CN205730549U - Row's formula drainage system mutually of ceramic filter - Google Patents
Row's formula drainage system mutually of ceramic filter Download PDFInfo
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- CN205730549U CN205730549U CN201620455101.2U CN201620455101U CN205730549U CN 205730549 U CN205730549 U CN 205730549U CN 201620455101 U CN201620455101 U CN 201620455101U CN 205730549 U CN205730549 U CN 205730549U
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- ceramic filter
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- drainage system
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Abstract
The utility model discloses row's formula drainage system mutually of a kind of ceramic filter, it includes first, second flow container, and first, second vacuum pump bled in the tank chamber of first, second flow container respectively, the filtrate (liquid of ceramic filter controls to lead to the first inlet of the first flow container or the second inlet of the second flow container through three-way diverter valve, and the bottom of first, second flow container is respectively arranged with first, second leakage fluid dram.During use, can be first by filter vacuum suction first flow container of ceramic filter, when the liquid level of the first flow container arrives the upper limit, again the filtrate of ceramic filter is gone in suction the second flow container, to arrange outside filtrate in first flow container the most at ambient pressure, the feed liquor of first, second flow container, discharge opeing action is controlled thus by cycle alternation, so that it is guaranteed that normal drainage.Use drainage system disclosed in this utility model can effectively reduce the size of the flow container for vacuum collecting filtrate, thus facilitate layout and the carrying out of maintenance work of Factory Building.
Description
Technical field
This utility model relates to solid-liquid separation technique field, is specifically related to the mutual of a kind of ceramic filter
Row's formula drainage system.
Background technology
Ceramic filter is a kind of collection electromechanics, Automated condtrol, ultrasonic waves for cleaning and poromerics
Etc. new and high technology in the solid-liquid separating equipment of one, its have efficient, energy-conservation, good filtration effect,
The features such as automaticity is high, operating cost is low, use this separation equipment to process the filtrate obtained clear
Clear comprehensively utilize, and filtration cakes torrefaction, therefore to filter medium strong adaptability, at present, pottery mistake
Filter is widely used in the industries such as coloured, chemical industry, mine, smelting, medicine, food.
In prior art, ceramic filter mainly by ceramic filter plate, vacuum system, to ore discharge system
Several parts compositions such as system, drainage system and frame, it is mainly based upon capillary micropore when using
Action principle, makes screen plate inner chamber produce pressure with outside by the vacuum filtration effect of drainage system
Difference, so that the serosity in hopper adsorbs the micropore on ceramic filter plate surface under condition of negative pressure
Place, the water in such serosity is pumped through the micropore of ceramic filter plate and is delivered to discharge opeing by pipeline
The flow container of system discharges with centralized collection, and the solid material in serosity is because of cannot be by micropore
It is trapped within the surface of ceramic filter plate, thus reaches the purpose of solid-liquid separation.
Actual during vacuum filtration, owing to the flow container of drainage system is under condition of negative pressure, therefore
Flow container cannot implement discharge opeing work while feed liquor, therefore reaches more than 40 for filter area
Bigger ceramic filter for, its drawing liquid amount is big, needs to configure the flow container of big volume, great Rong
Long-pending flow container takes up room greatly, adds the construction cost of Factory Building and the maintenance difficulty of equipment the most undoubtedly
Spending, and the layout of Factory Building is limited to, a therefore discharge opeing difficult problem certainly will affect the work of ceramic filter
Run.
Summary of the invention
The purpose of this utility model is to provide a kind of guarantee continuous draining, the pottery that automaticity is high
Row's formula drainage system mutually of filter.
For achieving the above object, the technical solution adopted in the utility model is: a kind of ceramic filter
Mutually row's formula drainage system, it is characterised in that: include first, second flow container, and respectively to the
One, the tank chamber of the second flow container carries out first, second vacuum pump bled, the filtrate of ceramic filter
Export the first inlet or the second of the second flow container controlling to lead to the first flow container through three-way diverter valve
Inlet, the bottom of first, second flow container is respectively arranged with first, second leakage fluid dram.
Use having the beneficial effects that of technique scheme generation: during use, can be first by ceramic filter
In filter vacuum suction first flow container of machine, when the liquid level of the first flow container arrives the upper limit, then will pottery
The filtrate of porcelain filter goes in suction the second flow container, simultaneously at ambient pressure by the filter in the first flow container
Outside liquid row after again evacuation stand-by, thus by cycle alternation control first, second flow container feed liquor,
Discharge opeing action, ensures that ceramic filter is in the state of filtered off with suction all the time.With existing skill
Art is compared, and uses drainage system disclosed in this utility model can not only guarantee holding of ceramic filter
Continuous sucking filtration discharge opeing, and the size of the flow container for vacuum collecting filtrate can be effectively reduced, thus
Facilitate layout and the carrying out of maintenance work of Factory Building.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the partial top view of Fig. 1；
Fig. 3 is the I portion enlarged drawing of Fig. 1.
Detailed description of the invention
A kind of mutually row's formula drainage system of ceramic filter, as shown in Figure 1-2, it includes first,
Second flow container 10,20, and is bled in the tank chamber of first, second flow container 10,20 respectively
First, second vacuum pump 30,40, the filtrate (liquid 51 of ceramic filter 50 is through triplet commutation
Valve 60 controls to lead to the first inlet 11 or the second feed liquor of the second flow container 20 of the first flow container 10
Mouthfuls 21, the bottom of first, second flow container 10,20 be respectively arranged with first, second leakage fluid dram 12,
22。
During use, can first guarantee that the first leakage fluid dram 12 of the first flow container 10 is closed, with
Time through the first vacuum pump 30 bleed control the first flow container 10 tank chamber be in negative pressure, now by control
Three-way valve 60 processed makes the filtrate (liquid 51 of ceramic filter 50 lead to through three-way diverter valve 60
First inlet 11 of one flow container 10；When the liquid level in the first flow container 10 arrives the upper limit,
It is in guaranteeing the second flow container 20 at negative pressure state, and the second leakage fluid dram 22 of the second flow container 20
In closed mode, then make the filtrate (liquid 51 of ceramic filter 50 by controlling three-way valve 60
Going to lead to the second inlet 21 of the second flow container 20, meanwhile, the first vacuum pump 30 stops
First flow container 10 is bled, and the first leakage fluid dram 12 of the first flow container 10 is opened and carried out discharge opeing,
Close the first leakage fluid dram 12 after treating discharge opeing, bled by the first vacuum pump 30 the most again and make the
Again negative pressure state it is in carry out the preparation collecting filtrate, such cycle alternation in one flow container 10
Carry out the feed liquor of first, second flow container 10,20, discharge opeing action, ensure that ceramic filter
Machine 50 is in the state of filtered off with suction all the time.Compared with prior art, use this utility model public
The drainage system opened can not only guarantee the lasting sucking filtration discharge opeing of ceramic filter 50, and permissible
Effectively reduce the size of flow container for vacuum collecting filtrate, not only facilitate the layout of Factory Building, save
Equipment investment cost, and it is easy to the carrying out of maintenance work, therefore can promote at relevant enterprise should
With.
As further preferred version: as shown in Figure 1-2, first, second vacuum pump 30,40
Bleeding point connect one of them joint of first, second Pneumatic three-way valve 31,41 respectively,
Two other joint of one Pneumatic three-way valve 31,41 connects the of air and the first flow container 10 respectively
One air vent 13, two other joint of the second Pneumatic three-way valve 41 connects air and second respectively
The second exhaust port 23 of flow container 20.So when the filtrate (liquid 51 of ceramic filter 50 is through threeway
When reversal valve 60 leads to the first inlet 11 of the first flow container 10, at the first Pneumatic three-way valve 31
In connection the first vacuum pump 30 and position of the first flow container 10, so that it is guaranteed that the first flow container 10
It is in tank under condition of negative pressure so that filtrate flows in the first flow container 10；When in the first flow container 10
When liquid level arrives the upper limit, by controlling three-way valve 60, the filtrate of ceramic filter 50 is gone out
Mouth 51 goes to lead to the second inlet 21 of the second flow container 20, meanwhile, the first Pneumatic three-way
Valve 31 is in connection air and the position of the first flow container 10, so that it is guaranteed that the tank of the first flow container 10
Inside it is in condition of normal pressure, so opens the first leakage fluid dram 12 and can complete the discharge opeing of the first flow container 10
Work.Certainly, the first flow container 10 is during discharge opeing, and the second flow container 20 is in feed liquor state,
And second Pneumatic three-way valve 41 be in connection the second vacuum pump 40 and position of the second inlet 21,
So can realize the alternately feed liquor of first, second flow container 10,20, discharge opeing work.
Further, as it is shown in figure 1, the outer wall of described first, second flow container 10,20 is distinguished
Being provided with first, second liquidometer 70,80 of liquid level in detecting tank, control unit is according to
One, the liquid level signal that the second liquidometer 70,80 sends controls the filtrate (liquid of ceramic filter 50
51 lead to the first inlet 11 of the first flow container 10 or the second flow container 20 through three-way diverter valve 60
Second inlet 21.In other words, control unit can be according to first, second flow container 10,20
Liquid level thus control first, second flow container 10,20 and carry out into, discharge opeing action, automatization
Degree is high.
Concrete, shown in Fig. 1-2, it is disposed with at the filtrate (liquid 51 of ceramic filter 50
Filtrate distribution pipe 52, filtrate distribution pipe 52 will flow out at the filtrate (liquid 51 of ceramic filter 50
Filtrate concentrate be delivered to flow into the first or second flow container 10,20 through three-way diverter valve 60.
Preferably, as it is shown in figure 1, first, second discharge opeing of first, second flow container 10,20
Being hingedly connected with first, second door 121,221 respectively at mouth 12,22, first, second is true
Empty pump 30,40 driving first, second door 121,221 of bleeding rotates to realize the around jointed shaft
One, the switching motion of the second leakage fluid dram 12,22, in other words, first, second door 121,
221 switch equivalent of from suction, and it can be according to the pressure condition in first/second flow container 10,20
Automatically the switching motion of first/second leakage fluid dram 12,22 is implemented.
Further, the top of described first, second flow container 10,20 is separately provided for inspection
Survey the Pressure gauge 90 of pressure inside the tank, may determine that this drainage system by the data of Pressure gauge 90
Running status, intuitive is strong.
Concrete, as it is shown in figure 1, described three-way diverter valve 60 is operated pneumatic valve；Threeway is changed
At valve 60, it is provided with the pressure transducer 100 of hydraulic pressure in detecting output channel, passes through pressure
Water pressures in sensor 100 detection output channel, so can facilitate and whether understand filtrate in time
It is in normal discharge state, safe and reliable.
Claims (7)
1. mutually row's formula drainage system of a ceramic filter, it is characterised in that: include first,
Second flow container (10,20), and respectively the tank chamber of first, second flow container (10,20) is entered
First, second vacuum pump (30,40) that row is bled, the filtrate (liquid of ceramic filter (50)
(51) control to lead to first inlet (11) of the first flow container (10) through three-way diverter valve (60)
Or second second inlet (21) of flow container (20), first, second flow container (10,20)
Bottom is respectively arranged with first, second leakage fluid dram (12,22).
The most according to claim 1, row's formula drainage system mutually of ceramic filter, its feature exists
In: the bleeding point of first, second vacuum pump (30,40) connects first, second pneumatic three respectively
One of them joint of logical valve (31,41), other the two of the first Pneumatic three-way valve (31,41)
Individual joint connects the first row QI KOU (13) of air and the first flow container (10) respectively, and second is pneumatic
Two other joint of three-way valve (41) connects air and the second row of the second flow container (20) respectively
QI KOU (23).
The most according to claim 2, row's formula drainage system mutually of ceramic filter, its feature exists
Liquid in: the outer wall of described first, second flow container (10,20) is separately provided for detecting tank
Position first, second liquidometer (70,80), control unit according to first, second liquidometer (70,
80) liquid level signal sent controls the filtrate (liquid (51) of ceramic filter (50) and changes through threeway
The first inlet (11) or second flow container (20) of the first flow container (10) is led to valve (60)
The second inlet (21).
4. according to row's formula drainage system mutually of ceramic filter described in claim 1 or 2 or 3,
It is characterized in that: filtrate (liquid (51) place of ceramic filter (50) is disposed with filtrate distribution pipe
(52), filtrate (liquid (51) place of ceramic filter (50) is flowed by filtrate distribution pipe (52)
The filtrate gone out is concentrated and is delivered to flow into the first or second flow container (10,20) through three-way diverter valve (60).
5. according to row's formula drainage system mutually of ceramic filter described in claim 1 or 2 or 3,
It is characterized in that: first, second leakage fluid dram (12,22) of first, second flow container (10,20)
Place is hingedly connected with first, second door (121,221) respectively, first, second vacuum pump (30,
Driving first, second door (121,221) of 40) bleeding rotates around jointed shaft to realize first,
The switching motion of the second leakage fluid dram (12,22).
The most according to claim 4, row's formula drainage system mutually of ceramic filter, its feature exists
In: it is intrinsic pressure that the top of described first, second flow container (10,20) is separately provided for detecting tank
The Pressure gauge (90) of power.
The most according to claim 4, row's formula drainage system mutually of ceramic filter, its feature exists
In: described three-way diverter valve (60) is operated pneumatic valve, and three-way diverter valve (60) place is provided with
The pressure transducer (100) of hydraulic pressure in detecting output channel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620455101.2U CN205730549U (en) | 2016-05-17 | 2016-05-17 | Row's formula drainage system mutually of ceramic filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620455101.2U CN205730549U (en) | 2016-05-17 | 2016-05-17 | Row's formula drainage system mutually of ceramic filter |
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| Publication Number | Publication Date |
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| CN205730549U true CN205730549U (en) | 2016-11-30 |
Family
ID=57364886
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| CN201620455101.2U Active CN205730549U (en) | 2016-05-17 | 2016-05-17 | Row's formula drainage system mutually of ceramic filter |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237593A (en) * | 2019-07-19 | 2019-09-17 | 马鞍山钢铁股份有限公司 | Ceramic filter filtrate discharge system and discharge method |
-
2016
- 2016-05-17 CN CN201620455101.2U patent/CN205730549U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237593A (en) * | 2019-07-19 | 2019-09-17 | 马鞍山钢铁股份有限公司 | Ceramic filter filtrate discharge system and discharge method |
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