[go: up one dir, main page]

EP1209282A1 - Process for milling a fibrous material - Google Patents

Process for milling a fibrous material Download PDF

Info

Publication number
EP1209282A1
EP1209282A1 EP01124186A EP01124186A EP1209282A1 EP 1209282 A1 EP1209282 A1 EP 1209282A1 EP 01124186 A EP01124186 A EP 01124186A EP 01124186 A EP01124186 A EP 01124186A EP 1209282 A1 EP1209282 A1 EP 1209282A1
Authority
EP
European Patent Office
Prior art keywords
overflow
grinding
wet
fibers
solids
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.)
Granted
Application number
EP01124186A
Other languages
German (de)
French (fr)
Other versions
EP1209282B1 (en
Inventor
Harald Selder
Samuel Dr. Schabel
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.)
Voith Patent GmbH
Original Assignee
Voith Paper Patent GmbH
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 Voith Paper Patent GmbH filed Critical Voith Paper Patent GmbH
Publication of EP1209282A1 publication Critical patent/EP1209282A1/en
Application granted granted Critical
Publication of EP1209282B1 publication Critical patent/EP1209282B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/002Control devices
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20Methods of refining
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D5/00Purification of the pulp suspension by mechanical means; Apparatus therefor
    • D21D5/02Straining or screening the pulp

Definitions

  • the invention relates to a method for grinding a paper pulp according to the preamble of claim 1.
  • Secondary fibers e.g. made from deinked waste paper. Relative in that too Homogeneously producible native pulp is occasionally coarser Fiber components or splinters, e.g. separated by a fractionating machine can be. Such fractionation machines work on the principle of Wet screening. In the case of secondary fibrous materials it is always larger Quality fluctuations to be expected, which can only be explained by an elaborate Have stock preparation sufficiently eliminated. Therefore, often at the end of the Preparation process once again used grinding apparatus, which for a Uniformity of the paper pulp, especially with regard to the geometric Fiber properties should provide. Apparatus for wet grinding of paper pulp are known and are referred to as refiners.
  • a method for controlling a refiner is known from US Pat. No. 3,604,646 the amount of substance supplied to it is determined from the consistency and volume flow. The specific work is regulated to a fixed constant value.
  • the invention is therefore based on the object of creating a method with which the equalization can be carried out better, more gently and cheaper.
  • the proportion of grinding resistant Ingredients e.g. Splinters or long fibers
  • An important indicator of this is the amount of solids in the overflow of this wet sieving, measurable e.g. With which Consistency.
  • the effectiveness of the grinding plant is based on the so determined Variations matched by the specific grinding work according to the invention is increased or decreased if larger or smaller amounts of meal-resistant Substance is present in the pulp suspension to be ground. So it will takes into account the fact that not only the amount of the substance to be ground, i.e. the Overflow, changes, but also the composition of the contained therein Solid. With this simple measure, the substance that is based on its geometry and rigidity to impair the sheet made from it would lead to timely and economical regrinding.
  • the specific Grinding work is the transferred grinding work after deduction based on the amount of solids the idle work consumed by the grinder.
  • the Suspended paper pulp 1 is first fed to a wet sieve 5.
  • a wet sieve 5 uses a pressure sorter or fractionator with one Siebelement, which is part of the supplied paper pulp 1 due to its Size, shape and / or flexibility.
  • the amount of solids in the overflow 3 reached material is determined at a measuring point 9 and the measured value to a controller 8 forwarded.
  • the overflow 3 becomes wet grinding immediately 6 fed.
  • the controllable grinding apparatus used for this contains a drive 7 and is preferably a refiner. After passing the grinding tools, the Material as ground paper pulp 4 in the subsequent processing stages.
  • the specific grinding work transferred in the wet grinding 6 is matched to the determined amount of solids or the amount of solids in the overflow 3.
  • the signal from the controller 8 is used to the To change the drive power of the grinding equipment.
  • the speed variation which is usually is more complex, but it is possible to keep the secondary edge length constant makes. The latter measure is particularly good for maintaining one even grinding suitable.
  • the secondary edge length is one important parameter of the grinding. It is calculated as the total knife length of one Grinding set that moves past the counter knives every second.
  • the specific grinding work 13 is linear Function (curve 13 ') adjusted based on the overflow quantity 14. This approach is based on the assumption that the increase in the sieve residue to a correspondingly larger amount of hard fibers and splinters is to be attributed and that a larger specific grinding work must be carried out to the same extent. Of course, other functions are also possible and through simple experiments determine.
  • the measuring point 9 is used to determine the consistency of the Overflow 3.
  • This easy-to-get signal serves as an indication of a change the amount of solids accumulating in the overflow 3 and solves the control process described out.
  • the W So determined consistency value also to control the grinding performance in the sense of Invention can be used.
  • Fig. 4 shows an application of the method according to the invention, in which the Wet grinding 6 is carried out as a high consistency grinding.
  • the overflow 3 brought to the desired solids content by a thickening 12. That included accumulating water is divided here into the dilution water W for the Material density control circuit (if available) and the dilution water W 'for addition in the ground paper pulp 4.
  • the wet grinding 6 is controlled by Measurement of the amount of substance with a measuring point 11, the value of which in a controller 10 is processed.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)

Abstract

To even out the characteristics of a suspended paper fiber material (1), using a controlled wet grinding (6), the suspended paper fibers are initially separated into fractions by a wet sieve (5) according to size and/or shape and/or flexibility. The amount of solid matter in the overflow (3) is determined, and the overflow is linked to the wet grinder on an increase in the solid content and, on a reduced solid content the overflow is lowered. To smooth out the characteristics of suspended paper fibers, the solid mater in the overflow is measured by density at a constant volume flow. The specific grinding action is proportional to the measured solid content at the overflow. The wet grinder is a perfecting mill, with its capacity set by positioning the grinding units to the grinding effort. It can also be set by a shift in the rotary speed at the same drive torque, so that the specific edge loading is constant. The material density is measured at the overflow, and then controlled by the addition of water on a time constant value. The wet sieve action is in a closed pressure sorter, so that the sieve separates the paper fiber suspension into fractions, so that the stiff and longer fibers and chips pass through the overflow and the more flexible and shorter fibers pass through.

Description

Die Erfindung bezieht sich auf ein Verfahren zur Mahlung eines Papierfaserstoffes gemäß dem Oberbegriff des Anspruchs 1.The invention relates to a method for grinding a paper pulp according to the preamble of claim 1.

Verfahren dieser Art werden bei der Aufbereitung von Papierfaserstoffen zur Papiererzeugung eingesetzt. Eine bevorzugte Anwendung finden sie, wenn der Papierfaserstoff für grafische Papiere, z.B. SC-Papiere oder LWC-Papiere, verwendet werden soll. Solche Sorten sind oft sehr dünn, etwa 50 bis 60 µm und stellen hohe Anforderungen an die optische Qualität. Daher ist es wichtig, eine besonders homogene Blattstruktur und Oberfläche zu erhalten, was voraussetzt, dass auch die Fasern bezüglich ihrer Geometrie besonders homogen sind.Methods of this type are used in the processing of paper pulp Paper production used. You will find a preferred application if the Paper pulp for graphic papers, e.g. SC papers or LWC papers used shall be. Such types are often very thin, around 50 to 60 µm, and are high Optical quality requirements. Therefore, it is important to be particularly homogeneous To maintain leaf structure and surface, which also presupposes the fibers are particularly homogeneous in terms of their geometry.

Als Rohstoffe für solche Sorten kommen entweder native Faserstoffe oder Sekundärfasern, z.B. aus deinktem Altpapier, zum Einsatz. Auch in dem an sich relativ homogen herstellbaren nativen Zellstoff befinden sich vereinzelt gröbere Faserbestandteile oder Splitter, die z.B. durch eine Fraktioniermaschine abgetrennt werden können. Solche Fraktioniermaschinen arbeiten nach dem Prinzip der Nasssiebung. Bei Sekundärfaserstoffen ist ohnehin immer mit größeren Qualitätsschwankungen zu rechnen, die sich nur durch eine aufwendige Stoffaufbereitung ausreichend eliminieren lassen. Daher werden oft am Ende des Aufbereitungsprozesses noch einmal Mahlapparate eingesetzt, welche für eine Vergleichmäßigung des Papierfaserstoffes, insbesondere bezüglich der geometrischen Fasereigenschaften sorgen sollen. Apparate zur Nassmahlung von Papierfaserstoff sind bekannt und werden als Refiner bezeichnet.Either native fibers or come as raw materials for such types Secondary fibers, e.g. made from deinked waste paper. Relative in that too Homogeneously producible native pulp is occasionally coarser Fiber components or splinters, e.g. separated by a fractionating machine can be. Such fractionation machines work on the principle of Wet screening. In the case of secondary fibrous materials it is always larger Quality fluctuations to be expected, which can only be explained by an elaborate Have stock preparation sufficiently eliminated. Therefore, often at the end of the Preparation process once again used grinding apparatus, which for a Uniformity of the paper pulp, especially with regard to the geometric Fiber properties should provide. Apparatus for wet grinding of paper pulp are known and are referred to as refiners.

Aus der US 3,604,646 ist ein Verfahren zur Regelung eines Refiners bekannt, bei dem die diesem zugeführte Stoffmenge aus Stoffdichte und Volumendurchsatz ermittelt wird. Die spezifische Arbeit wird auf einen festgelegten konstanten Wert geregelt.A method for controlling a refiner is known from US Pat. No. 3,604,646 the amount of substance supplied to it is determined from the consistency and volume flow. The specific work is regulated to a fixed constant value.

Die bisher bekannten Verfahren können die eingangs genannten Probleme nicht befriedigend lösen. In vielen Fällen muss eine unerwünscht hohe Weitermahlung in Kauf genommen werden, um eine akzeptable Vergleichmäßigung zu erzielen. Das schwächt nicht nur das Festigkeitspotential der Papierfasern, sondern kostet auch unnötig viel Mahlenergie. Ferner führt es zu einer weiteren Erhöhung des Entwässerungswiderstandes mit negativen Auswirkungen beim Pressen und Trocknen der daraus hergestellten Papierbahn.The previously known methods cannot address the problems mentioned at the outset solve satisfactorily. In many cases, an undesirably high resale must be paid for be taken to achieve an acceptable leveling. That weakens not only the strength potential of the paper fibers, but also costs unnecessarily much Grinding energy. It also leads to a further increase in Dewatering resistance with negative effects when pressing and drying the paper web made from it.

Der Erfindung liegt daher die Aufgabe zu Grunde, ein Verfahren zu schaffen, mit dem sich die Vergleichmäßigung besser, schonender und billiger durchführen lässt.The invention is therefore based on the object of creating a method with which the equalization can be carried out better, more gently and cheaper.

Diese Aufgabe wird durch die im Kennzeichen des Anspruchs 1 genannten Merkmale gelöst.This object is achieved by the features mentioned in the characterizing part of claim 1 solved.

Mit Hilfe des erfindungsgemäßen Verfahrens wird zunächst festgestellt, ob sich im Überlauf einer der Mahlung vorgeschalteten Nasssiebung der Anteil an mahlresistenten Bestandteilen, das sind z.B. Splitter oder Langfasern, ändert. Ein wichtiges Indiz hierfür ist die Feststoffmenge des Überlaufes dieser Nasssiebung, messbar z.B. mit dessen Stoffdichte. Die Wirksamkeit der Mahlanlage wird auf die so festgestellten Schwankungen abgestimmt, indem erfindungsgemäß dabei die spezifische Mahlarbeit erhöht oder gesenkt wird, wenn größere bzw. kleinere Mengen von mahlresistentem Stoff in der zu mahlenden Faserstoffsuspension vorliegen. Dabei wird also berücksichtigt, dass sich eben nicht nur die Menge des zu mahlenden Stoffes, also des Überlaufes, ändert, sondern auch die Zusammensetzung des darin enthaltenen Feststoffes. Mit dieser einfachen Maßnahme kann ganz gezielt der Stoff, der auf Grund seiner Geometrie und Steifigkeit zu Beeinträchtigungen des daraus hergestellten Blattes führen würde, rechtzeitig und ökonomisch nachgemahlen werden. Die spezifische Mahlarbeit ist die auf die Feststoffmenge bezogene übertragene Mahlarbeit nach Abzug der von der Mahlapparatur verbrauchten Leerlaufarbeit.With the aid of the method according to the invention, it is first determined whether there is any Overflow of a wet sieve upstream of the grinding the proportion of grinding resistant Ingredients, e.g. Splinters or long fibers, changes. An important indicator of this is the amount of solids in the overflow of this wet sieving, measurable e.g. With which Consistency. The effectiveness of the grinding plant is based on the so determined Variations matched by the specific grinding work according to the invention is increased or decreased if larger or smaller amounts of meal-resistant Substance is present in the pulp suspension to be ground. So it will takes into account the fact that not only the amount of the substance to be ground, i.e. the Overflow, changes, but also the composition of the contained therein Solid. With this simple measure, the substance that is based on its geometry and rigidity to impair the sheet made from it would lead to timely and economical regrinding. The specific Grinding work is the transferred grinding work after deduction based on the amount of solids the idle work consumed by the grinder.

Die Erfindung und ihre Vorteile werden erläutert und beschrieben an Hand von Zeichnungen. Dabei zeigen:

Fig. 1
ein einfaches Verfahrensschema zur Durchführung des endungsgemäßen Verfahren;
Fig. 2
ein einfaches Diagramm zur Steuerung;
Fig. 3 und 4
jeweils eine Variante.
The invention and its advantages are explained and described with reference to drawings. Show:
Fig. 1
a simple process scheme for performing the method according to the invention;
Fig. 2
a simple diagram for control;
3 and 4
one variant each.

Bei der Durchführung des erfindungsgemäßen Verfahrens gemäß Fig. 1 wird der suspendierte Papierfaserstoff 1 zunächst einer Nasssiebung 5 zugeführt. Diese bildet zwei Fraktionen, nämlich den Durchlauf 2 und den Überlauf 3. In der Regel wird für eine solche Nasssiebung 5 ein Drucksortierer oder Fraktionator verwendet mit einem Siebelement, das einen Teil des zugeführten Papierfaserstoffes 1 auf Grund seiner Größe, Form und/oder Flexibilität abweist. Die Feststoffmenge des in den Überlauf 3 gelangten Stoffes wird an einer Messstelle 9 ermittelt und der Messwert an einen Regler 8 weitergeleitet. Im einfachsten Fall wird der Überlauf 3 unmittelbar der Nassmahlung 6 zugeführt. Die hierzu verwendete regelbare Mahlapparatur enthält einen Antrieb 7 und ist vorzugsweise ein Mahlrefiner. Nach Passieren der Mahlwerkzeuge gelangt der Stoff als gemahlener Papierfaserstoff 4 in die nachfolgenden Aufbereitungsstufen. In günstigen Fällen kann er wieder mit dem Durchlauf 2 der Nasssiebung 5 vermischt werden. Entscheidend bei der Durchführung des erfindungsgemäßen Verfahrens ist, dass die in der Nassmahlung 6 übertragene spezifische Mahlarbeit abgestimmt wird auf die ermittelte Feststoffmenge oder den Feststoffmengenstrom im Überlauf 3. Bei dem hier gezeigten Beispiel wird das Signal des Reglers 8 dazu verwendet, um die Antriebsleistung der Mahlapparatur zu verändern. Bekanntlich besteht die Möglichkeit, den Mahldruck durch entsprechende Positionierung der Mahlgarnituren einzustellen. Eine andere Möglichkeit ist die Drehzahlvariation, welche zwar in der Regel aufwendiger ist, dafür aber die Konstanthaltung der sekundlichen Kantenlänge möglich macht. Die letztgenannte Maßnahme ist besonders gut zur Erhaltung einer gleichmäßigen Ausmahlung geeignet. Die sekundliche Kantenlänge ist bekanntlich eine wichtige Kenngröße der Mahlung. Sie wird errechnet als die gesamte Messerlänge einer Mahlgarnitur, die pro Sekunde an den Gegenmessern vorbeibewegt wird.1, the Suspended paper pulp 1 is first fed to a wet sieve 5. This forms two fractions, namely run 2 and overflow 3. As a rule, for such a wet sieve 5 uses a pressure sorter or fractionator with one Siebelement, which is part of the supplied paper pulp 1 due to its Size, shape and / or flexibility. The amount of solids in the overflow 3 reached material is determined at a measuring point 9 and the measured value to a controller 8 forwarded. In the simplest case, the overflow 3 becomes wet grinding immediately 6 fed. The controllable grinding apparatus used for this contains a drive 7 and is preferably a refiner. After passing the grinding tools, the Material as ground paper pulp 4 in the subsequent processing stages. In In favorable cases, it can be mixed again with the run 2 of the wet screening 5 become. It is crucial when carrying out the method according to the invention that the specific grinding work transferred in the wet grinding 6 is matched to the determined amount of solids or the amount of solids in the overflow 3. In this case Example shown, the signal from the controller 8 is used to the To change the drive power of the grinding equipment. As you know, there is the possibility adjust the grinding pressure by positioning the grinding sets accordingly. Another option is the speed variation, which is usually is more complex, but it is possible to keep the secondary edge length constant makes. The latter measure is particularly good for maintaining one even grinding suitable. As is well known, the secondary edge length is one important parameter of the grinding. It is calculated as the total knife length of one Grinding set that moves past the counter knives every second.

Gemäß dem Diagramm in Fig. 2 wird die spezifische Mahlarbeit 13 in einer linearen Funktion (Kurve 13') bezogen auf die Überlaufmenge 14 verstellt. Diesem Vorgehen liegt die Annahme zu Grunde, dass die Zunahme des Siebrückstandes auf eine entsprechend größere Menge an harten Fasern und Splittern zurückzuführen ist und dass eine im selben Maße größere spezifische Mahlarbeit geleistet werden muss. Natürlich sind auch andere Funktionen möglich und durch einfache Versuche zu ermitteln.According to the diagram in Fig. 2, the specific grinding work 13 is linear Function (curve 13 ') adjusted based on the overflow quantity 14. This approach is based on the assumption that the increase in the sieve residue to a correspondingly larger amount of hard fibers and splinters is to be attributed and that a larger specific grinding work must be carried out to the same extent. Of course, other functions are also possible and through simple experiments determine.

Bei der in Fig. 3 dargestellten Ausgestaltung des Verfahrens wird die Stoffdichte des Zulaufes in die Nassmahlung 6 durch geregelte Zuführung von Wasser W konstant gehalten. In diesem Fall dient die Messstelle 9 der Ermittlung der Stoffdichte des Überlaufes 3. Dieses leicht zu gewinnende Signal dient als Indiz für eine Veränderung der im Überlauf 3 anfallenden Feststoffmenge und löst den beschriebenen Regelvorgang aus. Zwar führt das zu einem veränderten Durchsatz an der der Nassmahlung 6 dienenden Mahlapparatur, eine solche Schwankung ist aber beim Mahlprozess leichter auszugleichen als eine Schwankung der Stoffdichte, die sich beim Verfahren gemäß Fig. 1 einstellt. Neben der Stoffdichteregelung selbst kann der vor Zugabe des Wassers W ermittelte Stoffdichtewert also auch zur Steuerung der Mahlleistung im Sinne der Erfindung verwendet werden.In the embodiment of the method shown in Fig. 3, the consistency of the Feed into the wet grinding 6 by controlled supply of water W constant held. In this case, the measuring point 9 is used to determine the consistency of the Overflow 3. This easy-to-get signal serves as an indication of a change the amount of solids accumulating in the overflow 3 and solves the control process described out. This leads to a changed throughput at the wet grinding 6 serving grinding apparatus, such a fluctuation is easier in the grinding process to compensate as a fluctuation in the consistency which occurs in the method according to FIG. 1 sets. In addition to the material density control itself, the W So determined consistency value also to control the grinding performance in the sense of Invention can be used.

Fig. 4 zeigt einen Anwendungsfall des erfindungsgemäßen Verfahrens, bei dem die Nassmahlung 6 als Hochkonsistenzmahlung durchgeführt wird. Bekanntlich kann mit einer Hochkonsistenzmahlung das Festigkeitspotential des Papierfaserstoffes besonders gut und ohne nennenswerte Faserkürzung genutzt werden. Hierzu wird der Überlauf 3 durch eine Eindickung 12 auf den gewünschten Feststoffgehalt gebracht. Das dabei anfallende Wasser wird hier aufgeteilt in das Verdünnungswasser W für den Stoffdichte-Regelkreislauf (falls vorhanden) und das Verdünnungswasser W' zur Zugabe in den gemahlenen Papierfaserstoff 4. Die Regelung der Nassmahlung 6 erfolgt durch Messung der Stoffmenge mit einer Messstelle 11, deren Wert in einem Regler 10 verarbeitet wird.Fig. 4 shows an application of the method according to the invention, in which the Wet grinding 6 is carried out as a high consistency grinding. As you know, with a high consistency grinding especially the strength potential of the paper pulp can be used well and without significant fiber shortening. The overflow 3 brought to the desired solids content by a thickening 12. That included accumulating water is divided here into the dilution water W for the Material density control circuit (if available) and the dilution water W 'for addition in the ground paper pulp 4. The wet grinding 6 is controlled by Measurement of the amount of substance with a measuring point 11, the value of which in a controller 10 is processed.

Claims (7)

Verfahren zur Vergleichmäßigung der Eigenschaften eines suspendierten Papierfaserstoffes (1) mit Hilfe einer in einer regelbaren Mahlapparatur durchgeführten Nassmahlung (6),
dadurch gekennzeichnet, dass der suspendierte Papierfaserstoff (1) zunächst in einer Nasssiebung (5) auf Grund seiner Größe und/oder Form und/oder Flexibilität fraktioniert wird,
dass die Feststoff-Menge des dabei in den Überlauf (3) gelangten Stoffes ermittelt wird und
dass anschließend der Überlauf (3) der Nassmahlung (6) zugeführt wird,
wobei die spezifische Mahlarbeit der Nassmahlung (6) bei steigender Feststoffmenge des Überlaufes (3) erhöht und bei sinkender Feststoffmenge des Überlaufes (3) abgesenkt wird.
Method for equalizing the properties of a suspended paper pulp (1) with the help of wet grinding (6) carried out in a controllable grinding apparatus,
characterized in that the suspended paper pulp (1) is first fractionated in a wet screening (5) due to its size and / or shape and / or flexibility,
that the amount of solids of the substance that has entered the overflow (3) is determined and
that the overflow (3) is then fed to the wet grinding (6),
the specific grinding work of the wet grinding (6) being increased as the amount of solids in the overflow (3) increases and decreasing as the amount of solids in the overflow (3) decreases.
Verfahren nach Anspruch 1,
dadurch gekennzeichnet, dass der Feststoffmengenstrom des Überlaufes (3) durch Messung von dessen Stoffdichte bei konstant gehaltenem Volumenstrom ermittelt wird.
Method according to claim 1,
characterized in that the solids flow rate of the overflow (3) is determined by measuring its bulk density with the volume flow kept constant.
Verfahren nach Anspruch 1 oder 2,
dadurch gekennzeichnet, dass die spezifische Mahlarbeit nach einer linearen Funktion in Abhängigkeit vom im Überlauf (3) ermittelten Feststoffmengenstrom eingestellt wird.
The method of claim 1 or 2,
characterized in that the specific grinding work is set according to a linear function as a function of the solids flow rate determined in the overflow (3).
Verfahren nach Anspruch 1, 2 oder 3,
dadurch gekennzeichnet, dass als Mahlapparatur ein Mahlrefiner verwendet und dass dessen Leistung durch Positionieren der Mahlwerkzeuge eingestellt wird, um die spezifische Mahlarbeit anzupassen.
The method of claim 1, 2 or 3,
characterized in that a grinding refiner is used as the grinding apparatus and that its output is adjusted by positioning the grinding tools in order to adapt the specific grinding work.
Verfahren nach einem der Ansprüche 1 bis 3,
dadurch gekennzeichnet, dass als Mahlapparatur ein Mahlrefiner verwendet wird und dass dessen Mahlleistung durch Drehzahländerung bei gleichem Antriebsmoment geregelt wird, so dass die spezifische Kantenbelastung konstant bleibt.
Method according to one of claims 1 to 3,
characterized in that a grinding refiner is used as the grinding apparatus and that its grinding capacity is regulated by changing the speed at the same drive torque, so that the specific edge load remains constant.
Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, dass die Stoffdichte des Überlaufes (3) gemessen und danach durch geregelte Zugabe von Wasser (W) auf einen zeitlich konstanten Wert eingeregelt wird.
Method according to one of the preceding claims,
characterized in that the consistency of the overflow (3) is measured and then regulated by a controlled addition of water (W) to a constant value over time.
Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, dass die Nasssiebung (5) in einem geschlossenen Drucksortierer durchgeführt wird, und zwar in der Weise, dass das darin befindliche Siebelement den suspendierten Papierfaserstoff (1) so fraktioniert, dass im Überlauf steifere Fasern, längere Fasern und Splitter angereichert werden und im Durchlauf flexiblere und kürzere Fasern.
Method according to one of the preceding claims,
characterized in that the wet sieving (5) is carried out in a closed pressure sorter, in such a way that the sieve element therein fractionates the suspended paper pulp (1) in such a way that stiff fibers, longer fibers and splinters are enriched in the overflow and in Pass through more flexible and shorter fibers.
EP01124186A 2000-11-21 2001-10-11 Process for milling a fibrous material Expired - Lifetime EP1209282B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10057682 2000-11-21
DE10057682A DE10057682A1 (en) 2000-11-21 2000-11-21 To smooth out the characteristics of suspended paper fibers, the suspension is separated into fractions at a wet sieve followed by wet grinding, with measurements at the overflow of the density of solids to set the grinding action

Publications (2)

Publication Number Publication Date
EP1209282A1 true EP1209282A1 (en) 2002-05-29
EP1209282B1 EP1209282B1 (en) 2006-05-03

Family

ID=7664071

Family Applications (1)

Application Number Title Priority Date Filing Date
EP01124186A Expired - Lifetime EP1209282B1 (en) 2000-11-21 2001-10-11 Process for milling a fibrous material

Country Status (3)

Country Link
EP (1) EP1209282B1 (en)
AT (1) ATE325223T1 (en)
DE (2) DE10057682A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008087107A1 (en) * 2007-01-17 2008-07-24 Voith Patent Gmbh Method for the production of high quality paper

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1874999A1 (en) * 2005-04-15 2008-01-09 Voith Patent GmbH Method for preparing paper-fibre raw material

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3604646A (en) * 1969-12-10 1971-09-14 Beloit Corp Mass rate control system for paper stock refiners
US4562969A (en) * 1984-03-05 1986-01-07 Mooch Domsjo Aktiebolag Process for preparing groundwood pulp as short fiber and long fiber fractions
DE19808355A1 (en) * 1998-02-27 1999-09-02 Voith Sulzer Papiertech Patent Paper fiber suspension grinding operation for papermaking fibers
WO2000031335A1 (en) * 1998-11-19 2000-06-02 Valmet Fibertech Ab Upgrading of tmp to an sc/lwc quality

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3604646A (en) * 1969-12-10 1971-09-14 Beloit Corp Mass rate control system for paper stock refiners
US4562969A (en) * 1984-03-05 1986-01-07 Mooch Domsjo Aktiebolag Process for preparing groundwood pulp as short fiber and long fiber fractions
DE19808355A1 (en) * 1998-02-27 1999-09-02 Voith Sulzer Papiertech Patent Paper fiber suspension grinding operation for papermaking fibers
WO2000031335A1 (en) * 1998-11-19 2000-06-02 Valmet Fibertech Ab Upgrading of tmp to an sc/lwc quality

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008087107A1 (en) * 2007-01-17 2008-07-24 Voith Patent Gmbh Method for the production of high quality paper

Also Published As

Publication number Publication date
ATE325223T1 (en) 2006-06-15
DE50109684D1 (en) 2006-06-08
DE10057682A1 (en) 2002-05-23
EP1209282B1 (en) 2006-05-03

Similar Documents

Publication Publication Date Title
DE60022212T2 (en) METHOD FOR PRODUCING PAPER OR PAPER
DE2701737A1 (en) PROCEDURES FOR PROCESSING AND CLEANING FIBER MATERIAL AND SYSTEM FOR CARRYING OUT SUCH A PROCESS
DE69923603T2 (en) RECYCLING TMP FIBROUS TO SC / LWC QUALITY
EP0908560A1 (en) Coated roll printing paper suitable for printing with cold-set links
DE10296378B4 (en) Method and arrangement for controlling a short circulation in a paper machine or the like
WO2009000348A1 (en) Method of processing waste paper
EP2851466B1 (en) Operating method for a material preparation
DE60119921T2 (en) METHOD FOR CONTROLLING THE PULP QUALITY
EP1209282B1 (en) Process for milling a fibrous material
DE102008063785A1 (en) Process for the treatment of waste paper-containing raw materials to form a fibrous suspension suitable for the production of graphic papers
DE2818660C2 (en)
EP1403422A1 (en) Process for treating waste paper
DE60214139T2 (en) METHOD OF CHECKING THE SORTING QUALITY BY MEANS OF FLOW RANGE AND CONSISTENCY OF THE SEMI-FINISHED SUBSTANCE
EP1247892B1 (en) Treatment of wood-containing waste paper
DE69907442T2 (en) METHOD AND DEVICE FOR THE TREATMENT OF FIBER SUSPENSIONS CONTAINING MINERALS, LIKE COATED WASTE PAPER, IN THE PRODUCTION OF PAPER
DE4417503C2 (en) Fiber material from paper processing
DE10218265C1 (en) Controlling fines concentration in waste paper suspensions, separates two streams from washer for direct return and adjustment of fines content
WO2012123529A1 (en) Method and device for controlling the filtering performance of a filter device
DE3822783A1 (en) METHOD FOR CONTROLLING THE ADDITION OF RETENTION AGENTS IN PAPER PRODUCTION
DE4031310C2 (en) Process for the production of at least two types of aqueous substance suspensions
EP1262594B1 (en) Process for separating specified materials from an aqueous fibrous material suspension
EP1874999A1 (en) Method for preparing paper-fibre raw material
DE69911979T2 (en) METHOD AND SYSTEM FOR SCREENING CHIPS
EP1070783B1 (en) Process to optimize the dosage of fixing agent for coated broke pulp
DE19928488C1 (en) Process for the meterable dilution of the fiber suspension in or before a headbox of a paper machine

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: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

17P Request for examination filed

Effective date: 20021129

AKX Designation fees paid

Designated state(s): AT DE FI

17Q First examination report despatched

Effective date: 20050203

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 DE FI

REF Corresponds to:

Ref document number: 50109684

Country of ref document: DE

Date of ref document: 20060608

Kind code of ref document: P

RAP2 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: VOITH PATENT GMBH

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

26N No opposition filed

Effective date: 20070206

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

Ref country code: DE

Payment date: 20071025

Year of fee payment: 7

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

Ref country code: AT

Payment date: 20071015

Year of fee payment: 7

Ref country code: FI

Payment date: 20071015

Year of fee payment: 7

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 NON-PAYMENT OF DUE FEES

Effective date: 20081011

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: 20090501

Ref country code: AT

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

Effective date: 20081011