CN2441795Y - High oxidation reduction level sterilized water generator - Google Patents
High oxidation reduction level sterilized water generator Download PDFInfo
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- CN2441795Y CN2441795Y CN 00218745 CN00218745U CN2441795Y CN 2441795 Y CN2441795 Y CN 2441795Y CN 00218745 CN00218745 CN 00218745 CN 00218745 U CN00218745 U CN 00218745U CN 2441795 Y CN2441795 Y CN 2441795Y
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Abstract
The utility model relates to a high oxidation reduction level sterilized water generator, which comprises an electrolytic bath, a ceramic sheet which is arranged on the middle part in the electrolytic bath, and an electrode positive plate and an electrodes negative plate which are respectively arranged on both sides of the ceramic sheet. The utility model also comprises passive electrode plates which are separately arranged between the electrode positive plate and the ceramic plate, and between the electrode negative and the ceramic plate. The passive electrode plates are porous structures. The utility model is a device which makes the sterilized water after the household-tap water which is added with a little of salt solution is electrolyzed in the electrolytic tank. The utility model can make acidic water of high oxidation reduction potential to be used as the sterilized water with high efficiency. The utility model has strongest sterilizing ability and better reducibility, and can not generate the secondary pollution to the ecological environment.
Description
The utility model relates to electrolyzer, particularly a kind of high redox potential disinfected water generator that adopts ion exchange technique.
After Britain agronomist Thompson in 1850 was found the ion-exchange phenomenon, through the century-old very long years, ion exchange technique was developed and applied in every respect, and especially the processing to water has obtained obvious improvement.The research of electroosmose process acquires a special sense, and Japanese scientist at first proposes the inversion that electrolytic reaction is not only an acid-basicity, also has the generation of reduction potential.With regard to acidic oxidation reduction potential water, property rapidly and the popularity and the reductibility of its disinfection function, all be other chemicalses can not compare.
With the water electrolysis principle, ceramic diaphragm is set in electrolyzer, add corrosion-resistant positive plate and negative plate, and time-controlled ion exchange technique, extensively be familiar with by people gradually, progressively become total knowledge.Through facts have proved, only possess these and be familiar with substantially, development product can only be primary, not mature enough.Because physical environment changes, as temperature, water temperature, pressure variation, get the quality of water random variation, add the variation of amount of electrolyte, factors such as the fluctuation of power supply source, can cause the cationic water of on time-controlled basis, being produced, be difficult to reach optimal control qualitatively, also the common means of producing of this kind, and power consumption is very big, thermal losses is not controlled yet, so efficient is very low.
The purpose of this utility model provides a kind of high redox potential disinfected water generator, and it can produce acidic water with high redox potential as high-effective disinfecting water, and alkaline water is fallen as discharge of wastewater.
A kind of high redox potential disinfected water generator described in the utility model, it comprises electrolyzer, the ceramic plate of installing in the middle of in electrolyzer, and the electrode anode plate and the electrode cathode plate that are provided with respectively in two sides of ceramic plate, the passive electrical pole plate that it also is included between electrode anode plate and the ceramic plate and is provided with respectively between electrode cathode plate and ceramic plate: described passive electrical pole plate is a vesicular structure.
The utility model is to add a kind of device that a little salt solution is produced after the electrolysis with ordinary tap water in electrolyzer, can produce acidic water with high redox potential, as high-effective disinfecting water, its sterilization ability extra-heavy, reductibility is also good especially, can not produce secondary pollution to ecotope.
Below in conjunction with accompanying drawing the utility model is elaborated.
Fig. 1 is a kind of structural representation of high redox potential disinfected water generator.
Fig. 2 is the plan structure synoptic diagram of electrode cathode plate in the above-mentioned machine.
Fig. 3 is the plan structure synoptic diagram of passive electrical pole plate in the above-mentioned machine.
Referring to Fig. 1, a kind of high redox potential disinfected water generator comprises electrolyzer 1, in electrolyzer 1 in the middle of the ceramic plate 2 of installing, and the electrode anode plate 3 and the electrode cathode plate 4 that are provided with respectively in two sides of ceramic plate 2.Between electrode anode plate 3 and the ceramic plate 2 and between electrode cathode plate 4 and ceramic plate 2, passive electrical pole plate 5 is set respectively.
In electrolyzer 1 with insulating micropore ceramics sheet 2 as barrier film, anode and negative electrode are divided into two cell bodies.Anode and negative electrode are arranged on the far-end of ceramic plate about 2 two sides, because dipolar gap ratio is bigger, the strength of electric field of electrolyzer 1 relatively a little less than, for compensating its defect, a passive electrical pole plate 5 ' is set in anode slot, another piece passive electrical pole plate 5 ' is set in cathode can.That is to say that passive electrical pole plate 5 promptly is provided with a pair of passive electrical pole plate 5 between electrode anode plate 3 and the ceramic plate 2 and be provided with one respectively between electrode cathode plate 4 and ceramic plate 2 in electrolyzer 1.
Passive electrical pole plate 5 promptly is provided with two pairs of passive electrical pole plates 5 between electrode anode plate 3 and the ceramic plate 2 and be provided with two respectively between electrode cathode plate 4 and ceramic plate 2 in electrolyzer 1.As shown in fig. 1, another to passive electrical pole plate 5 with label 5 " expression.Two pairs of passive electrical pole plates 5 so are set, can strengthen conductivity, reach the purpose of getting twice the result with half the effort.
Electroosmose process is used in tap water and adds small amount of electrolyte and carry out electrolysis treatment, it is a kind of very common method, from physics principle, anode requires corrosion-resistant, need between anode, negative electrode and the ceramic plate parallel each other outside, also need obtain uniform electric field, therefore, the linear content of two electrodes must equate that the imaginary area that is combined into also must equate.
The utility model is under the effect of uniform pulse DC electric field, the dielectric of micropore ceramics sheet 2 is partly punctured, though voltage breakdown is up to more than the 5KV, positively charged ion and negatively charged ion carry out two-way migration by ceramic capillary respectively, make to have the conducting in electric field of a certain amount of electrolytical water, produce medium heat and puncture, electrolyzer 1 water temperature is risen thereupon, energy is depleted, and electric current is big more, and loss is many more; Electrochemical breakdown, the physical structure that makes water clusters is by 15 H
2O changes to 5～6 molecular groupings, and the redox potential of water rises gradually at anode slot, more than 1100mV, progressively drops to negative value in cathode can, reach-below the 850mV.Meanwhile, it is acid that the pH value of anode slot is below 2.7, and the pH value of cathode can is alkalescence more than 11.
Referring to Fig. 2, for preventing the hurried rising of water temperature, must reduce working current, therefore electrode cathode plate 4 is designed to the trough of belt shape of fence structure.When effectively reducing working current, holding current density is constant like this.
Referring to Fig. 3, passive electrical pole plate 5 is vesicular structures.Hole on the passive electrical pole plate 5 is the hole of flare shape, is provided with spiral helicine cone around bellmouth orifice.Passive electrical pole plate 5 is designed to tubaeform porous and spirrillum conical structure form is very necessary.
As shown in Figure 1,6 of water-ins are provided with one, in order that simplified construction, this is by solenoid control.After anode slot is filled with by water, spill into cathode can from ceramic plate 2 tops, when the water of cathode can was injected into spillway 7, water monitor 10 was started working, and entering water electromagnetic valve is closed.Number in the figure 11 is for the sour water outlet of using, and label 12 is the alkaline water outlets as discharge of wastewater.
The control electrode probe 9 that is connected with Voltage pulsating direct-current supply and controller 8 thereof is equipped with in the bottom of ceramic plate 2, and dc pulse power supply and controller 8 thereof provide electric energy for anode, negative electrode, picks up electrical signal from control electrode probe 9, goes the keying of control electrode.When reaching desired oxidation power supply potential value, electrode supply is cut off, and at this moment, hummer is rung, and pilot lamp shows simultaneously.
Claims (6)
1. high redox potential disinfected water generator, it comprises electrolyzer, the ceramic plate of installing in the middle of in electrolyzer, and the electrode anode plate and the electrode cathode plate that are provided with respectively in two sides of ceramic plate, it is characterized in that the passive electrical pole plate that it also is included between electrode anode plate and the ceramic plate and is provided with respectively between electrode cathode plate and ceramic plate; Described passive electrical pole plate is a vesicular structure.
2. high redox potential disinfected water generator according to claim 1 is characterized in that, the trough of belt shape that described electrode cathode plate is a fence structure.
3. high redox potential disinfected water generator according to claim 1 is characterized in that, the hole on the described passive electrical pole plate is the hole of flare shape, is provided with spiral helicine cone around bellmouth orifice.
4. high redox potential disinfected water generator according to claim 1, it is characterized in that, described passive electrical pole plate promptly is provided with a pair of passive electrical pole plate between electrode anode plate and the ceramic plate and be provided with one respectively between electrode cathode plate and ceramic plate in electrolyzer.
5. high redox potential disinfected water generator according to claim 1, it is characterized in that, described passive electrical pole plate promptly is provided with two pairs of passive electrical pole plates between electrode anode plate and the ceramic plate and be provided with two respectively between electrode cathode plate and ceramic plate in electrolyzer.
6. high redox potential disinfected water generator according to claim 1 is characterized in that, the control electrode probe that is connected with Voltage pulsating direct-current supply and controller thereof is equipped with in the bottom of described ceramic plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00218745 CN2441795Y (en) | 2000-08-08 | 2000-08-08 | High oxidation reduction level sterilized water generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00218745 CN2441795Y (en) | 2000-08-08 | 2000-08-08 | High oxidation reduction level sterilized water generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2441795Y true CN2441795Y (en) | 2001-08-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00218745 Expired - Fee Related CN2441795Y (en) | 2000-08-08 | 2000-08-08 | High oxidation reduction level sterilized water generator |
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| Country | Link |
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| CN (1) | CN2441795Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110240388A (en) * | 2019-06-06 | 2019-09-17 | 河南工程学院 | Exchange electrode electro-osmosis sludge dewatering system and method based on voltage hierarchical detection |
| CN110255785A (en) * | 2019-07-13 | 2019-09-20 | 杭州胜于蓝环保科技有限公司 | Electric catalyticing system and the doctorization wastewater effluent processing method for applying to the system |
| WO2022213693A1 (en) * | 2021-04-07 | 2022-10-13 | 湖南满缘红水科技有限公司 | Low-salt eow electrolytic tank, low-salt eow electrolytic device, and low-salt eow preparation method |
-
2000
- 2000-08-08 CN CN 00218745 patent/CN2441795Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110240388A (en) * | 2019-06-06 | 2019-09-17 | 河南工程学院 | Exchange electrode electro-osmosis sludge dewatering system and method based on voltage hierarchical detection |
| CN110240388B (en) * | 2019-06-06 | 2023-09-12 | 河南工程学院 | Exchange electrode electroosmosis sludge dewatering system and method based on voltage grading detection |
| CN110255785A (en) * | 2019-07-13 | 2019-09-20 | 杭州胜于蓝环保科技有限公司 | Electric catalyticing system and the doctorization wastewater effluent processing method for applying to the system |
| CN110255785B (en) * | 2019-07-13 | 2023-08-04 | 杭州胜于蓝环保科技有限公司 | Electrocatalytic system and medical wastewater effluent treatment method applied to same |
| WO2022213693A1 (en) * | 2021-04-07 | 2022-10-13 | 湖南满缘红水科技有限公司 | Low-salt eow electrolytic tank, low-salt eow electrolytic device, and low-salt eow preparation method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |