Nothing Special   »   [go: up one dir, main page]

EP0198825B1 - Pulp washer - Google Patents

Pulp washer Download PDF

Info

Publication number
EP0198825B1
EP0198825B1 EP19840904213 EP84904213A EP0198825B1 EP 0198825 B1 EP0198825 B1 EP 0198825B1 EP 19840904213 EP19840904213 EP 19840904213 EP 84904213 A EP84904213 A EP 84904213A EP 0198825 B1 EP0198825 B1 EP 0198825B1
Authority
EP
European Patent Office
Prior art keywords
web
liquid
end rolls
upper portion
cellulose pulp
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.)
Expired
Application number
EP19840904213
Other languages
German (de)
French (fr)
Other versions
EP0198825A1 (en
Inventor
Lars Eyolf NÄSMAN
Alf Inge LINDSTRÖM
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 AT84904213T priority Critical patent/ATE56230T1/en
Publication of EP0198825A1 publication Critical patent/EP0198825A1/en
Application granted granted Critical
Publication of EP0198825B1 publication Critical patent/EP0198825B1/en
Expired legal-status Critical Current

Links

Images

Classifications

    • 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
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/02Washing ; Displacing cooking or pulp-treating liquors contained in the pulp by fluids, e.g. wash water or other pulp-treating agents
    • D21C9/06Washing ; Displacing cooking or pulp-treating liquors contained in the pulp by fluids, e.g. wash water or other pulp-treating agents in filters ; Washing of concentrated pulp, e.g. pulp mats, on filtering surfaces

Definitions

  • This invention relates to an apparatus for the liquid treatment of cellulose pulp, for example washing and dewatering
  • the invention more precisely, refers to an apparatus where the pulp from a head box is allowed to flow out and form a layer on a plane, endless liquid permeable web.
  • the web runs over two end rolls, and treatment liquid is supplied on the upper surface of the pulp layer at the same time as liquid is sucked away from the lower surface of the pulp layer to vacuum vessels beneath the web.
  • the web usually is a wire manufactured of plastic wires.
  • the wire is driven by one end roll and slides over the perforated covers on the underlying vacuum vessels. Owing to the friction between the wire and vessel covers, great forces are required for driving the wire, This gives rise, at the same time, to high tensile stresses in the wire, which thereby is restricted as to its possible length, because the tensile stress increases with the length of the contact surface between wire and vessel covers.
  • a pulp washer in which washing of the pulp is accomplished with the use of a pair of wire belts between which the pulp layer is provided.
  • a number of tensioning rolls and guide rolls are provided for the wire belts in order to provide the necessary flexibility for the belt to pass about the various rolls.
  • the present invention has the object to eliminate the aforesaid problems and at the same time to render further advantages possible.
  • the plastic wire referred to above is replaced by a perforated steel web.
  • a steel web having a thickness of between 0.5 and 1.5mm and an open area of between 8 and 25% has a substantially higher tensile strength than a wire. It is, further, relatively simple and inexpensive to repair damages in the web. Since a steel web also has a higher resistance to pressure, the dewatering of the pulp layer according to the invention can be carried out much more effectively.
  • a further advantage is that the open area in the covers of the vacuum vessels can be increased due to the inherent carrying capacity of the steel web.
  • Fig. 1 shows a liquid treatment apparatus according to the invention
  • Fig, 2 is a cross-section along II-II in Fig, 1.
  • the embodiment shown of the apparatus comprises an endless perforated steel web 1, which runs about a first and a second end roll 2 and, respectively, 3.
  • the rolls are mounted in a stand 4 so that the first roll 2 is movable by means of a stretching device 5, preferably a hydraulic one, for adjusting the web tension.
  • the driving is effected via the second roll 3, and both rolls preferably are coated with a friction-increasing surface layer.
  • a head box 6 is located for distributing the cellulose pulp in the form of a uniform layer on the web 1
  • a rotor 7 is located for deflocculating the pulp.
  • Beneath the web a plurality of vacuum vessels 8 are arranged one after the other in the longitudinal direction of the web. The vessels are provided with perforated covers acting as a support for the web 1.
  • Outlets 9 and, respectively, 10 are connected to the vessels 8 for the discharge of liquid and, respectively, gas.
  • Above the web means 11 for the supply of treatment liquid are located. Over the pulp layer a pressure difference is maintained for effecting liquid transport crosswise through the pulp layer.
  • the width of the pulp layer on the web is limited by two endless deckle straps 12, which follow along with the web 1. Also other means for limiting the width, of course, can be imagined.
  • a hood 13 is placed over the web 1.
  • a transfer device 14 for the pulp layer after its completed treatment is located, which for example has the form of a doctor blade. Beneath the same a conveying screw 15 is provided for conveying the pulp to subsequent processing steps.
  • Said second roll 3, also co-operates with means for pressing liquid from the pulp layer. According to the embodiment shown, these means are a liquid-permeable web 16, which is held pressed against the steel web 1. The web 16 runs over two small rolls 17,18 and a stretch roll 19.
  • the second end roll 3 is provided with grooves extending all about the roll to permit liquid to be pressed through the steel web 1. The liquid pressed off is collected in a trough 20 beneath the end roll 3. It is, of course, also possible to use other types of pressing means.
  • the pressing-off implies that a high dry content of the pulp can be obtained.
  • the pulp concentration for example, can be increased from about 8% to about 30% by this pressing-off. This implies that a greater part than normal of the chemical content of the pulp can be removed already in connection with the liquid treatment. It is possible from a chemical content of 6 - 10% at a conventional fourdrinier wire washing to come down to 1 - 3%. It is thereby possible, for example, to pass the pulp from the treatment plant directly to the bleach plant without further dewatering in special thickeners.
  • the steel web used preferably shall have a thickness of 0,5 - 1,5 mm.
  • the diameter of the end rolls must be adapted to the thickness of the web, because the bending stress in the web is directly proportional to the web thickness and reciprocally proportional to the roll diameter.
  • a suitable dimension of the rolls can be about 2 m diameter.
  • the hole size must be adapted to the pulp to be treated, but should be in the interval 0,5 - 1,5 mm diameter. It is also imaginable, of course, to form the holes as slits.
  • the open area must under all conditions be between 8 and 25%.
  • the length and width of the web are not critical, but can be adapted at option.
  • the desired width can be brought about by welding a number of narrow webs longitudinally to a wider web, because it is not possible to directly manufacture steel webs having widths here in question, for example about 6 m.
  • Steel webs normally are not manufactured in widths exceeding much more than one meter.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Paper (AREA)

Abstract

The apparatus comprises an endless perforated steel web (1), which runs about two end rolls (2, 3). A head box (6) for the pulp is located at the first roll (2) for distributing a pulp layer on the web. Along the web (1) means (11) are located for supplying treatment liquid to the pulp layer, and vessels (8) for receiving liquid from the lower surface of the pulp layer. In order to additionally increasing the dry content of the pulp, means (16) are provided for pressing-out liquid, which means co-operate with the steel web at its travel about the second roll (3). In connection to said roll (3) also a device (14) for transferring the pulp layer is located.

Description

  • This invention relates to an apparatus for the liquid treatment of cellulose pulp, for example washing and dewatering, The invention, more precisely, refers to an apparatus where the pulp from a head box is allowed to flow out and form a layer on a plane, endless liquid permeable web. The web runs over two end rolls, and treatment liquid is supplied on the upper surface of the pulp layer at the same time as liquid is sucked away from the lower surface of the pulp layer to vacuum vessels beneath the web.
  • In such apparatuses the web usually is a wire manufactured of plastic wires. The wire is driven by one end roll and slides over the perforated covers on the underlying vacuum vessels. Owing to the friction between the wire and vessel covers, great forces are required for driving the wire, This gives rise, at the same time, to high tensile stresses in the wire, which thereby is restricted as to its possible length, because the tensile stress increases with the length of the contact surface between wire and vessel covers. When it is desired in an existing mill to increase the capacity, it is therefore necessary in most cases to increase the wire width instead of the wire length. This would imply substantial re-construction of the mill, If a lengthening of the wire would have been possible, this could have been effected by relatively simple measures and at reasonable costs.
  • Due to the fact, that the wire is manufactured of interplaited plastic wires, a damage in the form of broken wires renders a very troublesome repair work necessary, which in most cases is so expensive that it is more economic to exchange the entire wire.
  • In FI-C-25 895 a pulp washer is disclosed in which washing of the pulp is accomplished with the use of a pair of wire belts between which the pulp layer is provided. A number of tensioning rolls and guide rolls are provided for the wire belts in order to provide the necessary flexibility for the belt to pass about the various rolls.
  • Further, in US-A-3 121 660, CH-A-392 239 and FR-C-14 477 603 are disclosed different kinds of papermaking machines where very thin and flexible metal sheets can be used for a fourdrinier- type wire. This type of thin sheets is necessary since in paper-making applications the fourdrinier wire or band is driven at a very high speed and is bent around a number of separate rolls. However, such a band could not satisfactorily be employed in a pulp washing apparatus.
  • The present invention has the object to eliminate the aforesaid problems and at the same time to render further advantages possible. According to the invention, the plastic wire referred to above is replaced by a perforated steel web. A steel web having a thickness of between 0.5 and 1.5mm and an open area of between 8 and 25% has a substantially higher tensile strength than a wire. It is, further, relatively simple and inexpensive to repair damages in the web. Since a steel web also has a higher resistance to pressure, the dewatering of the pulp layer according to the invention can be carried out much more effectively. A further advantage is that the open area in the covers of the vacuum vessels can be increased due to the inherent carrying capacity of the steel web.
  • The characterizing features of the invention are defined in greater detail in the attached claims.
  • The invention is described in the following, with reference to an embodiment thereof and to the accompanying drawings, in which Fig. 1 shows a liquid treatment apparatus according to the invention, and Fig, 2 is a cross-section along II-II in Fig, 1.
  • The embodiment shown of the apparatus comprises an endless perforated steel web 1, which runs about a first and a second end roll 2 and, respectively, 3. The rolls are mounted in a stand 4 so that the first roll 2 is movable by means of a stretching device 5, preferably a hydraulic one, for adjusting the web tension. The driving is effected via the second roll 3, and both rolls preferably are coated with a friction-increasing surface layer.
  • At the first roll 2 a head box 6 is located for distributing the cellulose pulp in the form of a uniform layer on the web 1, In the head box a rotor 7 is located for deflocculating the pulp. Beneath the web a plurality of vacuum vessels 8 are arranged one after the other in the longitudinal direction of the web. The vessels are provided with perforated covers acting as a support for the web 1.
  • Outlets 9 and, respectively, 10 are connected to the vessels 8 for the discharge of liquid and, respectively, gas. Above the web means 11 for the supply of treatment liquid are located. Over the pulp layer a pressure difference is maintained for effecting liquid transport crosswise through the pulp layer. The width of the pulp layer on the web is limited by two endless deckle straps 12, which follow along with the web 1. Also other means for limiting the width, of course, can be imagined. A hood 13 is placed over the web 1.
  • At the second roll 3 a transfer device 14 for the pulp layer after its completed treatment is located, which for example has the form of a doctor blade. Beneath the same a conveying screw 15 is provided for conveying the pulp to subsequent processing steps. Said second roll 3, also co-operates with means for pressing liquid from the pulp layer. According to the embodiment shown, these means are a liquid-permeable web 16, which is held pressed against the steel web 1. The web 16 runs over two small rolls 17,18 and a stretch roll 19. The second end roll 3 is provided with grooves extending all about the roll to permit liquid to be pressed through the steel web 1. The liquid pressed off is collected in a trough 20 beneath the end roll 3. It is, of course, also possible to use other types of pressing means. The pressing-off implies that a high dry content of the pulp can be obtained. The pulp concentration, for example, can be increased from about 8% to about 30% by this pressing-off. This implies that a greater part than normal of the chemical content of the pulp can be removed already in connection with the liquid treatment. It is possible from a chemical content of 6 - 10% at a conventional fourdrinier wire washing to come down to 1 - 3%. It is thereby possible, for example, to pass the pulp from the treatment plant directly to the bleach plant without further dewatering in special thickeners.
  • The steel web used preferably shall have a thickness of 0,5 - 1,5 mm. The diameter of the end rolls must be adapted to the thickness of the web, because the bending stress in the web is directly proportional to the web thickness and reciprocally proportional to the roll diameter. A suitable dimension of the rolls can be about 2 m diameter.
  • The hole size must be adapted to the pulp to be treated, but should be in the interval 0,5 - 1,5 mm diameter. It is also imaginable, of course, to form the holes as slits. The open area must under all conditions be between 8 and 25%.
  • The length and width of the web are not critical, but can be adapted at option. The desired width can be brought about by welding a number of narrow webs longitudinally to a wider web, because it is not possible to directly manufacture steel webs having widths here in question, for example about 6 m. Steel webs normally are not manufactured in widths exceeding much more than one meter.

Claims (4)

1. An apparatus for liquid treatment of cellulose pulp, comprising a pair of spaced-apart end rolls (2, 3) one of which is a drive roll (3), an endless perforated web (1) arranged about said pair of end rolls (2, 3) so as to provide a substantially horizontally disposed upper portion, said perforated web (1) being adapted to be driven by said end rolls, head box means (6) for supplying cellulose pulp to be treated directly onto said upper portion of said web (1) at the first roll (2), liquid collection means (8) arranged between said pair of end rolls (2, 3) for collecting liquid displaced from said cellulose pulp through said web (1) as said web is driven by said drive roll (3) relative to said liquid collection means, said liquid collection means (8) having a substantially horizontally disposed surface arranged beneath and in direct contact with said upper portion of said web (1), liquid inlet means (11) arranged above said upper portion of said web (1) for supplying a treatment liquid to said cellulose pulp supplied onto said upper portion of said web (1), means for applying a pressure differential across said upper portion of said web to force liquid from said cellulose pulp through said web into said liquid collection means (8) as said web is moved relative to said liquid collection means and removal means (14) for removing treated cellulose pulp from said web (1) after said cellulose pulp has been subjected to said liquid treatment,
characterized in that said web (1) is made of steel having a thickness of between 0.5 and 1.5 mm and being perforated so as to have an open area of between 8% and 25% and that means (16) for pressing-out liquid are arranged so as to cooperate with the steel web (1) at its travel about the second roll (3).
2. The liquid treatment apparatus of Claim 1 wherein said endless steel web (1) is supported by said pair of spaced-apart end rolls (2, 3) and said liquid collection means (8) arranged therebetween; wherein said endless steel web (1) includes a lower portion extending between said end rolls; and wherein said liquid treatment apparatus further includes means (5) for adjusting the spacing between said end rolls to adjust the tension on said endless steel web (1) and maintain said lower portion of said endless steel web substantially horizontally disposed.
3. The liquid treatment apparatus of Claim 2 wherein the length of said horizontally disposed surface of said liquid collection means (8) substantially corresponds to the spacing between said end rolls (2, 3).
4. The apparatus of Claim 2 wherein said liquid collection means (8) comprises a plurality of vessels (8) arranged between said pair of end rolls (2, 3), said vessels (8) each being arranged transversely of the longitudinal direction of movement of said endless web (1) and said vessels (8) collectively extending one after the other in said longitudinal direction of movement of said web, each of said vessels being provided with perforated covers in contact said upper portion of said web (1).
EP19840904213 1983-12-02 1984-11-12 Pulp washer Expired EP0198825B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT84904213T ATE56230T1 (en) 1983-12-02 1984-11-12 WASHING PLANT FOR PULP.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8306658A SE452344B (en) 1983-12-02 1983-12-02 DEVICE FOR CELLULOSAMASSA WASHING
SE8306658 1983-12-02

Publications (2)

Publication Number Publication Date
EP0198825A1 EP0198825A1 (en) 1986-10-29
EP0198825B1 true EP0198825B1 (en) 1990-09-05

Family

ID=20353557

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19840904213 Expired EP0198825B1 (en) 1983-12-02 1984-11-12 Pulp washer

Country Status (9)

Country Link
EP (1) EP0198825B1 (en)
JP (1) JPS61500558A (en)
AU (1) AU575883B2 (en)
CA (1) CA1265691A (en)
DE (1) DE3483161D1 (en)
FI (1) FI76848C (en)
NZ (1) NZ210131A (en)
SE (1) SE452344B (en)
WO (1) WO1985002424A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE444826B (en) * 1984-09-17 1986-05-12 Sunds Defibrator DEVICE FOR LIQUID TREATMENT OF MASS
SE448890B (en) * 1986-05-13 1987-03-23 Sunds Defibrator DEVICE FOR THE SUPPLY OF LIQUID IN TREATMENT OF PASS ON AN ENDLESS, CURRENT RANGE
AT394737B (en) * 1989-07-03 1992-06-10 Andritz Ag Maschf METHOD AND DEVICE FOR THE TREATMENT, IN PARTICULAR LAUNDRY, OF FIBER FUEL-LIQUID MIXTURES

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH392239A (en) * 1960-07-23 1965-05-15 Heimbach Gmbh Thomas Josef Filter web for sheet formation and for fabric drainage and drying in paper machines or the like
US3121660A (en) * 1961-02-13 1964-02-18 Jr Edward H Hall Fourdrinier wire and method of making the same
FR1477603A (en) * 1966-03-03 1967-04-21 Endless belt for different machines in a plant for making paper, cardboard or other sheet products from pulp
AU502276B2 (en) * 1976-04-22 1979-07-19 Rederiaktiebolag Et Nordstjernan Dewatering press

Also Published As

Publication number Publication date
SE8306658D0 (en) 1983-12-02
WO1985002424A1 (en) 1985-06-06
SE8306658L (en) 1985-06-03
CA1265691A (en) 1990-02-13
FI76848C (en) 1988-12-12
FI76848B (en) 1988-08-31
FI854787A0 (en) 1985-12-03
EP0198825A1 (en) 1986-10-29
SE452344B (en) 1987-11-23
JPS61500558A (en) 1986-03-27
DE3483161D1 (en) 1990-10-11
NZ210131A (en) 1986-07-11
AU575883B2 (en) 1988-08-11
FI854787A (en) 1985-12-03
AU3611684A (en) 1985-06-13

Similar Documents

Publication Publication Date Title
US3726758A (en) Twin-wire web forming system with dewatering by centrifugal forces
US4557802A (en) Apparatus for affecting a web drained on a wire
CA2019712C (en) Method and device for treatment of a fibrous material-fluid mixture
US5314585A (en) Low shear Uhle box
US3150037A (en) Papermaking machine utilizing centrifugal dewatering
EP0198825B1 (en) Pulp washer
KR880001124B1 (en) Top wire former
US3824152A (en) Twin wire paper forming with one wire wrapping a suction cylinder
EP0178271B1 (en) Apparatus for liquid treatment of pulp
US3236724A (en) Apparatus for making formed fibrous webs
DE69612499T2 (en) PAPER MACHINE FOR PRODUCING A SOFT CREPE PAPER TAPE
US5868903A (en) Device for dewatering and/or washing suspensions, in particular suspensions of fibrous materials
US5338408A (en) Paper forming unit with two dandy rolls
SU929773A1 (en) Press for dewatering fibrous material web
CA2113847A1 (en) Method and apparatus for detaching a traveling web from two wire belts
DE102004050593A1 (en) Press arrangement
CA2022779A1 (en) Dewatering device
JPS61258091A (en) Apparatus for concentrating aqueous suspension of papermaking pulp
SE8406466L (en) PROCEDURE AND DEVICE FOR CONTINUOUS TREATMENT OF FIBER MASS WITH TREATMENT LIQUID
CA2158728A1 (en) Traction-free web transport in a compression section
US6558557B1 (en) Process and a decker for bringing together two suspension layers
CA1275593C (en) Arrangement for liquid treatment of pulp
JPH0146239B2 (en)
CA1312488C (en) Dispersion roll for fourdrinier machine
CA1132838A (en) Method and apparatus for removing liquid from a moving web

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

17P Request for examination filed

Effective date: 19851111

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT DE FR GB SE

TCAT At: translation of patent claims filed
DET De: translation of patent claims
17Q First examination report despatched

Effective date: 19880704

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: SUNDS DEFIBRATOR INDUSTRIES AKTIENBOLAG

RAP3 Party data changed (applicant data changed or rights of an application transferred)

Owner name: SUNDS DEFIBRATOR INDUSTRIES AKTIEBOLAG

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT DE FR GB SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19900905

REF Corresponds to:

Ref document number: 56230

Country of ref document: AT

Date of ref document: 19900915

Kind code of ref document: T

ET Fr: translation filed
REF Corresponds to:

Ref document number: 3483161

Country of ref document: DE

Date of ref document: 19901011

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19901112

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

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

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

GBPC Gb: european patent ceased through non-payment of renewal fee
26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19941109

Year of fee payment: 11

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19941110

Year of fee payment: 11

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 19941111

Year of fee payment: 11

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Effective date: 19951112

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Effective date: 19960731

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19960801

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST