20100624

Kind code of ref document: P

REG Reference to a national code

Ref country code: PT

Ref legal event code: SC4A

Free format text: AVAILABILITY OF NATIONAL TRANSLATION

Effective date: 20100629

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: RIEDERER HASLER & PARTNER PATENTANWAELTE AG

REG Reference to a national code

Ref country code: RO

Ref legal event code: EPE

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20100512

LTIE Lt: invalidation of european patent or patent extension

Effective date: 20100512

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100823

REG Reference to a national code

Ref country code: PL

Ref legal event code: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100912

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100813

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

26N No opposition filed

Effective date: 20110215

BERE Be: lapsed

Owner name: GLUNZ A.G.

Effective date: 20101031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20101031

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502006006929

Country of ref document: DE

Effective date: 20110214

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20101011

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20101031

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20101011

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101113

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100512

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20101011

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100812

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 10

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 11

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PL

Payment date: 20170929

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20170810

Year of fee payment: 12

Ref country code: RO

Payment date: 20171002

Year of fee payment: 12

Ref country code: FR

Payment date: 20171023

Year of fee payment: 12

Ref country code: TR

Payment date: 20171011

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PT

Payment date: 20171003

Year of fee payment: 12

Ref country code: AT

Payment date: 20171018

Year of fee payment: 12

Ref country code: CH

Payment date: 20171023

Year of fee payment: 12

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 502006006929

Country of ref document: DE

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 467714

Country of ref document: AT

Kind code of ref document: T

Effective date: 20181011

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20190501

Ref country code: PT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20190411

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181031

Ref country code: RO

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181011

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181031

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181011

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181011

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181011