CN114409027A - Cross STREAMING electrode antibacterial device - Google Patents
Cross STREAMING electrode antibacterial device Download PDFInfo
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- CN114409027A CN114409027A CN202210059138.3A CN202210059138A CN114409027A CN 114409027 A CN114409027 A CN 114409027A CN 202210059138 A CN202210059138 A CN 202210059138A CN 114409027 A CN114409027 A CN 114409027A
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- 230000000844 anti-bacterial effect Effects 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 71
- 230000003385 bacteriostatic effect Effects 0.000 claims abstract description 23
- 238000007789 sealing Methods 0.000 claims abstract description 14
- 238000005868 electrolysis reaction Methods 0.000 claims description 15
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 239000010936 titanium Substances 0.000 claims description 6
- 229910052719 titanium Inorganic materials 0.000 claims description 6
- 125000006850 spacer group Chemical group 0.000 claims description 4
- IIWCXJSQZLPAPX-UHFFFAOYSA-N [Sn].[Ta].[Ir] Chemical compound [Sn].[Ta].[Ir] IIWCXJSQZLPAPX-UHFFFAOYSA-N 0.000 claims description 3
- CJTCBBYSPFAVFL-UHFFFAOYSA-N iridium ruthenium Chemical compound [Ru].[Ir] CJTCBBYSPFAVFL-UHFFFAOYSA-N 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000011248 coating agent Substances 0.000 claims description 2
- 238000000576 coating method Methods 0.000 claims description 2
- 230000005611 electricity Effects 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 14
- 230000001954 sterilising effect Effects 0.000 abstract description 12
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 10
- 125000002887 hydroxy group Chemical group [H]O* 0.000 abstract description 6
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 abstract description 5
- 230000002401 inhibitory effect Effects 0.000 abstract description 4
- 238000003780 insertion Methods 0.000 description 6
- 230000037431 insertion Effects 0.000 description 6
- 230000008878 coupling Effects 0.000 description 5
- 238000010168 coupling process Methods 0.000 description 5
- 238000005859 coupling reaction Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- -1 ozone ions Chemical class 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 241001415288 Coccidae Species 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000005672 electromagnetic field Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000003631 expected effect Effects 0.000 description 1
- 230000035784 germination Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Images
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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
-
- 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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
- C02F2001/46185—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water only anodic or acidic water, e.g. for oxidizing or sterilizing
-
- 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
- C02F2303/04—Disinfection
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General 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)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention provides an overflowing type electrode bacteriostatic device which comprises a chassis and an upper cover connected to the chassis in a sealing manner through a first annular sealing ring, wherein a cavity with an upward opening is formed between the chassis and the upper cover, a water inlet channel and a water outlet channel which are communicated with the cavity are arranged on a transverse hollow chassis, an electrode group used for carrying out electrolytic treatment on flowing water is arranged in the cavity, two electric wire inserting pieces extending outwards are arranged on the electrode group, and a first through hole through which a power supply wire inserting piece penetrates is arranged on the chassis. According to the over-flow type electrode bacteriostatic device provided by the invention, hydroxyl and ozone are generated by electrolyzing water, so that the effect of sterilizing and inhibiting the water in the over-flow type electrode bacteriostatic device is achieved, the sterilization treatment effect is improved, and the treatment cost is reduced.
Description
Technical Field
The invention relates to the technical field of water treatment, in particular to an overflowing type electrode bacteriostatic device.
Background
At present, along with environmental pollution's gradual aggravation, the water storage containers such as the pure water case of purifier, water dispenser, water purification case, former water tank on the market usually are UNICOM because of mostly with the atmosphere, and its water tank generally in the machine the inside, and the most shade and humidity of environment use the easy bacterium of nourishing of water purification case after a period, cause secondary pollution to the water purification, influence drinking water health.
Chinese patent application No. CN201611015293 discloses an overflowing sterilization apparatus and water purification equipment, which adopts ultraviolet LED cooperating with a reflective sleeve to realize the ultraviolet sterilization treatment of water flowing through a transparent tube, but finds in practice that the sterilization treatment effect of the treatment method needs higher treatment cost if it needs to reach the expected effect, and most of the structures are complex, and easily cause pollution to the environment.
Therefore, it is necessary to provide an over-flow type electrode bacteriostatic device to solve the above technical problems.
Disclosure of Invention
The invention mainly solves the technical problem of providing the overflowing type electrode bacteriostatic device, which generates hydroxyl and ozone by electrolyzing water so as to achieve the effect of sterilizing and inhibiting the water in the overflowing type electrode bacteriostatic device, and can reduce the treatment cost while improving the sterilization treatment effect.
In order to solve the technical problems, one technical scheme adopted by the invention is to provide an overflowing type electrode bacteriostatic device, which comprises a chassis 1 and an upper cover 12 connected to the chassis 1 in a sealing manner through a first annular sealing ring 11, wherein a cavity 2 with an upward opening is formed between the chassis 1 and the upper cover 12, a water inlet channel 13 and a water outlet channel 14 which are communicated with the cavity 2 are arranged on the transverse hollow chassis 1, an electrode group 3 for performing electrolytic treatment on flowing water is arranged in the cavity 2, two wire insertion pieces 31 extending outwards are arranged on the electrode group 3, and a first through hole 15 for the wire insertion pieces 31 to penetrate out is arranged on the chassis 1.
Preferably, including positive pole piece 32 and setting in the electrode group 3 negative pole piece 33 of positive pole piece 32 below, two electric wire inserted sheet 31 respectively with positive pole piece 32 with negative pole piece 33 electricity is connected, be equipped with a plurality of second through-holes 321 on the positive pole piece 32, be equipped with on the negative pole piece 33 with a plurality of with the third through-hole 331 that second through-hole 321 corresponds the setting.
Preferably, a spacer 34 is provided between the anode sheet 32 and the cathode sheet 33 to prevent direct contact therebetween.
Preferably, the bottom of the cavity 2 is provided with a support part 21 protruding upwards for supporting the cathode sheet 33.
Preferably, the position of the water inlet pipe mouth 131 of the water inlet channel 13 is connected with a first quick coupling 16 for quickly connecting the water inlet pipe through a second annular sealing ring 132, and the position of the water outlet pipe mouth 141 of the water outlet channel 14 is connected with a second quick coupling 17 for quickly connecting the water outlet pipe through a third annular sealing ring 142.
Preferably, the water inlet channel 13 and the water outlet channel 14 are symmetrically distributed on two ends of the chassis 1.
Preferably, the anode strip 32 is an electrode made of ruthenium iridium or iridium tantalum tin coating titanium as a basic material, and the cathode strip 33 is an electrode made of stainless steel or a titanium material.
Preferably, the cathode sheet 33 has the same shape as the anode sheet 32, and is preferably in the form of a mesh or a sheet.
The invention has the beneficial effects that: according to the over-flow type electrode bacteriostatic device provided by the invention, hydroxyl and ozone are generated by electrolyzing water, so that the effect of sterilizing and inhibiting the water in the over-flow type electrode bacteriostatic device is achieved, the sterilization treatment effect is improved, and the treatment cost is reduced.
Drawings
FIG. 1 is an enlarged structural view of an over-flow electrode bacteriostatic device provided by the invention;
FIG. 2 is an overall structure diagram of an over-flow electrode bacteriostatic device provided by the invention;
fig. 3 is a top view structural diagram of an over-flow type electrode bacteriostatic device provided by the invention;
FIG. 4 is a sectional view of the structure of FIG. 3A;
fig. 5 is a top view structural diagram of a chassis of an over-flow type electrode bacteriostatic device provided by the invention.
The names of the parts corresponding to the numerical identifiers in the drawings of the specification are respectively as follows:
a chassis 1; a cavity 2; an electrode group 3; a first annular seal ring 11; an upper cover 12; a water inlet passage 13; a water outlet passage 14; a first through hole 15; a first quick connector 16; a second quick coupling 17; a support portion 21; a wire insert 31; an anode sheet 32; a cathode sheet 33; a spacer 34; a water inlet pipe orifice 131; a second annular seal ring 132; a water outlet pipe port 141; a third annular seal ring 142; a second through hole 321; and a third through hole 331.
Detailed Description
The technical solution of the present invention will be described in detail with reference to the drawings.
Referring to fig. 1 to 5, the over-flow type electrode bacteriostatic device of the present embodiment includes a chassis 1 and an upper cover 12 hermetically connected to the chassis 1 through a first annular sealing ring 11, a cavity 2 with an upward opening is formed between the chassis 1 and the upper cover 12, a water inlet channel 13 and a water outlet channel 14 communicated with the cavity 2 are disposed on the transverse hollow chassis 1, an electrode group 3 for performing electrolysis treatment on water flowing through is disposed in the cavity 2, two outwardly extending electric wire insertion pieces 31 are disposed on the electrode group 3, and a first through hole 15 through which the electric power supply wire insertion piece 31 penetrates is disposed on the chassis 1.
In this embodiment, when the current applied to the wire insertion piece 31 is conducted to the electrode group 3, the water molecules flowing into the cavity 2 through the water inlet channel 13 can generate an electrolytic reaction and release hydroxyl and ozone, so as to achieve the sterilization and bacteriostasis effects on the water in the over-flow electrode bacteriostasis device.
In the embodiment, the electrode group 3 of the present application can continuously electrolyze in water to generate an oxidizing substance, so as to change the oxidation-reduction potential of the water body, thereby achieving the effect of inhibiting the mass propagation of bacteria,
in this embodiment, the electrode assembly 3 of the present application can continuously generate a large amount of oxidized ions, radicals, and free radicals in water during the electrolytic reaction, and under the synergistic effect with the electromagnetic field, these trace amounts of oxidizing substances can effectively prevent the mass propagation of microorganisms, and inhibit the rooting and germination of algae spores in water, thereby reducing the turbidity of circulating water, reducing the generation of biological soft scale, reducing the corrosion under scale, and replacing the addition of bactericide.
Preferably, the electrode group 3 includes an anode strip 32 and a cathode strip 33 disposed below the anode strip 32, the two wire insertion pieces 31 are electrically connected to the anode strip 32 and the cathode strip 33, the anode strip 32 is provided with a plurality of second through holes 321, and the cathode strip 33 is provided with a plurality of third through holes 331 corresponding to the second through holes 321.
In this embodiment, the anode plate 32 and the cathode plate 33 of the present application adopt a one-to-one multi-through-hole structure, which can effectively improve the electrolysis efficiency and improve the electrolysis effect, and the principle thereof lies in that water molecules can be in a power-off state when flowing through the anode plate 32, and then can generate an electrolysis reaction and release ozone ions, and the water molecules flowing through the cathode plate 33 can be in a power-on state, and can generate an electrolysis reaction and release hydroxyl ions (hydroxyl groups), and the products of the electrolysis of the anode plate 32 can be gathered in the second through-holes 321, so that the flowing water molecules can all react with each through-hole in the anode plate 32 and the cathode plate 33, and further fully react, thereby improving the electrolysis efficiency and improving the electrolysis effect.
Preferably, a separator 34 is provided between the anode sheet 32 and the cathode sheet 33 to prevent direct contact therebetween.
In this embodiment, during the water electrolysis process, the spacer 34 can ensure that the liquid level can submerge the anode sheet 32 and the cathode sheet 33 to the maximum extent, so as to avoid that the water molecules can not be in full contact with the contact surface between the anode sheet 32 and the cathode sheet 33 due to the contact state, thereby affecting the electrolysis reaction.
Preferably, the bottom of the chamber 2 is provided with a support portion 21 protruding upward for supporting the cathode sheet 33.
In this embodiment, in the process of electrolyzing water, if the bottom of the cathode sheet 33 directly contacts with the bottom of the cavity 2, the contact surface between the cathode sheet 33 and the cavity 2 is in a contact state, so that water molecules cannot be in full contact with the cathode sheet 33, thereby affecting the electrolytic reaction.
Preferably, the first quick coupling 16 for quick connection with the inlet pipe is connected to the inlet pipe 131 of the inlet channel 13 in a sealing manner through the second annular sealing ring 132, and the second quick coupling 17 for quick connection with the outlet pipe is connected to the outlet pipe 141 of the outlet channel 14 in a sealing manner through the third annular sealing ring 142.
Preferably, the water inlet channel 13 and the water outlet channel 14 are symmetrically distributed on both ends of the base plate 1.
In this embodiment, the symmetrically distributed water inlet channel 13 and water outlet channel 14 can effectively reduce the overall volume of the overflowing type sterilization and disinfection device, so that the structure is more compact.
Preferably, the anode sheet 32 is an electrode made of ruthenium iridium or iridium tantalum tin coated titanium as a base material, and the cathode sheet 33 is an electrode made of stainless steel or a titanium material.
In this embodiment, the anode sheet 32 and the cathode sheet 33 of the present application may also be electrodes made of other inert metals, and the present application is not limited in any way.
Preferably, the cathode sheet 33 has the same shape as the anode sheet 32, and is preferably in the form of a mesh or a sheet.
In this embodiment, the power of the over-flow electrode bacteriostatic device is generally designed to be high power, so that when water molecules flow to the electrode group 3, the electrode group 3 can immediately perform complete sterilization and bacteriostatic treatment on the flowing water molecules, and the mesh-shaped and sheet-shaped electrode plates can effectively improve the electrolysis efficiency and the electrolysis effect.
It can be seen that, with the implementation of the over-flow type electrode bacteriostasis device described in fig. 1 to 5, hydroxyl and ozone are generated by electrolyzing water, so that the water in the over-flow type electrode bacteriostasis device is sterilized and bacteriostatically, and the treatment cost is reduced while the sterilization treatment effect is improved.
In addition, the implementation of the over-flow type electrode bacteriostasis device described in fig. 1-5 has the advantages of more compact and simple structure, and can effectively improve the electrolysis efficiency and the electrolysis effect.
The above description is only an embodiment of the present invention, and not intended to limit the scope of the present invention, and all equivalent structures made by using the contents of the present specification and the drawings, or applied directly or indirectly to other related technical fields, are included in the scope of the present invention.
Claims (8)
1. An overflowing electrode bacteriostasis device is characterized in that: including chassis (1) and through first ring packing (11) sealing connection upper cover (12) on chassis (1), chassis (1) with be formed with opening cavity (2) up between upper cover (12), be equipped with on horizontal cavity chassis (1) with inlet channel (13) and exhalant canal (14) of cavity (2) intercommunication, be equipped with in cavity (2) and be used for carrying out electrolysis treatment's electrode group (3) to the water that flows through, be equipped with two outside extension's electric wire inserted sheet (31) on electrode group (3), be equipped with the confession on chassis (1) first through-hole (15) that electric wire inserted sheet (31) were worn out.
2. The over-flow electrode bacteriostatic device according to claim 1, characterized in that:
including positive pole piece (32) and setting in electrode group (3) negative pole piece (33) of positive pole piece (32) below, two electric wire inserted sheet (31) respectively with positive pole piece (32) with negative pole piece (33) electricity is connected, be equipped with a plurality of second through-holes (321) on positive pole piece (32), be equipped with on negative pole piece (33) with a plurality of with second through-hole (321) correspond third through-hole (331) that set up.
3. An over-flow electrode bacteriostatic device according to claim 2, characterized in that: and a spacer (34) for avoiding direct contact between the anode sheet (32) and the cathode sheet (33) is arranged between the anode sheet and the cathode sheet.
4. An over-flow electrode bacteriostatic device according to claim 2, characterized in that: the bottom of the cavity (2) is provided with a supporting part (21) which protrudes upwards and is used for supporting the cathode sheet (33).
5. An over-flow electrode bacteriostasis device according to any one of claims 1 to 4, wherein:
the water inlet pipe is characterized in that a first quick connector (16) used for being connected with a water inlet pipe quickly is connected to the position of a water inlet pipe orifice (131) of the water inlet channel (13) through a second annular sealing ring (132), and a second quick connector (17) used for being connected with a water outlet pipe quickly is connected to the position of a water outlet pipe orifice (141) of the water outlet channel (14) through a third annular sealing ring (142).
6. The over-flow electrode bacteriostatic device according to claim 1, characterized in that: the water inlet channel (13) and the water outlet channel (14) are symmetrically distributed on two ends of the chassis (1).
7. An over-flow electrode bacteriostatic device according to claim 2, characterized in that: the anode sheet (32) is an electrode made of ruthenium iridium or iridium tantalum tin coating titanium as a basic material, and the cathode sheet (33) is an electrode made of stainless steel or a titanium material.
8. An over-flow electrode bacteriostatic device according to claim 2, characterized in that: the cathode sheet (33) has the same shape as the anode sheet (32), and is in the shape of a mesh or a sheet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210059138.3A CN114409027A (en) | 2022-01-19 | 2022-01-19 | Cross STREAMING electrode antibacterial device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210059138.3A CN114409027A (en) | 2022-01-19 | 2022-01-19 | Cross STREAMING electrode antibacterial device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN114409027A true CN114409027A (en) | 2022-04-29 |
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ID=81274114
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210059138.3A Pending CN114409027A (en) | 2022-01-19 | 2022-01-19 | Cross STREAMING electrode antibacterial device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114409027A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20130030760A (en) * | 2010-04-30 | 2013-03-27 | 페르메렉덴꾜꾸가부시끼가이샤 | - membrane-electrode assembly electrolytic cell using the same method and apparatus for producing ozone water method for disinfection and method for wastewater or waste fluid treatment |
| CN106698602A (en) * | 2017-01-10 | 2017-05-24 | 昆山泰瑞克智能科技有限公司 | Electrolyzed water sterilization device and sterilization method |
| CN209082000U (en) * | 2018-09-13 | 2019-07-09 | 广州市德百顺电气科技有限公司 | A kind of ozone electrolyte chamber structure |
| CN111254453A (en) * | 2020-03-27 | 2020-06-09 | 广州市德百顺电气科技有限公司 | Ozone electrolysis chamber and ozone electrolysis chamber application module |
| CN217780823U (en) * | 2022-01-19 | 2022-11-11 | 郭力 | Cross STREAMING electrode antibacterial device |
-
2022
- 2022-01-19 CN CN202210059138.3A patent/CN114409027A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20130030760A (en) * | 2010-04-30 | 2013-03-27 | 페르메렉덴꾜꾸가부시끼가이샤 | - membrane-electrode assembly electrolytic cell using the same method and apparatus for producing ozone water method for disinfection and method for wastewater or waste fluid treatment |
| CN106698602A (en) * | 2017-01-10 | 2017-05-24 | 昆山泰瑞克智能科技有限公司 | Electrolyzed water sterilization device and sterilization method |
| CN209082000U (en) * | 2018-09-13 | 2019-07-09 | 广州市德百顺电气科技有限公司 | A kind of ozone electrolyte chamber structure |
| CN111254453A (en) * | 2020-03-27 | 2020-06-09 | 广州市德百顺电气科技有限公司 | Ozone electrolysis chamber and ozone electrolysis chamber application module |
| CN217780823U (en) * | 2022-01-19 | 2022-11-11 | 郭力 | Cross STREAMING electrode antibacterial device |
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