EP0886001B1 - Verfahren und Vorrichtung zur Dispergierung eines Papierfaserstoffes - Google Patents
Verfahren und Vorrichtung zur Dispergierung eines Papierfaserstoffes Download PDFInfo
- Publication number
- EP0886001B1 EP0886001B1 EP98101955A EP98101955A EP0886001B1 EP 0886001 B1 EP0886001 B1 EP 0886001B1 EP 98101955 A EP98101955 A EP 98101955A EP 98101955 A EP98101955 A EP 98101955A EP 0886001 B1 EP0886001 B1 EP 0886001B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- rotor
- teeth
- dispersing
- stator
- fine
- 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
- 238000000034 method Methods 0.000 title claims abstract description 30
- 239000000835 fiber Substances 0.000 title claims description 18
- 239000002002 slurry Substances 0.000 title claims 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 23
- 239000000463 material Substances 0.000 claims abstract description 16
- 239000006185 dispersion Substances 0.000 claims description 12
- 238000011144 upstream manufacturing Methods 0.000 claims 2
- 238000006073 displacement reaction Methods 0.000 claims 1
- 239000002245 particle Substances 0.000 claims 1
- 239000002657 fibrous material Substances 0.000 abstract description 9
- 238000010298 pulverizing process Methods 0.000 abstract 7
- 239000004744 fabric Substances 0.000 description 9
- 229920001131 Pulp (paper) Polymers 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000008719 thickening Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 241000237858 Gastropoda Species 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 101100117236 Drosophila melanogaster speck gene Proteins 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000994 depressogenic effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- 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
- D21B1/14—Disintegrating in mills
-
- 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
- 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
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71775—Feed mechanisms characterised by the means for feeding the components to the mixer using helical screws
-
- 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
- D21D1/006—Disc mills
-
- 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
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/912—Radial flow
- B01F2025/9121—Radial flow from the center to the circumference, i.e. centrifugal flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/47—Mixing of ingredients for making paper pulp, e.g. wood fibres or wood pulp
-
- 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
- B01F27/27—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
Definitions
- the invention relates to a method for dispersing paper pulp according to the Preamble of claim 1.
- Procedure of the above Be e.g. needed to improve the quality of fiber, which was obtained from waste paper. It is known that pulp by Dispersing can be homogenized and thereby significantly improved. There in many cases a fiber material is used that has a dry content between 15 and has 35% and has been brought to a temperature far above that Ambient temperature. It makes sense to heat up when the Fibrous material already has the consistency required for dispersion. With this Thickening process becomes a considerable part of what was previously in the pulp Water depressed, which firstly makes its viscosity essential when dispersing increases and secondly less water needs to be heated. The most important Thickening machines are screw presses and screen presses.
- the fibrous suspension is introduced and pressed between a screen and a roller or between two screens so that the water emerges. This creates a moist fibrous web.
- this membrane has a weight per unit area of between 500 and 2000 g / m 2 , although values that differ from this can also be useful.
- the wet web is removed from the area of the screen or screens and must then be torn into flat pieces. Although these can easily be brought to the desired temperature, a relatively long heating-up time is required. For example, warm-up times of several minutes have to be accepted, especially if a temperature above 90 ° C is desired.
- the hot crumb is then fed to the disperser. The whole requires a fairly complex system.
- the fiber suspension is between one Conveyor screw and a perforated jacket surrounding it, the Water leaks through the jacket.
- Shredding can e.g. in a shredder screw or a system with counter rotating Rotors are made, which is very expensive.
- a device is already known from WO 96/18769 A1, in which a device with "pulp" specified substance introduced into a screw conveyor and then in a Disk disperser is dispersed. To support the dispersion is in the Center of the disc disperser steam added. The fiber-vapor mixture then travels radially outwards from the center into the actual, between machining zone located on the disperger discs. The substance should be steam can be mixed and crushed and dispersed at the same time. With this known Device should only be able to heat the substance to a limited extent.
- Claim 15 defines an apparatus for performing the method. Preferred embodiments are defined in the dependent claims.
- the highly consistent paper pulp can either be used as a plug or in the form of a loose, just pre-shredded high consistency fabric directly into the clothing of one Dispergers can be entered.
- the fabric is then seen from the direction of flow the first crushing stage of the disperser is detected, crushed and swirled, whereby the fine fiber crumbs arise.
- the material is then cut to the necessary Temperature warmed up, due to the previous intensive comminution a relatively short heating-up time is sufficient
- the actual dispersion i.e.
- the material properties change in the dispersion zone, which changes connects downstream.
- the version shown here is a disperger set with a radial flow of material, with a stator 2 and a rotor 4. In principle, could an axial disperger or kneader can also be used.
- the Disperger 3 shown here is loaded radially inside, for which a first in the center of the rotor 4 Comminution element 5 is attached, which e.g. wing-shaped or cross-shaped Crushing strips 6 can carry.
- the stopper 1 pressed here becomes peeled off or grated and thereby broken up into fine crumbs, but here are not drawn.
- the vapor space 8 is essentially ring-shaped and does not contain any of the mechanical ones Dispersion teeth.
- dispersion is brought about by the fact that Teeth are moved relatively close together at a relatively high speed and the fiber between them is subjected to strong shear forces. This function only has that which adjoins the steam chamber 8 radially further outside Dispersing zone 9. There are then high peripheral speeds of the dispersing teeth possible and advantageous, while those lying radially further inside Crushing bars 6 are slower and therefore the incoming stopper 1 shred gently. The substance is therefore not within the vapor space 8 mechanically dispersed. If necessary, internals 18 (FIG. 4) can be present be that slow down the movement of the circulating fabric and loosen the fabric. The will be explained later.
- Heating steam ST is added via the steam pipes 11 brought into contact with the fiber. He is swirled in the steam room 8 or at least kept loosened so that it is well penetrated by the steam can.
- the heating is essentially achieved by condensation of the steam, i.e. Steam is constantly replenished.
- the make-up improves the swirl and the loosening of the fiber crumbs. After the dispersion, the dispersed falls Fibrous material S 'through outlet 13.
- the vapor space 8 is light due to the plug 1 and the substance in the dispersion zone 9 to seal against the outside world.
- the closure of the dispersion zone 9 is also advantageous by a throttle ring 10 because this controls the degree of filling of the set leaves.
- a throttle ring 10 In connection with the invention is a high and uniform degree of filling particularly advantageous in the dispersion zone 9, because otherwise the outer diameter of the Disperger set should be chosen very large to the specific desired To be able to transfer work to the pulp.
- a throttle ring is e.g. by DE 195 23 704 A1 is known.
- the highly consistent paper pulp is not as compact Grafting, but pre-shredded into a more or less loose form Dispersing device is entered.
- a pre-shredded material falls e.g. when the thickening has been carried out on a screen press, from which the Thickened paper pulp runs out as a wet web.
- Crushing e.g. in a snail
- the fabric becomes so wide pre-crushed that it can be conveyed in screw systems.
- the pre-shredded material is then before entering the Disperger 3 '- as shown here in Fig. 3 - by a feed screw 16 detects and directly into the central inlet of the disperser 3 'performed.
- This feed screw 16 can have a stuffing effect, that is but not necessary to carry out the method according to the invention. Much more it can also be designed as a band screw, which is only on the outside diameter has a helical band 17 and comparatively promotes. With Advantage, the fabric in it can already be preheated, possibly for what existing steam lines 11 'serve. Then the crushing step gentler on fibers and later heating to dispersion temperature is faster. If the fabric is relatively loosely fed into the central inlet of the disperser, it does not offer the support of a solid plug, as shown in Fig. 1. The However, fine comminution is possible because the material is less Radial speed has than the shredding bars 6, which on the Crushing element 5 are attached. Often the primary stator teeth 7 in addition to their slowing effect, they promote comminution.
- the heating steam ST is added on radially outer edge of the steam chamber 8 and thus different than in Fig.1.
- This is supposed to Countercurrent heating can be achieved, which of course is a corresponding Centrifugal field in the steam room 8 provided.
- the steam swirls the crumb in the steam room additionally on. Similar considerations regarding the optimal dam addition locations are also in other configurations, e.g. to start according to FIG. 1.
- Conceivable internals 18 and 18 'are 4 according to which the internals are anchored on the stator side.
- Such Baffles 18, 18 ' can e.g. round, rounded or with baffle edges Be pens.
- the inner row of the dispersing teeth 19 shown here belongs to the rotor.
- the fabric passes between these dispersing teeth and is pressed through the dispersing zone 9. In other cases, it can be advantageous to radially outer the vapor space through a To complete the row of teeth belonging to the stator.
Description
- Fig. 1
- die grundsätzlichen Verfahrensschritte anhand eines erfindungsgemäß ausgestalteten Dispergers;
- Fig. 2a+b
- ein Zerkleinerungselement in 2 Ansichten;
- Fig. 3
- eine Variante mit geänderter Stoffzuführung und geändertem Dampfraum;
- Fig. 4
- Teil des Dampfraumes in Draufsicht, schematisch.
Claims (22)
- Verfahren zur Dispergierung eines Papierfaserstoffes,
welches von einem hochkonsistenten Papierfaserstoff (S) ausgeht,
diesen in einem Zerkleinerungsschritt in feine Faserstoffkrümel umwandelt, und anschließend mit einem gas- bzw. dampfförmigen Heizmedium vermischt und aufheizt und
in einer zwischen Stator (2) und Rotor (4) liegenden Dispergierzone (9) eines Dispergers dispergiert,
dadurch gekennzeichnet, daß der Papierfaserstoff (S) in einen aufgelockerten Zustand versetzt wird,
daß er in einem ringförmigen Dampfraum (8) mit dem Heizmedium vermischt und aufgeheizt wird,
daß er dann in die Dispergierzone (9) geführt wird, in der die Faserstoffkrümel dispergiert werden, und
daß für die Vermischung des Papierfaserstoffes (S) mit dem Heizmedium, für die Aufheizung und für die Dispergierung dieselbe Vorrichtung benutzt wird. - Verfahren nach Anspruch 1,
dadurch gekennzeichnet, daß Zerkleinerungsschritt, Auflockerung, Aufheizung und Dispergierung zwischen Stator (2) und Rotor (4) eines Dispergers durchgeführt werden, wobei Stator (2) und Rotor (4) jeweils mit konzentrischen Zahnreihen versehen sind, und die Zähne axial in die Zwischenräume der Gegengamitur hineinreichen. - Verfahren nach Anspruch 1 oder 2,
dadurch gekennzeichnet, daß die feinen Faserstoffkrümel eine maximale Dicke von höchstens 5 mm haben. - Verfahren nach Anspruch 1, 2 oder 3,
dadurch gekennzeichnet, daß die feinen Faserstoffkrümel eine maximale Längenerstreckung von höchstens 10 mm haben. - Verfahren nach Anspruch 1, 2, 3 oder 4,
dadurch gekennzeichnet, daß die feinen Faserstoffkrümel in dem Heizmedium verwirbelt werden und zumindest während des überwiegenden Teils der erforderlichen Aufheizzeit in dem Wirbelzustand sind. - Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, daß die mittlere Verweilzeit der feinen Faserstoffkrümel im Dampfraum (8) zwischen 0,5 und 3 sec beträgt. - Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, daß das Heizmedium Heizdampf (ST) ist und im radial äußeren Bereich des Dampfraumes (8) zugegeben wird. - Verfahren nach einem der Ansprüche 1 bis 6,
dadurch gekennzeichnet, daß das Heizmedium Heizdampf (ST) ist und im radial inneren Bereich des Dampfraumes (8) zugegeben wird. - Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, daß im Dampfraum (8) Mittel vorgesehen sind, welche die Bewegung der darin befindlichen feinen Faserstoffkrümel abbremsen. - Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, daß die Radialbewegung des Faserstoffes in der Dispergierzone (9) gedrosselt wird. - Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, daß die maximale Geschwindigkeit des den Zerkleinerungsschritt auslösenden Werkzeuges zwischen 10 und 30 m/sec liegt. - Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, daß der Zerkleinerungsschritt mit Mitteln durchgeführt wird, die unmittelbar an den aus einer Entwässerungsschnecke ausgetretenen Stoffpfropfen angreifen. - Verfahren nach einem der Ansprüche 1 bis 11,
dadurch gekennzeichnet, daß der Zerkleinerungsschritt mit Mitteln durchgeführt wird, die an Faserstoff-Stücken angreifen, die durch Vorzerkleinem einer von einer Siebpresse abgelaufenen, feuchten Faserstoffbahn entstanden sind. - Verfahren nach einem der voranstehenden Ansprüche,
dadurch gekennzeichnet, daß der hochkonsistente Faserstoff auch bereits vor dem Zerkleinerungsschritt erwärmt wird. - Vorrichtung zur Durchführung des Verfahrens nach einem der voranstehenden Ansprüche mit einer Dispergergamitur,
welche mindestens einen stillstehenden Stator (2) und mindestens einen rotierbaren Rotor (4) umfaßt,
in der in einer Dispergierzone (9) mehrere Zahnreihen in einem Abstand von höchstens 3 mm relativ zueinander bewegbar sind,
wobei der Rotor (4) ein Zerkleinerungswerkzeug enthält,
welches sich in der Nähe der Einlaßöffnung für den zu dispergierenden, hochkonsistenten Faserstoff (S) befindet,
dadurch gekennzeichnet, daß das Zerkleinerungswerkzeug mit Schabern oder Messern versehen ist und daß sich stromabwärts ein ringförmiger Dampfraum (8) anschließt, der der Aufheizung des in der Zerkleinerungszone gebildeten feinen Krümelstoffes dient und daß radial weiter außen die Dispergierzone (9) folgt. - Vorrichtung nach Anspruch 15,
dadurch gekennzeichnet, daß der Dampfraum (8) stromaufwärts durch eine Statorzahnreihe begrenzt wird, wobei die dazugehörigen primären Statorzähne (7) bis auf einen Spalt von höchstens 3 mm an den Rotor heranreichen. - Vorrichtung nach Anspruch 16,
dadurch gekennzeichnet, daß die primären Statorzähne (7) einen Abstand von mindestens 50 mm in Umfangsrichtung haben. - Vorrichtung nach Anspruch 15, 16 oder 17,
dadurchg gekennzeichnet,
daß der Dampfraum (8) stromabwärts durch eine Rotorzahnreihe begrenzt wird, wobei die dazugehörigen primären Rotorzähne (7) bis auf einen Spalt von höchstens 3 mm an den Rotor heranreichen. - Vorrichtung nach Anspruch 15, 16, 17 oder 18,
dadurch gekennzeichnet, daß der Dampfraum (8) durch Dampfrohre (11) mit einer Dampfzuführleitung verbunden ist. - Vorrichtung nach Anspruch 15, 16, 17, 18 oder 19,
dadurch gekennzeichnet, daß die Dispergierzone (9) radial außen durch eine Drossel abgeschlossen wird, die den Durchströmquerschnitt einstellbar macht. - Vorrichtung nach Anspruch 20,
dadurch gekennzeichnet, daß die Drossel durch einen mit Öffnungen versehenen Drosselring (10) gebildet wird, wobei das Einstellen durch Verdrehen des Drosselringes (10) erfolgen kann. - Vorrichtung nach Anspruch 20,
dadurch gekennzeichnet, daß die Drossel durch einen Drosselring (10) gebildet wird, wobei das Einstellen durch Axialverschieben des Drosselringes (10) erfolgen kann.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19712653 | 1997-03-26 | ||
DE19712653A DE19712653C2 (de) | 1997-03-26 | 1997-03-26 | Verfahren und Vorrichtung zur Dispergierung eines Altpapierfaserstoffes |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0886001A1 EP0886001A1 (de) | 1998-12-23 |
EP0886001B1 true EP0886001B1 (de) | 2002-07-03 |
Family
ID=7824653
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP98101955A Expired - Lifetime EP0886001B1 (de) | 1997-03-26 | 1998-02-05 | Verfahren und Vorrichtung zur Dispergierung eines Papierfaserstoffes |
Country Status (5)
Country | Link |
---|---|
US (2) | US6250573B1 (de) |
EP (1) | EP0886001B1 (de) |
AT (1) | ATE220140T1 (de) |
DE (2) | DE19712653C2 (de) |
NO (1) | NO312683B1 (de) |
Cited By (1)
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RU2503490C1 (ru) * | 2012-08-21 | 2014-01-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Астраханский государственный университет" | Гидравлический смеситель для обработки воды коагулянтами |
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FI109135B (fi) | 1999-09-21 | 2002-05-31 | Metso Paper Inc | Menetelmä ja laite puukuitumassan käsittelemiseksi |
DE10108518A1 (de) * | 2000-04-11 | 2001-10-18 | Voith Paper Patent Gmbh | Vorrichtung zur Dispergierung von hochkonsistentem Papierfaserstoff |
DE10018262A1 (de) * | 2000-04-13 | 2001-10-18 | Voith Paper Patent Gmbh | Verfahren zur Dispergierung eines Papierfaserstoffes sowie Anlage zur Durchführung des Verfahrens |
DE10102449C1 (de) | 2001-01-19 | 2002-03-21 | Voith Paper Patent Gmbh | Vorrichtung zur Heiß-Dispergierung eines Papierfaserstoffes |
JP3451285B2 (ja) * | 2001-05-07 | 2003-09-29 | 有限会社美粒研 | 混合・粉砕微粒子化装置及びこれを用いた物質の微粒子化方法 |
DE10219843C1 (de) * | 2002-05-03 | 2003-08-21 | Voith Paper Patent Gmbh | Verfahren zur Dispergierung eines Papierfaserstoffes |
DE10219844C1 (de) | 2002-05-03 | 2003-09-18 | Voith Paper Patent Gmbh | Verfahren zur Heissdispergierung eines Papierfaserstoffes |
US7188792B2 (en) * | 2003-03-18 | 2007-03-13 | Gl&V Management Hungary Kft. | Refiner rotor assembly with a hub having flow-through ports |
DE102005012168A1 (de) * | 2005-03-17 | 2006-09-28 | Voith Paper Patent Gmbh | Verfahren und Vorrichtung zum Beladen von in einer Faserstoffsuspension enthaltenen Fasern mit Füllstoff |
WO2010009174A1 (en) * | 2008-07-14 | 2010-01-21 | 36 Degrees South, Inc. | Process and apparatus for drying and powderizing material |
KR100942504B1 (ko) | 2008-07-30 | 2010-02-12 | 이광원 | 음식물 쓰레기 분쇄장치 |
CN102203271B (zh) * | 2008-08-27 | 2015-09-09 | 易登尼有限公司 | 用于将生物质转化为生物燃料的材料和方法 |
AT507724B1 (de) * | 2008-12-23 | 2011-03-15 | Andritz Ag Maschf | Vorrichtung für die zerkleinerung eines zellulosehältigen aufgabegutes |
DE102010005517B4 (de) * | 2010-01-23 | 2012-04-19 | Gea Tuchenhagen Gmbh | Dispergierpumpe |
US8573523B2 (en) | 2010-03-30 | 2013-11-05 | Kok Technologies Inc. | Automatic and continuous rubber extracting device for extracting rubber from a rubber-bearing plant material |
RU2458732C1 (ru) * | 2011-01-12 | 2012-08-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Ярославский государственный технический университет" | Агрегат для смешения сыпучих материалов |
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RU2761241C1 (ru) * | 2021-04-28 | 2021-12-06 | Рашид Харисович Хакимов | Диспергатор |
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-
1997
- 1997-03-26 DE DE19712653A patent/DE19712653C2/de not_active Expired - Fee Related
-
1998
- 1998-02-05 AT AT98101955T patent/ATE220140T1/de active
- 1998-02-05 DE DE59804634T patent/DE59804634D1/de not_active Expired - Lifetime
- 1998-02-05 EP EP98101955A patent/EP0886001B1/de not_active Expired - Lifetime
- 1998-03-09 NO NO19981018A patent/NO312683B1/no not_active IP Right Cessation
- 1998-03-24 US US09/046,570 patent/US6250573B1/en not_active Expired - Fee Related
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2001
- 2001-05-04 US US09/848,351 patent/US6634583B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2503490C1 (ru) * | 2012-08-21 | 2014-01-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Астраханский государственный университет" | Гидравлический смеситель для обработки воды коагулянтами |
Also Published As
Publication number | Publication date |
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DE19712653A1 (de) | 1998-10-01 |
DE59804634D1 (de) | 2002-08-08 |
US20010015389A1 (en) | 2001-08-23 |
ATE220140T1 (de) | 2002-07-15 |
NO981018D0 (no) | 1998-03-09 |
NO981018L (no) | 1998-09-28 |
DE19712653C2 (de) | 2002-10-24 |
EP0886001A1 (de) | 1998-12-23 |
US6250573B1 (en) | 2001-06-26 |
US6634583B2 (en) | 2003-10-21 |
NO312683B1 (no) | 2002-06-17 |
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