EP0335870A1 - Refiner - Google Patents

Refiner

Info

Publication number
EP0335870A1
EP0335870A1 EP19870907111 EP87907111A EP0335870A1 EP 0335870 A1 EP0335870 A1 EP 0335870A1 EP 19870907111 EP19870907111 EP 19870907111 EP 87907111 A EP87907111 A EP 87907111A EP 0335870 A1 EP0335870 A1 EP 0335870A1
Authority
EP
European Patent Office
Prior art keywords
rotor
refiner
gap
stator
grinding
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.)
Withdrawn
Application number
EP19870907111
Other languages
German (de)
French (fr)
Inventor
Jorma Surakka
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.)
Sunds Defibrator Jylha OY
Original Assignee
Sunds Defibrator Jylha OY
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 Sunds Defibrator Jylha OY filed Critical Sunds Defibrator Jylha OY
Publication of EP0335870A1 publication Critical patent/EP0335870A1/en
Withdrawn legal-status Critical Current

Links

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
    • D21D1/20Methods of refining
    • D21D1/30Disc mills
    • 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
    • D21D1/30Disc mills
    • D21D1/303Double disc mills

Definitions

  • the present invention concerns a refiner, preferably a disc or conical refiner, with two opposed, closely adjacent bodies, whereof one at least, the so-called rotor, rotates, and which are provided with blades, the material to be refined being ground in the grinding gap between them and releases steam, said material to be refined being fed into the refiner substantially in the direction of the central axis of the blades.
  • a refiner preferably a disc or conical refiner, with two opposed, closely adjacent bodies, whereof one at least, the so-called rotor, rotates, and which are provided with blades, the material to be refined being ground in the grinding gap between them and releases steam, said material to be refined being fed into the refiner substantially in the direction of the central axis of the blades.
  • Dispersing of a fibreous substance, for instance wood chips, to become fibres fit for use i n paper manufacturing may be accomplished mechanically with a refiner, examples of such being a disc refiner and a conical refiner.
  • This so-called defibration is accomplished in that the chips are introduced into the refiner, whereto the material passes through between two opposed grinding blades.
  • the surfaces of the blades are full of grooves and elongated eminences, teeth, and at least one of the blades rotates, whereby the material is powerfully worked while passing through between the blades, and it is dispersed up to single fibre consistency.
  • the object of the present invention is to provide a refiner in which not only steam removal works properly but the more perfectly ground material travels together with the steam out from the blade gap and thereby reduces excessive refining.
  • Said aim is implemented in the refiner of the invention, which is characterized in that the grinding gap comprises a sorting zone in which the more completely ground fraction of the material to be refined, and part of the steam, are separated from the less completely ground fraction.
  • An advantageous embodiment of the invention is characterized in that the sorting zone is located, in the radial direction of the blades, substantially at their centre, and that the sorting zone is substantially annular.
  • Another advantageous embodiment of the invention is characterized in that in the stationary body, i n the so-called stator, is provided a substantially annular aperture close to the sorting zone, through which said removal of the more completely ground fraction and of the steam takes place.
  • the sorting zone comprises a projecting, substantially annular member formed on the rotor, which extends into an annular aperture in the stator, whereby an exit passage for the more completely ground material and for the steam is defined between the annular member and the annular aperture.
  • One more advantageous embodiment of the invention is characterized in that the mutually opposed surfaces of the annular member on the rotor and the mating aperture in the stator are fitted with blades.
  • the exit apertures are not susceptible to blocking and that the quantity of escaping steam and more completely ground material may easily be controlled.
  • the pressure in the removal chambers for the constituents passing by different routes can similarly be controlled, independent of each other.
  • Fig. 1 presents a vertical section of a disc refiner according to an embodiment of the invention.
  • Fig. 2 presents a vertical section of a disc refiner according to another embodiment of the invention.
  • Fig. 3 presents a vertical section of a disc refiner according to a third embodiment of the invention.
  • Fig. 1 a disc refiner comprising a stationary body 1, or stator, and a rotating body 2, or rotor.
  • the stator 1 and rotor 2 are on their mutually opposed surfaces provided with a stator blade 4,8 and a rotor blade 5,9.
  • matter to be refined such as wood chips
  • the material to be refined proceeds, to begin with, between the stator blade 4 and the rotor blade 5, whereat part of the material is ground to the desired degree of fineness, and steam is produced at the same time.
  • the refiner of the invention is provided with a sorting zone which in the embodiment of Fig. 1 consists of an annular, projecting member 6 attached to the rotor 1 and of a likewise annular aperture established for it in the stator 2 and extending into the stator chamber 3. While the annular member 6 is projecting, it also extends obliquely inwards towards the central axis of the refiner.
  • the surfaces facing each other of the annular member 6 attached to the rotor 1 and of the mating aperture formed in the stator 2 are provided with blades 10,11. At this point, however, the blade gap is larger than in the grinding gap proper between the blades 4,5 and 8,9.
  • the annular member is provided with numerous radial apertures 7 extending therethrough.
  • Fig. 2 is presented another embodiment of the invention, in which the stator 1 is located on both sides of the rotor 2.
  • the stator is provided with blades 16,17.
  • the rotor in turn is provided with blades 18,19,20.
  • the rotor shaft is indicated by reference numeral 21.
  • the feed tube for material to be refined is indicated with reference numeral 3.
  • the removal chamber for refined material in turn carries the reference numeral 12, as in the preceding figure.
  • Between the refiner blades 22 and 23 are defined grinding gaps 22,23,24. Between the grinding gaps 22 and 23 is located a sorting space 25, from which several passages 26 depart through the rotor 2, and which terminate in an annular space 27.
  • the operation of the refiner of Fig. 2 is as follows.
  • the material to be refined is fed from the tube 3 into the grinding gap 22.
  • the material contains fine-ground material and coarse, less finely ground material.
  • From the gap 22 also a strong steam flow discharges because the powerful grinding evaporates a great part Df the water contained i n the material to be ground.
  • Centrifugal force feeds material from the space 25 into the gap 23, where the material is more completely ground.
  • the grinding gap 23 is so shaped that its initial part is spacious, i.e., material is admitted into the gap, while the ultimate part is very narrow.
  • the steam produced in the gap 23 discharges into the space 25, and thence further through the passages 26 into the space 27, and through the grinding gap 24 into the removal chamber 12, because the gap 24 is short in comparison with the gap 23, and has no narrow portion like that in the gap 23.
  • This steam flow transports the fines along with itself from the initial part of the gap 23, and from the space 25 through the gap 24 into the removal chamber 12.
  • the coarse material remains in the initial part of the gap 23 by centrifugal action (the passages 26 also run against the centrifugal force) until it is finely ground and then is removed, entrained with the steam.
  • Fig. 3 is presented one more embodiment of disc refiner employing a sorting zone.
  • the stator of the refiner is indicated by reference numeral 28, and the stator blades with 29,30,31 and 32.
  • the rotor is indicated by reference numeral 33 and its shaft by numeral 34.
  • the front bearing of the shaft is indicated by numeral 35 and the packing, by 36.
  • Material to be ground is fed through the feed tube 37.
  • the removal chamber for refined material carries the reference numeral 38.
  • the rotor 33 is provided with apertures 39 extending therethrough.
  • the grinding gaps are indicated by reference numerals 40,41,42 and 43. In the initial part of the grinding gaps 42, in register with the apertures 39, is defined a sorting space 44, communicating with the space 45 through the apertures 39. From the sorting space 44 departs a sorting and transport gap 46, terminating in an annular space 47.
  • the walls of the gap 46 present eminences 48 and 49.
  • the operation of the refiner depicted in Fig. 3 is as follows.
  • the material to be refined is fed through the tube 37 into the grinding gap 40 whence it discharges into the space 45 in partly ground condition.
  • the apertures 39 are short and wide, whereby material is immediately also supplied into the spaces 44. From the spaces 44 and 45, centrifugal force feeds material into the grinding gaps 41 and 42, and which operate in like manner as the gap 23 in Fig. 2. It is thus understood that the steam produced in the gaps 40, 41 and 42 discharges through the wide sorting gap 46 into the space 47, and through the low-resistance grinding gap 43 into the removal chamber 38. Along with the steam, the finely ground material is removed, like in Fig. 1.
  • the gap 46 operates more efficiently than the passages 26 depicted in Fig. 2 because its walls are in motion relative to each other.
  • the gap 46 may therefore be made considerably narrower without incurring risk of blockage, whereby high velocity and transporting effect of the steam is achieved.
  • Departure of the coarse fraction may in addition prevented by means of eminences 48 and 49.
  • the ultimate part of the grinding gaps 41 and 42 may be almost totally dammed by the alternative implementation depicted in the bottom part of the figure, i n which the removal chamber is made to be very narrow at said gaps.
  • teeth may be provided on the outer margin of the disc, at the point 50, which comminute such material which has already entered the chamber and mix it so that it ends up back in the gap and i n sorting.

Landscapes

  • Paper (AREA)
  • Glass Compositions (AREA)

Abstract

Raffineur, de préférence conique ou à disques, comprenant deux corps opposés étroitement espacés, dont l'un au moins, à savoir le rotor (2), tourne et qui sont pourvus d'aubes (4, 8; 5, 9). Le matériau à raffiner est broyé dans l'espace de broyage formé entre les aubes, libère de la vapeur et est acheminé dans le raffineur essentiellement dans le sens de l'axe central des aubes. Dans les raffineurs existants, des efforts constants ont été faits pour éliminer la vapeur du processus de raffinage, par exemple en pratiquant des trous dans le rotor. Cependant, ces trous ont tendance à s'obstruer et ne laissent passer à travers eux par ce procédé aucun matériau finement broyé. Grâce à la présente invention, ces problèmes sont résolus par le fait que l'espace de broyage comporte une zone de tri, dans laquelle la partie du matériau à raffiner dont le broyage est le plus complet et une partie de la vapeur sont séparées de la partie du matériau dont le broyage est moins complet.Refiner, preferably conical or disc, comprising two opposite closely spaced bodies, at least one of which, namely the rotor (2), rotates and which are provided with blades (4, 8; 5, 9). The material to be refined is crushed in the grinding space formed between the blades, releases steam and is conveyed in the refiner essentially in the direction of the central axis of the blades. In existing refiners, constant efforts have been made to eliminate steam from the refining process, for example by drilling holes in the rotor. However, these holes tend to clog and do not allow any finely ground material to pass through them. Thanks to the present invention, these problems are solved by the fact that the grinding space comprises a sorting zone, in which the part of the material to be refined whose grinding is the most complete and part of the vapor are separated from the part of the material whose grinding is less complete.

Description

Ref i ner
The present invention concerns a refiner, preferably a disc or conical refiner, with two opposed, closely adjacent bodies, whereof one at least, the so-called rotor, rotates, and which are provided with blades, the material to be refined being ground in the grinding gap between them and releases steam, said material to be refined being fed into the refiner substantially in the direction of the central axis of the blades.
Dispersing of a fibreous substance, for instance wood chips, to become fibres fit for use i n paper manufacturing may be accomplished mechanically with a refiner, examples of such being a disc refiner and a conical refiner. This so-called defibration is accomplished in that the chips are introduced into the refiner, whereto the material passes through between two opposed grinding blades. The surfaces of the blades are full of grooves and elongated eminences, teeth, and at least one of the blades rotates, whereby the material is powerfully worked while passing through between the blades, and it is dispersed up to single fibre consistency.
In the refining process plenty of steam is produced and several ways have been tried to solve its removal. One problem solution is to make apertures through the disc in a disc refiner, to the input or to the exit chamber. Such designs also exist in which passages piercing through the blade have been provided, and for them, continuation passages through the disc. A design is also known in the art in which steam removal passages have been formed through the disc and behind the disc are further provided continuation passages. The aim of such solutions is merely steam removal, that is, they do not remove material which has already been properly ground, and the most difficult problem encountered in all of them is blocking of said passages or escaping of steam, in which case the steam escapes completely from the blade gap, and the operation is disturbed. Such blocking is primarily due to the fact that the dimensioning cannot be made such that the flow could keep the passages open.
The object of the present invention is to provide a refiner in which not only steam removal works properly but the more perfectly ground material travels together with the steam out from the blade gap and thereby reduces excessive refining. Said aim is implemented in the refiner of the invention, which is characterized in that the grinding gap comprises a sorting zone in which the more completely ground fraction of the material to be refined, and part of the steam, are separated from the less completely ground fraction.
An advantageous embodiment of the invention is characterized in that the sorting zone is located, in the radial direction of the blades, substantially at their centre, and that the sorting zone is substantially annular.
Another advantageous embodiment of the invention is characterized in that in the stationary body, i n the so-called stator, is provided a substantially annular aperture close to the sorting zone, through which said removal of the more completely ground fraction and of the steam takes place.
One more advantageous embodiment of the invention is characterized in that the sorting zone comprises a projecting, substantially annular member formed on the rotor, which extends into an annular aperture in the stator, whereby an exit passage for the more completely ground material and for the steam is defined between the annular member and the annular aperture.
One more advantageous embodiment of the invention is characterized in that the mutually opposed surfaces of the annular member on the rotor and the mating aperture in the stator are fitted with blades.
Among the most important advantages of the invention may be mentioned that the exit apertures are not susceptible to blocking and that the quantity of escaping steam and more completely ground material may easily be controlled. The pressure in the removal chambers for the constituents passing by different routes can similarly be controlled, independent of each other. The invention is described in the following i n detail with the aid of advantageous embodiment examples by referring to the drawings attached in which -
Fig. 1 presents a vertical section of a disc refiner according to an embodiment of the invention.
Fig. 2 presents a vertical section of a disc refiner according to another embodiment of the invention.
Fig. 3 presents a vertical section of a disc refiner according to a third embodiment of the invention.
In Fig. 1 is presented a disc refiner comprising a stationary body 1, or stator, and a rotating body 2, or rotor. The stator 1 and rotor 2 are on their mutually opposed surfaces provided with a stator blade 4,8 and a rotor blade 5,9. Into the so-called grinding gap between the blades is fed matter to be refined, such as wood chips, through a feed passage 3 with the aid of centrifugal force. The material to be refined proceeds, to begin with, between the stator blade 4 and the rotor blade 5, whereat part of the material is ground to the desired degree of fineness, and steam is produced at the same time.
The refiner of the invention is provided with a sorting zone which in the embodiment of Fig. 1 consists of an annular, projecting member 6 attached to the rotor 1 and of a likewise annular aperture established for it in the stator 2 and extending into the stator chamber 3. While the annular member 6 is projecting, it also extends obliquely inwards towards the central axis of the refiner. The surfaces facing each other of the annular member 6 attached to the rotor 1 and of the mating aperture formed in the stator 2 are provided with blades 10,11. At this point, however, the blade gap is larger than in the grinding gap proper between the blades 4,5 and 8,9. The annular member is provided with numerous radial apertures 7 extending therethrough.
The more completely ground material and part of the steam emerging from the gap between the blades 4 and 5 depart through the gap between the blades 10 and 11, or the exit passage into the stator chamber 13, and therefrom further to an exit 14 provided with a valve 15. The less completely ground constituent and the rest of steam pass through apertures 7 formed in the annul ar member, i nto the space between the b lades 8 and 9, where the material is ground and proceeds under centrifugal force effect towards the refiner chamber 12 and thence to further treatment.
In Fig. 2 is presented another embodiment of the invention, in which the stator 1 is located on both sides of the rotor 2. The stator is provided with blades 16,17. The rotor in turn is provided with blades 18,19,20. The rotor shaft is indicated by reference numeral 21. The feed tube for material to be refined is indicated with reference numeral 3. The removal chamber for refined material in turn carries the reference numeral 12, as in the preceding figure. Between the refiner blades 22 and 23 are defined grinding gaps 22,23,24. Between the grinding gaps 22 and 23 is located a sorting space 25, from which several passages 26 depart through the rotor 2, and which terminate in an annular space 27.
The operation of the refiner of Fig. 2 is as follows. The material to be refined is fed from the tube 3 into the grinding gap 22. When discharging into the space 25, the material contains fine-ground material and coarse, less finely ground material. From the gap 22 also a strong steam flow discharges because the powerful grinding evaporates a great part Df the water contained i n the material to be ground. Centrifugal force feeds material from the space 25 into the gap 23, where the material is more completely ground. The grinding gap 23 is so shaped that its initial part is spacious, i.e., material is admitted into the gap, while the ultimate part is very narrow. Therefore, the steam produced in the gap 23 discharges into the space 25, and thence further through the passages 26 into the space 27, and through the grinding gap 24 into the removal chamber 12, because the gap 24 is short in comparison with the gap 23, and has no narrow portion like that in the gap 23. This steam flow transports the fines along with itself from the initial part of the gap 23, and from the space 25 through the gap 24 into the removal chamber 12. The coarse material remains in the initial part of the gap 23 by centrifugal action (the passages 26 also run against the centrifugal force) until it is finely ground and then is removed, entrained with the steam.
In Fig. 3 is presented one more embodiment of disc refiner employing a sorting zone. Therein, the stator of the refiner is indicated by reference numeral 28, and the stator blades with 29,30,31 and 32. The rotor is indicated by reference numeral 33 and its shaft by numeral 34. The front bearing of the shaft is indicated by numeral 35 and the packing, by 36. Material to be ground is fed through the feed tube 37. The removal chamber for refined material carries the reference numeral 38. The rotor 33 is provided with apertures 39 extending therethrough. The grinding gaps are indicated by reference numerals 40,41,42 and 43. In the initial part of the grinding gaps 42, in register with the apertures 39, is defined a sorting space 44, communicating with the space 45 through the apertures 39. From the sorting space 44 departs a sorting and transport gap 46, terminating in an annular space 47. The walls of the gap 46 present eminences 48 and 49.
The operation of the refiner depicted in Fig. 3 is as follows. The material to be refined is fed through the tube 37 into the grinding gap 40 whence it discharges into the space 45 in partly ground condition. The apertures 39 are short and wide, whereby material is immediately also supplied into the spaces 44. From the spaces 44 and 45, centrifugal force feeds material into the grinding gaps 41 and 42, and which operate in like manner as the gap 23 in Fig. 2. It is thus understood that the steam produced in the gaps 40, 41 and 42 discharges through the wide sorting gap 46 into the space 47, and through the low-resistance grinding gap 43 into the removal chamber 38. Along with the steam, the finely ground material is removed, like in Fig. 1.
The gap 46 operates more efficiently than the passages 26 depicted in Fig. 2 because its walls are in motion relative to each other. The gap 46 may therefore be made considerably narrower without incurring risk of blockage, whereby high velocity and transporting effect of the steam is achieved. Departure of the coarse fraction may in addition prevented by means of eminences 48 and 49. The ultimate part of the grinding gaps 41 and 42 may be almost totally dammed by the alternative implementation depicted in the bottom part of the figure, i n which the removal chamber is made to be very narrow at said gaps. In addition, teeth may be provided on the outer margin of the disc, at the point 50, which comminute such material which has already entered the chamber and mix it so that it ends up back in the gap and i n sorting.
It is obvious to a person skilled in the art that the invention is not confined to the above presented embodiment examples, and that it may be varied within the scope of the claims following below. For instance, the invention does not exclusively concern disc refiners: it may equally be applied also to conical refiners.

Claims

C l a i ms
1. A refiner, preferably a disc or conical refiner with two opposed, closely spaced bodies, of which at least one, the so-called rotor (2), rotates and which are provided with blades (4,8;5,9) the material to be refined being ground in the grinding gap between them, releasing steam, said material to be refined being fed into the refiner substantially in the direction of the central axis of the blades, characterized in that in the grinding gap is defined a sorting zone in which the more completely ground fraction of the material to be refined and part of the steam separate from the less completely ground fraction.
2. Refiner according to claim 1, characterized i n that the sorting zone is located, in radial direction of the blades (4,855,9), substantially at their centre, and that the sorting zone is substantially annular.
3. Refiner according to claim 1 or 2, characterized in that in the stationary body, in the so-called stator (1), is established a substantially annular aperture close to the sorting zone, wherethrough said removal of the more completely ground fraction and of the steam takes place.
4. Refiner according to any one of claims 1 to 3, characterized in that the sorting zone comprises a projecting, substantially annular member (6) formed on the rotor (2) and extending into an annular aperture in the stator (1) and in which several radial apertures (7) are formed, whereby a removal passage for the more completely ground material and for the steam is formed between the annular member (6) and the annular aperture.
5. Refiner according to claim 4, characterized in that the mutually opposed surfaces of the annular member (6) on the rotor (2) and the mating aperture in the stator (1) are fitted with blades
(10, 11).
6. Refiner according to claim 4 or 5, characterized in that the gap between the annular member (6) on the rotor (2) and the mating aperture in the stator (1), the removal passage, is larger than the grinding gap between the rotor blade (5, 9) and the stator blade (4, 8).
7. Refiner according to any one of claims 4 to 6, characterized in that the diameter of the annular member (6) at the point fartherst away from the rotor (2) is smaller than that at the rotor.
8. Refiner according to claim 1 in which the stator (1) is located on both sides of the rotor (2), whereby the grinding gap (22,23,24) is established on both sides of the rotor, characterized in that the sorting zone comprises passages (26) passing through the rotor (2) from the first grinding gap (22, 23) to the second (24).
9. Refiner according to claim 8, characterized in that the passages (26) run obliquely towards the shaft of the refiner.
10. Refiner according to claim 1, characterized i n that the sort i ng zone consists of mutually parallel grinding gaps (41,42) defined by the stator (28) and the rotor (33), into the first of these being fed the material to be refined, and of a sorting gap (46) defined by the stator and the rotor and which is wider than the grinding gaps, and that the constituent which has been more completely ground along the sorting gap goes to a different grinding gap from that receiving the less completely ground constituent.
11. Refiner according to claim 10, characterized in that on the surfaces of the sorting gap (46) are provided eminences (48, 49), which mix the material flow.
12. Refiner according to claim 10 or 11, characterized in that the sorting gap (46) runs obliquely towards the shaft (34) of the refiner.
13. Refiner according to any Dne of claims 10 to 12, characterized in that the outermost part of the grinding gap (41) through which the less completely ground constituent goes is so shaped that the passing capacity of said gap is substantially lower than that of the grinding gap (43) through which the more completely ground con stituent passes after the sorting zone.
EP19870907111 1986-10-31 1987-10-28 Refiner Withdrawn EP0335870A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI864442 1986-10-31
FI864442A FI75000C (en) 1986-10-31 1986-10-31 RAFFINOER.

Publications (1)

Publication Number Publication Date
EP0335870A1 true EP0335870A1 (en) 1989-10-11

Family

ID=8523420

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19870907111 Withdrawn EP0335870A1 (en) 1986-10-31 1987-10-28 Refiner

Country Status (6)

Country Link
EP (1) EP0335870A1 (en)
JP (1) JPH02500604A (en)
AU (1) AU599722B2 (en)
FI (1) FI75000C (en)
NZ (1) NZ222366A (en)
WO (1) WO1988003189A1 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI92846C (en) * 1989-10-05 1995-01-10 Sunds Defibrator Jylha Oy Process for refining pulp mixture in a refiner
FI85882C (en) * 1989-10-05 1992-06-10 Sunds Defibrator Jylha Oy RAFFINOER FOER RAFFINERING AV PAPPERSMASSOR ELLER DYLIKA.
FI85391C (en) * 1989-10-05 1992-04-10 Sunds Defibrator Jylha Oy Konraffinör
US5248099A (en) * 1991-04-05 1993-09-28 Andritz Sprout-Bauer, Inc. Three zone multiple intensity refiner
US5335865A (en) * 1992-06-26 1994-08-09 Andritz Sprout-Bauer, Inc. Two-stage variable intensity refiner
DE102005004344B4 (en) * 2005-01-31 2007-10-04 Voith Patent Gmbh Process for grinding aqueous suspended pulp fibers
SE541111C2 (en) 2017-06-19 2019-04-09 Valmet Oy Steam evacuation in a pulp or fiber refiner

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NO127870B (en) * 1966-10-27 Kamyr Ab,Sw
GB2083375A (en) * 1980-09-08 1982-03-24 Cell Dev Inc Disc mills
US4378092A (en) * 1980-10-27 1983-03-29 Cell Develop, Inc. Method and apparatus for grinding pulp stock in pulp defibrating apparatus of the double rotating disc type
AU2576384A (en) * 1983-02-22 1984-09-10 Sunds Defibrator Aktiebolag Method and apparatus for manufacturing fibre pulp
SE435737B (en) * 1983-03-09 1984-10-15 Sunds Defibrator SET AND DEVICE FOR WHOLE OR PARTIAL RECOVERY OF ANGA, WHICH IS SUPPLIED OR GENERATED BY A PROCESS FOR THE PRODUCTION OF FIBER MASS SET AND DEVICE FOR WHOLE OR PARTIAL RECOVERY OF ANGA, WHICH IS ADDED OR GENERATED BY A PROCESS FOR A PROCESS

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO8803189A1 *

Also Published As

Publication number Publication date
JPH02500604A (en) 1990-03-01
AU599722B2 (en) 1990-07-26
FI864442A0 (en) 1986-10-31
FI75000B (en) 1987-12-31
WO1988003189A1 (en) 1988-05-05
NZ222366A (en) 1989-07-27
FI75000C (en) 1988-04-11
AU8155087A (en) 1988-05-25

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