CN201990737U - Electrode plate for electrolytic bath - Google Patents
Electrode plate for electrolytic bath Download PDFInfo
- Publication number
- CN201990737U CN201990737U CN2011200312306U CN201120031230U CN201990737U CN 201990737 U CN201990737 U CN 201990737U CN 2011200312306 U CN2011200312306 U CN 2011200312306U CN 201120031230 U CN201120031230 U CN 201120031230U CN 201990737 U CN201990737 U CN 201990737U
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- China
- Prior art keywords
- utility
- model
- battery lead
- lead plate
- electrode plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- 238000005265 energy consumption Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 239000000460 chlorine Substances 0.000 description 10
- 230000002378 acidificating effect Effects 0.000 description 7
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 6
- 229910052801 chlorine Inorganic materials 0.000 description 6
- 244000005700 microbiome Species 0.000 description 5
- 230000001954 sterilising effect Effects 0.000 description 5
- 239000003011 anion exchange membrane Substances 0.000 description 4
- 125000002091 cationic group Chemical group 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000008186 active pharmaceutical agent Substances 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- UPLPHRJJTCUQAY-WIRWPRASSA-N 2,3-thioepoxy madol Chemical compound C([C@@H]1CC2)[C@@H]3S[C@@H]3C[C@]1(C)[C@@H]1[C@@H]2[C@@H]2CC[C@](C)(O)[C@@]2(C)CC1 UPLPHRJJTCUQAY-WIRWPRASSA-N 0.000 description 1
- 102000010637 Aquaporins Human genes 0.000 description 1
- 108010063290 Aquaporins Proteins 0.000 description 1
- 102000015636 Oligopeptides Human genes 0.000 description 1
- 108010038807 Oligopeptides Proteins 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000037149 energy metabolism Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000003206 sterilizing agent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses an electrode plate for an electrolytic bath, which belongs to the technical field of the electrolytic bath and has the main technical scheme that the electrode plate comprises a body, wherein a plurality of through holes are distributed on the body. The utility model provides the electrode plate with the advantages of simple structure and little energy consumption, and the electrode plate is generally used for the electrolytic bath.
Description
Technical field
The utility model relates to a kind of electrolyzer accessory, more particularly, relates in particular to a kind of electrolyzer battery lead plate.
Background technology
In the current electrolysis sterilizing agent industry, the battery lead plate that electrolyzer uses is the whole plate in plane, the no aquaporin in surface, this kind design is at strongly-acid (or strong basicity) water of the same index of output, electric weight that is consumed and salt amount are relatively large, relatively do not have obvious power savings advantages with similar products.In addition, the sterilization mechanism of strong acidic electrolyzed water mainly contains following some:
(1) pH: the pH value scope that is suitable for microorganism existence, be 3～9 when microorganism germinates, during growth 4～9 (mould is 2.0～8.5), the pH value of strong acidic electrolyzed water is below 2.7, amphiprotic substance such as oligopeptides, polysaccharide etc. in the meeting havoc microorganism surface tissue, permeability of cell membrane is increased, and metabolic process is obstructed, and causes death;
(2) ORP: the suitable ORP scope of aerobic bacteria existence is+200～+ 800mV, anaerobic microorganism is-700～+ 200mV, and the redox potential that newly prepares strong acidic electrolyzed water is up to 1100mV, can change endocellular electricity and flow, thereby have a strong impact on energy metabolism of microorganism and the generation of ATP;
(3) available chlorine: the Cl in the water source
-Near oxidized formation HCLO anode, and the effective chlorine density of strong acidic electrolyzed water is 10～160mg/L is present in that sterilizing ability far is better than OCL in the acidic solution
-
As seen, this water needs to meet the requirements of situation in pH, ORP, available chlorine, and its sterilizing ability is the strongest.
So need control the parameter of three indexs simultaneously well, the control on the ratio of control pH value and effective chlorine density of battery lead plate in the three slot type electrolyzers of prior art is also unstable, usually in the time of the pH value can occurring and touch the mark requirement (pH:2-3), the concentration of available chlorine can be too high, too high when effective cl concn, can cause certain pollution to environment; (10～60mg/L) time, the pH value can be higher than index request again but when having controlled effective chlorine density.
The utility model content
The purpose of this utility model is at above-mentioned the deficiencies in the prior art, and a kind of simple in structure, battery lead plate that power consumption is few is provided.
The technical solution of the utility model is achieved in that a kind of electrolyzer battery lead plate, comprises body, is distributed with some through holes on its described body.
Above-mentioned a kind of electrolyzer is with in the battery lead plate, and described body one end is provided with joint pin.
Above-mentioned a kind of electrolyzer is with in the battery lead plate, and the aperture of described through hole is 1.5～10mm.
Above-mentioned a kind of electrolyzer is with in the battery lead plate, and the spacing between the through hole is 6～30mm.
After the utility model adopts said structure, by on original smooth battery lead plate, increasing some through holes, when two corresponding battery lead plates add volts DS, under the effect of DC electric field, Cl
-Be penetrated into anode slot by anion-exchange membrane, Na
+Be penetrated into cathode can by cationic exchange membrane, and original battery lead plate is flat, polar board surface does not have through hole, the Cl that is generated
-, Na
+Can only enter into anode slot or cathode can by the pole plate both sides, make the exchange capacity to weaken to some extent and consume; The utility model can effectively address the above problem after adopting said structure, has both guaranteed the quality of product, and the effect that reduces power consumption is arranged again.See table 1 for details: plate electrode and porous electrode experimental data compare:
Table 1 plate electrode and porous electrode experimental data are relatively
Illustrate: above-mentioned experimental data is by plate electrode and porous electrode are installed in same the equipment, measured when the sour water of the identical pH value of output, by above-mentioned experimental data as can be known, under sour water meets the requirements of situation, salt amount that battery lead plate of the present utility model consumes and electric weight have been saved production cost greatly well below plate electrode.
Description of drawings
The utility model is described in further detail below in conjunction with the embodiment in the accompanying drawing, but do not constitute any restriction of the present utility model.
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is a user mode reference drawing of the present utility model;
Fig. 3 is the decomposition texture synoptic diagram of Fig. 2.
Among the figure: body 1, through hole 2, joint pin 3, anion-exchange membrane 4, anode slot 5, cationic exchange membrane 6, cathode can 7, electrolytic bath 8.
Embodiment
Consult shown in Figure 1ly, a kind of electrolyzer battery lead plate of the present utility model comprises body 1, is provided with joint pin 3 at an end of body, and the pole plate joint pin is used to connect power supply, can make battery lead plate stably be fixed on electrolyzer inside again; Be evenly distributed with some through holes 2 on body 1, the aperture of through hole 2 is 1.5～10mm, and the spacing between the through hole 2 is 6～30mm.
The utility model is when concrete the use, consult Fig. 2, shown in Figure 3, battery lead plate body 1 of the present utility model is applied in the diaphragm electrolytic cell, battery lead plate body 1 is arranged between anion-exchange membrane 4 and cathode can 7 and cationic exchange membrane 6 and the anode slot 5, the battery lead plate body 1 that will be positioned at cathode can 7 is connected with positive source, the battery lead plate body 1 that will be positioned at anode slot 5 is connected with power cathode, electrolytic bath 8 is communicated with outer loop salt solution, anode slot 5 and cathode can 7 are communicated with outer loop water respectively, connect external dc power, under the effect of DC electric field, Cl
-Be penetrated into cathode can 7, Na by anion-exchange membrane 4
+Be penetrated into anode slot 5 by cationic exchange membrane 6.It is acid that the solution of cathode can 7 becomes, and contain a large amount of activeconstituentss, and redox potential is also higher, is strong acidic electrolyzed water and is called acidic oxidized electric potential water again.Acidic oxidation water refers to: when salt is with the volts DS electrolysis in water, and the redox potential (ORP) that anode side generates+more than the 1000mv, the anode water that pH2.7 is following.Because strong oxidized water has the unexistent function of general water, as: sterilizing power is strong, sterilization spectrum width, characteristics such as harmless, free from environmental pollution.
In sum, the utility model is as specification sheets and diagramatic content, makes actual sample and through repeatedly use test, from the effect of use test, provable the utility model can reach the purpose that it is expected, practical value is unquestionable.Above illustrated embodiment only is used for conveniently illustrating the utility model, is not the utility model is done any pro forma restriction.As the utility model in when combination, but realize two or the equal simple realization of plural electrolysis cells unitized construction, have in the technical field under any and know the knowledgeable usually, if in the scope that does not break away from technical characterictic that the utility model is carried, utilize technology contents that the utility model discloses to do the local equivalent embodiment that changes or modify, and do not break away from technical characterictic content of the present utility model, all still belong in the scope of the utility model technical characterictic.
Claims (4)
1. an electrolyzer battery lead plate comprises body (1), it is characterized in that: be distributed with some through holes (2) on the described body (1).
2. a kind of electrolyzer battery lead plate according to claim 1 is characterized in that: described body (1) one end is provided with joint pin (3).
3. a kind of electrolyzer battery lead plate according to claim 1 and 2 is characterized in that: the aperture of described through hole (2) is 1.5～10mm.
4. a kind of electrolyzer battery lead plate according to claim 3 is characterized in that: the spacing between the through hole (2) is 6～30mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200312306U CN201990737U (en) | 2011-01-28 | 2011-01-28 | Electrode plate for electrolytic bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200312306U CN201990737U (en) | 2011-01-28 | 2011-01-28 | Electrode plate for electrolytic bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201990737U true CN201990737U (en) | 2011-09-28 |
Family
ID=44667231
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200312306U Expired - Lifetime CN201990737U (en) | 2011-01-28 | 2011-01-28 | Electrode plate for electrolytic bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201990737U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103603005A (en) * | 2013-11-12 | 2014-02-26 | 广州赛爱环境保护技术开发有限公司 | Continuous weakly alkaline high-concentration hydrogen-rich water electrolysis device |
| CN106949552A (en) * | 2017-04-27 | 2017-07-14 | 北京立道立德环保设备有限责任公司 | The environmental improvement device and its control system and control method of a kind of underground piping |
-
2011
- 2011-01-28 CN CN2011200312306U patent/CN201990737U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103603005A (en) * | 2013-11-12 | 2014-02-26 | 广州赛爱环境保护技术开发有限公司 | Continuous weakly alkaline high-concentration hydrogen-rich water electrolysis device |
| CN103603005B (en) * | 2013-11-12 | 2016-08-17 | 广州赛爱环境保护技术开发有限公司 | Continuous way weakly alkaline high-concentration hydrogen-rich water electrolysis device |
| CN106949552A (en) * | 2017-04-27 | 2017-07-14 | 北京立道立德环保设备有限责任公司 | The environmental improvement device and its control system and control method of a kind of underground piping |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110928 |
|
| CX01 | Expiry of patent term |