专利摘要:
The invention provides a novel filter press comprising a filter chamber wall adapted to be axially displaced for exposing a plurality of filter units contained in the filter press. A certain clearance is provided between the substantially circular filter units and the interior wall surface of the housing or casing, the latter being sealed only adjacent its ends in cooperation with respective end walls. The sealing surfaces are disposed at locations away from the areas coming into contact with the filtering residues on evacuation and cleaning of the filter chamber. A particularly advantageous embodiment of a rotor for a filter press of this type is composed of rotor disks each comprising two axially displaceable rigid pressure plates which are prevented from being rotated by a hub disk interposed therebetween and non-rotatably mounted on the rotor shaft. The introduction of a pressure fluid through the rotor shaft into a cavity between the two plates permits the plates to be forced apart to thereby squeeze retained liquid from the filter cakes on the adjacent filter frames (FIG. 3).
公开号:SU1531841A3
申请号:SU864028731
申请日:1986-12-22
公开日:1989-12-23
发明作者:Купка Дитер
申请人:Бауко Баукооператион Гмбх (Фирма);
IPC主号:
专利说明:

one
(21) 4028731 / 23-26
(22) 12.22.86
(31) G 85 60 084.9
(32) 12/23/85 OZ) DE,
(46) 12/23/89. Bul Number 47
(71) Bauko Baukooption GmbH (AT)
(72) Pnter Kupka (DE)
(53) 66.067.3 (088.8)
(56) USSR Author's Certificate No. 70587, cl. On 01 D 25/12. 1948.
(54) FILTER PRESS AND ROTOR DISK .WHL FILTER PRESS
(57) The invention relates to filter presses and makes it possible to look at the degree of dehydration while ensuring the rapid removal of dry filtrates. The filter press has support plates 2, a shell 4 with an internal cavity of circular cross section, equipped with an arrangement for its axial movement, rotary disks 7 rigidly connected to the hollow shaft 8 and mounted rotatably and displaced relative to the auxiliary filtering means 28.
7 J JJJJ / 5 fS30 ZJ
//
with
(L
01
with
00
iju

cm
FIG.
3153
Fzggy i;,. ie, frames 6 are installed with kpl1,, 11l: 1-п: - (or to shell 4, which are interconnected KaMOjJM for pool) 1D) 1 30. The filtrate chambers 31 are equipped with exhaust pipe 10 with iiMf -ycKHMM clan} 1st (stopper), pro; - -: 1d 1de11 along the axis of the body. The shell 4 and the support plates 2 are fixed on the frame independently of the filter frames 6. The end walls 14 of the support ШП1ТЫ are equipped with 0-shaped sealing rings and made with grooves having a dovetail cross section. The sealing rings are placed in the grooves connected with r, pdol, o
The invention relates to a filter press and a rotor disk of a filter press.
The purpose of the invention is to increase the degree of dehydration while ensuring rapid removal of the dry filtration cake.
Pa figs. 1 and a filter press in the closed position of the housing J in FIG. 2 - the same, D is the open position of the body, on (lig. 3 - the same, n closed 11 °; body Auger 1, partial
incision; in fig. 4 - then w ;, (1) ragmeite on the magnification scale J on (lig. 5 - section L – pa of Fig. 3; figure 6 - section Fi-I) iia of fig. 3; in fig. 7 - rotary disk, one HHMi i cut; in fig. 8 - the same, in the increased masigga be; in fig. 9 - location of the rotor disk from the side of the hollow shaft; in fig. 10 - rotary disk, general view; in fig. 11 and 12 - the same, equipped with floating blocks, a general view.
Filter press 1 consists of support plates parallel to one another on the frame
2 related to each other
3. On the tires 3, they are installed} with the possibility of longitudinal movement of two, shell shells 4, predominantly cylindrical in shape, which are located on both sides of the middle support plate 2. In the space bounded by the shell shells 4, they are located axially in each closed position another is somewhat filtering. There is also a support device, a device for moving the hollow body in the axial direction relative to the bed. The rotor disk is equipped with eccentrically mounted spring-loaded guide bushes, forming a cavity of variable volume, and two rigid plates with a disk placed between them mounted on the hub. The rotor disk can also have axial floating blocks installed with the possibility of filling them with pressure medium in two working directions, while the blocks are made in the form of a piston-cylinder. 2 sec. and 9 hp f-ly, 12 ill.
units 5, each of which consists of a filter frame 6 and a corresponding rotor disk 7. The rotor disks 7 are rigidly connected to the hollow shaft 8 and mounted for rotation. The filter frames 6, regardless of the hulls A of the housing, are supported by base plates 2.
Chtangi 9 and pipe 10 are evenly distributed around the perimeter of the filter frames (Fig. 6).
Provided supporting shells
11. Covers 4 cases in the upper part have at least one hole
12, working on the inlet and outlet. In the lower part, each shell 4 of the housing has at least one shutter 13. Each of the chambers is bounded by the ends on one side of the middle support plate 2, and on the other side by the end wall 14. The end walls 14 are axially connected to the support plates
2 and supported by them. Their distance from the outer base plates 2 corresponds approximately to the axial length of the shell 4 of the housing, thereby, due to the axial movement, the corresponding filtrate chamber can be completely released (Fig. 2). Dp filter frame supports 6 in the support plates 2 there are two different | forms of support devices.
According to the first form of implementation (Fig.2
3 and 6) left-hand filtrate chamber. According to this exemplary embodiment, two axially arranged cameras pass through the filtration chamber.
the rods 9, fastened both to the base plate 2 and to the facing walls 14, and the end walls 14 are installed in the axial position and hold the filter frames 6 provided for this purpose with corresponding protrusions 1. The bottom of the frame 6 is supported by a pipe 10, which passes axially through the filtration chambers and a support, at least in the middle support plate 2. The rods 9 and the pipe 10 are evenly distributed around the perimeter of the filter frames (Fig. 6).
The filtration chamber in FIG. 2, 3 and 7 are made according to the second form of implementation.
In this example, the middle support plate 2 and the end walls 14 in the upper part of the perimeter of the hydraulic frame 6 are connected to each other by means of the supporting shells 11, having approximately a quarter circle in cross section and fixed on both sides of the upper highest point of the filter 6 on the middle supporting plate 2 and end walls 14, and the shell 11 overlap the chamber in the upper part approximately to the middle (Fig. 4).
The support shells 11 are plates of metal, tin, or polymer material and they have cameras 6 with MORE THAN FINGERS and threaded fingers, and the bottom of chamber 6 is supported by a pipe 10. Partitioning of the support structure in the 1P1-AH filter chamber into two support shells 11 has the advantage that during maintenance one of the loose shells can be dismantled, and the other holds a filtration frame. In order to avoid contaminating raids in the space between the support shells on the support plates.2 and the end walls 14, it is desirable to fill them with a nozzle in the form of strips (Fig. 7).
Using the hydraulic unit (Fig. 3) (cylinder 15 and piston ha 16), each hull shell 4 moves axially, the cylinder 15 being fixed on the hull shell 4, and piston drag ha 16 on the outer support plate 2. A device is provided for moving the hollow shaft axially with respect to the bed. To do this, on tires 3 is installed {Novlena is moved along the plate
0
five
0
five
0
five
0
five
0
five
17, on which the drive unit 18 is fixed for rotating the hollow shaft 8. The plate 17 with the right support plate 2 is connected by means of a hydraulic unit consisting of a cylinder 19 and a piston rod 20. The cylinder i9 is fixed on the plate 17, and the piston rod ha 20 - on the right support plate 2. With this hydraulic unit it is possible to replace the plates 17, the drive unit 18, the shaft 8 and the rotor discs 7. The rods 9 (FIG. 3) can be made in the form of tubes having intermediate spaces between the rotor discs discs 7 and filter frames; 6 holes that serve as supply lines Mi for rinsing air compressed air, etc. The pipe 10 has a three-way valve 21 through which the filtrate can be discharged.
The function of the rods in the second embodiment is performed by the frame 22 in the form of a cage or tube connecting the end wall 14 to the outer base plate 2 by means of bolted joints.
The filtration chamber (Fig. 4) at the ends, on the one hand, is bounded by the middle support plate 2, and on the other, by the end wall 14 and is closed outside by a rim 4 made in the form of a tube and installed by means of the supporting sulfur 23, in which holes are made guide tires 3 (mainly three, evenly distributed around the perimeter of the Liltr-press).
The middle support plate 2 and the right end wall 14 have an annular groove 24 or 25 along their perimeter, in which a sealing 0-ring 26 is located. The shell shell 4 has at its end machined sealing surfaces 27 which are in the open position of the filtration chamber mostly outside the area of its impact. The annular grooves 24 and 25 have a cross section preferably in the form of a dovetail, tapering towards their free side, and the annular seals 25 abut their ends. The chambers are provided with outwardly connecting chambers through which pressurized medium, in particular compressed air, can be introduced into the chamber, which allows refusing accurate sealing surfaces on the shells 4 of the body, the middle support plates 2 and the end walls 14. Alternatively, the snubber ring 26 can be seals from swollen bodies, compressed air. Each filter unit (fig. 3) consists of a frame 6 and a rotor disk 7. The blocks are located symmetrically, i.e. each filtering frame 6 has on both sides auxiliary filtering means 28, for example, in the form of a perforated plate or web, and each rotor disk 7 is provided on both sides with pressure surfaces 29. The filter cake 30 (Fig. 4) is between filtering means 28 and surfaces 29 (pulp chambers). The cavities formed by the auxiliary filtering means 28 of the chamber 31 of the filtrate are closed at the pipe 10 (lower part of FIG. 4). The rotor discs are made hollow and their internal space is connected with a hole in the hollow shaft 8. There is a gap 32 between the filtration chambers and the shaft 8, and between the rotor discs 7 and the frames 6 on the one hand and the casing 4 on the other side there is a gap 33. as soon as the shell 4 of the housing is pulled away from the 0-shaped rings 26 and the middle support plate 2 or end wall 14, or as soon as the seal is disconnected due to the removal of air from the sealing chambers, the shell can freely slide without touching the rotor disks and phi Because of the existing intermediate space, it is not affected by the impurities deposited there.
The design of the rotor disk (Fig. 7) consists of a hub disk 34 mounted on a rotating shaft 8 and having several eccentrically arranged guide sleeves 35 welded to the disk of the hub 34. The rotor disk 7 also consists of two rigid plates 36, which have the shape of a circle and are located on both sides of the disk; step No. 1 34. These plates 36 form the pressing surfaces of the rotor disk, are mounted on the shaft 8 with the possibility of axial displacement, and are sealed with O-ring o-rings 37, Gschhs in appropriate x ring grooves.
five
0
five
0
five
0
five
five
0
The plates 36 are pinched from rotation with respect to the shaft by means of guide pins 38, made in the form of sleeves, which are inserted into guide sleeves 33 through corresponding openings in the plates 36. Both plates 36 of the rotor disk 7 are retracted with each other by a return spring 39 At their outer perimeter, both plates 36 are connected to each other by means of an elastic ring-like seal 40, which is generally U or P-shaped. The outer pins of this seal 40 are fixed on the inner sides of the plates 36. The cavity 41 is closed by plates 36, a seal
40 and the shaft 8, at least through one hole made in the shaft 8, is connected with the axial hole 42 of the hollow shaft 8. By pumping pressure medium from the hollow shaft 8 through the transverse hole 43 into the cavity
41 the distance between the plates 36 may increase despite the tensile force of the springs 39. Each of the plates on its outer side forming the pressing surface has at least one transverse hole
43, going from the inner to the outer edge of the slab.
The guide bushes 38 (Fig. 8), the retaining plates 36 on the hub disk 34, have at their outer end a flange ring 44 mounted on the plate 36 by means of bolts 45. A 0-shaped o-ring seal 46 in the groove zone between the flange ring 44 and With the cylindrical section 47 of the guide sleeve 38, the cavity 41 is sealed from the outside. The return spring 39 is located inside the space closed by the sleeves 38, and is installed with the help of a washer 48 and a bolt 49 on the flange ring 44 of one of the directions gp51x of the sleeves. At the other end of the rod 39 is fastened using the same clamp 48, bolt 49 and nut 50, screwed on its outwardly protruding end of bolt 49, with such fastening with the help of nut 50 a certain force of the return spring 39 can be set. The seal 40 in cross section along both sides of the i-shaped section have external pins 51, which are tightly clamped between the shields 52 and the inside of the plate 36 with bolts 53. When filling the cavity 41 of the pressure pans, both plates 36 expand in the direction of arrow A, and U-shaped in cross section the seal 40 is deformed accordingly. When the pressure in the cavity 41 drops, the return springs 39 again bring both plates together until they are pressed against the ends of the guide sleeves 35.
Seal-side sealing (Fig. 9 is carried out using a device in which between the disc of the hub 34 and each of the plates 36 there is an elastic sealing ring 54 of a U-shaped cross section, clamped on the plate 36 by means of an annular washer 55 and bolt 45, and disk hub 34 - clamped by means of a corresponding ring-shaped washer 56 and bolt 45.
The protrusions 57 and, accordingly, the flute recesses in the washers 56 may facilitate installation and improve the sealing function.
Access from the hole 42 of the shaft 8 to the cavity 41 between the plates 36 ocynjecT- is through the transverse hole 43 in the wall of the shaft 8, as well as through its continued opening 58 in the disk of the hub 34. The material for seals 40 and 54 of the u-shaped cross section is the material mainly reinforced with cloth, rubber or polymer material. Such materials can, without damage, withstand, with appropriate geometrical dimensions, working pressures reaching a magnitude of the order of up to 20, while maintaining a high elastical strength.
The shaft 10 shows a plate 36 with three guide bushings 38 evenly distributed on it, flange rings 44 of which are fixed to the plate 36 by bolts 45. From the middle of the plate 36 to the front there pass three evenly distributed nonetrechnye holes 43. They go along an arc that, when starting counter-clockwise, the sediment moves outwards along these edges.
The rotor disk 7 (Fig. 11) consists of a hub disk 34 connected to a hollow shaft 8, made in the same way as the hub disk 34 (Fig. 7).
Instead of the guide bushings 35, the disk set 1-134 has hydraulic or pneumatic blocks (piston 59 - cylinder 60) floating on the disk 0
five
0
five
0
five
0
five
0
five
34, while the piston 59 is connected to one of the plates 36, and the cylinder 60 to the other plate 36. Since the blocks (piston-1 and 1pindr) transmit the rotation from the disks to the plates, they are made rigid in the direction transverse to their longitudinal axis . The plates 36 can have opposite edges axial flange rings 61 and 62 on their edges, inserted into each other and sealed against each other using 0-shaped rings 63 mounted on the front edge of the inner side of the outer flange ring 61.
The blocks (piston 59 - cylinder 60) are mainly used double acting blocks, in which the cylindrical chambers 64 and 65, located on both sides of the piston, can be filled with a pressure medium. Then the plates 36 can be moved apart from one another to fill the chamber 65, and to fill the other chamber 64 with a pressurized liquid, bring the plates closer to one another. In this case, two pipelines 66 and 67 are provided in the hollow shaft 8. Filling of chambers 64 and 65 is possible with the help of a valve mechanism (not shown) that switches the working medium to different chambers.
Phage 12 is represented by simplified blocks (piston 68 is cylinder 69), where plates 36 are returned to their original position by means of spring mechanisms 70.
In this case, for the operation of the blocks, the piston 68 - cylinder 69 can be used only the supply pipe 71 for the pressure medium.
The principle of the filter press follows.
Before starting the operation, the filtration chambers are closed with shells 4 of the body adjacent to the middle separation plate 2 of the filter press. The pulp to be filtered is then continuously withdrawn through the gate 13. The gaseous and volatile components discharged together with the pulp flow through the openings 12. The filtrate passes through the auxiliary filtering means 28 into the filtrate chambers located behind them and from there into the exhaust pipe 10. During movement, the hollow shaft 8 using the drive unit 18, it is brought into slow rotation, which is h: Nii, i g is reversed, the following hzie: G {1 pulp in the filtration chamber is in constant motion, due to which it is provided Sludge sedimentation on auxiliary filter media 28. In this case, the hollow shaft 8 can be reciprocated using hydraulic blocks 19 and 20, preferably with a decrease in pressure, and it can be evenly processed in accordance with its structure on the auxiliary filter means. When a sufficient amount of sludge is collected on the auxiliary filtering means, the next portion of pulp is supplied and the shaft 8 stops. Then a hollow shaft 8 is supplied to the rotor discs with pressurized medium (water or hydraulic oil). which expands the plates 36 against the compressive force of the springs 39, and presses the sediment on the auxiliary filter media to further dehydrate it. The pulp remaining in the filtration chamber is discharged through gate 13 and proceeds to the next filtration cycle. The pressurized medium is then discharged from the rotor discs 7. Compressed air can be blown through the tubular rods 9, if necessary, for further drying of the precipitates into the filtration chambers. The compressed air simultaneously removes sludge from the filtration chambers if it is not fully filled through the gates 13. Then the filtration chambers open axially peremegtseniyami shells 4 buildings. The space under the blocks 5 is now fully open and the precipitates can be removed from the auxiliary filter media by rotating the shaft 8 and the benefit of the 1st plates 36 in contact with the sediments. For this, the rotary disks 7 can be unfolded in the previously mentioned way or the shaft 8 by means of hydraulic blocks 19 and 20 can reciprocate.
By means of a three-way valve 21, a backwash is also possible, with washing liquid being supplied to the frames. This can occur 5 with both open and closed housing. In the future, it is possible to fill the filtration chambers.
s
0
five
0
five
0
five
0
five
The liquid that is supplied through the rods 9 with holes or nozzles, and then the washing liquid is discharged from the side of the shutter 13.
The precipitates during cleaning can be freely removed from the chamber downwards without contact with absorbing surfaces. Therefore, these sealing surfaces remain clean or require only minimal cleaning costs. Due to the intermediate volumes between the filter units and the casing shell, the cleaning of the filter chamber after it has been emptied is not required, as the remaining contaminants do not have a harmful effect.
权利要求:
Claims (11)
[1]
1. Filter press containing horizontally located on the frame of the body with a slurry for pulp, support plates, the shell, the internal cavity of which has a circular cross-section, several located in the housing axially one after another of the filter frames, the filtrate chamber, closed in the radial plane by filtering means; pulp chambers, formed between auxiliary filtering means and a rotary disk rigidly connected to the hollow shaft, mounted rotatably, characterized in that order to increase the degree of dewatering at ensuring rapid removal of the dry filter cake, is provided with a device for axial movement of the housing shell and the rotor disk movement device with respect to
auxiliary filtering media, filtering frames are installed with an annular gap to the casing, interconnected chambers for pulp, and the filtrate chambers are equipped with an exhaust pipe with an exhaust valve passing along the axis of the body, while the casing and supporting The plates are fixed in the frame, regardless of the filter frames.
[2]
2. The filter press according to claim 1, characterized in that the end walls of the r-porous plate are provided with O-different sealing rings and are filled with grooves having popeps
A dovetail-shaped cross-section is in this case smoothing rings placed in the slots associated with the supply of pressure medium in them.
[3]
3. The filter press according to claim 1, which is equipped with a support device made in the form of a support wall and hollow rods with bolts attached to the support plates.
[4]
4. The filter press according to claim 1, which is based on the fact that the support device is made in the form of shells attached to the base plate, having the form of an arc of a circle, an additional support machine and a cell frame, while an additional support wall is attached to base plate through the cell frame.
[5]
5. The filter press according to claim 1, characterized in that the shell is made with a shutter in its lower part.
[6]
6. The filter press according to claim 1, wherein the filter is equipped with a device for moving the hollow shaft in the axial direction relative to the bed.
[7]
7. A rotor disc for a filter press containing a pass through the filter press through a hollow shaft and several spaced apart from it with each other with the possibility of rotation of the discs containing a cavity connected to the hollow shaft opening and closed two symmetrically with respect to each other by auxiliary filtering means, characterized in that.
0
,
five
0
In order to increase the degree of decompression while ensuring quick removal of the dry filtration cake, it is equipped with eccentrically mounted spring-loaded bushings, which form a cavity of variable volume, with two hard glues with positioned. between them, a disk mounted on the hub, and elastic sealing elements, a closed cavity bounded by rigid plates, while located on the hollow shaft with the possibility of axial movement.
[8]
8. The rotor disc according to claim 7, in which it is provided with an edge extending along its axis and with i-shaped seals along the outer perimeter and the inner perimeter near the hollow shaft.
[9]
9. The rotor disc in accordance with claim 7, wherein the rotor plates are mounted on the hollow shaft by means of 0-rings.
[10]
10. The rotor disc according to claim 7, characterized in that it is provided with several axially floating blocks in the form of a piston-cylinder, wherein the piston of each block is connected
with one hard plate, and C11 1 Cindr with another hard plate, the blocks are connected with a line of adjustable supply of pressure medium passing along a hollow shaft.
[11]
11. The rotor disc according to claim 7, which is based on the fact that the units are installed with the possibility of iix filling with pressure medium in two working directions.
2 22
A / j
7 6
Phage. 2
ff 11
Sc |
00
"U
6
Fiel
36
51 g 52
Fie.8
Fie.9
36
FIG. ten
6362 61 // /
/
6
11
FIG. 12
类似技术:
公开号 | 公开日 | 专利标题
SU1531841A3|1989-12-23|Filter-press and rotary disc to filter-press
US4526688A|1985-07-02|Pressure filter with vibratory impactor
WO1993019830A1|1993-10-14|Filter apparatus and method
EP0243091A2|1987-10-28|Method of and apparatus for filtering a slurry
US5154825A|1992-10-13|Automatic filter press
CA2274683A1|1998-06-18|Apparatus for continuous purification of liquids, dewatering and drying of the separated solids
FI75500C|1988-07-11|Sludge filtration method and apparatus.
US5107757A|1992-04-28|Apparatus for dewatering waste material by capillary action
US3919087A|1975-11-11|Continuous pressure filtering and/or screening apparatus for the separation of liquids and solids
KR920002806B1|1992-04-04|Two-stage batch filter apparatus and filtration process
EP0226659B1|1989-05-17|Filter press
US4702845A|1987-10-27|Rotary drum filter
US4816147A|1989-03-28|Filter press-type filtering apparatus using rigid filter element
RU2217211C1|2003-11-27|Filtering plant for cleaning liquids from oil and petroleum products
CN212262499U|2021-01-01|Vertical rotary multi-station diaphragm filter press
KR100193751B1|1999-06-15|Centrifuge for Solid and Liquid Separation
SU488597A1|1975-10-25|Filter for cleaning liquids
CN112044127A|2020-12-08|Vertical rotary multi-station diaphragm filter press
SU1154214A1|1985-05-07|Pressure filter for purifying petroleum-containing waste water
SU1292803A1|1987-02-28|Filter
CN113813658A|2021-12-21|Slurry filter press for bridge pile foundation construction
JP3318461B2|2002-08-26|Filtration machine
SU1699522A1|1991-12-23|Liquid cleaning filter
RU1790973C|1993-01-30|Water cleaning filter
SU1380762A1|1988-03-15|Filter-press of piston type
同族专利:
公开号 | 公开日
NO170131B|1992-06-09|
DK624686A|1987-06-24|
JPH0431723B2|1992-05-27|
NO170131C|1992-09-16|
FI865258A|1987-06-24|
AU6689386A|1987-06-25|
BR8606395A|1987-10-13|
JPS62155910A|1987-07-10|
HUT45910A|1988-09-28|
AU590174B2|1989-10-26|
HU198634B|1989-11-28|
DK624686D0|1986-12-22|
DK168913B1|1994-07-11|
US4781828A|1988-11-01|
PL263077A1|1987-09-07|
DD252766A5|1987-12-30|
NO865255L|1987-06-24|
BG49377A3|1991-10-15|
FI84785C|1992-01-27|
CA1267032A|1990-03-27|
CZ280814B6|1996-04-17|
KR950001272B1|1995-02-15|
NO865255D0|1986-12-22|
PL154844B1|1991-09-30|
FI84785B|1991-10-15|
CZ969986A3|1996-02-14|
FI865258A0|1986-12-22|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

US2975903A|1957-10-31|1961-03-21|Process Filters Inc|Filter|
US3117083A|1960-11-09|1964-01-07|Przhilensky Jury Iosifovich|Mechanized automatic frame filter press|
US3948776A|1974-11-18|1976-04-06|Artisan Industries Inc.|Apparatus and system for generating a protective coating in a rotary concentrator for abrasive solids-containing fluids|
JPS5343824U|1977-09-16|1978-04-14|
US4235721A|1978-03-16|1980-11-25|Kurita Machinery Manufacturing Company Limited|Reinforcing patch plate applied to liquid passage hole in filter-surfaced expressing sheet on expressing filter plate|
JPS59230613A|1983-06-14|1984-12-25|Tsukishima Kikai Co Ltd|Concentrating filtering method and apparatus therefor|
US4722789A|1984-07-18|1988-02-02|Baukooperation Gmbh|Chamber filter press with rotor plates|AU584461B2|1985-09-06|1989-05-25|Kurita Machinery Manufacturing Co., Limited|Filter press|
DE3813343C2|1988-04-21|1994-11-17|Biersdorf Apparatebau|Rotor filter device for a liquid mixture|
US6117322A|1993-06-23|2000-09-12|Pall Corporation|Dynamic filter system|
US5679249A|1991-12-24|1997-10-21|Pall Corporation|Dynamic filter system|
FR2718053B1|1994-04-01|1996-05-31|Interbrew Sa|Elastic membrane filter press, filtration process using such a filter.|
DE19705855A1|1997-02-15|1998-09-03|Seitz Filter Werke|Filtration device|
JP3988002B2|1997-07-04|2007-10-10|株式会社ジーエス・ユアサコーポレーション|Filter-press type solid polymer water electrolysis cell|
DE69928640T2|1998-09-17|2006-06-08|Ishigaki Co. Ltd.|DRAINAGE DEVICE THROUGH CONTINUOUS CRUSHING|
AT411430B|2002-06-19|2004-01-26|Andritz Ag Maschf|FILTER OR SORTING DISC AND METHOD FOR PRODUCING IT|
DE10357520A1|2003-12-08|2005-07-07|Andreas Kufferath Gmbh & Co. Kg|Rotational shearing filter|
CN106621502B|2016-10-19|2019-01-04|核工业烟台同兴实业集团有限公司|A kind of turnover panel limit water receiving scraper device for belt filter press|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
DE8560084|1985-12-23|
[返回顶部]