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WO1990006394A1 - Dispositif de lavage de copeaux - Google Patents

Dispositif de lavage de copeaux Download PDF

Info

Publication number
WO1990006394A1
WO1990006394A1 PCT/SE1989/000669 SE8900669W WO9006394A1 WO 1990006394 A1 WO1990006394 A1 WO 1990006394A1 SE 8900669 W SE8900669 W SE 8900669W WO 9006394 A1 WO9006394 A1 WO 9006394A1
Authority
WO
WIPO (PCT)
Prior art keywords
chute
tank
chips
outlet
scrap
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.)
Ceased
Application number
PCT/SE1989/000669
Other languages
English (en)
Inventor
R. Baltsar Lundgren
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.)
Valmet AB
Original Assignee
Sunds Defibrator Industries AB
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 Industries AB filed Critical Sunds Defibrator Industries AB
Priority to FI912523A priority Critical patent/FI912523A7/fi
Publication of WO1990006394A1 publication Critical patent/WO1990006394A1/fr
Priority to NO912007A priority patent/NO912007D0/no
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/02Pretreatment of the raw materials by chemical or physical means
    • D21B1/023Cleaning wood chips or other raw materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/62Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/62Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
    • B03B5/626Helical separators
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C1/00Pretreatment of the finely-divided materials before digesting
    • D21C1/02Pretreatment of the finely-divided materials before digesting with water or steam

Definitions

  • This invention relates to the washing of chips from wood material.
  • the manutacture pT pulp normally proceeds from wood material, which was chipped to small pieces, so-called chips. With these chips also follow along heavy impurit ⁇ ies (scrap) such as gravel,, metal pieces and the like. These impurities must be removed before the chips chem ⁇ ically or mechanically are disintegrated to pulp. This removal takes place in a so-called chip washer, which can be designed in different ways.
  • the washing of the chips usually is carried out in two steps.
  • the first step comprises the removal of heavy impurities in a container, in which chips and water are stirred by a rotor provided with blades, whereby the impurities sink to the bottom. Thereafter sand- and finer impurities are removed in a screw thickener. Between these steps the chips are collected in a tank, from which they are pumped to the second step.
  • This conventional equipment has its weakness, because at a smaller size and weight of the impurities the separ ⁇ ation is uncertain, due to the fact that the particles to te separated are not caused to move to some separation zone, but are stirred together with the chips.
  • the present invention offers a solution of the aforesaid problem.
  • a tank equipped with a screw-shaped chute for chips and water the impurities can be separated along a relatively long sedimentation path and simultan ⁇ eously be affected by the centrifugal force. Chips and water, besides, are discharged continuously while at the same time the impurities are concentrated and thereby their separation is facilitated.
  • the invention implies that the first separation step and the pump tank in a conventional arrangement can be replaced by a device, which can be connected directly to the subsequent thickener.
  • Pig. 1 is a section through a device according to the invention, and Pig. 2 is a section II-II of the same device as shown in Pig. 1.
  • This embodiment of the invention comprises a cylindric tank 1, the size of which, of course, depends on the desir ⁇ ed capacity.
  • the tank can have a diameter, for example, of 1,5-3 m.
  • a chute 2 which extends in the form of a screw slightly more than one turn about the tank wall. Por achieving a satisfactory separation effect, the length of the chute 2 in the tank should be at least half a turn. Preferably the length should be at least one turn.
  • An inlet 3 for chips and water is located upwardly in the tank 1 at the upper end of the chute 2.
  • the chute is outwardly defined by the tank wall and inwardly by an edge 4, the height of which decreases downward along the chute.
  • the chute bottom is inclined outward to the tank wall, which inclination increases along the chute.
  • the chute can be steeper at the beginning.
  • the chute In its first part, preferably in its first quarter, the chute can also be provided with unevennesses or steps in the bottom, while its subsequent part should be smooth.
  • a scrap outlet 5 is located at the end of the chute adjacent the tank wall.
  • Said scrap outlet preferably is designed for interval discharge, i.e. provided with two valves open ⁇ ing altematingly.
  • a water supply conduit 6 is.connected to the scrap outlet 5 in order to bring about a counterflow through the scrap outlet.
  • the bottom of the tank 1 is ishaped conically so as to slope down to a central outlet 7 for washed chips. About the outlet 7 possibly one or several additional annular scrap traps 8 can be arranged. In connection to these traps openings can be located for manual emptying.
  • the chips to be washed are supplied together with water through the inlet 1 down into the chute 2 and follow the chute downward. Heavy objects and particles are collected by sedimentation on the chute bottom.
  • the separation of scrap is increased by action of the centrifugal force and by the fact, that the chute bottom is inclined outward to the tank wall. Unevennesses in the bottom of the first part of the chute and a steeper inclination promote the scrap removal in this ⁇ part of the chute, while in the subsequent part of the chute sedimentation is desired.
  • the additional scrap traps 8 which can be arranged about the central outlet, are a safety at extreme scrap loads which in exceptional cases can arise. Such loads may, for example, occur when the chips are taken with a bottom scraping device of a chip bucket from a chip plane.
  • the invention is not restricted to the embodim ⁇ ent shown, but can be varied within the scope of the in ⁇ vention idea.

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Detergent Compositions (AREA)
  • Paper (AREA)

Abstract

Dispositif de lavage de copeaux comprenant un réservoir cylindrique (1) muni en son sommet d'une entrée pour les copeaux et l'eau, ladite entrée étant placée directement devant la glissière (2), qui descend en forme de vis d'au moins un demi-tour à l'intérieur du réservoir (1). Une glissière (2) est délimitée extérieurement par la paroi du réservoir et intérieurement par une bordure (4) dont la hauteur diminue du haut vers le bas de la glissière. Au bout de la glissière et adjacent à la paroi du réservoir se trouve une sortie de déchets (5). Le fond du réservoir s'incline vers une sortie centrale.
PCT/SE1989/000669 1988-11-25 1989-11-20 Dispositif de lavage de copeaux Ceased WO1990006394A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
FI912523A FI912523A7 (fi) 1988-11-25 1989-11-20 Hakkeen puhdistuslaite
NO912007A NO912007D0 (no) 1988-11-25 1991-05-24 Anordning for flisvasking.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8804261-9 1988-11-25
SE8804261A SE462566B (sv) 1988-11-25 1988-11-25 Anordning foer tvaettning av flis

Publications (1)

Publication Number Publication Date
WO1990006394A1 true WO1990006394A1 (fr) 1990-06-14

Family

ID=20374062

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SE1989/000669 Ceased WO1990006394A1 (fr) 1988-11-25 1989-11-20 Dispositif de lavage de copeaux

Country Status (8)

Country Link
EP (1) EP0445143A1 (fr)
JP (1) JPH04501891A (fr)
AU (1) AU4522189A (fr)
CA (1) CA2003768A1 (fr)
FI (1) FI912523A7 (fr)
NZ (1) NZ231500A (fr)
SE (1) SE462566B (fr)
WO (1) WO1990006394A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114180343A (zh) * 2021-10-29 2022-03-15 淮北矿业股份有限公司 一种输灰系统改造方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4857094B2 (ja) * 2006-12-01 2012-01-18 前澤工業株式会社 沈砂分離設備

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2658618A (en) * 1949-07-14 1953-11-10 Vogel Walter Separation of solid materials of different specific gravities
US3765532A (en) * 1971-07-12 1973-10-16 Rex Chainbelt Inc Wood chip washer
WO1984004058A1 (fr) * 1983-04-13 1984-10-25 Mineral Deposits Ltd Separateur en spirale

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2658618A (en) * 1949-07-14 1953-11-10 Vogel Walter Separation of solid materials of different specific gravities
US3765532A (en) * 1971-07-12 1973-10-16 Rex Chainbelt Inc Wood chip washer
WO1984004058A1 (fr) * 1983-04-13 1984-10-25 Mineral Deposits Ltd Separateur en spirale

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114180343A (zh) * 2021-10-29 2022-03-15 淮北矿业股份有限公司 一种输灰系统改造方法

Also Published As

Publication number Publication date
EP0445143A1 (fr) 1991-09-11
JPH04501891A (ja) 1992-04-02
FI912523A0 (fi) 1991-05-24
NZ231500A (en) 1991-07-26
AU4522189A (en) 1990-06-26
FI912523A7 (fi) 1991-05-24
SE462566B (sv) 1990-07-16
SE8804261D0 (sv) 1988-11-25
CA2003768A1 (fr) 1990-05-25

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