CN206843849U - Disc stack multiple roll filtrate machine - Google Patents
Disc stack multiple roll filtrate machine Download PDFInfo
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- CN206843849U CN206843849U CN201720713731.XU CN201720713731U CN206843849U CN 206843849 U CN206843849 U CN 206843849U CN 201720713731 U CN201720713731 U CN 201720713731U CN 206843849 U CN206843849 U CN 206843849U
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- mainframe box
- filtrate
- roller group
- disc stack
- corrugation rolls
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- 239000000706 filtrate Substances 0.000 title claims abstract description 55
- 239000007788 liquid Substances 0.000 claims abstract description 48
- 239000000463 material Substances 0.000 claims abstract description 39
- 238000007599 discharging Methods 0.000 claims abstract description 23
- 238000002156 mixing Methods 0.000 claims description 16
- 238000003756 stirring Methods 0.000 claims description 13
- 230000033228 biological regulation Effects 0.000 claims description 11
- 230000001105 regulatory effect Effects 0.000 claims description 8
- 230000007246 mechanism Effects 0.000 claims description 7
- 230000006835 compression Effects 0.000 claims description 5
- 238000007906 compression Methods 0.000 claims description 5
- 238000009434 installation Methods 0.000 claims description 5
- 230000003828 downregulation Effects 0.000 claims description 3
- 230000003827 upregulation Effects 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 3
- 239000002002 slurry Substances 0.000 description 21
- 230000005484 gravity Effects 0.000 description 8
- 238000001914 filtration Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 238000005183 dynamical system Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 230000001476 alcoholic effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
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- 238000000151 deposition Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000010985 leather Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 235000014121 butter Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011981 development test Methods 0.000 description 1
- 230000005489 elastic deformation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 238000004076 pulp bleaching Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- -1 work Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
It the utility model is related to a kind of disc stack multiple roll filtrate machine, it includes mainframe box, the bottom of mainframe box opens up mainframe box filtrate (liquid, the middle part of mainframe box is arranged at intervals upper roller group and lower roller group, each roller group includes multiple corrugation rolls for being rotatably installed on mainframe box tank wall and being driven by actuating unit, each corrugation rolls in each roller group it is parallel and successively close to and be in linear array；The anterior of mainframe box sets mainframe box charging aperture, rear portion sets mainframe box discharging opening, space between two roller groups forms the service aisle of linking mainframe box charging aperture and mainframe box discharging opening, and service aisle is gradually reduced from its feed end to its discharge end in the curve-like and service aisle that rise after falling before from its feed end to its discharge end.The utility model has the advantages of de- liquid enrichment effect is good, operating efficiency is high, service life is long, applicable material concentration scope is wide.
Description
Technical field
Solid-liquid separating equipment field is the utility model is related to, specifically a kind of disc stack multiple roll filtrate machine.
Background technology
Solid-liquid separating equipment is widely used in industrial multiple fields, such as in sewage disposal, pulping and paper-making industry
Pulp washing, bleaching delignification liquid and finished pulp take off liquid enrichment, and light industry, chemical fibre, pharmacy, alcoholic, food, leather industry etc. need
The industry of filtrate is carried out to material.Solid-liquid separating equipment mainly includes being used for the de- black liquor of pulp washing press filtration, floated for paper pulp
Butter white liquor and the de- liquid enrichment equipment of press filtration for finished pulp and the sludge for sewage disposal system take off liquid enrichment equipment.
Traditional solid-liquid separating equipment species is various, there is double nets, folder net, horizontal stripes, drum-type, double helix, single-screw, sleeping
The de- hydraulic pressure filter enrichment type of the diversified forms such as spiral shell, plate and frame, the structure of each type and operation principle are different, respectively there is advantage and not
Foot.Such as：Double nets, folder net, the 7-15 days average life of filter press net, the price of a secondary net it is general thousands of in addition on
Wan Yuan, operating cost are high；Horizontal belt liquid remover, the discharge concentration of drum-type liquid remover are too low, and only 15% or so, rinse water wave
Fei great, operating efficiency are low；Centrifuge power consumption is more, double helix liquid remover, single-screw liquid remover in operation, helical axis and filter screen with
Material does Relative friction motion, and the life-span of helical axis and filter screen, at most only left and right, operating cost were high one year.In a word, it is traditional
Solid-liquid separating equipment generally existing input concentration narrow range, discharge concentration is low, efficiency is low, poor reliability, short life, operating cost
The defects of high, power consumption height, waste water resource.
Based on above mentioned problem, it is reasonable to have developed a kind of principle novel structure through development test for many years by this case utility model people
Solid-liquid separating equipment, the equipment be not only suitable for pulp washing press filtration take off black liquor, again be applied to association with pulp bleaching press filtration take off white liquor, also
Liquid enrichment is taken off suitable for finished pulp press filtration（Concentration is improved, is easy to transport for long-distance）, and be more suitable for municipal wastewater and handle, be light
The press filtration of the industry material such as work, chemical fibre, pharmacy, alcoholic, food, leather industry takes off liquid enrichment.
Utility model content
The technical problems to be solved in the utility model is to provide that a kind of de- liquid enrichment effect is good, operating efficiency is high, using the longevity
Life is long, is applicable the wide disc stack multiple roll filtrate machine of material concentration scope.
In order to solve the above technical problems, disc stack multiple roll filtrate machine of the present utility model includes mainframe box, the bottom of mainframe box
Mainframe box filtrate (liquid is opened up, it is characterized in that the upper roller group of middle part interval setting and lower roller group, each roller group of the mainframe box are equal
Including multiple corrugation rolls for being rotatably installed on mainframe box tank wall and being driven by actuating unit, each ripple in each roller group rolls out
Row and successively close to and curvilinear arrangement；The anterior of mainframe box sets mainframe box charging aperture, and rear portion sets mainframe box discharging opening,
Space between two roller groups forms the service aisle of linking mainframe box charging aperture and mainframe box discharging opening, and service aisle enters from it
Material end is gradually reduced to its discharge end in the curve-like and service aisle risen after falling before from its feed end to its discharge end.
Using said structure, the service aisle for conveying slurry from the front to the back is formed by upper and lower two roller groups, by each
The rotation of corrugation rolls conveys to slurry provides power, and filtrate is flowed out from the gap of corrugation rolls immediate vicinity, and the filtrate of outflow falls on
The bottom of mainframe box, and discharged via mainframe box filtrate (liquid.Passage is shaped to fall before after the curve-like that rises and
Service aisle is gradually reduced, and takes off liquid zone in the anterior gravity that formed of service aisle, the de- liquid of extruding is formed at the rear portion of service aisle
Area, it be concave regions that gravity, which takes off liquid zone, and under gravity, filtrate is fully sunk and from bottom outflow, realizes initial filter, slurry after
The continuous extruding for conveying and being gradually reduced into service aisle backward takes off liquid zone, is acted in the extrusion fit of upper roller group and lower roller group
Under, a part of filtrate is extruded from slurry, and another part filtrate, which is extruded and sinks to gravity, takes off liquid zone.It can be seen that two de- liquid
Area, which coordinates, fully to filter out the filtrate in slurry, and de- liquid enrichment effect is more preferable, meanwhile, using the rotation of roller as conveying power,
It is longer to convey reliable and stable and service life, convenient maintenance is changed.
The corrugation rolls include roll shaft and the multiple disks being sleeved on roll shaft, and each disk stacks successively at the middle part of roll shaft
Set and form the roll body of corrugation rolls, be provided for the annulus of filtrate, each roller group in corrugation rolls between adjacent two disk
Disk end on middle adjacent corrugations roller along close to position is staggered and two end faces of each corrugation rolls roll body correspond to respectively it is flat
It is neat to set.The roll surface of corrugation rolls is concavo-convex alternate corrugated, and the formation for corrugated roll surface can be directly in whole roll body table
Annular groove is opened up on face, this case preferably uses multiple disks to stack to form roll surface as undulatory roll body, adjacent corrugations roller
On disk end be staggered along position, form corrugated filtrate gap in immediate vicinity, the filtrate gap and adjacent discs it
Between annulus be used to filtrate, flexibly set according to the species and granular size of slurry for the big I in gap.For
Installation fit form between this kind of structure type and roller and roller of corrugation rolls, on the one hand can more flexible convenient setting filtrate
With the size in gap or gap, on the other hand can also increase whole roll body intensity and roller and roller between the stability that coordinates,
In addition, the structure stacked using this kind of disk, has been also convenient for carrying out maintenance replacing to single disk.
The bottom of the mainframe box discharging opening is installed with the discharging bottom plate being obliquely installed, and the top for the bottom plate that discharges is hinged
Have can rotation up and down regulation pressing plate, regulation pressing plate is obliquely installed and is provided with the mainframe box above it for adjusting its inclination
The flexible pressurizing mechanism of angle.Regulation pressing plate cooperatively forms the governor motion of mainframe box discharging opening size with the bottom plate that discharges, by
Flexible pressurizing mechanism, the extruding at pressing plate and service aisle rear portion take off liquid zone and coordinated, material extruded jointly, so as to enter one
Step improves de- liquid enrichment effect, meanwhile, the flexible tune to discharge concentration can be realized by the adjustment to regulation pressing plate angle of inclination
Section.
The flexible pressurizing mechanism includes sleeve that is vertically arranged and being fixedly mounted on mainframe box tank wall, the inside of sleeve
Lower slide is provided with the pressure head of extended sleeve bottom end, and the bottom of pressure head is resisted against on the top surface of regulation pressing plate, sleeve it is interior
Portion upper end is slidably fitted with sliding block, and tapped through hole is offered in the middle part of sliding block, rotates and pacifies in the surface of sleeve on mainframe box tank wall
Equipped with vertically arranged regulating bolt, the screw rod of regulating bolt is stretched into sleeve and is screwed onto in above-mentioned tapped through hole, sliding block
Compression spring is connected between lower end and the upper end of pressure head.Using the structure, regulating bolt is rotated by spanner etc., can be to sliding block
Highly it is adjusted, so as to the amount of elastic deformation of adjustable compression spring, and then the pressure size of pressure head is adjusted, to adjusting pressing plate
Angle be adjusted.Using the flexible pressure head structure of compressed spring type so that regulation pressing plate has certain flexible buffer amount,
Effectively slurry can be avoided to block while extruding.
The filtrate machine also includes agitator tank, is installed with filter cylinder inside agitator tank, uniform filter opening or filter on the barrel of filter cylinder
Seam, the bottom of agitator tank open up agitator tank filtrate (liquid, and the stirring vane driven by stirring motor is provided with filter cylinder；Filter cylinder its
In the top of a side wall offer the filter cylinder discharging opening connected with mainframe box charging aperture.Stirring vane is set in filter cylinder, will can be starched
Material stirs, and effectively avoids material from depositing.Filter hole or filter seam are set on filter cylinder, filtrate can be flowed out from filter hole or filter seam, and
Finally discharged from agitator tank filtrate (liquid, it is seen then that agitator tank also has pre-filtered function concurrently.
The front portion of the filter cylinder sets gradually blending bin and material feeding box, and the bottom of blending bin connects with the bottom of filter cylinder, mixes
The top of mould assembling connects with the top of material feeding box, and the bottom of material feeding box opens up material inlet.Slurry for needing dosing, mixed
Dosing in mould assembling, the slurry after dosing flow into the bottom of filter cylinder, can be equal by medicine and slurry agitation by the stirring vane in filter cylinder
It is even.
Separated between the blending bin and material feeding box by dividing plate, the top of dividing plate sets the V that can connect two tanks top
Shape opening, it is slidably fitted with for adjusting the baffle plate of openings of sizes so as to form the adjustable metering weir of flow on dividing plate.V-arrangement is set
Opening, and the size of V openings is adjusted by baffle plate, so as to flexibly being adjusted to flowing into the inventory in blending bin
It is whole.Wherein, the characteristics of bottom rate by V-arrangement opening is small, top flux is big so that Flow-rate adjustment is more stable more reliable.
Overflow pipe is installed, the bottom of overflow pipe passes the bottom wall of material feeding box and form overflow in the middle part of the material feeding box
Mouthful, the opening position that the top of overflow pipe is extended upwardly to close to material feeding box top is ended.Overflow pipe coordinates to charging with metering weir
Amount is adjusted, and so as to control appropriate material to enter blending bin, unnecessary material then flows out from overflow pipe and returns to feed bin.
In summary, the utility model is with de- liquid enrichment effect is good, operating efficiency is high, service life is long, is applicable material
The advantages of concentration range is wide.
Brief description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and detailed description：
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the fit structure schematic diagram of two corrugation rolls；
Fig. 3 is A portions mplifying structure schematic diagram in Fig. 2；
Fig. 4 is common disc structure schematic diagram；
Fig. 5 is the disk one of which structural representation of end；
Fig. 6 is the disk another kind structural representation of end；
Fig. 7 is the concrete structure schematic diagram at mainframe box discharging opening position.
Embodiment
Referring to the drawings, disc stack multiple roll filtrate machine of the present utility model includes mainframe box 1, and the bottom of mainframe box 1 opens up main frame
Case filtrate (liquid 2, the middle part of mainframe box 1 are arranged at intervals upper roller group and lower roller group, and each roller group includes multiple be rotatably installed in
The corrugation rolls 3 driven on mainframe box tank wall and by actuating unit, each corrugation rolls 3 in each roller group it is parallel and successively close to and be in
Curve shape arranges；Mainframe box 1 it is anterior set mainframe box charging aperture 4, rear portion sets mainframe box discharging opening 5, two roller groups it
Between space form the service aisle 6 of linking mainframe box charging aperture 4 and mainframe box discharging opening 5, service aisle 6 from its feed end extremely
Its discharge end is gradually reduced in the curve-like and service aisle 6 risen after falling before from its feed end to its discharge end.
In said structure, the passage 6 for conveying slurry from the front to the back is formed by upper and lower two roller groups, by each ripple
The rotation of roller 3 conveys to slurry provides power, and filtrate is flowed out from the gap of the immediate vicinity of corrugation rolls 3, and the filtrate of outflow falls on master
The bottom of cabinet, and discharged via mainframe box filtrate (liquid 2.Passage 6 is shaped to fall before after the curve-like that rises and
Channel width is gradually reduced, and takes off liquid zone in the anterior gravity that formed of service aisle 6, it is de- to form extruding at the rear portion of service aisle 6
Liquid zone.It is concave regions that gravity, which takes off liquid zone, and under gravity, filtrate is fully sunk and flowed out from bottom, realizes initial filter, slurry
The extruding for continuing to convey and be gradually reduced into service aisle backward takes off liquid zone, is acted in the extrusion fit of upper roller group and lower roller group
Under, a part of filtrate is extruded from slurry, and another part filtrate, which is extruded and sinks to gravity, takes off liquid zone.It can be seen that two de- liquid
Area, which coordinates, fully to filter out the filtrate in slurry, and de- liquid enrichment effect is more preferable, meanwhile, using the rotation of roller as conveying power,
It is longer to convey reliable and stable and service life, convenient maintenance is changed.
Referring to the drawings, corrugation rolls 3 include roll shaft 31 and the multiple disks 32 being sleeved on roll shaft 31, and each disk 32 is in roll shaft
31 middle part stacks successively sets and is formed the roll body of corrugation rolls, and filtrate is provided between adjacent two disk 32 in corrugation rolls 3
Annulus 33, disk end in each roller group on adjacent corrugations roller 3 along close to position is staggered and each corrugation rolls roller
Two end faces of body correspond to concordant set respectively.So-called corrugation rolls 3 refer to roll surface for concavo-convex alternate corrugated, for corrugated
The formation of roll surface, can directly open up annular groove on whole roll body surface, and this case preferably stacks shape using multiple disks 32
It is undulatory roll body into roll surface, the disk end on adjacent corrugations roller 3 is staggered along position, and corrugated is formed in immediate vicinity
Filtrate gap 27, the annulus 33 between the filtrate gap 27 and adjacent discs is used to filtrate, for gap or gap
Big I flexibly set according to the species and granular size of slurry.For this kind of structure type and roller and roller of corrugation rolls 3
Between installation fit form, on the one hand can the more flexible convenient size that filtrate gap or gap are set, on the other hand also
Can increase whole roll body intensity and roller and roller between the stability that coordinates, in addition, the structure stacked using this kind of disk,
Facilitate and maintenance replacing is carried out to single disk 32.
For the concrete structure of disk 32, as shown in Figure 4, Figure 5 and Figure 6, including three kinds of structure types, wherein, shown in Fig. 4
For the common structure of disk 32, the center of plain disk 32 opens up disk through hole 320, and the middle part of the wherein side of disk 32 sets ring
Shape erecting bed 321, edge set the heavy platform 322 of annular, and disk 32 is sleeved on roll shaft 31 by disk through hole 320, adjacent
Disk 3 is stacked, forms annulus 33 by the heavy platform 322 of annular successively by annular erecting bed 321.Plain disk end is along position
Section be tooth form, the roll body immediate vicinity tooth form engagement of adjacent corrugations roller, due to the engagement type roll body of this kind of tooth form both ends with
Leak occurs between mainframe box tank wall, therefore, the disc structure of end is additionally set at the leak position, such as Fig. 5 and Fig. 6 institutes
Show, the disk of end and the main distinction of plain disk are that section of its end along position is half tooth form, for the heavy platform of annular and
Ring-like erecting bed, it can be provided with or without as the case may be.In Fig. 2 two corrugation rolls, corrugation rolls above are complete
Portion uses common disc structure, and the middle part of underlying corrugation rolls uses common disk, and only two end uses end
The disc structure in portion, left end use for the disk shown in Fig. 5, right-hand member use for the disk shown in Fig. 6.
Referring to the drawings, the bottom of mainframe box discharging opening 5 is installed with the discharging bottom plate 7 being obliquely installed, discharging bottom plate 7
Top be hinged with can rotation up and down regulation pressing plate 8, regulation pressing plate 8 is obliquely installed and is provided with use on the mainframe box 1 above it
In the flexible pressurizing mechanism for adjusting its angle of inclination.Regulation pressing plate 8 cooperatively forms the size of mainframe box discharging opening 5 with discharging bottom plate 7
Governor motion, by flexible pressurizing mechanism, the extruding for adjusting pressing plate 8 and the rear portion of service aisle 6 takes off liquid zone and coordinated, jointly to thing
Material is extruded, so as to can further improve de- liquid enrichment effect, meanwhile, pass through the adjustment energy to regulation pressing plate 8 angle of inclination
Realize the flexible modulation to discharge concentration.
Reference picture 7, for flexible pressurizing mechanism, it includes sleeve that is vertically arranged and being fixedly mounted on mainframe box tank wall
9, the interior lower end of sleeve 9 is slidably fitted with the pressure head 10 of the extended bottom of sleeve 9, and the bottom of pressure head 10 is resisted against regulation pressing plate
On 8 top surface, the inner upper end of sleeve 9 is slidably fitted with sliding block 11, and the middle part of sliding block 11 offers tapped through hole, mainframe box tank wall
On vertically arranged regulating bolt 12 is rotatablely equipped with the surface of sleeve 9, the screw rod of regulating bolt 12 is stretched into sleeve 9 simultaneously
It is screwed onto in above-mentioned tapped through hole, compression spring 13 is connected between the lower end of sliding block 11 and the upper end of pressure head 12.In the structure, lead to
Cross spanner etc. and rotate regulating bolt 12, the height of sliding block 11 can be adjusted, so as to the elastic shape of adjustable compression spring 13
Variable, and then the pressure size of pressure head 10 is adjusted, the angle for adjusting pressing plate 8 is adjusted.Using the flexibility of compressed spring type
The structure of pressure head 10 so that regulation pressing plate 8 has certain flexible buffer amount, effectively slurry can be avoided to block while extruding.
Referring to the drawings, filtrate machine also includes agitator tank 14, the inside of agitator tank 14 installation filter cylinder 15, on the barrel of filter cylinder 15
Cloth filter opening or filter seam, the bottom of agitator tank 14 opens up agitator tank filtrate (liquid 26, is provided with filter cylinder 15 and is driven by stirring motor 16
Dynamic stirring vane 17；The top of the wherein side wall of filter cylinder 15 offers the filter cylinder discharging opening 18 connected with mainframe box charging aperture 4.
Stirring vane 17 is set in filter cylinder 15, can be uniform by slurry agitation, effectively avoid material from depositing.Filter hole or filter are set on filter cylinder 15
Seam, filtrate can be flowed out from filter opening or filter seam, and finally be discharged from agitator tank filtrate (liquid 26, and therefore, agitator tank 14 also has concurrently
Pre-filtered function.
Referring to the drawings, the front portion of filter cylinder 15 sets gradually blending bin 19 and material feeding box 20, the bottom of blending bin 19 and filter cylinder
15 bottom connection, the top of blending bin 19 connect with the top of material feeding box 20, and the bottom of material feeding box 20 opens up material inlet 21.
Slurry for needing dosing, the dosing in blending bin 19, the slurry after dosing flows into the bottom of filter cylinder 15, by filter cylinder 15
Stirring vane 17 can be uniform by medicine and slurry agitation.
Referring to the drawings, separated between blending bin 19 and material feeding box 20 by dividing plate 22, the top of dividing plate 22 sets and can connected
The V-arrangement opening on two tanks top, being slidably fitted with dividing plate 22 can so as to form flow for adjusting the baffle plate 23 of openings of sizes
The metering weir of tune.The size of V openings is adjusted by baffle plate 23, so as to carry out spirit to the inventory flowed into blending bin
Adjustment living.By the characteristics of bottom rate of V-arrangement opening is small, top flux is big so that Flow-rate adjustment is more stable more reliable.Charging
The middle part of case 20 is provided with overflow pipe 24, and the bottom of overflow pipe 24 passes the bottom wall of material feeding box 20 and forms overflow outlet 25, overflows
The opening position that the top of flow tube 24 extends upwardly to close to the top of material feeding box 20 is ended.Overflow pipe 24 coordinates to charging with metering weir
Amount is adjusted, and so as to control appropriate material to enter blending bin 19, unnecessary material then flows out from overflow pipe 24 and returns to confession
Feed bin.
For the actuating unit of corrugation rolls, a set of dynamical system can be used or use a set of dynamical system per several rollers.
Dynamical system includes frequency-conversion and speed-regulation motor and reducer with big speed ratio, and wherein transmission system can use gear, and be moistened using oil sump
Sliding sealing protection cover.The rotating speed of corrugation rolls can according to yield, material variety from water-based, input concentration and discharge concentration will
Ask and be adjusted, the rotating speed of each corrugation rolls can be synchronized, can also successively decrease or progressively increase from being fed to discharging as needed, realize section
Can consumption reduction.
In summary, the utility model is not limited to above-mentioned embodiment.Those skilled in the art, this reality is not being departed from
On the premise of with new spirit and scope, some change or modification can be done.Above-mentioned change or modification each fall within book practicality
New protection domain.
Claims (8)
1. a kind of disc stack multiple roll filtrate machine, including mainframe box（1）, mainframe box（1）Bottom open up mainframe box filtrate (liquid（2）,
It is characterized in that the mainframe box（1）Middle part be arranged at intervals upper roller group and lower roller group, each roller group and include multiple rotational installations
The corrugation rolls driven on mainframe box tank wall and by actuating unit（3）, each corrugation rolls in each roller group（3）It is parallel and tight successively
Adjacent and curvilinear arrangement；Mainframe box（1）Anterior mainframe box charging aperture is set（4）, rear portion sets mainframe box discharging opening（5）,
Space between two roller groups forms linking mainframe box charging aperture（4）With mainframe box discharging opening（5）Service aisle（6）, work
Passage（6）From its feed end to its discharge end in the curve-like and service aisle risen after falling before（6）From its feed end to its
Discharge end is gradually reduced.
2. disc stack multiple roll filtrate machine as claimed in claim 1, it is characterized in that the corrugation rolls（3）Including roll shaft（31）And suit
In roll shaft（31）On multiple disks（32）, each disk（32）In roll shaft（31）Middle part stack successively and set and form corrugation rolls
Roll body, corrugation rolls（3）Upper adjacent two disk（32）Between be provided for the annulus of filtrate（33）, it is adjacent in each roller group
Corrugation rolls（3）On disk end along close to position it is staggered and two end faces of each corrugation rolls roll body correspond to concordantly set respectively
Put.
3. disc stack multiple roll filtrate machine as claimed in claim 1 or 2, it is characterized in that the mainframe box discharging opening（5）Bottom consolidate
Dingan County is equipped with the discharging bottom plate being obliquely installed（7）, discharge bottom plate（7）Top be hinged with can rotation up and down regulation pressing plate（8）,
Adjust pressing plate（8）It is obliquely installed and the mainframe box above it（1）On flexible pressurizing machine for adjusting its angle of inclination is installed
Structure.
4. disc stack multiple roll filtrate machine as claimed in claim 3, it is characterized in that the flexible pressurizing mechanism include it is vertically arranged and
The sleeve being fixedly mounted on mainframe box tank wall（9）, sleeve（9）Interior lower end be slidably fitted with extended sleeve（9）Bottom
Pressure head（10）, pressure head（10）Bottom be resisted against regulation pressing plate（8）Top surface on, sleeve（9）Inner upper end be slidably installed
There is sliding block（11）, sliding block（11）Middle part offers tapped through hole, in sleeve on mainframe box tank wall（9）Surface be rotatablely equipped with
Vertically arranged regulating bolt（12）, regulating bolt（12）Screw rod stretch into sleeve（9）It is interior and be screwed onto in above-mentioned tapped through hole,
Sliding block（11）Lower end and pressure head upper end between connect compression spring（13）.
5. disc stack multiple roll filtrate machine as claimed in claim 1, it is characterized in that the filtrate machine also includes agitator tank（14）, stirring
Case（14）Inside installation filter cylinder（15）, filter cylinder（15）Barrel on uniform filter opening or filter seam, agitator tank（14）Bottom open up and stir
Mix case filtrate (liquid（26）, filter cylinder（15）Inside it is provided with by stirring motor（16）The stirring vane of driving（17）, filter cylinder（15）Its
In the top of a side wall offer and mainframe box charging aperture（4）The filter cylinder discharging opening of connection（18）.
6. disc stack multiple roll filtrate machine as claimed in claim 5, it is characterized in that the filter cylinder（15）Front portion set gradually mixing
Case（19）And material feeding box（20）, blending bin（19）Bottom and filter cylinder（15）Bottom connection, blending bin（19）Top with entering
Hopper（20）Top connection, material feeding box（20）Bottom open up material inlet（21）.
7. disc stack multiple roll filtrate machine as claimed in claim 6, it is characterized in that the blending bin（19）And material feeding box（20）Between
Pass through dividing plate（22）Separate, dividing plate（22）Top set and can connect the V-arrangement opening on two tanks top, dividing plate（22）It is upper to slide peace
Equipped with the baffle plate for adjusting openings of sizes（23）So as to form the adjustable metering weir of flow.
8. disc stack multiple roll filtrate machine as claimed in claim 7, it is characterized in that the material feeding box（20）Middle part overflow is installed
Pipe（24）, overflow pipe（24）Bottom pass material feeding box（20）Bottom wall and formed overflow outlet（25）, overflow pipe（24）Top
End is extended upwardly to close to material feeding box（20）The opening position cut-off on top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720713731.XU CN206843849U (en) | 2017-06-20 | 2017-06-20 | Disc stack multiple roll filtrate machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720713731.XU CN206843849U (en) | 2017-06-20 | 2017-06-20 | Disc stack multiple roll filtrate machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206843849U true CN206843849U (en) | 2018-01-05 |
Family
ID=60800984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720713731.XU Active CN206843849U (en) | 2017-06-20 | 2017-06-20 | Disc stack multiple roll filtrate machine |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107419580A (en) * | 2017-06-20 | 2017-12-01 | 郭鹏 | Disc stack multiple roll filtrate machine |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107419580A (en) * | 2017-06-20 | 2017-12-01 | 郭鹏 | Disc stack multiple roll filtrate machine |
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Effective date of registration: 20180725 Address after: 261011 Weicheng District, Weifang City, Shandong Province, No. 289 Patentee after: Weifang Shanshui environmental protection machinery manufacturing Co., Ltd. Address before: 261011 Weifang road environmental protection machinery manufacturing Co., Ltd. 289, CO Jian Road, Weicheng District, Weifang, Shandong Patentee before: Guo Peng |