WO2022233658A1 - Ventilvorrichtung für einen scheibenfilter - Google Patents
Ventilvorrichtung für einen scheibenfilter Download PDFInfo
- Publication number
- WO2022233658A1 WO2022233658A1 PCT/EP2022/061145 EP2022061145W WO2022233658A1 WO 2022233658 A1 WO2022233658 A1 WO 2022233658A1 EP 2022061145 W EP2022061145 W EP 2022061145W WO 2022233658 A1 WO2022233658 A1 WO 2022233658A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- filtrate
- reservoir
- bridge
- valve device
- zone
- Prior art date
Links
- 239000000706 filtrate Substances 0.000 claims abstract description 159
- 238000000034 method Methods 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 27
- 239000000725 suspension Substances 0.000 claims description 20
- 230000007704 transition Effects 0.000 claims description 4
- 230000000149 penetrating effect Effects 0.000 claims description 3
- 238000012216 screening Methods 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims 1
- 230000000903 blocking effect Effects 0.000 abstract description 2
- 239000000835 fiber Substances 0.000 description 19
- 230000000694 effects Effects 0.000 description 10
- 238000004904 shortening Methods 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000010276 construction Methods 0.000 description 2
- 239000012065 filter cake Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000006735 deficit Effects 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/15—Filters with filtering elements which move during the filtering operation with rotary plane filtering surfaces
- B01D33/21—Filters with filtering elements which move during the filtering operation with rotary plane filtering surfaces with hollow filtering discs transversely mounted on a hollow rotary shaft
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/70—Filters with filtering elements which move during the filtering operation having feed or discharge devices
- B01D33/74—Filters with filtering elements which move during the filtering operation having feed or discharge devices for discharging filtrate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/80—Accessories
- B01D33/82—Means for pressure distribution
Definitions
- Valve device for a disc filter The invention relates to a valve device for a disc filter.
- Disc filters are used for separating liquids from a suspension, in particular a fibrous suspension, with a container for receiving the suspension, a rotatably mounted floating shaft extending horizontally in the container and several filter disks fastened to the floating shaft and spaced apart axially.
- the filter discs consist of several separate filter disc sectors in the shape of a sector of a circle.
- the flea wave has a number of separate channels, the channels being connected to different filter disk sectors and some of the channels being connected to a vacuum source.
- the channels rotating with the Flohlwelle open into a valve housing at least at one end of the shaft.
- the valve housing there is at least one non-rotating vacuum valve, which on the one hand is connected to a vacuum source and on the other hand covers at least one channel opening which changes during the rotation of the Flohlwelle.
- Disc filters of this type as described in DE102010039512 and US Pat. No. 3,452,874, are used for thickening the suspension and in the paper industry, in particular for pulp recovery.
- the flea shaft is usually connected to a vacuum source by means of a valve device.
- a fleece layer forms on the filter discs as a result of the pressure difference between the fibrous suspension and the interior of the filter discs. Depending on the immersion position, filtrate of different qualities reaches the interior of the filter discs and thus the flea shaft.
- the valve device is provided for the separate discharge of different filtrate qualities.
- the valve device switches between discharge of the filtrate at atmospheric pressure and at negative pressure, also referred to as vacuum. So that no false air can penetrate into the negative pressure zone known as the vacuum zone, the channel/channels of the Flohlwelle assigned to a sector are covered by a cover known as a filtrate bridge for entry into and exit from the vacuum zone completely dimmed.
- the filtrate outflow is interrupted by the filtrate bridge when switching from atmosphere to vacuum and also from vacuum to atmosphere. It is known from WO 99/25456 and EP 400 787 to provide an adjustable filtrate bridge through which the sectors of atmosphere and vacuum can be adjusted. As a result, an optimization of the discharge of different filtrate qualities can be adapted to different pulp properties or operating situations
- DE22 03 657 A1 discloses a control head for rotary vacuum filters for a flea wave.
- the flea wave is connected to filter sectors and the filter sectors communicate with channels running in the flea wave.
- a control plate is provided at the end of the Flohlwelle, via which the channels in the Flohlwelle are charged with compressed air or vacuum.
- the filter sectors are pressurized accordingly via the channels, so that formation of a layer of sludge by the applied vacuum or the rejection of the filter cake from the filter segment is possible.
- the thickness of the filter cake that forms can be controlled by regulating the applied pressure.
- Another valve for a disc filter is known from GB736815.
- Today's disc filter valve assembly has an atmospheric zone and a negative pressure zone, also referred to as the vacuum zone.
- a vacuum valve for providing a vacuum zone is arranged in the valve device.
- the valve housing has an opening for an inflow of filtrate from channels of a flea shaft of the disc filter. So that no false air can get into the negative pressure zone, filtrate bridges are provided to block off the channels for a transfer into or out of the negative pressure zone.
- the filtrate flow is stopped when a channel or the channels assigned to a filter disc sector are completely blocked off. This can cause a backwater and also a Backflow of filtrate into the channel(s) and back into the filter disc sectors may occur.
- This back pressure can have a negative effect on the layer of fiber material already formed on the respective filter disc sector. Partial detachment of this layer may occur.
- the decelerated filtrate flow must be accelerated again, which has a negative effect on the efficiency of the disc filter.
- At least one of the filtrate bridges is designed with an undercover. This means that an assigned channel of the disc filter is not completely blocked off by this filtrate bridge. This ensures that the filtrate flow is never completely interrupted when passing through this filtrate bridge, which is designed with an undercover. A backlog of the filtrate produced is at least reduced. As a result, the use of this valve device contributes to optimizing the performance of a disc filter.
- the filtrate bridge formed with an undercover is provided with a reservoir.
- the reservoir is intended for liquid.
- the filtrate bridge alone is no longer provided for complete blocking of the channels/the channel when changing from the atmospheric zone to the negative pressure zone and vice versa.
- the reservoir can provide liquid dimming instead of full dimming.
- the negative pressure in the negative pressure zone can be maintained by the flow resistance of the liquid flowing from the reservoir. Due to the fact that there is no complete dimming due to the shortened bridge, the filtrate flow is reduced but not completely stopped. The pressure in the negative pressure zone causes the filtrate to flow prematurely accelerated. An inflow of gaseous volumes is prevented by the reservoir independently of the filtrate flow from the channels. As a result, the time of an effective negative pressure can be extended, which has an advantageous effect on the formation of the fiber layer. In addition, a better fit of the fiber layer on the filter disk sector allows a gentler activation of the
- the fibrous layer itself acts as a
- the premature modulation can have an advantageous effect on the formation of the fiber layer, in particular the formation of a denser fiber layer.
- the liquid provided by the reservoir can ensure that liquid flows onto the undercover area. This prevents the volume of gas from getting directly into the negative pressure zone via the undercover area.
- the reservoir can be filled with liquid through a supply line or, according to a preferred embodiment, directly with filtrate.
- the reservoir comprises an inlet opening for filling with filtrate.
- the reservoir is thus automatically filled with the filtrate produced during operation.
- a separate liquid supply for filling the reservoir is therefore not required, which has an advantageous effect on the design effort. If, in particular, filling with cloudy filtrate is provided, it can be ensured that the reservoir is always sufficiently filled. Also during commissioning, turbid filtrate accumulates directly during commissioning when a filter disc sector is immersed in the suspension. As a result, automatic filling of the reservoir can also be guaranteed when it is put into operation.
- the reservoir has an inlet opening for filling with clear filtrate, preferably with super clear filtrate, having.
- This filling can preferably be provided in addition to an inflow and filling of the reservoir with cloudy filtrate. Deterioration of the filtrate discharged in the vacuum zone through the use of the reservoir is avoided by preferred filling with clear filtrate.
- the preferred supply of clear filtrate, in particular super clear filtrate can be realized, for example, by means of a valve or a line guide or filtrate guide in the valve device.
- the super clear filtrate usually flows into the valve device with a higher flow pressure, so that such a preferred filling can be implemented with little technical effort
- the reservoir is filled by filtrate supplied from the channels of the valve device outside the negative pressure zone of the valve device.
- the reservoir can be filled by guiding the filtrate inlets in the atmosphere zone.
- a pump or valve for ensuring the filling of the reservoir is not required. Thus, the required design effort is low.
- the reservoir is provided on the filtrate bridge provided on the inlet side to the vacuum zone.
- the filtrate bridge provided on the inlet side to the vacuum zone can be shortened. This shortens the dimming time for entry into the negative pressure zone. This allows the filtrate to drain off more quickly. This also has the consequence that the intake of the filtrate discharge requires less re-acceleration and there is only a reduced backwater of filtrate.
- the volume of filtrate is large, especially when entering the negative pressure zone. It is therefore particularly important to avoid a backwater of filtrate when it enters the vacuum zone.
- the filtrate flow is significantly lower when leaving the vacuum zone, since a dense layer of fibers has already formed on the filter disc sector. An interruption by a filtrate bridge thus briefly stops the significantly lower filtrate flow. The resulting effects, such as a backwater, are clear lower. Strictly speaking, the panes are no longer immersed when the vacuum is switched off. So only the residual filtrate present in the sectors and the channels is discharged. The fiber layer does not completely seal against the atmosphere, but represents a flow resistance. It is this leakage air that makes it possible for the system to be emptied. The amount of leakage air varies depending on the fiber. However, the filtrate flowing off ensures that no air can penetrate into the negative pressure zone. The system drains to varying degrees in the drying area with at least partially emerged panes
- the reservoir is preferably firmly connected to this filtrate bridge. It is then ensured that the area of the shortened filtrate bridge is consistently well covered by the liquid in the reservoir. If the filtrate bridge is adjustable in the circumferential direction, the reservoir moves at the same time when the filtrate bridge is adjusted.
- An alternative solution is to position the reservoir in a stationary manner.
- the reservoir is preferably mounted on the housing of the vacuum valve, preferably even firmly connected to this housing.
- the reservoir is not automatically moved with an adjustable filtrate bridge, but the entire adjustment range of the filtrate bridge can be covered by a corresponding design of the reservoir.
- the reservoir is thus stored in a fixed position and a change in the filtrate bridge, apart from a shortened design, is not necessary. The design effort is therefore particularly low.
- the extent of the at least one filtrate bridge provided with a reservoir is shorter in the circumferential direction than the extent of the channel(s) connected to a filter disc sector. It has been found that as little as 2° under-coverage results in a noticeable improvement in maintaining filtrate flow. Undercoverage is the minimum area that is not covered by the filtrate bridge when stopped down. So they catch one Channels assigned to the filter disk sector exceed 20° and the filtrate bridge extends over a circumferential sector of 18°, so the undercoverage is 2°. It is assumed here that the filtrate bridge completely covers the channels in the radial direction.
- the reservoir has a fleas extending in the circumferential direction and these fleas in
- Circumferential direction together with the extension of the filtrate bridge connected to the reservoir is at least as large as the extension of the channels connected to a filter disc sector in the circumferential direction.
- the reservoir has an opening on the side facing the channels. The liquid in the reservoir is present through this opening. This liquid is sucked into the negative pressure zone by the acting pressure of the negative pressure zone. This prevents gaseous volumes from penetrating.
- the reservoir is arranged in relation to the boundary edges of the filtrate bridge.
- Each filtrate bridge has in
- a boundary edge in the direction of the low-pressure zone and a boundary edge in the atmospheric zone It has been found to be preferable to provide the reservoir on the boundary edge of the filtrate bridge facing away from the negative pressure zone.
- the reservoir connects with its opening to this boundary edge in the circumferential direction.
- the area of the shortened filtrate bridge is covered by the opening of the reservoir.
- the reservoir itself can extend beyond the radial extent of the filtrate bridge.
- a continuous application of liquid can be ensured by an inlet in the direction of the opening. This prevents gaseous volumes from penetrating into the vacuum zone. Due to the possibility of also being able to arrange volumes offset to the side of the filtrate bridge, the available installation space can be used flexibly.
- the inlet opening of the reservoir for filling the reservoir can thus be spatially adapted to the filtrate flow patterns to be expected within the valve device.
- the reservoir has a maximum capacity of 100 liters. This capacity ensures that emptying does not occur.
- a reservoir with this capacity can be spatially well arranged without disturbing the outflow of filtrate.
- a reservoir with a capacity of 100 liters, preferably 50 liters and particularly preferably at least 30 liters has proven to be advantageous. It has proven advantageous to provide a reservoir with a volume of at least 10 liters. If the filtrate flowing out of the channels is large, then correspondingly less liquid is sucked in from the reservoir and the volume of the reservoir can be designed to be correspondingly smaller, which has an advantageous effect on the required installation space. It can be particularly advantageous to provide the opening of the reservoir following the boundary edge facing the negative pressure zone.
- Disc filters are used to separate liquids from a suspension.
- the disc filter has a trough for receiving a suspension and a hollow shaft which extends horizontally in the container and is rotatably mounted. Filter disks which are spaced apart axially are fastened to the hollow shaft.
- the filter discs consist of several separate filter disc sectors in the shape of a sector of a circle.
- the hollow shaft has several separate channels and the channels communicate with different filter disc sectors. At least part of the channels is connected to a vacuum source. The channels rotate with the hollow shaft and open at least one shaft end into a valve housing of a valve device according to an embodiment described above.
- the interruption of the filtrate flow for a transition into or out of a vacuum zone is shortened.
- dimming takes place only partially through a filtrate bridge.
- a flow of gas into the negative pressure zone is prevented by flooding the undercover area with liquid.
- Flooding of the undercover area can preferably be ensured by a reservoir that can be filled with liquid.
- FIG. 1 Schematic representation of a hollow shaft with valve device
- FIG. 2 Schematic representation of a disk filter
- FIG. 3 Schematic representation of the valving of the disc filter and the filtrate flows
- Fig. 4 Enlarged section of a filtrate bridge with reservoir
- the slide filter 1 has filter disks 9 .
- the filter discs 9 are mounted on a central, horizontal Flohlwelle 13 with conical channels 15.
- a valve device 20, also referred to as a filtrate valve, is located on an outlet side of the Flohlwelle 13.
- the filtrate valve 20 can have webs for separating different filter zones or filtrate qualities.
- a barometric downpipe for generating a negative pressure for a negative pressure zone is connected to the outside of the filtrate valve 20 .
- the filtrate valve 20 has an atmosphere zone and a vacuum zone of a vacuum valve 23 .
- the vacuum valve 23 is separated from the atmosphere zone by a housing 25 of the vacuum valve.
- Filtrate bridges 31, 32 are provided for a transition from the atmospheric zone to the negative pressure zone and vice versa.
- a suspension 7 is conveyed into a suspension feed 5 .
- the suspension is fed to a trough 3 of the disc filter 1 in a uniformly distributed manner.
- the flea shaft 13 with the filter discs 9 is installed in the trough 3.
- the filter discs are covered by a fluff 4.
- the filter disks 9 are divided into filter disk sectors 11 .
- the filter disks 9 rotate slowly and one filter disk sector 11 after the other is immersed in the suspension 7 .
- a fiber layer also referred to as a fiber mat, is formed under hydrostatic pressure on the respective filter disc sector 11 and a cloudy filtrate, also referred to as FF (foul filtrate), is separated. This fiber layer that is formed represents a flow resistance and a filter medium during further dewatering.
- the Flaupte dewatering takes place in a vacuum zone 24.
- a high capacity and a pure filtrate also referred to as clear filtrate CF (clear filtrate)
- clear filtrate CF clear filtrate
- the hollow shaft 13 is divided into sixteen separate channels 15, corresponding to the number of filter disk sectors 11 of the filter disk 9.
- Each filter disk sector is connected through a recess 17 in the hollow shaft to an associated channel in the hollow shaft for draining off the filtrate.
- the cross section of the channels 15 widens to
- the valve device 20 is mounted on the hollow shaft 13 .
- a wear disk with two adjustable filtrate bridges 31, 32 is located between the housing 21 of the valve device 20 and the hollow shaft 13.
- the stationary housing 21 of the valve device 20 is sealed off from the rotating hollow shaft 13 by the wear disk.
- the direction of rotation of the hollow shaft 13 is denoted by 45 .
- the channels 15 of the hollow shaft 13 open into the housing 21 of the valve device 20.
- a reservoir 61 is formed here in the area of the first filtrate bridge 31 .
- the second filtrate bridge 32 adjusts one end of the negative pressure zone 24 from which atmospheric conditions prevail again.
- the positions of the filtrate bridges 31, 32 can be adapted to the respective task, such as the quality of the suspension.
- a fixed division between the atmospheric zone 22 and the negative pressure zone 24 can be provided.
- a valve device 20 is shown in FIG.
- a drain 55 for a clear filtrate and a drain 57 for a super-clear filtrate are provided.
- the filtrate of the atmosphere zone 22 is referred to as cloudy filtrate FF and the filtrate of the vacuum zone 24 as clear filtrate CF.
- the resulting filtrate qualities are shown as a function of the angular position of the filter disc sector 11.
- valve device 20 prevents the formation of large air bubbles in the upper part of the valve and thus ensures a continuous transport of small air bubbles into the downcomer. This ensures a stable and high vacuum and consequently a high capacity and outlet consistency.
- the pressures prevailing in the vacuum zone are in the range from 0.1 to 0.6 bar.
- An embodiment of a filtrate bridge 31 with a reservoir 61 is shown in FIG. In previous valve devices 20 of disc filters 1, a channel 15 of the hollow shaft 13 is completely blocked by a filtrate bridge 31, 32, so that no leakage air can get into the vacuum zone 24 at a transition between the two pressure zones 22, 24.
- the filtrate flow flowing out of the channel 15 of the hollow shaft 13 in the atmospheric part is stopped upon entry into the negative pressure zone 24 .
- the rotation of the hollow shaft 13 opens the channel 15 back to the negative pressure zone 24 and the flow of filtrate begins again.
- This stopping has an effect on the throughput and the filtrate quality of the disc filter 1.
- the filtrate can accumulate and even the filtrate can flow back.
- a reduced adhesion or a slight lifting can occur between the fiber layer that has already been formed and the filter disk sector 11 .
- a slight lifting or resuspension of the fiber mat formed in the atmosphere zone 22 can also occur.
- Orifices with a hole pattern in the vacuum area following the filtrate bridge have also been provided for a particularly gentle build-up of the filtrate flow.
- this achieves a steady build-up and therefore a gentle build-up of the filtrate flow, this further delays the build-up of the full negative pressure and shortens the time at full negative pressure.
- FIG. 4 shows a filtrate bridge 31 with a reservoir 61 for reducing the dimming time.
- the fitrate bridge 31 covers an angular range in the circumferential direction. This angular range is referred to as the extent of the filtrate bridge in the circumferential direction 39 .
- the filtrate bridge 31 has a boundary edge 35 facing the vacuum zone 24 and a boundary edge 33 facing away from the vacuum zone 24 .
- the filtrate bridge 31 has an extension in the radial direction 37 to cover the radial extension of the channels 15 .
- the reservoir 61 shown here is cup-shaped and has an inlet opening 63 for liquid.
- the reservoir 61 has a height 69 and a radial extension 67 .
- the reservoir 61 adjoins the filtrate bridge 31 at the boundary edge 35 facing away from the vacuum zone.
- the reservoir 61 has an opening 65 on the side facing the channels 15 .
- the shortening area 41 of the filtrate bridge 31 is shown in FIG. 4 for illustration purposes. This shortening area 41 characterizes the area of an undercoverage.
- the delimiting edge 33 ' that is drawn in characterizes the original delimiting edge without undercoverage.
- the channel 15 of the hollow shaft 13 passing through this filtrate bridge 31 is never completely blocked by the filtrate bridge 31 .
- An opening 65 of the reservoir 61 is formed in the area of the shortening 41 , so that the shortening area 41 is always fully charged with liquid through the opening 65 of the reservoir 61 .
- the filtrate bridge 31 is completely shortened over the entire radial extent 37 of the channels.
- the extension of the reservoir in the circumferential direction goes beyond the cut area 41, so that sufficient liquid volume for dimming by means of liquid is available.
- the reservoir 61 has a filling volume in the range from 10 to 100 liters.
- the required filling volume of the reservoir can be adjusted to the undercover area and the suspension.
- the reservoir is to be designed in such a way that it is ensured that no volume of gas penetrates into the underpressure zone 24 via the undercover 41 . Gas volume does not mean the air bubbles contained in the filtrate and trapped by the filtrate.
- the reservoir 61 is attached to the housing 25 of the vacuum valve 23 and covers the entire adjustment range of the filtrate bridge 31 with its opening 65 .
- the reservoir 61 could also be attached to the filtrate bridge 31 itself.
- the opening 65 can then be designed to match the shortening area 41 of the filtrate bridge 31 .
- the opening 65 of the reservoir 61 is then also adjusted.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Valve Housings (AREA)
- Details Of Valves (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE2351372A SE2351372A1 (en) | 2021-05-04 | 2022-04-27 | Valve device for a disc filter |
DE112022001056.8T DE112022001056A5 (de) | 2021-05-04 | 2022-04-27 | Ventilvorrichtung für einen Scheibenfilter |
ATA9088/2022A AT526990A5 (de) | 2021-05-04 | 2022-04-27 | Ventilvorrichtung für einen Scheibenfilter |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102021111464.0 | 2021-05-04 | ||
DE102021111464.0A DE102021111464A1 (de) | 2021-05-04 | 2021-05-04 | Ventilvorrichtung für einen Scheibenfilter |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2022233658A1 true WO2022233658A1 (de) | 2022-11-10 |
Family
ID=81850230
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2022/061145 WO2022233658A1 (de) | 2021-05-04 | 2022-04-27 | Ventilvorrichtung für einen scheibenfilter |
Country Status (4)
Country | Link |
---|---|
AT (1) | AT526990A5 (de) |
DE (2) | DE102021111464A1 (de) |
SE (1) | SE2351372A1 (de) |
WO (1) | WO2022233658A1 (de) |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB736815A (en) | 1952-12-08 | 1955-09-14 | Paxman & Co Ltd Davey | Improvements in distributing valves for rotary suction filters |
US3452874A (en) | 1967-11-02 | 1969-07-01 | Dorr Oliver Inc | Trunnion valve for continuous rotary filters |
DE2203657A1 (de) | 1971-01-27 | 1972-08-17 | Erie Development Co., Cleveland, Ohio (V.StA.) | Vakuumscheibenfilter |
EP0400787A2 (de) | 1989-04-17 | 1990-12-05 | Ingersoll-Rand Company | Einstellbare Klappe für Rotationsfilter |
WO1996003196A1 (en) * | 1994-07-25 | 1996-02-08 | Ingersoll-Rand Company | Air inflow restrictor for disc filters |
WO1999025456A1 (en) | 1997-11-13 | 1999-05-27 | Beloit Technologies, Inc. | Adjustable control valve system for rotating disc filter |
DE102010039512A1 (de) | 2010-08-19 | 2012-02-23 | Voith Patent Gmbh | Scheibenfilterdichtung |
WO2013038069A1 (fr) * | 2011-09-16 | 2013-03-21 | Gaudfrin | Dispositif de réduction du frottement entre des plaques d'étanchéité d'unités de filtration et son utilisation dans un procède de filtration |
WO2018109258A1 (en) * | 2016-12-16 | 2018-06-21 | Outotec (Finland) Oy | Distributor valve body for a vacuum filter, a combination and a vacuum filter having such a distribution valve body, and methods related thereto |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3622103A1 (de) * | 1986-07-02 | 1988-02-25 | Alfons Dipl Ing Schotten | Scheiben - membran - pressfilter |
-
2021
- 2021-05-04 DE DE102021111464.0A patent/DE102021111464A1/de not_active Withdrawn
-
2022
- 2022-04-27 SE SE2351372A patent/SE2351372A1/en unknown
- 2022-04-27 AT ATA9088/2022A patent/AT526990A5/de unknown
- 2022-04-27 WO PCT/EP2022/061145 patent/WO2022233658A1/de active Application Filing
- 2022-04-27 DE DE112022001056.8T patent/DE112022001056A5/de active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB736815A (en) | 1952-12-08 | 1955-09-14 | Paxman & Co Ltd Davey | Improvements in distributing valves for rotary suction filters |
US3452874A (en) | 1967-11-02 | 1969-07-01 | Dorr Oliver Inc | Trunnion valve for continuous rotary filters |
DE2203657A1 (de) | 1971-01-27 | 1972-08-17 | Erie Development Co., Cleveland, Ohio (V.StA.) | Vakuumscheibenfilter |
EP0400787A2 (de) | 1989-04-17 | 1990-12-05 | Ingersoll-Rand Company | Einstellbare Klappe für Rotationsfilter |
WO1996003196A1 (en) * | 1994-07-25 | 1996-02-08 | Ingersoll-Rand Company | Air inflow restrictor for disc filters |
WO1999025456A1 (en) | 1997-11-13 | 1999-05-27 | Beloit Technologies, Inc. | Adjustable control valve system for rotating disc filter |
DE102010039512A1 (de) | 2010-08-19 | 2012-02-23 | Voith Patent Gmbh | Scheibenfilterdichtung |
WO2013038069A1 (fr) * | 2011-09-16 | 2013-03-21 | Gaudfrin | Dispositif de réduction du frottement entre des plaques d'étanchéité d'unités de filtration et son utilisation dans un procède de filtration |
WO2018109258A1 (en) * | 2016-12-16 | 2018-06-21 | Outotec (Finland) Oy | Distributor valve body for a vacuum filter, a combination and a vacuum filter having such a distribution valve body, and methods related thereto |
Also Published As
Publication number | Publication date |
---|---|
AT526990A5 (de) | 2024-07-15 |
DE112022001056A5 (de) | 2024-02-01 |
DE102021111464A1 (de) | 2022-11-10 |
SE2351372A1 (en) | 2023-11-30 |
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