CN1359857A - Process and apparatus for treating water by magneto-electric dialysis - Google Patents
Process and apparatus for treating water by magneto-electric dialysis Download PDFInfo
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- CN1359857A CN1359857A CN02101904A CN02101904A CN1359857A CN 1359857 A CN1359857 A CN 1359857A CN 02101904 A CN02101904 A CN 02101904A CN 02101904 A CN02101904 A CN 02101904A CN 1359857 A CN1359857 A CN 1359857A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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Abstract
A magneto-electric dialysis process for desalinating seawater, preparing salt from seawater and desalting industrial water is characterized by that on the basis is existing electric dialysis equipment, a static magnetic field is additionally used to directionally shift the cations and anions in flowing solution. Its apparatus is composed of a casing with different water inlets and outlets and electrodes, a group of cationic exchange membranes and anionic exchange membranes, which are alternatively arranged between anode and cathode, and a permanent magnet attached to each wall of the casing. Its advantages are high throughput, less electric consumption and not scaling.
Description
Technical field
The present invention relates to a kind of method and apparatus with electrochemical treatment water, especially a kind of charged particle that moves in the solution that utilizes is offset by the effect of Lip river logical sequence magnetic force, and the magnetic treatment scale removal effect of water, existing electrodialytic membranes isolation technique is carried out improved method and apparatus.It can be widely used in sea water desaltination, brackish water desalination, the concentrated salt manufacturing of seawater, industrial water supply desalination etc.
Background technology
The existing electroosmose process that carries out water treatment with electrochemical method, it is a selection perviousness of utilizing ion-exchange membrane, makes the electrolyte ion in the water make directional migration under the effect of DC electric field, realizes the desalination or the concentrated salt manufacturing of water.Its detailed process is: the positive and negative ion that saline hydrolysis becomes in the solution is made directional migration by acting on anion-exchange membrane, the cationic exchange membrane of DC electric field.Can see from Fig. 1 and Fig. 2 that with the electrodialyzer that this method is made it is to be that example is illustrated with the sea water desaltination.It include one have former water (seawater) import 11 (11a and 11b), electrode washing water inlet 16 (wherein 16b is that the import of anode wash-down water, 16a are the imports of negative electrode wash-down water) on it, (12b is the outlet of anode wash-down water, flows out the diluted acid chlorine water in electrode washing liquid outlet 12; 12a is negative electrode wash-down water outlet, flows out sig water NaOH), the housing 1 of the outlet 13 (wherein the desalination water outlet is 13b for the outlet of 13a, condensed water) of the water after handling; Installing electrodes 2 (wherein anode is that 2a, negative electrode are 2b) and between negative electrode and anode, install one group and be alternately and the cationic exchange membrane 3 and the anion-exchange membrane 4 that are provided with at interval in the housing.Former water enters electrodialyzer from sea intake 11, and on two electrodes, connect direct current, then (← represents the migration of Na+ ionic from the Na+ ion in the sea water solution, the electing property migration on cationic exchange membrane 3, anion-exchange membrane 4 of CL-ion, zero → represent the CL-ionic to move), finally the outlet 13a from diluting compartment confesses desalination water, and 13b flows out concentrated seawater from the condensed water outlet.Carried out for some time of after at said process, because of fouling, polarization of electrode occurring on ion-exchange membrane and two electrodes, the speed of sea water desaltination has been slowed down gradually, effluent characteristics reduces, power consumption increases.The shortcoming of existing electrodialytic method and equipment thereof is: 1) it is to finish by the migration that saline hydrolysis in the solution becomes positive and negative ion to do to select voluntarily on the yin, yang ion-exchange membrane by electric field action, the travelling speed of positive and negative ion all depends on structure, material and the current density of electrodialyzer, the character of processed water etc., in case it is appropriate that equipment is made, adorned, above-mentioned each parameter all settles, so water treatment speed and processing quality also all can't improve again, current efficiency can't improve again, current consumption just can't reduce; 2) if after fouling and polarization of electrode have appearred in yin, yang ion-exchange membrane and two electrodes, reduced the electrodialysis performance and the work-ing life of film, electrode,, also must unpick and wash when serious so must wash processing to it, thereby reduced the ability of water treatment, and this troublesome poeration is time-consuming again; If adopt the method for frequently pole-reversing, though can partly solve fouling and polar problem, the utmost point also must stop production, influence productivity at every turn.
Summary of the invention
The present invention will solve above-mentioned problems of the prior art, provide that a kind of water treatment is effective, speed is fast, processing power is big and the method and apparatus of the simple and reliable treating water by magneto-electric dialysis of method, and make its equipment also have characteristics such as simple and reasonable, easy to use and reliable.
The method for the treatment of water by magneto-electric dialysis of the present invention is characterized in: in the space of electrodialysis process water, increase a static magnetic field that can make yin, yang ion in the fluent solution do attitude drift.
The method for the treatment of water by magneto-electric dialysis of the present invention, its static magnetic field strength are not less than 0.5T (tesla).
A kind of magnetoelectricity dialyzer made from the inventive method, it contains and has original water inlet on it, the electrode washing water inlet, the electrode washing water out, the housing of desalination water outlet and condensed water outlet, electrode is housed in the housing, between positive and negative two electrodes, is equipped with one group and is alternately and spaced cationic exchange membrane and anion-exchange membrane, it is characterized in that: its housing with two all parallel shell walls of the water (flow) direction and the sense of current on the permanent magnetic plate of fitting respectively.
The above-mentioned magnetoelectricity dialyzer made from the inventive method, its housing is except being the high permeability material plate with all parallel two shell walls of the water (flow) direction and the sense of current, all the other each shell walls are low magnetically permeable material plate.
The above-mentioned magnetoelectricity dialyzer made from the inventive method, have between its two electrodes and can make the power supply that yin, yang the two poles of the earth exchange switch lock, simultaneously original water inlet, desalination water outlet, condensed water outlet, with former water water-supply pipe, desalination water delivery line, concentrated solution delivery line on the reversing valve into and out of state of convertible fluid on housing all is housed.
The above-mentioned magnetoelectricity dialyzer made from the inventive method, it also can be equipped with magnet piece on former water water-supply pipe.Handle in advance magnetization is done in water inlet, remove the ferromagnetic particle in the water inlet, prevent that effectively this particle from entering magnetoelectricity dialyzer of the present invention, influencing the water treatment effect of magnetoelectricity dialysis.
The invention has the beneficial effects as follows: 1) the present invention improves traditional method with electrodialysis process water, it by static magnetic field to the electromagnetic induction power that ion produced in the current (Lip river logical sequence magnetic force), increased the ion attitude drift power under the simple electric field action, thereby improve the water treatment capacity of equipment, and save electric energy; 2) added magnetic field increases the freeness of effects of ion, reduces hydration of ion, increases the selective permeability of ion on the yin, yang ionic membrane again, thereby reduces the liquid resistance and film hinders, and makes that water treatment efficiency improves more, power consumption more significantly reduces; 3) magnetic treatment of water helps the scale removal of electrodialysis appts, thereby reduces the frequency of unpicking and washing pause or frequently pole-reversing, the service efficiency and the work-ing life of also having improved equipment; 4) with the magnetoelectricity dialyzer of the inventive method, it simple and reasonable, easily manufactured, and compare with existing electrodialyzer, just on its housing, add two permanent magnetic plates, therefore can make things convenient for, renovate to having electrodialyzer now widely.
To and contrast accompanying drawing by example below, the present invention will be further described below.
Description of drawings
Fig. 1 and Fig. 2, Fig. 3 are respectively the structural representation of existing electrodialyzer and perspective view, front view;
Fig. 4 is two permanent magnetic plates that are used on the magnetoelectricity dialyzer of the present invention;
The front view of Fig. 5 magnetoelectricity dialyzer of the present invention;
Fig. 6 be magnetoelectricity dialyzer of the present invention had for implementing the convertible water (flow) direction that frequently pole-reversing is provided with and pipeline, the circuit of polarity of electrode figure is set.
Label declaration to each accompanying drawing is as follows:
The 1-housing; 11-original water inlet (wherein 11a leads to diluting compartment, and 11b leads to the concentration compartments); 12-electrode washing water out (wherein 12b is anode flushing outlet, and 12a is the outlet of negative electrode wash-down water); The outlet of 13a-desalination water; The outlet of 13b-condensed water; The 14-anolyte compartment; The 15-cathode compartment; 16-electrode washing water inlet (wherein 16b is the import of anode wash-down water, and 16a is the import of negative electrode wash-down water); 17-high permeability material plate; The 18-diluting compartment; The 19-concentration compartments; 2-electrode (wherein 2a-anode, 2b-negative electrode); The 3-cationic exchange membrane; The 4-anion-exchange membrane; The 5-power supply switches lock; The 6-permanent magnetic plate; 7-hangs down the magnetically permeable material plate; The 8-reversing valve; 9-forbids symbol; The 10-magnet piece; 20-magnetoelectricity dialyzer of the present invention; The former water water-supply pipe of 21-; 23-desalination water delivery line; 24-condensed water delivery line; The magnetic line of force bearing mark that the B-permanent magnetic plate produces.
Embodiment
The method of embodiment 1. present embodiments is in the space of electrodialysis process water, increases a static magnetic field that makes yin, yang ion in the fluent solution do attitude drift.
So-called electrodialysis space, can from the structural representation of the existing electrodialyzer Fig. 1 and Fig. 2 and perspective view, see, positive and negative ion in the solution (is represented the migration of positive ion with ← respectively among the figure, zero → represent the migration of negative ion), under the DC electric field effect, positive ion is to the negative electrode skew and optionally see through cationic exchange membrane, the skew of negative ion anode also optionally sees through anion-exchange membrane, its electric field to ionic biasing force Fe is: Fe=qE (q is the ionic electric weight, and E is a strength of electric field).As in the space of this electrodialysis process water, increase by one by two permanent magnetic plates 6 shown in Figure 4 (they by outside be attached to existing electrodialyzer among Fig. 3 before, on the outside wall surface of back two housings, that is the aidc on the permanent magnetic plate 6, efhg fits to the outer side wall AIDC of housing 1 respectively, on the EFHG, the magnetic line of force direction that permanent magnetic plate produces is the B direction), form the structure of the magnetoelectricity dialyzer of the present embodiment shown in Fig. 5, then in the space of existing electrodialysis process water, increase the moon that can make in the fluent solution, the static magnetic field of positively charged ion attitude drift, make ion also be subjected to Lip river logical sequence magnetic force Fm effect, (q is the ionic electric weight to the big or small Fm=qvB of this power, v is a flow velocity, and B is a magneticstrength); Because Fm is consistent with the direction of Fe, so suffered actual shifts power F=Fe+Fm of ion, the effect of this power greater than by electric field separately to the biasing force Fe of ionization, so the speed of ion skew improves greatly, and because the effect of magnetic treatment has reduced hydration, increase ionic freeness and the selective permeability of ion on ion-exchange membrane of effects of ion, thereby reduced liquid resistance and the film resistance in the electrodialysis process, the current efficiency of water treatment is improved.In a word, in the electrodialysis space, increase by one and can make the yin, yang ion in the fluent solution do to improve the ability of water treatment after the static magnetic field of attitude drift, can reduce current consumption again, and can also prevent the fouling and the polarization of electrode of film and electrode effectively.
Can from Fig. 5, see with the structure on its housing of magnetoelectricity dialyzer of present embodiment method manufacturing, and its internal structure can see figures.1.and.2.It contains the band housing 1 of six shell walls in front and back up and down, have original water inlet 11a and 11b (over 11a and 11b must divide except at frequently pole-reversing the time at upper and lower two shell walls of housing, the pipe 11a of all the other situations and 11b are that to merge two be one), (wherein 16b is the import of anode wash-down water to electrode washing water inlet 16,16a is the import of negative electrode wash-down water), (12b is the outlet of anode wash-down water, as flowing out the diluted acid chlorine water in electrode bath outlet 12; 12a is negative electrode flushing outlet, as flowing out sig water NaOH), desalination water outlet 13a and condensed water outlet 13b; Anolyte compartment 14 and cathode compartment 15 are arranged in the housing, and having in the anolyte compartment has negative electrode 2b in anode 2a, the cathode compartment, is cationic exchange membrane 3 and anion-exchange membrane 4 that one group of alternate intervals is arranged between anode and negative electrode; Housing with the outer side of all parallel two shell walls of the water (flow) direction and the sense of current on the permanent magnetic plate 6 of fitting respectively.
Former water enters the magnetoelectricity dialyzer of present embodiment from import 11a and 11b, and on two electrodes, connect direct current, (q is the ionic electric weight to electric field to ionic biasing force Fe=qE, E is a strength of electric field), ion also is subjected to the effect of Lip river logical sequence magnetic force Fm=qvB (q is the ionic electric weight, and v is a flow velocity, and B is a magneticstrength) simultaneously, because of Fm consistent with the direction of Fe, so the suffered actual shifts power F=Fe+Fm of ion; Therefore, positive and negative ion in the fluent solution is under DC electric field and the acting in conjunction of static magnetic field induced, positive ion is to the negative electrode skew and optionally see through cationic exchange membrane 3, the negative ion anode is offset and optionally see through anion-exchange membrane 4, finally the outlet 13a from diluting compartment confesses desalination water, and 13b flows out condensed water from the condensed water outlet.
Different is that static magnetic field strength should be not less than 0.5T (tesla) to the method for embodiment 2. and embodiment 1.Because Lip river logical sequence magnetic force Fm is directly proportional with magneticstrength B, magneticstrength is big more, and effect is just good more; If can enough 20T above superconductor high-intensity magnetic field then even more ideal.In addition because Lip river logical sequence magnetic force Fm=qvB is a vector, so with the electrodialysis space of magnetoelectricity dialyzer of the present invention must be no loop type flow through along whole face so that liquid flows, the total direction of flow velocity is consistent.Can also know that from Fm=qvB the increase flow stream velocity not only helps improving static magnetic field ionic is designed biasing force, also helps the water treatment speed that improves whole magnetoelectricity dialysis equipment.
Embodiment 3. can see from Fig. 5, is being high magnetic conductance material plates 17 with embodiment 1, embodiment 2 different is its housing with all parallel two shell walls of current, the sense of current, and remaining shell wall is low magnetic permeable material plate.Overcoming magnetic field shielding effect, and reduced effect to externally-applied magnetic field because of all the other shell walls.
Embodiment 4. can be as can see from Figure 6, and it can carry out frequently pole-reversing to the equipment of embodiment 1, embodiment 2, embodiment 3 to eliminate fouling, the polarization on electrode and the yin, yang ion-exchange membrane.Its structure is on original water inlet 11a and 11b, desalination water outlet 13a condensed water outlet 13b the reversing valve 8 of current to be housed all, and the power supply switching lock 5 that can make the exchange of yin, yang the two poles of the earth is housed in circuit.
When the magnetoelectricity dialyzer is carried out the operation of falling the utmost point, but switching lock 5, energize makes that original negative electrode becomes anode, anode becomes negative electrode, also make current commutation among pipe 11a, 11b, 13a, the 13b simultaneously by reversing valve 8.The 9th, forbid symbol, promptly reversing valve is forbidding that according with 9 place's water pipes closes, and connects with other two water pipes that reversing valve joins.
During the energising of present embodiment magnetoelectricity dialyzer, shown in Fig. 6 a, 11a, 11b connect with former water water-supply pipe 21 by the reversing valve 8 of current.The former water that is entered by 11a becomes desalination water through the desalination processing of magnetoelectricity dialyzer 20, through 13a, reversing valve 8, draws from desalination water delivery line 23 then; The former water that is entered by 11b becomes condensed water after magnetoelectricity dialyzer concentration, this after 13b, reversing valve 8 flow out from condensed water delivery line 24.Fig. 6 b is the streamflow regime of the magnetoelectricity dialyzer after representing extremely, at this moment switch lock 5 by power supply and make that original negative electrode becomes anode, anode becomes negative electrode, managing 13a, pipe 13b simultaneously connects with former water water-supply pipe 21 by the reversing valve 8 of current, former water by 13b enter the magnetoelectricity dialyzer fall after the pole change diluting compartment and be processed into desalination water, flow out the magnetoelectricity dialyzer by 11b; Enter the former water of magnetoelectricity dialyzer by 13a, be processed into condensed water in the concentration compartments of falling after the pole change, and flow out the magnetoelectricity dialyzer by 11a; Current among the last 11b are drawn by desalination water delivery line 23 by reversing valve, and the current among the 11a are flowed out by condensed water delivery line 24 by reversing valve.
Embodiment 5. sees from Fig. 6, and it can be in embodiment 1, embodiment 2, embodiment 3, embodiment 4 installs magnet piece 10 on the former water water-supply pipe 21 of magnetoelectricity dialyzer, and it can remove ferromagnetic particle in advance, in case it is piled up in equipment.
Claims (7)
1, a kind of method for the treatment of water by magneto-electric dialysis is characterized in that: in the space of electrodialysis process water, increase a static magnetic field that makes yin, yang ion in the fluent solution do attitude drift.
2, the method for the treatment of water by magneto-electric dialysis according to claim 1 is characterized in that: said static magnetic field strength is not less than 0.5T (tesla).
3, a kind of magnetoelectricity dialyzer made from the inventive method, it contains and has original water inlet (11) on it, electrode washing water inlet (16), electrode washing liquid outlet (12), the housing (1) of desalination water outlet (13A) and condensed water outlet (13b), electrode (2) is housed in the housing, and between positive and negative two electrodes, be equipped with one group and be alternately and spaced cationic exchange membrane (3) and anion-exchange membrane (4), it is characterized in that: its housing with two all parallel shell walls of the water (flow) direction and the sense of current on the permanent magnetic plate (6) of fitting respectively.
4, magnetoelectricity dialyzer according to claim 3 is characterized in that: said housing (1) is except being the high permeability material plate (17) with all parallel two shell walls of the water (flow) direction and the sense of current, and all the other each shell walls are low magnetically permeable material plate (7).
5, according to claim 3 or 4 described magnetoelectricity dialyzers, it is characterized in that: have the power supply that yin, yang two electrodes are exchanged between said two electrodes and switch lock (5), on original water inlet (11a), (11b), desalination water outlet (13a), condensed water outlet (13b) and former water water-supply pipe (21), desalination water delivery line (23), concentrated solution delivery line (24), the reversing valve into and out of state (8) of convertible fluid on housing is housed all simultaneously.
6, according to claim 3 or 4 described magnetoelectricity dialyzers, it is characterized in that: magnet piece (10) is housed on the said former water water-supply pipe (21).
7, magnetoelectricity dialyzer according to claim 5 is characterized in that: magnet piece (10) is housed on the said former water water-supply pipe (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021019045A CN1162341C (en) | 2002-01-10 | 2002-01-10 | Process and apparatus for treating water by magneto-electric dialysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021019045A CN1162341C (en) | 2002-01-10 | 2002-01-10 | Process and apparatus for treating water by magneto-electric dialysis |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100026332A Division CN1228253C (en) | 2002-01-10 | 2002-01-10 | Water treating magnetoelectric dialysis process |
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| Publication Number | Publication Date |
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| CN1359857A true CN1359857A (en) | 2002-07-24 |
| CN1162341C CN1162341C (en) | 2004-08-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB021019045A Expired - Fee Related CN1162341C (en) | 2002-01-10 | 2002-01-10 | Process and apparatus for treating water by magneto-electric dialysis |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103073096A (en) * | 2013-02-26 | 2013-05-01 | 昆明理工大学 | Device for processing charged ions in waste water through electromagnetism with electrodialysis |
| CN103406025A (en) * | 2013-08-28 | 2013-11-27 | 中国石油化工股份有限公司 | Technology for continuously removing heat steady salts from alcohol amine desulfurization solution by using double-membrane reactor-magnetic electrodialysis method |
| CN104098162A (en) * | 2013-04-15 | 2014-10-15 | 刘华鑫 | Electromagnetic water treatment apparatus |
| CN106458652A (en) * | 2014-04-23 | 2017-02-22 | 麻省理工学院 | Method and apparatus for partially desalinating produced water to form extraction fluid used for fossil fuel extraction |
| CN113716656A (en) * | 2021-09-18 | 2021-11-30 | 昆明理工大学 | Method for efficiently recycling saline sewage through magnetic synergistic electrodialysis |
| CN113998762A (en) * | 2021-11-04 | 2022-02-01 | 广东工业大学 | Electrodialysis sewage treatment device with magnet and electrodialysis sewage treatment method |
-
2002
- 2002-01-10 CN CNB021019045A patent/CN1162341C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103073096A (en) * | 2013-02-26 | 2013-05-01 | 昆明理工大学 | Device for processing charged ions in waste water through electromagnetism with electrodialysis |
| CN104098162A (en) * | 2013-04-15 | 2014-10-15 | 刘华鑫 | Electromagnetic water treatment apparatus |
| CN103406025A (en) * | 2013-08-28 | 2013-11-27 | 中国石油化工股份有限公司 | Technology for continuously removing heat steady salts from alcohol amine desulfurization solution by using double-membrane reactor-magnetic electrodialysis method |
| CN103406025B (en) * | 2013-08-28 | 2016-11-09 | 中国石油化工股份有限公司 | A kind of double membrane stack-magnetoelectricity dialysis is utilized to remove the device of heat stable salts in amine desulphurization solvent continuously |
| CN106458652A (en) * | 2014-04-23 | 2017-02-22 | 麻省理工学院 | Method and apparatus for partially desalinating produced water to form extraction fluid used for fossil fuel extraction |
| CN113716656A (en) * | 2021-09-18 | 2021-11-30 | 昆明理工大学 | Method for efficiently recycling saline sewage through magnetic synergistic electrodialysis |
| CN113998762A (en) * | 2021-11-04 | 2022-02-01 | 广东工业大学 | Electrodialysis sewage treatment device with magnet and electrodialysis sewage treatment method |
| CN113998762B (en) * | 2021-11-04 | 2023-02-28 | 广东工业大学 | Electrodialysis sewage treatment device with magnet and electrodialysis sewage treatment method |
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| CN1162341C (en) | 2004-08-18 |
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