EP0279022A1 - Méthode et installation pour triturer de la pâte de papier - Google Patents

Méthode et installation pour triturer de la pâte de papier Download PDF

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Publication number
EP0279022A1
EP0279022A1 EP87114370A EP87114370A EP0279022A1 EP 0279022 A1 EP0279022 A1 EP 0279022A1 EP 87114370 A EP87114370 A EP 87114370A EP 87114370 A EP87114370 A EP 87114370A EP 0279022 A1 EP0279022 A1 EP 0279022A1
Authority
EP
European Patent Office
Prior art keywords
mixer
consistency
opening
pulp
sieve
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.)
Granted
Application number
EP87114370A
Other languages
German (de)
English (en)
Other versions
EP0279022B1 (fr
Inventor
Jochen Krebs
Heinrich Lang
Wolfgang Dr. Siewert
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.)
Sulzer Escher Wyss GmbH
Original Assignee
Sulzer Escher Wyss GmbH
Escher Wyss GmbH
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 Sulzer Escher Wyss GmbH, Escher Wyss GmbH filed Critical Sulzer Escher Wyss GmbH
Priority to AT87114370T priority Critical patent/ATE67254T1/de
Publication of EP0279022A1 publication Critical patent/EP0279022A1/fr
Application granted granted Critical
Publication of EP0279022B1 publication Critical patent/EP0279022B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • D21B1/30—Defibrating by other means
    • D21B1/34—Kneading or mixing; Pulpers
    • D21B1/345—Pulpers

Definitions

  • the invention relates to a method according to the preamble of claim 1 and an installation for carrying out the method according to the preamble of claim 7.
  • the previously known high consistency pulper with the connected dilution devices work overall with interruptions, each time after processing a filling of the high-consistency detergent, the latter is emptied, and after the content has been diluted and possibly cleaned, a new filling is processed.
  • the invention aims to provide a method of the type mentioned which is suitable for continuous work.
  • the method according to claims 4 to 6 is suitable for contaminated raw materials, such as waste paper.
  • Claims 7 to 16 relate to the system for carrying out the method, and they relate to particularly advantageous and novel details.
  • FIG. 1 shows a system which contains a high-consistency pulper 1 and a mixer 2.
  • the high-consistency pulper 1 contains two dissolving elements 5 and 6 driven by motors 3 and 4.
  • the mixer 2 contains a mixing element 8 driven by a motor 7, e.g. a stirring propeller. Behind the mixing element 8 there is a sieve 10, which delimits an accepting material space 11, from which an outlet line 12 with a pump 13 leads from the system to the outside.
  • the pulper 1 and the mixer 2 are connected by an opening 14 in the lower region of the wall 15 of the high-consistency pulper.
  • the water supply from a line 9 is designated W, the supply of undissolved substance with B.
  • 1 bale B of the undissolved substance with the appropriate amount of water is fed into the high-consistency pulper, so that when the pulp is dissolved, the consistency of the partially dissolved pulp is 10 to 20%. With this consistency, the paper stock is crumbly, i.e. not pumpable with centrifugal pumps.
  • the system according to FIG. 2 serves to dissolve contaminated raw material, e.g. Waste paper.
  • the system according to FIG. 2 is provided with a cleaning circuit which contains a schematically represented sieving device 20, e.g. a drum screen with collecting pan 21 for the continuous material and an overflow 22 for the overflow material, which is separated out and deposited.
  • a schematically represented sieving device 20 e.g. a drum screen with collecting pan 21 for the continuous material and an overflow 22 for the overflow material, which is separated out and deposited.
  • the screening device 20 is connected to the mixer 2 by a line 23.
  • a line 24 leads from the collecting trough 21 back into the high-consistency solver 1.
  • a line 25 connects the on Sump pan 21 with an accept material space 26 of the high-consistency fabric solver 1. This is formed in a manner known per se behind a sieve 27, along which the arms of the dissolving member 5 move during operation.
  • An outlet line 28 with a pump 30 leads outward from the accepted substance space 26.
  • the pulp suspension is fed from the interior of the mixer 2 to the screening device 20, in which the existing impurities, such as plastic films, etc., are excreted.
  • the cleaned pulp suspension was fed through line 25 to the accept material space 26 and serves to dilute crumbly fibrous material which passes from the high-consistency material dissolver 1 into the accept material space 26 through the sieve 27.
  • the pulp suspension obtained is discharged through line 28.
  • the system shown in FIG. 2 can be operated in such a way that the part of the sieve pass of the sieve device 20 which is returned through the line 24 into the high-consistency pulp solver represents its only supply of water which serves to dissolve the bales B.
  • the excess sieve pass ie the diluted paper stock suspension, passes through line 25 into the accept material space 26 and out of this through line 28 as accept material.
  • Water can be added as required through a connection 29, a centrifugal pump 30 ensuring good mixing of the water with the paper stock suspension from line 25 and with the diluted, originally crumbly material which has passed through the sieve 27 into the accept material room 26 .
  • the housing 16 of the mixer 2 at the location of the opening 14 has a larger diameter E than the diameter D of the opening 14.
  • an annular flow of the already diluted paper stock suspension around the crumbly material penetrating through the opening 14 is formed, which is thereby prevented from flowing back into the high-consistency pulp remover 1.
  • the housing 16 is designed such that it tapers conically away from the opening 14. This supports a circulating flow in the housing 16 in its axial plane.
  • the mixer 2 is preferably firmly connected to the high consistency pulper 1 as a mechanical unit, e.g. by welding the housing 16 to the housing 15 of the pulper 1.
  • the size of the opening 14 is selected so that it allows the installation and removal of the mixing element 8 and, in the embodiment according to FIG. 1, the sieve 10 from the pulper 1 allows.
  • FIGS. 3 and 4 show possibilities for controlling the movement of the crumbly substance from the material dissolver 1 into the mixer 2.
  • the opening 14 is assigned an adjustable flap K, which, depending on its position, more or less supports the movement by deflecting a larger or smaller part of the circulating flow U into the opening 14, or the flow from the pulper 1 in the mixer 2 brakes (position K ⁇ in Figure 3).
  • an opening screw S is assigned to the opening 14, which can run faster or slower as required and thus accelerates or slows down the flow from the pulper 1 into the mixer 2.
  • this figure shows a mixer 2 with a vertical axis, which can also be provided within the scope of the invention.
EP87114370A 1987-01-20 1987-10-01 Méthode et installation pour triturer de la pâte de papier Expired - Lifetime EP0279022B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT87114370T ATE67254T1 (de) 1987-01-20 1987-10-01 Verfahren sowie anlage zur aufloesung von papierstoff.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH19487 1987-01-20
CH194/87 1987-01-20

Publications (2)

Publication Number Publication Date
EP0279022A1 true EP0279022A1 (fr) 1988-08-24
EP0279022B1 EP0279022B1 (fr) 1991-09-11

Family

ID=4181400

Family Applications (1)

Application Number Title Priority Date Filing Date
EP87114370A Expired - Lifetime EP0279022B1 (fr) 1987-01-20 1987-10-01 Méthode et installation pour triturer de la pâte de papier

Country Status (3)

Country Link
EP (1) EP0279022B1 (fr)
AT (1) ATE67254T1 (fr)
DE (2) DE3704461A1 (fr)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2650768A1 (fr) * 1989-08-10 1991-02-15 Voith Gmbh Procede pour traiter les vieux papiers et installation pour la mise en oeuvre du procede
EP0414602A2 (fr) * 1989-08-21 1991-02-27 Valmet Paper Machinery Inc. Procédé et dispositif pour la séparation d'impuretés d'une pâte à papier dans des pulpeurs
WO1994009202A1 (fr) * 1992-10-20 1994-04-28 Valmet-Tampella Inc. Melangeur utilise pour la reduction en pate
EP1347093A1 (fr) * 2002-03-19 2003-09-24 Comer SpA Hélice de brassage de suspensions solides-liquides dans un réservoir de traitement
WO2008099180A1 (fr) 2007-02-16 2008-08-21 Brunob Ii B. V. Appareil et procédés de mélange et de distribution d'échantillons liquides ou pulvérulents
WO2014139502A1 (fr) * 2013-03-15 2014-09-18 Hans-Joachim Boltersdorf Liquéfacteur pourvu d'un tube de transport et procédé pour faire fonctionner un liquéfacteur
CN104846677A (zh) * 2015-05-26 2015-08-19 苏州达泰佳机械科技有限公司 一种纸浆生产装置
CN106638097A (zh) * 2016-10-18 2017-05-10 中山市为客包装制品有限公司 造纸打浆机
CN108547168A (zh) * 2018-04-27 2018-09-18 江苏妙卫纸业有限公司 一种卫生纸多工艺一体化生产加工设备
CN108978299A (zh) * 2018-07-23 2018-12-11 恒安（重庆）生活用纸有限公司 一种水力碎浆装置
CN109403113A (zh) * 2018-11-30 2019-03-01 赵颖颖 一种基于流体循环压强差搅拌的瓦楞废纸环保回收装置
CN109594379A (zh) * 2018-12-06 2019-04-09 徐州利华环保科技有限公司 一种连续式多级水力碎浆机及其工作方法
CN110644268A (zh) * 2019-10-15 2020-01-03 中顺洁柔（云浮）纸业有限公司 一种纸巾生产的碎浆机结构

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109322198A (zh) * 2018-12-06 2019-02-12 徐州利华环保科技有限公司 一种高效搅拌结构的碎浆机及其工作方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3474972A (en) * 1966-06-02 1969-10-28 Tadashi Kobayashi Device for simultaneously making pulp,cleaning and screening paper
GB2015594A (en) * 1978-03-07 1979-09-12 Escher Wyss Gmbh Treating waste paper for the production of new paper
EP0073609A2 (fr) * 1981-08-20 1983-03-09 The Black Clawson Company Tamis rotatif
FR2529593A1 (fr) * 1982-07-02 1984-01-06 Voith Gmbh Procede et appareil de traitement de papier de recuperation
EP0120766A1 (fr) * 1983-03-25 1984-10-03 E. + M. Lamort Société Anonyme dite: Procédé et dispositif de triage d'un mélange de pâte à papier et d'impuretés
EP0123068A2 (fr) * 1983-03-26 1984-10-31 J.M. Voith GmbH Procédé pour l'élimination d'un pulper
AT378792B (de) * 1983-01-25 1985-09-25 Ferrometall Eisen Und Schrotth Verfahren zum wiedergewinnen der einzelkomponenten aus mit metallfolie, insbesondere aluminiumfolie,kaschiertem papier oder karton

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2441681A1 (fr) * 1978-11-17 1980-06-13 Lamort E & M Perfectionnements aux procedes et appareils de desintegration de matieres cellulosiques
DE3334448A1 (de) * 1982-10-19 1984-04-19 J.M. Voith Gmbh, 7920 Heidenheim Stoffloeser

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3474972A (en) * 1966-06-02 1969-10-28 Tadashi Kobayashi Device for simultaneously making pulp,cleaning and screening paper
GB2015594A (en) * 1978-03-07 1979-09-12 Escher Wyss Gmbh Treating waste paper for the production of new paper
EP0073609A2 (fr) * 1981-08-20 1983-03-09 The Black Clawson Company Tamis rotatif
FR2529593A1 (fr) * 1982-07-02 1984-01-06 Voith Gmbh Procede et appareil de traitement de papier de recuperation
AT378792B (de) * 1983-01-25 1985-09-25 Ferrometall Eisen Und Schrotth Verfahren zum wiedergewinnen der einzelkomponenten aus mit metallfolie, insbesondere aluminiumfolie,kaschiertem papier oder karton
EP0120766A1 (fr) * 1983-03-25 1984-10-03 E. + M. Lamort Société Anonyme dite: Procédé et dispositif de triage d'un mélange de pâte à papier et d'impuretés
EP0123068A2 (fr) * 1983-03-26 1984-10-31 J.M. Voith GmbH Procédé pour l'élimination d'un pulper

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2650768A1 (fr) * 1989-08-10 1991-02-15 Voith Gmbh Procede pour traiter les vieux papiers et installation pour la mise en oeuvre du procede
EP0414602A2 (fr) * 1989-08-21 1991-02-27 Valmet Paper Machinery Inc. Procédé et dispositif pour la séparation d'impuretés d'une pâte à papier dans des pulpeurs
EP0414602A3 (en) * 1989-08-21 1991-09-25 Oy Tampella Ab Method and apparatus for removing impurities from paper pulp in pulpers
US5125584A (en) * 1989-08-21 1992-06-30 Oy Tampella Ab Method and apparatus for removing impurities from paper pulp in pulpers
WO1994009202A1 (fr) * 1992-10-20 1994-04-28 Valmet-Tampella Inc. Melangeur utilise pour la reduction en pate
AU669012B2 (en) * 1992-10-20 1996-05-23 Valmet Corporation Mixing device in pulping
US5681429A (en) * 1992-10-20 1997-10-28 Valmet Paper Machinery Inc. Mixing device in pulping
EP1347093A1 (fr) * 2002-03-19 2003-09-24 Comer SpA Hélice de brassage de suspensions solides-liquides dans un réservoir de traitement
WO2008099180A1 (fr) 2007-02-16 2008-08-21 Brunob Ii B. V. Appareil et procédés de mélange et de distribution d'échantillons liquides ou pulvérulents
AU2008215918B2 (en) * 2007-02-16 2012-05-17 Corn Products Development, Inc. Apparatus for and methods of mixing and dispensing liquid or powdery samples
WO2014139502A1 (fr) * 2013-03-15 2014-09-18 Hans-Joachim Boltersdorf Liquéfacteur pourvu d'un tube de transport et procédé pour faire fonctionner un liquéfacteur
CN104846677A (zh) * 2015-05-26 2015-08-19 苏州达泰佳机械科技有限公司 一种纸浆生产装置
CN104846677B (zh) * 2015-05-26 2017-01-04 浙江康诚工业产品设计有限公司 一种纸浆生产装置
CN106638097A (zh) * 2016-10-18 2017-05-10 中山市为客包装制品有限公司 造纸打浆机
CN108547168A (zh) * 2018-04-27 2018-09-18 江苏妙卫纸业有限公司 一种卫生纸多工艺一体化生产加工设备
CN108978299A (zh) * 2018-07-23 2018-12-11 恒安（重庆）生活用纸有限公司 一种水力碎浆装置
CN109403113A (zh) * 2018-11-30 2019-03-01 赵颖颖 一种基于流体循环压强差搅拌的瓦楞废纸环保回收装置
CN109403113B (zh) * 2018-11-30 2020-07-28 浙江富兴服装有限公司 一种基于流体循环压强差搅拌的瓦楞废纸环保回收装置
CN109594379A (zh) * 2018-12-06 2019-04-09 徐州利华环保科技有限公司 一种连续式多级水力碎浆机及其工作方法
CN110644268A (zh) * 2019-10-15 2020-01-03 中顺洁柔（云浮）纸业有限公司 一种纸巾生产的碎浆机结构
CN110644268B (zh) * 2019-10-15 2020-12-01 中顺洁柔（云浮）纸业有限公司 一种纸巾生产的碎浆机结构

Also Published As

Publication number Publication date
DE3772967D1 (de) 1991-10-17
ATE67254T1 (de) 1991-09-15
DE3704461C2 (fr) 1992-10-22
EP0279022B1 (fr) 1991-09-11
DE3704461A1 (de) 1988-07-28

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