CN206063964U - A kind of ceramic filter drainage system - Google Patents
A kind of ceramic filter drainage system Download PDFInfo
- Publication number
- CN206063964U CN206063964U CN201621113167.XU CN201621113167U CN206063964U CN 206063964 U CN206063964 U CN 206063964U CN 201621113167 U CN201621113167 U CN 201621113167U CN 206063964 U CN206063964 U CN 206063964U
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- CN
- China
- Prior art keywords
- vacuum
- ceramic filter
- drainage system
- tank
- water
- 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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Abstract
The utility model discloses a kind of ceramic filter drainage system, the drainage system is connected by transparent hose with the distributor in ceramic filter, and Pneumatic vacuum ball valve is provided with transparent hose, the drainage system also includes vacuum tank, discharging tube, sealing radiator, vacuum pump, step sedimentation tank and filtrate water collection box, vacuum pressure regulating valve is provided with the top of the vacuum tank, the side of vacuum tank is connected with one end of the Pneumatic vacuum ball valve, opposite side is connected with vacuum pump, the lower end of vacuum tank is connected with discharging tube, it is connected with sealing radiator by discharging tube, the side of water tank is connected by stainless steel tube with one end of step sedimentation tank, the other end of step sedimentation tank is connected with the filtrate water collection box by return water pipe.The system ensure that the quality of filtrate recycle-water, can serve as ceramic filter and filters personal backwashing water use, it is not necessary to any power running equipment, greatly reduces equipment fault.
Description
Technical field
This utility model is related to a kind of drainage system, more particularly to a kind of ceramic filter drainage system.
Background technology
Ceramic filter be integrate electromechanics, micropore ceramics, Automated condtrol, ultrasound wave cleaning etc. new and high technology it is new
Generation ore dressing dehydration equipment.Mainly it is made up of host computer system purging system, dewatering system and microcomputer automatic control system, wherein taking off
Water system is also vapour-liquid distribution system, its objective is the vacuum environment for needed for equipment provides production, and extracts ceramic wafer
Filtrate reach outer row via vacuum barrel.
With the raising of the requirement to pelletizing plant to breeze moisture, it is unstable very that vacuum pressure often occurs in original drainage system Jing
The situation of vacuum pressure is lost to the short time, or the vacuum pressure of vacuum pump output is always maintained at long-time maximum, it is impossible to root
According to the property adjustments vacuum pressure of material, cause vacuum pump scaling loss often, the electronic equipment action that contains on drainage system and when
Between cooperation there is interruption, problems above directly affects the moisture of breeze, so increase unnecessary secondary filter into
This.Filtrate water is observed simultaneously, in order to check whether ceramic wafer damages, is open type by its discharge tube, is all flowed into and do close machine
Recirculated water is done, causes to waste significantly.Prior art can only do provisional process, there is no the solution of more thorough more system.
Original drainage system, the state that there is vacuum decompression, vacuum pressure are unstable, and electronic equipment has the state of Jing often failures, leads
Cause to run dirt, or vacuum pressure causes the abrasion that vacuum pump is unnecessary particular up to vacuum pump peak load, needs 200 per hour
The water service of cubic meter, greatly waste of resource, causes the raising of the cost of product.
Utility model content
This utility model provides a kind of ceramic filter drainage system, can carry out discharge opeing using the pressure discrepancy in elevation, and will filter
Liquid is recycled：Vacuum pressure level size is controlled with the discrepancy in elevation that water is noted, while filtrate water is switched to reclaim by outer row
Step sedimentation is reclaimed, so as to use as backwashing water.
This utility model adopts following technical proposals：The drainage system passes through saturating with the distributor in ceramic filter
It is bright hose connection, and Pneumatic vacuum ball valve is provided with transparent hose, the drainage system also includes vacuum tank, discharging tube, sealing
Water tank, vacuum pump, step sedimentation tank and filtrate water collection box, are provided with vacuum pressure regulating valve, very at the top of the vacuum tank
The side of slack tank is connected with one end of the Pneumatic vacuum ball valve, and opposite side is connected with vacuum pump, the lower end of vacuum tank with
Discharging tube connects, and is connected with sealing radiator by discharging tube, and the side of sealing radiator is with one end of step sedimentation tank by not
Rust fastener for connection, the other end of step sedimentation tank are connected with described filtrate water collection box one end by stainless steel tube, and filtrate water is returned
The other end for receiving case draws a clear water pipeline, and clear water pipeline is connected with the ceramic filter.
The connection is sealing pipeline connection.
The sealing radiator is more than 10 meters with the difference in height of vacuum barrel.
2 times for transparent sealing piping volume sum of the volume of the sealing radiator.
The vacuum tank is dome vacuum tank.
Observation port is provided with above the sealing radiator, dust cover on observation port, is added.Bottom adds oneself of point off density position
Water apopore, for bottom irrigation at ordinary times, and in emergency circumstances feed-tank moisturizing.
Be provided with multi stage precipitation case in the step sedimentation tank, every grade of settling tank lower end adds blow-off pipe, blow-off pipe with give ore deposit
Case connects to reclaim mineral contained in settling tank.
The volume of filtrate water collection box should meet the water yield of the required ceramic filter required for just starting.
Description of the drawings
Below in conjunction with the accompanying drawings and embodiment is described in further detail to this utility model：
Fig. 1 is the structural representation of the present invention.
Specific embodiment
In order that the purpose of this utility model, technical scheme and advantage become more apparent, below in conjunction with accompanying drawing and enforcement
Example, is further elaborated to this utility model.It should be appreciated that specific embodiment described herein is only to explain
This utility model, is not used to limit this utility model.
As shown in figure 1, this utility model provides a kind of ceramic filter drainage system, the drainage system and ceramic mistake
Distributor 1 in filter is connected by transparent hose, and Pneumatic vacuum ball valve 2 is provided with transparent hose, the drainage system
Also include vacuum tank 3, discharging tube 4, sealing radiator 5, vacuum pump 6, step sedimentation tank 7 and filtrate water collection box 8, the vacuum
The top of tank 3 is provided with vacuum pressure regulating valve 9, and the side of vacuum tank 3 is connected with one end of the Pneumatic vacuum ball valve 2, separately
Side is connected with vacuum pump 6, and the lower end of vacuum tank 3 is connected with discharging tube 4, is connected with sealing radiator 5 by discharging tube 4,
The side of sealing radiator 5 is connected by stainless steel tube with one end of step sedimentation tank 7, and the other end of step sedimentation tank 7 passes through back
Receive water pipe to be connected with the filtrate water collection box 8.As all granule foreigns are the therefore common ladder of ore particle and quartz particles
Level sedimentation tank 7 just can meet the requirement filtered, by the length of the good step sedimentation tank of experiment control 7, the position of precipitation dividing plate, now
The step sedimentation tank of finished product version is built in field.The other end of step sedimentation tank 7 passes through stainless steel tube and the filtrate water collection box 8 one
A clear water pipeline 10 is drawn in end connection, the other end of filtrate water collection box 8, and clear water pipeline 10 is connected with the ceramic filter
Connect, the moisture flowed out in clear water pipeline is Liang Ge branches, and an affluent-dividing enters the counter-flushing pipeline of ceramic filter, another point
Seal water pipe road is entered in tributary, and filtrate water collection box is connected with backwashing water pipeline, water seal water pipeline in ceramic filter, is used for
Ceramic filter runs and cleans required tap water volume, and filtrate water is both used for the water seal of backwashing water and vacuum pump.
In whole system, except being supplied to ceramic filter add in addition to water pump filtrate water, running device need not be added, together
When also reduce many running devices.Filtrate water is all reclaimed for the tap water needed for ceramic filter backwashing water, pickling, very
Empty pump water seal water and filter element cleaning tap water, replace the supply of original tap water completely.
The connection is the connection of sealing pipeline and due to the environment for having pickling, through the multiple filtrate water sampling at scene
Chemical examination, containing 5% or so nitric acid in water in the case of pickling, return water pipe and soldering opening go out to use acidproof material-paving and
Connection.
Be provided with multi stage precipitation case in the step sedimentation tank 7, every grade of settling tank lower end adds blow-off pipe, blow-off pipe with give ore deposit
Case connects.
The volume of the filtrate water collection box 8 should meet the water yield of the required ceramic filter required for just starting.
The sealing radiator 5 is more than 10 meters with the difference in height of vacuum barrel.
The volume of the sealing radiator 5 is seal piping volume sum 2 times, and sealing radiator is highly more than 1 meter, width
For 1 meter, return water pipe enters more than sealing radiator water surface 200mm.
The vacuum tank 3 is dome vacuum tank, is analyzed according to relevant knowledges such as engineering mechanics, stress analyses, will be existing
The vacuum tank of flat-top is changed to dome vacuum tank, greatly enhances its fastness, while end adds vacuum pressure regulating valve thereon
9, so vacuum pressure can reasonably be adjusted according to feed preparation unit size and greatly reduce unnecessary abrasion, it is also possible to can be according to ore deposit
Vacuum pressure needed for property adjustments.
Observation port is provided with above the sealing radiator 5, dust cover on observation port, is added；Sealing radiator 5 is that filtrate water is first
It is introduced at unhurried current, as slow 5 bottom of sealing radiator of current easily accumulates sludge first, so end opens up observation port thereon,
Find that in time deposition is processed in time, but as filtrate water is recycled, open up observation port and will hold thereon and add seal cover board,
In order to avoid cause unnecessary water pollution.
For the condition of negative pressure for overcoming vacuum internal pressure to be -0.092MPa, sealing radiator 5 is with vacuum barrel 3 it is necessary to have 10
The discrepancy in elevation of rice is required.As 10 high water columns are 1 atmospheric pressure, required vacuum pressure and water column are converted, and the operating of vacuum pump 6 is adjusted
In 9 goalkeeper's filtrate water pipe of section vacuum pressure regulating valve, water is raised to the height of required vacuum pressure.Filtration of the ore pulp through ceramic wafer
Breeze falls into belt, and filtrate water end count seal water tank 5 arrives step sedimentation tank 7, by once in a while due to ceramic wafer damage run into ore deposit granule
After sedimentation filtration is fallen, finally flowing into filtrate water collection box 8 is used for the backwashing water use of ceramic filter.If operation equipment mistake
Many or separate unit ceramic filter is excessive using ceramics, and trapezoidal Sedimentation tank 7 is changed to water purifying equipment so；Under sealing radiator 5
Portion can add multiple spot high pressure apopore, can both clear up water tank bottom and pile up sludge for a long time, again can be close in Emergency time
Seal water tank add water guarantee equipment normal operation.
Vacuum pressure can be adjusted to not exceed the present invention arbitrary value of vacuum pump peak load, while being not in that
The situation that vacuum fails or vacuum is reduced, while filtrate water completely seals pipeline recovery does not result in secondary pollution,
Junction transparent hose connection reduces vibration damage to be easy to see whether to exist run ore deposit state simultaneously, and filtrate water is individually reclaimed,
Enter back into recovery pond leading portion and add sedimentation filtration system, it is ensured that the quality of filtrate recycle-water, as the recoil that ceramic filter is used by oneself
Wash water is used.A whole set of drainage system does not need any power running equipment, and the equipment usage amount for greatly reducing reduces equipment event
Barrier, while reducing the supply of 200 cubic metres of tap waters per hour.
Claims (9)
1. a kind of ceramic filter drainage system, it is characterised in that：Distributor in the drainage system and ceramic filter
Connected by transparent hose, and Pneumatic vacuum ball valve is provided with transparent hose, the drainage system also includes vacuum tank, discharge opeing
Pipe, sealing radiator, vacuum pump, step sedimentation tank and filtrate water collection box, are provided with vacuum pressure tune at the top of the vacuum tank
Section valve, the side of vacuum tank are connected with one end of the Pneumatic vacuum ball valve, and opposite side is connected with vacuum pump, vacuum tank
Lower end is connected with discharging tube, is connected with sealing radiator by discharging tube, the side of sealing radiator and one end of step sedimentation tank
Connected by stainless steel tube, the other end of step sedimentation tank is connected with described filtrate water collection box phase one end by stainless steel tube,
The other end of filtrate water collection box draws a clear water pipeline, and clear water pipeline is connected with the ceramic filter.
2. according to a kind of ceramic filter drainage system described in claim 1, it is characterised in that the connection is seal pipe
Road connects.
3. according to a kind of ceramic filter drainage system described in claim 1, it is characterised in that the sealing radiator and vacuum
The difference in height of bucket is more than 10 meters.
4. according to a kind of ceramic filter drainage system described in claim 2, it is characterised in that the volume of the sealing radiator
To seal 2 times of piping volume sum.
5. according to a kind of ceramic filter drainage system described in claim 1, it is characterised in that the vacuum tank is that dome is true
Slack tank.
6. according to a kind of ceramic filter drainage system described in claim 1, it is characterised in that set above the sealing radiator
There is observation port, on observation port, add dust cover.
7. according to a kind of ceramic filter drainage system described in claim 1, it is characterised in that the sealing radiator bottom adds
If the running water outlet hole of point off density position.
8. according to a kind of ceramic filter drainage system described in claim 1, it is characterised in that set in the step sedimentation tank
Have a multi stage precipitation case, every grade of settling tank lower end adds blow-off pipe, blow-off pipe be connected to ore deposit case.
9. according to a kind of ceramic filter drainage system described in claim 1, it is characterised in that the filtrate water collection box
Volume should meet the water yield of the ceramic filter required for just starting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621113167.XU CN206063964U (en) | 2016-10-11 | 2016-10-11 | A kind of ceramic filter drainage system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621113167.XU CN206063964U (en) | 2016-10-11 | 2016-10-11 | A kind of ceramic filter drainage system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206063964U true CN206063964U (en) | 2017-04-05 |
Family
ID=58442148
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621113167.XU Expired - Fee Related CN206063964U (en) | 2016-10-11 | 2016-10-11 | A kind of ceramic filter drainage system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206063964U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002623A (en) * | 2019-05-05 | 2019-07-12 | 天津工业大学 | A kind of dye wastewater treatment precipitation adsorption purification device |
-
2016
- 2016-10-11 CN CN201621113167.XU patent/CN206063964U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002623A (en) * | 2019-05-05 | 2019-07-12 | 天津工业大学 | A kind of dye wastewater treatment precipitation adsorption purification device |
| CN110002623B (en) * | 2019-05-05 | 2023-11-21 | 天津工业大学 | Precipitation adsorption purification device for dye wastewater treatment |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170405 Termination date: 20171011 |