EP0423092A2 - Procedure for the refining of a pulp mixture or equivalent in a refiner - Google Patents

Procedure for the refining of a pulp mixture or equivalent in a refiner Download PDF

Info

Publication number
EP0423092A2
EP0423092A2 EP90850322A EP90850322A EP0423092A2 EP 0423092 A2 EP0423092 A2 EP 0423092A2 EP 90850322 A EP90850322 A EP 90850322A EP 90850322 A EP90850322 A EP 90850322A EP 0423092 A2 EP0423092 A2 EP 0423092A2
Authority
EP
European Patent Office
Prior art keywords
refiner
returned
pulp
blades
refining
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Withdrawn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
EP90850322A
Other languages
German (de)
French (fr)
Other versions
EP0423092A3 (en
Inventor
Jorma Lumiainen
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 EP0423092A2 publication Critical patent/EP0423092A2/en
Publication of EP0423092A3 publication Critical patent/EP0423092A3/en
Withdrawn legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20Methods of refining
    • D21D1/22Jordans
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20Methods of refining
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20Methods of refining
    • D21D1/30Disc mills

Definitions

  • the present invention relates to a procedure for the refin­ing of a pulp mixture or equivalent in a refiner comprising oppositely placed refiner blades, of which the rotor blade rotates and the stator blade is stationary, a pulp refining zone being formed between the blades.
  • the motion of the rotor blade relative to the stator blade gives rise to a strong turbulence of the pulp mixture in the grooves of the blades.
  • the pulp flows in the refiner in various directions.
  • the pulp flows towards the delivery side in the grooves of both blades.
  • the pulp in addition to the flow to­wards the delivery side, the pulp also flows transversely from the rotor blade to the stator blade and vice versa, and in the grooves of the stator blade the pulp also flows back towards the infeed side.
  • the object of the invention is to create a procedure that achieves this aim.
  • the pro­cedure of the invention is characterized in that, by making use of the forces generated by the rotation of the rotor blade, the pulp mixture is separated into fractions or part of the pulp mixture is directed away from the area of the refiner blades for fractionation.
  • a preferred embodiment of the invention is characterized in that at least one of the fractions obtained is returned to the same refiner.
  • Another preferred embodiment of the invention is character­ized in that at least one of the fractions obtained is returned to a separate refiner designed for this fraction.
  • Yet another preferred embodiment of the invention is char­acterized in that the fraction to be returned is returned to the infeed side of the refiner.
  • An advantage provided by the procedure of the invention is that it makes it possible to refine those fractions which need refining and to avoid overrefining fractions already refined.
  • Fig. 1 illustrates the turbulent flow occurring in the grooves 5, 4 between the rotor blade 1 and the stator blade 2.
  • the rotor blade rotates in the direction indicated by arrow 3.
  • the grooves of the rotor blade are directly opposite to those of the stator blade.
  • the rotor blade 1 has turned a little to the right.
  • Fig. 2 illustrates the internal pulp flow within the re­finer.
  • the pulp flows in several direc­tions.
  • the pulp flows in the grooves 4, 5 of both the stator 2 and the rotor 1 blades towards the delivery side 6.
  • the pulp also flows transversely from the rotor blade 1 to the stator blade 2 and from the stator blade back to the rotor blade, and in the grooves 4 of the stator blade 2 the pulp also flows back towards the infeed side 7.
  • the different directions of flow are indicated with arrows in fig. 2.
  • Fig. 3 illustrates the principle on which the refiner is utilized for separating pulp into fractions.
  • the direction of rotation of the rotor blade 1 is again indicated by arrow 3.
  • the procedure of the invention makes use of the motion of the rotor blade 1 (circumferential speed approx. 15-40 m/s) to achieve fractionation at points 8 and 10, where the pulp mixture is separated into corresponding fractions 8a, 8b, 8c and 10a, 10b, 10c. It is also possible to direct part of the pulp mixture out of the refiner at point 9 for external fractionation, resulting in fractions 9a, 9b, 9c. At least one of the fractions obtained is re­turned either to the same refiner or to a different refiner designed for the refining of this particular fraction.
  • This fraction can be returned either to the infeed side 7, to the area of the refining zone or to the return flow taking place from the delivery side 6 to the stator blade 2.
  • the invention is in no way restricted by the manner in which the forces generated by the rotary motion of the rotor blade are utilized for fractionation.
  • the possible alternatives are e.g. the use of top separators in conjunction with the refiner blades, a hole or holes made through the blades, various screens etc.

Abstract

1. Procedure for the refining of a pulp mixture or equivalent in a refiner comprising oppositely placed refiner blades (1, 2), of which the rotor blade (1) rotates and the stator blade (2) is stationary, a pulp refining zone being formed between the blades. In the refiners currently used, there is no adequate provision for ensuring that the refiner will refine that fraction which has not yet been refined or that the fractions already refined will not be over-refined. The procedure of the invention solves this problem in that, by making use of the forces generated by the rotation of the rotor blade (1), the pulp mixture is separated into fractions or part of the pulp mixture is directed away from the area of the refiner blades for fractionation.

Description

  • The present invention relates to a procedure for the refin­ing of a pulp mixture or equivalent in a refiner comprising oppositely placed refiner blades, of which the rotor blade rotates and the stator blade is stationary, a pulp refining zone being formed between the blades.
  • As is well known, the motion of the rotor blade relative to the stator blade gives rise to a strong turbulence of the pulp mixture in the grooves of the blades. During the re­fining process, the pulp flows in the refiner in various directions. At the infeed end of the refining zone, the pulp flows towards the delivery side in the grooves of both blades. In the refining zone, in addition to the flow to­wards the delivery side, the pulp also flows transversely from the rotor blade to the stator blade and vice versa, and in the grooves of the stator blade the pulp also flows back towards the infeed side.
  • As the pulp mixture fed into the refiner is inhomogeneous, containing different fibre fractions, it is essential for the achievement of good refining results that it should be possible to refine those fractions which need refining and to avoid overrefining fractions already refined as well as to avoid superfluous and damaging refining of fractions which need no refining at all. The object of the invention is to create a procedure that achieves this aim. The pro­cedure of the invention is characterized in that, by making use of the forces generated by the rotation of the rotor blade, the pulp mixture is separated into fractions or part of the pulp mixture is directed away from the area of the refiner blades for fractionation.
  • A preferred embodiment of the invention is characterized in that at least one of the fractions obtained is returned to the same refiner.
  • Another preferred embodiment of the invention is character­ized in that at least one of the fractions obtained is returned to a separate refiner designed for this fraction.
  • Yet another preferred embodiment of the invention is char­acterized in that the fraction to be returned is returned to the infeed side of the refiner.
  • An advantage provided by the procedure of the invention is that it makes it possible to refine those fractions which need refining and to avoid overrefining fractions already refined.
  • In the following, the invention is described in detail by the aid of examples of preferred embodiments by referring to the attached drawings, in which
    • Fig. 1 illustrates the priniciple of the turbulence occurring in the grooves of the refiner blades at two different stages.
    • Fig. 2 illustrates the principle of pulp flow within the refiner.
    • Fig. 3 illustrates the principle of fractionation by the procedure of the invention.
  • Fig. 1 illustrates the turbulent flow occurring in the grooves 5, 4 between the rotor blade 1 and the stator blade 2. The rotor blade rotates in the direction indicated by arrow 3. In the first picture the grooves of the rotor blade are directly opposite to those of the stator blade. In the second picture, the rotor blade 1 has turned a little to the right.
  • Fig. 2 illustrates the internal pulp flow within the re­finer. During refining, the pulp flows in several direc­tions. At the entry end of the refining zone, the pulp flows in the grooves 4, 5 of both the stator 2 and the rotor 1 blades towards the delivery side 6. In the refining zone, besides flowing towards the delivery side 6, the pulp also flows transversely from the rotor blade 1 to the stator blade 2 and from the stator blade back to the rotor blade, and in the grooves 4 of the stator blade 2 the pulp also flows back towards the infeed side 7. The different directions of flow are indicated with arrows in fig. 2.
  • Fig. 3 illustrates the principle on which the refiner is utilized for separating pulp into fractions. The direction of rotation of the rotor blade 1 is again indicated by arrow 3. The procedure of the invention makes use of the motion of the rotor blade 1 (circumferential speed approx. 15-40 m/s) to achieve fractionation at points 8 and 10, where the pulp mixture is separated into corresponding fractions 8a, 8b, 8c and 10a, 10b, 10c. It is also possible to direct part of the pulp mixture out of the refiner at point 9 for external fractionation, resulting in fractions 9a, 9b, 9c. At least one of the fractions obtained is re­turned either to the same refiner or to a different refiner designed for the refining of this particular fraction. This fraction can be returned either to the infeed side 7, to the area of the refining zone or to the return flow taking place from the delivery side 6 to the stator blade 2.
  • The invention is in no way restricted by the manner in which the forces generated by the rotary motion of the rotor blade are utilized for fractionation. Among the possible alternatives are e.g. the use of top separators in conjunction with the refiner blades, a hole or holes made through the blades, various screens etc.
  • It is obvious to a person skilled in the art that of the invention is not restricted to the examples of its embodi­ments described above, but that it may instead be varied within the scope of the following claims.

Claims (6)

1. Procedure for the refining of a pulp mixture or equiva­lent in a refiner comprising oppositely placed refiner blades (1, 2), of which the rotor blade (1) rotates and the stator blade (2) is stationary, a pulp refining zone being formed between the blades, characterized in that, by making use of the forces generated by the rotation of the rotor blade (1), the pulp mixture is separated into fractions or part of the pulp mixture is directed away from the area of the refiner blades for fractionation.
2. Procedure according to claim 1, character­ized in that at least one of the fractions obtained (8a-c, 9a-c, 10a-c) is returned to the same refiner.
3. Procedure according to claim 1, character­ized in that at least one of the fractions obtained (8a-c, 9a-c, 10a-c) is returned to a separate refiner designed for this fraction.
4. Procedure according to claim 2 or 3, charac­terized in that the fraction to be returned (8a-c, 9a-c, 10a-c) is returned to the infeed side of the refiner.
5. Procedure according to claim 2 or 3, charac­terized in that the fraction to be returned (8a-c, 9a-c, 10a-c) is returned to the area of the refining zone of the refiner.
6. Procedure according to claim 2 or 3, charac­terized in that the fraction to be returned (8a-c, 9a-c, 10a-c) is returned to the return flow taking place from the delivery side (6) of the refiner to the stator blade (2).
EP19900850322 1989-10-05 1990-10-01 Procedure for the refining of a pulp mixture or equivalent in a refiner Withdrawn EP0423092A3 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI894730 1989-10-05
FI894730A FI92846C (en) 1989-10-05 1989-10-05 Process for refining pulp mixture in a refiner

Publications (2)

Publication Number Publication Date
EP0423092A2 true EP0423092A2 (en) 1991-04-17
EP0423092A3 EP0423092A3 (en) 1992-03-25

Family

ID=8529101

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19900850322 Withdrawn EP0423092A3 (en) 1989-10-05 1990-10-01 Procedure for the refining of a pulp mixture or equivalent in a refiner

Country Status (2)

Country Link
EP (1) EP0423092A3 (en)
FI (1) FI92846C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111270544A (en) * 2020-02-27 2020-06-12 安德里茨(中国)有限公司 Refiner grinding disc, refiner, rotor and refiner

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1343452A (en) * 1957-05-24 1963-11-22 Process for defibrating and refining cellulosic materials
FR1508780A (en) * 1966-02-01 1968-01-05 Celleco Ab Pulp pounding process
WO1988000992A1 (en) * 1986-08-07 1988-02-11 Sunds Defibrator Aktiebolag Apparatus for treatment of fibre suspensions
WO1988003189A1 (en) * 1986-10-31 1988-05-05 Sunds Defibrator Jylhä Oy Refiner
US4820381A (en) * 1987-02-25 1989-04-11 Internationa Paper Company Pulp refiner with fluidizing inlet

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1343452A (en) * 1957-05-24 1963-11-22 Process for defibrating and refining cellulosic materials
FR1508780A (en) * 1966-02-01 1968-01-05 Celleco Ab Pulp pounding process
WO1988000992A1 (en) * 1986-08-07 1988-02-11 Sunds Defibrator Aktiebolag Apparatus for treatment of fibre suspensions
WO1988003189A1 (en) * 1986-10-31 1988-05-05 Sunds Defibrator Jylhä Oy Refiner
US4820381A (en) * 1987-02-25 1989-04-11 Internationa Paper Company Pulp refiner with fluidizing inlet

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
TAPPI vol. 65, no. 7, 1 July 1982, ATLANTA pages 80 - 83; FOX, BRODKEY AND NISSAN: 'INSIDE A DISK REFINER' *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111270544A (en) * 2020-02-27 2020-06-12 安德里茨(中国)有限公司 Refiner grinding disc, refiner, rotor and refiner
CN111270544B (en) * 2020-02-27 2022-02-01 安德里茨(中国)有限公司 Refiner grinding disc, refiner, rotor and refiner

Also Published As

Publication number Publication date
FI92846C (en) 1995-01-10
FI894730A0 (en) 1989-10-05
FI894730A (en) 1991-04-06
FI92846B (en) 1994-09-30
EP0423092A3 (en) 1992-03-25

Similar Documents

Publication Publication Date Title
US4776957A (en) Rotating element for a screening apparatus with a contour surface
KR900002099B1 (en) High consistency pressure screen and method of separating accepts and rejects
SE502906C2 (en) Refining elements
ATE69995T1 (en) COMBINED MIXING AND CONVEYING DEVICE FOR HIGH VISCOSE LIQUIDS.
JP2000512707A (en) Rotor of turbine machine having blades mountable in groove and rotor blades
ES471837A1 (en) Impact decorticator
DE20001236U1 (en) fan
EP0423092A2 (en) Procedure for the refining of a pulp mixture or equivalent in a refiner
FI88414C (en) Device for treating fiber suspension
FI77481C (en) Strainer.
KR950015907A (en) Rotor of rolling electric machine
US5918822A (en) Channeled pulp rotor
JPH02118190A (en) Pulper
DE2315786A1 (en) METHOD OF PUMPING LIQUID METALS BY IMPACT AND PUMP TO PERFORM THIS PROCEDURE
JPS61207689A (en) Screening apparatus
FI85882B (en) RAFFINOER FOER RAFFINERING AV PAPPERSMASSOR ELLER DYLIKA.
EP3430197B1 (en) Method for screening and a screening apparatus
CN208973567U (en) A kind of food processing machine crushing knife
CN208372850U (en) A kind of cleaning agent high speed emulsion dispersion mechanism
EP0421968A2 (en) Conical refiner
AU7293100A (en) Method and device for processing pulp
US20110253327A1 (en) Method for refining cellulose fibers in aqueous suspension as well as refiner filling to implement said method
CN210993807U (en) Emulsifying machine head and high-shear emulsifying machine
JPS63158028A (en) Cutter for mixer
SU1423147A1 (en) Mixer

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT DE FR GB IT SE

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT DE FR GB IT SE

17P Request for examination filed

Effective date: 19920408

17Q First examination report despatched

Effective date: 19940323

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 19941003