CN110240231A - A kind of Fliod fluid decontamination system and purification method - Google Patents
A kind of Fliod fluid decontamination system and purification method Download PDFInfo
- Publication number
- CN110240231A CN110240231A CN201910574630.2A CN201910574630A CN110240231A CN 110240231 A CN110240231 A CN 110240231A CN 201910574630 A CN201910574630 A CN 201910574630A CN 110240231 A CN110240231 A CN 110240231A
- Authority
- CN
- China
- Prior art keywords
- solenoid valve
- clean unit
- holding vessel
- purification
- fluid
- 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.)
- Granted
Links
- 238000000746 purification Methods 0.000 title claims abstract description 57
- 239000012530 fluid Substances 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000005202 decontamination Methods 0.000 title claims abstract description 11
- 230000003588 decontaminative effect Effects 0.000 title claims abstract description 11
- 239000003990 capacitor Substances 0.000 claims abstract description 53
- 239000002245 particle Substances 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 238000004140 cleaning Methods 0.000 claims abstract description 23
- 230000010287 polarization Effects 0.000 claims abstract description 5
- 238000000605 extraction Methods 0.000 claims description 11
- 238000000926 separation method Methods 0.000 claims description 7
- 238000009825 accumulation Methods 0.000 claims description 5
- 230000008929 regeneration Effects 0.000 claims description 5
- 238000011069 regeneration method Methods 0.000 claims description 5
- 239000004677 Nylon Substances 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims description 3
- 239000002657 fibrous material Substances 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 229920001778 nylon Polymers 0.000 claims description 3
- 229920002994 synthetic fiber Polymers 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 12
- 239000000126 substance Substances 0.000 abstract description 11
- 230000005611 electricity Effects 0.000 abstract description 9
- 239000003344 environmental pollutant Substances 0.000 abstract description 9
- 231100000719 pollutant Toxicity 0.000 abstract description 9
- 239000002699 waste material Substances 0.000 abstract description 9
- 238000004064 recycling Methods 0.000 abstract description 7
- 239000010865 sewage Substances 0.000 abstract description 7
- 229910021529 ammonia Inorganic materials 0.000 abstract description 6
- 230000007420 reactivation Effects 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 5
- 150000003839 salts Chemical class 0.000 abstract description 5
- 238000001914 filtration Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 9
- 238000005406 washing Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Classifications
-
- 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
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
-
- 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
-
- 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
- C02F1/4608—Treatment of water, waste water, or sewage by electrochemical methods using electrical discharges
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- 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
- C02F2201/46—Apparatus for electrochemical processes
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Electrostatic Separation (AREA)
Abstract
The present invention discloses a kind of Fliod fluid decontamination system and purification method, it is related to sewage waste liquor field of purification, including purification device, it include a clean unit in the purification device, the clean unit is 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, the salt in solution is removed by the way of ionization, ammonia and other polarization pollutants, also holding vessel is cooperated 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, it does not need to introduce clean liquid from the external world, it does not need using filtering yet Substance.
Description
Technical field
The present invention relates to sewage waste liquor field of purification, and in particular to a kind of Fliod fluid decontamination system and purification method.
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 Fliod fluid decontamination system and purification methods, clean unit are arranged, using ionization
Mode remove the salt in solution, ammonia and other polarization pollutants and chemical substance, organic substance or micropollutants are also logical
It crosses hydraulic system cooperation holding vessel to wash clean unit twice, not only play the role of to clean unit reactivation, but also collect
Electric isolated ionizing particle, and the liquids recovery of the ionizing particle containing high concentration is convenient for subsequent discharge into holding vessel
It recycling, the first cleaning solution and the second cleaning solution are derived from source of supply in this system, it does not need to introduce clean liquid from the external world,
It does not need using filter material, good purification of the present invention, and recycling is collected to pollutant, does not have to expend other resources
Secondary pollution will not be generated.
A kind of Fliod fluid decontamination system and purification method, including purification device, include in the purification device purification singly
Member, the clean unit equipped with condenser and contained structure, the contained structure inner containment have it is one or more connect or
The circulation capacitor that parallel connection is electrically connected, fluid to be processed can flow between the electrode of circulation capacitor, and purify single
Member is also connected electrically to DC power supply, the electrode that the DC power supply is connected to circulation capacitor by being equipped with the control circuit of controller, institute
The conductive layer for stating the electrode of circulation capacitor has several surface holes, and the surface holes provide the attachment surface with fluid exchange；
Further include hydraulic system in the purification device, the hydraulic system by supply line to clean unit supply to
The fluid of processing, supply line obtain untreated stoste from source of supply and are intercepted by the first solenoid valve, and stoste passes through purification
It is transported in extraction conduit after unit, extraction conduit is subdivided into services branch and evacuates branch, and the services branch is by the
Two solenoid valves intercept, and for the stoste after transport process, the evacuation branch is intercepted by third solenoid valve, wash for conveying first
Wash stream and the second cleaning solution；
It further include holding vessel in the purification device, the holding vessel is existed by the conveyance conduit intercepted by the 4th solenoid valve
Exit is hydraulically connected to supply line, and circulating pump is provided on the conveyance conduit, and the holding vessel is also connected in input terminal
To evacuation branch, and holding vessel is also connected with the delivery pipe intercepted by the 5th valve.
Preferably, the circulation capacitor 4 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 described and the capacitor 4 that circulates electrode, the separation layer porous is synthesized by what is insulated
Material or fibrous material are made, and include but are not limited to glass or nylon fabric.
Preferably, the circulating pump 70, which can also be arranged in, evacuates in branch 9, to extract first from clean unit 2
They are simultaneously sent in holding vessel 12 by cleaning solution and the second cleaning solution.
Preferably, a kind of fluid purification, it is characterised in that: steps are as follows:
Step 1: first passing through control circuit makes circulation capacitor 4 be in the charging stage, waits the circulation capacitor 4 in clean units 2
Expected operating voltage is loaded and reached, into working stage, is then opened the first solenoid valve 6 and second solenoid valve 10
And third solenoid valve 11 and the 4th solenoid valve 14 are closed, the stoste in source of supply 100 flows to clean unit 2 by supply line 5,
The circulation capacitor 4 of clean unit 2 during working stage, therefore the particle ionized had it is opposite polar corresponding to them
Electrode attracts, and leads to ionic particles building up in identical electrodes, so that the purification of stoste occur；
Step 2: as purification carries out, once the electrode of circulation capacitor 4 reaches program saturation, there will be pole in fluid
Change particle, enter regeneration stage immediately, at this stage during, first the first solenoid valve 16 and third solenoid valve 11 are closed and the
Two solenoid valves 10 and the 4th solenoid valve 14 are opened, and the first scrub stream flows out into supply line 5 from holding vessel 12, are forced and are included
Cleaned stoste in clean unit 2 and in extraction conduit 7 is flowed away towards services branch 8, is then shut off all valves；
Step 3: circulation capacitor 4 is made to be again at discharge regime by control circuit again, then by 11 He of third solenoid valve
4th solenoid valve 14 is opened and the first solenoid valve 16 and second solenoid valve 10 remain turned-off, and the first scrub stream leaves holding vessel 12,
Across clean unit 2, the ionizing particle of removal accumulation on the electrode, and it is transmitted back to holding vessel 12, carries out the first scrub stream and follow
Ring；
Step 4: after the first scrub stream recycles a period of time, second solenoid valve 10 and the 4th solenoid valve 14 are closed simultaneously
And first solenoid valve 16 and third solenoid valve 11 when opening, source of supply 100 flows out stoste and serves as the second scrub stream, the second scrub stream
Clean unit 2 is flowed to by supply line 5, is flow back into holding vessel 12 until by evacuating branch 9, the second scrub stream can be
Replacement is present in the first scrub stream of high concentration ionizing particle in clean unit 2, and it can also remove and be still in circulation
Residual ionizing particle on the electrode of capacitor 4；
Step 5: finally circulation capacitor 4 is made first to be in the no-voltage stage for a period of time by control circuit again, then again
Into the charging stage, waits the circulation capacitor 4 in clean units 2 to load and reach expected operating voltage, into work rank
Then first solenoid valve 16 and second solenoid valve 10 are opened and third solenoid valve 11 and the 4th solenoid valve 14 are closed, again by section
Carry out stoste purification.
Preferably, when liquid reaches horizontal quota in holding vessel 12, or setting interval time and interval time reach
Afterwards, the 5th valve 16 is opened with the ionizing particle liquid containing high concentration inside certain flow rate discharge holding vessel 12.
Preferably, the second washing flow velocity for reaching holding vessel 12 is substantially equal to through delivery pipe 15 from 12 row of holding vessel
The flow velocity of concentrating streams out, the flow velocity are set smaller than 5% of the overall flow rate from the processing of clean unit 2 and the fluid purified,
Most preferably it is set as 2%.
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 purification method flow chart of the invention；
Wherein, 1, purification device, 2, clean unit, 3, contained structure, 4, circulation capacitor, 5, supply line, the 6, first electricity
Magnet valve, 7, extraction conduit, 8, services branch, 9, evacuation branch, 10, second solenoid valve, 11, third solenoid valve, 12, holding vessel,
13, conveyance conduit, the 14, the 4th solenoid valve, 15, discharge tube, the 16, the 5th valve, 36, DC power supply, 70, circulating pump, 100, 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 Fliod fluid decontamination system and purification method, including purification device 1, the purification device 1
In include a clean unit 2, the clean unit 2 holds inside the contained structure 3 equipped with condenser and contained structure 3
The circulation capacitor 4 that one or more serial or parallel connections of receiving are electrically connected, fluid to be processed can be in circulation capacitors 4
It is flowed between electrode, and clean unit 2 is also connected electrically to DC power supply 36, the DC power supply 36 is electric by the control for being equipped with controller
Road is connected to 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
Attachment surface with fluid exchange is provided；The material for constituting conductive layer can be the electrochemical process for becoming known for flow condensation device
Any material, such as sponge shaped activated carbon.
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 is supplied by supply line 5 to clean unit 2
To fluid to be processed, supply line 5 obtains untreated stoste from source of supply 100 and is intercepted by the first solenoid valve 6, stoste
By being transported in extraction conduit 7 after clean unit 2, extraction conduit 7 is subdivided into services branch 8 and evacuates branch 9, described
Services branch 8 is intercepted by second solenoid valve 10, and for the stoste after transport process, the evacuation branch 9 is by third solenoid valve 11
It intercepts, for conveying the first scrub stream and the second cleaning solution；
It further include holding vessel 12 in the purification device 1, the holding vessel 12 is defeated by being intercepted by the 4th solenoid valve 14
It send pipeline 13 to be hydraulically connected to supply line 5 in exit, circulating pump 70, the holding vessel is provided on the conveyance conduit 13
12 are also connected to evacuation branch 9 in input terminal, and holding vessel 12 is also connected with the delivery pipe 15 intercepted by the 5th valve 16.Using electricity
From mode remove the salt in solution, ammonia and other polarization pollutants and chemical substance, organic substance or micropollutants, also
Cooperate holding vessel 12 to wash clean unit 2 twice by hydraulic system, both played the role of to 2 reactivation of clean unit,
The isolated ionizing particle of electricity is had collected again, and the liquids recovery of the ionizing particle containing high concentration is convenient for into holding vessel 12
Subsequent discharge recycles, and the first cleaning solution and the second cleaning solution are derived from source of supply 100 in this system, does not need to introduce from the external world
Clean liquid is not needed using filter material yet.
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 described and the capacitor 4 that circulates electrode, the separation layer by the porous synthetic material that insulate or
Fibrous material is made, and includes but are not limited to glass or nylon fabric.The electricity for allowing fluid to flow through can be isolated in separation layer
Pole.
The circulating pump 70 can also be arranged in evacuate branch 9 on, with extracted from clean unit 2 first cleaning solution and
They are simultaneously sent in holding vessel 12 by the second cleaning solution.Position, which is arranged, in circulating pump 70 to be adjusted flexibly.
A kind of fluid purification, it is characterised in that: steps are as follows:
Step 1: first passing through control circuit makes circulation capacitor 4 be in the charging stage, waits the circulation capacitor 4 in clean units 2
Expected operating voltage is loaded and reached, into working stage, is then opened the first solenoid valve 6 and second solenoid valve 10
And third solenoid valve 11 and the 4th solenoid valve 14 are closed, the stoste in source of supply 100 flows to clean unit 2 by supply line 5,
The circulation capacitor 4 of clean unit 2 during working stage, therefore the particle ionized had it is opposite polar corresponding to them
Electrode attracts, and leads to ionic particles building up in identical electrodes, so that the purification of stoste occur；
Step 2: as purification carries out, once the electrode of circulation capacitor 4 reaches program saturation, (i.e. saturation state is saturated shape
The ability of electrode adsorption ion can weaken significantly under state), there will be polarizable particles in fluid, enter regeneration stage immediately,
During the stage, first the first solenoid valve 16 and third solenoid valve 11 are closed and second solenoid valve 10 and the 4th solenoid valve 14 are beaten
It opens, the first scrub stream flows out into supply line 5 from holding vessel 12, forces included in clean unit 2 and in extraction conduit 7
Cleaned stoste towards services branch 8 flow away, be then shut off all valves；
Step 3: circulation capacitor 4 is made to be again at discharge regime by control circuit again, then by 11 He of third solenoid valve
4th solenoid valve 14 is opened and the first solenoid valve 16 and second solenoid valve 10 remain turned-off, and the first scrub stream leaves holding vessel 12,
Across clean unit 2, the ionizing particle of removal accumulation on the electrode, and it is transmitted back to holding vessel 12, carries out the first scrub stream and follow
Ring；
Step 4: after the first scrub stream recycles a period of time, second solenoid valve 10 and the 4th solenoid valve 14 are closed simultaneously
And first solenoid valve 16 and third solenoid valve 11 when opening, source of supply 100 flows out stoste and serves as the second scrub stream, the second scrub stream
Clean unit 2 is flowed to by supply line 5, is flow back into holding vessel 12 until by evacuating branch 9, the second scrub stream can be
Replacement is present in the first scrub stream of high concentration ionizing particle in clean unit 2, and it can also remove and be still in circulation
Residual ionizing particle on the electrode of capacitor 4；
Step 5: finally circulation capacitor 4 is made first to be in the no-voltage stage for a period of time by control circuit again, then again
Into the charging stage, waits the circulation capacitor 4 in clean units 2 to load and reach expected operating voltage, into work rank
Then first solenoid valve 16 and second solenoid valve 10 are opened and third solenoid valve 11 and the 4th solenoid valve 14 are closed, again by section
Carry out stoste purification.
Charging stage, wherein the circulation capacitor 4 in clean unit 2 loads and reaches expected operating voltage, such as
Equal to 1.6V, and enter working stage, wherein fluid stream to be processed is forced through in the case where loading electrode, purification
For the circulation capacitor 4 of unit 2 during working stage, the particle due to ionization is had the polar respective electrode opposite with them
Attract, lead to ionic particles building up in identical electrodes, so that the purification of the fluid from polarizable particles occur.
The unit period (the unit period refers to: system carries out stoste purification-clean unit washing-and carries out stoste purification again)
A regeneration stage is provided, once reaching the program saturation of electrode, polarizable particles present in fluid will be reached.In the rank
During section, in the case where electrode deactivates, cleaning solution is forced into clean unit 2, then removes the ionization of accumulation on the electrode
Particle.
Liquid reaches horizontal quota (corresponding liquid level sensor, but holding vessel 12 is arranged in holding vessel 12 in holding vessel 12
Middle liquid level, which reaches, specifies high Du Shi to reach horizontal quota) when, or setting interval time and after interval time reaches, it beats
The 5th valve 16 is opened with the ionizing particle liquid containing high concentration inside certain flow rate discharge holding vessel 12.Carry out recycling and reusing.
The the second washing flow velocity for reaching holding vessel 12 be substantially equal to through delivery pipe 15 be discharged from holding vessel 12 it is dense
The flow velocity of contracting fluid, the flow velocity are set smaller than 5% of the overall flow rate from the processing of clean unit 2 and the fluid purified, most preferably
It is set as 2%.Second cleaning solution can replace the ionizing particle liquid that holding vessel 12 includes high concentration, next time clear for serving as
Wash the first cleaning solution when clean unit 2.
Specific embodiment and principle:
Before purifying to the stoste in source of supply 100, first passing through control circuit makes to circulate capacitor 4 in charging rank
Section waits circulation capacitor 4 in clean units 2 to load and reaches expected operating voltage, about 1.6V, into working stage,
Then the first solenoid valve 6 and second solenoid valve 10 are opened and third solenoid valve 11 and the 4th solenoid valve 14 is closed, source of supply 100
In stoste clean unit 2 is flowed to by supply line 5, the circulation capacitor 4 of clean unit 2 is during working stage, therefore electricity
From particle by with opposite with them polar respective electrode attraction, lead to ionic particles gradually tiring out in identical electrodes
Product, so that the purification of stoste occur；
As purification carries out, once the electrode of circulation capacitor 4 reaches program saturation, there will be polarizable particles in fluid,
Enter regeneration stage immediately, at this stage period, first by the first solenoid valve 16 and the closing of third solenoid valve 11 and the second electromagnetism
Valve 10 and the 4th solenoid valve 14 are opened, and the first scrub stream flows out into supply line 5 from holding vessel 12, are forced and are included in purification
Cleaned stoste in unit 2 and in extraction conduit 7 is flowed away towards services branch 8, is then shut off all valves, then pass through control
Circuit processed makes circulation capacitor 4 be again at discharge regime, then by third solenoid valve 11 and the 4th solenoid valve 14 opening and first
Solenoid valve 16 and second solenoid valve 10 remain turned-off, and the first scrub stream leaves holding vessel 12, pass through clean unit 2, removal accumulation
Ionizing particle on the electrode, and it is transmitted back to holding vessel 12, carry out the first scrub stream circulation；
After the first scrub stream recycles a period of time, second solenoid valve 10 and the 4th solenoid valve 14 are closed and first is electric
When magnet valve 16 and third solenoid valve 11 are opened, source of supply 100 flows out stoste and serves as the second scrub stream, and the second scrub stream passes through supply
Pipeline 5 flows to clean unit 2, flow back into holding vessel 12 until by evacuating branch 9, the second scrub stream can be in clean unit
Replacement is present in the first scrub stream of high concentration ionizing particle in 2, and it can also remove the electricity for being still in circulation capacitor 4
Residual ionizing particle on extremely, when liquid reaches horizontal quota in holding vessel 12, or setting interval time and interval time
After reaching, the 5th valve 16 is opened with the ionizing particle liquid containing high concentration inside certain flow rate discharge holding vessel 12, and is reached
Second washing flow velocity of holding vessel 12 is substantially equal to the flow velocity for the concentrating streams being discharged by delivery pipe 15 from holding vessel 12,
The flow velocity is set smaller than 5% of the overall flow rate from the processing of clean unit 2 and the fluid purified, is most preferably 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 clean units 2 to load and reaches expected operating voltage, into working stage, then
First solenoid valve 16 and second solenoid valve 10 are opened and third solenoid valve 11 and the 4th solenoid valve 14 are closed, carries out stoste again
Purification.
Based on above-mentioned, clean unit 2 is arranged in the present invention, and the salt in solution, ammonia and other poles are removed by the way of ionization
Change pollutant and chemical substance, organic substance or micropollutants, also cooperates holding vessel 12 to clean unit by hydraulic system
2 are washed twice, have not only been played the role of to 2 reactivation of clean unit, but also have collected the isolated ionizing particle of electricity, and will contain
The liquids recovery of the ionizing particle of high concentration is recycled convenient for subsequent discharge into holding vessel 12, in this system the first cleaning solution with
Second cleaning solution is derived from source of supply 100, does not need to introduce clean liquid from the external world, also not need using filter material, this hair
Bright good purification, 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 Fliod fluid decontamination system and purification method, which is characterized in that including purification device (1), in the purification device (1)
Including a clean unit (2), the clean unit (2) is equipped with condenser and contained structure (3), the contained structure (3)
The circulation capacitor (4) that inner containment has one or more serial or parallel connections to be electrically connected, fluid to be processed can flow
It is flowed between the electrode of energization appearance (4), and clean unit (2) is also connected electrically to DC power supply (36), the DC power supply (36) passes through
Control circuit equipped with controller is connected to the electrode of circulation capacitor (4), and the conductive layer of the electrode of circulation capacitor (4) has
Several surface holes, the surface holes provide the attachment surface with fluid exchange；
It further include hydraulic system in the purification device (1), the hydraulic system passes through supply line (5) to clean unit (2)
Fluid to be processed is supplied, supply line (5) is from the untreated stoste of source of supply (100) acquisition and by the first solenoid valve (6)
It intercepts, stoste is transported in extraction conduit (7) after passing through clean unit (2), and extraction conduit (7) is subdivided into services branch
(8) and branch (9) are evacuated, the services branch (8) is intercepted by second solenoid valve (10), for the stoste after transport process, institute
It states and evacuates branch (9) by third solenoid valve (11) interception, for conveying the first scrub stream and the second cleaning solution；
It further include holding vessel (12) in the purification device (1), the holding vessel (12) by the 4th solenoid valve (14) by being intercepted
Conveyance conduit (13) be hydraulically connected to supply line (5) in exit, be provided with circulating pump on the conveyance conduit (13)
(70), the holding vessel (12) is also connected in input terminal and evacuates branch (9), and holding vessel (12) is also connected with by the 5th valve
(16) delivery pipe (15) intercepted.
2. a kind of Fliod fluid decontamination system according to claim 1 and purification method, it is characterised in that: the circulation capacitor
(4) two or more superposed electrodes facing with each other are disposed with, electrode is flattened round thin slice or coils the flat of formation
Flat round cylinder.
3. a kind of Fliod fluid decontamination system according to claim 1 and purification method, it is characterised in that: the circulation capacitor
(4) separation layer is set between electrode, and the separation layer is made of the porous synthetic material or fibrous material insulating, including but not
It is only limitted to glass or nylon fabric.
4. a kind of Fliod fluid decontamination system according to claim 1 and purification method, it is characterised in that: the circulating pump (70)
Can also be arranged in evacuate branch (9) on, with extracted from clean unit (2) the first cleaning solution and the second cleaning solution and by it
Be sent in holding vessel (12).
5. a kind of fluid purification according to claim 1, it is characterised in that: steps are as follows:
Step 1: first passing through control circuit makes circulation capacitor (4) be in the charging stage, waits the circulation capacitor in clean units (2)
(4) it loads and reaches expected operating voltage, into working stage, then by the first solenoid valve (6) and second solenoid valve
(10) it opens and third solenoid valve (11) and the 4th solenoid valve (14) is closed, the stoste in source of supply (100) passes through supply line
(5) it flows to clean unit (2), the circulation capacitor (4) of clean unit (2) is during working stage, therefore the particle ionized is had
There is the polar respective electrode opposite with them to attract, leads to ionic particles building up in identical electrodes, to occur
The purification of stoste；
Step 2: as purification carries out, once the electrode of circulation capacitor (4) reaches program saturation, there will be polarization in fluid
Particle, immediately enter regeneration stage, at this stage during, first by the first solenoid valve (16) and third solenoid valve (11) closing and
Second solenoid valve (10) and the 4th solenoid valve (14) are opened, and the first scrub stream flows out into supply line from holding vessel (12)
(5), force include clean unit (2) neutralize extraction conduit (7) in cleaned stoste towards services branch (8) flow away,
It is then shut off all valves；
Step 3: again by control circuit make to circulate capacitor (4) be again at discharge regime, then by third solenoid valve (11) and
4th solenoid valve (14) is opened and the first solenoid valve (16) and second solenoid valve (10) remain turned-off, and the first scrub stream leaves storage
Tank (12) passes through clean unit (2), removal accumulation ionizing particle on the electrode, and is transmitted back to holding vessel (12), carries out the
One scrub stream circulation；
Step 4: after the first scrub stream recycles a period of time, second solenoid valve (10) and the 4th solenoid valve (14) are closed simultaneously
And first solenoid valve (16) and third solenoid valve (11) when opening, source of supply (100) outflow stoste serve as the second scrub stream, second
Scrub stream flows to clean unit (2) by supply line (5), flow back into holding vessel (12) until by evacuating branch (9), the
Two scrub streams can replace the first scrub stream for being present in high concentration ionizing particle in clean unit (2), and it can also
Removal is still in the residual ionizing particle on the electrode of circulation capacitor (4)；
Step 5: finally again by control circuit make circulate capacitor (4) first be in the no-voltage stage for a period of time, then again into
Enter the charging stage, the circulation capacitor (4) in clean units (2) is waited to load and reach expected operating voltage, into work
Stage, then by the first solenoid valve (16) and second solenoid valve (10) opening and third solenoid valve (11) and the 4th solenoid valve (14)
It closes, carries out stoste purification again.
6. a kind of fluid purification according to claim 5, it is characterised in that: liquid reaches water in holding vessel (12)
When flat quota, or setting interval time and after interval time reaches, opens the 5th valve (16) and be discharged with certain flow rate and store
The internal ionizing particle liquid containing high concentration of tank (12).
7. according to right want 6 described in a kind of fluid purification, it is characterised in that: reach holding vessel (12) the second cleaning solution
Flow velocity is substantially equal to the flow velocity for the concentrating streams being discharged by delivery pipe (15) from holding vessel (12), which is set smaller than
The 5% of the overall flow rate for the fluid for handling and purifying from clean unit (2), is most preferably set as 2%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910574630.2A CN110240231B (en) | 2019-06-28 | 2019-06-28 | Fluid purification system and purification method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910574630.2A CN110240231B (en) | 2019-06-28 | 2019-06-28 | Fluid purification system and purification method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110240231A true CN110240231A (en) | 2019-09-17 |
| CN110240231B CN110240231B (en) | 2021-09-28 |
Family
ID=67890150
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910574630.2A Active CN110240231B (en) | 2019-06-28 | 2019-06-28 | Fluid purification system and purification method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110240231B (en) |
Citations (29)
| 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 |
| CN101107200A (en) * | 2005-01-27 | 2008-01-16 | 荷兰联合利华有限公司 | Water softening device and method |
| 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 CN201910574630.2A patent/CN110240231B/en active Active
Patent Citations (29)
| 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 |
| CN101107200A (en) * | 2005-01-27 | 2008-01-16 | 荷兰联合利华有限公司 | Water softening device and method |
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110240231B (en) | 2021-09-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109457440B (en) | Water treatment circulation system, control method thereof and clothes treatment device | |
| CN102319626A (en) | Improved fluid iron removal method and device | |
| CN110787512A (en) | Pickling process for metal filter element | |
| US9919937B2 (en) | System for recovering multiple kinds of ions | |
| CN110240231A (en) | A kind of Fliod fluid decontamination system and purification method | |
| CN108569794A (en) | A kind of reverse osmosis purified water system | |
| Chang et al. | Biosorption of lead, copper, and cadmium with continuous hollow-fiber microfiltration processes | |
| CN205061637U (en) | Based on capacitanc seawater desalination equipment under direct current field effect | |
| JP2003285067A (en) | Full automatic and energy saving deionization system | |
| CN102351336A (en) | Electroplating wastewater treatment process | |
| CN105293745B (en) | Cold-rolling pickling wastewater recycling treatment process system | |
| CN110143649A (en) | A kind of two-way Fliod fluid decontamination system | |
| CN107746134A (en) | A kind of full room comprehensive water treatment system of intelligent control and method for treating water | |
| CN202610333U (en) | Recycling system for waste system in photoelectric cell wet process | |
| CN215924688U (en) | Membrane module treatment device for filtering sewage | |
| CN1316110C (en) | Purifying system for rinsing water of washing machine and rinsing control method | |
| CN213112904U (en) | Chemical waste acid recovery processing device | |
| CN104810135A (en) | Kerosene oil gas phase cleaning and drying system and method for transformer body | |
| CN114733580A (en) | Dynamic continuous ion exchange device | |
| CN204324964U (en) | A kind of filter plant based on electromagnetic water treatment | |
| CN207918569U (en) | A kind of full room comprehensive water treatment system of intelligent control | |
| CN107309263B (en) | High concentration, complete circulation type soil, in solid waste pollutant chemical leaching separation method and its separation system | |
| CN202529921U (en) | Treatment device for nickel rinse water for electroplating nickel aminosulfonate | |
| CN103184151A (en) | Device for high-efficient separation of magnetotactic bacteria in high gradient magnetic field | |
| CN112851005A (en) | Zero-emission treatment system and method for uranium-containing underground water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240826 Address after: Room 1717, 17th Floor, Building 1, Lanzhou Zhongtianjian Plaza, 194 Xijin West Road, Qilihe District, Lanzhou City, Gansu Province 730050 Patentee after: Gansu Dinglian Environmental Protection Technology Co.,Ltd. Country or region after: China Address before: 243000 2, 1669 north section of Huo Li Shan Road, Ma'anshan high tech Zone, Anhui Patentee before: MAANSHAN XINQIAO INDUSTRIAL DESIGN Co.,Ltd. Country or region before: China |
|
| TR01 | Transfer of patent right |