Hydrogen production and dissolution device

Abstract

Disclosed in the present invention is a hydrogen production and dissolution device, comprising a housing, a vertical frame, a power supply assembly, an electrolysis assembly, a treatment assembly, a reaction assembly, and a heat dissipation assembly. The vertical frame is arranged in the housing; the housing comprises a reaction chamber and a power supply chamber, and the power supply chamber and the reaction chamber are separated by means of a partition plate; the power supply assembly is arranged in the power supply chamber; the electrolysis assembly, the treatment assembly, and the reaction assembly are arranged in the reaction chamber; the electrolysis assembly comprises a water tank and an electrolyzer; the treatment assembly comprises a gas-liquid separator; the reaction assembly comprises a pressure booster and reaction tanks, and ultrasonic generators are arranged inside the reaction tanks; and the heat dissipation assembly comprises first heat dissipation fans and second heat dissipation fans, wherein the first heat dissipation fans are arranged in the power supply chamber, and the second heat dissipation fans are arranged in the reaction chamber. The present invention can simultaneously realize hydrogen production and dissolution operations without additional storage and transportation of hydrogen, thereby reducing potential safety hazards.

Description

A hydrogen production and dissolution equipment Technical Field

[0001] The present invention relates to the technical field of hydrogen production equipment, and in particular to hydrogen production and dissolution equipment. Background Art

[0002] Amidst the global energy transition and increasing environmental protection requirements, hydrogen energy, as a clean, efficient, and renewable energy source, is gaining widespread recognition and application. Hydrogen water, formed by dissolving hydrogen in water, not only possesses unique health benefits but also demonstrates significant potential for application in areas such as water purification and wastewater treatment, making it a popular choice in the market. Traditional hydrogen production technologies primarily include water electrolysis and production from fossil fuels. In practice, these technologies typically rely on core equipment such as electrolyzers and collection tanks. The electrolyzer decomposes water into hydrogen and oxygen, while the collection tank stores the generated hydrogen. However, dissolving hydrogen in water requires transportation or delivery, followed by specialized dissolution equipment or techniques. This process not only involves multiple steps and equipment, increasing operational complexity, but also carries potential safety risks during the storage and transfer of hydrogen. Hydrogen is a highly leaky and explosive gas, and improper handling can cause serious safety incidents. Summary of the Invention

[0003] The technical problem to be solved by the present invention is to provide a hydrogen production and dissolution equipment that can simultaneously perform hydrogen production and dissolution operations, without the need for additional storage and transportation of hydrogen, thereby reducing safety hazards.

[0004] In order to solve the above technical problems, the present invention provides a hydrogen production and dissolution equipment, including a shell, a stand, a power supply component, an electrolysis component, a processing component, a reaction component and a heat dissipation component. The stand is arranged in the shell, and the shell includes a reaction chamber and a power supply chamber. The power supply chamber and the reaction chamber are separated by a partition. The power supply component is arranged in the power supply chamber, and the electrolysis component, the processing component and the reaction component are arranged in the reaction chamber.

[0005] The electrolysis component includes a water tank and an electrolyzer, the water tank is connected to the electrolyzer, the electrolyzer is electrically connected to the power supply component, the processing component includes a gas-liquid separator, the gas-liquid separator is connected to the electrolyzer, the reaction component includes a supercharger and a reaction tank, one end of the supercharger is connected to the gas-liquid separator, and the other end of the supercharger is connected to the reaction tank, the supercharger pressurizes the reaction tank, and an ultrasonic generator is provided in the reaction tank.

[0006] [Corrected 11.08.2025 according to Rule 91] The heat dissipation assembly includes a first heat dissipation fan and a second heat dissipation fan, the first heat dissipation fan is arranged in the power supply chamber, and the second heat dissipation fan is arranged in the reaction chamber and located on the side of the electrolyzer.

[0007] As an improvement to the above solution, the electrolysis assembly also includes a pump component, which is arranged below the water tank and fixed on the stand. The input end of the pump component is connected to the water tank, and the output end of the pump component is connected to an external chiller, and the external chiller is connected to the electrolyzer.

[0008] As an improvement to the above solution, the electrolyzer includes a water inlet, a hydrogen outlet, an oxygen outlet, a negative electrode connection port and a positive electrode connection port. The water inlet is connected to an external chiller, the hydrogen outlet is connected to the gas-liquid separator, the oxygen outlet is connected to the water tank, and the negative electrode connection port and the positive electrode connection port are respectively connected to the electrodes of the power supply assembly.

[0009] As an improvement of the above-mentioned scheme, the processing component also includes a purifier and a cooling tank, the gas-liquid separator includes a hydrogen outlet, the hydrogen outlet is connected to the inlet end of the purifier, and the purifier is connected to an external heat source; one end of the cooling tank is connected to the outlet end of the purifier, and the other end of the cooling tank is connected to the supercharger, and the cooling tank is connected to an external cooling device.

[0010] As an improvement of the above-mentioned scheme, the reaction tank also includes a tank body, the ultrasonic generator is arranged at the bottom of the tank body, and the top opening of the tank body is provided with a screw cover, a flange ring, a telescopic drive member and a locking rod. The edge of the screw cover is provided with a protrusion, the inner edge of the flange ring is provided with a limiting groove, and the edge of the limiting groove is provided with an installation notch. The protrusion can pass through the installation notch and be screwed into the limiting groove to form a limiting connection. The fixed end of the telescopic drive member is fixed to the outside of the flange ring, one end of the locking rod is connected to the movable end of the telescopic drive member, and the telescopic drive member can drive the other end of the locking rod to telescope in the installation notch.

[0011] As an improvement of the above-mentioned solution, the reaction assembly also includes a locking mechanism, which includes a rocker arm and a handle. Mounting blocks are provided on both sides of the edge of the flange ring. One end of the rocker arm is hinged to one of the mounting blocks, and the other end of the rocker arm is connected to the other mounting block through a pin. A pull rod is provided on the top of the rotary cover, and the pull rod protrudes from the surface of the rotary cover. There are two pull rods and they are arranged in parallel. The rocker arm can be inserted between the two pull rods, and the handle is fixed to the top of the rocker arm.

[0012] As an improvement of the above solution, the shell also includes an operating cover, which is arranged at an angle. The side wall of the tank body is provided with a mounting ring, which is fixed to the operating cover, and the rotating cover, the flange ring, the telescopic drive member and the locking mechanism are exposed on the surface of the operating cover.

[0013] As an improvement of the above-mentioned scheme, the stand includes a support plate, and there are multiple reaction tanks. The bottoms of the multiple reaction tanks are fixed on the support plate and tilted. The angle between the center line of the reaction tank and the horizontal plane is in the range of 40°-50°, and a solenoid valve is provided between the supercharger and each of the reaction tanks.

[0014] As an improvement of the above solution, the gas-liquid separator is communicated with an external cooling device, and the gas-liquid separator further includes a liquid outlet, which is communicated with the bottom of the water tank.

[0015] As an improvement of the above solution, the hydrogen production and dissolution equipment further includes a safety component, which includes a leakage sensor. The leakage sensor is arranged in the reaction chamber and located on the side of the reaction tank.

[0016] The implementation of the present invention has the following beneficial effects:

[0017] The hydrogen production and dissolution equipment of the present invention comprises a housing, a stand, a power supply assembly, an electrolysis assembly, a processing assembly, a reaction assembly, and a heat dissipation assembly, wherein the electrolysis assembly comprises a water tank and an electrolyzer, the processing assembly comprises a gas-liquid separator, and the reaction assembly comprises a supercharger and a reaction tank. Water in the water tank can enter the electrolyzer for electrolysis, and the generated hydrogen is separated into gas and liquid by the gas-liquid separator. After treatment, the hydrogen enters the reaction tank and is pressurized by the supercharger. The reaction tank is filled with pure water and is equipped with an ultrasonic generator. Under high pressure, the ultrasonic generator can promote the dissolution of hydrogen in water. This allows the simultaneous production and dissolution of hydrogen without the need for additional storage and transportation of hydrogen. Moreover, the shell includes a reaction chamber and a power chamber, and the power chamber and the reaction chamber are separated by a partition. The power supply assembly is arranged in the power chamber, and the electrolysis assembly, the processing assembly and the reaction assembly are arranged in the reaction chamber. The hydrogen production and dissolution equipment also includes a heat dissipation assembly, and the first heat dissipation fan and the second heat dissipation fan of the heat dissipation assembly are respectively arranged in the power chamber and the reaction chamber. By isolating the components used for electrolysis and hydrogen dissolution from the power supply assembly, even if hydrogen leakage occurs, hydrogen can be avoided as much as possible from contacting the components in the power supply assembly. Moreover, the first heat dissipation fan and the second heat dissipation fan can promote air circulation, and even if hydrogen leaks, it can prevent aggregation, so it is highly safe and can reduce safety hazards. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] FIG1 is a schematic structural diagram of a hydrogen production and dissolution device according to the present invention;

[0019] FIG2 is a schematic flow diagram of a hydrogen production and dissolution device according to the present invention;

[0020] FIG3 is a schematic structural diagram of an electrolyzer according to the present invention;

[0021] FIG4 is a schematic diagram of the split structure of the reaction tank of the present invention;

[0022] FIG5 is a schematic diagram of the installation angle of the reaction tank of the present invention. DETAILED DESCRIPTION

[0023] To make the objectives, technical solutions, and advantages of the present invention more apparent, the present invention will be further described in detail below with reference to the accompanying drawings. It is hereby stated that any directional terms such as "up," "down," "left," "right," "front," "back," "inside," and "outside" that appear or will appear herein are based solely on the accompanying drawings and are not intended to limit the present invention.

[0024] 1 and 2 , an embodiment of the present invention discloses a hydrogen production and dissolution device, comprising a shell 1, a stand 2, a power supply assembly 7, an electrolysis assembly 3, a processing assembly 4, a reaction assembly 5 and a heat dissipation assembly 6. The stand 2 is arranged in the shell 1 and is used to support the power supply assembly 7, the electrolysis assembly 3, the processing assembly 4, the reaction assembly 5 and the heat dissipation assembly 6. The shell 1 wraps and protects the stand 2. A power supply chamber 11 and a reaction chamber 12 are provided in the shell 1. The power supply chamber 11 and the reaction chamber 12 are separated by a partition 13. The power supply assembly 7 is arranged in the power supply chamber 11, and the electrolysis assembly 3, the processing assembly 4 and the reaction assembly 5 are arranged in the reaction chamber 12. The partition 13 is sealed to prevent hydrogen from entering the power supply chamber 11 when it overflows, and to prevent hydrogen from contacting electronic control devices that may produce open flames.

[0025] The electrolysis component 3 includes a water tank 31 and an electrolyzer 32, the water tank 31 is connected to the electrolyzer 32, the water tank 31 contains water, the water is passed into the electrolyzer 32 for electrolysis, and the electrolysis can produce oxygen and hydrogen, the electrolyzer 32 is electrically connected to the power supply component 7, and the power supply component 7 supplies power to the electrolyzer 32, the processing component 4 includes a gas-liquid separator 41, the gas-liquid separator 41 is connected to the electrolyzer 32, the hydrogen produced by electrolysis is passed into the gas-liquid separator 41, the excess liquid is separated from the hydrogen in the gas-liquid separator 41, and the hydrogen is preliminarily purified. After the gas is treated, the reaction component includes a supercharger 51 and a reaction tank 52. One end of the supercharger 51 is connected to the gas-liquid separator 41, and the other end of the supercharger 51 is connected to the reaction tank 52. Hydrogen can enter the reaction tank 52, and the reaction tank 52 is filled with pure water. The supercharger 51 pressurizes the reaction tank 52 and can provide a high-pressure environment in the reaction tank 52. An ultrasonic generator 53 is provided in the reaction tank 52. The ultrasonic generator 53 can promote the dissolution and diffusion of hydrogen molecules by generating high-frequency vibration waves, thereby accelerating the reaction of hydrogen and water.

[0026] [Corrected on 11.08.2025 according to Rule 91] The hydrogen production and dissolution equipment also includes a heat dissipation component 6, which includes a first heat dissipation fan 61 and a second heat dissipation fan 62. The first heat dissipation fan 61 is arranged in the power cavity 11, and the second heat dissipation fan is arranged in the reaction cavity 12 and is located on the side of the electrolyzer 32. The first heat dissipation fan 61 and the second heat dissipation fan 62 can dissipate heat for the power cavity 11 and the electrolyzer 32 respectively, and can blow away the hydrogen and oxygen in the cavity while reducing the temperature of the components to prevent the generation of open flames, so as to further ensure safety.

[0027] The beneficial effects of the embodiments of the present invention are as follows:

[0028] The hydrogen production and dissolution equipment of the embodiment of the present invention is provided with a housing 1, a stand 2, a power supply assembly 7, an electrolysis assembly 3, a processing assembly 4, a reaction assembly 5, and a heat dissipation assembly 6, wherein the electrolysis assembly 3 includes a water tank 31 and an electrolyzer 32, the processing assembly 4 includes a gas-liquid separator 41, and the reaction assembly 5 includes a supercharger 51 and a reaction tank 52. The water in the water tank 31 can enter the electrolyzer 32 for electrolysis, and the generated hydrogen is separated into gas and liquid by the gas-liquid separator 41. After treatment, the hydrogen enters the reaction tank 52 and is pressurized by the supercharger 51. The reaction tank 52 is filled with pure water and is provided with an ultrasonic generator 53. Under a high-pressure environment, the ultrasonic generator 53 can promote the dissolution of hydrogen in water. Thus, hydrogen production and dissolution operations can be carried out simultaneously without the need for additional storage and transportation of hydrogen. Moreover, the shell 1 includes a reaction chamber 12 and a power chamber 11, and the power chamber 11 and the reaction chamber 12 are separated by a partition 13. The power supply component 7 is arranged in the power chamber 11, and the electrolysis component 3, the processing component 4 and the reaction component 5 are arranged in the reaction chamber 12. The hydrogen production and dissolution equipment also includes a heat dissipation component 6, and the first heat dissipation fan 61 and the second heat dissipation fan 62 of the heat dissipation component 6 are respectively arranged in the power chamber 11 and the reaction chamber 12. By isolating the components used for electrolysis and hydrogen dissolution from the power supply component 7, even if hydrogen leakage occurs, hydrogen can be avoided as much as possible from contacting the components in the power supply component 7, and the first heat dissipation fan 61 and the second heat dissipation fan 62 can promote air circulation, and even if hydrogen leaks, it can prevent aggregation, with high safety, which can reduce safety hazards.

[0029] Specifically, the electrolysis assembly 3 further includes a pump 33, which is preferably a water pump. The pump 33 is disposed below the water tank 31. The input end of the pump 33 is in communication with the water tank 31, and the output end of the pump 33 is in communication with an external chiller. The external chiller is in communication with the electrolyzer 32. Water in the water tank 31 enters the input end of the pump 33 by gravity and negative pressure. The pump 33 then passes the water into the external chiller. The chiller controls the temperature of the water, ensuring that the water reaches a set temperature before entering the electrolyzer 32. This prevents the water temperature from being too high, thereby preventing it from affecting the electrolysis efficiency and damaging the electrolyzer 32.

[0030] Referring to FIG3 , the electrolyzer 32 includes a water inlet 321, a hydrogen outlet 322, an oxygen outlet 323, a negative electrode connection port 324, and a positive electrode connection port 325. The water inlet 321 is connected to an external chiller, the hydrogen outlet 322 is connected to the gas-liquid separator 41, the oxygen outlet 323 is connected to the water tank 31, and the negative electrode connection port 324 and the positive electrode connection port 325 are respectively connected to the electrodes of the power supply assembly 7. The hydrogen produced in the electrolyzer 32 enters the gas-liquid separator 41 through the hydrogen outlet 322 for processing, while the produced oxygen and excess water vapor return to the water tank 31 through the oxygen outlet 323. The oxygen is discharged from the water tank 31, while the excess water vapor can return to the water tank 31 for circulation. The separate discharge of oxygen and hydrogen can minimize safety risks.

[0031] In order to further process the hydrogen and improve the efficiency of hydrogen dissolution, the processing component 4 also includes a purifier 42, and the gas-liquid separator 41 includes a hydrogen outlet 411. The hydrogen outlet 411 is connected to the inlet end of the purifier 42, and the purifier 42 is connected to an external heat source. The dried hydrogen will enter the purifier 42, and the external heat source will heat the hydrogen in the purifier 42. By utilizing the differences in diffusion rate and adsorption characteristics between hydrogen and other substances, impurities such as water vapor, oxygen, carbon dioxide, and chlorine contained in the hydrogen are removed to further purify the hydrogen. The purified hydrogen can increase the purity of the dissolved hydrogen, thereby improving the efficiency of hydrogen dissolution.

[0032] To cool the purified hydrogen gas to facilitate subsequent hydrogen dissolution, the processing assembly 4 further includes a cooling chamber 43. One end of the cooling chamber 43 is connected to the outlet of the purifier 42, and the other end of the cooling chamber 43 is connected to the supercharger 51. The cooling chamber 43 is also connected to an external cooling device. The purified hydrogen gas enters the cooling chamber 43, where it is cooled by the external cooling device. After cooling, the hydrogen gas is then passed into the supercharger 51 and from there into the reaction tank 52 for hydrogen dissolution.

[0033] The reaction tank 52 further includes a tank body 521, and the ultrasonic generator 53 is arranged at the bottom of the tank body 521. By arranging the ultrasonic generator 53 at the bottom of the tank body 521, the ultrasonic wave generated can be propagated more evenly and cover the entire solution, and help prevent hydrogen bubbles from gathering at the bottom and reduce the formation of bubble clusters, thereby avoiding the bubble clusters affecting the effect of hydrogen dissolution.

[0034] Referring to Figure 4, due to the high pressure in the reaction tank 52, in order to ensure the stable operation of dissolved hydrogen and reduce safety hazards, a screw cover 54, a flange ring 55, a telescopic drive member 56 and a locking rod 57 are provided at the top opening of the tank body 521. The screw cover 54 is used to seal the tank body 521, and the flange ring 55, the telescopic drive member 56 and the locking rod 57 are used to lock the screw cover 54 to prevent leakage or explosion. The edge of the screw cap 54 is provided with a protrusion 541, the flange ring 55 is annular, the outer side of the flange ring 55 is fixed to the tank body 521, the inner edge of the flange ring 55 is provided with a limiting groove 551, and the edge of the limiting groove 551 is provided with a mounting notch 552. When sealing, the protrusion 541 can pass through the mounting notch 552 and be screwed into the limiting groove 551 to form a limiting connection. The screw cap 54 covers the top opening of the tank body 521, and the limiting groove 551 can limit the screw cap 54 in the direction of the center line of the reaction tank 52 to prevent the screw cap 54 from being accidentally opened. The screw cap 54 can only be opened when it is rotated to the position where the protrusion 541 corresponds to the mounting notch 552. Furthermore, in order to prevent the rotary cover 54 from rotating to the position where the protrusion 541 corresponds to the mounting notch 552, the fixed end of the telescopic driving member 56 is fixed to the outer side of the flange ring 55, and one end of the locking rod 57 is connected to the movable end of the telescopic driving member 56. The telescopic driving member 56 can drive the other end of the locking rod 57 to be telescoped in the mounting notch 552. When locked, the telescopic driving member 56 drives the locking rod 57 to extend into the mounting notch 552. If the rotary cover 54 rotates, the side of the protrusion 541 will abut against the locking rod 57, so that the rotation of the rotary cover 54 is hindered, thereby preventing the rotary cover 54 from being accidentally opened and ensuring the safe operation of the system.

[0035] Further, referring to Figure 4, in order to ensure safe operation, the reaction component also includes a locking mechanism 59, which includes a rocker arm 591 and a handle 592. Mounting blocks 553 are provided on both sides of the edge of the flange ring 55, and mounting grooves are provided in the mounting blocks 553. One end of the rocker arm 591 is hinged to one of the mounting blocks 553, and the other end of the rocker arm 591 is connected to the other mounting block 553 through a latch 593. The rocker arm 591 can swing around one of the mounting blocks 553 at the top of the flange ring 55. The latch 593 is used to lock the rocker arm 591. After locking, the rocker arm 591 cannot swing. A pull rod 542 is provided at the top of the rotary cover 54. The pull rod 542 protrudes from the surface of the rotary cover 54 and is in a "door" shape. There are two pull rods 542 and they are arranged in parallel. The rocker arm 591 can be inserted between the two pull rods 542. When closing, the pull rod 542 is used to rotate the rotary cover 54 so that the protrusion 541 is screwed into the limit groove 551, and the pull rod 542 is parallel to the swing plane of the rocker 591. Then, the rocker 591 is swung between the two pull rods 542, and the other end of the rocker 591 is fixed with the pin 593. At this time, if the rotary cover 54 rotates, the pull rod 542 will abut against the side of the rocker 591, so that the rocker 591 can prevent the rotary cover 54 from driving the pull rod 542 to rotate, which can further prevent the rotary cover 54 from opening accidentally. When it is necessary to open the rotary cover 54, first pull out the latch 593, and then swing the rocker arm 591 upward. At this time, the rocker arm 591 releases the restriction on the pull rod 542, and at the same time, the telescopic drive member 56 drives the locking rod 57 to retract, and the restriction on the protrusion 541 by the locking rod 57 is released. Then, the pull rod 542 is used to rotate the rotary cover 54 in the opposite direction, so that the protrusion 541 is rotated out of the limiting groove 551, and then the rotary cover 54 can be pulled out.

[0036] In addition, in order to facilitate the user to perform operations such as inspection, feeding, and discharging of the reaction tank 52, the shell also includes an operation cover 14, which is tilted. The side wall of the tank body 521 is provided with a mounting ring 525, and the mounting ring 525 is fixed on the operation cover 14. The rotary cover 54, the flange ring 55, the telescopic drive member 56 and the locking mechanism 59 are exposed on the surface of the operation cover 14. The tilted setting of the operation cover 14 is conducive to facing the user, making it convenient for the user to operate the rotary cover 54.

[0037] In addition, the stand 2 includes a support plate 21. There are multiple reaction tanks 52, and the bottoms of the multiple reaction tanks 52 are fixed to the support plate 21 and tilted. This tilting arrangement can reduce the overall height of the reaction tanks 52, facilitating operations such as adding materials to the openings of the reaction tanks 52. The support plate 21 can secure the multiple reaction tanks 52, allowing the multiple reaction tanks 52 to simultaneously dissolve hydrogen, thereby increasing the output of a single hydrogen dissolution. A solenoid valve 58 is installed between the booster 51 and each reaction tank 52 to individually control whether each reaction tank 52 dissolves hydrogen. Moreover, by being tilted, the area of ​​the horizontal cross-section of the reaction tank 52 at a certain height is larger than the diameter at that height. Therefore, compared to a vertical arrangement, the area for the hydrogen and water reaction and dissolution is larger, which can further improve the hydrogen dissolution efficiency. At the same time, because the ultrasonic generator 53 located at the bottom can reduce the aggregation of bubbles at the bottom, the bubbles at the bottom will float upward. Since the wall of the reaction tank 52 is tilted, the bubbles will gradually approach the inclined side wall during the floating process, thereby forcing the bubbles to move to the wall of the reaction tank 52, preventing the bubbles from affecting the reaction in the middle, thereby improving the hydrogen dissolution efficiency. Specifically, referring to Figure 5, the angle α between the centerline of the reaction tank 52 and the horizontal plane ranges from 40° to 50°.

[0038] To further enhance safety, the reactor 52 is equipped with a pressure relief valve 522, which communicates with an external flame arrester 524. A one-way valve 523 is located between the pressure relief valve 522 and the flame arrester 524. When the pressure within the reactor 52 is too high, the pressure relief valve 522 can be opened to partially discharge the hydrogen. The discharged hydrogen is then protected by the flame arrester 524 to prevent deflagration. Furthermore, the gas-liquid separator 41 is connected to an external cooling device and includes a liquid outlet 412, which communicates with the bottom of the water tank 31. The external cooling device condenses the liquid in the hydrogen, which is then discharged back into the water tank 31 through the liquid outlet 412.

[0039] In addition, referring to FIG1 , the hydrogen production and dissolution equipment further includes a safety component 8, which includes a leakage sensor 81. The leakage sensor 81 is arranged in the reaction chamber and located on the side of the reaction tank 52. The leakage sensor 81 can detect the area around the reaction tank 52. Once a hydrogen leak is detected, the system will be shut down to prevent accidents, thereby further improving safety.

[0040] The above is a preferred embodiment of the present invention. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the principles of the present invention. These improvements and modifications are also considered to be within the scope of protection of the present invention.

Claims

1. [Corrected 11.08.2025 according to Rule 91] A hydrogen production and dissolution device, characterized in that: The invention comprises a shell, a stand, a power supply assembly, an electrolytic assembly, a processing assembly, a reaction assembly and a heat dissipation assembly, wherein the stand is arranged in the shell, the shell comprises a reaction chamber and a power supply chamber, the power supply chamber and the reaction chamber are separated by a partition, the power supply assembly is arranged in the power supply chamber, and the electrolytic assembly, the processing assembly and the reaction assembly are arranged in the reaction chamber; The electrolysis assembly includes a water tank and an electrolyzer, the water tank is in communication with the electrolyzer, the electrolyzer is electrically connected to the power supply assembly, the processing assembly includes a gas-liquid separator, the gas-liquid separator is in communication with the electrolyzer, the reaction assembly includes a supercharger and a reaction tank, one end of the supercharger is in communication with the gas-liquid separator, the other end of the supercharger is in communication with the reaction tank, the supercharger pressurizes the reaction tank, and an ultrasonic generator is provided in the reaction tank; The heat dissipation assembly includes a first heat dissipation fan and a second heat dissipation fan. The first heat dissipation fan is arranged in the power supply cavity, and the second heat dissipation fan is arranged in the reaction cavity and located on the side of the electrolyzer.

2. The hydrogen production and dissolution equipment according to claim 1, characterized in that: The electrolysis assembly also includes a pump component, which is arranged below the water tank and fixed on the stand. The input end of the pump component is connected to the water tank, and the output end of the pump component is connected to an external chiller, and the external chiller is connected to the electrolyzer.

3. The hydrogen production and dissolution equipment according to claim 1, characterized in that: The electrolyzer includes a water inlet, a hydrogen outlet, an oxygen outlet, a negative electrode connection port and a positive electrode connection port. The water inlet is connected to an external chiller, the hydrogen outlet is connected to the gas-liquid separator, the oxygen outlet is connected to the water tank, and the negative electrode connection port and the positive electrode connection port are respectively connected to the electrodes of the power supply assembly.

4. The hydrogen production and dissolution equipment according to claim 1, characterized in that: The processing component also includes a purifier and a cooling tank. The gas-liquid separator includes a hydrogen outlet, which is connected to the inlet end of the purifier. The purifier is connected to an external heat source. One end of the cooling tank is connected to the outlet end of the purifier, and the other end of the cooling tank is connected to the supercharger. The cooling tank is connected to an external cooling device.

5. The hydrogen production and dissolution equipment according to claim 1, characterized in that: The reaction tank also includes a tank body, the ultrasonic generator is arranged at the bottom of the tank body, and the top opening of the tank body is provided with a screw cover, a flange ring, a telescopic drive member and a locking rod, the edge of the screw cover is provided with a protrusion, the inner edge of the flange ring is provided with a limiting groove, the edge of the limiting groove is provided with a mounting notch, the protrusion can pass through the mounting notch and be screwed into the limiting groove to form a limiting connection, the fixed end of the telescopic drive member is fixed to the outer side of the flange ring, one end of the locking rod is connected to the movable end of the telescopic drive member, and the telescopic drive member can drive the other end of the locking rod to telescope in the mounting notch.

6. The hydrogen production and dissolution equipment according to claim 5, characterized in that: The reaction assembly also includes a locking mechanism, which includes a rocker arm and a handle. Mounting blocks are provided on both sides of the edge of the flange ring. One end of the rocker arm is hinged to one of the mounting blocks, and the other end of the rocker arm is connected to the other mounting block through a pin. A pull rod is provided on the top of the rotary cover, and the pull rod protrudes from the surface of the rotary cover. There are two pull rods and they are arranged in parallel. The rocker arm can be inserted between the two pull rods, and the handle is fixed to the top of the rocker arm.

7. The hydrogen production and dissolution equipment according to claim 1, characterized in that: The shell also includes an operating cover, which is arranged at an angle. The side wall of the tank body is provided with a mounting ring, which is fixed to the operating cover. The rotary cover, the flange ring, the telescopic drive member and the locking mechanism are exposed on the surface of the operating cover.

8. The hydrogen production and dissolution equipment according to claim 7, characterized in that: The stand includes a supporting plate, and there are multiple reaction tanks. The bottoms of the multiple reaction tanks are fixed on the supporting plate and arranged at an angle. The angle between the center line of the reaction tank and the horizontal plane ranges from 40° to 50°. A solenoid valve is provided between the supercharger and each of the reaction tanks.

9. The hydrogen production and dissolution equipment according to claim 1, characterized in that: The gas-liquid separator is communicated with an external cooling device. The gas-liquid separator further comprises a liquid outlet, which is communicated with the bottom of the water tank.

10. The hydrogen production and dissolution equipment according to claim 1, characterized in that: The hydrogen production and dissolution equipment further includes a safety component, which includes a leakage sensor. The leakage sensor is arranged in the reaction chamber and located on the side of the reaction tank.

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