JP3082837U - Structure of oxyhydrogen fuel generator - Google Patents

Abstract

(57) [Problem] To provide a structure of an oxyhydrogen fuel generator capable of safely replenishing an electrolyte or the like at any time without stopping the machine and controlling the temperature of the flame at the same time. A main body, a first electrolytic cell, a second electrolytic cell, a cooling fan, a water storage tank, and a temperature control tank.
0, a plurality of radiating tubes 70, a power distribution unit 80, and the like, and these structures are connected by a conduit to effectively generate oxyhydrogen gas.
30, the radiating tube 70 provides cooling and drying effects to improve the quality of gas, and also allows the water tank 50 to replenish the electrolyte at any time.
At 0, a liquid level measuring pipe 57 and a liquid level sensor 58 are installed adjacent to each other, and the electrolytic solution in the water storage tank 50 and the temperature control are adjusted as needed without stopping the machine by installing the water storage box and the liquid storage boxes 14 and 15. Vessel 6
At the same time, the temperature of the flame is adjusted and maintained at the same time as the replenishment of the cooling liquid of 0 is performed.

Description

[Detailed description of the invention]

[0001]

[Technical field to which the invention belongs]

 The present invention relates to the structure of an oxyhydrogen fuel generator, in which the electrolyte in the water storage tank or the temperature-lowering liquid in the temperature control tank can be replenished as needed to maintain and control the flame temperature without stopping the machine. Related to.

[0002]

[Prior art]

 The oxyhydrogen fuel generator having a known structure is mainly of an electrolysis type, and supplies oxyhydrogen fuel by mixing hydrogen and oxygen generated after the electrolyte in the electrolytic cell is electrolyzed and then sending out the mixture. is there. Its structure mainly consists of an outer shell, an electrolytic cell, a heat radiator, an explosion arrester, a cooling cylinder, a storage cylinder, and an electric box. The radiator includes a helical radiator tube and a fan, and the fan is installed outside the radiator tube, and a water injection pump is connected to an outlet end of the radiator tube. The electrolytic cell is composed of a plurality of strip-shaped electrolytic electrode plates, temperature control switches are provided on both sides on the outside, and a water injection pipe is provided behind the switch, and the explosion is provided above the water injection pipe. Prevention devices are installed. A water level controller is provided in front of the electrolytic cell, and a water level tube is provided outside thereof. In the storage cylinder, the conduit and the electrolytic cell are connected at the upper part, and a pressure gauge is installed outside the upper end thereof. The pressure gauge is controlled by a pressure controller, and an oxyhydrogen mixed gas is provided. The pressure is measured. A conduit and a storage cylinder are connected to the bottom of the cooling cylinder, and a pipe is further provided on one side outside. A conduit and a heater are connected to the bottom of the explosion arrester, and a pressure stabilizer is installed on the outside, and a pressure gauge is installed on the pressure stabilizer. Provides a spray on the outside. With the above structure, the oxy-hydrogen mixed gas generated by electrolysis of the water inside the electrolytic cell is collected by the storage cylinder, and is ejected from the spray after passing through the temperature-lowering cylinder, the explosion-prevention device, and the pressure stabilizer in this order. Provide fuel.

[0003]

[Problems to be solved by the invention]

 However, the known structure of the oxyhydrogen generator has the following disadvantages. Since the electrolytic cell is composed of a plurality of plate-like electrolytic electrode plates arranged in a dense manner, when the electrolytic solution is poured between the electrolytic electrode plates, the speed at which the electrolytic solution flows between the electrolytic electrode plates is extremely high. Slowly, when the water extraction pump of the heat radiator extracts the electrolyte in the electrolytic cell and radiates heat, the electrolyte at the water discharge end of the electrolytic tank decreases, and the electrolyte in the tank becomes inclined. In such a situation, there is a possibility that the electrolytic effect at the water discharge end of the electrolytic cell becomes insufficient and the electrolytic effect is reduced, or an oxide film is formed due to the high temperature of the electrolytic electrode plate, which further reduces the electrolytic effect. is there. The size of the electrolytic cell is designed in accordance with the amount of gas generated. However, since the amount of gas generated and the amount of water consumption are in direct proportion, for example, the amount of gas generated per hour Is 1800NL / hr., The hourly consumption of water is 1.0L / hr. Therefore, when the consumption of the electrolyte reaches a certain level, the machine must be stopped and refilled. Must stop working. The oxy-hydrogen mixture gas has no problems such as acetylene or gas with black smoke or toxicity or carbon monoxide.However, since it is a gas that is flammable and has the danger of explosion, an explosion prevention device is provided. However, there is always the danger of explosion. In view of these drawbacks, the present invention provides a structure of the oxyhydrogen fuel generator according to the present invention, which is safe and can adjust the temperature of the flame by replenishing the electrolyte at any time without stopping the machine.

[0004]

[Means for Solving the Problems]

 It mainly consists of the main body, the first electrolytic cell, the second electrolytic cell, a cooling fan, a water storage tank, a temperature control tank, a plurality of radiating tubes, a power distribution section, and the like. I will provide a. In addition to this purpose, the design of the first and second electrolyzer structures provides superior cooling effects, and the multiple radiating tubes provide cooling and drying effects for oxyhydrogen, thereby reducing gaseous emissions. Improve quality. In addition, the installation of the water tank will replenish the electrolyte in the first and second electrolysis tanks at any time so that the electrolysis time can be effectively extended. A liquid level measuring tube and a liquid level sensor are installed adjacent to the water storage tank and temperature control tank, and the electrolyte and temperature control in the water storage tank are performed as needed without stopping the machine by installing a water storage box and a liquid storage box. Replenish the cooling liquid in the tank and adjust and maintain the temperature of the flame at the same time.

[0005]

[Embodiment]

 As shown in FIGS. 1, 2, and 6, the present invention mainly includes a main body 10, a first electrolytic cell 20, a second electrolytic cell 30, a cooling fan 40, a water storage tank 50, a temperature control tank 60, and a plurality of radiating tubes 70. , And a power distribution unit 80. The main body 10 is made of a metal as shown in FIGS. 1 and 2, an outer shell 11 is provided at an outer edge, and a ventilation hole 12 is provided at a bottom portion. Is provided with a vent hole 13 on one side. A water storage box 14 and a liquid storage box 15 are provided at a lower end of the main body 10, and pumps 16 and 17 are provided in the water storage box 14 and the liquid storage box 15, respectively. Reference numeral 17 denotes an electrolytic solution and a cooling liquid which are fed into the water storage box 14 and the liquid storage box 15.

In the first electrolytic cell 20, as shown in FIGS. 3 and 4, the first electrolytic cell 20 is provided above the ventilation hole 12 of the main body 10. The packings 22 are assembled in a crossed manner, and are further fixed by bolts 23. A first water supply port 24 is provided below one side of the first electrolytic cell 20, and a first bleed port 25 is provided at the other upper end. As shown in FIGS. 3 and 4, the second electrolytic cell 30 is provided above the ventilation hole 12 of the main body 10 and adjacent to the first electrolytic cell 20. It has the same structure as the structure of. The second electrolytic cell 30 is assembled by crossing a plurality of electrolytic electrode plates 31 and insulating packings 32, and these are fixed by bolts 33. A second water supply port 34 is provided at a lower end on one side of the second electrolytic cell 30, and a second bleeding port 35 is provided at the other upper end.

As shown in FIGS. 2 and 5, the cooling fan 40 is provided above the first electrolytic cell 20 and the second electrolytic cell 30, and when the cooling fan 40 is started, air is supplied to the bottom of the main body 10. Of the outer shell 11, and is discharged from the air outlet 13 on one side of the outer shell 11. As shown in FIGS. 6 and 8, the water storage tank 50 is provided in the main body 10 and is in a sealed state. At the lower end of the water storage tank 50, two water outlets 51 are provided. . A plurality of air supply ports 52 and a gas rising pipe 53 are provided at an upper end, and two air outlets 54 are provided at an upper end of the gas rising pipe 53. Further, a safety valve 55 is provided at the upper end, and a liquid level indicator 56 and a liquid level detecting pipe 57 are provided on the tank wall of the water storage tank 50. The liquid level indicator 56 and the liquid level detecting pipe 57 are It penetrates the water tank 50, the pipe wall is made of a transparent material or the like, and two sets of liquid position sensors 58 for adjusting the height are provided on the liquid level detecting pipe 57. A water inlet pipe 59 is further provided at the lower end of the water storage tank 50, and a backflow prevention valve 591 is provided on the water inlet pipe 59. One end of the water inlet pipe 59 is connected to the water storage box 14 of the air vent 12 of the main body 10, and the water storage box 14 is switched by a signal from the liquid position sensor 58.

[0008] As shown in FIGS. 6 and 9, the temperature control tank 60 is provided in the main body 10 and is in a hermetically sealed state. The lower end of the low-temperature trachea 61 is located at the bottom of the inside of the temperature control tank 60, and the upper end of the high-temperature trachea 62 is located at the upper end of the inside of the temperature control tank 60. A backflow prevention valve 63 is further provided on the trachea 61. An elevating pipe 64 is provided at the upper end of the temperature control tank 60, a terminal vent 65 is provided on the gas elevating pipe 64, and a safety valve 66 is provided at an upper end of the terminal vent 65. A liquid level indicator 67 and a liquid level detecting pipe 68 are provided on the wall of the temperature control tank 60. The liquid level indicator 67 and the liquid level detecting pipe 68 penetrate through the temperature control tank 60, and the pipe wall is made of a transparent material or the like. A liquid level sensor 69 for adjusting the height position is provided on the liquid level detecting pipe 68, a water inlet pipe 691 is provided at a lower end of the temperature control tank 60, and a backflow prevention valve 692 is provided on the water inlet pipe 691. One end of the water inlet pipe 691 is connected to the liquid storage box 15 of the air outlet 13 of the main body 10. The liquid storage box 15 is switched by a signal from the liquid level sensor 69.

As shown in FIG. 7, the radiator tube 70 is provided above the cooling fan 40, an air supply end 71 is provided at one end of the radiator tube 70, and an air outlet tube 72 is provided at the other end. Further, a plurality of radiation fins 73 are provided at the upper end of the radiation pipe 70. As shown in FIGS. 2 and 10, the power distribution unit 80 is provided above the cooling fan 40, on which a plurality of electric components, a pressure switch 81, and a pressure adjustment valve 82 are provided. A connection end 83 is connected to one end of 81. One end of the pressure regulating valve 82 is provided with a gas inlet end 84, and the other end is provided with two or two or more gas outlet ends 85.

[0010] As shown in FIG. 11, each end port described below is connected using the conduit 90. The connection ends are the water outlet 51 of the water storage tank 50 and the first water supply port 24 of the first electrolysis tank 20, the water discharge port 51 of the water storage tank 50 and the second water supply port 34 of the second electrolysis tank 30, A first extraction port 25 of the first electrolytic cell 20 and an air supply end 71 of the radiator tube 70; a second air outlet 35 of the second electrolytic cell 30 and an air supply end 71 of the radiator tube 70; 70, the air supply port 52 of the water storage tank 50, the air supply port 54 of the water riser 53 of the water storage tank 50, the connection end 83 on the pressure switch 81 of the power distribution unit 80, and the water storage tank 50. The gas outlet end 54 on the pressure control valve 82 of the power distribution unit 80, the gas outlet end 85 of the pressure control valve 82, and the low-temperature air pipe 61 of the temperature control tank 60; The gas delivery end 85 of the pressure control valve 82 and the hot air pipe 62 of the temperature control tank 60.

With the above-described structure, an appropriate amount of electrolyte is injected into the water storage tank 50, a temperature-lowering liquid is injected into the temperature control tank 60, and the electrolyte is supplied from both outlets 51 of the water storage tank 50 respectively. Hydrogen and oxygen are supplied from the first water supply port 24 and the second water supply port 34 into the first electrolytic cell 20 and the second electrolytic cell 30 by the action of the electrolytic electrode plates 21 and 31 from the electrolytic solution. The oxyhydrogen gas is sent out from the first bleed port 25 of the first electrolyzer 20 and the second bleed port 35 of the second electrolyzer 30, passes through the radiator tube 70, and flows into the water reservoir 50. To reach. The oxyhydrogen gas is sent to the pressure switch 81 and the pressure control valve 82 of the power distribution unit 80 from the outlet port 54 at the upper end of the gas rising pipe 53, and the gas sending end 85 of the pressure control valve 82 changes the gas to the temperature. It is fed into the control tank 60. Finally, the gas is sent out through the terminal vent 65 at the end of the temperature control tank 60 to provide the gas to the user.

[0012]

[Effect of the invention]

 According to the present invention, the first and second electrolytic cells are combined in a state in which a plurality of electrolytic electrode plates and an insulating packing are intersected, and are further fixed by being tightened with a plurality of bolts. The plurality of electrolytic electrode plates are directly exposed to the outside, and the electrolytic baths are also fixed above the ventilation holes of the main body and below the cooling fan. Air is sucked in from the ventilation holes and starts cooling work directly on both the electrolytic cells, and is further discharged from the ventilation holes on one side of the outer shell. And succeeded in providing an excellent cooling effect.

[0013] The oxyhydrogen gas generated by the electrolysis has a constant temperature and humidity, so that the oxyhydrogen gas is sent from the first extraction port of the first electrolytic cell and the second outlet of the second electrolytic cell, The water is sent out to the water storage tank via the radiator tube.At this time, since a plurality of radiator tubes are installed above the cooling fan and a plurality of radiator fins are provided on the surface, And, when the humid oxyhydrogen passes through the radiator tube, the plurality of radiator tubes provide the effect of lowering the temperature and cooling the oxyhydrogen gas, so that the temperature and humidity of the oxyhydrogen gas are both reduced, and Water droplets generated after cooling were collected in the water storage tank and reused, so that the quality of the gas was further improved by cooling and drying the oxyhydrogen.

In the water storage tank, the two water outlets are connected to the first electrolytic cell and the second electrolytic cell by a conduit and penetrated, and the electrolyte in the water tank replenishes the electrolytic liquid in the first and second electrolytic cells as needed. In addition to effectively extending the electrolysis time, the liquid level tubes in the water storage tank made it possible to determine the electrolyte levels in the water storage tank, the first and second electrolysis tanks. By injecting an appropriate amount of electrolyte into the water tank, the liquid level of the electrolyte is revealed by the liquid level indicator, and the liquid level of the liquid level detecting tube is observed by two liquid level sensors. When the water level in the tank is higher or lower than the measurement range of the two level sensors, the level sensor emits a warning sound, etc., and the water tank notifies the start of the pump in the water tank from time to time. The electrolyte in the reservoir is pumped by the pump through the water inlet pipe into the reservoir, and when the electrolyte returns to a normal liquid level, the level sensor signals the pump to take action. The backflow prevention valve provided on the inlet pipe prevents the electrolyte from circulating. Also, by injecting an appropriate amount of cooling liquid into the temperature control tank, the cooling liquid is indicated by a liquid level indicator so that the operator can check the liquid position. Is detected by the liquid level sensor, and when the liquid level in the temperature control tank is lower than the measuring range of the sensor, the position sensor immediately starts the pump in the storage box, and the cooling liquid in the storage box is pumped. When the water is supplied to the water inlet pipe and injected into the temperature control tank, and the temperature-lowering liquid is replenished to the normal position, the pump is immediately notified to stop the operation by the sensor, and the water is supplied to the water inlet pipe. A backflow prevention valve is provided to prevent the circulation of the cooling liquid.

[0015] Installation of a pressure switch and a pressure control valve in the power distribution unit, a backflow prevention valve for preventing circulation of the cooling liquid on the low-temperature trachea of the temperature control tank, a safety valve for the temperature control tank, a safety valve for the water tank, and the like. By design, the electrolysis operation can be performed safely, and oxyhydrogen gas is directly provided to the user, which is more secure than the conventional case that does not require a storage cylinder. .

Therefore, besides the purpose of providing oxyhydrogen, an excellent cooling effect can be provided by designing the structure of the first and second electrolytic cells, and the oxyhydrogen is further cooled and dried by a plurality of radiating tubes. By doing so, we succeeded in improving the gas quality at the same time. In addition, the installation of a water storage tank made it possible to replenish the electrolyte in the first and second electrolysis tanks at any time, which effectively extended the working time. In addition, the liquid level detecting tube and liquid level detector installed adjacent to the water storage tank and the temperature control tank, and also the water storage box, may be installed at any time without stopping the machine depending on the installation of the liquid storage box. In addition, it became possible to replenish the cooling liquid in the temperature control tank, and at the same time, succeeded in controlling and maintaining the temperature of the flame.

[Brief description of the drawings]

FIG. 1 is a perspective view 1 of the present invention.

FIG. 2 is a perspective view 2 of the present invention.

FIG. 3 is an explanatory view of the structure and assembly of the present invention.

FIG. 4 is a structural explanatory view of a first electrolytic cell and a second electrolytic cell of the present invention.

FIG. 5 is an explanatory view illustrating the structure and assembly of the present invention.

FIG. 6 is a diagram illustrating the structure and assembly of the present invention.

FIG. 7 is an explanatory diagram 4 illustrating the structure and assembly of the present invention.

FIG. 8 is a sectional view of the structure of the water storage tank of the present invention.

FIG. 9 is a cross-sectional view of the structure of the temperature control tank of the present invention.

FIG. 10 is a cross-sectional view of the structure of the power distribution unit of the present invention.

FIG. 11 is a structural explanatory view of a power distribution unit of the present invention.

[Explanation of symbols]

 DESCRIPTION OF SYMBOLS 10 Main body 11 Outer shell 12 Ventilation hole 13 Vent hole 14 Water storage box 15 Liquid storage box 16 Pump 17 Pump 20 First electrolytic tank 21 Electrode electrode plate 22 Insulation packing 23 Bolt 24 First water supply port 25 First bleed port 30 Second Electrolyzer 31 Electrolyte electrode plate 32 Insulation packing 33 Bolt 34 Second water supply port 35 Second bleed port 40 Cooling fan 50 Water storage tank 51 Water outlet 52 Air supply port 53 Gas rising pipe 54 Air outlet 55 Safety valve 56 Liquid level indicator 57 liquid level detecting pipe 58 liquid level sensor 59 water inlet pipe 591 backflow prevention valve 60 temperature control tank 61 low temperature trachea 62 high temperature trachea 63 backflow prevention valve 64 gas rising pipe 65 terminal vent 66 safety valve 67 liquid level indicator 68 liquid Position detection pipe 69 Liquid level sensor 691 Water inlet pipe 692 Backflow prevention valve 70 Radiator pipe 71 Supply Air end 72 Air exit end 73 Radiation fin 80 Power distribution unit 81 Pressure switch 82 Pressure control valve 83 Connecting end 84 Gas inlet end 85 Gas outlet end 90 Conduit

Claims (4)

[Utility model registration claims] 1. An oxyhydrogen fuel generator mainly comprising a main body, a first electrolytic cell, a second electrolytic cell, a cooling fan, a water storage tank, a temperature control tank, a plurality of radiating tubes, a power distribution unit, and the like. The outer side has an outer shell provided with an air outlet on one side, the bottom has a blower hole, and the lower side is inside a water storage box provided with a pump for sending out an electrolytic solution and a cooling liquid, respectively. A main body having an inside of the liquid storage box, fixed above the main body ventilation hole, assembled with a plurality of electrolytic electrode plates and a plurality of insulating packings, and fixed by tightening bolts; A first electrolytic tank provided with a first water supply port on one side and a first bleeding port on the other side, and a plurality of electrolytic electrode plates and a plurality of insulating packings, which are fixed above the main body ventilation holes. Are assembled together and tightened with bolts and fixed A second electrolytic cell provided with a second water supply port on one side and a second bleeding port on the other; a cooling fan installed above the first electrolytic cell and the second electrolytic cell; Two outlets are provided which are connected to a first water inlet of the first electrolyzer and a second water inlet of the second electrolyzer by a conduit, and a plurality of air inlets and two outlets are provided above. An air vent is provided, and an elevating pipe provided with a safety valve at the uppermost end is provided. On the wall surface, a water storage tank and a penetrating pipe wall are made of a transparent material, and two sets of height positions are provided. A liquid level detecting tube provided with a liquid level sensor capable of adjusting the liquid level is installed, and further, a backflow prevention valve is provided at a lower end, and one end is provided in a water storage box of the main body to detect the liquid level. A water inlet is provided which is connected to one end of the pump whose switch is activated by the signal of the vessel. A low-temperature trachea whose upper end is located at the bottom of the temperature control tank and is provided with a check valve, and whose upper end is an upper end inside the temperature control tank. There is a high-temperature trachea located at the top, and at the top end there is an air vent at the end and at the top end there is an air riser provided with a safety valve. , A liquid level display control pipe penetrating the temperature control tank with a transparent material, and a liquid level detecting pipe provided with a liquid level sensor capable of adjusting the height position are provided. A temperature control tank provided with a water inlet pipe having one end connected to a pump provided in the liquid storage box and having a switch activated by a signal from the liquid level sensor; provided on a cooling fan; Is a first extraction port of the first electrolytic cell and a second outlet of the second electrolytic cell by a conduit. A plurality of radiating tubes having a plurality of radiating fins, and a plurality of radiating tubes having a plurality of radiating fins at the other end, the plurality of radiating fins being connected to a plurality of air supply ports above the water storage tank; And a power distribution unit in which a plurality of electric components are disposed, such as a pressure switch having a connection end at one end, a pressure control valve having a gas inlet end and two or more gas outlet ends, and the like. A conduit connects the connection end of the pressure switch to the outlet of the water tank, and a gas inlet end to which the pressure control valve is connected and the air outlet of the water tank. The structure of the oxyhydrogen fuel generator, wherein the end is connected to a low-temperature trachea and a high-temperature trachea of the temperature control tank. 2. The structure of an oxyhydrogen fuel generator according to claim 1, wherein a liquid level tube is provided on a tank wall of said water storage tank. 3. The structure of the oxyhydrogen fuel generator according to claim 1, wherein a liquid level tube is provided on a wall of the temperature control tank. 4. The structure of the oxyhydrogen fuel generator according to claim 1, wherein a backflow prevention valve is provided in the low-temperature trachea of the temperature control tank to prevent circulation of the cooling liquid.