CN207445701U - A kind of diaphragm filter press - Google Patents
A kind of diaphragm filter press Download PDFInfo
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- CN207445701U CN207445701U CN201721380210.3U CN201721380210U CN207445701U CN 207445701 U CN207445701 U CN 207445701U CN 201721380210 U CN201721380210 U CN 201721380210U CN 207445701 U CN207445701 U CN 207445701U
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Abstract
The utility model provides a kind of diaphragm filter press, it is related to sterol filter plant technical field, including rack, diaphragm filtering plate components, thrust plate, pressure strip, the driving device being arranged on the outside of pressure strip, air supply pipe, air supply pipe is equipped with several branch pipes being connected with diaphragm filtering plate components, and diaphragm filtering plate components are respectively equipped with inlet tube and outlet tube.Diaphragm filter press provided by the utility model, effect is inflated to membrane by using to the form that diaphragm filtering plate components are directly supplied, and then the filter cake between compression membrane filter plate is expanded by membrane, achieve the purpose that further separation of solid and liquid, service life is shortened, reduces energy consumption, while the filter cloth monomer of the closing outside filter plate can effectively carry out the sealing between filter plate, the phenomenon of leakage generated in traditional filtering processes is avoided, there is good using effect and extensive promotional value.
Description
Technical field
The utility model belongs to sterol filter plant technical field, is to be related to a kind of diaphragm filter press more specifically.
Background technology
Natural phytosterin is using soyabean deodorization distillate during natural VE is produced, and esterifying liquid is through cold
Analysis, crystallization, separation, washing, dissolving, recrystallization, separation, drying obtain sterol sterling, during sterol refines, sterol
Filtering link it is most important to the production operation of sterol.Earliest filter type is that the liquids containing sterol are used tripodia
The filter plants such as formula centrifuge, filtering earthenware, bag filter carry out its separation of solid and liquid.These equipment all there are it is fatal the shortcomings that:
Filter area is small, and efficiency is low, inconvenient, and labor intensity is big, severe operational environment, inefficiency.Van-type press filtration is selected later
Machine is filtered, and is greatly improved to problem above, this is a much progress of the sector.But the problem of following
Mainly the sealing of chamber-type press filter mainly seals, this sealing side by the filter cloth between filter plate and the mechanical pressure of filter plate
Formula is with the extension of usage time, and the obturation effect between filter cloth and filter plate is bad, and in filtering, pressure is slightly larger or purging is too quickly, filter
The phenomenon of leakage will be generated between plate, causes loss of material and environmental pollution, great inconvenience is brought to production operation；Secondly,
The Purge methods of chamber type filter are that purge gas is directed through inside material, by purge gas by the Liquid Residue between sterol crystals
Body is taken out of, and since filter plate is more, this Purge methods gas easily forms short circuit, causes purging uneven, and purge time extends, and
And purge gas also has very big waste, not only smell is big for gas band damage material, will also result in material and solvent loss.
Utility model content
The purpose of this utility model is to provide a kind of diaphragm filter press, are filtered with solving sterol in the prior art
The technical issues of air demand is big in equipment filter process, filter efficiency is low.
To achieve the above object, the technical solution adopted in the utility model is：A kind of diaphragm filter press is provided, including machine
Frame, both sides are set up in the diaphragm filtering plate components being slidably matched above two crossbeams of the rack and with the crossbeam, consolidate respectively
Surely be arranged at described rack one end and parallel to the diaphragm filtering plate components set thrust plate, be arranged at the rack other end
For the diaphragm filtering plate components to be made to be filled to the pressure strip of one side compression of thrust plate, the driving that is connected with the pressure strip
It puts, is equipped with below the rack parallel to the crossbeam and for the air supply pipe to diaphragm filtering plate components supply, the confession
Tracheae is equipped with several branch pipes being connected with the diaphragm filtering plate components, is respectively equipped on the outside of the diaphragm filtering plate components
For the inlet tube for making the liquid to be filtered entrance and for making the outlet tube that the filtrate after filtering is discharged.
As further optimization, diaphragm filtering plate components include several perpendicular to the crossbeam and the membrane of laid out in parallel
Filter plate, the both sides plate face of the membrane filter plate are equipped with to be passed through the cavity of liquid to be filtered, and the inner surface of the cavity is equipped with
Evenly arranged protrusion, formed between the protrusion to make filtrate by diversion trench, the center of the cavity is equipped with and is used for
The inlet opening of liquid to be filtered is passed through, the outer surface of the cavity is equipped with membrane, and the plate face four corners of the membrane filter plate, which are equipped with, to be used
In the fluid hole for discharging filtrate, the diversion trench is led to the fluid hole inside the plate body of the membrane filter plate by water conservancy diversion
Road connects.
As further optimization, the inlet opening of the membrane filter plate adjacent with the thrust plate is connected with the inlet tube,
The fluid hole of the membrane filter plate adjacent with the thrust plate is connected with the outlet tube.
As further optimization, protrusion includes the basis protrusion for forming the diversion trench and is used to support described
The support protrusion of membrane, the support protrusion are arranged at the periphery of the inlet opening and are uniformly placed with several.
As further optimization, support protrusion is protruded outward in the basis protrusion.
As further optimization, the area of support protrusion is more than the area of the basis protrusion.
As further optimization, the interface being connected with the branch pipe, the interface are equipped with below the side of membrane filter plate
It is connected by the plenum duct inside the cavity with the inner surface of the cavity.
As further optimization, the side of membrane filter plate is equipped with to be set up in the hangers of the crossbeam, the crossbeam
Side is equipped with to pull the drag hook component of the hangers, and the drag hook component includes setting parallel to the crossbeam length direction
Guide rail and be slidably matched with the guide rail and for pulling the drag hook of the hangers.
As further optimization, thickness of the hangers on the crossbeam length direction is less than the thickness of the membrane filter plate
Degree.
As further optimization, branch pipe is rubber hose.
The advantageous effect of diaphragm filter press provided by the utility model is：Diaphragm filter press provided by the utility model,
Effect is inflated to membrane by using to the form that diaphragm filtering plate components are directly supplied, and then passes through membrane turgor pressure
Liquid in filter cake is extruded, achievees the purpose that further separation of solid and liquid, each filter plate individually supplies by the filter cake between contracting membrane filter plate
The mode of gas greatly reduces filter cake air-loss in extrusion process, and gas consumption reduces, and shortens service life, reduces energy
Consumption, while the filter cloth monomer of the closing outside filter plate can effectively carry out the sealing between filter plate, avoid producing in traditional filtering processes
The raw phenomenon of leakage has good using effect and extensive promotional value.
Description of the drawings
It, below will be to embodiment or the prior art in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
Attached drawing is briefly described needed in description, it should be apparent that, the accompanying drawings in the following description is only that this practicality is new
Some embodiments of type, for those of ordinary skill in the art, without having to pay creative labor, can be with
Other attached drawings are obtained according to these attached drawings.
Fig. 1 is a kind of structure diagram for diaphragm filter press that the utility model embodiment provides；
Fig. 2 is the schematic cross-sectional view of A-A in the utility model embodiment Fig. 1；
Fig. 3 is the schematic cross-sectional view that the turnover of B-B in the utility model embodiment Fig. 2 is cutd open；
Fig. 4 is in the utility model embodiment Fig. 3 I partial enlargement structural representation.
Wherein, each reference numeral in figure：
100- diaphragm filtering plate components；110- membrane filter plates；111- inlet openings；112- fluid holes；113- protrusions；114- bases
Protrusion；115- support protrusions；116- flow-guiding channels；120- membranes；130- inlet tubes；140- outlet tubes；150- hangers；160- is drawn
Hook assembly；161- guide rails；162- drag hooks；200- thrust plates；300- pressure strips；400- driving devices；510- air supply pipes；520- branch
Pipe；530th, plenum duct.
Specific embodiment
In order to which technical problem to be solved in the utility model, technical solution and advantageous effect is more clearly understood, with
Lower combination accompanying drawings and embodiments, are further elaborated the utility model.It should be appreciated that specific reality described herein
It applies example to be only used to explain the utility model, is not used to limit the utility model.
It should be noted that when element is referred to as " being fixed on " or " being arranged at " another element, it can be directly another
On one element or it is connected on another element.When an element is known as " being connected to " another element, it can
To be directly to another element or be indirectly connected on another element.
It is to be appreciated that term " length ", " width ", " on ", " under ", "front", "rear", "left", "right", " vertical ",
The orientation or position relationship of the instructions such as " level ", " top ", " bottom " " interior ", " outer " are to be closed based on orientation shown in the drawings or position
System is for only for ease of description the utility model and simplifies description rather than instruction or imply that signified device or element are necessary
With specific orientation, with specific azimuth configuration and operation, therefore it is not intended that limitation to the utility model.
In addition, term " first ", " second " are only used for description purpose, and it is not intended that instruction or hint relative importance
Or the implicit quantity for indicating indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include one or more this feature.In the description of the utility model, " multiple " are meant that two or two
More than, unless otherwise specifically defined.
Also referring to Fig. 1 and Fig. 4, now diaphragm filter press provided by the utility model is illustrated.Diaphragm filter press,
It is set up in the diaphragm filtering plate components 100 being slidably matched above two crossbeams of rack and with crossbeam respectively including rack, both sides, consolidates
Surely the thrust plate 200 that is arranged at rack one end and is set parallel to diaphragm filtering plate components 100 is arranged at the rack other end for making
Pressure strip 300 of the diaphragm filtering plate components 100 to 200 1 side compression of thrust plate, the driving device 400 that is connected with pressure strip 300, machine
It is equipped with below frame parallel to crossbeam and for the air supply pipe 510 to the supply of diaphragm filtering plate components 100, if air supply pipe 510 is equipped with
The dry branch pipe 520 being connected with diaphragm filtering plate components 100, the outside of diaphragm filtering plate components 100, which is respectively provided with, to be made to treat
The inlet tube 130 that filtrate enters and the outlet tube 140 for discharging the filtrate after filtering.Carrying out the filter process of sterol
In, driving device 400 drives pressure strip 300 to wait to be pressed to setting position to 200 1 side compression diaphragm filtering plate components 100 of thrust plate
It postpones, the liquid to be filtered being sent into from inlet tube 130, and sequentially passes through the diaphragm filtering plate components 100 arranged along crossbeam direction, pass through
Filtrate is discharged through outlet tube 140 outside diaphragm filtering plate components 100 after diaphragm filtering plate components 100 filter, and then pressure strip 300 is to driving
400 one side of device is moved, and is opened diaphragm filtering plate components 100 and is made its internal separation, realizes the removing of filter residue.What is be filtered
In the process, by air supply pipe 510 and branch pipe 520 to being inflated inside diaphragm filtering plate components 100, realize to by filter residue boil down to
The effect of filter cake is inflated the diaphragm filtering plate components 100 using individual loading line, avoids tradition and borrows outlet tube
140 be inflated caused by gas leak, effectively raise filter cake compression efficiency, saved energy loss.
A kind of diaphragm filter press provided by the utility model, compared with prior art, membrane pressure provided by the utility model
Filter is inflated effect to membrane by using to the form that diaphragm filtering plate components are directly supplied, and then passes through membrane
Filter cake between expansion compression membrane filter plate, the liquid in filter cake is extruded, achievees the purpose that further separation of solid and liquid, each filter plate
The mode individually supplied greatly reduces filter cake air-loss in extrusion process, and gas consumption reduces, and shortens service life, drops
Low energy consumption, while the filter cloth monomer of the closing outside filter plate can effectively carry out the sealing between filter plate, avoid traditional filtering mistake
The phenomenon of leakage generated in journey, filter effect is more preferable, has good using effect and extensive promotional value.
As further optimization, also referring to Fig. 2 to Fig. 4, as diaphragm filter press provided by the utility model
A kind of specific embodiment, diaphragm filtering plate components 100 include several perpendicular to crossbeam and the membrane filter plate 110 of laid out in parallel,
The both sides plate face of membrane filter plate 110 is equipped with to be passed through the cavity of liquid to be filtered, and the inner surface of cavity is equipped with evenly arranged
Protrusion 113, formed between protrusion 113 to make filtrate by diversion trench, the center of cavity is equipped with to be passed through liquid to be filtered
Inlet opening 111, the outer surface of cavity is equipped with membrane 120, and the plate face four corners of membrane filter plate 110 are equipped with to discharge filtrate
Fluid hole 112, diversion trench connected with fluid hole 112 inside the plate body of membrane filter plate 110 by flow-guiding channel 116.Membrane
Filter plate 110 is provided with several, is arranged on by side frames on front and rear two crossbeams, and can be along cross beam movement, on membrane filter plate 110
The cavity of setting is for accommodating liquid to be filtered, and by the filtering of the membrane 120 set on membrane filter plate 110, material residue stays in two
In the opposite cavity of neighboring separators filter plate 110, filtrate is entered by membrane 120 in diversion trench, and then is led to through flow-guiding channel 116
Then fluid hole 112 is discharged through outlet tube 140, realize filter action process.
As further optimization, also referring to Fig. 1 to Fig. 4, as diaphragm filter press provided by the utility model
A kind of specific embodiment, the inlet opening 111 of the membrane filter plate 110 adjacent with thrust plate 200 are connected with inlet tube 130, with stopping
The fluid hole 112 of the adjacent membrane filter plate 110 of push plate 200 is connected with outlet tube 140.The liquid to be filtered introduced in inlet tube 130
It flow between inlet opening 111 and the membrane 120 of two membrane filter plates 110, then filtrate passes through the membrane 120 of both sides through membrane
Flow-guiding channel 116 inside filter plate 110 converges at fluid hole 112 and discharges, and realizes what liquid to be filtered was filtered through membrane 120
Effect.Fluid hole 112 is arranged at the four corners of membrane filter plate 110, when membrane filter plate 110 is in impaction state, each goes out liquid
It is connected to form one by connecting the discharge for realizing filtrate in filter process with outlet tube 140, to sum up, foring under hole 112
Feed liquor and the circuit for going out liquid, realize the effect effectively filtered in filter process.
As further optimization, also referring to Fig. 2 to Fig. 4, as diaphragm filter press provided by the utility model
A kind of specific embodiment, protrusion 113 include the basis protrusion 114 for forming diversion trench and are used to support membrane 120
Support protrusion 115, support protrusion 115 are arranged at the periphery of inlet opening 111 and are uniformly placed with several.Basic protrusion 114
It sets to form diversion trench, for making to drain into from the flow-guiding channel 116 of membrane filter plate 110 through the filtered filtrate of membrane 120
At outlet tube 140.115 size of opposite support protrusion that basic protrusion 114 is set is smaller, and opposite support protrusion 115 of arranging is close
Some, realize that diversion trench gathers, convenient for the effect of filtrate outflow.Basic protrusion 114 and support protrusion 115 may be employed it is a variety of not
Same shape, such as circle, rectangle, hexagon, triangle, can play same effect.Support protrusion 115 is then filtered in membrane
Several larger protruding points on the surface of plate 110 are provided, the disengaging of filter cake, while the support protrusion 115 are carried out convenient for the later stage
It sets convenient for the feeding of gas in gas replenishment process, convenient for ensureing that process is smoothed out.
As further optimization, also referring to Fig. 2 to Fig. 4, as diaphragm filter press provided by the utility model
A kind of specific embodiment, support protrusion 115 are protruded outward in basic protrusion 114.Support protrusion 115 is in order to embody good branch
Support effect is arranged to protrude outward in the form of basic protrusion 114, ensures good support effect, reduces inflation difficulty, is convenient for
The progress of filter cake compression section.
As further optimization, also referring to Fig. 3 to Fig. 4, as diaphragm filter press provided by the utility model
A kind of specific embodiment, the area of support protrusion 115 are more than the area of basis protrusion 114.Support protrusion 115 rises as main
The part of supporting role, area comparative basis protrusion 114 set it is bigger, convenient for during filter cake compressive charge is carried out, making
Membrane 120 smoothly departs from the position of diversion trench, convenient for being compressed to filter cake.
As further optimization, also referring to Fig. 3 to Fig. 4, as diaphragm filter press provided by the utility model
A kind of specific embodiment, the side lower section of membrane filter plate 110 are equipped with the interface being connected with branch pipe 520, and interface passes through in cavity
The plenum duct 530 in portion is connected with the inner surface of cavity.Interface is arranged on 110 side of membrane filter plate, the effect of branch pipe 520 be by
Gas in air supply pipe 510 is passed through by plenum duct 530 between membrane 120 and membrane filter plate 110, and gas is filled with membrane respectively
Between filter plate 110 and the membrane of its both sides 120, realization is bloated by membrane 120 outward between two neighboring separators 120 of compression
Filter cake effect, in sterol filter process, filtrate is discharged from fluid hole 140, air supply pipe 510, branch pipe 520 and supplies gas at this time
There are gas in passage 530, gas has appropriate compression in the case where filtrate acts on, but not filtrate is caused to flow in air supply pipe 510,
When filter residue reaches it is a certain amount of after, be passed through gas, the filter residue accommodated between two membrane filter plates 110 be compressed into filter cake.
As further optimization, also referring to Fig. 1 to Fig. 4, as diaphragm filter press provided by the utility model
A kind of specific embodiment, the side of membrane filter plate 110 are equipped with to be set up in the hangers 150 of crossbeam, and beam sides, which are equipped with, to be used
In pull hangers 150 drag hook component 160, drag hook component 160 include parallel to crossbeam length direction set guide rail 161 and
It is slidably matched with guide rail 161 and for pulling the drag hook 162 of hangers 150.Drag hook component 160 be used for from both sides simultaneously by it is same every
The hangers 150 of membrane filtration plate 110 is pulled to the different mistakes of 300 one side of 200 one side of thrust plate or pressure strip, corresponding filtering and scarfing cinder
Journey realizes the pulling to two opposite directions.
As further optimization, also referring to Fig. 1 to Fig. 2, as diaphragm filter press provided by the utility model
A kind of specific embodiment, thickness of the hangers 150 on crossbeam length direction are less than the thickness of membrane filter plate 110.Hangers 150 is thick
Degree can make to leave the gap being put into for drag hook 162 between two neighboring hangers 150, realize less than the thickness of membrane filter plate 110
Drag hook is to the drawing effect of hangers 150.162 upper end of drag hook sets coupler body moving up and down, and coupler body moves down in moving process
Avoid with 150 location conflicts of hangers, at the hangers position pulled needed for arrival, then the coupler body for stretching out upper end is carried out to hangers
150 traction action.
As further optimization, also referring to Fig. 1 to Fig. 2, as diaphragm filter press provided by the utility model
A kind of specific embodiment, branch pipe 520 are rubber hose.Branch pipe 520 is mainly used for supplying, and during scarfing cinder adjacent two every
Membrane filtration plate 110 will realize the separation of a determining deviation, so branch pipe 520 needs have certain length, membrane filtration plate 110 be avoided to move
The drawing of branch pipe 520 is caused to be limited in the process, flexible rubber hose can avoid the rigidity drawing in moving process.
Use process：
(1), start driving device 400, it is made to drive pressure strip 300 to 200 1 side compression diaphragm filtering plate components of thrust plate
100；
(2), after setting position is pressed to, from inlet tube 130 be sent into liquid to be filtered, liquid sequentially through several every
Membrane filtration plate 110, into the cavity formed between two adjacent membrane filter plates 110, feed liquor pressure effect under, filtrate penetrate every
Film 120 flow to fluid hole 112 by flow-guiding channel 116 into diversion trench and is discharged through outlet tube 140 outside diaphragm filtering plate components 100；
(3), after a certain amount of filter residue is formed between two adjacent membrane filter plates 110, feed liquor is stopped, then through air supply pipe
510 and the interface of from branch pipe 520 to 110 side of membrane filter plate be passed through gas, membrane 120 is swollen to filter residue one side under aeration
It is swollen, until filter residue, which is squeezed, becomes closely knit filter cake, stop inflation；
(4), starting driving device 400 makes pressure strip 300 be moved to 400 one side of driving device, and drag hook 162 is sequentially by membrane
Filter plate 110 is pulled to 300 one side of pressure strip, and the filter cake between two neighboring membrane filter plate 110 is removed, realizes the clear of filter cake
It removes, so far completes filter operation.
Diaphragm filter press provided by the utility model, by using the form pair directly supplied to diaphragm filtering plate components
Membrane is inflated effect, and then expands the filter cake between compression membrane filter plate by membrane, and the liquid in filter cake is extruded, is reached
The purpose of further separation of solid and liquid, the mode that each filter plate individually supplies make filter cake air-loss in extrusion process subtract significantly
Small, gas consumption reduces, and shortens service life, reduces energy consumption, while the filter cloth monomer of the closing outside filter plate can be effective
The sealing between filter plate is carried out, avoids the phenomenon of leakage generated in traditional filtering processes, with good using effect and widely
Promotional value.
The above is only the preferred embodiments of the present utility model only, is not intended to limit the utility model, all in this practicality
All any modification, equivalent and improvement made within new spirit and principle etc., should be included in the guarantor of the utility model
Within the scope of shield.
Claims (10)
1. a kind of diaphragm filter press, it is characterised in that：It is set up in respectively including rack, both sides above two crossbeams of the rack
And be slidably matched with the crossbeam diaphragm filtering plate components (100), be fixedly installed on described rack one end and parallel to it is described every
The thrust plate (200) of film filter plate assembly (100) setting is arranged at the rack other end and for making the diaphragm filtering plate components
(100) pressure strip (300) to (200) one side compression of thrust plate, the driving device being connected with the pressure strip (300)
(400), it is equipped with below the rack parallel to the crossbeam and for the air supply pipe to the diaphragm filtering plate components (100) supply
(510), the air supply pipe (510) is equipped with the branch pipe (520) that several are connected with the diaphragm filtering plate components (100), institute
State be respectively provided on the outside of diaphragm filtering plate components (100) make liquid to be filtered enter inlet tube (130) and for making filtering
The outlet tube (140) of filtrate discharge afterwards.
2. a kind of diaphragm filter press as described in claim 1, it is characterised in that：The diaphragm filtering plate components (100) are if include
Dry a perpendicular to the membrane filter plate of the crossbeam and laid out in parallel (110), the both sides plate face of the membrane filter plate (110) is equipped with
For being passed through the cavity of the liquid to be filtered, the inner surface of the cavity is equipped with evenly arranged raised (113), the protrusion
(113) formed to make between the filtrate by diversion trench, the center of the cavity is equipped with described to be filtered for being passed through
The inlet opening (111) of liquid, the outer surface of the cavity are equipped with membrane (120), and the plate face four corners of the membrane filter plate (110) are set
The fluid hole (112) for making the filtrate discharge is useful for, the diversion trench is with the fluid hole (112) in the membrane filter plate
(110) connected inside plate body by flow-guiding channel (116).
3. a kind of diaphragm filter press as claimed in claim 2, it is characterised in that：The adjacent membrane with the thrust plate (200)
The inlet opening (111) of filter plate (110) is connected with the inlet tube (130), the adjacent membrane filter plate with the thrust plate (200)
(110) fluid hole (112) is connected with the outlet tube (140).
4. a kind of diaphragm filter press as claimed in claim 2, it is characterised in that：The protrusion (113) is included for being formed
It states the basis raised (114) of diversion trench and is used to support the support protrusion (115) of the membrane (120), the support protrusion
(115) it is arranged at the periphery of the inlet opening (111) and is uniformly placed with several.
5. a kind of diaphragm filter press as claimed in claim 4, it is characterised in that：The support protrusion (115) protrude outward in
The basis is raised (114).
6. a kind of diaphragm filter press as claimed in claim 5, it is characterised in that：The area of the support protrusion (115) is more than
The area on the basis raised (114).
7. a kind of diaphragm filter press as claimed in claim 2, it is characterised in that：Below the side of the membrane filter plate (110)
Equipped with the interface being connected with the branch pipe (520), the interface passes through the plenum duct (530) inside the cavity and the type
The inner surface connection of chamber.
8. a kind of diaphragm filter press as claimed in claim 2, it is characterised in that：The side of the membrane filter plate (110) is equipped with
For being set up in the hangers of the crossbeam (150), the beam sides are equipped with to pull the drag hook component of the hangers (150)
(160), the drag hook component (160) includes leading parallel to the guide rail (161) of crossbeam length direction setting and with described
Rail (161) is slidably matched and the drag hook (162) for pulling the hangers (150).
9. a kind of diaphragm filter press as claimed in claim 8, it is characterised in that：The hangers (150) is in the crossbeam length
Thickness on direction is less than the thickness of the membrane filter plate (110).
10. a kind of diaphragm filter press as described in claim 1, it is characterised in that：The branch pipe (520) is rubber hose.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721380210.3U CN207445701U (en) | 2017-10-24 | 2017-10-24 | A kind of diaphragm filter press |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721380210.3U CN207445701U (en) | 2017-10-24 | 2017-10-24 | A kind of diaphragm filter press |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207445701U true CN207445701U (en) | 2018-06-05 |
Family
ID=62281392
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721380210.3U Active CN207445701U (en) | 2017-10-24 | 2017-10-24 | A kind of diaphragm filter press |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207445701U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109011748A (en) * | 2018-09-07 | 2018-12-18 | 安徽金贺财建筑工程有限公司 | A kind of efficient membrane filter plate filter press |
| CN109045785A (en) * | 2018-08-21 | 2018-12-21 | 嘉兴市嘉盛印染有限公司 | A kind of plate and frame filter press |
| CN109395861A (en) * | 2018-11-08 | 2019-03-01 | 丹阳市美尔鑫化工有限公司 | A kind of aluminium pigment preparation ball milling, screening and the press filteration system of environmental protection |
| CN109865326A (en) * | 2019-03-14 | 2019-06-11 | 杭州安永环保科技有限公司 | The diaphragm plate of filter sheet core energy reuse |
| WO2020088071A1 (en) * | 2018-10-30 | 2020-05-07 | 杨作星 | Solid-liquid separation system for pneumatic conveying fluid bidirectional mixed pressing |
| CN113069802A (en) * | 2021-04-26 | 2021-07-06 | 重庆派斯克刀具制造股份有限公司 | Grinding fluid filters slag discharging device |
| CN114028848A (en) * | 2021-11-19 | 2022-02-11 | 临朐恒辉新材料有限公司 | Plate-frame filter for producing aluminum hydroxide powder |
-
2017
- 2017-10-24 CN CN201721380210.3U patent/CN207445701U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109045785A (en) * | 2018-08-21 | 2018-12-21 | 嘉兴市嘉盛印染有限公司 | A kind of plate and frame filter press |
| CN109011748A (en) * | 2018-09-07 | 2018-12-18 | 安徽金贺财建筑工程有限公司 | A kind of efficient membrane filter plate filter press |
| WO2020088071A1 (en) * | 2018-10-30 | 2020-05-07 | 杨作星 | Solid-liquid separation system for pneumatic conveying fluid bidirectional mixed pressing |
| CN109395861A (en) * | 2018-11-08 | 2019-03-01 | 丹阳市美尔鑫化工有限公司 | A kind of aluminium pigment preparation ball milling, screening and the press filteration system of environmental protection |
| CN109865326A (en) * | 2019-03-14 | 2019-06-11 | 杭州安永环保科技有限公司 | The diaphragm plate of filter sheet core energy reuse |
| CN113069802A (en) * | 2021-04-26 | 2021-07-06 | 重庆派斯克刀具制造股份有限公司 | Grinding fluid filters slag discharging device |
| CN114028848A (en) * | 2021-11-19 | 2022-02-11 | 临朐恒辉新材料有限公司 | Plate-frame filter for producing aluminum hydroxide powder |
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