ES2225318T3 - PROCEDURE FOR THE DISPERSION OF A PAPER FIBER MATERIAL AS WELL AS INSTALLATION TO PERFORM THE PROCEDURE. - Google Patents
PROCEDURE FOR THE DISPERSION OF A PAPER FIBER MATERIAL AS WELL AS INSTALLATION TO PERFORM THE PROCEDURE.Info
- Publication number
- ES2225318T3 ES2225318T3 ES01103044T ES01103044T ES2225318T3 ES 2225318 T3 ES2225318 T3 ES 2225318T3 ES 01103044 T ES01103044 T ES 01103044T ES 01103044 T ES01103044 T ES 01103044T ES 2225318 T3 ES2225318 T3 ES 2225318T3
- Authority
- ES
- Spain
- Prior art keywords
- disperser
- hammers
- fiber material
- hammer cylinder
- dispersion
- 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.)
- Expired - Lifetime
Links
Classifications
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/83—Mixing plants specially adapted for mixing in combination with disintegrating operations
- B01F33/831—Devices with consecutive working receptacles, e.g. with two intermeshing tools in one of the receptacles
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/004—Methods of beating or refining including disperging or deflaking
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/20—Methods of refining
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/20—Methods of refining
- D21D1/30—Disc mills
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/57—Mixing high-viscosity liquids with solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1121—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades pin-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
- B01F27/2711—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with intermeshing elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/836—Mixing plants; Combinations of mixers combining mixing with other treatments
- B01F33/8361—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating
- B01F33/83612—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating by crushing or breaking
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Dispersion Chemistry (AREA)
- Paper (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
Procedimiento para la dispersión de un material de fibras de papel, así como instalación para realizar el procedimiento.Procedure for dispersion of a material of paper fibers, as well as installation to perform the process.
La invención se refiere a un procedimiento para la dispersión de material de fibras de papel según el preámbulo de la reivindicación 1.The invention relates to a method for the dispersion of paper fiber material according to the preamble of claim 1
Los procedimientos del tipo indicado anteriormente se emplean, por ejemplo, para mejorar la calidad del material de fibras que se ha obtenido de papel usado. Se sabe que el material de fibras de papel puede homogeneizarse por dispersión y con ello puede mejorarse fundamentalmente. Para ello se elabora un material de fibras de alta consistencia que presenta un contenido en materia seca entre el 15 y 35%. En muchos casos se dispersa con una temperatura que se sitúa ampliamente por encima de la temperatura ambiente. Las guarniciones del dispersor con las que se realizan procedimientos de este tipo son compactas y tienen una magnífica acción dispersora. No obstante, suponen un flujo homogéneo del material. Dado que el tiempo de estadía entre ellos de la materia sólo es muy corto, no pueden compensarse las irregularidades. La consecuencia sería una dispersión no homogénea.The procedures of the indicated type previously used, for example, to improve the quality of fiber material obtained from used paper. It is known that the Paper fiber material can be homogenized by dispersion and This can be fundamentally improved. To do this, a high consistency fiber material that has a content in dry matter between 15 and 35%. In many cases it is dispersed with a temperature that is widely above the temperature ambient. The gaskets of the disperser with which they are made procedures of this type are compact and have a magnificent dispersing action However, they assume a homogeneous flow of material. Since the time of stay between them of the matter It is only very short, irregularities cannot be compensated. The consequence would be a non-homogeneous dispersion.
En el caso del proceso de espesamiento realizado se seca por presión una parte considerable del agua presente anteriormente en el material de fibras, con lo que, en primer lugar, aumenta fundamentalmente su viscosidad en la dispersión y, en segundo lugar, dado el caso, tiene que calentarse conjuntamente menos agua. Una máquina especialmente económica para el espesamiento es la prensa de extrusión. En el caso de una prensa de extrusión, la suspensión de material de fibras se seca por prensado entre un tornillo sin fin de transporte y una envoltura agujereada que lo rodea, con lo que el agua sale a través de los huecos de la envoltura. El cuerpo prensado o tapón que se forma con ello se expulsa fuera del tornillo sin fin y se parte en trozos parciales. Los trozos parciales son relativamente grandes y, por tanto, conducen a un caudal irregular a través de los aparatos subsiguientes.In the case of the thickening process performed a considerable part of the water present is dried under pressure previously in the fiber material, so, first of all, fundamentally increases its viscosity in the dispersion and, in second, if necessary, it has to be heated together less water. An especially economic machine for thickening It is the extrusion press. In the case of an extrusion press, the suspension of fiber material is dried by pressing between a transport screw and a perforated envelope that surrounds, so that water flows through the gaps of the envelope. The pressed body or plug that forms with it is Eject out of the worm and split into partial pieces. Partial pieces are relatively large and therefore lead to irregular flow through the devices subsequent.
A partir del documento DE 197 12 653 A1 se conoce un dispositivo de dispersión en el que se alimenta directamente el tapón que se origina en una prensa de extrusión. Además, se tritura en una herramienta de fragmentación con rascadores o cuchillas que se encuentran en el conducto de alimentación del dispersor.From document DE 197 12 653 A1 it is known a dispersion device in which the feed is fed directly stopper that originates from an extrusion press. In addition, it is crushed in a fragmentation tool with scrapers or blades that They are located in the feed duct of the disperser.
La tarea de la invención es crear un dispositivo con el que se consiga alimentar a la dispersión el tapón de alta consistencia que llega de la prensa de extrusión, de manera que se garantice una dispersión especialmente uniforme con una alta seguridad de funcionamiento.The task of the invention is to create a device with which the high plug can be fed to the dispersion consistency that comes from the extrusion press, so that it guarantee a particularly uniform dispersion with high operating safety
Esta tarea se soluciona totalmente mediante las características citadas en la parte caracterizadora de la reivindicación 1.This task is completely solved by characteristics cited in the characterizing part of the claim 1.
Con ayuda del nuevo procedimiento es posible elaborar un material de alta consistencia que puede procesarse correctamente en un dispersor. El cilindro de martillos empleado según la invención toma los trozos de tapón comprimidos al prensar el agua y los fracciona, especialmente porque los martillos giratorios actúan conjuntamente con las piezas de impacto que están fijas en el perímetro. Los fragmentos mayores permanecen más tiempo en la zona de tratamiento hasta que puedan pasar, de manera que el flujo de material al dispersor se vuelve muy homogéneo. Entonces se tritura adicionalmente y se arremolina en la zona radialmente interna de las guarniciones del dispersor, con lo que se originan aglomeraciones de fibras muy finas. En caso de que así se desee, la alimentación de vapor se realiza en una zona de calentamiento aguas abajo de las guarniciones para calentar el material a la temperatura necesaria. Además, como consecuencia de la trituración llevada a cabo es suficiente con un tiempo de calentamiento relativamente corto. La verdadera dispersión, es decir, la modificación de las propiedades del material, tiene lugar en la zona de dispersión de las guarniciones, que está adyacente aguas abajo.With the help of the new procedure it is possible make a high consistency material that can be processed correctly in a disperser. The hammer cylinder used according to the invention it takes the compressed plug pieces when pressed water and split them, especially because the hammers swivels act in conjunction with the impact pieces that are fixed on the perimeter. Larger fragments stay longer in the treatment area until they can pass, so that the material flow to the disperser becomes very homogeneous. Then additionally crush and swirl radially in the area internal of the disperser fittings, with which they originate agglomerations of very fine fibers. If so desired, the Steam feeding is done in a water heating zone below the fittings to heat the material to the temperature necessary. In addition, as a result of the crushing taken to out is enough with a relatively warm up time short. The true dispersion, that is, the modification of material properties, takes place in the dispersion zone of the trimmings, which is adjacent downstream.
La invención y sus ventajas se explican mediante dibujos. A este respecto, muestran:The invention and its advantages are explained by drawings. In this regard, they show:
la figura 1, de forma esquemática, la instalación para realizar el procedimiento según la invención;Figure 1, schematically, the installation to perform the process according to the invention;
la figura 2, otra vista de una instalación similar;Figure 2, another view of an installation Similary;
la figura 3, de forma esquemática, el dispositivo de distribución según la invención.Figure 3, schematically, the device of distribution according to the invention.
La figura 1 muestra detalles de una instalación que es especialmente adecuada para realizar el procedimiento según la invención. En la parte superior de la imagen se observa la prensa 8 de extrusión en la que, a partir del material S1 acuoso de fibras de papel, se seca por presión una gran parte del agua W. Con ello se genera un material S2 de fibras compacto altamente consistente que se rompe en grandes trozos al final de la prensa de extrusión y cae hacia abajo en un pequeño pozo 10 de caída en el dispositivo 9 de distribución que se encuentra debajo. Éste incluye como componente fundamental un cilindro 1 de martillos con martillos 2 fijados en él y movidos de forma giratoria. El cilindro 1 de martillos trabaja conjuntamente con piezas 3 de impacto que se están fijas, aplicadas en la periferia, es decir, en la carcasa del dispositivo 9 de distribución, de manera que puede producirse la acción ya descrita. Este tipo de piezas de impacto pueden ser, tal como se muestra aquí, en forma de varillas, con alineación radial o, por ejemplo, también cúbicas o en forma de discos. A través de una tolva 11 de caída, el material S3 de fibras altamente consistente tratado de esta manera llega a un tornillo 7 sin fin de transporte que está instalado directamente antes del dispersor 4. Este tornillo 7 sin fin impulsa el material S3 de fibras a la zona central del dispersor 4, de manera que llega entre las guarniciones 5 y 6 del dispersor y se dispersa. Las guarniciones presentan hileras dentadas concéntricas que se ensamblan axialmente entre sí, las cuales se desplazan entre sí con una pequeña separación. Por tanto, el rotor y el estator no se presionan uno contra el otro. Este tipo de guarniciones del dispersor son especialmente efectivas, sin embargo, requieren un flujo de material lo más uniforme posible para la dispersión homogénea.Figure 1 shows details of an installation which is especially suitable for performing the procedure according to the invention. In the upper part of the image you can see the press 8 extrusion in which, from the aqueous fiber material S1 of paper, a large part of the W water is dried under pressure. generates a highly consistent compact fiber S2 material that it breaks into large pieces at the end of the extrusion press and falls down in a small pit 10 of fall in the device 9 of distribution below. This includes as a component fundamental a hammer cylinder 1 with hammers 2 fixed on it and moved in a rotating way. Hammer cylinder 1 works together with impact parts 3 that are fixed, applied on the periphery, that is, on the housing of the device 9 of distribution, so that the action already described can occur. These types of impact pieces can be, as shown here, in the form of rods, with radial alignment or, for example, also cubic or in the form of discs. Through a drop hopper 11, the highly consistent fiber S3 material treated in this way reaches a screw 7 endless transport that is installed directly before the disperser 4. This worm 7 drives the fiber material S3 to the central zone of the disperser 4, of way that arrives between the fittings 5 and 6 of the disperser and it scattered The trimmings have concentric serrated rows which are axially assembled with each other, which move between Yes with a small separation. Therefore, the rotor and the stator do not they press against each other. This type of trimmings dispersers are especially effective, however, they require a material flow as uniform as possible for dispersion homogeneous
En muchos casos se lleva el material para la dispersión a una alta temperatura, para lo cual está presente aquí una alimentación 12 de vapor. Con ayuda de esta alimentación 12 de vapor se alimenta vapor D de agua caliente en el espacio entre las dos guarniciones del dispersor. De forma conveniente esto tiene lugar en una zona 13 caliente en forma de anillo que se encuentra radialmente dentro de la verdadera zona 14 del dispersor de las guarniciones. En la zona 14 del dispersor actúan las hileras dentadas que se ensamblan unas en otras, de manera que el material de fibras de papel de alta consistencia se dispersa de forma conocida en sí misma. Luego, el material S4 de fibras de papel dispersado sale del dispersor a través de una abertura del fondo.In many cases the material for the high temperature dispersion, for which it is present here a 12 steam feed. With the help of this food 12 of steam feeds steam D of hot water in the space between the two disperser fittings. Conveniently this has place in a hot ring-shaped zone 13 that is radially within the true zone 14 of the disperser of the fittings. In rows 14 of the disperser the rows act teeth that are assembled into each other, so that the material of high consistency paper fibers disperses so known in itself. Then, the S4 paper fiber material dispersed leaves the disperser through an opening of the background.
La figura 2 ilustra la disposición de los dispositivos empleados para realizar el procedimiento en otra vista, y, concretamente, en la dirección de observación del dispersor 4. Empleando un dispositivo 4 de distribución construido según las reivindicaciones se consigue no sólo una distribución óptima del material que se presenta en la prensa 8 de extrusión, sino también la ventaja de una disposición que permite ahorrar espacio. En el caso de la realización industrial del procedimiento debe seleccionarse una prensa 8 de extrusión con un diámetro del eje relativamente grande debido concretamente a las cantidades relativamente grandes. El material de fibras que se presenta al final del eje sin fin no es fluido y, por tanto, debería poder caer hacia abajo verticalmente de forma fundamentalmente libre. La posición del dispositivo 9 de distribución de la forma indicada permite captar el material de fibras que se presenta en todo el diámetro de la prensa 8 de extrusión y, tras el tratamiento correspondiente, desviarlo al pozo 10 de caída que se dispone debajo. Por tanto, es apropiado disponer el cilindro 1 de martillos en ángulo recto respecto a la dirección principal de transporte de la prensa 8 de extrusión. Esta unidad, es decir, el eje de tornillo sin fin y el dispositivo 9 de distribución, pueden disponerse entonces de forma conveniente en relación con el dispersor 4, en función de las condiciones espaciales.Figure 2 illustrates the arrangement of the devices used to perform the procedure in another view, and, specifically, in the direction of observation of the disperser 4. Using a distribution device 4 constructed according to the claims are achieved not only an optimal distribution of material presented in the extrusion press 8 but also the advantage of a provision that saves space. At case of industrial performance of the procedure must select an extrusion press 8 with a shaft diameter relatively large due specifically to the quantities relatively large The fiber material presented to the End of the endless shaft is not fluid and therefore should be able to fall down vertically fundamentally free. The position of the distribution device 9 as indicated allows to capture the fiber material that is presented throughout the diameter of extrusion press 8 and, after treatment corresponding, divert it to the well 10 that is available below. Therefore, it is appropriate to arrange the hammer cylinder 1 at right angles to the main transport direction of The extrusion press 8. This unit, that is, the screw shaft endless and the distribution device 9, can be arranged then conveniently in relation to the disperser 4, in function of spatial conditions.
La figura 3 muestra la estructura básica del dispositivo 9 de distribución con el cilindro 1 de martillos. El cilindro 1 de martillos con longitud L incluye un número de martillos 2 cuyos extremos más exteriores giran en un círculo con el diámetro D. Éstos actúan conjuntamente con las piezas 3 de impacto fijadas en la carcasa 15 de este dispositivo. Con ello se consigue que el material de fibras de papel de trozos gruesos que se presenta primero se triture. La trituración tiene lugar ya con una acción de fuerza relativamente reducida, lo que debe conducir a que sólo este comprimido el material de fibras de papel que se presenta aquí y a que sólo lleve a disolver nuevamente este compuesto. Esto no puede compararse, por ejemplo, con el papel usado presente en bandas húmedas, tal como se trata, por ejemplo, en una deshilachadora. De forma conveniente, las separaciones a entre las piezas 3 de impacto fijas contiguas axialmente se seleccionan de tal manera que el material S2 de fibras de alta consistencia se calibra en medio, de manera que se evita, por tanto, el paso de trozos de material triturados todavía demasiado poco. Las partículas que han pasado a través tienen entonces una medida máxima definida en una dirección de estiramiento de, por ejemplo, 30 mm. Eventualmente, la separación a debe determinarse mediante un ensayo sencillo. También podría ser ventajoso hacerla variable, de manera que la máquina pueda ajustarse a diferentes requisitos. También la separación b axial entre los martillos 2 y las piezas 3 de impacto que se encuentran tiene una intensa influencia sobre la acción de trituración de este dispositivo. Ésta es de forma ventajosa entre 5 y 20 mm.Figure 3 shows the basic structure of the distribution device 9 with hammer cylinder 1. He hammer cylinder 1 with length L includes a number of 2 hammers whose outermost ends rotate in a circle with the diameter D. These act together with the impact pieces 3 fixed in the casing 15 of this device. This is achieved that the thick-cut paper fiber material presented It is crushed first. Crushing already takes place with an action of relatively reduced force, which should lead to only this compressed the paper fiber material presented here and to that only leads to dissolve this compound again. This can not compare, for example, with the used paper present in bands wet, as it is treated, for example, in a fraying machine. From convenient way, the separations between the impact pieces 3 axially contiguous fixed are selected such that the S2 material of high consistency fibers is calibrated in medium, of so that the passage of pieces of material is therefore avoided crushed yet too little. The particles that have passed to through then have a maximum measure defined in one direction of stretching of, for example, 30 mm. Eventually, the separation a must be determined by a simple test. It could also be advantageous to make it variable, so that the machine can be adjusted to different requirements. Also the axial separation b between hammers 2 and the impact pieces 3 found have a intense influence on the crushing action of this device. This is advantageously between 5 and 20 mm.
La forma de los martillos 2 o las piezas 3 de impacto ha de seleccionarse de forma conveniente. Aquí se muestran formas muy simples para mostrar únicamente el funcionamiento. También pueden tener, por ejemplo, forma de hoz o estar colocados de forma inclinada vistos en la dirección perimetral. También puede concebirse dotarlos de blindajes sin desgaste para prolongar su vida útil.The shape of hammers 2 or pieces 3 of impact has to be selected conveniently. Here are shown Very simple ways to show only the operation. They can also be, for example, sickle-shaped or placed inclined shape seen in the perimeter direction. also can conceive to provide them with armor without wear to prolong their life Useful.
Claims (19)
- 1.1.1.1.
- disposición de un material (S1) acuoso de fibras de papel;disposition of a material (S1) aqueous paper fibers;
- 1.2.1.2.
- secado por presión de una parte del agua (W) para formar un material (S2) de fibras de papel con trozos gruesos de alta consistencia;pressure drying of a part of the water (W) to form a material (S2) of paper fibers with pieces thick of high consistency;
- 1.3.1.3.
- transportar el material de fibras de papel de alta consistencia a un dispersor (4);transport the fiber material of high consistency paper to a disperser (4);
- 1.4.1.4.
- dispersión con un dispersor (2) que presenta como mínimo dos guarniciones (5, 6) del dispersor, las cuales contienen en cada caso varias hileras dentadas que se engranan unas dentro de otras y que se mueven relativamente entre sí con una separación, con lo que se dispersa el material de fibras de papel altamente consistente,dispersion with a disperser (2) that It has at least two trimmings (5, 6) of the disperser, the which contain in each case several serrated rows that meshed within each other and that move relative to each other with a separation, thereby dispersing the fiber material of highly consistent paper,
- 1.5.1.5.
- el material (S2) de fibras de trozos gruesos con alta consistencia se proporciona antes de la dispersión en el área de acción de un cilindro (1) de martillos giratorio, el cual está dotado de martillos (2) giratorios que actúan conjuntamente con piezas (3) de impacto periféricas que están fijas, de manera que tiene lugar un aflojamiento y una compensación del material (S2) de fibras altamente consistente.he material (S2) of coarse-cut fibers with high consistency provides before dispersion in the area of action of a rotating hammer cylinder (1), which is equipped with rotary hammers (2) acting together with parts (3) of peripheral impacts that are fixed, so that a loosening and compensation of fiber material (S2) highly consistent
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10018262A DE10018262A1 (en) | 2000-04-13 | 2000-04-13 | Process for dispersing a paper pulp and plant for carrying out the process |
DE10018262 | 2000-04-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2225318T3 true ES2225318T3 (en) | 2005-03-16 |
Family
ID=7638558
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES01103044T Expired - Lifetime ES2225318T3 (en) | 2000-04-13 | 2001-02-09 | PROCEDURE FOR THE DISPERSION OF A PAPER FIBER MATERIAL AS WELL AS INSTALLATION TO PERFORM THE PROCEDURE. |
Country Status (7)
Country | Link |
---|---|
US (1) | US20010037866A1 (en) |
EP (1) | EP1147805B1 (en) |
JP (1) | JP2001348791A (en) |
AT (1) | ATE274370T1 (en) |
CA (1) | CA2344103A1 (en) |
DE (2) | DE10018262A1 (en) |
ES (1) | ES2225318T3 (en) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI111393B (en) * | 2001-12-18 | 2003-07-15 | Metso Paper Inc | Wrecking system for a paper machine or similar |
FI112875B (en) * | 2001-12-18 | 2004-01-30 | Metso Paper Inc | Preliminary arrangements for a paper machine or equivalent |
FI120551B (en) * | 2001-12-19 | 2009-11-30 | Metso Paper Inc | Projection arrangement of a paper machine or equivalent |
AT411604B (en) * | 2002-03-27 | 2004-03-25 | Andritz Ag Maschf | METHOD AND DEVICE FOR DISPERSING A PAPER FIBER FIBER |
CN100347374C (en) * | 2005-08-30 | 2007-11-07 | 天津科技大学 | Fibre detaching apparatus with high shearing |
DE202006008820U1 (en) | 2006-06-03 | 2006-08-17 | Frymakoruma Ag | Apparatus for dispersing and/or homogenizing liquids comprises processing unit comprising two independently rotating concentric toothed wheels driven on horizontal shafts |
AT507837B1 (en) * | 2008-12-29 | 2010-10-15 | Andritz Ag Maschf | METHOD AND DEVICE FOR DRAINING AND DISPERSING A FIBROUS MATERIAL |
DE202014101719U1 (en) * | 2013-04-12 | 2014-04-29 | Valmet Technologies, Inc. | dispersant |
DE102013226597A1 (en) * | 2013-12-19 | 2015-06-25 | Voith Patent Gmbh | Disperser-heating |
US20220062837A1 (en) * | 2018-12-21 | 2022-03-03 | Nanorial Technologies Ltd. | Apparatus, methods, and systems for mixing, dispersing substances |
CN110075746A (en) * | 2019-04-23 | 2019-08-02 | 安徽华文塑胶科技有限公司 | A kind of heavy metal-polluted soil stabilizer treatment system and processing method |
CN111608000A (en) * | 2020-05-26 | 2020-09-01 | 陈爱丽 | Paper recycling device capable of introducing shredded paper once based on paper volume change |
FI20225817A1 (en) * | 2022-09-21 | 2024-03-22 | Valmet Technologies Oy | Disperger |
CN115556265B (en) * | 2022-10-10 | 2024-09-10 | 江苏亨睿弗劳恩新材料研发有限公司 | Chopped fiber dispersing device and dispersing method |
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GB241053A (en) * | 1924-12-23 | 1925-10-15 | Edward Benton Fritz | Improvements in hydrating beating and refining machine |
DE670057C (en) * | 1936-09-22 | 1939-01-11 | Kuehnle Kopp Kausch Ag | Feeding device for loosening, emulsifying and stirring devices |
FR978530A (en) * | 1942-12-17 | 1951-04-16 | Improvements to machines for emulsifying and refining pasty materials | |
SE7609972L (en) * | 1976-09-09 | 1978-03-10 | Sunds Ab | DEVICE FOR REFINING FIBER MATERIAL |
JPS5430907A (en) * | 1977-08-10 | 1979-03-07 | Kobayashi Seisakusho | Beater for waste paper |
US5200038A (en) * | 1985-08-28 | 1993-04-06 | International Paper Company | Pulp refiner with fluidizing inlet |
US4820381A (en) * | 1987-02-25 | 1989-04-11 | Internationa Paper Company | Pulp refiner with fluidizing inlet |
SE461919B (en) * | 1988-08-30 | 1990-04-09 | Cellwood Machinery Ab | SET FOR TREATMENT OF TREASURY FIBER, SEPARATELY CONTAINING RECOVERY PAPER, AND DISPERSE BEFORE IMPLEMENTATION OF THE PROCEDURE |
JP2964751B2 (en) * | 1991-12-18 | 1999-10-18 | 王子製紙株式会社 | Pulping method of pressure-sensitive adhesive waste paper |
DE4233286A1 (en) * | 1992-10-02 | 1994-04-07 | Voith Gmbh J M | Process for the treatment of printed waste paper |
JPH08127988A (en) * | 1994-10-28 | 1996-05-21 | Chuetsu Pulp Kogyo Kk | Substratum for label and method for recycling the same |
SE506803C2 (en) * | 1996-07-25 | 1998-02-16 | Cellwood Machinery Ab | Method and plant for bleaching recycled pulp |
DE19712653C2 (en) * | 1997-03-26 | 2002-10-24 | Voith Paper Fiber Systems Gmbh | Method and device for dispersing a waste paper pulp |
-
2000
- 2000-04-13 DE DE10018262A patent/DE10018262A1/en not_active Withdrawn
-
2001
- 2001-02-09 ES ES01103044T patent/ES2225318T3/en not_active Expired - Lifetime
- 2001-02-09 AT AT01103044T patent/ATE274370T1/en not_active IP Right Cessation
- 2001-02-09 EP EP01103044A patent/EP1147805B1/en not_active Expired - Lifetime
- 2001-02-09 DE DE50103371T patent/DE50103371D1/en not_active Expired - Fee Related
- 2001-04-11 JP JP2001113172A patent/JP2001348791A/en not_active Ceased
- 2001-04-12 CA CA002344103A patent/CA2344103A1/en not_active Abandoned
- 2001-04-12 US US09/832,873 patent/US20010037866A1/en not_active Abandoned
Also Published As
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JP2001348791A (en) | 2001-12-21 |
DE50103371D1 (en) | 2004-09-30 |
EP1147805B1 (en) | 2004-08-25 |
DE10018262A1 (en) | 2001-10-18 |
CA2344103A1 (en) | 2001-10-13 |
US20010037866A1 (en) | 2001-11-08 |
EP1147805A1 (en) | 2001-10-24 |
ATE274370T1 (en) | 2004-09-15 |
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