CN114318382B - Ozone generation and transmission device with mesopore overcurrent design - Google Patents

Abstract

The invention discloses an ozone generation and transmission device with a mesoporous flow-through design, which comprises an upper box body and a lower end cover, wherein the upper box body is vertically arranged, 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, an overflow hole is formed in a partition plate between the cathode water tank chamber and the anode water tank chamber, and the lower end cover is connected with the bottom surface of the upper box body in a sealing way. The device has the effect of miniaturizing the device.

Description

Ozone generation and transmission device with mesopore overcurrent design

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 mesoporous overcurrent design.

Background

Ozone is used as a strong oxidant, has strong oxidizing capability, 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, generates oxygen after the ozone is disinfected, and is difficult to generate secondary pollution, thus being a relatively environment-friendly disinfection and sterilization gas. However, ozone is very easy to decompose and is difficult to store effectively, so that it is generally used in the present process when ozone is used.

In the related art, the ozone generating and conveying 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 a communication hose, and one ends of the two communication hoses, which are far away from the water inlet hose, are communicated with the public water tank; the two air outlet hoses are respectively communicated with two nozzles at the top end of the ozone generator, the two air outlet hoses are respectively connected with a cathode electrolytic tank and an anode electrolytic tank of the ozone generator, the other ends of the two air outlet hoses are respectively connected with a cathode water tank and an anode water tank, and gas generated by the cathode electrolytic tank and the anode electrolytic tank is led out through the cathode water tank and the anode water tank; in the process of preparing ozone, the liquid level of water in the cathode water tank gradually rises, the liquid level of water in the anode water tank gradually decreases, and excessive water in the cathode water tank is timely supplemented into the anode water tank through the public water tank.

With respect to the related art in the above, the inventors consider that: among the above-mentioned technical scheme, realize the intercommunication between negative pole water tank and the positive pole water tank through public water tank, but public water tank occupation space is great in equipment, and the pipeline of connecting public water tank is also more for public water tank occupation equipment's space further increases, makes equipment size great, under the condition that satisfies certain ozone production volume, hardly accomplish the miniaturization with equipment.

Disclosure of Invention

In order to miniaturize the equipment, the application provides an ozone generating and conveying device with a mesoporous overcurrent design.

The application provides an ozone generation conveyer of mesopore overcurrent design adopts following technical scheme:

the utility model provides an ozone generation conveyer of mesopore overflow design, ozone generation conveyer includes upper portion box body and lower extreme cover, upper portion box body is vertical to be set up, be provided with in the upper portion box body and run through cathode water tank room and the positive pole water tank room of top and bottom, the cathode water tank room with overflow aperture has been seted up on the baffle between the positive pole water tank room, lower extreme cover sealing connection in the bottom surface of upper portion box body.

Through adopting above-mentioned technical scheme, at the in-process of electrolysis water preparation ozone, the liquid level of the indoor water of cathode water tank can rise gradually, when the liquid level of water exceeds the overflow aperture, the indoor water of cathode water tank can flow to the positive pole water tank in, make up water to the positive pole water tank in, through the design of overflow aperture, can replace public water tank, can save the space that public water tank occupy, also can save the hose that public water tank connects, reduced the space that the pipeline of arranging occupy for equipment structure is compacter, thereby can accomplish the miniaturization with equipment.

Optionally, the ozone generating and conveying device further comprises an ozone generator, wherein the ozone generator is arranged on the bottom surface of the lower end cover, and a cathode electrolytic tank and an anode electrolytic tank are arranged in the ozone generator; 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 cathode water inlet pipe and the cathode gas-water communicating pipe are communicated with the cathode electrolytic tank, the anode water inlet pipe and the anode gas-water communicating pipe are communicated with the anode electrolytic tank, the cathode water inlet pipe is used for conveying water into the cathode electrolytic tank, 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 tank, 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 tank through the cathode water inlet pipe, the water in the anode water tank chamber flows into the anode electrolytic tank 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 generated in the cathode electrolytic tank is discharged into the cathode water tank chamber through the cathode gas-water communicating pipe for collection, the ozone generated in the anode electrolytic tank 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 air outlet hoses, hoses connected between all parts can be omitted, the space occupied by arrangement pipelines is reduced, the equipment structure is more compact, and therefore the equipment can be miniaturized.

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 water inlet pipe is communicated with the cathode transverse communicating pipe, the anode water inlet pipe is communicated with the anode transverse communicating pipe, and the cathode transverse communicating pipe and the anode transverse communicating pipe are connected with an external water source.

Through adopting above-mentioned technical scheme, to the horizontal communicating pipe water delivery of negative pole, water is filling up the cathode electrolysis trough earlier, and then continue to pour into water to the cathode tank room, when water overflowed the overflow aperture, water flowed into the positive pole tank room through the overflow aperture, and the indoor water of positive pole tank pours into the anode electrolysis trough through the positive pole inlet tube into, through the design of overflow aperture, only need to carry out water flow delivery to the horizontal communicating pipe of negative pole, need not to carry out rivers through the pipeline that adds, thereby can reduce the space that the pipeline occupies, and then can further accomplish miniaturization with equipment.

Optionally, the top end of the cathode gas-water communicating tube extends out of the top surface of the lower end cover, and the top end of the anode gas-water communicating tube extends out of the top surface of the lower end cover.

By adopting the technical scheme, the hydrogen generated in the cathode electrolytic tank 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 roll drives the ozone generating and conveying device to vibrate, abnormal sound is generated, the ozone generating and conveying device is easy to fall off due to long-time vibration, and the top end of the cathode gas-water communicating pipe extends out of the top surface of the lower end cover, so that the top end of the cathode gas-water communicating pipe is positioned at a higher position, and the influence of the discharged hydrogen on water stirring is smaller; ozone generated in the anode electrolytic tank is discharged into the anode water tank chamber through the anode gas-water communicating pipe, the ozone drives water in the anode water tank chamber to roll, the water rolls to drive the ozone generation conveying device to vibrate, abnormal sound is generated, the ozone generation conveying device is easy to fall off due to long-time vibration, the top end of the anode gas-water communicating pipe extends out of the top surface of the lower end cover, the top end of the anode gas-water communicating pipe is positioned at a higher position, the influence of discharged ozone on water stirring is small, and therefore the generation of abnormal sound and the occurrence of the situation that the ozone generation conveying device falls off can be reduced.

Optionally, upper portion box body top surface sealing connection has the upper end cover, upper end cover top surface fixedly connected with connecting seat, the top of connecting seat in positive pole water tank room, be provided with the air current groove in the connecting seat, the air current groove with positive pole water tank room intercommunication, upper end cover top surface fixedly connected with gas tube, the gas tube wears to locate in the connecting seat, and with the air current groove intercommunication.

Through adopting above-mentioned technical scheme, the indoor hydrogen of cathode water tank enters into the positive pole water tank indoor through the overflow aperture, and hydrogen mixes with the indoor ozone of positive pole water tank, and the mixed gas rises to collect in the air current inslot, outside the ozone is taken place to transfer through the gas tube export again, need not to export the gas in cathode water tank and the positive pole water tank through the hose respectively to can further save the use of hose, be favorable to further accomplishing the miniaturization with equipment.

Optionally, the indoor vertical cue that is provided with of cathode water tank, the top of cue passes the top surface of connecting seat, and fixed connection in on the connecting seat, the cue is located the air current inslot, the cover is equipped with the float switch on the cue, the float switch is in slide on the cue, the float switch receives the buoyancy of water to rise and can control to get into the shutoff of the rivers of the horizontal communicating pipe of cathode, the float switch resumes to the home position and can control to get into the opening of the rivers of the horizontal communicating pipe of cathode.

By adopting the technical scheme, in the process of preparing ozone, the liquid level in the anode water tank chamber can be gradually reduced, and the liquid level in the cathode water tank chamber can be gradually increased; when the liquid level of the cathode water tank chamber overflows through the overflow hole, water flows to the anode water tank chamber, so that the liquid level in the anode water tank chamber is gradually increased; when the float switch is upwards lifted by buoyancy, the float switch is lifted, the water flow of the cathode transverse communicating pipe is closed, and the water supply to the cathode water tank chamber is stopped; in the continuous electrolysis process, the liquid level in the anode water tank chamber gradually decreases, the float switch falls to the original position, the cathode transverse communicating pipe is opened to supply water to the cathode water tank chamber continuously, the liquid level in the cathode water tank chamber gradually increases, and the reciprocating circulation is carried out, so that the water source in the anode water tank chamber is sufficient, and the continuous operation of the electrolysis reaction is facilitated.

Optionally, a center frame is sleeved at the bottom end of the ball rod, the center frame is fixedly connected to the ball rod, and the ball float switch is positioned in the center frame; the inner peripheral surface of the center frame is fixedly connected with a bottom plate, and the bottom plate is arranged at the bottom end of the floating club; the center frame peripheral face is provided with first breach, first breach with the inside intercommunication of center frame, first breach is located the bottom plate top, center frame peripheral face is provided with the second breach, the second breach with the inside intercommunication of center frame, the second breach with center frame bottom surface intercommunication, the second breach is located the below of bottom plate.

By adopting the technical scheme, when the ozone in the anode water tank chamber ascends upwards from the anode gas-water communicating pipe, the ozone easily drives the floating ball switch to ascend, and when the liquid level in the anode water tank chamber does not reach the set height, the ozone drives the floating ball switch to ascend, so that the cathode water flow pipe is easily closed, the water supply in the cathode water tank chamber is stopped, the liquid level in the anode water tank chamber is gradually reduced until the water source is consumed, the electrolytic reaction is stopped, the ozone generation is stopped, and the use of a customer is influenced; through add the center frame outside the float switch, ozone gas directly strikes the center frame, and ozone gas flows from the second breach department of center frame for ozone gas is very little to the effort of float switch, thereby can reduce the condition emergence that ozone drove the float switch and rise, and then can guarantee ozone and take place conveyer's normal use.

Optionally, the central frame global integrated into one piece has a plurality of spacing, and a plurality of spacing is around central frame a week evenly distributed, and a plurality of spacing butt are in the inner wall of positive pole water tank room.

Through adopting above-mentioned technical scheme, center rest global integrated into one piece has a plurality of spacing, and spacing restriction center rest takes place the skew, makes the center rest keep vertical state, can reduce the frictional force between float switch and the cue on the one hand, on the other hand can reduce the influence of ozone to the float switch.

Optionally, the height of the overflow hole (13) is higher than the water level controlled by the float switch (68).

By adopting the technical scheme, the water flow in the anode water tank chamber can be blocked from flowing into the cathode water tank chamber because the height of the overflow hole is higher than the water level controlled by the float switch (68), and the water in the anode cavity can become saturated ozone water in the electrolysis process, so that the ozone content is high, and the service life of the cathode electrode is reduced because the water containing ozone flows into the cathode electrolytic tank.

In summary, the present application includes at least one of the following beneficial technical effects:

in the process of preparing ozone by electrolyzing water, the liquid level of water in the cathode water tank chamber gradually rises, when the liquid level of water exceeds the overflow hole, the water in the cathode water tank chamber flows into the anode water tank chamber, water is supplemented into the anode water tank chamber, the public water tank can be replaced by the design of the overflow hole, the space occupied by the public water tank can be saved, a hose connected with the public water tank can be omitted, the space occupied by an arrangement pipeline is reduced, the equipment structure is more compact, and the equipment can be miniaturized;

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 tank through the cathode water inlet pipe, the water in the anode water tank chamber flows into the anode electrolytic tank 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 generated in the cathode electrolytic tank is discharged into the cathode water tank chamber through the cathode gas-water communicating pipe for collection, the ozone generated in the anode electrolytic tank 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 air outlet hoses, hoses connected among all parts can be omitted, the space occupied by arrangement pipelines is reduced, the equipment structure is more compact, and therefore the equipment can be miniaturized;

the cathode water tank is filled with water firstly, then the cathode water tank is filled with water continuously, when water flows into the anode water tank through the overflow hole, the water in the anode water tank is filled into the anode water tank through the anode water inlet pipe, and the water is only required to be conveyed to the cathode water tank through the design of the overflow hole, so that water flow conveying is not required to be carried out through an external pipeline, the occupied space of the pipeline can be reduced, and the equipment can be miniaturized further.

Drawings

Fig. 1 is a schematic structural view of an ozone generating and transporting device according to an embodiment of the present application.

Fig. 2 is a schematic cross-sectional view of the upper case of the ozone generating and transporting device.

Fig. 3 is a schematic view of the structure of the upper end cap in the ozone generating and transporting device.

Fig. 4 is a schematic cross-sectional view of the upper end cap and the cue stick in the ozone generating and delivering device.

Fig. 5 is an enlarged schematic view of the portion a in fig. 1.

Fig. 6 is a schematic view of the structure of the upper end cap and the cue stick in the ozone generating and delivering device.

Fig. 7 is a schematic view showing a cross-sectional structure of an upper case of the ozone generating and transporting device.

Fig. 8 is a schematic cross-sectional view of the lower end cap and the adapter rack in the ozone generating and transporting device.

Fig. 9 is a schematic view of the structure of the lower end cap in the ozone generating and transporting device.

Fig. 10 is an enlarged schematic view of a portion B in fig. 1.

Fig. 11 is a schematic sectional view of the transfer frame in the ozone generating and transporting device.

Fig. 12 is a schematic view of the structure of the transfer frame in the ozone generating and transporting device.

Fig. 13 is a schematic view of the structure of the transfer frame in the ozone generating and transporting device.

Fig. 14 is a schematic view of an explosion structure of an ozone generator in the ozone generating and transporting device.

Fig. 15 is a schematic view of another perspective exploded view of an ozone generator in an ozone generating and delivering device.

Reference numerals illustrate:

1. an upper case; 11. a cathode water tank chamber; 12. an anode water tank chamber; 13. an overflow aperture; 14. a heat radiation fin; 15. a placement groove; 16. a fan; 17. a baffle; 18. a power supply cover; 2. an upper end cap; 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. a gas 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 clamping block; 283. pressing the plate; 29. a first elastic plate; 291. a first clamping block; 3. a lower end cap; 301. a fourth elastic plate; 3011. a third clamping 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 inlet pipe; 36. an anode water inlet pipe; 37. a cathode gas-water communicating tube; 38. an anode gas-water communicating pipe; 39. a third elastic plate; 391. a limiting block; 4. an ozone generator; 401. a cathode prefabricated film; 402. a cathode collector plate; 403. an anode prefabricated film; 404. an anode collector plate; 405. a cathode gasket; 406. a cathode side plate; 407. an anode gasket; 408. an anode side plate; 41. a positioning plate; 411. a stop block; 412. a conductive interface; 42. a cathode electrode plate; 43. a cathode plate; 431. a cathode electrolytic 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 seal groove; 453. a cathode sealing cushion block; 4531. a cathode water flow hole; 4532. a cathode airflow hole; 454. a cathode water flow tube; 455. a cathode gas flow tube; 46. an anode electrode plate; 47. an anode plate; 471. an anode electrolytic cell; 472. an anode seal groove; 48. a second slide plate; 481. a second roller; 482. an anode water flow seal 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; 61. a nut; 62. a support plate; 63. a gas seal ring; 64. a deformation groove; 66. a center frame; 661. a bottom plate; 662. a first notch; 663. a second notch; 664. a limit bar; 67. a top plate; 68. a float switch; 7. a transfer frame; 71. a chute; 72. a sliding table; 721. a boss; 73. a third notch; 74. a support plate; 741. a partition plate; 742. a conductive copper reed; 75. a fixing plate; 751. a slot.

Detailed Description

The present application is described in further detail below in conjunction with figures 1-15.

The embodiment of the application discloses an ozone generation and transmission device with a splicing structure. Referring to fig. 1, the ozone generating and transmitting device comprises an upper box body 1, an upper end cover 2, a lower end cover 3, a switching frame 7 and an ozone generator 4, wherein the upper box body 1 is vertically arranged, the upper end cover 2 is connected with the top end of the upper box body 1 in a sealing way, the lower end cover 3 is connected with the bottom end of the upper box body 1 in a sealing way, the switching frame 7 is arranged on the bottom surface of the lower end cover 3, and the ozone generator 4 is arranged on the bottom surface of the switching frame 7; the adapter frame 7 is used for detachably connecting the ozone generator 4, the lower end cover 3 is used for enabling 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 case 1 is in a rectangular parallelepiped shape, a cathode water tank chamber 11 and an anode water tank chamber 12 are provided in the upper case 1, the cathode water tank chamber 11 is used for storing purified water and transferring hydrogen, the anode water tank chamber 12 is used for storing purified water and transferring ozone, the cathode water tank chamber 11 and the anode water tank chamber 12 are vertically arranged and are communicated with the bottom end face of the upper case 1 and the top end face of the upper case 1, the cathode water tank chamber 11 and the anode water tank chamber 12 are rectangular parallelepiped chambers, and the cathode water tank chamber 11 and the anode water tank chamber 12 are symmetrically arranged with respect to the upper case 1; the overflow holes 13 are arranged on the partition plate between the cathode water tank chamber 11 and the anode water tank chamber 12, the overflow holes 13 are communicated with the cathode water tank chamber 11 and the anode water tank chamber 12, purified water in the cathode water tank chamber 11 can flow into the anode water tank chamber 12 through the overflow holes 13, the design of the overflow holes 13 can replace a public water tank, and the space occupied by the public water tank and a pipeline connected with the public water tank is reduced.

Referring to fig. 1, a plurality of heat dissipation fins 14 are uniformly formed on the peripheral surface of the upper case 1, the heat dissipation fins 14 are vertically arranged and uniformly distributed along the peripheral surface of the upper case 1, and heat dissipation in the upper case 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 heat dissipation of the upper box body 1 is further accelerated by the fan 16; the side of the upper box body 1 far away from one side of the fan 16 is integrally formed with two baffles 17, the two baffles 17 are vertical and are respectively positioned at the side edges of the two sides of the side of the upper box body 1, a power cover 18 is arranged between the two baffles 17, and a power supply and a control driving circuit for controlling the running of the ozone generating and conveying device are arranged between the power cover 18 and the baffles 17.

Referring to fig. 2 and 3, the upper end cover 2 is a cuboid 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 positioned on the bottom face of one end of the upper end cover 2, the top end of the anode water tank chamber 12 is positioned on the bottom face of the other end of the upper end cover 2, a first sealing groove 21 is arranged on the bottom face of the upper end cover 2, 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 positioned 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; the bottom of the first sealing groove 21 is integrally formed with a cathode limiting plate 23 which is arranged around the port of the cathode water tank chamber 11, 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 surfaces of the anode limiting plate 22 and the cathode limiting plate 23 are respectively sleeved with a first sealing ring 24, one side, adjacent to the two first sealing rings 24, of each first sealing ring is integrally formed, the first sealing rings 24 are located in the first sealing grooves 21, the first sealing rings 24 are abutted to the top end surfaces of the upper box body 1, the top ends of the upper end cover 2 and the upper box body 1 are sealed through the first sealing rings 24, and gas escape is effectively prevented.

Referring to fig. 2 and 4, a connection seat 25 is integrally formed on the top surface of the upper end cover 2, the connection seat 25 is positioned right above the anode water tank chamber 12, a gas flow groove 251 is arranged in the connection seat 25, and the gas flow groove 251 is communicated with the bottom surface of the upper end cover 2; the top surface of the upper end cover 2 is integrally formed with a gas pipe 26, the gas pipe 26 is arranged along the length direction of the upper end cover 2, the gas pipe 26 passes through the connecting seat 25, the gas pipe 26 is communicated with an air flow 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 air flow groove 251, and then are led out of the ozone generating and conveying device through the gas pipe 26, a hose which is respectively connected with the cathode water tank chamber 11 and the anode water tank chamber 12 and is used for guiding out gas is replaced by the gas pipe 26, and the gas pipe 26 has the characteristics of small volume and compact connection with the upper end cover 2, so that the occupied space of the hose can be reduced, and the equipment is beneficial to being miniaturized; the outer peripheral surface of the air outlet end of the air pipe 26 is integrally formed with a male connector 261, the air inlet end of the air pipe 26 is sleeved with a female connector 262, and the female connector 262 is integrally formed at the end part of the air inlet end of the air pipe 26; the male interface 261 is connected with an L-shaped quick female connector 27 in a sealing way, and the inner wall of the female interface 262 is connected with an L-shaped quick male connector 28 in a sealing way; when a plurality of ozone generating and conveying devices are spliced, the male connector 261 is spliced in the female connector 262 of the adjacent gas pipe 26 and is in sealing connection, 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 pipe 26 replaces a cathode public gas pipe and an anode public gas pipe, so that the space occupied by the cathode public gas pipe and the anode public gas pipe can be reduced.

Referring to fig. 1 and 3, the top surface of the upper end cover 2 is integrally formed with a first elastic plate 29, 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 at one side of the gas pipe 26 far away from the power cover 18, one side surface of the first elastic plate 29 close to the first connector is integrally formed with a first clamping block 291, the outer circumferential surface of the l-shaped quick female connector 27 is integrally formed with a limiting ring 5, the axis of the limiting ring 5 is collinear with the axis of the gas pipe 26, and the first clamping block 291 is clamped on the limiting ring 5; the side of the limit ring 5 near the air pipe 26 is provided with a first guiding inclined plane, and the side of the first clamping block 291 far away from the first elastic plate 29 is provided with a second guiding inclined plane matched with the first guiding inclined plane.

Referring to fig. 1 and 5,L, the outer peripheral surface of the quick male connector 28 is integrally formed with a second elastic plate 281, the second elastic plate 281 is parallel to the female connector 262, a second clamping block 282 is integrally formed on a side surface of the second elastic plate 281, which is close to the female connector 262, a pressing plate 283 is integrally formed on a side surface of the second elastic plate 281, which is far away from the female connector 262, the pressing plate 283 is located at an end of the second elastic plate 281, a limiting ring 5 is integrally formed on the outer peripheral surface of the female connector 262, an axis of the limiting ring 5 is collinear with an axis of the gas pipe 26, the second clamping block 282 is clamped on the limiting ring 5, and a third guiding inclined surface matched with the first guiding inclined surface is arranged on a side of the second clamping block 282, which is close to the gas pipe 26.

Referring to fig. 1, when a plurality of gas pipes 26 are spliced, the male connectors 261 on the gas pipes 26 are inserted into the female connectors 262 on the adjacent gas pipes 26, the first clamping blocks 291 on the first elastic plates 29 are clamped on the limiting rings 5 on the adjacent female connectors 262, and in the process of splicing the gas pipes 26, the first elastic plates 29 are elastically bent in the sliding process of the first guiding inclined surfaces and the second guiding inclined surfaces, and the gas pipes 26 are continuously inserted, so that the first clamping blocks 291 are clamped on the limiting rings 5, thereby realizing the splicing between the adjacent upper end covers 2.

Referring to fig. 2 and 4, a ball rod 6 is vertically disposed in the anode water tank chamber 12, the top end of the ball rod 6 passes through the top surface of the connecting seat 25, a nut 61 is connected with the end portion in a threaded manner, the nut 61 is abutted to the top surface of the connecting seat 25, the ball rod 6 is located in the air flow groove 251, a supporting plate 62 is integrally formed on the peripheral surface of the top end of the ball rod 6, the supporting plate 62 is located in the air flow groove 251, an air sealing ring 63 is sleeved on the top end of the ball rod 6, the air sealing ring 63 is located on the top surface of the supporting plate 62, and the air sealing ring 63 is abutted to the bottom of the air flow groove 251.

Referring to fig. 4, a deformation groove 64 is formed in the end surface of the bottom end of the cue 6, two ends of the deformation groove 64 are communicated with the peripheral surface of the cue 6, an annular clamping groove is formed in the peripheral surface of the bottom end of the cue 6, a center frame 66 is arranged at the bottom end of the cue 6, the center frame 66 is cylindrical, a bottom plate 661 is integrally formed in the inner peripheral surface of the center frame 66, the cue 6 passes through the middle position of the bottom plate 661, and the bottom plate 661 is clamped in the annular clamping groove.

Referring to fig. 2 and 6, the central frame 66 is provided with two symmetrically arranged first notches 662 on the peripheral surface, 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 symmetrically arranged second notches 663 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 and the second notches 663 are staggered; the central frame 66 global integrated into one piece has four spacing bars 664, and four spacing bars 664 are vertical to be set up, and four spacing bars 664 evenly distributed around central frame 66 a week, and four spacing bars 664 butt in the inner wall of positive pole water tank chamber 12 utilize spacing bars 664 butt positive pole water tank chamber 12 inner wall, can keep the cue 6 in vertical state, and central frame 66 just is in vertical state.

Referring to fig. 2 and 4, a top plate 67 is sleeved on the cue stick 6 and integrally formed, the top plate 67 is positioned in the center frame 66 and at the top end of the center frame 66, and two symmetrically arranged through holes are formed in the top surface of the top plate 67; the ball rod 6 is sleeved with a ball float switch 68, the ball float switch 68 can slide on the ball rod 6, the ball float switch 68 is located in the center frame 66 and between the top plate 67 and the bottom plate 661, the ball float switch 68 can control the closing of the water flow entering the upper box body 1 due to the rising of the buoyancy of water, the ball float switch 68 can control the opening of the water flow entering the upper box body 1 due to the restoration to the original position, and the top plate 67 is located below the overflow hole 13.

In the process of preparing ozone by electrolyzing water, the liquid level of water in the cathode water tank chamber 11 can be gradually increased, when the liquid level of water exceeds the overflow hole 13, the water in the cathode water tank chamber 11 can flow into the anode water tank chamber 12 to supplement water into the anode water tank chamber 12, the public water tank can be replaced by the design of the overflow hole 13, the space occupied by the public water tank can be saved, a hose connected with the public water tank can be omitted, the space occupied by a distribution pipeline is reduced, the equipment structure is more compact, and the equipment can be miniaturized.

When the liquid level in the anode water tank 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 tank chamber 12 gradually drops, the float switch 68 is restored to the original position, and the float switch 68 can control the water flow entering the upper box body 1 to be opened.

The center frame 66 is sleeved outside the float switch 68, and ascending ozone gas in the anode water tank chamber 12 acts on the center frame 66, so that the ascending ozone gas is reduced to drive the float switch 68 to ascend, and the float switch 68 can more accurately control 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 bottom end of the cathode water tank chamber 11 is located on the top face of one end of the lower end cover 3, the bottom end of the anode water tank chamber 12 is located on the top face of the other end of the lower end cover 3, the top face of the lower end cover 3 is provided with a second sealing groove 31, the bottom of the second sealing groove 31 is also integrally formed with an anode limiting plate 22 arranged around the periphery of the port of the anode water tank chamber 12 and a cathode limiting plate 23 arranged around the periphery of the port of the cathode water tank chamber 11, the outer peripheral faces of the anode limiting plate 22 and the cathode limiting plate 23 are respectively sleeved with a second sealing ring 32, one side, adjacent to the two second sealing rings 32, of the second sealing rings 32 are integrally formed in the second sealing groove 31, and the second sealing rings 32 are abutted to the bottom end face of the upper box body 1.

Referring to fig. 1, 9 and 10, the bottom surface of the lower end cap 3 is integrally formed with a cathode lateral communication tube 33 and an anode lateral communication tube 34, the cathode lateral communication tube 33 and the anode lateral communication tube 34 being parallel to each other and disposed along the length direction of the lower end cap 3, both ends of the cathode lateral communication tube 33 and the anode lateral communication tube 34 extending out of the upper end cap 2; female interfaces 262 are respectively sleeved on the outer peripheral surface of the water inlet end of the cathode transverse communicating pipe 33 and the outer peripheral surface of the water inlet end of the anode transverse communicating pipe 34, the two female interfaces 262 are respectively integrally formed on the cathode transverse communicating pipe 33 and the anode transverse communicating pipe 34, limiting rings 5 are respectively sleeved on the outer peripheral surfaces of the two female interfaces 262 and are integrally formed, L-shaped quick male connectors 28 are respectively and hermetically connected to the two female interfaces 262, second elastic plates 281 are integrally formed on the peripheral surfaces of the L-shaped quick male connectors 28, the second elastic plates 281 are parallel to the female interfaces 262, second clamping blocks 282 are clamped on the limiting rings 5, the floating ball switch 68 can control the closing of water flow entering the cathode transverse communicating pipe 33 due to the rising of the buoyancy of water, and the floating ball switch 68 can control the opening of water flow entering the cathode transverse communicating pipe 33 due to the restoration to the original position.

Referring to fig. 2 and 9, the outer circumferential surface of the water outlet end of the cathode transverse communication tube 33 and the outer circumferential surface of the water outlet end of the anode transverse communication tube 34 are integrally formed with male connectors 261, one side surface of the lower end cover 3, which is close to the male connectors 261, is integrally formed with two fourth elastic plates 301, the end parts of the fourth elastic plates 301 are integrally formed with third clamping blocks 3011, the two male connectors 261 are positioned 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 circumferential surface of the L-shaped quick female connector 27 is sleeved with a limiting ring 5 and integrally formed, the third clamping blocks 3011 are clamped on the limiting ring 5, and the third clamping blocks 3011 are provided with sixth guiding inclined surfaces which are mutually matched with the first guiding inclined surfaces on the limiting ring 5.

Referring to fig. 2, when the plurality of ozone generating and transmitting devices are spliced, the male connector 261 on the cathode transverse communicating tube 33 is inserted into the female connector 262 on the adjacent cathode transverse communicating tube 33, and is in sealing connection, the male connector 261 on the anode transverse communicating tube 34 is inserted into the female connector 262 on the adjacent anode transverse communicating tube 34, and is in sealing connection, the third clamping block 3011 is clamped on the limiting ring 5, and in the process of inserting the male connector 261, the sixth guiding inclined surface slides on the first guiding inclined surface, the fourth elastic plate 301 is elastically bent, and the cathode transverse communicating tube 33 and the anode transverse communicating tube 34 are continuously pushed, so that the third clamping block 3011 is clamped on the limiting ring 5, and thus the lower end cover 3 can be spliced.

Referring to fig. 2 and 9, the bottom surface of the lower end cap 3 is integrally formed with a cathode inlet pipe 35 and an anode inlet pipe 36, the cathode inlet pipe 35 and the anode inlet pipe 36 are vertically disposed, the cathode inlet pipe 35 and the anode inlet pipe 36 are positioned between the cathode lateral communication pipe 33 and the anode lateral communication pipe 34, the cathode inlet pipe 35 is communicated with the cathode lateral communication pipe 33, the cathode inlet pipe 35 is communicated with the bottom surface of the second seal groove 31, and is communicated with the cathode water tank chamber 11; the anode inlet pipe 36 communicates with the anode lateral communication pipe 34, and the anode inlet pipe 36 communicates with the bottom surface of the second seal groove 31 and communicates with the anode tank chamber 12.

Referring to fig. 2 and 9, the bottom surface of the lower end cap 3 is integrally formed with a cathode gas-water communication pipe 37 and an anode gas-water communication pipe 38, the cathode gas-water communication pipe 37 and the anode gas-water communication pipe 38 are vertically disposed, the cathode gas-water communication pipe 37 and the anode gas-water communication pipe 38 are located between the cathode lateral communication pipe 33 and the anode lateral communication pipe 34, the top end of the cathode gas-water communication pipe 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 communication pipe 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 communication pipe 38 is located below the center frame 66; the intermediate position integrated into one piece that power lid 18 one side was kept away from to lower end cover 3 has third elastic plate 39, and third elastic plate 39 is located the bottom of lower end cover 3, and third elastic plate 39 bottom surface integrated into one piece has stopper 391, and stopper 391 is located the one end that third elastic plate 39 kept away from lower end cover 3, and one side that stopper 391 kept away from lower end cover 3 is provided with the fifth guide slope.

Referring to fig. 8 and 11, the adapter frame 7 is fixedly connected to the bottom surface of the lower end cover 3, the adapter frame 7 is cuboid, the bottom surface of the adapter frame 7 is provided with a chute 71, the chute 71 is cuboid, the chute 71 is communicated with one side surface of the adapter frame 7 far away from the power cover 18, sliding tables 72 are uniformly formed on two symmetrical side inner walls of the chute 71, the sliding tables 72 are located in the notches of the chute 71, bosses 721 are integrally formed on the top surfaces of the two sliding tables 72, and the bosses 721 are located at one end of the sliding tables 72 close to the power cover 18.

Referring to fig. 9 and 12, the bottom ends of the cathode water inlet pipe 35 and the anode water inlet pipe 36 pass through the bottom of the chute 71, and the bottom ends of the cathode gas-water communicating pipe 37 and the anode gas-water communicating pipe 38 pass through the bottom of the chute 71; the intermediate position of the side surface of the transfer frame 7 far away from the power cover 18 is provided with a third notch 73, the bottom surface of the third elastic plate 39 is abutted to the top surface of the transfer frame 7, the third notch 73 is located under 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 in the middle position of the top surface of one end of the transfer frame 7 far away from the third notch 73, the top end of the support plate 74 is positioned between the baffles 17, the support plate 74 is parallel to the power cover 18, three isolation plates 741 are integrally formed on the side surface of one side of the support plate 74 close to the power 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 transfer frame 7, and the interval between the middle isolation plates 741 and the adjacent isolation plates 741 is equal; the support plate 74 is close to two conductive copper reeds 742 of side fixedly connected with of power lid 18, two conductive copper reeds 742 are located between two adjacent division boards 741 respectively, the intermediate position integrated into one piece that is close to power lid 18 side of switching frame 7 has fixed plate 75, two slots 751 with the mutual joint of two conductive copper reeds 742 bottom have been seted up to fixed plate 75 top surface, slot 751 communicates with the top surface of fixed plate 75 and the bottom surface of fixed plate 75, the elastic part bottom of two conductive copper reeds 742 extends to the bottom surface of switching frame 7, two conductive copper reeds 742 are connected with the power electricity.

Referring to fig. 1 and 14, the top end of the ozone generator 4 is mounted in the chute 71 of the adapter frame 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 in the middle of the chute 71, and the positioning plate 41 is disposed vertically and along the length direction of the third elastic plate 39.

Referring to fig. 12 and 14, a stop 411 is integrally formed on the top end surface of the positioning plate 41, the stop 411 is located in the third notch 73, one side surface of the stop 411 abuts against the side surface of the stop 391, which is 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, away from the stop 391, of the stop 411; 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 the two sides of the proton exchange membrane 44 are respectively abutted with sealing gaskets, and the two sealing gaskets are positioned at 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 on the inner side of the sealing gasket, the side surface of one side of the cathode prefabricated membrane 401, which is far away from the proton exchange membrane 44, is abutted with a cathode collector plate 402, and the cathode collector plate 402 is positioned on the inner side of the sealing gasket; the side surface of the proton exchange membrane 44, which is far away from the cathode prefabricated membrane 401, is abutted with an anode prefabricated membrane 403, the anode prefabricated membrane 403 is positioned at the inner side of the sealing gasket, the side surface of the anode prefabricated membrane 403, which is far away from the proton exchange membrane 44, is abutted with an anode collector plate 404, and the anode collector plate 404 is positioned at the inner side of the sealing gasket.

Referring to fig. 14 and 15, the cathode electrode plate 42 is fixedly connected to a side surface of the positioning plate 41, the side surface of the cathode electrode plate 42 is abutted against a side surface of the cathode collector plate 402, the cathode plate 43 is fixedly connected to a side surface of the cathode electrode plate 42, which is far away from the positioning plate 41, a cathode electrolytic bath 431 is provided on a side surface of the cathode plate 43, which is close to the cathode electrode plate 42, a cathode seal groove 432 is provided around the cathode electrolytic bath 431, a seal gasket is provided in the cathode seal groove 432, and the seal gasket is abutted against the cathode electrode plate 42.

Referring to fig. 14, a first sliding plate 45 is integrally formed on a side surface of the cathode plate 43, which is far away from the positioning plate 41, the first sliding plate 45 is in a cuboid shape, the first sliding plate 45 is positioned at the top end of the cathode plate 43, the first sliding plate 45 is positioned in the sliding groove 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, which is far away from the positioning plate 41, is rotationally connected with a first roller 451, the first roller 451 is abutted against the top surface of the sliding table 72, the first roller 451 is positioned at one end of the first sliding plate 45, which is far away from the boss 721, the length of the boss 721 is larger than the diameter of the first roller 451, and the top surface of the first sliding plate 45 is abutted against the bottom surface of the sliding groove 71; the top surface of the cathode plate 43 is provided with a cathode water flow seal groove 452, a cathode seal cushion block 453 is arranged in the cathode water flow seal groove 452, and the cathode seal cushion block 453 is abutted to the bottom end of the cathode water inlet pipe 35 and the bottom end of the cathode gas-water communicating pipe 37.

Referring to fig. 12 and 14, a cathode water flow pipe 454 and a cathode gas flow pipe 455 are integrally formed on a side surface of the cathode plate 43 far from the cathode electrolytic tank 431, the cathode water flow pipe 454 and the cathode gas flow pipe 455 are vertically arranged, the bottom end of the cathode water flow pipe 454 and the bottom end of the cathode gas flow pipe 455 are both communicated with the cathode electrolytic tank 431, the top end of the cathode water flow pipe 454 and the top end of the cathode gas flow pipe 455 are both communicated with the bottom of the cathode water flow seal groove 452, and the length of the cathode water flow pipe 454 is longer than the length of the cathode gas flow pipe 455; the cathode sealing cushion 453 is provided with a cathode water flow hole 4531 and a cathode air flow hole 4532, a cathode water flow pipe 454 is communicated with the cathode water inlet pipe 35 through the cathode water flow hole 4531, and the cathode air flow pipe 455 is communicated with the cathode air water communicating pipe 37 through the cathode air flow hole 4532; the side surface of the cathode plate 43 far away from the electrolytic tank is fixedly connected with a cathode gasket 405, the side surface 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 is abutted to a side surface of the anode 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 arranged on a side surface of the anode plate 47 close to the anode electrode plate 46, an anode sealing groove 472 is arranged around the anode electrolytic tank 471, and a sealing gasket is arranged in the anode sealing groove 472 and abutted to the anode electrode plate 46.

Referring to fig. 15, a second sliding plate 48 is integrally formed on a side surface of the anode plate 47 away from the positioning plate 41, the second sliding plate 48 is in a cuboid shape, the second sliding plate 48 is positioned at the top end of the anode plate 47, the second sliding plate 48 is positioned in the sliding groove 71, the bottom surface of the second sliding plate 48 is in sliding fit with the top surface of the boss 721, a second rolling shaft 481 is rotatably connected to the side surface of the second sliding plate 48 away from the positioning plate 41, the second rolling shaft 481 is abutted against the top surface of the sliding groove 72, the second rolling shaft 481 is positioned at one end of the second sliding plate 48 away from the boss 721, the second rolling shaft 481 has the same structure as the first rolling shaft 451, the length of the boss 721 is larger than the diameter of the second rolling shaft 481, and the top surface of the second sliding plate 48 is abutted against the bottom surface of the sliding groove 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 is abutted to 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 tube 484 and an anode gas flow tube 485 are integrally formed on the side surface of the anode plate 47 far from the anode electrolytic bath 471, the anode water flow tube 484 and the anode gas flow tube 485 are vertically arranged, the bottom end of the anode water flow tube 484 and the bottom end of the anode gas flow tube 485 are both communicated with the anode electrolytic bath 471, the top end of the anode water flow tube 484 and the top end of the anode gas flow tube 485 are both communicated with the bottom of the anode water flow seal groove 482, and the length of the anode water flow tube 484 is longer than that of the anode gas flow tube 485; the anode sealing cushion block 483 is provided with an anode water flow hole 4831 and an anode air 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 air flow pipe 485 is communicated with the anode gas water communicating pipe 38 through the anode air flow hole 4832; the side surface of the anode plate 47 far away from one side of the electrolytic tank is fixedly connected with an anode gasket 407, the side surface of the anode gasket 407 far 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, the side surface of the positioning plate 41 far from the side of the stop 411 is inserted with two conductive interfaces 412, the two conductive interfaces 412 are respectively and electrically connected to two conductive copper spring plates, and the two conductive interfaces 412 are respectively and electrically connected to the cathode electrode plate 42 and the anode electrode plate 46.

When the ozone generator 4 is installed, the first sliding plate 45 and the second sliding plate 48 are disassembled 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 plane of the stop block 411 is abutted against the fifth guide inclined plane of the limiting block 391, the third elastic plate 39 is elastically bent, the fourth guide inclined plane passes over the fifth guide inclined plane, so that one side surface of the stop block 411 is abutted against the side surface of the limiting block 391, which is 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 released, and the ozone generator 4 can be pulled out from the chute 71, so that the convenience of the operator for disassembling the ozone generator 4 can be improved, and the problem that the disassembly and the assembly of the ozone generator 4 are not convenient enough can be solved.

Because the water inlet pipe and the air-water communicating pipe extend out of the bottom of the chute 71, when the ozone generator 4 is inserted into the chute 71, the end parts of the water inlet pipe and the air-water communicating pipe both squeeze the sealing cushion block, 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 on the sealing cushion block 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 slide on the sliding table 72, the water inlet pipe and the air-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 rolling shaft 451 and the second rolling shaft 481 slide on the sliding table 72, so that the top surface of the ozone generator 4 is abutted to the bottom of the sliding groove 71, the blocking effect of the ozone generator 4 during disassembly and assembly can be reduced, and the convenience of the ozone generator 4 during disassembly and assembly is further improved; 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 cathode water inlet pipe 35 is filled with the cathode electrolytic tank 431, then the water flow 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 is gradually raised, the water in the anode water tank chamber 12 rises with the water supply floating ball switch 68, the water flow entering the cathode transverse communicating pipe 33 stops, and when the floating ball switch 68 descends to the original position, the water flow entering the cathode transverse communicating pipe 33 is opened.

When the plurality of ozone generating and transmitting devices are spliced, the plurality of cathode transverse communicating pipes 33 are spliced with each other, the plurality of anode transverse communicating pipes 34 are spliced, and water in the cathode transverse communicating pipes 33 flows into each spliced cathode water tank chamber 11 through the cathode water inlet pipe 35 respectively; the spliced anode water tank chamber 12 forms a communicating vessel through the spliced anode transverse communicating pipe 34, and can mutually supplement water sources.

The hydrogen generated in the ozone generator 4 flows into the cathode water tank chamber 11 through the cathode gas communicating pipe, the generated ozone flows into the anode water tank chamber 12 through the anode gas 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 is collected in the airflow groove 251, and the mixed gas is led out through the gas pipe 26 to be transmitted, so that the gas in the cathode water tank and the gas in the anode water tank are not required to be led out through hoses respectively, the use of the hoses can be further saved, and the miniaturization of 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 circuit, and no excessive pipelines are needed for connection.

The plurality of 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 sealing 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 sealing 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 in sealing connection, 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 cover 2 can be spliced, the pipeline is exposed when the ozone generator 4 is spliced, the space occupied by the pipeline can be reduced, and the equipment can be miniaturized.

The implementation principle of the ozone generation and transmission device with the mesopore flow-through design in the embodiment of the application is as follows: in the process of preparing ozone by electrolyzing water, the liquid level of water in the cathode water tank chamber 11 can be gradually increased, when the liquid level of water exceeds the overflow hole 13, the water in the cathode water tank chamber 11 can flow into the anode water tank chamber 12 to supplement water into the anode water tank chamber 12, the public water tank can be replaced by the design of the overflow hole 13, the space occupied by the public water tank can be saved, a hose connected with the public water tank can be omitted, the space occupied by a distribution pipeline is reduced, the equipment structure is more compact, and the equipment can be miniaturized.

The foregoing are all preferred embodiments of the present application, and are not intended to limit the scope of the present application in any way, therefore: all equivalent changes in structure, shape and principle of this application should be covered in the protection scope of this application.

Claims (5)

1. An ozone generation and transmission device with a mesoporous flow-through design is characterized in that: the ozone generator comprises an upper box body (1), an ozone generator (4) and a lower end cover (3), wherein the upper box body (1) is vertically arranged, a cathode water tank chamber (11) and an anode water tank chamber (12) penetrating through the top end and the bottom end are arranged in the upper box body (1), overflow holes (13) are formed in a partition plate between the cathode water tank chamber (11) and the anode water tank chamber (12), the lower end cover (3) is connected to the bottom surface of the upper box body (1) in a sealing mode, the ozone generator (4) is installed on the bottom surface of the lower end cover (3), a cathode water inlet pipe (35) and an anode water inlet pipe (36) are arranged on the bottom surface of the lower end cover (3), the top end of the cathode water inlet pipe (35) is communicated with the cathode of the cathode water tank chamber (11), the top end of the cathode water inlet pipe (35) is communicated with the anode water tank chamber (12), and the bottom end of the anode water inlet pipe (36) is communicated with the anode of the ozone generator (4); a cathode electrolytic tank (431) and an anode electrolytic tank (471) are arranged in the ozone generator (4); the bottom surface of the lower end cover (3) is also provided with a cathode gas-water communicating pipe (37) and an anode gas-water communicating pipe (38), the cathode gas-water communicating pipe (37) is communicated with the cathode water tank chamber (11), and the anode gas-water communicating pipe (38) is communicated with the anode water tank chamber (12); the cathode water inlet pipe (35) and the cathode gas-water communicating pipe (37) are communicated with the cathode electrolytic tank (431), the anode water inlet pipe (36) and the anode gas-water communicating pipe (38) are communicated with the anode electrolytic tank (471), the cathode water inlet pipe (35) is used for conveying water into the cathode electrolytic tank (431), the cathode gas-water communicating pipe (37) is used for discharging hydrogen into the cathode water tank chamber (11), the anode water inlet pipe (36) is used for conveying water into the anode electrolytic tank (471), and the anode gas-water communicating pipe (38) is used for discharging ozone into the anode water tank chamber (12); the bottom surface of the lower end cover (3) is provided with a cathode transverse communicating pipe (33) and an anode transverse communicating pipe (34), the outer wall of the cathode transverse communicating pipe (33) and the outer wall of the anode transverse communicating pipe (34) are fixedly connected to the bottom surface of the lower end cover (3), a cathode water inlet pipe (35) is communicated with the cathode transverse communicating pipe (33), an anode water inlet pipe (36) is communicated with the anode transverse communicating pipe (34), and the cathode transverse communicating pipe (33) and the anode transverse communicating pipe (34) are both connected with an external water source; the upper box body (1) is characterized in that an upper end cover (2) is connected to the top surface of the upper box body (1) in a sealing manner, a connecting seat (25) is fixedly connected to the top surface of the upper end cover (2), the connecting seat (25) is positioned at the top of the anode water tank chamber (12), an air flow groove (251) is formed in the connecting seat (25), the air flow groove (251) is communicated with the anode water tank chamber (12), an air pipe (26) is fixedly connected to the top surface of the upper end cover (2), and the air pipe (26) penetrates through the connecting seat (25) and is communicated with the air flow groove (251); the cathode water tank chamber (11) is internally and vertically provided with a ball float (6), the top end of the ball float (6) penetrates through the top surface of the connecting seat (25) and is fixedly connected to the connecting seat (25), the ball float (6) is positioned in the air flow groove (251), the ball float (6) is sleeved with a ball float switch (68), the ball float switch (68) slides on the ball float (6), the ball float switch (68) is lifted by buoyancy of water to control the water flow entering the cathode transverse communicating pipe (33) to be closed, and the ball float switch (68) is restored to the original position to control the water flow entering the cathode transverse communicating pipe (33) to be opened.

2. An ozone generating and transporting device of a mesoporous overcurrent design as set forth in 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).

3. An ozone generating and transporting device of a mesoporous overcurrent design as set forth in claim 1, wherein: a center frame (66) is sleeved at the bottom end of the ball rod (6), the center frame (66) is fixedly connected to the ball rod (6), and the ball float switch (68) is positioned in the center frame (66); the inner peripheral surface of the center frame (66) is fixedly connected with a bottom plate (661), and the bottom plate (661) is arranged at the bottom end of the floating ball rod (6); the center frame (66) global first breach (662) is provided with, first breach (662) with inside intercommunication of center frame (66), first breach (662) are located bottom plate (661) top, center frame (66) global second breach (663) that is provided with, second breach (663) with inside intercommunication of center frame (66), second breach (663) with center frame (66) bottom surface intercommunication, second breach (663) are located the below of bottom plate (661).

4. An ozone generating and transporting device of a mesoporous overcurrent design as set forth in claim 3, wherein: the periphery of the center frame (66) is integrally formed with a plurality of limit bars (664), the limit bars (664) are uniformly distributed around the center frame (66) in a circle, and the limit bars (664) are abutted against the inner wall of the anode water tank chamber (12).

5. An ozone generating and transporting device of a mesoporous overcurrent design as set forth in claim 1, wherein: the height of the overflow hole (13) is higher than the water level controlled by the float switch (68).