NZ231915A - Thickening pulp slurry using filter drum - Google Patents

Thickening pulp slurry using filter drum

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Publication number
NZ231915A
NZ231915A NZ23191589A NZ23191589A NZ231915A NZ 231915 A NZ231915 A NZ 231915A NZ 23191589 A NZ23191589 A NZ 23191589A NZ 23191589 A NZ23191589 A NZ 23191589A NZ 231915 A NZ231915 A NZ 231915A
Authority
NZ
New Zealand
Prior art keywords
drum
filter
slurry
plate
face
Prior art date
Application number
NZ23191589A
Inventor
Aaro Ahlgren
Original Assignee
Sunds Defibrator Rauma 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 Rauma Oy filed Critical Sunds Defibrator Rauma Oy
Priority to NZ23191589A priority Critical patent/NZ231915A/en
Publication of NZ231915A publication Critical patent/NZ231915A/en

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Description

-Dir-'-*- t* , u-or, F 3S»; &2.lk5./QU 2 3 DEC 1991 •' 'i. 'i® } > 1 * ^ » r » « • I • « <r j . ,0, jo.;.: j-, AMr.-.D-D under Section , ^ *.f th ■ik.„ iiiLP*1 -TrNTS I 2 IDfr; S. ' Patents Form No. 5 PATENTS ACT 1953 COMPLETE SPECIFICATION "METHOD FOR THICKENING OF SLURRY AND FOR ITS TREATMENT WITH LIQUID AS WELL AS A DRUM FILTER" WE, SUNDS DEFIBRATOR RAUMA OY, a Finnish Corporation of PL 34, 28101 Pori, FINLAND, hereby declare this invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement: 1 (followed by la) 23 1 f\ The present invention concerns a method for thickening of slurry and for its treatment with liquid, whereat the slurry to be thickened is passed onto the filter face of a drum revolving in a basin and the treatment liquid is passed through the pulp web formed on the drum and whereat the consistency of the pulp web is increased by pressing a compression plate against the pulp web. The invention also concerns a drum filter for thickening of slurry and for its treatment with liquid, which said filter comprises a basin, a filter drum revolving in the basin, a box fitted above the drum, means for producing a positive pressure in the space formed by the basin and by the box, means for feeding slurry onto the outer face of the drum, means for passing the treatment liquid onto the pulp web placed on the drum, means for detaching the thickened pulp web from the drum, as well as means for removing the filtrate from inside the drum, whereat the filter is provided with a flexible plate placed after the pulp-feed point at a distance from the outer face of the drum.
For the thickening and washing of fibrous slurries, in particular of cellulosic fibrous slurry or pulp slurry, filters are used in which the fibrous slurry is thickened on a revolving drum. The fibrous slurry is passed into the feed box of the filter as diluted to an appropriate consistency. The fibrous slurry is thickened by filtration by means of a difference in pressure onto the face of the filter drum, which said face, as the drum revolves, carries the thickened slurry further. Washing water is passed onto the pulp web placed on the drum face, said water passing through the pulp web into the drum while displacing chemicals contained in the pulp.
When attempts are made to increase the capacity of a washing drum by increasing the speed of rotation and the consistency of the pulp web, a problem that is encountered is how to provide a uniform pulp web. If the pulp web becomes uneven, the washing result cannot be made good.
In the US Patent 4,085,003 a washing drum is described wherein a compression plate to be pressed against the pulp web is employed. By means of the plate, the consistency of the pulp is increased and the uniformity of the pulp web is improved. The plate is provided with rigidifying ribs, and it is pressed against the pulp web by means of actuator members provided at the outer end of the plate. It is problem of this prior-art device that occasionally the washing liquid starts flowing to below the compression plate. This comes from the fact that the compression plate is rigid and is not always placed tightly against the pulp web, especially if the pulp web is uneven.
The object of the present invention is to provide a drum filter wherein the operation of the compression plate is arranged in a simpler and more efficient way as compared with prior art. The method in accordance with the invention is characterized in that the compression force of the compression plate is produced by means of a pressure effective at the convex side of the plate. The drum filter in accordance with the invention is characterized in that the flexible plate can be pressed towards the drum by means of a pressure effective at the convex side of the plate.
By means of a drum filter in accordance with the invention, the consistency of the pulp web can be increased highly efficiently right before the washing, at the same time as a uniform pulp web is provided. This is important in order that a good washing result could be obtained. When the compression force of the plate is produced by means of pressure, no particular actuator member is required. Since a resilient compression plate is also pressed well against an uneven pulp web, the washing liquid has not access to below the plate at the trailing edge of the compression plate.
The invention and its details will be described in more detail in the following with reference to the accompanying drawings, wherein Figure 1 is a cross-sectional 3 view of one embodiment of the drum filter in accordance with the invention, and Figure 2 of another embodiment.
The drum filter comprises a basin 1 and, above the basin, a hood 2, which together form a closed space. Into 5 the basin, a revolving drum 3 is fitted, which is provided with a filtering wire face. The filter is provided with a blower 4 so as to maintain a positive pressure in the space defined by the basin and the hood and placed outside the drum. The direction of rotation of the drum is 10 clockwise in the drawing.
In the lower part of the filter, there is a feed box 5 for feeding the pulp onto the drum face. By the effect of the difference in pressure, the filtrate water runs out of the web into the interior of the drum. The drum-side 15 wall of the feed box is sealed by means of a lip seal 6 against the moving face of the drum. The other wall 7 of the feed box follows the shape of the drum at a distance, whereby a pulp-web formation zone 8 remains between the drum and the wall 7.
The washing water of the first washing stage is passed into the space 9 above the feed box, from where it is pressed through the pulp web and the drum into the drum. At the upper edge of the drum-side wall of the washing-water space 9,,as an extension of the wall 7, a flexible, 25 resilient plate 10 is attached over the entire length of the drum. The upper edge of the plate 10 can move freely towards the drum, and the pressure of the washing water effective at the convex side of the plate presses the plate against the pulp web.
The washing water of the second washing zone is passed onto the drum face out of the jet pipes 11.
Between the flexible plate 10 and the drum, after the pulp-web formation zone 8, a thickening zone 12 is formed, wherein the plate compresses the pulp and removes liquid 35 out of the pulp. The plate is not provided with any rigidifying members, but it is placed freely against the pulp web depending on the pressure effective at the other side of the plate. 4 The pulp web 13 continues its run further on the drum face through the second washing zone, and by the effect of the pressure outside the drum water is separated from the pulp web into the drum. At the point 14 the pulp web 5 is detached from the drum face in a way in itself known.
The filtrate water is removed out of the drum.
In the figure, the level of the washing water is denoted with the reference numeral 15, and the level of the filtrate water with the reference numeral 16. 10 Besides by means of the hydrostatic pressure of the washing water, the compression force of the compression plates can also be affected by means of the air pressure effective inside the hood. By adjusting the air pressure, it is also possible to adjust the compression force. 15 It is also possible to run the washing stages so that no water from the first stage enters into the space 9, but all the washing water is introduced into the second washing stage out of the jet pipes 11. In such a case, it is only the pressure in the gas space in the hood that 20 acts upon the flexible plate 10.
The material of the plate 10 is most appropriately a synthetic material. It is important that the friction between the plate and the pulp web should be as low as possible in order that the pulp web should follow the 25 moving face of the drum, whose friction is higher than the friction of the plate.
In tests that have been carried out, it has been possible to increase the consistency of the pulp by means of the compression plate from a consistency of 5 to 8 % 30 at the initial end of the plate to a consistency of 13 to 16 % at the final end of the plate, in other words, one half of the water present in the pulp was removed within the thickening zone.
Fig. 2 shows an embodiment of the invention provided 35 with two separate thickening zones 12 and 12' and with two flexible plates 10 and 10'. The washing "water of the second washing zone is passed into the second washing-water space 9' placed above the first washing-water space 9. 2319 15 The invention is not confined to the embodiments described above alone, but it may show variation in different ways within the scope of the patent claims. The invention can also be applied in single-stage washing, and 5 so also in washing comprising a higher number of washings. Besides to the washing of pulp, it can also be applied to treatment of pulp with other liquids. If necessary, it is possible to fit liquid-collecting basins inside the drum in a way in itself known, in which case the filtrates 10 from the different washing stages can be collected separately and, if necessary, be passed, e.g., to the preceding washing stage.
It is possible to construct a similar compression plate also for a suction washer, in which case the hood 15 is not pressurized but, on the contrary, there is negative pressure inside the drum.
NUvv A/itNDED

Claims (8)

WHAT WE CLAIM IS;- 1. A method for thickening of slurry and for its treatment with liquid, wherein the slurry to be thickened is passed onto a filter face of a drum revolving in a basin and the treatment liquid is passed through a pulp web formed on the, drum and wherein the consistency of the pulp web is increased by pressing a flexible compression plate against the pulp web by means of a pressure acting upon the face of the plate facing away from the drum, characterised in that it is the hydrostatic pressure of the treatment liquid and/or the overpressure of the gas within the space surrounding the drum which act upon the face of the compression plate facing away from the drum. 2. A method as claimed in claim 1, characterised in that the compression force of the compression plate is adjusted by adjusting the gas pressure prevailing in the space surrounding the drum. 3. A drum filter for thickening of slurry and for its treatment with liquid, which said filter comprises a basin, a filter drum revolving in the basin, means for producing a difference in pressure between the space outside the drum and the space inside the drum, means for feeding slurry onto the outer face of the drum, means for passing the treatment liquid onto a pulp web placed on the drum, means for detaching the thickened pulp web from the drum, as well as means for removing the filtrate from inside the drum, wherein the filter / is provided with a flexible compression plate placed after a AS AMENDED 231915 WHAT WE CLAIM IS:-
1. A method for thickening of slurry and for its treatment with liquid, wherein the slurry to be thickened is passed onto a filter face of a drum revolving in a basin and the treatment liquid is passed through a pulp web formed on the drum and wherein the consistency of the pulp web is increased by pressing a flexible compression plate against the pulp web by means of a pressure acting upon the face of the plate facing away from the drum, characterised in that it is solely the hydrostatic pressure of the treatment liquid and the overpressure of the gas within the space surrounding the drum which act upon the face of the compression plate facing away from the drum.
2. A method as claimed in claim 1, characterised in that the compression force of the compression plate is adjusted by adjusting the gas pressure prevailing in the space surrounding the drum.
3. A drum filter for thickening of slurry and for its treatment with liquid, which said filter comprises a basin, a filter drum revolving in the basin, means for producing a difference in pressure between the space outside the drum and the space inside the drum, means for feeding slurry onto the outer face of the drum, means for passing the treatment liquid onto a pulp web placed on the drum, means for detaching the thickened pulp web from the drum, as well as means for removing the filtrate from inside the drum, wherein the filter is provided with a flexible compression plate placed after a 231^15 NOW AMENDED pulp-feed point at a distance from the outer face of the drum, which flexible plate can be pressed toward the drum by means of a pressure effective at the side of the plate that is facing away from the drum, characterised in that the compression plate is located so that the hydrostatic pressure of the treatment liquid and/or the overpressure of the gas within the space surrounding the drum acts upon the face of the plate facing away from the drum. 4. A drum filter as claimed in claim 3, characterised in that the flexible plate at the same time forms a wall for the treatment liquid space. 5. The drum filter as claimed in claim 3, wherein several flexible plates have been fitted on the circumference of the drum one after the other. 6. The drum filter as claimed in claim 4, wherein several flexible plates have been fitted on the circumference of the drum one after the other. 7. A method for thickening of slurry as claimed in claim 1 and substantially as hereinbefore described with reference to Figure 1 or Figure 2 of the accompanying drawings. 8. A drum filter for thickening a slurry, substantially as hereinbefore described with reference to and as shown in the figure 1 or figure 2 of the accompanying drawings. SUNDS DEFIBRATOR RAUMA OY by their authorised agents P.L. BERRY & ASSOCIATES 1 AS AMENDED 231915 pulp-feed point at a distance from the outer face of the drum, which flexible plate can be pressed toward the drum by means of a pressure effective at the side of the plate that is facing away from the drum, characterised in that it is solely the hydrostatic pressure of the treatment liquid and the overpressure of the gas within the space surrounding the drum which act upon the face of the plate facing away from the drum.
4. A drum filter as claimed in claim 3, characterised in that the flexible plate at the same time forms a wall for the treatment liquid space.
5. The drum filter as claimed in claim 3, wherein several flexible plates have been fitted on the circumference of the drum one after the other.
6. The drum filter as claimed in claim 4, wherein several flexible plates have been fitted on the circumference of the drum one after the other.
7. A method for thickening of slurry as claimed in claim 1 and substantially as hereinbefore described with reference to Figure 1 or Figure 2 of the accompanying drawings.
8. A drum filter for thickening a slurry, substantially as hereinbefore described with reference to and as shown in the figure 1 or figure 2 of the accompanying drawings. SUNDS DEFIBRATOR RAUMA OY. by their authorised agents, P.L. BERRY & ASSOCIATES. 7 /
NZ23191589A 1989-12-21 1989-12-21 Thickening pulp slurry using filter drum NZ231915A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
NZ23191589A NZ231915A (en) 1989-12-21 1989-12-21 Thickening pulp slurry using filter drum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NZ23191589A NZ231915A (en) 1989-12-21 1989-12-21 Thickening pulp slurry using filter drum

Publications (1)

Publication Number Publication Date
NZ231915A true NZ231915A (en) 1991-12-23

Family

ID=19923088

Family Applications (1)

Application Number Title Priority Date Filing Date
NZ23191589A NZ231915A (en) 1989-12-21 1989-12-21 Thickening pulp slurry using filter drum

Country Status (1)

Country Link
NZ (1) NZ231915A (en)

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