CN110143649A - A kind of two-way Fliod fluid decontamination system - Google Patents
A kind of two-way Fliod fluid decontamination system Download PDFInfo
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- CN110143649A CN110143649A CN201910575528.4A CN201910575528A CN110143649A CN 110143649 A CN110143649 A CN 110143649A CN 201910575528 A CN201910575528 A CN 201910575528A CN 110143649 A CN110143649 A CN 110143649A
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- solenoid valve
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4691—Capacitive deionisation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/005—Valves
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/05—Conductivity or salinity
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
Abstract
The present invention discloses a kind of two-way Fliod fluid decontamination system, it is related to sewage waste liquor field of purification, including purification device, it include the first clean unit and the second clean unit in the purification device, first clean unit and the second clean unit are equipped with condenser and contained structure, the circulation capacitor that the contained structure inner containment has one or more serial or parallel connections to be electrically connected, clean unit is set, the salt in solution is removed by the way of ionization, ammonia and other polarization pollutants, also to cooperate holding vessel to wash clean unit twice by hydraulic system, both played the role of to clean unit reactivation, the isolated ionizing particle of electricity is had collected again, and by the liquids recovery of the ionizing particle containing high concentration into holding vessel, convenient for subsequent discharge recycling, the first cleaning solution and the second cleaning solution are derived from source of supply in this system , do not need to introduce clean liquid from the external world, not need using filter material yet.
Description
Technical field
The present invention relates to sewage waste liquor field of purification, and in particular to a kind of two-way Fliod fluid decontamination system.
Background technique
As environmental protection is got more and more attention, requirement of the various regions to trade effluent discharging of waste liquid is also increasingly stringenter, because
This, enterprise generally requires first to purify and discharge again to sewage waste liquor, and the purification device and method of various sewage waste liquors also come into being.
The cost of major part sewage waste liquor purification is all more expensive at present, and cleaning equipment can may also generate secondary dirt
Dye, and the purification of most of sewage waste liquor be all it is simple depollute, can not accomplish recycling, i.e., violate again can for increasing cost
Sustainable development theory.
Particularly with the enterprise in chemical plant etc, the sewage waste liquor generated in industrial process is not only measured greatly, but also in waste liquid
Often containing a large amount of chloride, sulfate, nitrate, nitrite, ammonia and other polarization pollutants, these polluter sheets
Body is also the material that chemical plant needs.
Summary of the invention
The purpose of the present invention is to provide a kind of two-way Fliod fluid decontamination systems, clean unit are arranged, by the way of ionization
The salt in solution, ammonia and other polarization pollutants and chemical substance, organic substance or micropollutants are removed, also by hydraulic
System cooperation holding vessel washs clean unit twice, has not only played the role of to clean unit reactivation, but also have collected ionization
The ionizing particle of precipitation, and the liquids recovery of the ionizing particle containing high concentration is recycled into holding vessel convenient for subsequent discharge,
The first cleaning solution and the second cleaning solution are derived from source of supply in this system, do not need to introduce clean liquid from the external world, also not need
Using filter material, good purification of the present invention, and recycling is collected to pollutant, it will not be produced without expending other resources
Raw secondary pollution.
A kind of two-way Fliod fluid decontamination system, including purification device include the first clean unit and the in the purification device
Two clean units, first clean unit and the second clean unit are equipped with condenser and contained structure, the receiving knot
The circulation capacitor that structure inner containment has one or more serial or parallel connections to be electrically connected, fluid to be processed can circulate
Flowed between the electrode of capacitor, the conductive layer of the electrode of the circulation capacitor has several surface holes, the surface holes provide with
The attachment surface of fluid exchange；
It further include hydraulic system in the purification device, the hydraulic system includes source of supply, and source of supply is by always supplying
Pipeline supply stoste to be processed, and total supply line is subdivided into first supply pipe road and second supply pipe road respectively to the first purification
Unit and the second clean unit supply stoste to be processed, and are both provided with one on first supply pipe road and second supply pipe road
First solenoid valve is transported to the first extraction conduit and second by the liquid of the first clean unit and the second clean unit and extracts
In pipeline；
First extraction conduit is subdivided into first service branch and first and evacuates branch, and second extraction conduit is again
It is subdivided into second service branch and second and evacuates branch, the first service branch and second service branch are all connected to total service
Branch, total services branch are all connected to for purified liquid, the first evacuation branch to be discharged with the second evacuation branch
Branch is evacuated to total, total evacuations branch is connected to holding vessel, for the first scrub stream of conveying and the second cleaning solution, described the
Second solenoid valve one and second solenoid valve two, first evacuation point are respectively arranged on one services branch and second service branch
Third solenoid valve one and third solenoid valve two are respectively arranged in branch and the second evacuation branch；
The holding vessel conveys the first scrub stream by total conveyance conduit, and total conveyance conduit is subdivided into the first conveying point
Branch and the second conveying branches, first conveying branches and the second conveying branches are respectively communicated to first supply pipe road and second and supply
Pipeline is answered, and the first conveying branches and the second conveying branches are respectively arranged with the 4th solenoid valve one and the 4th solenoid valve two.
It preferably, further include logic control element, the logic control element is connected to conductivity sensor, the conductance
It there are two rate sensor is set, is separately positioned in the first extraction conduit and the second extraction conduit, is used to check the first extraction conduit
With the conductivity of fluid in the second extraction conduit, and logic control element is also connected to flowmeter, and the flowmeter also is provided with two
It is a, it is separately positioned on first supply pipe road and second supply pipe road, is used to check the first clean unit and the second clean unit
The stoste flow velocity of inlet.
Preferably, first clean unit and the second clean unit are also connected electrically to DC power supply, and the DC power supply passes through
Control circuit equipped with controller is connected to the electrode of circulation capacitor, and the controller is connect with logic control element, for controlling
System is applied to the voltage on the electrode of circulation capacitor.
Preferably, further include drive control device, the drive control device is connect with each solenoid valve, and drive control device also with
Logic control element is connected with controller, for controlling each electromagnetic valve work.
Preferably, the circulation capacitor is disposed with two or more superposed electrodes facing with each other, and electrode is flat
The flattened cylinder that discoid thin slice or coiling are formed.
Preferably, separation layer is set between the electrode of the circulation capacitor, the separation layer porous synthesizes material by what is insulated
Material or fibrous material are made, and include but are not limited to glass or nylon fabric.
Preferably, circulating pump is additionally provided on total conveyance conduit, the circulating pump can also be arranged in total evacuate and divide
Zhi Shang, to extract the first cleaning solution and the second cleaning solution from the first clean unit and the second clean unit and be sent to them
In holding vessel.
The present invention has the advantages that setting clean unit, removes the salt in solution, ammonia and other poles by the way of ionization
Change pollutant and chemical substance, organic substance or micropollutants, also by hydraulic system cooperation holding vessel to clean unit into
Row washs twice, has not only played the role of to clean unit reactivation, but also has collected the isolated ionizing particle of electricity, and will contain highly concentrated
The liquids recovery of the ionizing particle of degree is recycled into holding vessel convenient for subsequent discharge, and the first cleaning solution and second is washed in this system
It washs liquid and is derived from source of supply, do not need to introduce clean liquid from the external world, also not need using filter material, clean-up effect of the present invention
It is good, and recycling is collected to pollutant, secondary pollution will not be generated without expending other resources.
Detailed description of the invention
Fig. 1 is the structure principle chart of apparatus of the present invention；
Fig. 2 is the first clean unit work washing flow figure in the present invention；
Wherein, 1, purification device, the 2 ', first clean unit, the 2 ", second clean unit, 3, contained structure, 4, flow-thru electrode
Hold, 5, total supply line, 50 ', first supply pipe road, 50 ", second supply pipe road, the 60, first solenoid valve, the 7 ', first extraction tube
Road, the 7 ", second extraction conduit, 8 ', first service branch, 8 ", second service branch, 8, total services branch, the 9 ', first evacuation point
Branch, 9 ", second evacuates branch, and 9, always evacuate branch, 100 ', second solenoid valve one, 100 ", second solenoid valve two, 110 ', third
Solenoid valve one, 110 ", third solenoid valve two, 12, holding vessel, 13, total conveyance conduit, the 130 ', first conveyance conduit, 130 ",
Two conveyance conduits, the 140 ', the 4th solenoid valve one, the 140 ', the 4th solenoid valve two, 15, discharge tube, the 16, the 5th valve, 22, control
Device processed, 23, logic control element, 24, drive control device, 25, conductivity sensor, 26, flowmeter, 70, circulating pump, 200, confession
Ying Yuan.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to
Specific embodiment, the present invention is further explained.
As shown in Figure 1 to Figure 2, a kind of two-way Fliod fluid decontamination system, including purification device 1 include in the purification device 1
First clean unit 2' and the second clean unit 2 ", the first clean unit 2' and the second clean unit 2 " are equipped with condensation
Device and contained structure 3, the flow-thru electrode that 3 inner containment of contained structure has one or more serial or parallel connections to be electrically connected
Hold 4, fluid to be processed can flow between the electrode of circulation capacitor 4, and the conductive layer of the electrode of the circulation capacitor 4 has
Several surface holes, the surface holes provide the attachment surface with fluid exchange；The material for constituting conductive layer, which can be, to be become known for flowing
Any material of the electrochemical process of dynamic condenser, and sponge shaped activated carbon is generally included, such as from PTFE and carbon particle
Compliant conductive piece.
Constitute the size of the layers of separator material between the size of the conductive material layer of electrode, shape and distribution or insertion electrode
The theme of concrete right requirement is not constituted, because they are well known to those skilled in the art, no longer in detail
Thin description.
It further include hydraulic system in the purification device 1, the hydraulic system includes source of supply 200, and source of supply 200 passes through
Total supply line 50 supplies stoste to be processed, and total supply line 50 is subdivided into first supply pipe road 50' and second supply pipe road
50 " supply stoste to be processed to the first clean unit 2' and the second clean unit 2 " respectively, and first supply pipe road 50' and the
It is both provided with first solenoid valve 60 on two supply lines 50 ", passes through the first clean unit 2' and the second clean unit 2 "
Liquid is transported in the first extraction conduit 70' and the second extraction conduit 70 "；
The first extraction conduit 70' be subdivided into first service branch 80' and first evacuate branch 90', described second
Extraction conduit 70 " is subdivided into second service branch 80 " and second and evacuates branch 90 ", the first service branch 80' and second
Services branch 80 " is all connected to total services branch 8, and for purified liquid to be discharged, described first takes out total services branch 8
The evacuation of space division branch 90' and second branch 90 " is all connected to total evacuation branch 9, and total evacuation branch 9 is connected to holding vessel 12,
For conveying the first scrub stream and the second cleaning solution, it is respectively set in the first service branch 80' and second service branch 80 "
Have one 100' of second solenoid valve and second solenoid valve 2 100 ", the first evacuation branch 90' and second is evacuated to be divided in branch 90 "
It is not provided with one 110' of third solenoid valve and third solenoid valve 2 110 "；
The holding vessel 12 conveys the first scrub stream by total conveyance conduit 13, and total conveyance conduit 13 is subdivided into first
Conveying branches 130' and the second conveying branches 130 ", the first conveying branches 130' and the second conveying branches 130 " are respectively communicated with
To first supply pipe road 50' and second supply pipe road 50 ", and the first conveying branches 130' and the second conveying branches 130 " are set respectively
It is equipped with one 140' of the 4th solenoid valve and the 4th solenoid valve 2 140 ".Remove the salt in solution by the way of ionization, ammonia and other
Polarization pollutant and chemical substance, organic substance or micropollutants also cooperate holding vessel 12 net to two by hydraulic system
Change unit to be washed twice, not only play the role of to clean unit reactivation, but also have collected the isolated ionizing particle of electricity, and will
The liquids recovery of ionizing particle containing high concentration is recycled into holding vessel 12 convenient for subsequent discharge, the first washing in this system
Liquid and the second cleaning solution are derived from source of supply 200, do not need to introduce clean liquid from the external world, also not need using filter material.
It further include logic control element 23, the logic control element 23 is connected to conductivity sensor 25, the conductance
There are two rate sensor 25 is set, it is separately positioned in the first extraction conduit 70' and the second extraction conduit 70 ", is used to check first
The conductivity of fluid in extraction conduit 70' and the second extraction conduit 70 ", and logic control element 23 is also connected to flowmeter 26,
The flowmeter 26 also is provided with two, is separately positioned on first supply pipe road 50' and second supply pipe road 50 ", is used to check
The stoste flow velocity of the 2 " inlet first clean unit 2' and the second clean unit.Logic control element 23 can control this system
Work, controls the first clean unit 2' and the second clean unit 2 " purifies stoste, and switches and washed.
The first clean unit 2' and the second clean unit 2 " are also connected electrically to DC power supply, and the DC power supply is by being equipped with
The control circuit of controller 22 is connected to the electrode of circulation capacitor 4, and the controller 22 connect with logic control element 23, is used for
Control is applied to the voltage on the electrode of circulation capacitor 4.Controller 22 controls more accurately and rapidly.
Further include drive control device 24, the drive control device 24 is connect with each solenoid valve, and drive control device 24 also with
Logic control element 23 and controller 22 connect, for controlling each electromagnetic valve work.Drive control device 24 controls more accurately and rapidly.
The circulation capacitor 4 is disposed with two or more superposed electrodes facing with each other, and electrode is flattened round
The flattened cylinder that thin slice or coiling are formed.Facilitate collection ionizing particle.
Separation layer is set between the electrode of the circulation capacitor 4, and the separation layer is more by height non-conductive (insulating)
Hole synthetic material or fibrous material are made, and include but are not limited to glass or nylon fabric.Permission fluid can be isolated in separation layer
The electrode flowed through.
Circulating pump 70 is additionally provided on total conveyance conduit 13, total evacuation branch can also be arranged in the circulating pump 70
On 9, with extracted from the first clean unit 2' and the second clean unit 2 " the first cleaning solution and the second cleaning solution and by they
It is sent in holding vessel 12.Position, which is arranged, in circulating pump 70 to be adjusted flexibly.
Specific embodiment and principle:
First clean unit 2' for being purified to the stoste in source of supply 200, to the stoste in source of supply 200 into
Before row purification, first passing through control circuit makes circulation capacitor 4 be in the charging stage, waits the circulation capacitor 4 in the first clean unit 2'
Expected operating voltage, about 1.6V are loaded and reached, into working stage, is then controlled accordingly by drive control device 24
Solenoid valve open and close, first supply pipe road 50' and first service branch 80' is connected, and the first conveying branches 130'
It evacuates branch 90' with first to disconnect, the stoste in source of supply 200 flows to clean unit 2 by supply line 5, clean unit 2
Capacitor 4 circulate during working stage, therefore the particle ionized is attracted with the polar respective electrode opposite with them, is led
Ionizing particle building up in identical electrodes, so that the purification of stoste occur；
As purification carries out, the electrode of circulation capacitor 4 can be increasingly saturated, and will have polarizable particles in fluid, immediately
Into regeneration stage, at this stage period, disconnect the first evacuation branch 90', and first supply pipe road 50', the first conveying point
Branch 130' and first service branch 80' conducting, the first scrub stream flow out into the first clean unit 2' from holding vessel 12, force
Include the cleaned stoste in the first clean unit 2' and in extraction conduit 7 towards the diffluence of services branch 8, is then shut off institute
There is a valve, then discharge regime is again at by the control circuit capacitor 4 that makes to circulate, then by first supply pipe road 50', first defeated
Branch 130' and first is sent to evacuate branch 90' conducting, first service branch 80' disconnection, the first scrub stream is left holding vessel 12, worn
The first clean unit 2', the ionizing particle of removal accumulation on the electrode are crossed, and is transmitted back to holding vessel 12, carries out the first scrub stream
Circulation；
After the first scrub stream recycles a period of time, the first conveying branches 130', first are evacuated into branch 90' conducting, the
One conveying branches 130' and first service branch 80' is disconnected, and source of supply 200 flows out stoste and serves as the second scrub stream, the second washing
Stream flows to the first clean unit 2', flow back into holding vessel 12 until by the first evacuation branch 90', the second scrub stream can be
Replacement is present in the first scrub stream of high concentration ionizing particle in first clean unit 2', and it can also remove and be still in
The residual ionizing particle to circulate on the electrode of capacitor 4, when liquid reaches horizontal quota in holding vessel 12, or when setting interval
Between and after interval time reaches, open the 5th valve 16 with the ionizing particle containing high concentration inside certain flow rate discharge holding vessel 12
Liquid, and the second washing flow velocity for reaching holding vessel 12 is substantially equal to the concentration being discharged by delivery pipe 15 from holding vessel 12
The flow velocity of fluid, which is set smaller than 5% of the overall flow rate from the first clean unit 2' processing and the fluid purified, optimal
Choosing is set as 2%；
Finally so that circulation capacitor 4 is first in the no-voltage stage for a period of time by control circuit again, is then again introduced into and fills
The electric stage waits the circulation capacitor 4 in the first clean unit 2' to load and reaches expected operating voltage, into work rank
Then section is connected first supply pipe road 50' and first service branch 80', and the first conveying branches 130' and first is evacuated and divided
Branch 90' is disconnected, and carries out stoste purification again, while being switched to the second clean unit 2 " and starting to wash；
The washing process and principle of second clean unit 2 " are identical as the washing process of the first clean unit 2' and principle, and two
One progress stoste of person purifies another and washs, and switching staggeredly carries out.
Based on above-mentioned, clean unit is arranged in the present invention, and the salt in solution, ammonia and other polarization are removed by the way of ionization
Pollutant and chemical substance, organic substance or micropollutants also cooperate holding vessel to carry out clean unit by hydraulic system
It washs, has not only played the role of to clean unit reactivation twice, but also have collected the isolated ionizing particle of electricity, and high concentration will be contained
Ionizing particle liquids recovery into holding vessel, recycled convenient for subsequent discharge, the first cleaning solution and second washs in this system
Liquid is derived from source of supply, does not need to introduce clean liquid from the external world, also not need using filter material, clean-up effect of the present invention
It is good, and recycling is collected to pollutant, secondary pollution will not be generated without expending other resources.
As known by the technical knowledge, the present invention can pass through the embodiment party of other essence without departing from its spirit or essential feature
Case is realized.Therefore, embodiment disclosed above, in all respects are merely illustrative, not the only.Institute
Have within the scope of the present invention or is included in the invention in the change being equal in the scope of the present invention.
Claims (7)
1. a kind of two-way Fliod fluid decontamination system, which is characterized in that include the in the purification device (1) including purification device (1)
(2') with the second clean unit (2 "), (2') first clean unit is all equipped with one clean unit with the second clean unit (2 ")
There are condenser and contained structure (3), contained structure (3) inner containment there are one or more serial or parallel connections to be connected electrically in one
The circulation capacitor (4) risen, fluid to be processed can flow between the electrode of circulation capacitor (4), circulation capacitor (4)
The conductive layer of electrode has several surface holes, and the surface holes provide the attachment surface with fluid exchange；
It further include hydraulic system in the purification device (1), the hydraulic system includes source of supply (200), and source of supply (200) is logical
It crosses total supply line (50) and supplies stoste to be processed, and total supply line (50) is subdivided into first supply pipe road (50') and second
(2') supply line (50 ") supplies stoste to be processed, and first to the first clean unit respectively with the second clean unit (2 ")
It is both provided with first solenoid valve (60) on supply line (50') and second supply pipe road (50 "), passes through the first clean unit
(2') it is transported in the first extraction conduit (70') and the second extraction conduit (70 ") with the liquid of the second clean unit (2 ")；
First extraction conduit (70') is subdivided into first service branch (80') and first and evacuates branch (90'), and described the
Two extraction conduits (70 ") are subdivided into second service branch (80 ") and second and evacuate branch (90 "), the first service branch
(80') and second service branch (80 ") are all connected to total services branch (8), after total services branch (8) is for being discharged purification
Liquid, described first, which evacuates branch (90') and second, evacuates branch (90 ") and is all connected to total evacuation branch (9), total pumping
Space division branch (9) is connected to holding vessel (12), for conveying the first scrub stream and the second cleaning solution, the first service branch
Second solenoid valve one (100') and second solenoid valve two (100 "), institute are respectively arranged in (80') and second service branch (80 ")
It states and is respectively arranged with third solenoid valve one (110') and third electricity in the first evacuation branch (90') and the second evacuation branch (90 ")
Magnet valve two (110 ")；
The holding vessel (12) conveys the first scrub stream by total conveyance conduit (13), and total conveyance conduit (13) is subdivided into the
One conveying branches (130') and the second conveying branches (130 "), first conveying branches (130') and the second conveying branches
(130 ") are respectively communicated to first supply pipe road (50') and second supply pipe road (50 "), and the first conveying branches (130') and
Two conveying branches (130 ") are respectively arranged with the 4th solenoid valve one (140') and the 4th solenoid valve two (140 ").
2. a kind of two-way Fliod fluid decontamination system according to claim 1, it is characterised in that: further include logic control element
(23), the logic control element (23) is connected to conductivity sensor (25), there are two the conductivity sensor (25) sets,
Be separately positioned in the first extraction conduit (70') and the second extraction conduit (70 "), be used to check the first extraction conduit (70') and
The conductivity of the second interior fluid of extraction conduit (70 "), and logic control element (23) is also connected to flowmeter (26), the flow
Meter (26) also is provided with two, is separately positioned on first supply pipe road (50') and second supply pipe road (50 "), is used to check the
The one clean unit (2') stoste flow velocity with second clean unit (2 ") inlet.
3. a kind of two-way Fliod fluid decontamination system according to claim 2, it is characterised in that: first clean unit is (2')
It is also connected electrically to DC power supply with the second clean unit (2 "), the DC power supply is connected by being equipped with the control circuit of controller (22)
To the electrode of circulation capacitor (4), the controller (22) connect with logic control element (23), is applied to flow-thru electrode for controlling
Hold the voltage on the electrode of (4).
4. a kind of two-way Fliod fluid decontamination system according to claim 3, it is characterised in that: further include drive control device
(24), the drive control device (24) connect with each solenoid valve, and drive control device (24) also with logic control element (23) and
Controller (22) connection, for controlling each electromagnetic valve work.
5. a kind of two-way Fliod fluid decontamination system according to claim 1, it is characterised in that: the circulation capacitor (4) is successively
Two or more superposed electrodes facing with each other are provided with, electrode is flattened round thin slice or the flattened cylindrical that coiling is formed
Body.
6. a kind of two-way Fliod fluid decontamination system according to claim 1, it is characterised in that: the electricity of circulation capacitor (4)
Separation layer is set between pole, and the separation layer is made of the porous synthetic material or fibrous material insulating, includes but are not limited to
Glass or nylon fabric.
7. a kind of two-way Fliod fluid decontamination system according to claim 1, it is characterised in that: on total conveyance conduit (13)
Be additionally provided with circulating pump (70), the circulating pump (70) can also be arranged in it is total evacuate on branch (9), with from the first clean unit
With extract the first cleaning solution and the second cleaning solution in the second clean unit (2 ") and they be sent in holding vessel (12).
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| CN201910575528.4A CN110143649B (en) | 2019-06-28 | 2019-06-28 | Double-circuit fluid purification system |
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Citations (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10156344A (en) * | 1996-10-03 | 1998-06-16 | Toray Ind Inc | Water purifier, fresh water generator and washing method therefor |
| US6346187B1 (en) * | 1999-01-21 | 2002-02-12 | The Regents Of The University Of California | Alternating-polarity operation for complete regeneration of electrochemical deionization system |
| US20030098266A1 (en) * | 2001-09-07 | 2003-05-29 | Lih-Ren Shiue | Fully automatic and energy-efficient deionizer |
| EP1348670A1 (en) * | 2002-03-27 | 2003-10-01 | Luxon Energy Devices Corporation | Fully automatic and energy-efficient capacitive deionizer |
| CN101331088A (en) * | 2005-12-14 | 2008-12-24 | 通用电气公司 | Supercapacitor desalination devices |
| CN101563296A (en) * | 2006-12-19 | 2009-10-21 | 通用电气公司 | Supercapacitor desalination device and method of making |
| CN101595064A (en) * | 2007-02-01 | 2009-12-02 | 通用电气公司 | The desalting method and the device that comprise electrode of super capacitor |
| US20110024354A1 (en) * | 2009-07-30 | 2011-02-03 | General Electric Company | Desalination system and method |
| CN102030393A (en) * | 2010-10-28 | 2011-04-27 | 常州爱思特净化设备有限公司 | Electro-adsorption desalination energy-saving system and method |
| CN102167463A (en) * | 2010-02-26 | 2011-08-31 | 通用电气公司 | Water disposal facility and method |
| CN102211803A (en) * | 2010-04-09 | 2011-10-12 | 苏润西 | Device for separating electro-adsorption water-based solution ions and operation method thereof |
| CN102545390A (en) * | 2010-12-28 | 2012-07-04 | 通用电气公司 | Charging or discharging system and method |
| WO2012090062A1 (en) * | 2010-12-29 | 2012-07-05 | Idropan Dell'orto Depuratori S.R.L. | Flow-through capacitor assembly for the treatment of a fluid |
| CN102689951A (en) * | 2012-06-12 | 2012-09-26 | 爱思特水务科技有限公司 | Electric adsorption system, electric adsorption module modified system and corresponding method |
| CN102863055A (en) * | 2011-07-08 | 2013-01-09 | 通用电气公司 | Desalting system and method |
| CN103130363A (en) * | 2011-11-28 | 2013-06-05 | 通用电气公司 | Desalination system and desalination method |
| CN103130362A (en) * | 2011-11-23 | 2013-06-05 | 通用电气公司 | Water treatment device and method |
| CN103269982A (en) * | 2010-12-30 | 2013-08-28 | 豪威株式会社 | Water treatment apparatus and water treatment method using the same |
| CN104023812A (en) * | 2011-12-29 | 2014-09-03 | 豪威株式会社 | Apparatus for water treatment using capacitive deionization and method for controlling the same |
| CN104520242A (en) * | 2012-06-27 | 2015-04-15 | 皇家飞利浦有限公司 | An apparatus and a method of generating bubbles and foams |
| KR20150042481A (en) * | 2013-10-11 | 2015-04-21 | 이종화 | The Seawater desalinatipn system using energy cross and reuse in capacitive double electrolytic cell |
| CN106006869A (en) * | 2016-06-27 | 2016-10-12 | 南京师范大学 | Capacitance desalter provided with cross diversion pipes |
| CN107406282A (en) * | 2015-03-20 | 2017-11-28 | 艺康美国股份有限公司 | System and method for the capacitive deionization of fluid |
| CN107531520A (en) * | 2015-04-14 | 2018-01-02 | 皇家飞利浦有限公司 | Electro Sorb cleaning system with recycling |
| CN107624106A (en) * | 2015-01-16 | 2018-01-23 | Dwi莱布尼茨互动材料研究所协会 | The method of continuous water desalination and ion isolation is carried out by capacitive deionization and its single module flows electrode assembly |
| KR20190036428A (en) * | 2017-09-27 | 2019-04-04 | 주식회사 경동나비엔 | Boiler and water heating device |
| CN109678259A (en) * | 2017-10-18 | 2019-04-26 | 罗伯特·博世有限公司 | Device and method for making fluid deionization |
| CN111936428A (en) * | 2018-04-05 | 2020-11-13 | 三菱电机株式会社 | Water treatment device and water treatment method |
-
2019
- 2019-06-28 CN CN201910575528.4A patent/CN110143649B/en active Active
Patent Citations (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10156344A (en) * | 1996-10-03 | 1998-06-16 | Toray Ind Inc | Water purifier, fresh water generator and washing method therefor |
| US6346187B1 (en) * | 1999-01-21 | 2002-02-12 | The Regents Of The University Of California | Alternating-polarity operation for complete regeneration of electrochemical deionization system |
| US20030098266A1 (en) * | 2001-09-07 | 2003-05-29 | Lih-Ren Shiue | Fully automatic and energy-efficient deionizer |
| EP1348670A1 (en) * | 2002-03-27 | 2003-10-01 | Luxon Energy Devices Corporation | Fully automatic and energy-efficient capacitive deionizer |
| CN101331088A (en) * | 2005-12-14 | 2008-12-24 | 通用电气公司 | Supercapacitor desalination devices |
| CN101563296A (en) * | 2006-12-19 | 2009-10-21 | 通用电气公司 | Supercapacitor desalination device and method of making |
| CN101595064A (en) * | 2007-02-01 | 2009-12-02 | 通用电气公司 | The desalting method and the device that comprise electrode of super capacitor |
| US20110024354A1 (en) * | 2009-07-30 | 2011-02-03 | General Electric Company | Desalination system and method |
| CN102167463A (en) * | 2010-02-26 | 2011-08-31 | 通用电气公司 | Water disposal facility and method |
| CN102211803A (en) * | 2010-04-09 | 2011-10-12 | 苏润西 | Device for separating electro-adsorption water-based solution ions and operation method thereof |
| CN102030393A (en) * | 2010-10-28 | 2011-04-27 | 常州爱思特净化设备有限公司 | Electro-adsorption desalination energy-saving system and method |
| CN102545390A (en) * | 2010-12-28 | 2012-07-04 | 通用电气公司 | Charging or discharging system and method |
| WO2012090062A1 (en) * | 2010-12-29 | 2012-07-05 | Idropan Dell'orto Depuratori S.R.L. | Flow-through capacitor assembly for the treatment of a fluid |
| CN103269982A (en) * | 2010-12-30 | 2013-08-28 | 豪威株式会社 | Water treatment apparatus and water treatment method using the same |
| CN102863055A (en) * | 2011-07-08 | 2013-01-09 | 通用电气公司 | Desalting system and method |
| CN103130362A (en) * | 2011-11-23 | 2013-06-05 | 通用电气公司 | Water treatment device and method |
| CN103130363A (en) * | 2011-11-28 | 2013-06-05 | 通用电气公司 | Desalination system and desalination method |
| CN104023812A (en) * | 2011-12-29 | 2014-09-03 | 豪威株式会社 | Apparatus for water treatment using capacitive deionization and method for controlling the same |
| CN102689951A (en) * | 2012-06-12 | 2012-09-26 | 爱思特水务科技有限公司 | Electric adsorption system, electric adsorption module modified system and corresponding method |
| CN104520242A (en) * | 2012-06-27 | 2015-04-15 | 皇家飞利浦有限公司 | An apparatus and a method of generating bubbles and foams |
| KR20150042481A (en) * | 2013-10-11 | 2015-04-21 | 이종화 | The Seawater desalinatipn system using energy cross and reuse in capacitive double electrolytic cell |
| CN107624106A (en) * | 2015-01-16 | 2018-01-23 | Dwi莱布尼茨互动材料研究所协会 | The method of continuous water desalination and ion isolation is carried out by capacitive deionization and its single module flows electrode assembly |
| CN107406282A (en) * | 2015-03-20 | 2017-11-28 | 艺康美国股份有限公司 | System and method for the capacitive deionization of fluid |
| CN107531520A (en) * | 2015-04-14 | 2018-01-02 | 皇家飞利浦有限公司 | Electro Sorb cleaning system with recycling |
| CN106006869A (en) * | 2016-06-27 | 2016-10-12 | 南京师范大学 | Capacitance desalter provided with cross diversion pipes |
| KR20190036428A (en) * | 2017-09-27 | 2019-04-04 | 주식회사 경동나비엔 | Boiler and water heating device |
| CN109678259A (en) * | 2017-10-18 | 2019-04-26 | 罗伯特·博世有限公司 | Device and method for making fluid deionization |
| CN111936428A (en) * | 2018-04-05 | 2020-11-13 | 三菱电机株式会社 | Water treatment device and water treatment method |
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