CN205145788U - Liquid filtration system - Google Patents
Liquid filtration system Download PDFInfo
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- CN205145788U CN205145788U CN201520905769.8U CN201520905769U CN205145788U CN 205145788 U CN205145788 U CN 205145788U CN 201520905769 U CN201520905769 U CN 201520905769U CN 205145788 U CN205145788 U CN 205145788U
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- filter
- stoste
- filter element
- recoil
- clear liquid
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Abstract
The utility model discloses a liquid filtration system, including at least two -stage filtration unit, all be provided with the filter among the filter unit, the filter has the stoste import that supplies to wait to filter the stoste entering, the concentrated stoste exhaust stoste export that forms when supplying to have filtered clear solution exhaust purified liquor outlet and supplying the filtration, clear solution collection device is connected to each purified liquor outlet, among the filter unit at different levels among stoste export and the adjacent filter unit of subordinate of filter the stoste import of filter link to each other, the former liquid pump of stoste access connection of the filter among the chopped -off head filter unit, the stoste exit linkage stoste collection device of the filter among the final stage filter unit. The utility model discloses can realize liquid continuous filtration, improve filter fineness, and reduce the filtration energy consumption, greatly reduced liquid filter manufacturing cost.
Description
Technical field
The utility model relates to liquid filtering field, is specifically related to a kind of fluid filter system.
Background technology
Liquid filtering refers to and the liquid containing impurity is flow through the filter medium with certain porosity, and the impurity in liquid is trapped within dielectric surface or inner and remove.Use comparatively general filter type to comprise two kinds in current liquid filtering, one is terminal type liquid filtering, and another kind is cross-current type liquid filtering.Terminal type filter element is adopted in terminal type sedimeter, go out in entering beyond stoste to be filtered or in the form entering to go out pass through filter element, impurity in stoste to be filtered is intercepted at filter element surface, after filtering a period of time, filter element surface can deposit one deck filter cake, the filter efficiency of filter element is caused to reduce thus, regenerate to make filter element, need the filter cake of scheduled shut down cleaning and filtering element surface, this kind of filter in use needs repeatedly to stop, make production process discontinuous, also larger economic loss can be caused time serious.What adopt in cross-current type sedimeter is cross-flow filtration element, stoste to be filtered also can wash away filter element surface when being filtered by this kind of filter element, after filtration, the clear liquid of gained is concentrated and is discharged, after filtration, remaining concentration stock solution reenters in cross-flow filtration element after discharging and filters under circulating pump effect, realize the circulating filtration of concentration stock solution in cross-flow filtration element, this kind of filter can realize continuous seepage in filter, but its process circulating pump needs to overcome the circulating filtration that larger resistance realizes concentration stock solution, considerably increase production cost thus.
Utility model content
Technical problem to be solved in the utility model is that providing a kind of can realize continuous seepage and the fluid filter system of reduction production cost.
In order to solve above-mentioned prior art problem, the utility model is achieved through the following technical solutions:
The utility model fluid filter system comprises at least double-filtration unit, filter is provided with in described filter element, filter has the stoste import entered for stoste to be filtered, for crossing the purified liquor outlet that cleaner liquid is discharged and the stoste outlet of discharging for the concentration stock solution formed when filtering, purified liquor outlet connects clear liquid gathering-device, the stoste outlet of each filter element middle filtrator is connected with the stoste import of adjacent subordinate's filter element middle filtrator, the stoste import of the filter in chopped-off head filter element connects raw liquor pump, the stoste outlet of the filter in final stage filter element connects stock solution collection device.Stoste to be filtered realizes continuous seepage step by step by above-mentioned multistage filtering unit and filters, improve filtering accuracy, after filtration, remaining concentration stock solution enters into subordinate's filter element continuation filtration under the effect of raw liquor pump, continue filtration kinetic energy, and do not need in filter process additionally to overcome resistance, thus reduce plant energy consumption, decrease production cost.Concentration stock solution collecting pit, makes the concentration stock solution of discharging from whole fluid filter system obtain centralized collection thus, is convenient to thus focus on it.
As the further improvement of aforesaid liquid filtration system, the consistent and quantity of the filter specification of filter element at different levels is successively decreased step by step.The clear liquid filtered is had to export in every grade of filter element, therefore the concentration stock solution amount that every grade of filter element middle filtrator receives from upper level is reducing gradually, in order to more reasonably distribute the number of filters of every grade of filter element, according to the principle that above-mentioned concentration stock solution amount reduces gradually, should ensure that the filter area of every grade of filter element is successively decreased step by step, when each metre filter area is certain, the number of filters of every grade of filter element is successively decreased step by step.
As the further improvement of aforesaid liquid filtration system, the concentration stock solution that in higher level's filter element, the stoste outlet of all filters is discharged always is flow in the filter in adjacent subordinate filter element by stoste manifold again, and described purified liquor outlet is connected with the backpurge system of backwash filter respectively.The filter in subordinate's filter element is flow to again after gathering, make to filter kinetic energy to be gathered, be assigned in the filter in subordinate's filter element better, described purified liquor outlet is connected with backpurge system, when certain filter in certain grade of filter element needs backwash, open the hollow filter inside configuration of this backwashing system to this filter and carry out backwash, other filter in this grade of filter element and the equal normal filtration of filter in other grade of filter element, ensure that thus and carry out filter operation while backwash is carried out, further enhance the continuous filtration function of this fluid filter system.
As a kind of preferred structure of backpurge system, purified liquor outlet is connected with clear liquid gathering-device by clear liquid pipe, clear liquid pipe side extends recoil tube, recoil tube is provided with the recoil by-pass valve control controlling backwash liquid and pass through and block, each recoil tube gathers to be formed to be responsible for and to be connected with clear liquid gathering-device, supervisor is provided with recoil pump clear liquid being pumped into filter interior, and each stoste import department is provided with stoste by-pass valve control.Adopt said structure that backflush operation and filter operation can not be clashed, control recoil pump recoil by stoste by-pass valve control keeps remaining filter normally to export clear liquid in requisition for the filter of backwash simultaneously, and recoil by-pass valve control controls to need the filter of backwash stopping stoste entering and keeps remaining filter normally to input stoste simultaneously.
As the further improvement of aforesaid liquid filtration system, described stoste by-pass valve control, recoil by-pass valve control and recoil pump are all connected with control device.Determine that each filter needs to carry out the cycle of backwash according to practical experience, this cycle is set in control device, the open and close of convenient control backflush operation Central Plains hydraulic control valve door, recoil by-pass valve control and recoil pump thus, automatically controlled by control device, thereby reduce the workload of operating personnel.
Further, described filter comprises housing and at least one filter element, described filter element is the hollow filter structure being arranged at enclosure interior, stoste to be filtered plays certain souring when enclosure interior circulates to hollow filtration surface, the filter cake of hollow filter body structure surface is discharged along with stoste, clear liquid after filtration is discharged from purified liquor outlet after entering the hollow region of hollow filter structure, makes the filter efficiency of hollow filter structure keep stable thus.
One as hollow filter structure is preferred, and described hollow filter structure is the hollow filter plate that porous metal film surrounds, and described purified liquor outlet is the short tube extended from one end of hollow filter, and this short tube is connected with clear liquid gathering-device through housing.This kind of hollow filter structure effective filtration area is larger, makes filter effect better.Described lower portion is provided with the bracing frame supporting tow sides filter membrane.In order to avoid hollow filter plate generation deformation in filter process, need to arrange at hollow filter intralamellar part the bracing frame supporting porous metal film, keep its filter effect to stablize thus.Preferred described porous metal film is flake, and its thickness is 5 ~ 1500 μm, and average pore size is 0.05 ~ 100 μm, and porosity is 15% ~ 70%, facts have proved, porous metal film filter effect is with this understanding best.
As the further improvement of aforesaid liquid filtration system, the flowing velocity that described raw liquor pump controls stoste and concentration stock solution is 0.5 ~ 3.0m/s.Filter effect is best under these conditions for the flow velocity of stoste and concentration stock solution.
Accompanying drawing explanation
Below by way of accompanying drawing and detailed description of the invention, the utility model is further described.
Fig. 1 is schematic diagram of the present utility model.
Fig. 2 is the structure chart of the utility model middle filtrator.
Fig. 3 is the structure chart of hollow filter plate in the utility model.
Detailed description of the invention
Fig. 1 shows a kind of structure of fluid filter system, comprise first order filter element 3, second level filter element 4 and third level filter element 5, described first order filter element 3 comprises the first filter 310, second filter 320 and the 3rd filter 330, described second level filter element 4 comprises the 4th filter 410 and the 5th filter 420, the 6th filter 510 is only provided with in described third level filter element 5, filter specification in filter element at different levels is consistent, first filter 310 in first order filter element 3, second filter 320 and the 3rd filter 330 are connected with stoste groove 1, also be provided with raw liquor pump 2 between the two, stoste to be filtered in stoste groove 1 can be pumped in first order filter element 3 by raw liquor pump 2, first filter 310 in first order filter element 3, be connected with second level filter element 3 after second filter 320 and the 3rd filter 330, by stoste pipe A, the stoste concentrate produced in first order filter element 3 is dispensed to the 4th filter 410 in second level filter element 3 and the 5th filter 420, described 4th filter 410 and the 5th filter 420 are by the 6th filter 510 in stoste pipe A and third level filter element 4, the stoste concentrate produced by second level filter element 3 is input in the 6th filter 510 by stoste pipe A.Described first order filter element 3, the stoste import department of each filter in second level filter element 4 and third level filter element 5 is equipped with stoste control valve, corresponding relation is that the stoste import of the first filter 310 is provided with the first stoste valve a1, the stoste import of the second filter 320 is provided with the second stoste valve a2, the stoste import of the 3rd filter 330 is provided with the 3rd stoste valve a3, the stoste import of the 4th filter 410 is provided with the 4th stoste valve a4, the stoste import of the 5th filter 420 is provided with Wuyuan fluid valve a5, the stoste import of the 6th filter 510 is provided with the 6th stoste valve a6.Described first order filter element 3, filter in second level filter element 4 and third level filter element 5 is connected with clean solution tank 6 respectively by clear liquid pipe B, each clear liquid pipe B side expenditure recoil tube C, each recoil tube C is all equipped with recoil control valve, corresponding relation is that the recoil tube C of the first filter 310 is provided with the first recoil valve b1, the recoil tube C of the second filter 320 is provided with the second recoil valve b2, the recoil tube C of the 3rd filter 330 is provided with the 3rd recoil valve b3, the recoil tube C of the 4th filter 410 is provided with the 4th recoil valve b4, the recoil tube C of the 5th filter 420 is provided with the 5th recoil valve b5, the recoil tube C of the 6th filter 510 is provided with the 6th recoil valve b6, each recoil tube C gathers formation supervisor and is communicated with clean solution tank 6, described supervisor is provided with recoil pump 7, clear liquid can be pumped into filter by recoil pump 7, above-mentioned stoste control valve, recoil control valve, recoil pump is all connected with control device 9, PLC selected by this control device, described 6th filter 510 stoste discharge place is connected with stoste concentrate collecting pit 8.In figure, the arrow points of stoste pipe A is stoste flow direction, and clear liquid pipe B upward arrow is oriented to clear liquid flow direction, the flow direction of clear liquid for recoiling when recoil tube C upward arrow is oriented to recoil.
Fig. 2 shows a kind of structure of the first filter, all the other filtration device structures are consistent with the first filtration device structure, described first filter comprises housing 311 and three groups of filter elements, filter element often in group is spaced and parallel setting from top to down, each filter element can form one group of filter element in the frame by clamping, also can directly be connected with housing 311 separately, described filter element is the hollow filter structure 314 being arranged at housing 311 inside, described hollow filter structure 314 is provided with the purified liquor outlet for crossing cleaner liquid discharge, described purified liquor outlet passes from housing 311 side, described housing 311 is provided with the stoste import 312 entered for stoste to be filtered and the stoste outlet 313 of discharging for concentration stock solution after filtration, described housing 311 can be cylindric, also can be cubic, in figure, arrow points is stoste flow direction in the filter.
Fig. 3 shows a kind of structure of hollow filter plate, comprising described hollow filter structure 314 is hollow filter plate, described hollow filter plate comprise the framework 3140 that forms as the frame combination on each batten rib and be arranged at framework 3140 up and down before and after porous metal film 3141 on six faces, described purified liquor outlet is the short tube 3142 extended from hollow filter one end, this short tube 3142 is passed housing 311 top and is connected with clean solution tank 6 by clear liquid pipe B, described filter element is the hollow filter structure 314 being arranged at housing 311 inside, described framework 3140 interior parallel is arranged at intervals with the bracing frame 3143 of bar tabular.Described framework 3140, short tube 3142 and bracing frame 3143 all adopt stainless steel material, all adopt and be weldingly connected between three and porous metal film 3141.
Preferred described filter membrane adopts the application number of the applicant to be flexible, porous metal forming in the earlier application of 201410609038.9, described porous metal film is flake, its thickness is 5 ~ 1500 μm, average pore size is 0.05 ~ 100 μm, porosity is 15% ~ 70%, and the flowing velocity that described raw liquor pump controls stoste and concentration stock solution is 0.5 ~ 3.0m/s.Under above-mentioned filter condition, filter effect is better.
Using method of the present utility model is: under normal filtration state, stoste control valve is all in open mode, recoil control valve is all in closed condition with recoil pump, stoste to be filtered in stoste groove pumps into first order filter element under the effect of raw liquor pump, cross cleaner liquid in first order filter element and flow into clean solution tank by clear liquid pipe, the stoste concentrate filtering gained gathers distribution and enters second level filter element, second level filter element has been crossed cleaner liquid and has been flowed into clean solution tank equally, filter the stoste concentrate of gained to gather and enter third level filter element, after this stoste concentrate filters by third level filter element, the cleaner liquid of crossing of gained flows into clean solution tank, stoste concentrate enters in stoste concentrate collecting pit the most at last.When needs carry out recoil cleaning to certain filter, such as, when needing recoil cleaning the first filter, PLC controls closedown first stoste valve a1, control to open the first recoil valve and recoil pump simultaneously, now stoste is not had to flow in the first filter, also flow out without clear liquid simultaneously, by the clear liquid in clean solution tank, the hollow filter intralamellar part be pumped in the first filter carries out backwash to recoil pump, in this process, other filter keeps filter operation inconvenience, the backwash process time is very short, general lasting a few second, therefore the filter operation for the first filter can not produce obvious impact, thus achieve the continuous filtration to liquid, in the process that stoste transmits step by step, next stage always relies on the power of upper level, do not need to overcome larger resistance, because this reducing the energy consumption of this process, greatly reduce production cost.
Claims (10)
1. fluid filter system, comprise at least double-filtration unit, filter is provided with in described filter element, described filter has the stoste import (312) entered for stoste to be filtered, for crossing the purified liquor outlet that cleaner liquid is discharged and stoste outlet (313) of discharging for the concentration stock solution formed when filtering, described purified liquor outlet connects clear liquid gathering-device, it is characterized in that: stoste outlet (313) of filter element middle filtrator at different levels is connected with the stoste import (312) of adjacent subordinate's filter element middle filtrator, the stoste import (312) of the filter in chopped-off head filter element connects raw liquor pump (2), stoste outlet (313) of the filter in final stage filter element connects stock solution collection device.
2. fluid filter system as claimed in claim 1, is characterized in that: the consistent and quantity of the filter specification of filter element at different levels is successively decreased step by step.
3. fluid filter system as claimed in claim 2, it is characterized in that: the concentration stock solution that in higher level's filter element, stoste outlet (313) of all filters is discharged is gathered by stoste pipe (A) in the filter flow to again in adjacent subordinate filter element, and described purified liquor outlet is connected with the backpurge system of backwash filter respectively.
4. fluid filter system as claimed in claim 3, it is characterized in that: purified liquor outlet is connected with clear liquid gathering-device by clear liquid pipe (B), clear liquid pipe (B) side extends recoil tube (C), recoil tube (C) is provided with the recoil by-pass valve control controlling backwash liquid and pass through and block, each recoil tube (C) gathers to be formed to be responsible for and to be connected with clear liquid gathering-device, supervisor is provided with the recoil pump (7) clear liquid being pumped into filter interior, and each stoste import (312) place is provided with stoste by-pass valve control.
5. fluid filter system as claimed in claim 4, is characterized in that: described stoste by-pass valve control, recoil by-pass valve control and recoil pump (7) are all connected with control device (9).
6. fluid filter system as claimed in claim 1, it is characterized in that: described filter comprises housing (311) and at least one filter element, described filter element is for being arranged at the inner hollow filter structure (314) of housing (311).
7. fluid filter system as claimed in claim 6, it is characterized in that: the hollow filter plate that described hollow filter structure (314) surrounds for porous metal film (3141), described purified liquor outlet is the short tube (3142) extended from one end of hollow filter, and this short tube (3142) is connected with clear liquid gathering-device through housing (311).
8. fluid filter system as claimed in claim 7, is characterized in that: described hollow filter intralamellar part is provided with the bracing frame (3143) supporting porous metal film (3141).
9. fluid filter system as claimed in claim 7, is characterized in that: described porous metal film (3141) is flake, and its thickness is 5 ~ 1500 μm, and average pore size is 0.05 ~ 100 μm, and porosity is 15% ~ 70%.
10. fluid filter system as claimed in claim 1, is characterized in that: the flowing velocity that described raw liquor pump (2) controls stoste and concentration stock solution is 0.5 ~ 3.0m/s.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520905769.8U CN205145788U (en) | 2015-11-13 | 2015-11-13 | Liquid filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520905769.8U CN205145788U (en) | 2015-11-13 | 2015-11-13 | Liquid filtration system |
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| Publication Number | Publication Date |
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| CN205145788U true CN205145788U (en) | 2016-04-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520905769.8U Active CN205145788U (en) | 2015-11-13 | 2015-11-13 | Liquid filtration system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108786263A (en) * | 2018-09-06 | 2018-11-13 | 浙江海河环境科技有限公司 | A kind of process and device of pre-filtering and filter press linkage fast filtering |
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2015
- 2015-11-13 CN CN201520905769.8U patent/CN205145788U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108786263A (en) * | 2018-09-06 | 2018-11-13 | 浙江海河环境科技有限公司 | A kind of process and device of pre-filtering and filter press linkage fast filtering |
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