EP0198825B1 - Pulp washer - Google Patents
Pulp washer Download PDFInfo
- 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
Links
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 18
- 239000010959 steel Substances 0.000 claims abstract description 18
- 239000001913 cellulose Substances 0.000 claims description 9
- 229920002678 cellulose Polymers 0.000 claims description 9
- 239000010410 layer Substances 0.000 description 11
- 238000005406 washing Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-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
- D21C9/02—Washing ; Displacing cooking or pulp-treating liquors contained in the pulp by fluids, e.g. wash water or other pulp-treating agents
- D21C9/06—Washing ; 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
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. Ahood 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. Theweb 16 runs over twosmall rolls 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 atrough 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)
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).
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)
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)
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 |
-
1983
- 1983-12-02 SE SE8306658A patent/SE452344B/en unknown
-
1984
- 1984-11-07 NZ NZ21013184A patent/NZ210131A/en unknown
- 1984-11-12 JP JP50416684A patent/JPS61500558A/en active Pending
- 1984-11-12 WO PCT/SE1984/000383 patent/WO1985002424A1/en active IP Right Grant
- 1984-11-12 EP EP19840904213 patent/EP0198825B1/en not_active Expired
- 1984-11-12 DE DE8484904213T patent/DE3483161D1/en not_active Expired - Fee Related
- 1984-11-12 AU AU36116/84A patent/AU575883B2/en not_active Ceased
- 1984-11-30 CA CA000469004A patent/CA1265691A/en not_active Expired - Fee Related
-
1985
- 1985-12-03 FI FI854787A patent/FI76848C/en not_active IP Right Cessation
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 |
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