CN114182274A - Ozone generation and transmission device designed without water pipe - Google Patents
Ozone generation and transmission device designed without water pipe Download PDFInfo
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- CN114182274A CN114182274A CN202111659561.9A CN202111659561A CN114182274A CN 114182274 A CN114182274 A CN 114182274A CN 202111659561 A CN202111659561 A CN 202111659561A CN 114182274 A CN114182274 A CN 114182274A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 480
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 125
- 230000005540 biological transmission Effects 0.000 title claims abstract description 13
- 239000007789 gas Substances 0.000 claims description 100
- 238000007789 sealing Methods 0.000 claims description 60
- 238000004891 communication Methods 0.000 claims description 23
- 230000002093 peripheral effect Effects 0.000 claims description 19
- 238000005868 electrolysis reaction Methods 0.000 claims description 15
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 14
- 239000001257 hydrogen Substances 0.000 claims description 14
- 229910052739 hydrogen Inorganic materials 0.000 claims description 14
- 238000005192 partition Methods 0.000 claims description 2
- 238000009428 plumbing Methods 0.000 claims 8
- 238000000746 purification Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 2
- 230000000149 penetrating effect Effects 0.000 abstract 1
- 239000012528 membrane Substances 0.000 description 16
- 238000010586 diagram Methods 0.000 description 8
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 7
- 229910052802 copper Inorganic materials 0.000 description 7
- 239000010949 copper Substances 0.000 description 7
- 238000004659 sterilization and disinfection Methods 0.000 description 7
- 230000017525 heat dissipation Effects 0.000 description 6
- 238000002955 isolation Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 238000007599 discharging Methods 0.000 description 4
- 230000002159 abnormal effect Effects 0.000 description 3
- 230000002349 favourable effect Effects 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- 239000008213 purified water Substances 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 235000014676 Phragmites communis Nutrition 0.000 description 1
- 241000973497 Siphonognathus argyrophanes Species 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/13—Ozone
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses an ozone generation and transmission device without a water pipe, which comprises an upper box body, a lower end cover and an ozone generator, wherein a cathode water tank chamber and an anode water tank chamber penetrating through the top end and the bottom end are arranged in the upper box body; the lower end cover is hermetically connected to the bottom surface of the upper box body, the bottom surface of the lower end cover is provided with a cathode water inlet pipe, an anode water inlet pipe, a cathode gas-water communicating pipe and an anode gas-water communicating pipe, the cathode water inlet pipe and the cathode gas-water communicating pipe are communicated with the cathode water tank chamber, and the anode water inlet pipe and the anode gas-water communicating pipe are communicated with the anode water tank chamber; the ozone generator is internally provided with a cathode electrolytic cell and an anode electrolytic cell, a cathode water inlet pipe and a cathode gas-water communicating pipe are communicated with the cathode electrolytic cell, and an anode water inlet pipe and an anode gas-water communicating pipe are communicated with the anode electrolytic cell. This application has the effect of accomplishing the miniaturization with equipment.
Description
Technical Field
The invention relates to the technical field of disinfection and sterilization equipment, in particular to an ozone generation and transmission device with a water-free pipe design.
Background
Ozone is used as a strong oxidant, is usually used for sterilization and disinfection due to strong oxidizing capability, generates oxygen after sterilization and disinfection, is not easy to generate secondary pollution, and is relatively environment-friendly sterilization gas. At present, ozone is widely applied to various aspects such as drinking water treatment, medical water treatment, municipal sewage treatment, food disinfection and sterilization, air purification and the like. However, since ozone is extremely easily decomposed and is difficult to store efficiently, it is generally used for the present preparation when ozone is used.
In the related technology, the ozone generation and delivery device comprises a cathode water tank, an anode water tank, a public water tank and an ozone generator, wherein ozone is prepared by the ozone generator, two water inlet hoses are respectively communicated with two nozzles at the bottom end of the ozone generator, the two water inlet hoses are respectively connected with a cathode electrolytic tank and an anode electrolytic tank of the ozone generator, and the other ends of the two water inlet hoses are respectively connected with the cathode water tank and the anode water tank to supply purified water into the ozone generator; the two water inlet hoses are connected with communicating hoses, and one ends of the two communicating hoses, which are far away from the water inlet hoses, are communicated with a common water tank; and the two air outlet hoses are respectively communicated with two nozzles at the top end of the ozone generator and are respectively connected with a cathode electrolytic cell and an anode electrolytic cell of the ozone generator to lead out the gas generated by the cathode electrolytic cell and the anode electrolytic cell.
With respect to the related art in the above, the inventors consider that: the transportation of pure water and the discharge of ozone are realized through each hose to above-mentioned each part, because the hose is more, it is great to arrange the pipeline occupation space, and equipment need provide certain space and arrange the pipeline for equipment size is great, satisfies under the condition of certain ozone production volume, hardly accomplishes the miniaturization with equipment.
Disclosure of Invention
In order to miniaturize the equipment, the application provides an ozone generation and transmission device without a water pipe.
The application provides an ozone generation conveyer of no water pipe design adopts following technical scheme:
an ozone generation and transmission device designed without a water pipe comprises an upper box body, a lower end cover and an ozone generator, wherein the upper box body is vertically arranged, and a cathode water tank chamber and an anode water tank chamber which penetrate through the top end and the bottom end are arranged in the upper box body; the lower end cover is connected to the bottom surface of the upper box body in a sealing mode, a cathode water inlet pipe, an anode water inlet pipe, a cathode gas-water communicating pipe and an anode gas-water communicating pipe are arranged on the bottom surface of the lower end cover, the cathode water inlet pipe and the cathode gas-water communicating pipe are communicated with the cathode water tank chamber, and the anode water inlet pipe and the anode gas-water communicating pipe are communicated with the anode water tank chamber; the ozone generator is internally provided with a cathode electrolytic cell and an anode electrolytic cell, the cathode water inlet pipe and the cathode gas-water communicating pipe are communicated with the cathode electrolytic cell, the anode water inlet pipe and the anode gas-water communicating pipe are communicated with the anode electrolytic cell, the cathode water inlet pipe is used for conveying water into the cathode electrolytic cell, the cathode gas-water communicating pipe is used for discharging hydrogen into the cathode water tank chamber, the anode water inlet pipe is used for conveying water into the anode electrolytic cell, and the anode gas-water communicating pipe is used for discharging ozone into the anode water tank chamber.
By adopting the technical scheme, water is stored in the cathode water tank chamber and the anode water tank chamber, the water in the cathode water tank chamber enters the cathode electrolytic cell through the cathode water inlet pipe, the water in the anode water tank chamber flows into the anode electrolytic cell through the anode water inlet pipe, and the cathode water inlet pipe and the anode water inlet pipe replace two water inlet hoses; the hydrogen that produces in the cathode electrolysis cell is discharged into the cathode water tank indoor through cathode gas water communicating pipe and is collected, the ozone that produces in the anode electrolysis cell is discharged into the anode water tank indoor through anode gas water communicating pipe and is collected, anode gas water communicating pipe and cathode gas water communicating pipe have replaced two hoses of giving vent to anger, alright in order to save the hose of connecting between each part, the space that the pipeline that has arranged occupy has been reduced, make equipment structure compacter, thereby can accomplish the miniaturization with equipment.
Optionally, the ozone generator includes a cathode plate and an anode plate, the cathode plate is hermetically connected to the bottom end of the cathode water inlet pipe and the bottom end of the cathode gas-water communicating pipe, and the anode plate is hermetically connected to the bottom end of the anode water inlet pipe and the bottom end of the anode gas-water communicating pipe; the cathode electrolytic cell is arranged on one side surface of the cathode plate close to the anode plate, a cathode water flow tube and a cathode airflow tube are arranged on the side surface of the cathode plate far away from the anode plate, the cathode water flow tube and the cathode airflow tube are both communicated with the cathode electrolytic cell, the communication position of the cathode water flow tube is higher than that of the cathode airflow tube, the cathode water flow tube is communicated with the pipe orifice of the cathode water inlet tube, and the cathode airflow tube is communicated with the pipe orifice of the cathode gas-water communicating pipe; the anode electrolytic tank is arranged on one side surface of the anode plate close to the cathode plate, the side surface of the anode plate far away from the cathode plate is provided with an anode water flow pipe and an anode airflow pipe, the anode water flow pipe and the anode airflow pipe are both communicated with the anode electrolytic tank, the communication position of the anode water flow pipe is higher than the communication position of the anode airflow pipe, the anode water flow pipe is communicated with the pipe orifice of the anode water inlet pipe, and the anode airflow pipe is communicated with the pipe orifice of the anode gas-water communicating pipe; the cathode plate and one side surface of the anode plate, which are close to each other, are connected in a sealing way, and the cathode electrolytic tank is communicated with the anode electrolytic tank.
By adopting the technical scheme, the water inlet end of the cathode water flow pipe is directly communicated with the pipe orifice of the cathode water inlet pipe, the air outlet end of the cathode airflow pipe is directly communicated with the pipe orifice of the cathode air-water communicating pipe, and the water inlet end of the cathode water flow pipe and the air outlet end of the cathode airflow pipe are arranged at the same end of the cathode plate compared with the case that the water inlet end of the cathode water flow pipe is arranged at the bottom end of the ozone generator, so that a hose at one end connected between the cathode water inlet pipe and the cathode water flow pipe can be omitted; the end of intaking of positive pole rivers pipe directly communicates with positive pole inlet tube mouth of pipe, the end of giving vent to anger of positive pole air current pipe directly communicates with the mouth of pipe of positive pole air water communicating pipe, compare through the end setting of intaking with positive pole rivers pipe in ozone generator's bottom, the end of giving vent to anger with the end setting of the end of giving vent to anger of the end of the positive pole rivers pipe and positive pole air current pipe is in the same end of positive pole plate, alright in order to save one section hose of being connected between positive pole inlet tube and the positive pole rivers pipe, thereby can further reduce the space that the pipeline that arranges occupy, and then can further accomplish the miniaturization with equipment.
Optionally, the top end of the cathode gas-water communicating pipe extends out of the top surface of the lower end cover, and the top end of the anode gas-water communicating pipe extends out of the top surface of the lower end cover.
By adopting the technical scheme, hydrogen generated in the cathode electrolytic cell is discharged into the cathode water tank chamber through the cathode gas-water communicating pipe, the hydrogen drives water in the cathode water tank chamber to roll, the water rolls to drive the ozone generation and transmission device to vibrate to generate abnormal sound, and the ozone generation and transmission device is easy to fall off due to long-time vibration; the ozone that produces in the positive pole electrolysis trough discharges into the positive pole water tank indoor through positive pole air water communicating pipe, ozone drives the indoor water of positive pole water tank and rolls, water rolls and drives ozone and takes place conveyer vibration, produce the abnormal sound, long-time vibration makes ozone take place conveyer and drops easily, because the top of positive pole air water communicating pipe extends the top surface of lower extreme lid, the top of positive pole air water communicating pipe is in higher position, make the influence of exhaust ozone stirring to water less, thereby can reduce the production of abnormal sound and reduce the condition that ozone takes place conveyer and drop and take place.
Optionally, the bottom surface of the lower end cover is provided with a cathode transverse communicating pipe and an anode transverse communicating pipe, the outer wall of the cathode transverse communicating pipe and the outer wall of the anode transverse communicating pipe are fixedly connected to the bottom surface of the lower end cover, the cathode inlet pipe is communicated with the cathode transverse communicating pipe, the anode inlet pipe is communicated with the anode transverse communicating pipe, and the cathode transverse communicating pipe and the anode transverse communicating pipe are connected to an external water source.
By adopting the technical scheme, when water is input into the cathode water tank chamber, the water is input into the cathode transverse communicating pipe, the cathode electrolytic tank is filled with the water firstly, and then the water is continuously injected into the cathode water tank chamber; when water is input into the anode water tank chamber, water is input into the anode transverse communicating pipe, the anode electrolytic tank is filled with water, water is injected into the anode water tank chamber, the cathode transverse communicating pipe and the anode transverse communicating pipe replace two communicating hoses, and therefore the communicating hoses can be omitted, the space occupied by the arrangement pipelines can be further reduced, and further miniaturization of equipment can be achieved.
Optionally, an overflow hole is formed in a partition plate between the cathode water tank chamber and the anode water tank chamber.
Through adopting above-mentioned technical scheme, when only horizontal communicating pipe water delivery of anticathode, water is filled the negative pole electrolysis trough earlier, resume to injecting water in the negative pole water tank room again, when water overflowed the overflow hole, water flows into in the positive pole water tank room through the overflow hole, water in the positive pole water tank room pours into the positive pole electrolysis trough into through the positive pole inlet tube in, design through the overflow hole, on the one hand, only need horizontal communicating pipe water delivery of anticathode, thereby the input of water delivery equipment has been reduced, on the other hand, can replace public water tank through the design of overflow hole, negative pole water tank room can continuously supply water for positive pole water tank room, alright save public water tank, thereby can reduce public water tank and the space that the pipeline that is connected with public water tank occupies, and then can further accomplish the miniaturization with equipment.
Optionally, the cathode transverse communicating pipe on the lower end cover is provided with a water outlet end adjacent to the water outlet end of the cathode transverse communicating pipe on the lower end cover, the cathode transverse communicating pipe on the lower end cover is provided with a water inlet end connected with the water inlet end of the anode transverse communicating pipe in a sealing manner and communicated with the water inlet end of the anode transverse communicating pipe on the lower end cover, and the cathode transverse communicating pipe is connected with an external water source.
By adopting the technical scheme, when the ozone generation and transmission units are spliced, the cathode transverse communicating pipe is used for conveying water, one part of water is filled in the cathode electrolytic tank at first, then the water is continuously injected into the cathode water tank chamber, and the other part of water flows to the adjacent cathode transverse communicating pipe through the cathode transverse communicating pipe; water overflows the overflow hole, water flows into the positive pole water tank indoor through the overflow hole, water in the positive pole water tank indoor partly pours into the positive pole electrolysis trough into through the positive pole inlet tube in, another part is through the horizontal communicating pipe of the horizontal communicating pipe flow direction adjacent positive pole of positive pole, make the indoor rivers intercommunication of conveyer positive pole water tank take place for the ozone of concatenation, form the communicating vessel, can make up water mutually, link directly with the horizontal communicating pipe of adjacent negative pole through the horizontal communicating pipe of negative pole, the horizontal communicating pipe of positive pole links directly with the horizontal communicating pipe of adjacent positive pole, thereby can further save the use of hose, be favorable to further accomplishing the miniaturization with equipment.
Optionally, the top surface of the upper box body is hermetically connected with an upper end cover, the top surface of the upper end cover is fixedly connected with a connecting seat, the connecting seat is located at the top of the anode water tank chamber, an airflow groove is formed in the connecting seat and is communicated with the anode water tank chamber, and a gas pipe is fixedly connected to the top surface of the upper end cover and penetrates through the connecting seat and is communicated with the airflow groove.
Through adopting above-mentioned technical scheme, the indoor hydrogen of cathode water tank enters into the anode water tank through the overflow hole indoor, and hydrogen mixes with the indoor ozone of anode water tank, and the mist rises to collect in the chute, and export ozone through the gas pipe again and take place outside the conveying, need not respectively through the gaseous derivation in hose with cathode water tank and the anode water tank to can further save the use of hose, be favorable to further accomplishing the miniaturization with equipment.
Optionally, the gas outlet end of the gas tube of the upper end cover is connected with the gas inlet end of the gas tube of the adjacent upper end cover in a sealing manner.
Through adopting above-mentioned technical scheme, direct intercommunication between air duct and the adjacent air duct is derived the mist by a pipeline, need not to concentrate the mist that each ozone takes place conveyer and produce through the hose again and derive again to can further save the use of hose, be favorable to further accomplishing the miniaturization with equipment.
Optionally, a plurality of heat dissipation fins are fixedly connected to the circumferential surface of the upper box body.
By adopting the technical scheme, as the peripheral surface of the upper box body is fixedly connected with the plurality of radiating fins, the radiating of heat in the upper box body is accelerated by the radiating fins; because a fan is arranged on one side surface of the upper box body, the heat in the upper box body is further accelerated to be dissipated through the fan.
In summary, the present application includes at least one of the following beneficial technical effects:
water is stored in the cathode water tank chamber and the anode water tank chamber, the water in the cathode water tank chamber enters the cathode electrolytic cell through the cathode water inlet pipe, hydrogen generated in the cathode electrolytic cell is discharged into the cathode water tank chamber through the cathode water-gas communicating pipe to be collected, and the cathode water inlet pipe and the anode water inlet pipe replace two water inlet hoses; the water in the anode water tank chamber flows into the anode electrolytic cell through the anode water inlet pipe, ozone generated in the anode electrolytic cell is discharged into the anode water tank chamber through the anode gas-water communicating pipe for collection, the anode gas-water communicating pipe and the cathode gas-water communicating pipe replace two gas outlet hoses, so that hoses connected among all parts can be omitted, the space occupied by the arrangement pipelines is reduced, the equipment structure is more compact, and the equipment can be miniaturized;
the water inlet end of the cathode water flow pipe is directly communicated with the pipe orifice of the cathode water inlet pipe, the gas outlet end of the cathode airflow pipe is directly communicated with the pipe orifice of the cathode gas-water communicating pipe, and compared with the method that the water inlet end of the cathode water flow pipe is arranged at the bottom end of the ozone generator, the water inlet end of the cathode water flow pipe and the gas outlet end of the cathode airflow pipe are arranged at the same end of the cathode plate, a hose at one end connected between the cathode water inlet pipe and the cathode water flow pipe can be omitted; the water inlet end of the anode water flow pipe is directly communicated with the pipe orifice of the anode water inlet pipe, the gas outlet end of the anode airflow pipe is directly communicated with the pipe orifice of the anode gas-water communicating pipe, and compared with the method that the water inlet end of the anode water flow pipe is arranged at the bottom end of the ozone generator, the water inlet end of the anode water flow pipe and the gas outlet end of the anode airflow pipe are arranged at the same end of the anode plate, a section of hose connected between the anode water inlet pipe and the anode water flow pipe can be omitted, so that the space occupied by the arrangement pipeline can be further reduced, and the equipment can be further miniaturized;
when only horizontal communicating pipe water delivery of anticathode, water is earlier to fill cathode electrolysis trough, resume to injecting water in the cathode water tank room, water when overflowing the overflow hole, water flows into in the anode water tank room through the overflow hole, water in the anode water tank room pours into in the anode electrolysis trough through the positive pole inlet tube, design through the overflow hole, on the one hand, only need horizontal communicating pipe water delivery to the anticathode, thereby the input of water delivery equipment has been reduced, on the other hand, can replace public water tank through the design of overflow hole, cathode water tank room can last for anode water tank room supplies water, alright in order to save public water tank, thereby can reduce public water tank and the space that the pipeline that is connected with public water tank occupied, and then can further accomplish the miniaturization with equipment.
Drawings
Figure 1 is the application of the embodiment of the ozone generation conveyor structure diagram.
Figure 2 is the ozone generation conveyor middle and upper box section structure diagram.
Figure 3 is a schematic view of the upper end cap of the ozone generating and delivering device.
Figure 4 is a schematic cross-sectional view of the upper end cap and float rod of the ozone generating and delivering device.
Fig. 5 is an enlarged schematic view of a portion a in fig. 1.
Figure 6 is a schematic view of the structure of the upper end cap and the float rod in the ozone generating and conveying device.
Figure 7 is another perspective sectional structure diagram of the upper box body of the ozone generating and conveying device.
Figure 8 is the ozone generating conveyor lower end cover and the adapter rack section structure diagram.
Figure 9 is the ozone generation conveyor lower end cap structure diagram.
Fig. 10 is an enlarged schematic view of a portion B in fig. 1.
Figure 11 is the ozone generating conveyor in the switching frame structure diagram.
Figure 12 is the ozone generating conveyor in the switching frame structure diagram.
Figure 13 is the ozone generating conveyor in the switching frame structure diagram.
Figure 14 is an exploded view of the ozone generator of the ozone generating conveyor.
Figure 15 is another perspective exploded view of the ozone generator of the ozone generating conveyor.
Description of reference numerals:
1. an upper box body; 11. a cathode water tank chamber; 12. an anode water tank chamber; 13. an overflow aperture; 14. a heat dissipating fin; 15. a placement groove; 16. a fan; 17. a baffle plate; 18. a power supply cover; 2. an upper end cover; 21. a first seal groove; 22. an anode limiting plate; 23. a cathode limiting plate; 24. a first seal ring; 25. a connecting seat; 251. an air flow groove; 26. a gas pipe; 261. a male interface; 262. a female interface; 27. an L-shaped quick female joint; 28. an L-shaped quick male connector; 281. a second elastic plate; 282. a second fixture block; 283. a pressing plate; 29. a first elastic plate; 291. a first clamping block; 3. a lower end cover; 301. a fourth elastic plate; 3011. a third fixture block; 31. a second seal groove; 32. a second seal ring; 33. a cathode transverse communicating tube; 34. an anode transverse communicating pipe; 35. a cathode water inlet pipe; 36. an anode water inlet pipe; 37. a cathode gas-water communicating pipe; 38. an anode gas-water communicating pipe; 39. a third elastic plate; 391. a limiting block; 4. an ozone generator; 401. a cathode pre-fabricated film; 402. a cathode collector plate; 403. anode pre-membrane; 404. an anode collector plate; 405. a cathode pad; 406. a cathode side plate; 407. an anode gasket; 408. an anode side plate; 41. positioning a plate; 411. a stopper; 412. a conductive interface; 42. a cathode electrode plate; 43. a cathode plate; 431. a cathodic electrolysis cell; 432. a cathode seal groove; 44. a proton exchange membrane; 45. a first slide plate; 451. a first roller; 452. a cathode water flow sealing groove; 453. a cathode sealing cushion block; 4531. a cathode water flow hole; 4532. a cathode airflow aperture; 454. a cathode water flow tube; 455. a cathode gas flow tube; 46. an anode electrode plate; 47. an anode plate; 471. an anodic electrolytic cell; 472. an anode sealing groove; 48. a second slide plate; 481. a second roller; 482. an anode water flow sealing groove; 483. an anode sealing cushion block; 4831. an anode water flow hole; 4832. an anode gas flow aperture; 484. an anode water flow tube; 485. an anode gas flow tube; 5. a limiting ring; 6. a cue stick; 61. a nut; 62. a support plate; 63. a gas seal ring; 64. a deformation groove; 66. a center frame; 661. a base plate; 662. a first notch; 663. a second notch; 664. a limiting strip; 67. a top plate; 68. a float switch; 7. a transfer rack; 71. a chute; 72. a sliding table; 721. a boss; 73. a third notch; 74. a support plate; 741. a separator plate; 742. a conductive copper reed; 75. a fixing plate; 751. and (4) a slot.
Detailed Description
The present application is described in further detail below with reference to figures 1-15.
The embodiment of the application discloses conveyer takes place for ozone with mosaic structure. Referring to fig. 1, the ozone generating and conveying device comprises an upper box body 1, an upper end cover 2, a lower end cover 3, an adapter frame 7 and an ozone generator 4, wherein the upper box body 1 is vertically arranged, the upper end cover 2 is hermetically connected to the top end of the upper box body 1, the lower end cover 3 is hermetically connected to the bottom end of the upper box body 1, the adapter frame 7 is installed on the bottom surface of the lower end cover 3, and the ozone generator 4 is installed on the bottom surface of the adapter frame 7; the switching frame 7 is used for detachably connecting the ozone generator 4, the lower end cover 3 is used for allowing external pure water to enter the ozone generator 4 through the lower end cover 3, the ozone generator 4 is used for electrolyzing the pure water to generate ozone, water vapor generated in the ozone generator 4 is communicated with the upper box body 1 through the lower end cover 3, the upper box body 1 is used for water vapor communication, storage and gas output, and the upper end cover 2 is used for outputting the gas in the upper box body 1 to the outside.
Referring to fig. 2, the upper box body 1 is a cuboid, a cathode water tank chamber 11 and an anode water tank chamber 12 are arranged inside the upper box body 1, the cathode water tank chamber 11 is used for storing purified water and hydrogen for transportation, the anode water tank chamber 12 is used for storing purified water and ozone for transportation, the cathode water tank chamber 11 and the anode water tank chamber 12 are both vertically arranged and communicated with the bottom end face of the upper box body 1 and the top end face of the upper box body 1, the cathode water tank chamber 11 and the anode water tank chamber 12 are both cuboid cavities, and the cathode water tank chamber 11 and the anode water tank chamber 12 are symmetrically arranged about the upper box body 1; be provided with overflow hole 13 on the baffle between 11 and the positive pole water tank room 12 of negative pole water tank room, overflow hole 13 and 11 and the positive pole water tank room 12 intercommunications of negative pole water tank room, and the pure water in the 11 negative pole water tank rooms can flow into in the positive pole water tank room 12 through overflow hole 13, and public water tank can be replaced in the design of overflow hole 13, has reduced the space that public water tank and the pipeline of being connected with public water tank occupy.
Referring to fig. 1, a plurality of heat dissipation fins 14 are integrally formed on the circumferential surface of the upper box body 1, the heat dissipation fins 14 are vertically arranged and uniformly distributed along the circumferential surface of the upper box body 1, and the heat dissipation in the upper box body 1 can be accelerated by using the heat dissipation fins 14; a placing groove 15 is formed between the radiating fins 14 on one side surface of the upper box body 1, the distance between the placing groove 15 and the cathode water tank chamber 11 is equal to the distance between the placing groove 15 and the anode water tank chamber 12, a fan 16 is arranged in the placing groove 15, the fan 16 is a frameless fan 16, a motor of the fan 16 is fixedly connected to the bottom of the placing groove 15, and the fan 16 is used for further accelerating the heat dissipation of the upper box body 1; the side of upper portion box body 1 one side far away from fan 16 integrated into one piece has two baffles 17, and two baffles 17 are vertical, and are located the both sides side of upper portion box body 1 side respectively, are provided with power lid 18 between two baffles 17, are used for placing the power and are used for placing the control drive circuit of control ozone generation conveyer operation between power lid 18 and the baffle 17.
Referring to fig. 2 and 3, the upper end cover 2 is a rectangular flat plate, the upper end cover 2 is fixedly connected to the top end face of the upper box body 1, the top end of the cathode water tank chamber 11 is located on the bottom face of one end of the upper end cover 2, the top end of the anode water tank chamber 12 is located on the bottom face of the other end of the upper end cover 2, the bottom face of the upper end cover 2 is provided with a first sealing groove 21, an anode limiting plate 22 arranged around the port of the anode water tank chamber 12 is integrally formed at the bottom of the first sealing groove 21, the anode limiting plate 22 is located in the anode water tank chamber 12, and the outer peripheral face of the anode limiting plate 22 is attached to the inner wall of the anode water tank chamber 12; a cathode limiting plate 23 arranged around the port of the cathode water tank chamber 11 in a circle is integrally formed at the bottom of the first sealing groove 21, the cathode limiting plate 23 is positioned in the cathode water tank chamber 11, and the outer peripheral surface of the cathode limiting plate 23 is attached to the inner wall of the cathode water tank chamber 11; the outer peripheral face of positive pole limiting plate 22 and negative pole limiting plate 23 all overlaps and is equipped with first sealing washer 24, and one side integrated into one piece that two first sealing washers 24 are adjacent, and first sealing washer 24 is located first seal groove 21, and first sealing washer 24 butt is in the top terminal surface of upper portion box body 1, seals upper end cover 2 and 1 top of upper portion box body through first sealing washer 24, effectively prevents that gas from escaping.
Referring to fig. 2 and 4, a connecting seat 25 is integrally formed on the top surface of the upper end cover 2, the connecting seat 25 is located right above the anode water tank chamber 12, an airflow groove 251 is formed in the connecting seat 25, and the airflow groove 251 is communicated with the bottom surface of the upper end cover 2; the gas pipe 26 is integrally formed on the top surface of the upper end cover 2, the gas pipe 26 is arranged along the length direction of the upper end cover 2, the gas pipe 26 penetrates through the connecting seat 25, the gas pipe 26 is communicated with an airflow groove 251 of the connecting seat 25, hydrogen in the cathode water tank chamber 11 is transported into the anode water tank chamber 12 through an overflow hole 13, the hydrogen and ozone are mixed and collected to the airflow groove 251 and then are led out of the ozone generation and transmission device through the gas pipe 26, the gas pipe 26 is used for replacing hoses which are respectively connected with the cathode water tank chamber 11 and the anode water tank chamber 12 and lead the gas out, and the gas pipe 26 has the characteristics of small volume and compact connection with the upper end cover 2, so that the space occupied by the hoses can be reduced, and the miniaturization of equipment is facilitated; the outer peripheral surface of the gas outlet end of the gas pipe 26 is integrally formed with a male connector 261, the gas inlet end of the gas pipe 26 is sleeved with a female connector 262, and the female connector 262 is integrally formed at the end of the gas inlet end of the gas pipe 26; the male connector 261 is hermetically connected with an L-shaped quick female connector 27, and the inner wall of the female connector 262 is hermetically connected with an L-shaped quick male connector 28; when a plurality of ozone generating and conveying devices are spliced, the male connector 261 is inserted into the female connector 262 of the adjacent gas pipe 26 and is connected in a sealing manner, the mixed gas in each upper box body 1 is discharged from the same gas path through the splicing of the gas pipes 26, and the spliced gas pipes 26 replace the cathode common gas pipe and the anode common gas pipe, so that the space occupied by the cathode common gas pipe and the anode common gas pipe can be reduced.
Referring to fig. 1 and 3, a first elastic plate 29 is integrally formed on the top surface of the upper end cover 2, one end of the first elastic plate 29 extends out of the upper end cover 2 and is located at the same end of the upper end cover 2 as the male connector 261, the first elastic plate 29 is located on one side of the gas tube 26 away from the power supply cover 18, a first clamping block 291 is integrally formed on one side surface of the first elastic plate 29 close to the first connector, a limiting ring 5 is integrally formed on the outer peripheral surface of the L-shaped quick female connector 27, the axis of the limiting ring 5 is collinear with the axis of the gas tube 26, and the first clamping block 291 is clamped on the limiting ring 5; the side of the limit ring 5 near the gas pipe 26 is provided with a first guiding inclined surface, and the side of the first block 291 away from the first elastic plate 29 is provided with a second guiding inclined surface matched with the first guiding inclined surface.
Referring to fig. 1 and 5, a second elastic plate 281 is integrally formed on the outer peripheral surface of the L-shaped quick male connector 28, the second elastic plate 281 is parallel to the female connector 262, a second stopper 282 is integrally formed on a side surface of the second elastic plate 281 close to the female connector 262, a pressing plate 283 is integrally formed on a side surface of the second elastic plate 281 far from the female connector 262, the pressing plate 283 is located at an end portion of the second elastic plate 281, a stopper ring 5 is also integrally formed on the outer peripheral surface of the female connector 262, an axis of the stopper ring 5 is collinear with an axis of the gas pipe 26, the second stopper 282 is clamped on the stopper ring 5, and a third guide inclined surface matched with the first guide inclined surface is arranged on a side of the second stopper 282 close to the gas pipe 26.
Referring to fig. 1, when a plurality of gas tubes 26 are spliced, the male connector 261 on each gas tube 26 is inserted into the female connector 262 on the adjacent gas tube 26, the first fixture block 291 on the first elastic plate 29 is clamped on the limiting ring 5 on the adjacent female connector 262, and in the splicing process of the gas tubes 26, the first elastic plate 29 is elastically bent during the sliding process of the first guide inclined plane and the second guide inclined plane, so that the gas tubes 26 are continuously inserted, and the first fixture block 291 is clamped on the limiting ring 5, thereby realizing the splicing between the adjacent upper end covers 2.
Referring to fig. 2 and 4, a ball float rod 6 is vertically arranged in the anode water tank chamber 12, the top end of the ball float rod 6 penetrates through the top surface of the connecting seat 25, a nut 61 is connected with an end thread, the nut 61 abuts against the top surface of the connecting seat 25, the ball float rod 6 is located in the airflow groove 251, a supporting plate 62 is integrally formed on the periphery of the top end of the ball float rod 6, the supporting plate 62 is located in the airflow groove 251, a gas sealing ring 63 is sleeved on the top end of the ball float rod 6, the gas sealing ring 63 is located on the top surface of the supporting plate 62, and the gas sealing ring 63 abuts against the bottom of the airflow groove 251.
Referring to fig. 4, a deformation groove 64 is formed in the end surface of the bottom end of the ball lever 6, two ends of the deformation groove 64 are communicated with the circumferential surface of the ball lever 6, an annular clamping groove is formed in the circumferential surface of the bottom end of the ball lever 6, a center frame 66 is arranged at the bottom end of the ball lever 6, the center frame 66 is cylindrical, a bottom plate 661 is integrally formed on the inner circumferential surface of the center frame 66, the ball lever 6 penetrates through the middle of the bottom plate 661, and the bottom plate 661 is clamped in the annular clamping groove.
Referring to fig. 2 and 6, two first notches 662 symmetrically arranged are arranged on the peripheral surface of the central frame 66, the first notches 662 are communicated with the interior of the central frame 66, the first notches 662 are positioned above the bottom plate 661, two second notches 663 symmetrically arranged are arranged on the peripheral surface of the central frame 66, the second notches 663 are communicated with the interior of the central frame 66, the second notches 663 are communicated with the bottom surface of the central frame 66, the second notches 663 are positioned below the bottom plate 661, and the first notches 662 are arranged in a staggered manner with the second notches 663; the peripheral integrated into one piece of centre frame 66 has four spacing 664, and four spacing 664 vertical settings, four spacing 664 around centre frame 66 a week evenly distributed, four spacing 664 butt in the inner wall of positive pole water tank room 12, utilize spacing 664 butt positive pole water tank room 12 inner wall, can keep the ball arm float 6 in vertical state, and centre frame 66 just is in vertical state.
Referring to fig. 2 and 4, a top plate 67 is sleeved on the cue 6 and integrally formed, the top plate 67 is positioned in the central frame 66 and at the top end of the central frame 66, and two through holes symmetrically arranged are formed in the top surface of the top plate 67; the ball cock 68 is sleeved on the ball cock rod 6, the ball cock 68 can slide on the ball cock rod 6, the ball cock 68 is positioned in the center frame 66 and positioned between the top plate 67 and the bottom plate 661, the rising of the buoyancy force of the water on the ball cock 68 can control the closing of the water flow entering the upper box body 1, the ball cock 68 returns to the original position and can control the opening of the water flow entering the upper box body 1, and the top plate 67 is positioned below the overflow hole 13.
In-process at electrolytic water preparation ozone, the liquid level of the water in the negative pole water tank room 11 can rise gradually, when the liquid level of water surpassed overflow hole 13, water in the negative pole water tank room 11 can flow to in the positive pole water tank room 12, make up water in the positive pole water tank room 12, design through overflow hole 13, can replace public water tank, the space that public water tank occupy can be saved, the hose that public water tank connects also can be saved, the space that the pipeline that arranges occupy has been reduced, make equipment structure compacter, thereby can accomplish the miniaturization with equipment.
When the liquid level in the anode water chamber 12 gradually rises, the water flow drives the float switch 68 to rise, the float switch 68 controls the water flow entering the upper box body 1 to stop, and when the liquid level in the anode water chamber 12 gradually falls, the float switch 68 returns to the original position, and the float switch 68 can control the water flow entering the upper box body 1 to be switched on.
The center frame 66 is sleeved outside the float switch 68, and the rising ozone gas in the anode water chamber 12 acts on the center frame 66, so that the rising ozone gas drives the float switch 68 to rise, and the float switch 68 can more accurately control the water flow to enter the upper box body 1.
Referring to fig. 7 and 8, the lower end cover 3 is a cuboid flat plate, the lower end cover 3 is fixedly connected to the bottom end face of the upper box body 1, the 11 bottom ends of the cathode water tank chambers are located on the top face of the 3 one ends of the lower end cover, the 12 bottom ends of the anode water tank chambers are located on the top face of the 3 other ends of the lower end cover, the 3 top faces of the lower end cover are provided with second seal grooves 31, the same integrated into one piece of the tank bottom of the second seal grooves 31 is provided with anode limiting plates 22 arranged around the 12 port of the anode water tank chambers and cathode limiting plates 23 arranged around the 11 port of the cathode water tank chambers, the outer peripheral faces of the anode limiting plates 22 and the cathode limiting plates 23 are all sleeved with second seal rings 32, one side of the two adjacent second seal rings 32 is integrally formed, the second seal rings 32 are located in the second seal grooves 31, and the second seal rings 32 are abutted to the bottom end face of the upper box body 1.
Referring to fig. 1, 9 and 10, a cathode transverse communication pipe 33 and an anode transverse communication pipe 34 are integrally formed on the bottom surface of the lower end cover 3, the cathode transverse communication pipe 33 and the anode transverse communication pipe 34 are parallel to each other and are arranged along the length direction of the lower end cover 3, and both ends of the cathode transverse communication pipe 33 and the anode transverse communication pipe 34 extend out of the upper end cover 2; the end outer peripheral face of intaking of the horizontal communicating pipe 33 of negative pole and the end outer peripheral face of intaking of the horizontal communicating pipe 34 of positive pole all overlap and are equipped with female interface 262, two female interface 262 respectively integrated into one piece in the horizontal communicating pipe 33 of negative pole and the horizontal communicating pipe 34 of positive pole, two female interface 262 outer peripheral faces all overlap and are equipped with spacing ring 5 and integrated into one piece, equal sealing connection has the quick male joint 28 of L type on two female interface 262, the quick male joint 28 global integrated into one piece of L type has second elastic plate 281, second elastic plate 281 is parallel to each other with female interface 262, second fixture block 282 joint is on spacing ring 5, float switch 68 receives the buoyancy of water and rises and to control the closing of the rivers that get into the horizontal communicating pipe 33 of negative pole, float switch 68 resumes to the opening of the rivers that can control to get into the horizontal communicating pipe 33 of negative pole in situ.
Referring to fig. 2 and 9, a male connector 261 is integrally formed on the outer peripheral surface of the water outlet end of the cathode transverse communication pipe 33 and the outer peripheral surface of the water outlet end of the anode transverse communication pipe 34, two fourth elastic plates 301 are integrally formed on one side surface of the lower end cover 3 close to the male connector 261, a third clamping block 3011 is integrally formed on the end portion of each fourth elastic plate 301, the two male connectors 261 are located between the two fourth elastic plates 301, the two male connectors 261 are respectively and hermetically connected with an L-shaped quick female connector 27, the outer peripheral surface of each L-shaped quick female connector 27 is sleeved with a limiting ring 5 and is integrally formed, the third clamping block 3011 is clamped on the limiting ring 5, and the third clamping block 3011 is provided with a sixth guiding inclined surface which is matched with the first guiding inclined surface on the limiting ring 5.
Referring to fig. 2, when a plurality of ozone generating and conveying devices are spliced, the male connector 261 on the cathode transverse communication pipe 33 is inserted into the female connector 262 on the adjacent cathode transverse communication pipe 33 and is connected in a sealing manner, the male connector 261 on the anode transverse communication pipe 34 is inserted into the female connector 262 on the adjacent anode transverse communication pipe 34 and is connected in a sealing manner, the third clamping block 3011 is clamped on the limit ring 5, in the process of inserting the male connector 261, the sixth guide inclined plane slides on the first guide inclined plane, the fourth elastic plate 301 is bent elastically, the cathode transverse communication pipe 33 and the anode transverse communication pipe 34 are continuously pushed, the third clamping block 3011 is clamped on the limit ring 5, and therefore the lower end covers 3 can be spliced.
Referring to fig. 2 and 9, a cathode inlet pipe 35 and an anode inlet pipe 36 are integrally formed on the bottom surface of the lower end cover 3, the cathode inlet pipe 35 and the anode inlet pipe 36 are vertically arranged, the cathode inlet pipe 35 and the anode inlet pipe 36 are positioned between the cathode transverse communicating pipe 33 and the anode transverse communicating pipe 34, the cathode inlet pipe 35 is communicated with the cathode transverse communicating pipe 33, and the cathode inlet pipe 35 is communicated with the bottom surface of the second seal groove 31 and communicated with the cathode water tank chamber 11; the anode inlet pipe 36 is communicated with the anode transverse communicating pipe 34, and the anode inlet pipe 36 is communicated with the bottom surface of the second seal groove 31 and communicated with the anode water tank chamber 12.
Referring to fig. 2 and 9, a cathode gas-water communicating tube 37 and an anode gas-water communicating tube 38 are integrally formed on the bottom surface of the lower end cover 3, the cathode gas-water communicating tube 37 and the anode gas-water communicating tube 38 are vertically arranged, the cathode gas-water communicating tube 37 and the anode gas-water communicating tube 38 are located between the cathode transverse communicating tube 33 and the anode transverse communicating tube 34, the top end of the cathode gas-water communicating tube 37 passes through the bottom of the second seal groove 31 and extends into the cathode water tank chamber 11, the top end of the anode gas-water communicating tube 38 passes through the bottom of the second seal groove 31 and extends into the anode water tank chamber 12, and the anode gas-water communicating tube 38 is located below the center frame 66; the middle position of the side surface of the lower end cover 3 far away from the power cover 18 is integrally formed with a third elastic plate 39, the third elastic plate 39 is located at the bottom end of the lower end cover 3, a limiting block 391 is integrally formed on the bottom surface of the third elastic plate 39, the limiting block 391 is located at one end of the third elastic plate 39 far away from the lower end cover 3, and a fifth guide inclined plane is arranged on one side of the limiting block 391 far away from the lower end cover 3.
Referring to fig. 8 and 11, the switching frame 7 is fixedly connected to the bottom surface of the lower end cover 3, the switching frame 7 is a rectangular parallelepiped, a sliding groove 71 is formed in the bottom surface of the switching frame 7, the sliding groove 71 is a rectangular parallelepiped, the sliding groove 71 and the switching frame 7 are communicated with one side surface far away from the power supply cover 18, sliding tables 72 are integrally formed on inner walls of two symmetrical sides of the sliding groove 71, the sliding tables 72 are located in notches of the sliding groove 71, bosses 721 are integrally formed on top surfaces of the two sliding tables 72, and the bosses 721 are located at one ends of the sliding tables 72 close to the power supply cover 18.
Referring to fig. 9 and 12, the bottom end of the cathode water inlet pipe 35 and the bottom end of the anode water inlet pipe 36 pass through the bottom of the chute 71, and the bottom end of the cathode gas-water communicating pipe 37 and the bottom end of the anode gas-water communicating pipe 38 pass through the bottom of the chute 71; a third notch 73 is formed in the middle of the side surface of the adapter rack 7 away from the power cover 18, the bottom surface of the third elastic plate 39 abuts against the top surface of the adapter rack 7, the third notch 73 is located right below the third elastic plate 39, and the limiting block 391 is close to the third notch 73.
Referring to fig. 1 and 13, a support plate 74 is integrally formed at the middle position of the top surface of one end of the adapter rack 7 far away from the third notch 73, the top end of the support plate 74 is located between the baffles 17, the support plate 74 is parallel to the power supply cover 18, three isolation plates 741 are integrally formed on the side surface of the support plate 74 close to one side of the power supply cover 18, the three isolation plates 741 are vertically arranged, the bottom ends of the three isolation plates 741 are fixedly connected to the top surface of the adapter rack 7, and the distances between the middle isolation plate 741 and the adjacent isolation plates 741 are equal; two conductive copper spring plates 742 are fixedly connected to the side face of the support plate 74 close to the power supply cover 18, the two conductive copper spring plates 742 are respectively located between the two adjacent isolation plates 741, a fixing plate 75 is integrally formed in the middle of the side face of the adapter frame 7 close to the power supply cover 18, two slots 751 clamped with the bottom ends of the two conductive copper spring plates 742 are formed in the top face of the fixing plate 75, the slots 751 are communicated with the top face of the fixing plate 75 and the bottom face of the fixing plate 75, the bottom ends of elastic parts of the two conductive copper spring plates 742 extend to the bottom face of the adapter frame 7, and the two conductive copper spring plates 742 are electrically connected with a power supply.
Referring to fig. 1 and 14, the top end of the ozone generator 4 is installed in the sliding slot 71 of the adaptor bracket 7, the ozone generator 4 includes a positioning plate 41, a cathode electrode plate 42, a cathode plate 43 and a proton exchange membrane 44, the top end of the positioning plate 41 is disposed at the middle position of the sliding slot 71, and the positioning plate 41 is vertically disposed and disposed along the length direction of the third elastic plate 39.
Referring to fig. 12 and 14, a stopper 411 is integrally formed on the top end surface of the positioning plate 41, the stopper 411 is located in the third notch 73, one side surface of the stopper 411 abuts against the side surface of the limiting block 391 close to the third elastic plate 39, and a fourth guiding inclined surface matched with the fifth guiding inclined surface is arranged on the side of the stopper 411 far away from the limiting block 391; the middle of the positioning plate 41 is hollow, the proton exchange membrane 44 is arranged in the middle of the positioning plate 41, the side surfaces of two sides of the proton exchange membrane 44 are respectively abutted with sealing washers, and the two sealing washers are positioned on the inner side of the positioning plate 41; the side surface of one side of the proton exchange membrane 44 is abutted with a cathode prefabricated membrane 401, the cathode prefabricated membrane 401 is positioned at the inner side of the sealing washer, the side surface of one side of the cathode prefabricated membrane 401 far away from the proton exchange membrane 44 is abutted with a cathode collector plate 402, and the cathode collector plate 402 is positioned at the inner side of the sealing washer; the side surface of the proton exchange membrane 44, which is far away from the cathode prefabricated membrane 401, is abutted with the anode prefabricated membrane 403, the anode prefabricated membrane 403 is positioned on the inner side of the sealing washer, the side surface of the anode prefabricated membrane 403, which is far away from the proton exchange membrane 44, is abutted with the anode collector plate 404, and the anode collector plate 404 is positioned on the inner side of the sealing washer.
Referring to fig. 14 and 15, the cathode electrode plate 42 is fixedly connected to a side surface of one side of the positioning plate 41, the side surface of the cathode electrode plate 42 abuts against a side surface of the cathode collector plate 402, the cathode plate 43 is fixedly connected to a side surface of one side of the cathode electrode plate 42 away from the positioning plate 41, a cathode electrolytic tank 431 is arranged on a side surface of the cathode plate 43 close to the cathode electrode plate 42, a cathode sealing groove 432 is arranged around the cathode electrolytic tank 431 in a circle, and a sealing gasket abuts against the cathode electrode plate 42 is arranged in the cathode sealing groove 432.
Referring to fig. 14, a first sliding plate 45 is integrally formed on the side surface of the cathode plate 43 away from the positioning plate 41, the first sliding plate 45 is rectangular, the first sliding plate 45 is located at the top end of the cathode plate 43, the first sliding plate 45 is located in the chute 71, the bottom surface of the first sliding plate 45 is in sliding fit with the top surface of the boss 721, the side surface of the first sliding plate 45 away from the positioning plate 41 is rotatably connected with a first roller 451, the first roller 451 abuts against the top surface of the sliding table 72, the first roller 451 is located at the end of the first sliding plate 45 away from the boss 721, the length of the boss 721 is greater than the diameter of the first roller 451, and the top surface of the first sliding plate 45 abuts against the bottom surface of the chute 71; the cathode plate 43 has a cathode water flow sealing groove 452 on the top surface thereof, a cathode sealing pad 453 is disposed in the cathode water flow sealing groove 452, and the cathode sealing pad 453 abuts against the bottom end of the cathode water inlet pipe 35 and the bottom end of the cathode gas-water communication pipe 37.
Referring to fig. 12 and 14, a cathode water flow pipe 454 and a cathode airflow pipe 455 are integrally formed on the side of the cathode plate 43 away from the cathode electrolytic bath 431, the cathode water flow pipe 454 and the cathode airflow pipe 455 are vertically arranged, the bottom end of the cathode water flow pipe 454 and the bottom end of the cathode airflow pipe 455 are both communicated with the cathode electrolytic bath 431, the top end of the cathode water flow pipe 454 and the top end of the cathode airflow pipe 455 are both communicated with the bottom of the cathode water flow sealing groove 452, and the length of the cathode water flow pipe 454 is greater than that of the cathode airflow pipe 455; the cathode sealing cushion 453 is provided with a cathode water flow hole 4531 and a cathode airflow hole 4532, the cathode water flow pipe 454 is communicated with the cathode water inlet pipe 35 through the cathode water flow hole 4531, and the cathode airflow pipe 455 is communicated with the cathode gas-water communicating pipe 37 through the cathode airflow hole 4532; the side of the cathode plate 43 far away from the electrolytic bath is fixedly connected with a cathode gasket 405, the side of the cathode gasket 405 far away from the cathode plate 43 is provided with a cathode side plate 406, and the cathode side plate 406 is clamped in the cathode plate 43.
Referring to fig. 13 and 15, the ozone generator 4 further includes an anode electrode plate 46 and an anode plate 47, the anode electrode plate 46 is fixedly connected to a side surface of the positioning plate 41 away from the cathode electrode plate 42, a side surface of the anode electrode plate 46 abuts against a side surface of the anode current collecting plate 404, the anode plate 47 is fixedly connected to a side surface of the anode electrode plate 46 away from the positioning plate 41, an anode electrolytic tank 471 is disposed on a side surface of the anode plate 47 close to the anode electrode plate 46, an anode sealing groove 472 is disposed around the anode electrolytic tank 471, and a sealing gasket is disposed in the anode sealing groove 472 and abuts against the anode electrode plate 46.
Referring to fig. 15, a second sliding plate 48 is integrally formed on the side surface of the anode plate 47 away from the positioning plate 41, the second sliding plate 48 is rectangular, the second sliding plate 48 is located at the top end of the anode plate 47, the second sliding plate 48 is located in the chute 71, the bottom surface of the second sliding plate 48 is in sliding fit with the top surface of the boss 721, the side surface of the second sliding plate 48 away from the positioning plate 41 is rotatably connected with a second roller 481, the second roller 481 abuts against the top surface of the sliding table 72, the second roller 481 is located at one end of the second sliding plate 48 away from the boss 721, the second roller 481 is identical in structure to the first roller 451, the length of the boss 721 is greater than the diameter of the second roller 481, and the top surface of the second sliding plate 48 abuts against the bottom surface of the chute 71; the top surface of the anode plate 47 is provided with an anode water flow sealing groove 482, an anode sealing cushion block 483 is arranged in the anode water flow sealing groove 482, and the anode sealing cushion block 483 abuts against the bottom end of the anode water inlet pipe 36 and the bottom end of the anode gas-water communicating pipe 38.
Referring to fig. 12 and 15, an anode water flow pipe 484 and an anode gas flow pipe 485 are integrally formed on the side surface of the anode plate 47 away from the anode electrolytic tank 471, the anode water flow pipe 484 and the anode gas flow pipe 485 are vertically arranged, the bottom end of the anode water flow pipe 484 and the bottom end of the anode gas flow pipe 485 are both communicated with the anode electrolytic tank 471, the top end of the anode water flow pipe 484 and the top end of the anode gas flow pipe 485 are both communicated with the bottom of the anode water flow sealing groove 482, and the length of the anode water flow pipe 484 is greater than that of the anode gas flow pipe 485; the anode sealing cushion block 483 is provided with an anode water flow hole 4831 and an anode gas flow hole 4832, the anode water flow pipe 484 is communicated with the anode water inlet pipe 36 through the anode water flow hole 4831, and the anode gas flow pipe 485 is communicated with the anode gas water communicating pipe 38 through the anode gas flow hole 4832; the side of the anode plate 47 away from the side of the electrolytic tank is fixedly connected with an anode gasket 407, the side of the anode gasket 407 away from the anode plate 47 is provided with an anode side plate 408, and the anode side plate 408 is clamped in the anode plate 47.
Referring to fig. 13 and 14, two conductive interfaces 412 are inserted into a side surface of the positioning plate 41 away from the stopper 411, the two conductive interfaces 412 are electrically connected to the two conductive copper spring pieces respectively, and the two conductive interfaces 412 are electrically connected to the cathode electrode plate 42 and the anode electrode plate 46 respectively.
When the ozone generator 4 is installed, the first sliding plate 45 and the second sliding plate 48 are detached into the sliding groove 71, the first sliding plate 45 and the second sliding plate 48 slide on the sliding table 72, the fourth guide inclined surface of the stopper 411 abuts against the fifth guide inclined surface of the limiting block 391, the third elastic plate 39 is elastically bent, and the fourth guide inclined surface passes over the fifth guide inclined surface, so that one side surface of the stopper 411 abuts against the side surface of the limiting block 391 close to the lower end cover 3, and the ozone generator 4 is fixed in the sliding groove 71 without fixing the ozone generator 4 through screws; when the ozone generator 4 needs to be disassembled, the limiting block 391 is jacked upwards, the third elastic plate 39 is bent, the abutting state of the limiting block 391 and the stop block 411 is removed, the ozone generator 4 can be pulled out from the sliding groove 71, the convenience of disassembling and assembling the ozone generator 4 by an operator can be improved, and the problem that the ozone generator 4 is not convenient to disassemble and assemble can be further improved.
Because the water inlet pipe and the air-water communicating pipe both extend out of the groove bottom of the chute 71, when the ozone generator 4 is inserted into the chute 71, the ends of the water inlet pipe and the air-water communicating pipe both extrude the sealing cushion blocks, the first sliding plate 45 and the second sliding plate 48 slide on the sliding table 72, the friction force of the water inlet pipe and the air-water communicating pipe to the sealing cushion blocks is large, and the ozone generator 4 is difficult to push; through the design of the boss 721, the first sliding plate 45 and the second sliding plate 48 firstly slide on the sliding table 72, the water inlet pipe and the gas-water communicating pipe are difficult to contact with the sealing cushion block, so that the blocking effect on the ozone generator 4 is small, the first sliding plate 45 and the second sliding plate 48 slide on the boss 721, and the first roller 451 and the second roller 481 slide on the sliding table 72, so that the top surface of the ozone generator 4 abuts against the bottom of the sliding groove 71, thereby reducing the blocking effect when the ozone generator 4 is assembled and disassembled, and further improving the convenience when the ozone generator 4 is assembled and disassembled; when the ozone generator 4 is disassembled, the ozone generator 4 can be disassembled without disassembling the water inlet hose and the air outlet hose, so that the convenience of disassembly and assembly can be further improved.
By introducing water flow into the cathode transverse communicating pipe 33, the water flow is filled in the cathode electrolytic tank 431 through the cathode water inlet pipe 35, and then is injected into the cathode water tank chamber 11 through the cathode water inlet pipe 35, when the liquid level is higher than the overflow hole 13, the water flow in the cathode water tank chamber 11 flows into the anode water tank chamber 12, the water flow in the anode water tank chamber 12 enters the anode electrolytic tank 471 through the anode water inlet pipe 36, the water level in the anode water tank chamber 12 gradually rises, the water in the anode water tank chamber 12 moves the float switch 68 to rise, the water flow entering the cathode transverse communicating pipe 33 stops, and when the float switch 68 falls to the original position, the water flow entering the cathode transverse communicating pipe 33 is opened.
When a plurality of ozone generating and conveying devices are spliced, a plurality of cathode transverse communicating pipes 33 are spliced with each other, a plurality of anode transverse communicating pipes 34 are spliced, and water flow in the cathode transverse communicating pipes 33 flows into each spliced cathode water tank chamber 11 through a cathode water inlet pipe 35; the spliced anode water chamber 12 forms a communicating vessel through the spliced anode transverse communicating tube 34, and can supplement water sources with each other.
The hydrogen produced in the ozone generator 4 flows into the cathode water tank chamber 11 through the cathode gas communicating pipe, the produced ozone flows into the anode water tank chamber 12 through the anode gas water communicating pipe 38, the hydrogen in the cathode water tank chamber 11 flows into the anode water tank chamber 12 through the overflow hole 13, and is mixed with the ozone in the anode water tank chamber 12, the mixed gas rises and collects in the airflow groove 251, and then the ozone is led out through the gas pipe 26 to be transmitted, and the gas in the cathode water tank and the gas in the anode water tank do not need to be led out through hoses respectively, so that the use of the hoses can be further saved, and the miniaturization of the equipment is facilitated. When a plurality of ozone generating and conveying devices are spliced, the mixed gas collected in the gas pipe 26 is discharged through the same gas path without connecting excessive pipelines.
The ozone generating and conveying devices are spliced, the male connector 261 of the cathode transverse communicating pipe 33 is inserted into the female connector 262 on the adjacent cathode transverse communicating pipe 33 and is in sealed connection, the male connector 261 of the anode transverse communicating pipe 34 is inserted into the female connector 262 of the adjacent anode transverse communicating pipe 34 and is in sealed connection, the third clamping blocks 3011 on the two fourth elastic plates 301 are clamped on the limiting rings 5 of the two female connectors 262, and the lower end cover 3 can be spliced; the male connector 261 on the gas pipe 26 is inserted into the female connector 262 on the adjacent gas pipe 26 and is connected in a sealing manner, at the moment, the first clamping block 291 on the first elastic plate 29 is clamped on the limiting ring 5 on the female connector 262, so that the adjacent upper end covers 2 can be spliced, the exposure of pipelines when the ozone generator 4 is spliced is reduced, the space occupied by the pipelines can be reduced, and the equipment can be miniaturized.
The implementation principle of the ozone generation and transmission device without the water pipe design in the embodiment of the application is as follows: water is input into the cathode transverse communicating pipe 33, water flow is filled into the cathode electrolytic tank 431 through the cathode water inlet pipe 35 firstly, then is injected into the cathode water tank chamber 11 through the cathode water inlet pipe 35, the water level in the cathode water tank chamber 11 exceeds the overflow hole 13, the water flow enters the anode water tank chamber 12 through the overflow hole 13, the water in the anode water tank chamber 12 flows into the anode electrolytic tank 471 through the anode water inlet pipe 36, the cathode water inlet pipe 35 and the anode water inlet pipe 36 are more compact than water inlet hoses, and the cathode water inlet pipe 35 and the anode water inlet pipe 36 replace two water inlet hoses; the hydrogen that produces in the cathode electrolytic bath 431 is collected in discharging into negative pole water tank room 11 through negative pole gas water communicating pipe 37, the ozone that produces in the positive pole electrolytic bath 471 is collected in discharging into positive pole water tank room 12 through positive pole gas water communicating pipe 38, negative pole gas water communicating pipe 37 and positive pole gas water communicating pipe 38 are compacter than the hose structure of giving vent to anger, positive pole gas water communicating pipe 38 and negative pole gas water communicating pipe 37 have replaced two hoses of giving vent to anger, alright save the hose of connecting between each part, the space that the pipeline that arranges occupied has been reduced, make equipment structure compacter, thereby can accomplish the miniaturization with equipment.
The above embodiments are preferred embodiments of the present application, and the protection scope of the present application is not limited by the above embodiments, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.
Claims (9)
1. The utility model provides an ozone of no water pipe design takes place conveyer which characterized in that: the ozone water purifier comprises an upper box body (1), a lower end cover (3) and an ozone generator (4), wherein the upper box body (1) is vertically arranged, and a cathode water tank chamber (11) and an anode water tank chamber (12) which penetrate through the top end and the bottom end are arranged in the upper box body (1); the lower end cover (3) is connected to the bottom surface of the upper box body (1) in a sealing mode, a cathode water inlet pipe (35), an anode water inlet pipe (36), a cathode gas-water communicating pipe (37) and an anode gas-water communicating pipe (38) are arranged on the bottom surface of the lower end cover (3), the cathode water inlet pipe (35) and the cathode gas-water communicating pipe (37) are communicated with the cathode water tank chamber (11), and the anode water inlet pipe (36) and the anode gas-water communicating pipe (38) are communicated with the anode water tank chamber (12); be provided with cathode electrolysis groove (431) and positive pole electrolysis trough (471) in ozone generator (4), negative pole inlet tube (35) with negative pole gas water communicating pipe (37) communicate in negative pole electrolysis trough (431), positive pole inlet tube (36) with positive pole gas water communicating pipe (38) communicate in positive pole electrolysis trough (471), negative pole inlet tube (35) be used for to water transmission in negative pole electrolysis trough (431), negative pole gas water communicating pipe (37) be used for to discharge hydrogen in negative pole water tank room (11), positive pole inlet tube (36) be used for to water transmission in positive pole electrolysis trough (471), positive pole gas water communicating pipe (38) be used for to discharge ozone in positive pole water tank room (12).
2. The non-plumbing ozone generating conveyor of claim 1, wherein: the ozone generator (4) comprises a cathode plate (43) and an anode plate (47), wherein the cathode plate (43) is connected to the bottom end of the cathode water inlet pipe (35) and the bottom end of the cathode gas-water communicating pipe (37) in a sealing mode, and the anode plate (47) is connected to the bottom end of the anode water inlet pipe (36) and the bottom end of the anode gas-water communicating pipe (38) in a sealing mode; the cathode electrolytic tank (431) is arranged on one side surface of the cathode plate (43) close to the anode plate (47), the side surface of the cathode plate (43) far away from the anode plate (47) is provided with a cathode water flow pipe (454) and a cathode airflow pipe (455), the cathode water flow pipe (454) and the cathode airflow pipe (455) are both communicated with the cathode electrolytic tank (431), the communication position of the cathode water flow pipe (454) is higher than the communication position of the cathode airflow pipe (455), the cathode water flow pipe (454) is communicated with the nozzle of the cathode water inlet pipe (35), and the cathode airflow pipe (455) is communicated with the nozzle of the cathode gas-water communicating pipe (37); the anode electrolytic tank (471) is arranged on one side surface of the anode plate (47) close to the cathode plate (43), the side surface of the anode plate (47) far away from one side of the cathode plate (43) is provided with an anode water flow pipe (484) and an anode airflow pipe (485), the anode water flow pipe (484) and the anode airflow pipe (485) are both communicated with the anode electrolytic tank (471), the communication position of the anode water flow pipe (484) is higher than the communication position of the anode airflow pipe (485), the anode water flow pipe (484) is communicated with the nozzle of the anode water inlet pipe (36), and the anode airflow pipe (485) is communicated with the nozzle of the anode gas-water communicating pipe (38); the side surfaces of the cathode plate (43) and the anode plate (47) close to each other are connected in a sealing way, and the cathode electrolytic tank (431) is communicated with the anode electrolytic tank (471).
3. The non-plumbing ozone generating conveyor of claim 1, wherein: the top end of the cathode gas-water communicating pipe (37) extends out of the top surface of the lower end cover (3), and the top end of the anode gas-water communicating pipe (38) extends out of the top surface of the lower end cover (3).
4. The non-plumbing ozone generating conveyor of claim 1, wherein: the utility model discloses a water purification device, including bottom end cover (3), bottom end cover (3) bottom surface is provided with horizontal communicating pipe of negative pole (33) and horizontal communicating pipe of positive pole (34), the outer wall of the horizontal communicating pipe of negative pole (33) with the outer wall fixed connection of the horizontal communicating pipe of positive pole (34) in the bottom surface of bottom end cover (3), negative pole inlet tube (35) with the horizontal communicating pipe of negative pole (33) intercommunication, positive pole inlet tube (36) with the horizontal communicating pipe of positive pole (34) intercommunication, the horizontal communicating pipe of negative pole (33) with external water source is all connected to the horizontal communicating pipe of positive pole (34).
5. The non-plumbing ozone generating conveyor of claim 4 wherein: an overflow hole (13) is formed in a partition plate between the cathode water tank chamber (11) and the anode water tank chamber (12).
6. The non-plumbing ozone generating conveyor of claim 5, wherein: on lower extreme cover (3) the horizontal communicating pipe of negative pole (33) goes out water end and adjacent on lower extreme cover (3) the horizontal communicating pipe of negative pole (33) is intake end sealing connection and is linked together, on lower extreme cover (3) the horizontal communicating pipe of positive pole (34) goes out water end and adjacent on lower extreme cover (3) the horizontal communicating pipe of positive pole (34) advances water pipe sealing connection and intercommunication, the horizontal communicating pipe of negative pole (33) is connected with external water source.
7. The non-plumbing ozone generating and conveying apparatus of claim 5, wherein: the top surface of the upper box body (1) is connected with an upper end cover (2) in a sealing mode, the top surface of the upper end cover (2) is fixedly connected with a connecting seat (25), the connecting seat (25) is located at the top of an anode water tank chamber (12), an airflow groove (251) is formed in the connecting seat (25), the airflow groove (251) is communicated with the anode water tank chamber (12), the top surface of the upper end cover (2) is fixedly connected with a gas pipe (26), and the gas pipe (26) penetrates through the connecting seat (25) and is communicated with the airflow groove (251).
8. The non-plumbing ozone generating conveyor of claim 7 wherein: the gas outlet end of the gas pipe (26) of the upper end cover (2) is connected with the gas inlet end of the gas pipe (26) of the adjacent upper end cover (2) in a sealing mode.
9. The non-plumbing ozone generating conveyor of claim 1, wherein: the peripheral surface of the upper box body (1) is fixedly connected with a plurality of radiating fins (14); the ozone generating and conveying device is characterized in that a fan (16) is installed on the radiating fin (14) on one side of the upper box body (1), and a control driving circuit used for controlling the operation of the ozone generating and conveying device is arranged on one side, opposite to the fan (16), of the upper box body (1).
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