TWI694175B - Automatic electrolysis device - Google Patents

Abstract

The automatic electrolysis device of present invention comprises: a supplement mechanism, a stirring mechanism, an electrolysis mechanism, a mixture mechanism, a sensing mechanism and a control mechanism. The supplement mechanism and the stirring mechanism provide a water and a saline solution respectively. The electrolysis mechanism processes the electrolysis to the saline solution to form an oxidation multiple gases. The mixture mechanism mixes the water with the oxidation multiple gases to obtain an oxidation multiple gaseous solution. The sensing mechanism senses the liquid levels of the saline solution and the oxidation multiple gaseous solution to form liquid level messages and process the operation of the supplement mechanism, the stirring mechanism, the electrolysis mechanism and the mixture mechanism, producing the saline solution and the oxidation multiple gaseous solution. Thus, the present invention produces the oxidation multiple gaseous solution automatically to reduce the labor cost and further improve the production efficiency.

Description

Automatic electrolysis device

The invention relates to an electrolytic device capable of mass-producing an oxidizing system composite gaseous aqueous solution, in particular to an electrolytic device capable of automatically producing an oxidizing system composite gaseous aqueous solution, so as to reduce labor costs.

Since the oxidized composite gas itself has an unpaired free active electron, the oxidized composite gaseous aqueous solution has a strong oxidizing ability and can be used to oxidize proteins, peptides, DNA or RNA of pathogens such as bacteria, viruses, molds, etc. In the past, these pathogens have been eliminated, and because the gaseous oxidized composite gas cannot provide users with convenient use, it is currently used in industries such as health care, food processing, environmental protection, industrial water, Xumu breeding, and sewage treatment... It often dissolves the oxidized composite gas in water to form the oxidized composite gaseous aqueous solution, so that users can easily use the oxidized composite aqueous solution for disinfection, sterilization and deodorization.

However, in order to improve the aforementioned deficiencies, conventional electrolysis devices are currently used to electrolyze brine to form an oxidized composite gas, and then dissolve the oxidized composite gas in water to form an oxidized composite gaseous aqueous solution. However, when it is known When the electrolysis device performs electrolysis, the conventional electrolysis device needs to hire an operator to control the residual capacity of the brine, and when the operator finds that the residual capacity of the brine is too small, the operator must manually operate the conventional electrolysis device To allow the conventional electrolysis device to produce more saline solution. After operating the conventional electrolysis device for a period of time, the operator must take the time to confirm the residual capacity of the saline solution to avoid the depletion of the saline solution, and then learn the electrolysis Only the device can continue to produce the oxidized composite gaseous aqueous solution, resulting in the conventional electrolysis device unable to mass-produce the oxidized composite gaseous aqueous solution in a short time.

The main purpose of the present invention is to reduce the number of operators who operate the electrolysis device, and control the electrolysis device to automatically produce the oxidized composite gaseous aqueous solution by the control mechanism, so that the electrolysis device can produce a large amount of the oxidized composite gaseous aqueous solution in a short time, and then let The user can conveniently use the oxidation-type composite gaseous aqueous solution for disinfection, sterilization and deodorization.

In order to achieve the foregoing object, the present invention relates to an automated electrolysis device, which is mainly composed of a supply mechanism, a stirring mechanism, an electrolysis mechanism, a mixing mechanism, a sensing mechanism, and a control mechanism. It is used to provide an aqueous solution, and the stirring mechanism is used to receive the aqueous solution, and stir the aqueous solution with a plurality of salt particles to form a brine aqueous solution containing salt, then the electrolytic mechanism has an electrolytic cell connected to the stirring mechanism and an A power supply unit connected to the electrolytic cell, the electrolytic cell is used to contain the saline solution, and the power supply unit can provide a voltage to the electrolytic cell, and the electrolytic cell electrolyzes the saline solution to form an oxidized composite type gas.

In addition, the mixing mechanism has a gas-liquid mixing component and a product tank connected to the gas-liquid mixing component. The gas-liquid mixing component is simultaneously connected to the supply mechanism and the electrolytic cell, and mixes the aqueous solution with the oxidizing composite gas Forming an oxidized composite gaseous aqueous solution that is sent to the product tank, wherein the sensing mechanism has a first liquid level sensor mounted on the stirring mechanism and a second liquid level sensor mounted on the product tank The first liquid level sensor can sense the water level of the brine solution in the stirring mechanism to form a first liquid level sensing message, and the second liquid level sensor can sense the level The water level of the above-mentioned oxidized composite gaseous aqueous solution in the finished product tank forms a second liquid level sensing message.

In addition, the control mechanism is connected to the supply mechanism, the stirring mechanism, the electrolysis mechanism, the mixing mechanism and the sensing mechanism at the same time. The control mechanism can control the operation of the supply mechanism and the stirring mechanism according to the first liquid level sensing message to generate The saline aqueous solution, and the control mechanism can control the operation of the supply mechanism, the electrolysis mechanism, and the mixing mechanism according to the second liquid level sensing information, so that the product tank is filled with the oxidation-based composite gaseous aqueous solution.

In a preferred embodiment, the gas-liquid mixing unit has a reaction tank containing the aqueous solution and a gas mixer receiving the oxidized composite gas. The reaction tank is connected to a first motor, and the first motor can The aqueous solution inside the reaction tank first flows through the gas mixer and then returns to the inside of the reaction tank, so that the aqueous solution entrains the oxidation-based composite gas and flows back into the reaction tank to give way to the reaction The aqueous solution in the tank is converted into the above-mentioned oxidation-based composite gaseous aqueous solution.

The sensing mechanism further has a third liquid level sensor installed in the reaction tank, the third liquid level sensor can sense the water level of the oxidized composite gaseous aqueous solution in the reaction tank to form A third liquid level sensing message, and the control mechanism activates the supply mechanism, the electrolysis mechanism, and the gas mixer according to the third liquid level sensing message to generate the oxidation-type composite gaseous aqueous solution.

In this embodiment, the sensing mechanism further has a second concentration sensor installed in the reaction tank, and the second concentration sensor can sense the oxidation-based composite gaseous aqueous solution in the reaction tank Concentration to form a second concentration message that is transmitted to the control mechanism, and the control mechanism controls the delivery of the oxidation-based composite gaseous aqueous solution to the product tank according to the second concentration message.

In another preferred embodiment, the mixing mechanism further includes a second motor and a dilution tank, the second motor is located between the product tank and the dilution tank, and can flow the oxidized composite gaseous aqueous solution into the dilution tank The dilution tank is connected to the supply mechanism and receives the aqueous solution and the oxidized composite gaseous aqueous solution, so that the aqueous solution and the oxidized composite gaseous aqueous solution are mixed inside the dilution tank to form a concentration lower than the oxidized system Dilute oxidation complex gaseous aqueous solution of complex gaseous aqueous solution.

Wherein, the sensing mechanism further has a fourth liquid level sensor installed in the dilution tank, the fourth liquid level sensor can sense the water level of the diluted oxidizing composite gaseous solution in the dilution tank High and low to form a fourth liquid level sensing message, and the control mechanism activates the supply mechanism and the second motor to operate according to the fourth liquid level sensing message, and allows the aqueous solution and the oxidized composite gaseous aqueous solution to flow into the above The inside of the dilution tank forms the above-mentioned diluted oxidation system composite gaseous aqueous solution.

In yet another preferred embodiment, the sensing mechanism further has a temperature sensor installed in the electrolytic cell, the temperature sensor can sense the temperature of the brine solution in the electrolytic cell to form a transmission to The temperature information of the control mechanism enables the control mechanism to generate a warning message or stop the power supply unit from supplying voltage to the electrolytic cell according to the temperature information.

In still another preferred embodiment, the electrolysis cell of the electrolysis mechanism is connected to the supply mechanism so that the electrolysis cell can receive the aqueous solution, and the electrolysis cell is provided with an electric discharge valve that restricts the flow of liquid, wherein the sensing mechanism A fifth liquid level sensor mounted on the electrolytic cell is further provided, and the fifth liquid level sensor can sense the level of the aqueous solution in the electrolytic cell to form a fifth liquid level sensing message Then, the control mechanism activates the operation of the electric control valve according to the fifth liquid level sensing message, so that the aqueous solution located inside the electrolytic cell can be discharged.

In the foregoing four embodiments, the stirring mechanism has a brine stirring tank connected to the supply mechanism and a brine storage tank connected to the brine stirring tank. The brine storage tank is used to hold the brine aqueous solution and install the sensor A first liquid level sensor of the sensing mechanism, and the sensing mechanism further has a first concentration sensor installed in the brine stirring tank, the first concentration sensor can sense the position in the brine stirring tank The salt concentration of the brine solution forms a first concentration message transmitted to the control mechanism, and the control mechanism controls the delivery of the brine solution to the brine storage tank according to the first concentration message.

In addition, a flow meter capable of calculating and changing the liquid flow rate and an electric control valve that restricts the flow of liquid are provided between the stirring mechanism and the electrolytic cell. The flow meter and the electric control valve are electrically connected to the control mechanism, and when the control When the mechanism receives the second concentration message, the electronically controlled valve will allow the saline solution to flow to the flowmeter, causing the flowmeter to calculate the flow rate of the saline solution, when the flowmeter calculates the flow rate of the saline solution has reached a preset Value, the electronically controlled valve will stop the flow of the saline solution to the flowmeter.

The present invention is characterized in that the sensing mechanism senses the remaining capacity of both the brine aqueous solution and the oxidized composite gaseous aqueous solution, and when the sensing mechanism senses that the capacity of both the brine aqueous solution and the oxidized composite gaseous aqueous solution is too small , The control mechanism will control the supply mechanism, the stirring mechanism, the electrolysis mechanism and the mixing mechanism to operate to automatically produce the brine aqueous solution and the oxidation-type composite gaseous aqueous solution, thereby reducing the operation personnel to reduce the labor cost when the electrolysis device is in operation In addition, the electrolytic device can produce a large amount of oxidized composite gaseous aqueous solution in a short time.

In order to facilitate a deeper and more clear and detailed understanding and understanding of the structure, use and characteristics of the present invention, the preferred embodiment is cited, and the detailed description in conjunction with the drawings is as follows:

Referring to FIG. 1, the automated electrolysis device 1 of the present invention is mainly composed of a supply mechanism 10, a stirring mechanism 20, an electrolysis mechanism 30, a mixing mechanism 40, a sensing mechanism 50, and a control mechanism 60. The supply mechanism 10 is used to provide an aqueous solution. In this embodiment, the supply mechanism 10 has an aqueous solution input pipe 11 capable of conveying the aqueous solution and an aqueous solution storage tank 12 connected to the aqueous solution input pipe 11, and the aqueous solution storage tank 12 is used to contain the above Aqueous solution, and connected to a first aqueous solution output pipe 13, a second aqueous solution output pipe 14, a third aqueous solution output pipe 15 and a fourth aqueous solution output pipe 16, whereby when the aqueous solution flows into the aqueous solution through the aqueous solution input pipe 11 In the storage tank 12, the above-mentioned aqueous solution inside the aqueous solution storage tank 12 can flow into the first, second, third, and fourth aqueous solution output pipes 13, 14, 15, 16 respectively.

The stirring mechanism 20 has a brine stirring tank 21 and a brine storage tank 22. The brine stirring tank 21 is connected to the first aqueous solution output pipe 13 of the supply mechanism 10 so that the above-mentioned aqueous solution can flow into the brine stirring tank 21 through the first aqueous solution outlet pipe 13 In the inside of the salt water stirring tank 21, the above-mentioned aqueous solution and the plurality of salt particles can be stirred to form a salt water aqueous solution containing salt. In this embodiment, the above-mentioned plurality of salt particles can be manually added to the inside of the salt water stirring tank 21, Among them, the brine storage tank 22 has a brine inlet pipe 23 capable of conveying the brine aqueous solution and a brine outlet pipe 24 capable of conveying the brine aqueous solution, and the brine inlet pipe 23 is connected to the brine stirring tank 21 so that it is located in the brine stirring tank 21 The above-mentioned brine solution can flow into the interior of the brine storage tank 22 through the brine input pipe 23, so that the brine storage tank 22 can store the above-mentioned brine solution, wherein the brine output pipe 24 is installed with a flow meter 25 capable of calculating and changing the liquid flow rate and One electric control valve 26 that restricts the flow of liquid.

Please refer to FIGS. 1 and 2, the electrolysis mechanism 30 has an electrolysis cell 31, a switching unit 32 and a power supply unit 33. The electrolysis cell 31 is connected to the switching unit 32 and is provided with an electrolysis output connected to the mixing mechanism 40 Tube 311, two upper discharge tubes 312, and two lower discharge tubes 313, and one of the upper discharge tube 312 and one of the lower discharge tubes 313 are both connected to a cathode (not shown) of the electrolytic cell 31, the other Both the discharge pipe 312 and the other lower discharge pipe 313 are connected to an anode (not shown) of the electrolytic cell 31. In addition, each lower discharge pipe 313 is provided with a discharge electric control valve 314 which can restrict the flow of liquid, and The switching unit 32 is connected to the second aqueous solution output pipe 14 of the supply mechanism 10 and the brine output pipe 24 of the stirring mechanism 20 at the same time, and can selectively control the above-mentioned aqueous solution or the above-mentioned brine aqueous solution to flow into the interior of the electrolytic cell 31, as shown in FIG. 2 In this embodiment, the switching unit 32 has a first brine inlet pipe 321, a second brine inlet pipe 322, a first aqueous solution inlet pipe 323, and a second aqueous solution inlet pipe 324, the first and second brine inlet pipes Both 321 and 322 are connected to the brine outlet pipe 24, and the first brine inlet pipe 321 is installed with a first switching electric control valve 321a capable of restricting the flow of the brine solution, and the second brine inlet pipe 322 is installed with a restriction of the flow of the brine solution The second switching electric control valve 322a, in which the first and second aqueous solution inlet pipes 323, 324 are both connected to the second aqueous solution output pipe 14, and the first aqueous solution inlet water 323 is installed to limit the flow of the third aqueous switching Electronically controlled valve 323a, the second aqueous solution inlet 324 is equipped with a fourth switching electrically controlled valve 324a capable of restricting the flow of the aqueous solution. As shown in FIG. 3, both the first brine inlet pipe 321 and the first aqueous solution inlet pipe 323 are in communication In a first introduction tube 325 connected to the anode of the electrolytic cell 31, both the second brine inlet tube 322 and the second aqueous solution 343 are connected to a second introduction tube 326 connected to the cathode of the electrolytic cell 31.

Referring again to FIG. 1, the power supply unit 33 is electrically connected to the electrolytic cell 31. As shown in the figure, the flow meter 25 and the electric control valve 26 are located between the stirring mechanism 20 and the electrolytic cell 31, and the electric control The valve 26 can selectively allow the brine output pipe 24 to assume a connected state or a closed state, wherein when the brine output pipe 24 assumes a connected state through the electronic control valve 26, the brine aqueous solution can flow from the brine storage tank 22 to the switching unit 32 On the contrary, when the brine output pipe 24 is in a closed state through the electric control valve 26, the brine aqueous solution cannot flow from the brine storage tank 22 to the switching unit 32.

Referring again to FIG. 1, the mixing mechanism 40 has a gas-liquid mixing component 41, a product tank 42 and a dilution tank 43. The gas-liquid mixing component 41 has a reaction tank 411 connected to the product tank 42 and a electrolytic output The gas mixer 412 of the tube 311 allows the gas-liquid mixing assembly 41 to be simultaneously connected to the supply mechanism 10 and the electrolytic cell 31, wherein a first mixing tube 413 and a second mixing device are provided between the reaction tank 411 and the gas mixer 412 The tube 414 connects the reaction tank 411 to the gas mixer 412 through the first and second mixing tubes 413 and 414, and the reaction tank 411 is connected to the second aqueous solution output pipe 14 of the supply mechanism 10, so that the reaction tank 411 can receive the above-mentioned aqueous solution .

As shown in FIG. 3, the gas mixer 412 is provided with a mixing part 412a connected to the electrolysis output tube 311. The mixing part 412a presents a hollow state, and the internal pore diameter is smaller than the first and second mixing tubes 413, 414, and One end of the mixing portion 412a extends to form a first connection portion 412b connected to the first mixing tube 413, and at the end remote from the first connection portion 412b, a second connection portion 412c connected to the second mixing tube 414 is formed. The internal apertures of the first and second connecting portions 412b and 412c are tapered. In addition, the product tank 42 has a product input pipe 421 connected to the reaction tank 411 and a product output pipe 422 connected to the dilution tank 43. 43 is connected to the fourth aqueous solution output pipe 16 of the supply mechanism 10 for receiving the aforementioned aqueous solution.

Referring again to FIG. 1, the sensing mechanism 50 has a first liquid level sensor 51, a second liquid level sensor 52, a third liquid level sensor 53, and a fourth liquid level sensing 54, a fifth liquid level sensor 55, a temperature sensor 56, a first concentration sensor 57 and a second concentration sensor 58, as shown in the figure, the first liquid level sensor 51 is installed in the brine storage tank 22 of the stirring mechanism 20, and can sense the level of the above-mentioned brine aqueous solution in the brine storage tank 22, and the second liquid level sensor 52 is installed in the finished tank 42 and can sense the position The water level of the liquid in the finished product tank 42, wherein the third liquid level sensor 53 is installed in the reaction tank 411, and can sense the water level of the liquid in the reaction tank 411, and the fourth liquid level sensor The sensor 54 is installed in the dilution tank 43 and can sense the water level of the liquid in the dilution tank 43. In addition, both the fifth liquid level sensor 55 and the temperature sensor 56 are installed in the electrolytic cell 31. Among them, the fifth liquid level sensor 55 can sense the water level of the liquid in the electrolytic cell 31, and the temperature sensor 56 can sense the temperature of the liquid in the electrolytic cell 31, as shown in the figure, the first A concentration sensor 57 is installed in the brine stirring tank 21 and can be used for the concentration of the liquid in the brine stirring tank 21, then the second concentration sensor 58 is installed in the reaction tank 411 and can sense the liquid in the reaction tank 411 In addition, the control mechanism 60 is simultaneously connected to the supply mechanism 10, the stirring mechanism 20, the electrolysis mechanism 30, the mixing mechanism 40 and the sensing mechanism 50, and can control the supply mechanism 10, the stirring mechanism 20, the electrolysis mechanism 30, the mixing mechanism 40 Operate with the sensing mechanism 50.

Please refer to FIGS. 3 and 5A. When the automated electrolysis device 1 performs electrolysis, the control mechanism 60 opens the electric control valve 26 of the stirring mechanism 20, and the first and second switching electric control valves 321a, 322a and electrolysis of the switching unit 32 The electric control valve 314 of the tank 31 discharges, so that the electric control valve 26 will continue to supply the saline solution in the brine storage tank 22 to the switching unit 32, and the switching unit 32 will introduce the saline solution into the electrolytic cell 31. So that the electrolytic solution 31 is filled with the saline solution, because the saline solution electric control valve 26 inside the saline storage tank 22 will continue to flow into the electrolytic cell 31, and the saline solution inside the electrolytic cell 31 When the liquid level is higher than the height of the upper discharge pipe 312, part of the brine solution will be discharged through the upper discharge pipe 312 to prevent the brine solution from overflowing into the electrolytic cell 31. Next, the power supply unit 33 provides a voltage to the electrolytic cell 31. Let the electrolyzer 31 electrolyze the above brine solution to produce a redox reaction, and then the electrolyzed brine solution will form an oxidized composite gas that can flow into the electrolysis output tube 311. In this embodiment, the oxidized system The compound gas is chlorine dioxide, hypochlorous acid or ozone.

After the brine solution is electrolyzed, the salt concentration of the brine solution in the electrolytic cell 31 will decrease. However, the brine solution in the brine storage tank 22 will continue to flow into the electrolytic cell 31 through the electronic control valve 26 In the electrolytic cell 31, the electrolytic solution 31 can continue to supplement the saline solution with a high salt concentration during the electrolytic operation to avoid a decrease in the salt concentration of the saline solution in the electrolytic cell 31.

As shown in FIG. 5B, after forming the oxidized composite gas, the oxidized composite gas flows to the gas mixer 412 of the gas-liquid mixing module 41 through the electrolytic output tube 311, and the control mechanism 60 controls the supply mechanism 10 to provide the above The aqueous solution allows the above-mentioned aqueous solution to flow into the reaction tank 411 of the gas-liquid mixing assembly 41 through the third aqueous solution output pipe 15, and then, the control mechanism 60 starts a first motor 415 assembled in the first mixing pipe 413, and the first motor 415 will continuously flow the above-mentioned aqueous solution inside the reaction tank 411 into the bulk mixer 412 from the first mixing tube 413, and then flow back into the inside of the reaction tank 411 from the second mixing tube 414. When the mixing section 412a of the mixer 412 is smaller than the inner diameter of the mixing section 412a than the first and second mixing tubes 413 and 414, the flow rate of the aqueous solution is increased, and the oxidized composite gas flowing into the gas mixer 412 can It is quickly brought into the reaction tank 411 by the aqueous solution. When the oxidizing composite gas flows into the reaction tank 411, a part of the oxidizing composite gas is mixed with the aqueous solution in the reaction tank 411 to form The oxidative composite gaseous aqueous solution, and the remaining oxidative composite gas will flow into the reaction tank 411 and be mixed with the aqueous solution inside the reaction tank 411 to form the oxidative composite gaseous aqueous solution. The inner diameter of the portion 412a is smaller than that of the first and second mixing tubes 413 and 414. In order to prevent the above-mentioned aqueous solution from flowing into the gas mixer 412, the above-mentioned aqueous solution will flow back to the reaction tank 411 from the first mixing tube 413. A plurality of gas mixers 412 can be provided between the two mixing tubes 414 to allow the reverse osmosis aqueous solution to be shunted to the plurality of gas mixers 412. In this embodiment, the oxidation-based composite gaseous aqueous solution is chlorine dioxide Aqueous solution, hypochlorous acid aqueous solution or ozone aqueous solution.

When the oxidized composite gaseous aqueous solution is just formed in the reaction tank 411, the oxidized composite gaseous aqueous solution has a low concentration of oxidized composite gas, but because the first motor 415 will re-sink the oxidized composite gaseous aqueous solution Into the gas mixer 412, and then the oxidized composite gaseous aqueous solution is returned to the reaction tank 411, so that more of the oxidized composite gas will flow into the reaction tank 411, and then the oxidized composite gaseous aqueous solution The concentration of the oxidized composite gas will gradually increase. When the concentration of the oxidized composite gas of the oxidized composite gaseous aqueous solution reaches a preset value, the control mechanism 60 will turn off the first motor 415, so that the oxidized composite gas The gaseous aqueous solution of the type can no longer flow into the gas mixer 412 through the first mixing tube 413.

Next, the control mechanism 60 controls that the oxidized composite gaseous aqueous solution can flow into the inside of the product tank 42 through the product input pipe 421. If the oxidized composite gaseous aqueous solution is to be used directly, the product tank 42 can directly discharge the oxidized system Compound gaseous aqueous solution, wherein if the oxidized composite gas of the oxidized composite gaseous aqueous solution is too concentrated, turn on a second motor 423 installed in the product output pipe 422 to let the oxidized composite gaseous After the aqueous solution dilution tank 43 is inside, the supply mechanism 10 flows the aqueous solution into the dilution tank 43 through the fourth aqueous solution output pipe 16, and mixes the aqueous solution and the oxidizing composite gaseous aqueous solution inside the dilution tank 43 to form a The diluted oxidizing composite gaseous solution is lower in concentration than the oxidizing composite gaseous solution.

As shown in FIG. 5C, when the electrolysis cell 31 performs electrolysis, the saline solution in the brine storage tank 22 continues to flow into the interior of the electrolysis cell 31 through the electric control valve 26, so that the brine in the brine storage tank 22 The aqueous solution continues to decrease, and when the first liquid level sensor 51 senses that the water level of the saline solution in the brine storage tank 22 is too low, the first liquid level sensor 51 will form a transmission to the control mechanism 60 The first liquid level sensing message enables the control mechanism 60 to control the supply mechanism 10 and the stirring mechanism 20 to operate according to the first liquid level sensing message, so that the supply mechanism 10 provides the above-mentioned aqueous solution to the brine stirring tank of the stirring mechanism 20 21. Further, the stirring mechanism 20 will stir the formed brine solution, and the first concentration sensor 57 can sense the concentration of the brine solution in the brine stirring tank 21, when in the brine stirring tank 21 When the concentration of the saline solution reaches a preset value, the first concentration sensor 57 forms a first concentration message transmitted to the control mechanism 60, and the control mechanism 60 controls the transmission of the saline solution to the saline storage tank according to the first concentration message In the interior of 22, when the brine storage tank 22 is filled with the saline solution, the first liquid level sensor 51 senses that the height of the saline solution in the brine storage tank 22 is too high, the first liquid level sensor The device 51 will form a first stop message transmitted to the control mechanism 60, so that the control mechanism 60 controls the supply mechanism 10 and the stirring mechanism 20 to stop operation according to the first stop signal to stop the production of the saline solution.

As shown in FIG. 5D, the above-mentioned oxidized composite gaseous aqueous solution inside the finished product tank 42 will gradually be consumed after use, and when the second liquid level sensor 52 senses the oxidized composite compound inside the finished product tank 42 When the water level of the gaseous aqueous solution is too low, the second liquid level sensor 52 will form a second liquid level sensing message transmitted to the control mechanism 60, so that the control mechanism 60 can be based on the second liquid level sensing information. Control the supply mechanism 10, the electrolysis mechanism 30 and the mixing mechanism 40 to operate, wherein when the control mechanism 60 receives the second liquid level sensing message, the control mechanism 60 first controls the supply mechanism 10 to operate, so that the supply mechanism 10 provides the above The brine aqueous solution flows into the inside of the electrolysis cell 31, and then, the control mechanism 60 controls the power supply unit 33 to supply voltage to the electrolysis cell 31, and the electrolysis cell 31 electrolyzes the brine aqueous solution to generate the oxidation-based composite gas, and then the mixing mechanism 40 The generated oxidized composite gaseous aqueous solution can fill the finished product tank 42. In addition, when the finished product tank 42 is filled with the oxidized composite gaseous aqueous solution, the second liquid level sensor 52 senses that it is inside the finished product tank 42 When the water level of the above-mentioned oxidized composite gaseous aqueous solution is too high, the second liquid level sensor 52 will form a second stop message transmitted to the control mechanism 60, so that the control mechanism 60 controls the supply according to the second stop message The mechanism 10, the electrolysis mechanism 30 and the mixing mechanism 40 stop operating to stop the production of the above-mentioned oxidation-based composite gaseous aqueous solution.

Please refer to FIG. 5E. When the third liquid level sensor 53 senses that the water level of the above-mentioned oxidized composite gaseous aqueous solution in the reaction tank 411 is too low, the third liquid level sensor 53 will form a The third liquid level sensing message transmitted to the control mechanism 60 enables the control mechanism 60 to activate the supply mechanism 10, the electrolysis mechanism 30, and the gas mixer 412 according to the third liquid level sensing message to generate the above-mentioned oxidized compound type The gaseous aqueous solution, and the second concentration sensor 58 can sense the concentration of the oxidized composite gaseous aqueous solution in the reaction tank 411 when the oxidized composite gaseous aqueous solution is generated in the reaction tank 411. When the concentration of the oxidized composite gaseous aqueous solution in the interior reaches a preset value, the second concentration sensor 58 will form a second concentration message transmitted to the control mechanism 60, so that the control mechanism 60 controls according to the second concentration information The oxidation-based composite gaseous aqueous solution is delivered to the product tank 42, and then the supply mechanism 10, the electrolysis mechanism 30 and the mixing mechanism 40 are stopped to stop the production of the oxidation-based composite gaseous aqueous solution.

As shown in FIG. 5F, the above-mentioned diluted oxidation system composite gaseous aqueous solution inside the dilution tank 43 is gradually consumed after being used. When the fourth liquid level sensor 54 senses the above-mentioned dilution oxidation inside the dilution tank 43 When the water level of the composite gaseous aqueous solution is too low, the fourth liquid level sensor 54 will form a fourth liquid level sensing message that is transmitted to the control mechanism 60, so that the control mechanism 60 can be based on the fourth liquid level sensing message. The supply mechanism 10 and the second motor 423 are operated to allow the aqueous solution and the oxidized composite gaseous aqueous solution to flow into the dilution tank 43 to form the diluted oxidized composite gaseous aqueous solution, and when the dilution tank 43 is filled with the dilution When the oxidation-type composite gaseous aqueous solution, the fourth liquid level sensor 54 senses that the water level of the above-mentioned diluted oxidation-type composite gaseous aqueous solution is too high, the fourth liquid level sensor 54 will form A fourth stop message transmitted to the control mechanism 60 causes the control mechanism 60 to stop the operation of the supply mechanism 10 and the second motor 423 according to the fourth stop signal to stop the production of the above-mentioned oxidation-based composite gaseous aqueous solution.

As shown in FIG. 5G, when the automated electrolysis device 1 is going to perform a cleaning operation, the control mechanism 60 controls the supply mechanism 10 to provide the above-mentioned aqueous solution to the switching unit 32, and the control mechanism 60 further turns on the third and fourth switching electrical controls of the switching unit. Valves 323a and 324a allow the above-mentioned aqueous solution to flow into the anode and cathode of the electrolytic cell 31 for cleaning to form a wastewater aqueous solution. When the fifth liquid level sensor 55 senses that the water level of the aforementioned aqueous wastewater solution in the electrolytic cell 31 is too high When it is high, the fifth liquid level sensor 55 will form a fifth liquid level sensing message transmitted to the control mechanism 60, and the control mechanism 60 opens the discharge electric control valve 314 according to the fifth liquid level sensing message. The above-mentioned wastewater aqueous solution located inside the electrolytic cell 31 is discharged to a wastewater recovery tank (not shown) through the lower discharge pipe 313.

As shown in FIG. 5H, when the electrolyzer 31 electrolyzes the saline solution, the temperature of the saline solution will increase, and when the temperature sensor 56 senses that the temperature of the saline solution in the electrolytic cell 31 is too high , The temperature sensor 56 will generate a temperature message and transmit the temperature information to the control mechanism 60, wherein the control mechanism 60 can generate a warning message indicating that the temperature of the electrolytic cell 31 is too high or stop the power supply according to the temperature information The supply unit 33 supplies a voltage to the electrolytic cell 31, so that the electrolytic cell 31 cannot perform the oxidation-reduction reaction on the above brine aqueous solution.

The above-mentioned embodiments are only for the convenience of describing the present invention and are not limiting. Without departing from the spirit of the present invention, those skilled in the art who are familiar with this industry and applying the patent scope of the present invention and various simple modifications and modifications made by the invention description should still Included in the following patent applications.

1: Automated electrolysis device 10: Supply organization 11: Aqueous solution input pipe 12: Aqueous solution storage tank 13: The first aqueous solution output tube 14: The second aqueous solution output tube 15: The third aqueous solution output tube 16: The fourth aqueous solution output tube 20: stirring mechanism 21: brine stirring tank 22: brine storage tank 23: brine input pipe 24: brine output pipe 25: Flowmeter 26: Electric control valve 30: Electrolysis mechanism 31: electrolytic cell 311: Electrolytic output tube 312: Upper discharge pipe 313: Lower discharge pipe 314: Emission control valve 32: Switching unit 321: The first brine inlet pipe 321a: The first switching electric control valve 322: Second brine inlet pipe 322a: Second switching electric control valve 323: the first aqueous solution into the water pipe 323a: The third switching electric control valve 324: the second aqueous solution into the water pipe 324a: Fourth switching electric control valve 325: first introduction tube 326: Second inlet tube 33: Power supply unit 40: Mixed institutions 41: Gas-liquid mixing assembly 411: Reaction tank 412: Gas mixer 412a: Mixing Department 412b: First connection 412c: Second connection 413: The first mixing tube 414: Second mixing tube 415: First motor 42: Finished tank 421: finished product input tube 422: Finished output tube 423: Second motor 43: dilution tank 50: sensing mechanism 51: The first liquid level sensor 52: Second level sensor 53: Third level sensor 54: Fourth liquid level sensor 55: Fifth liquid level sensor 56: temperature sensor 57: The first concentration sensor 58: Second concentration sensor 60: Control agency

1 is a schematic diagram of an automated electrolysis device of the present invention; FIG. 2 is a schematic diagram of an electrolytic cell; FIG. 3 is a schematic diagram of a switching unit; FIG. 4 is a schematic diagram of a gas mixer; FIG. 5A is a schematic diagram of an electrolysis mechanism performing electrolysis; Schematic diagram of the mixing mechanism forming an oxidized composite gaseous aqueous solution; FIG. 5C is a schematic diagram of the first liquid level sensor used in conjunction with the control mechanism; FIG. 5D is a second liquid level sensor used in conjunction with the first concentration sensor in the control mechanism Schematic diagram for use; FIG. 5E is a schematic diagram of a third liquid level sensor and a second concentration sensor used in conjunction with a control mechanism; FIG. 5F is a schematic diagram of a fourth liquid level sensor used in conjunction with a control mechanism; FIG. 5G A schematic diagram of the fifth liquid level sensor cooperated with the control mechanism to clean the electrolytic cell; and FIG. 5H is a schematic diagram of the temperature sensor used in conjunction with the control mechanism.

1: Automated electrolysis device

10: Supply organization

11: Aqueous solution input pipe

12: Aqueous solution storage tank

13: The first aqueous solution output tube

14: The second aqueous solution output tube

15: The third aqueous solution output tube

16: The fourth aqueous solution output tube

20: stirring mechanism

21: brine stirring tank

22: brine storage tank

23: brine input pipe

24: brine output pipe

25: Flowmeter

26: Electric control valve

30: Electrolysis mechanism

31: electrolytic cell

311: Electrolytic output tube

312: Upper discharge pipe

313: Lower discharge pipe

314: Emission control valve

32: Switching unit

33: Power supply unit

40: Mixed institutions

41: Gas-liquid mixing assembly

411: Reaction tank

412: Gas mixer

413: The first mixing tube

414: Second mixing tube

415: First motor

42: Finished tank

421: finished product input tube

422: Finished output tube

423: Second motor

43: dilution tank

50: sensing mechanism

51: The first liquid level sensor

52: Second level sensor

53: Third level sensor

54: Fourth liquid level sensor

55: Fifth liquid level sensor

56: temperature sensor

57: The first concentration sensor

58: Second concentration sensor

60: Control agency

Claims (9)

An automated electrolysis device includes: a supply mechanism for providing an aqueous solution; a stirring mechanism for receiving the above aqueous solution and stirring the above aqueous solution with a plurality of salt particles to form a brine aqueous solution containing salt; an electrolysis mechanism having An electrolytic cell connected to the stirring mechanism and a power supply unit connected to the electrolytic cell, the electrolytic cell is used to contain the brine aqueous solution, and the power supply unit can provide a voltage to the electrolytic cell, allowing the electrolytic cell to The brine aqueous solution is electrolyzed to form an oxidized composite gas; a mixing mechanism has a gas-liquid mixing component and a product tank connected to the gas-liquid mixing component, the gas-liquid mixing component is simultaneously connected to the supply mechanism and the electrolytic cell, Mixing the aqueous solution with the oxidizing composite gas to form an oxidizing composite gaseous aqueous solution that is sent to the product tank; a sensing mechanism having a first liquid level sensor mounted on the stirring mechanism and a The second liquid level sensor of the finished product tank, the first liquid level sensor can sense the water level of the brine solution in the stirring mechanism to form a first liquid level sensing message, and the second The liquid level sensor can sense the water level of the oxidized composite gaseous aqueous solution in the inside of the finished product tank to form a second liquid level sensing message; and a control mechanism, which is simultaneously connected to the supply mechanism, the stirring mechanism, Electrolysis mechanism, mixing mechanism and sensing mechanism, the control mechanism can control the supply mechanism and the stirring mechanism to operate according to the first liquid level sensing message to generate the saline solution, and the control mechanism can control the second liquid level Sensing the message to control the operation of the supply mechanism, the electrolysis mechanism and the mixing mechanism, so that the finished product tank is filled with the oxidation-type composite gaseous aqueous solution. The automated electrolysis device according to claim 1, wherein the stirring mechanism has a brine stirring tank connected to the supply mechanism and a brine storage tank connected to the brine stirring tank, the brine storage tank is used to hold the brine Water solution, and install the first liquid level sensor of the above sensing mechanism. The automated electrolysis device according to claim 2, wherein the sensing mechanism further has a first concentration sensor installed in the brine stirring tank, the first concentration sensor can sense the position in the brine stirring tank The salt concentration of the saline solution is used to form a first concentration message transmitted to the control mechanism, and the control mechanism controls the transfer of the saline solution to the saline storage tank according to the first concentration message. The automatic electrolysis device according to claim 1, wherein a flow meter capable of calculating and changing the liquid flow rate and an electric control valve for restricting the flow of liquid are provided between the stirring mechanism and the electrolytic cell, and the flow meter and the electric control valve Electrically connected to the control mechanism, and when the control mechanism receives the second concentration message, the electronically controlled valve will allow the saline solution to flow to the flow meter, causing the flow meter to calculate the flow rate of the saline solution, when the When the flowmeter calculates that the flow rate of the saline solution has reached a preset value, the electronic control valve stops the flow of the saline solution to the flowmeter. The automated electrolysis device according to claim 1, wherein the gas-liquid mixing unit has a reaction tank containing the aqueous solution and a gas mixer that receives the oxidation-based composite gas, and the reaction tank is connected to a first motor, The first motor can flow the aqueous solution inside the reaction tank first through the gas mixer and back to the inside of the reaction tank, so that the aqueous solution entrains the oxidation-based composite gas and flows back into the reaction tank To allow the aqueous solution in the reaction tank to be converted into the oxidized composite gaseous aqueous solution; the sensing mechanism further has a third liquid level sensor installed in the reaction tank, the third liquid level sensor can sense Locate the water level of the oxidized composite gaseous aqueous solution in the reaction tank to form a third liquid level sensing message; the control mechanism activates the supply mechanism, electrolysis mechanism and gas according to the third liquid level sensing message The mixer operates to produce the above-mentioned oxidized composite gaseous aqueous solution. The automated electrolysis device according to claim 5, wherein the sensing mechanism further has a second concentration sensor installed in the reaction tank, and the second concentration sensor can sense the position inside the reaction tank The concentration of the oxidized composite gaseous aqueous solution forms a second concentration message transmitted to the control mechanism, and the control mechanism controls the oxidized composite gaseous aqueous solution to be transported to the product tank according to the second concentration information. The automated electrolysis device according to claim 1, wherein the mixing mechanism further includes a second motor and a dilution tank, the second motor is located between the finished tank and the dilution tank, and can combine the oxidation type The gaseous aqueous solution flows into the inside of the dilution tank, and the dilution tank is connected to the supply mechanism and receives the aqueous solution and the oxidized composite gaseous aqueous solution. The aqueous solution and the oxidized composite gaseous aqueous solution are mixed inside the dilution tank to form a A diluted oxidized composite gaseous aqueous solution having a concentration lower than that of the oxidized composite gaseous aqueous solution; the sensing mechanism further has a fourth liquid level sensor installed in the dilution tank, the fourth liquid level sensor can sense Locating the water level of the diluted oxidizing composite gaseous aqueous solution in the dilution tank to form a fourth liquid level sensing message; the control mechanism activates the supply mechanism and the second liquid level sensor according to the fourth liquid level sensing message The motor operates to allow the aqueous solution and the oxidizing composite gaseous aqueous solution to flow into the dilution tank to form the diluted oxidizing composite gaseous aqueous solution. The automated electrolysis device according to claim 1, wherein the sensing mechanism further has a temperature sensor installed in the electrolytic cell, the temperature sensor can sense the position of the brine solution in the electrolytic cell The temperature forms a temperature message transmitted to the control mechanism, so that the control mechanism generates a warning message according to the temperature information or stops the power supply unit from supplying voltage to the electrolytic cell. The automated electrolysis device according to claim 1, wherein the electrolysis cell of the electrolysis mechanism is connected to the supply mechanism so that the electrolysis cell can receive the aqueous solution, and the electrolysis cell is provided with an electric discharge valve that restricts the flow of liquid; The sensing mechanism further has a fifth liquid level sensor installed in the electrolytic cell, and the fifth liquid level sensor can sense the water level of the aqueous solution in the electrolytic cell to form a fifth liquid The position sensing message; and the control mechanism activates the operation of the electric control valve according to the fifth level sensing message, so that the aqueous solution inside the electrolytic cell can be discharged.

Images