CN207405061U - A kind of vertical sludge filter press - Google Patents
A kind of vertical sludge filter press Download PDFInfo
- Publication number
- CN207405061U CN207405061U CN201721310203.6U CN201721310203U CN207405061U CN 207405061 U CN207405061 U CN 207405061U CN 201721310203 U CN201721310203 U CN 201721310203U CN 207405061 U CN207405061 U CN 207405061U
- Authority
- CN
- China
- Prior art keywords
- partition
- babinet
- filter press
- deflector hole
- filter core
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a kind of vertical sludge filter presses, the inside of babinet is arranged at intervals with first partition and second partition, babinet is divided into three parts by first partition and second partition, respectively operating room, filter chamber and storage room, the inner surface of operating room is provided with hydraulic cylinder, the output terminal of hydraulic cylinder is provided with filter press plate, deflector hole is offered on the outer surface of first partition, the inner ring of deflector hole is provided with strainer, the bottom of deflector hole is provided with Coalescence filter core, and the bottom of second partition is arranged to storage room；This vertical sludge filter press, medium completes unidirectional delivery in box house, conductivity higher, Coalescence filter core separates the water of emulsified state from medium, and larger water droplet is gathered into, multigroup Coalescence filter core while draws water accelerate filter efficiency while filtering accuracy is maintained, improve work efficiency, it realizes that water resource recycles, controls production cost.
Description
Technical field
The utility model is related to treating sludge technical fields, are specially a kind of vertical sludge filter press.
Background technology
With the waste water that the progress in epoch and the development of economic society, people generate, the more and more waste water controls of sewage are
So become a social problem, in existing sewage disposal process, generally require and settle the discarded object in sewage
And it is made to be changed into sludge, and sludge filter press is then to apply the machinery that mechanical force realizes filtering in filter medium one side, mainly
For the separation of solid and liquid of sludge, industrial sludge dehydration is mostly used for, is the ideal equipment of environmental improvement and resource reclaim, it can also
Process is leached applied to the separation of solid and liquid in industrial production or liquid, is used widely at home in environment-friendly engineering project, it is dirty
It needs to go water process to sludge progress desiccation in mud processing, can so reduce the water content in sludge, be follow-up Treatment of Sludge
It offers convenience, the effects that sludge drying is by diafiltration or evaporation removes the process of most of water content, it will usually make from sludge
It uses sludge filter press and carries out compacting dehydration, in order to cater to the theory of sustainable development in today's society, how to improve resource profit
With rate and work efficiency, control production cost is the main problem that current enterprise faces, and in existing filtering equipment, operation is multiple
Miscellaneous, equipment investment is big, and production cost is excessively high, is unfavorable for sustainable development.
Utility model content
The purpose of this utility model is to provide a kind of vertical sludge filter presses, possess work efficiency height, medium flow field communication
The characteristics of fast, solves the problems of the prior art.
To achieve the above object, the utility model provides following technical solution：A kind of vertical sludge filter press, including case
Body, the outer surface of the babinet offer feed inlet and discharge port respectively, and feed inlet is arranged on case with the non-contour opposition of discharge port
The both sides of body, the bottom of the discharge port are provided with water outlet, end are both provided at the port of water outlet, feed inlet and discharge port
Lid, the end cap uniformly engage respectively with water outlet, feed inlet with discharge port, and the inside of the babinet is also arranged at intervals with first
Partition plate and second partition, first partition and second partition babinet inner horizontal set, the first partition and second every
Babinet is divided into three parts by plate, is respectively operating room, filter chamber and storage room；
The inner surface of the operating room is provided with hydraulic cylinder, and hydraulic cylinder is fixedly mounted on the top of operating room, the hydraulic pressure
The output terminal of cylinder is provided with filter press plate, and the outer ring of filter press plate and the inner wall of babinet are seamless applying, and the bottom of operating room is provided with
One partition plate offers deflector hole on the outer surface of the first partition, and deflector hole is uniformly arranged in the plate face of first partition, led
The inner ring of discharge orifice is provided with strainer, and the outer ring of the strainer is chimeric with the inner wall fixation of deflector hole, and the bottom of deflector hole is provided with
Coalescence filter core, Coalescence filter core are vertically arranged between first partition and second partition, and the bottom of the second partition is arranged to store up
Room is deposited, the outer surface of storage room, which corresponds to, offers water outlet.
Preferably, the inner wall of the embedded babinet in the outer ring of the first partition and second partition, first partition, second partition
It is handled with babinet junction via sealing technology.
Preferably, the output terminal of the hydraulic cylinder fixes welding straight down and with the one side of filter press plate.
Preferably, the Coalescence filter core is equidistantly arranged at intervals simultaneously circular array form in the plate face of second partition.
Preferably, the bottom of the Coalescence filter core is chimeric with second partition fixation, the top of Coalescence filter core and first partition
Bottom surface abut.
Compared with prior art, the beneficial effects of the utility model are as follows：
This vertical sludge filter press, box house each area is mutually isolated, seals against each other, and does not generate association, and then really
Material controllability higher in operation is protected, medium completes unidirectional delivery, conductivity higher, Water Transport in box house
More accurate, sludge is completed to squeeze in operating room, and internal moisture stress departs from and penetrates deflector hole conducts to filter chamber, and again
It is secondary to be conducted and finally in storage room centralized collection, Coalescence filter core the operation is stable, structure to storage room under the action of Coalescence filter core
Intensity is high, has water-wet behavior, it can not only filter out the mechanical admixture in medium, and can also make emulsification by being demulsified, coalescing
The water of state is separated from medium, and gathers into larger water droplet, in favor of further realizing the conduction of medium, Duo Zuju
Filter core draws water simultaneously is tied, accelerates filter efficiency while filtering accuracy is maintained, improve work efficiency, and extract sludge
In moisture, realize resource circulation utilization, control production cost.
Description of the drawings
Fig. 1 is the overall structure figure of the utility model.
Fig. 2 is that the local of the utility model splits design sketch.
Fig. 3 is the second partition top view of the utility model.
In figure：1 babinet, 11 feed inlets, 12 discharge ports, 13 water outlets, 14 end caps, 15 operating rooms, 16 filter chambers, 17 storages
Room, 2 first partitions, 21 deflector holes, 22 strainers, 23 Coalescence filter cores, 3 second partitions, 4 hydraulic cylinders, 41 filter press plates.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
- 3 are please referred to Fig.1, a kind of vertical sludge filter press, including babinet 1, the outer surface of babinet 1 offers charging respectively
Mouth 11 and discharge port 12, feed inlet 11 are arranged on the both sides of babinet 1 with non-contour oppose of discharge port 12, and feed inlet 11 is arranged on behaviour
Make edge on the outside of room 15, discharge port 12 is arranged on the outside lower edge of operating room 15, and sludge is inputted by feed inlet 11, by discharge port
12 outputs, the bottom of discharge port 12 are provided with water outlet 13, and water outlet 13, feed inlet 11 at the port of discharge port 12 with being respectively provided with
There is end cap 14, closed end cap 14 can ensure that babinet 1 is relatively closed, and maintain metastable working condition, and sludge is avoided to exist
Jump out babinet 1 during extruding, improve security during single unit system work, end cap 14 respectively with water outlet 13, feed inlet
11 uniformly engage with discharge port 12, and the inside of babinet 1 is also arranged at intervals with first partition 2 and second partition 3,2 He of first partition
Second partition 3 is set in the inner horizontal of babinet 1, and babinet 1 is divided into three parts by first partition 2 and second partition 3, point
Not Wei operating room 15, filter chamber 16 and storage room 17, the inner wall of the embedded babinet 1 in outer ring of first partition 2 and second partition 3,
First partition 2, second partition 3 are handled with 1 junction of babinet via sealing technology, and 1 inside each area of babinet is mutually isolated, phase
Mutually sealing, does not generate association, and then ensures material controllability higher in operation, and medium is completed unidirectionally inside babinet 1
It transfers, conductivity higher, Water Transport is also more accurate, and sludge is completed to squeeze in operating room 15, and internal moisture stress departs from
And conducted through deflector hole 21 to filter chamber 16, and conduct to storage room 17 under the action of Coalescence filter core 23 and finally exist again
17 centralized collection of storage room.
The inner surface of operating room 15 is provided with hydraulic cylinder 4, and hydraulic cylinder 4 is fixedly mounted on the top of operating room 15, hydraulic cylinder 4
Output terminal fix straight down and with the one side of filter press plate 41 and weld, hydraulic cylinder 4 works and drives filter press plate 41 at the uniform velocity downwards
Transmission, and complete to squeeze for sludge, the output terminal of hydraulic cylinder 4 is provided with filter press plate 41, outer ring and the babinet 1 of filter press plate 41
Inner wall is seamless applying, and the bottom of operating room 15 is provided with first partition 2, and deflector hole 21 is offered on the outer surface of first partition 2,
Deflector hole 21 is uniformly arranged in the plate face of first partition 2, and the inner ring of deflector hole 21 is provided with strainer 22, and strainer 22 is completed tentatively
Filtering, and the larger impurity of volume is obstructed, it is allowed to rest on inside operating room 15, the outer ring of strainer 22 and the inner wall of deflector hole 21
Fixed chimeric, the bottom of deflector hole 21 is provided with Coalescence filter core 23, and the bottom of Coalescence filter core 23 is chimeric with the fixation of second partition 3,
The top of Coalescence filter core 23 and the bottom surface of first partition 2 abut that constraint coalescence is filtered jointly for first partition 2 and second partition 3
Core 23 so that Coalescence filter core 23 is in opposing stationary working condition, and Coalescence filter core 23 selects glass fibre, structural strength
Height, which can effectively play filtration, better, and Coalescence filter core 23 has water-wet behavior, it can not only be filtered out
Mechanical admixture in medium, and the water of emulsified state can also be made to be separated from medium, and coalesced by being demulsified, coalescing
For larger water droplet, in favor of further realizing the conduction of medium, the equi-spaced apart in the plate face of second partition 3 of Coalescence filter core 23
Simultaneously circular array form, multigroup Coalescence filter core 23 while draws water are set, accelerate filtering while filtering accuracy is maintained
Efficiency improves work efficiency, and extracts the moisture in sludge, realizes resource circulation utilization, controls production cost, Coalescence filter core
23 are vertically arranged between first partition 2 and second partition 3, and the bottom of second partition 3 is arranged to storage room 17, storage room 17
Outer surface corresponds to and offers water outlet 13.
In summary：This vertical sludge filter press, 1 inside each area of babinet is mutually isolated, seals against each other, and does not generate pass
Connection, and then ensures material controllability higher in operation, and medium completes unidirectional delivery inside babinet 1, conductivity higher,
Water Transport is also more accurate, sludge operating room 15 complete squeeze, internal moisture stress depart from and penetrate deflector hole 21 to
Filter chamber 16 is conducted, and is conducted to storage room 17 under the action of Coalescence filter core 23 and finally concentrated in storage room 17 again and received
Collection, 23 the operation is stable of Coalescence filter core, structural strength is high, has water-wet behavior, it can not only filter out the mechanical admixture in medium, and
And the water of emulsified state can also be made to be separated from medium by being demulsified, coalesce, and larger water droplet is gathered into, in favor of
It further realizes the conduction of medium, multigroup Coalescence filter core 23 while draws water, accelerates filtering while filtering accuracy is maintained
Efficiency improves work efficiency, and extracts the moisture in sludge, realizes resource circulation utilization, controls production cost.
While there has been shown and described that the embodiment of the utility model, for the ordinary skill in the art,
It is appreciated that in the case where not departing from the principle of the utility model and spirit can these embodiments be carried out with a variety of variations, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (5)
1. a kind of vertical sludge filter press, including babinet（1）, it is characterised in that：The babinet（1）Outer surface offer respectively
Feed inlet（11）With discharge port（12）, feed inlet（11）With discharge port（12）Non- contour opposition is arranged on babinet（1）Both sides, institute
State discharge port（12）Bottom be provided with water outlet（13）, water outlet（13）, feed inlet（11）With discharge port（12）Port at
It is both provided with end cap（14）, the end cap（14）Respectively with water outlet（13）, feed inlet（11）With discharge port（12）Uniformly engaging,
The babinet（1）Inside be also arranged at intervals with first partition（2）And second partition（3）, first partition（2）And second partition
（3）In babinet（1）Inner horizontal set, the first partition（2）And second partition（3）By babinet（1）It is divided into three
Part is respectively operating room（15）, filter chamber（16）And storage room（17）；
The operating room（15）Inner surface be provided with hydraulic cylinder（4）, hydraulic cylinder（4）It is fixedly mounted on operating room（15）Top
Portion, the hydraulic cylinder（4）Output terminal be provided with filter press plate（41）, filter press plate（41）Outer ring and babinet（1）Interior wall seamless
Fitting, operating room（15）Bottom be provided with first partition（2）, the first partition（2）Outer surface on offer deflector hole
（21）, deflector hole（21）In first partition（2）Plate face on uniformly arrange, deflector hole（21）Inner ring be provided with strainer（22）,
The strainer（22）Outer ring and deflector hole（21）Inner wall fix chimeric, deflector hole（21）Bottom be provided with Coalescence filter core
（23）, Coalescence filter core（23）In first partition（2）And second partition（3）Between be vertically arranged, the second partition（3）Bottom
It is arranged to storage room（17）, storage room（17）Outer surface correspond to offer water outlet（13）.
2. a kind of vertical sludge filter press according to claim 1, it is characterised in that：The first partition（2）With second
Partition plate（3）The embedded babinet in outer ring（1）Inner wall, first partition（2）, second partition（3）With babinet（1）Junction is via close
Seal process.
3. a kind of vertical sludge filter press according to claim 1, it is characterised in that：The hydraulic cylinder（4）Output terminal
Straight down and and filter press plate（41）One side fix welding.
4. a kind of vertical sludge filter press according to claim 1, it is characterised in that：The Coalescence filter core（23）Second
Partition plate（3）Plate face on equidistantly be arranged at intervals and circular array form.
5. a kind of vertical sludge filter press according to claim 1, it is characterised in that：The Coalescence filter core（23）Bottom
With second partition（3）It is fixed chimeric, Coalescence filter core（23）Top and first partition（2）Bottom surface abut.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721310203.6U CN207405061U (en) | 2017-10-11 | 2017-10-11 | A kind of vertical sludge filter press |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721310203.6U CN207405061U (en) | 2017-10-11 | 2017-10-11 | A kind of vertical sludge filter press |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207405061U true CN207405061U (en) | 2018-05-25 |
Family
ID=62319535
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721310203.6U Expired - Fee Related CN207405061U (en) | 2017-10-11 | 2017-10-11 | A kind of vertical sludge filter press |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207405061U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109701992A (en) * | 2018-12-28 | 2019-05-03 | 合肥森特环境工程有限公司 | A kind of pure physics and efficient solid waste dehydration device and its application method |
| CN115259616A (en) * | 2022-08-04 | 2022-11-01 | 李欣 | Sump oil sludge treatment equipment based on granulation dehydration and use method thereof |
-
2017
- 2017-10-11 CN CN201721310203.6U patent/CN207405061U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109701992A (en) * | 2018-12-28 | 2019-05-03 | 合肥森特环境工程有限公司 | A kind of pure physics and efficient solid waste dehydration device and its application method |
| CN115259616A (en) * | 2022-08-04 | 2022-11-01 | 李欣 | Sump oil sludge treatment equipment based on granulation dehydration and use method thereof |
| CN115259616B (en) * | 2022-08-04 | 2023-08-08 | 大庆腾辉石油工程技术服务有限公司 | Dirty oil sludge treatment equipment based on granulation dehydration and use method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180525 Termination date: 20191011 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |