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WO1996018769A1 - Means for treatment of particle mass - Google Patents

Means for treatment of particle mass Download PDF

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Publication number
WO1996018769A1
WO1996018769A1 PCT/NO1995/000226 NO9500226W WO9618769A1 WO 1996018769 A1 WO1996018769 A1 WO 1996018769A1 NO 9500226 W NO9500226 W NO 9500226W WO 9618769 A1 WO9618769 A1 WO 9618769A1
Authority
WO
WIPO (PCT)
Prior art keywords
pulp
disperser
disc
particulate material
steam
Prior art date
Application number
PCT/NO1995/000226
Other languages
French (fr)
Inventor
Tom Egenes
Terje Fjellkleiv
Esten Nordal
Original Assignee
Kvaerner Hymac A.S.
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 Kvaerner Hymac A.S. filed Critical Kvaerner Hymac A.S.
Priority to AU42729/96A priority Critical patent/AU4272996A/en
Publication of WO1996018769A1 publication Critical patent/WO1996018769A1/en

Links

Classifications

    • 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
    • D21D1/008—Discs
    • 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
    • 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
    • D21B1/32—Defibrating by other means of waste paper
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/64—Paper recycling

Definitions

  • the invention relates to a device for processing particulate material comprising a grinder, means for introducing a particulate material into the grinder; a disc disperser and means for transferring particulate material from the grinder to the disc disperser, means for removing particulate material from the disc disperser; and means for introducing steam into the device to heat the particulate material.
  • particulate material especially wood fibre pulp and more specifically pulp containing recycled paper
  • a plurality of process steps comprising dewatering in a dewatering zone with the aid of a screw press, thereby increasing the concentration of the pulp.
  • the pulp is then conducted to a heating zone, where the pulp is advanced whilst steam is added.
  • the heated pulp is subsequently fed to a disc disperser where the pulp is processed to reduce the amount of impurities in the pulp, such as printer's ink, wax, bitumen and so forth.
  • a slowly rotating screw is used in the heating zone where steam is added at certain points across the screw through a manifold.
  • the steam emits thermal energy on condensation, and the pulp is heated.
  • the screw may be whole or in pieces.
  • a preheating screw of this kind is usually dimensioned for about three minutes residence time and about 50% of filling.
  • the speed of rotation of a preheater of this type is in the range of 5 to 15 revolutions/minute.
  • the slow rotation of the screw causes little mixing of the pulp, so that there may be large temperature gradients in the pulp.
  • the condensing steam will thus have poor contact with the pulp particles.
  • the pulp particles may be quite large in a conventional preheater, so a relatively long time is required to heat the pulp particles through.
  • a device is therefore proposed wherein a very good mixing of steam and particulate material can be obtained so that the pulp is heated evenly, at the same time as it is ensured that the pulp particles are so small that they rapidly become thoroughly heated.
  • the pulp particles are reduced in size in that a rapidly rotating grinder is used to mix pulp and steam.
  • a device for the processing of particulate material comprising a grinder, means for introducing a particulate material into the grinder; a disc disperser and means for transferring particulate material from the grinder to the disc disperser; means for removing the particulate material from the disc disperser, and means for introducing steam into the device to heat the particulate material, said device being characterised in that the grinder is a disc disperser.
  • the amount of the impurities in the pulp such as printer's ink. wax, bitumen and so forth will, as known from prior art, be reduced.
  • the means for adding steam to open centrally into the first disc disperser that is used as a rapidly rotating grinder is especially expedient for the means for adding steam to open centrally into the first disc disperser that is used as a rapidly rotating grinder.
  • the means for adding steam can also open centrally into the second disc disperser.
  • the first disc disperser can function as a predisperser where impurities are dispersed whilst the pulp is relatively cold, which will be advantageous for certain printer's inks, such as laser and Xerox, whereas the second disc disperser will function as a main disperser whilst the pulp is hot, which will be advantageous in the case of impurities such as so-called stickies and so forth.
  • the means for introducing the particulate material into the first disc disperser may to advantage comprise a screw feeder having a hollow shaft for supplying steam to the first disc disperser, thereby obtaining the advantage that the steam is fed centrally into the disc disperser and the pulp therein.
  • the means for transferring the particulate material can comprise a screw feeder with a hollow shaft for feeding steam to the interior of the attached disc disperser.
  • Figure 1 is a purely schematic illustration of a device according to the invention
  • Figure 2 is a purely schematic illustration of a modified embodiment of a device according to the invention.
  • Figure 3 is a more artistic perspective view of a plant where a device according to the invention is used.
  • the device illustrated in Fig. 1 comprises a disc disperser 1 with a screw feeder 2.
  • the disc disperser 1 essentially comprises a stator disc 3 and a rotor disc 4, driven by a motor 5.
  • the device comprises a second disc disperser 8, constructed in the same way as the first disc disperser 1, i.e., with a screw feeder 9, a stator disc 10 and a rotor disc 11 , driven by a motor 12.
  • the pulp which is to be processed is introduced into the screw feeder 2 as shown by means of the arrow 6. From the first disc disperser 1 the pulp treated therein passes to the screw feeder 9, as indicated by means of the arrow 7.
  • Dispersed pulp exits the second disperser 8 as indicated by means of the arrow 13.
  • Steam as a heating medium can be supplied to the first disperser 1 through the hollow shaft 14 of the screw feeder 2, as indicated by means of the arrow 15. The steam can in this way be fed centrally into the disc disperser 1 , and thus centrally into the pulp introduced into the disc disperser by means of the screw feeder 2.
  • the second disc disperser 8 has an attached screw feeder 9 having a solid shaft 16.
  • the device according to the invention may also be realised in a modified form, as shown in Fig. 2.
  • the only difference between the device in Fig. 1 and that in Fig. 2 is that the shaft of the screw feeder 9 is made as a hollow shaft 16', through which steam can be fed as indicated by means of the arrow 17.
  • Figure 3 shows a plant where the device according to the invention is used.
  • the same reference numerals are used here for the plant components which correspond to those shown in Fig. 2.
  • the plant comprises a screw press 18, having a pulp inlet 19 and an outlet 20, which goes to a screw feeder 2 via an inflow 6.
  • the screw feeder 2 is attached to a disc disperser 1.
  • the outlet of the disc disperser 1 is connected to a screw conveyor whose function corresponds to the arrow 7 in Fig. 2 and has therefore been given the same reference numeral.
  • the screw conveyor 7 has an outlet which opens into a screw feeder 9, attached to a second disc disperser 8.
  • the outlet of the disc disperser 8 is designated 13 in accordance with the corresponding arrow in Figure 2. Steam can be fed to the disc disperser 1 and/or 8 according to need through respective steam pipes 15,17 which are connected to the respective hollow shafts 14J 6'.
  • the screw press 18 represents a dewatering zone where the pulp is dewatered. Thence, the pulp passes to the first disc disperser 1. Steam is added in the centre of the disc disperser 1, and can simultaneously also be added in the disc disperser 8, which receives pulp from the disc disperser 1.
  • the pulp is mixed well with the added steam at the same time as the size of the pulp particles is reduced.
  • the second disperser 8 a reduction of the amount of impurities, such as printer's ink, wax, bitumen and so forth, is carried out in a known way.
  • the disc disperser 1 may also be used as a predisperser, the two dispersers then operating under different temperature conditions.
  • the predisperser 1 will disperse impurities whilst the pulp is relatively cold, which is advantageous in the case of certain printer's inks such as laser and Xerox, whilst the disperser 8 as main disperser will disperse whilst the pulp is hot, which is advantageous in the case of impurities such as stickies and so forth.
  • the advantage is obtained that the preheating period is very short, as a consequence of the good mix of steam and pulp and also minimal size of the pulp particles. It will be possible to mix bleaching chemicals into the pulp and/pr improve the efficiency of the actual dispersion of the impurity particles in the pulp.
  • the device is flexible and provides the possibility of dispersion at two temperature levels, cold and hot pulp respectively (steam supply in the second disperser only).

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Inorganic Insulating Materials (AREA)
  • Paper (AREA)

Abstract

The invention relates to a device for processing particulate material comprising a grinder (1), means (2) for introducing a particulate material into the grinder; a disc disperser (8) and means (7, 9) for transferring particulate material from te grinder (1) to the disc disperser (8), means (13) for removing particulate material from the disc disperser (8); and means (14) for adding steam to the device to heat the particulate material. The invention is characterised in that the grinder (1) is a rapidly rotating grinder in the form of a disc disperser.

Description

Means for treatment of particle mass
The invention relates to a device for processing particulate material comprising a grinder, means for introducing a particulate material into the grinder; a disc disperser and means for transferring particulate material from the grinder to the disc disperser, means for removing particulate material from the disc disperser; and means for introducing steam into the device to heat the particulate material.
According to conventional technique, particulate material, especially wood fibre pulp and more specifically pulp containing recycled paper, can be processed by means of a plurality of process steps comprising dewatering in a dewatering zone with the aid of a screw press, thereby increasing the concentration of the pulp. From the dewatering zone the pulp is then conducted to a heating zone, where the pulp is advanced whilst steam is added. The heated pulp is subsequently fed to a disc disperser where the pulp is processed to reduce the amount of impurities in the pulp, such as printer's ink, wax, bitumen and so forth.
As a rule, a slowly rotating screw is used in the heating zone where steam is added at certain points across the screw through a manifold. The steam emits thermal energy on condensation, and the pulp is heated. The screw may be whole or in pieces. A preheating screw of this kind is usually dimensioned for about three minutes residence time and about 50% of filling. The speed of rotation of a preheater of this type is in the range of 5 to 15 revolutions/minute. The slow rotation of the screw causes little mixing of the pulp, so that there may be large temperature gradients in the pulp. The condensing steam will thus have poor contact with the pulp particles. The pulp particles may be quite large in a conventional preheater, so a relatively long time is required to heat the pulp particles through.
The equipment used today also requires a relatively large space. Clearly therefore, there is a need for better equipment with which the process outlined hereinabove can be carried out in a faster and cheaper manner, and which occupies less space.
According to the invention, a device is therefore proposed wherein a very good mixing of steam and particulate material can be obtained so that the pulp is heated evenly, at the same time as it is ensured that the pulp particles are so small that they rapidly become thoroughly heated. The pulp particles are reduced in size in that a rapidly rotating grinder is used to mix pulp and steam. Thus, according to the invention a device is proposed for the processing of particulate material comprising a grinder, means for introducing a particulate material into the grinder; a disc disperser and means for transferring particulate material from the grinder to the disc disperser; means for removing the particulate material from the disc disperser, and means for introducing steam into the device to heat the particulate material, said device being characterised in that the grinder is a disc disperser.
In the disc disperser which is used as a rapidly rotating grinder, particles will be produced that are so small they will capable of being heated through rapidly.
According to the invention, it is especially advantageous if the means for adding the steam open into the disperser that is used as a rapidly rotating shredder.
In a device of this kind the size of the pulp particles will be reduced so that they become so small that they rapidly become thoroughly heated under the influence of the added steam. An exceptionally good mixing of steam and pulp is obtained so that the pulp is heated evenly.
In the subsequent disc disperser, the amount of the impurities in the pulp, such as printer's ink. wax, bitumen and so forth will, as known from prior art, be reduced.
According to the invention, it is especially expedient for the means for adding steam to open centrally into the first disc disperser that is used as a rapidly rotating grinder.
According to the invention, the means for adding steam can also open centrally into the second disc disperser.
The practical realisation of the invention results in a unique preheating concept which will be capable of giving an extremely short preheating period because of the good mixing of steam/pulp and the minimal size of the pulp particles.
It becomes possible to admix chemicals which bleach the pulp and/or improve the efficiency of the actual dispersion of the impurity particles in the pulp.
Of particular interest is the fact that dispersion at two temperature levels, cold and hot pulp respectively, also becomes possible. In the last-mentioned case, the first disc disperser can function as a predisperser where impurities are dispersed whilst the pulp is relatively cold, which will be advantageous for certain printer's inks, such as laser and Xerox, whereas the second disc disperser will function as a main disperser whilst the pulp is hot, which will be advantageous in the case of impurities such as so-called stickies and so forth.
According to the invention, the means for introducing the particulate material into the first disc disperser may to advantage comprise a screw feeder having a hollow shaft for supplying steam to the first disc disperser, thereby obtaining the advantage that the steam is fed centrally into the disc disperser and the pulp therein.
According to the invention, the means for transferring the particulate material can comprise a screw feeder with a hollow shaft for feeding steam to the interior of the attached disc disperser.
The invention will now be described in more detail with reference to the drawings, wherein:
Figure 1 is a purely schematic illustration of a device according to the invention;
Figure 2 is a purely schematic illustration of a modified embodiment of a device according to the invention; and
Figure 3 is a more artistic perspective view of a plant where a device according to the invention is used.
The device illustrated in Fig. 1 comprises a disc disperser 1 with a screw feeder 2. The disc disperser 1 essentially comprises a stator disc 3 and a rotor disc 4, driven by a motor 5. Furthermore, the device comprises a second disc disperser 8, constructed in the same way as the first disc disperser 1, i.e., with a screw feeder 9, a stator disc 10 and a rotor disc 11 , driven by a motor 12.
The pulp which is to be processed is introduced into the screw feeder 2 as shown by means of the arrow 6. From the first disc disperser 1 the pulp treated therein passes to the screw feeder 9, as indicated by means of the arrow 7.
Dispersed pulp exits the second disperser 8 as indicated by means of the arrow 13. Steam as a heating medium can be supplied to the first disperser 1 through the hollow shaft 14 of the screw feeder 2, as indicated by means of the arrow 15. The steam can in this way be fed centrally into the disc disperser 1 , and thus centrally into the pulp introduced into the disc disperser by means of the screw feeder 2.
The second disc disperser 8 has an attached screw feeder 9 having a solid shaft 16.
The device according to the invention may also be realised in a modified form, as shown in Fig. 2. The only difference between the device in Fig. 1 and that in Fig. 2 is that the shaft of the screw feeder 9 is made as a hollow shaft 16', through which steam can be fed as indicated by means of the arrow 17.
Figure 3 shows a plant where the device according to the invention is used. The same reference numerals are used here for the plant components which correspond to those shown in Fig. 2.
The plant comprises a screw press 18, having a pulp inlet 19 and an outlet 20, which goes to a screw feeder 2 via an inflow 6. The screw feeder 2 is attached to a disc disperser 1. The outlet of the disc disperser 1 is connected to a screw conveyor whose function corresponds to the arrow 7 in Fig. 2 and has therefore been given the same reference numeral. The screw conveyor 7 has an outlet which opens into a screw feeder 9, attached to a second disc disperser 8. The outlet of the disc disperser 8 is designated 13 in accordance with the corresponding arrow in Figure 2. Steam can be fed to the disc disperser 1 and/or 8 according to need through respective steam pipes 15,17 which are connected to the respective hollow shafts 14J 6'.
The screw press 18 represents a dewatering zone where the pulp is dewatered. Thence, the pulp passes to the first disc disperser 1. Steam is added in the centre of the disc disperser 1, and can simultaneously also be added in the disc disperser 8, which receives pulp from the disc disperser 1.
In the disc disperser 1 the pulp is mixed well with the added steam at the same time as the size of the pulp particles is reduced.
In the second disperser 8 a reduction of the amount of impurities, such as printer's ink, wax, bitumen and so forth, is carried out in a known way. The disc disperser 1 may also be used as a predisperser, the two dispersers then operating under different temperature conditions. The predisperser 1 will disperse impurities whilst the pulp is relatively cold, which is advantageous in the case of certain printer's inks such as laser and Xerox, whilst the disperser 8 as main disperser will disperse whilst the pulp is hot, which is advantageous in the case of impurities such as stickies and so forth.
By means of the invention the advantage is obtained that the preheating period is very short, as a consequence of the good mix of steam and pulp and also minimal size of the pulp particles. It will be possible to mix bleaching chemicals into the pulp and/pr improve the efficiency of the actual dispersion of the impurity particles in the pulp.
The device is flexible and provides the possibility of dispersion at two temperature levels, cold and hot pulp respectively (steam supply in the second disperser only).
Steam may in addition be added at other points, wherever desirable, such as indicated by means of the arrow D in Fig. 1.

Claims

P a t e n t c l a i m s
1.
A device for processing particulate material comprising a grinder (1 ), means (2) for introducing a particulate material into the grinder: a disc disperser (8) and means (7,9) for transferring particulate material from the grinder (1) to the disc disperser (8), means (13) for removing particulate material from the disc disperser (8); and means (14) for introducing steam into the device to heat the particulate material, characterised in that the grinder (1) is a disc disperser.
2.
A device as disclosed in Claim 1, characterised in that the means (14) for adding steam open into the disc disperser used as a rapidly rotating grinder (1).
3.
A device as disclosed in Claim 2, characterised in that the means (14) for adding steam open centrally into the first disc disperser (1).
4.
A device as disclosed in Claims 1 to 3, characterised in that means for adding steam also open centrally (16') into the second disc disperser (8).
5.
A device as disclosed in one of Claims 1 to 4, characterised in that the means for feeding the particulate material to the first disc disperser (1) comprise a screw feeder (2) having a hollow shaft (14) for feeding steam (15) to the first disc disperser (1).
6.
A device according to one of Claims 1 to 5, characterised in that the means for transferring particulate material comprise a screw feeder (9) having a hollow shaft (16') for feeding steam (17).
PCT/NO1995/000226 1994-12-14 1995-12-07 Means for treatment of particle mass WO1996018769A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU42729/96A AU4272996A (en) 1994-12-14 1995-12-07 Means for treatment of particle mass

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO944847A NO180241C (en) 1994-12-14 1994-12-14 Device for processing particle mass
NO944847 1994-12-14

Publications (1)

Publication Number Publication Date
WO1996018769A1 true WO1996018769A1 (en) 1996-06-20

Family

ID=19897755

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NO1995/000226 WO1996018769A1 (en) 1994-12-14 1995-12-07 Means for treatment of particle mass

Country Status (3)

Country Link
AU (1) AU4272996A (en)
NO (1) NO180241C (en)
WO (1) WO1996018769A1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19712653A1 (en) * 1997-03-26 1998-10-01 Voith Sulzer Stoffaufbereitung Dispersal of compacted paper fibre mass
DE19712651A1 (en) * 1997-03-26 1998-10-01 Voith Sulzer Stoffaufbereitung Method and device for producing a hot, mostly paper fiber-containing crumb
US6651839B2 (en) 2001-01-19 2003-11-25 Voith Paper Patent Gmbh Device for hot dispersing fibrous paper stock and a method hot dispersing the stock
WO2004046455A1 (en) * 2002-11-18 2004-06-03 M-Real Oyj Method and apparatus for producing mechanical fibers
WO2006097180A1 (en) * 2005-03-17 2006-09-21 Voith Patent Gmbh Method and device for charging fibers contained in a fibrous suspension with a filler
CN1306113C (en) * 2002-03-27 2007-03-21 安德里茨有限公司 Method and appts. for dispersing regenerated fiber pulp
CN102356194A (en) * 2009-03-17 2012-02-15 美卓造纸机械公司 Method, system and refiner for refining of wood chips or pulp fibers

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4235665A (en) * 1976-06-30 1980-11-25 American Defibrator, Inc. Method and apparatus for producing fiber pulp in a steam pressurized grinding system
WO1994027713A1 (en) * 1993-05-24 1994-12-08 Andritz-Patentverwaltungs-Gesellschaft M.B.H. Mixer, especially high-performance mixer for fine-grinding pre-ground materials

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4235665A (en) * 1976-06-30 1980-11-25 American Defibrator, Inc. Method and apparatus for producing fiber pulp in a steam pressurized grinding system
WO1994027713A1 (en) * 1993-05-24 1994-12-08 Andritz-Patentverwaltungs-Gesellschaft M.B.H. Mixer, especially high-performance mixer for fine-grinding pre-ground materials

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19712651A1 (en) * 1997-03-26 1998-10-01 Voith Sulzer Stoffaufbereitung Method and device for producing a hot, mostly paper fiber-containing crumb
EP0886001A1 (en) * 1997-03-26 1998-12-23 Voith Sulzer Papiertechnik Patent GmbH Process and apparatus to disperse a paper fibers slurry
US6073865A (en) * 1997-03-26 2000-06-13 Voith Sulzer Papiertechnik Patent Gmbh Process and devices for manufacturing a hot friable material
US6250573B1 (en) 1997-03-26 2001-06-26 Voith Sulzer Papiertechnik Patent Gmbh Process and device for the dispersion of a fibrous paper material
DE19712653C2 (en) * 1997-03-26 2002-10-24 Voith Paper Fiber Systems Gmbh Method and device for dispersing a waste paper pulp
US6634583B2 (en) 1997-03-26 2003-10-21 Voith Paper Patent Gmbh Process and device for the dispersion of a fibrous paper material
DE19712653A1 (en) * 1997-03-26 1998-10-01 Voith Sulzer Stoffaufbereitung Dispersal of compacted paper fibre mass
US6651839B2 (en) 2001-01-19 2003-11-25 Voith Paper Patent Gmbh Device for hot dispersing fibrous paper stock and a method hot dispersing the stock
CN1306113C (en) * 2002-03-27 2007-03-21 安德里茨有限公司 Method and appts. for dispersing regenerated fiber pulp
WO2004046455A1 (en) * 2002-11-18 2004-06-03 M-Real Oyj Method and apparatus for producing mechanical fibers
JP2006506547A (en) * 2002-11-18 2006-02-23 アムーレアル オサケ ユキチュア ユルキネン Method and apparatus for producing mechanically refined fibers
US7237733B2 (en) 2002-11-18 2007-07-03 M-Real Oyj Method and apparatus for producing mechanical fibers
RU2336382C2 (en) * 2002-11-18 2008-10-20 М-Риал Оий Method of mechanical fibre mass production and associated device
CN100458011C (en) * 2002-11-18 2009-02-04 M-真实公司 Method and apparatus for producing mechanical fibers
WO2006097180A1 (en) * 2005-03-17 2006-09-21 Voith Patent Gmbh Method and device for charging fibers contained in a fibrous suspension with a filler
CN102356194A (en) * 2009-03-17 2012-02-15 美卓造纸机械公司 Method, system and refiner for refining of wood chips or pulp fibers

Also Published As

Publication number Publication date
NO180241B (en) 1996-12-02
NO180241C (en) 1997-03-12
NO944847D0 (en) 1994-12-14
NO944847L (en) 1996-06-17
AU4272996A (en) 1996-07-03

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