CN220703351U - Swimming pool water electrolysis reactor - Google Patents
Swimming pool water electrolysis reactor Download PDFInfo
- Publication number
- CN220703351U CN220703351U CN202322049322.2U CN202322049322U CN220703351U CN 220703351 U CN220703351 U CN 220703351U CN 202322049322 U CN202322049322 U CN 202322049322U CN 220703351 U CN220703351 U CN 220703351U
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- Prior art keywords
- swimming pool
- water
- pool water
- electrolytic
- reactor shell
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 131
- 230000009182 swimming Effects 0.000 title claims abstract description 71
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 37
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 abstract description 16
- 241000195493 Cryptophyta Species 0.000 abstract description 8
- 241000894006 Bacteria Species 0.000 abstract description 6
- 238000004140 cleaning Methods 0.000 abstract description 6
- 229910001425 magnesium ion Inorganic materials 0.000 abstract description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 abstract description 5
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 abstract description 5
- 239000011575 calcium Substances 0.000 abstract description 5
- 229910001424 calcium ion Inorganic materials 0.000 abstract description 5
- 230000001580 bacterial effect Effects 0.000 abstract description 4
- 230000005684 electric field Effects 0.000 abstract description 4
- 230000000737 periodic effect Effects 0.000 abstract description 4
- 230000002035 prolonged effect Effects 0.000 abstract description 4
- 230000035484 reaction time Effects 0.000 abstract description 4
- 229910003460 diamond Inorganic materials 0.000 description 13
- 239000010432 diamond Substances 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 4
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000028327 secretion Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model provides a swimming pool water electrolysis reactor, which comprises an electrolysis reactor shell and an anode rod. The bottom end of the electrolytic reactor shell in the length direction is provided with a water inlet which is arranged at the tangential position of the electrolytic reactor shell; the water inlet is arranged in such a way that swimming pool water spirally rises between the electrolytic reactor shell and the anode rod, so that the reaction time of the swimming pool water in the reactor is prolonged, the swimming pool water can react more thoroughly, and finally flows out from the water outlet. Specifically, when raw water enters through the water inlet arranged on the swimming pool water electrolysis reactor, bacterial algae can be killed under the action of an electric field, and simultaneously organic matters containing ammonia nitrogen in water are oxidized and decomposed at the anode, so that the ammonia nitrogen content in water is reduced, calcium and magnesium ions in water are adsorbed by the cathode, and periodic cleaning can be realized. Therefore, the swimming pool water electrolysis reactor can kill bacteria and algae in the swimming pool water, can reduce the ammonia nitrogen content in the water, and can clean the swimming pool water well.
Description
Technical Field
The utility model relates to the technical field related to water treatment equipment, in particular to a swimming pool water electrolysis reactor.
Background
Swimming pools are important places for people to enjoy leisure and recreation, and the water quality of the swimming pools is affected in various aspects. For example, the environment, air, rain, dust, sunlight, temperature, etc., can affect swimming pool water quality. For example, when people swim in a swimming pool, human secretions, bacteria, viruses and the like carried by the human secretions can be brought into the swimming pool water, so that a large amount of bacteria can be bred, and if swimming stadiums with unqualified water quality are selected, serious potential safety hazards can be brought.
In order to ensure the sanitation of the swimming pool, the normal natatorium can treat the water of the swimming pool, and the treatment usually adopts a manual or automatic administration mode, but the administration amount is controlled improperly, or the disinfectant is not uniformly distributed in the water of the swimming pool, so that the concentration of residual chlorine in the water of the swimming pool is suddenly high and suddenly low, which can have adverse effects on human bodies, and the mode can only sterilize and can not reduce the ammonia nitrogen content. The organic matters containing ammonia nitrogen in the swimming pool are greatly increased after being accumulated for a period of time, the content of the organic matters is high, the skin and eyes of people can be harmed, the harm degree is high, and particularly, the swimming pool for children is poor in self-made power, the swimming pool water is cool, the organic matters containing ammonia nitrogen are easy to urinate after being stimulated, and the content of the organic matters and bacteria of the ammonia nitrogen is easier to be higher. Thus, efforts are being made in the industry to address how to better purify the pool water.
Disclosure of Invention
In view of the above, the present utility model aims to provide a swimming pool water electrolysis reactor which can sterilize, remove algae and reduce ammonia nitrogen and is convenient for periodic cleaning.
To achieve the object, the utility model provides a swimming pool water electrolysis reactor, which comprises an electrolysis reactor shell and an anode rod; the top end of the electrolytic reactor shell in the length direction is provided with a water outlet, the bottom end of the electrolytic reactor shell in the length direction is provided with a water inlet, and the water inlet is arranged at the tangential position of the electrolytic reactor shell; the electrolytic reactor comprises an electrolytic reactor shell, an anode rod, a flange cover plate, an anode binding post and a cathode binding post, wherein the anode rod is arranged in the electrolytic reactor shell, one end of the anode rod is arranged on the flange cover plate, the flange cover plate is detachably arranged at the end part of the electrolytic reactor shell, which is close to the water outlet, and the anode binding post is connected with the anode binding post, and the cathode binding post is arranged at the side edge of the end part of the swimming pool electrolytic reactor, which is close to the water outlet. The anode binding post is connected with the positive electrode of the power supply, and the cathode binding post is connected with the negative electrode of the power supply. Meanwhile, in view of the fact that the electrolysis efficiency of direct current is higher than that of alternating current, the power supply is a direct current power supply, and the output voltage of the power supply ranges from DC 5V to 24V; the output current of the power supply ranges from 10-100A.
Preferably, a gasket is arranged between the anode rod and the flange cover plate.
Preferably, the flange cover plate and the end part of the electrolytic reactor shell close to the water outlet side are correspondingly provided with a plurality of flange connecting bolt holes uniformly distributed along the circumferential direction. Further, the flange cover plate is connected to the end of the electrolytic reactor shell through a flange. During installation, the flange connection bolt holes on the flange cover plate are aligned with the flange connection bolt holes on the electrolytic reactor shell, then the flange cover plate and the electrolytic reactor shell can be connected through inserting bolts into the flange connection bolt holes and screwing down, and when cleaning is needed, the electrolytic reactor shell can be easily disassembled only by unscrewing the bolts. Of course, the flange cover plate is provided with the rubber sheet with the one side that electrolytic reactor casing contacted, prevents that the infiltration from appearing in junction.
Preferably, the shape of the electrolytic reactor housing is cylindrical, and the shape of the anode rod is bar-shaped.
Preferably, the length of the anode rod inserted into the electrolytic reactor housing is not less than half the length of the electrolytic reactor housing. More preferably, the length of the anode rod inserted into the electrolytic reactor housing is three-fourths of the length of the electrolytic reactor housing, so that a better reaction of the swimming pool water is ensured.
It is also possible that the anode rod comprises a pole piece and a boron doped diamond film, and the boron doped diamond film is coated on the surface of the pole piece. The boron-doped diamond has the characteristics of large hydrogen evolution and oxygen evolution window, and can use a sample with larger voltage to treat swimming pool water by adding three thousandths of salt, and the boron-doped diamond has strong chemical stability and can not react with solute in water or aqueous solution; the boron-doped diamond film has adsorption inertia, compared with other electrode materials, the boron-doped diamond film has low adsorptivity to generated hydroxyl free radicals, free radicals in the solution can not gather on the surface of the boron-doped diamond film in the reaction process, and electrolytic oxidation of organic matters can not be influenced, so that better reaction can be carried out on swimming pool water.
Compared with the prior art, the utility model has the following beneficial effects:
the utility model provides a swimming pool water electrolysis reactor, which comprises an electrolysis reactor shell and an anode rod. The top end of the electrolytic reactor shell in the length direction is provided with a water outlet, the bottom end of the electrolytic reactor shell in the length direction is provided with a water inlet, and the water inlet is arranged at the tangential position of the electrolytic reactor shell; the water inlet is arranged in such a way that swimming pool water spirally rises between the electrolytic reactor shell and the anode rod, so that the reaction time of the swimming pool water in the reactor is prolonged, the swimming pool water can react more thoroughly, and finally flows out from the water outlet. Specifically, when raw water enters through the water inlet arranged on the swimming pool water electrolysis reactor, bacterial algae can be killed under the action of an electric field, and simultaneously organic matters containing ammonia nitrogen in water are oxidized and decomposed at the anode, so that the ammonia nitrogen content in water is reduced, calcium and magnesium ions in water are adsorbed by the cathode, and periodic cleaning can be realized. Therefore, the swimming pool water electrolysis reactor has a simple structure, can kill bacteria and algae in the swimming pool water, can reduce the ammonia nitrogen content in the water, remove calcium and magnesium ions in the water, and can clean the swimming pool water well.
Drawings
FIG. 1 is a schematic cross-sectional view of a swimming pool water electrolysis reactor according to the present utility model;
FIG. 2 is a schematic view of the overall structure of the swimming pool water electrolysis reactor according to the present utility model;
wherein:
1-gasket, 2-bolt, 3-anode rod, 4-electrolytic reactor shell, 5-flange cover plate, 41-water outlet, 42-water inlet, 43-cathode binding post, 31-anode binding post.
Detailed Description
The embodiments described below are only some, but not all, embodiments of the utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1 and 2, the present utility model provides a swimming pool water electrolysis reactor comprising an electrolysis reactor housing 4 and an anode rod 3; a water outlet 41 is formed in the top end of the electrolytic reactor shell 4 in the length direction, a water inlet 42 is formed in the bottom end of the electrolytic reactor shell 4 in the length direction, and the water inlet 42 is formed in the tangential position of the electrolytic reactor shell 4; the anode rod 3 is arranged in the electrolytic reactor shell 4, one end of the anode rod 3 is arranged on a flange cover plate 5, the flange cover plate 5 is detachably arranged at the end part of the electrolytic reactor shell 4, which is close to the water outlet 41, and the anode rod 3 is connected with an anode binding post 31, and a cathode binding post 43 is arranged at the side edge of the end part of the swimming pool water electrolytic reactor, which is close to the water outlet 41. The anode terminal 31 is connected to the positive electrode of the power supply, and the cathode terminal 43 is connected to the negative electrode of the power supply. Meanwhile, in view of the fact that the electrolysis efficiency of direct current is higher than that of alternating current, the power supply is a direct current power supply, and the output voltage of the power supply ranges from DC 5V to 24V; the output current of the power supply ranges from 10-100A.
When the swimming pool water electrolysis reactor is used, firstly, three thousandths of salt is added into swimming pool water, then the water inlet 42 of the swimming pool water electrolysis reactor is connected with a water outlet of the swimming pool, and water added with salt enters from the water inlet 42, and as the water inlet 42 is arranged at the tangential position of the electrolysis reactor shell 4, the swimming pool water spirally rises between the electrolysis reactor shell 4 and the anode rod 3, so that the reaction time of the swimming pool water in the reactor is prolonged, the swimming pool water is more thoroughly reacted, and when the swimming pool water enters, the anode binding post 31 is connected with the anode of a power supply, the cathode binding post 43 is connected with the cathode of the power supply, then the entering swimming pool water is taken as an anode through the anode rod 3, the electrolysis reactor shell 4 is taken as a cathode, bacterial algae can be killed under the action of an electric field, meanwhile, the organic matters containing ammonia nitrogen in the water are oxidatively decomposed at the anode, so that the ammonia nitrogen content in the water is reduced, calcium magnesium ions in the water are absorbed by the cathode to form dirt, and then the water flows out from the water outlet 41. When the inside impurities are to be cleaned, the flange cover 5 may be opened, and the electrolytic reactor case 4 may be made of stainless steel.
Preferably, a gasket 1 is disposed between the anode rod 3 and the flange cover 5 for isolation.
Preferably, the flange cover 5 and the end of the electrolytic reactor housing 4 near the water outlet 41 are provided with flange connection bolt holes. Further, the flange cover plate 5 is fixed to the end of the electrolytic reactor housing 4 by bolts 2. During installation, the flange cover plate 5 and the electrolytic reactor shell 4 can be connected by aligning the flange connection bolt holes on the flange cover plate 5 with the flange connection bolt holes on the electrolytic reactor shell 4 and then inserting the bolts 2 into the flange connection bolt holes and screwing down, and when cleaning is needed, the bolts 2 are only required to be unscrewed and can be easily detached. Of course, the surface of the flange cover plate 5, which is contacted with the electrolytic reactor shell 4, is provided with a rubber sheet to prevent water seepage at the joint.
Preferably, the electrolytic reactor housing 4 has a cylindrical shape, and the anode rod 3 has a rod shape.
Preferably, the length of the anode rod 3 inserted into the electrolytic reactor housing 4 is not less than half the length of the electrolytic reactor housing 4. More preferably, the length of the anode rod 3 inserted into the electrolytic reactor housing 4 is three-fourths the length of the electrolytic reactor housing 4, so that a better reaction of the swimming pool water is ensured.
Preferably, the anode rod 3 comprises a pole core and a boron-doped diamond film, and the boron-doped diamond film is coated on the surface of the pole core. The boron-doped diamond has the characteristics of large hydrogen evolution and oxygen evolution window, can use a sample with larger voltage to treat swimming pool water added with three thousandths of salt, has strong chemical stability, and can not react with solute in water or aqueous solution; the boron-doped diamond film has adsorption inertia, compared with other electrode materials, the boron-doped diamond film has low adsorptivity to generated hydroxyl free radicals, free radicals in the solution can not gather on the surface of the boron-doped diamond film in the reaction process, and electrolytic oxidation of organic matters can not be influenced, so that better reaction can be carried out on swimming pool water.
The utility model provides a swimming pool water electrolysis reactor, which comprises an electrolysis reactor shell 4 and an anode rod 3. A water outlet 41 is formed in the top end of the electrolytic reactor shell 4 in the length direction, a water inlet 42 is formed in the bottom end of the electrolytic reactor shell 4 in the length direction, and the water inlet 42 is formed in the tangential position of the electrolytic reactor shell 4; the water inlet 42 is arranged in such a way that the swimming pool water spirally rises between the electrolytic reactor shell 4 and the anode rod 3, the reaction time of the swimming pool water in the reactor is prolonged, the swimming pool water is enabled to react more thoroughly, and finally the swimming pool water flows out from the water outlet 41. Specifically, when raw water enters through the water inlet 42 arranged on the swimming pool water electrolysis reactor, bacterial algae can be killed under the action of an electric field, and simultaneously organic matters containing ammonia nitrogen in water are oxidized and decomposed at the anode, so that the ammonia nitrogen content in water is reduced, calcium and magnesium ions in water are adsorbed by the cathode, and periodic cleaning can be realized. Therefore, the swimming pool water electrolysis reactor has a simple structure, can kill bacteria and algae in the swimming pool water, can reduce the ammonia nitrogen content in the water, remove calcium and magnesium ions in the water, and can clean the swimming pool water well.
The foregoing disclosure is only illustrative of the preferred embodiments of the present utility model and is not to be construed as limiting the scope of the utility model, which is defined by the appended claims.
Claims (6)
1. A swimming pool water electrolysis reactor, characterized in that: the swimming pool water electrolysis reactor comprises an electrolysis reactor shell and an anode rod; the top end of the electrolytic reactor shell in the length direction is provided with a water outlet, the bottom end of the electrolytic reactor shell in the length direction is provided with a water inlet, and the water inlet is arranged at the tangential position of the electrolytic reactor shell; the electrolytic reactor comprises an electrolytic reactor shell, an anode rod, a flange cover plate, an anode binding post and a cathode binding post, wherein the anode rod is arranged in the electrolytic reactor shell, one end of the anode rod is arranged on the flange cover plate, the flange cover plate is detachably arranged at the end part of the electrolytic reactor shell, which is close to the water outlet, and the anode binding post is connected with the anode binding post, and the cathode binding post is arranged at the side edge of the end part of the swimming pool electrolytic reactor, which is close to the water outlet.
2. The swimming pool water electrolysis reactor of claim 1, wherein: a gasket is arranged between the anode rod and the flange cover plate.
3. The swimming pool water electrolysis reactor of claim 1, wherein: the flange cover plate and the end part of the side, close to the water outlet, of the electrolytic reactor shell are correspondingly provided with a plurality of flange connection bolt holes uniformly distributed along the circumferential direction.
4. A swimming pool water electrolysis reactor according to claim 3, wherein: the flange cover plate is fixed at the end part of the electrolytic reactor shell through bolts.
5. The swimming pool water electrolysis reactor of claim 1, wherein: the shape of the electrolytic reactor shell is cylindrical, and the shape of the anode rod is bar-shaped.
6. The swimming pool water electrolysis reactor of claim 1, wherein: the length of the anode rod inserted into the electrolytic reactor housing is not less than half the length of the electrolytic reactor housing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202322049322.2U CN220703351U (en) | 2023-08-01 | 2023-08-01 | Swimming pool water electrolysis reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322049322.2U CN220703351U (en) | 2023-08-01 | 2023-08-01 | Swimming pool water electrolysis reactor |
Publications (1)
Publication Number | Publication Date |
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CN220703351U true CN220703351U (en) | 2024-04-02 |
Family
ID=90443839
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN202322049322.2U Active CN220703351U (en) | 2023-08-01 | 2023-08-01 | Swimming pool water electrolysis reactor |
Country Status (1)
Country | Link |
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CN (1) | CN220703351U (en) |
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2023
- 2023-08-01 CN CN202322049322.2U patent/CN220703351U/en active Active
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