CN218951506U - Equipment for generating acid-base water through electrolysis - Google Patents
Equipment for generating acid-base water through electrolysis Download PDFInfo
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- CN218951506U CN218951506U CN202320005620.9U CN202320005620U CN218951506U CN 218951506 U CN218951506 U CN 218951506U CN 202320005620 U CN202320005620 U CN 202320005620U CN 218951506 U CN218951506 U CN 218951506U
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Abstract
The utility model belongs to the field of cleaning and disinfection, in particular to equipment for generating acid-base water by electrolysis, which aims at the problems of low production efficiency and easy pollution in the prior art, and provides the scheme.
Description
Technical Field
The utility model relates to the technical field of cleaning and disinfection, in particular to equipment for generating acid-base water by electrolysis.
Background
The slightly acidic hypochlorous acid water has pH value of 5.0-6.5 and high bactericidal effect, and is also called slightly acidic electrolyzed water and slightly acidic oxidation potential water. In the field of cleaning and disinfection, compared with the current commonly used sodium hypochlorite or alcohol bactericides, the disinfectant can ensure the safety and has the characteristics of reducing the cost and the environmental load.
However, the acid-alkali water of the prior device is mainly stirred and configured by various materials, the efficiency is low, a large amount of pollution is easy to generate in the production and manufacturing process, and meanwhile, the produced acid-alkali water has low disinfection efficiency and inconvenient operation.
Disclosure of Invention
Based on the technical problems of low production efficiency and easy pollution in the prior art, the utility model provides equipment for generating acid-base water by electrolysis.
The utility model provides equipment for generating acid and alkali water through electrolysis, which comprises an RO water machine, wherein the output end of the RO water machine is communicated with a water purifying tank, a pipeline at the output end of the RO water machine is communicated with a salt dissolving tank, the output end of the salt dissolving tank is communicated with a salt water tank, the output end of the water purifying tank is communicated with an acid making electrolytic tank, the pipeline at the output end of the water purifying tank is communicated with an alkali making electrolytic tank, one output end of the acid making electrolytic tank and one output end of the alkali making electrolytic tank are communicated with an acid water tank, the other output ends of the acid making electrolytic tank and the alkali making electrolytic tank are communicated with an alkaline water tank, the output end of the salt water tank is communicated with a salt water peristaltic pump R1, the salt water peristaltic pump R1 is respectively communicated with the acid making electrolytic tank and the alkali making electrolytic tank through pipelines, the bottoms of the acid water tank are communicated with an alkaline water outlet, and power wires of the acid making electrolytic tank and the alkali making electrolytic tank are connected with an electrolytic power supply.
Preferably, the top outside the brine tank is fixedly provided with a brine tank upper water level gauge, and the bottom outside the brine tank is fixedly provided with a brine tank lower water level gauge.
Preferably, the top outside the acid water tank is fixedly provided with an acid water tank upper water gauge, and the bottom outside the acid water tank is fixedly provided with an acid water tank lower water gauge.
Preferably, the top outside the clean water tank is fixedly provided with an upper water level gauge of the clean water tank, and the bottom outside the clean water tank is fixedly provided with a lower water level gauge of the clean water tank.
Preferably, an alkali water tank upper water level gauge is fixedly arranged at the top end of the outer part of the alkali water tank, and an alkali water tank lower water level gauge is fixedly arranged at the bottom end of the outer part of the alkali water tank.
Preferably, a main control board is connected among the brine tank, the alkali tank, the acid tank, the RO water machine and the water purifying tank through line wires.
Preferably, the input end of the main control board is connected with a control power supply through a wire, and the output end of the main control board is connected with a display board through a wire.
Preferably, the electromagnetic valve groups are fixedly arranged on the pipelines of the salt dissolving tank, the water purifying tank, the acid making electrolytic tank and the alkali making electrolytic tank.
Preferably, the rear end communication on the right side of the top of the salt dissolving tank is communicated with the output end of the RO water machine, the front end on the right side of the top of the salt dissolving tank is communicated with the water outlet end of the salt dissolving tank, and the water inlet end of the salt dissolving tank is communicated with the water outlet end of the bottom of the salt dissolving tank.
Preferably, a water stop plate, a submersible pump and a concentration detector are respectively arranged in the brine tank.
The beneficial effects of the utility model are as follows: the raw materials are simple and common, the operation is simple and convenient, the PH and the available chlorine can be adjusted at will, the use is convenient, the environment is protected, the pollution is avoided, the dissolving process is convenient, the required concentration data is set by only injecting enough NaCL or potassium chloride and other organic salts at random, the required concentration brine can be automatically prepared, and the salt concentration proportioning precision is high.
Drawings
FIG. 1 is a schematic diagram of a left-hand structure of an apparatus for generating acid-base water by electrolysis according to the present utility model;
FIG. 2 is a schematic diagram of the internal structure of an apparatus for generating acid-base water by electrolysis according to the present utility model;
FIG. 3 is a schematic diagram of a brine tank of an apparatus for generating acid-base water by electrolysis according to the present utility model;
FIG. 4 is a schematic diagram of an acid water tank structure of an apparatus for generating acid-base water by electrolysis according to the present utility model;
FIG. 5 is a schematic diagram of a clean water tank structure of an apparatus for generating acid-base water by electrolysis according to the present utility model;
fig. 6 is a schematic diagram of an alkaline water tank structure of an apparatus for generating acid-alkaline water by electrolysis according to the present utility model.
In the figure: 1. a salt dissolving tank; 2. a water level gauge is arranged on the brine tank; 3. a brine tank lower water level gauge; 4. a brine tank; 5. an alkali water tank; 6. an acid water tank; 7. a water level gauge is arranged on the acid water tank; 8. a water level gauge under the acid water tank; 9. an acid making electrolytic tank; 10. an alkaline-producing electrolytic tank; 11. an electrolytic power supply; 12. controlling a power supply; 13. RO water machine; 14. a clean water tank; 15. a water level gauge is arranged on the water purifying tank; 16. a water level gauge under the water purifying tank; 17. a water level gauge is arranged on the alkali water tank; 18. a water level gauge under the alkali water tank; 19. an electromagnetic valve group; 20. a main control board; 21. a display panel; 22. an acid water outlet; 23. an alkaline water outlet; 24. a brine peristaltic pump R1; 25. a waste water tank; 26. and a waste water overflow pipeline.
Detailed Description
The utility model is further illustrated below in connection with specific embodiments.
Example 1
Referring to FIGS. 1-6, an apparatus for generating acid-base water by electrolysis is provided in this embodiment, which comprises an RO water machine 13, the RO water machine 13 is called RO machine or RO reverse osmosis water purifier, the output end of the RO water machine 13 is communicated with a clean water tank 14, the clean water tank 14 has thirty liters capacity, the pipeline of the output end of the RO water machine 13 is communicated with a salt dissolving tank 1, the salt dissolving tank 1 is also called salt tank, the twenty kg capacity, the output end of the salt dissolving tank 1 is communicated with a salt tank 4, the salt tank 4 is also called salt liquid tank, the output end of the clean water tank 14 is communicated with an acid making electrolytic tank 9, the acid making electrolytic tank 9 is also called acid electrolytic tank A, the pipeline of the output end of the clean water tank 14 is communicated with an alkali making electrolytic tank 10, the alkali making electrolytic tank 10 is also called alkali electrolytic tank B, one output ends of the acid making electrolytic tank 9 and the alkali making electrolytic tank 10 are communicated with an acid water tank 6, the other output ends of the acid making electrolytic tank 9 and the alkali making electrolytic tank 10 are communicated with an alkali water tank 5, the alkaline water tank 5 is called an alkaline water tank, the acid water tank 6 is called an acid water tank, the output end of the salt water tank 4 is communicated with a salt water peristaltic pump R1, the salt water peristaltic pump R1 is called a peristaltic pump or R1, the salt water peristaltic pump R1 is respectively communicated with the acid making electrolytic tank 9 and the alkaline making electrolytic tank 10 through pipelines, the bottom of the acid water tank 6 is communicated with an acid water outlet 22, the output end of the alkaline water tank 5 is communicated with an alkaline water outlet 23, the alkaline water outlet 23 is a washing water outlet, the power lines of the acid making electrolytic tank 9 and the alkaline making electrolytic tank 10 are connected with an electrolysis power supply 11 through wires, the top end outside the salt water tank 4 is fixedly provided with a salt water tank upper water level meter 2, the salt water tank upper water level meter 2 is a Y3 water level meter, the water level meter is Y1, Y2, Y3, Y4, Y5, Y6, Y7 and Y8, the bottom end outside the salt water tank 4 is fixedly provided with a salt water tank lower water level meter 3, the brine tank lower water gauge 3 is a Y4 water gauge, the top end of the outer part of the acid water tank 6 is fixedly provided with an acid tank upper water gauge 7, the acid tank upper water gauge 7 is a Y5 water gauge, the bottom end of the outer part of the acid water tank 6 is fixedly provided with an acid tank lower water gauge 8, the acid tank lower water gauge 8 is a Y6 water gauge, the top end of the outer part of the water purifying tank 14 is fixedly provided with a water purifying tank upper water gauge 15, the water purifying tank upper water gauge 15 is a Y1 water gauge, the bottom end of the outer part of the water purifying tank 14 is fixedly provided with a water purifying tank lower water gauge 16, the water purifying tank lower water gauge 16 is a Y2 water gauge, the top end of the outer part of the alkali water tank 5 is fixedly provided with an alkali tank upper water gauge 17, the alkali tank upper water gauge 17 is a Y7 water gauge, the bottom end of the outer part of the alkali water tank 5 is fixedly provided with an alkali tank lower water gauge 18, the alkali tank lower water gauge 18 is a Y8 water gauge, the brine tank 4, the alkaline water tank 5, the acid water tank 6, the RO water machine 13 and the clean water tank 14 are connected with a main control board 20 through circuit wires, the input end of the main control board 20 is connected with a control power supply 12 through circuit wires, the output end of the main control board 20 is connected with a display board 21 through circuit wires, the electromagnetic valve group 19 is fixedly arranged on the pipelines of the salt dissolving tank 1, the clean water tank 14, the acid making electrolytic tank 9 and the alkali making electrolytic tank 10, the electromagnetic valve group 19 is provided with a plurality of electromagnetic valves which are respectively a number 1 electromagnetic valve, a number 2 electromagnetic valve, a number 3 electromagnetic valve, a number 4 electromagnetic valve, a number 5 electromagnetic valve, a number 6 electromagnetic valve, a number 7 electromagnetic valve and a number 8 electromagnetic valve, the electromagnetic valve is arranged at the water inlet end of the salt dissolving tank 1, the electromagnetic valve is number 2 on the right side of the bottom of the alkali making electrolytic tank 10, the electromagnetic valve is number 5 on the left side of the bottom of the alkali making electrolytic tank 10, the electromagnetic valve is number 3 on the left side of the bottom of the acid making electrolytic tank 9, the electromagnetic valve is number 4 on the right side of the bottom of the acid making electrolytic tank 9, the pipeline that clean water tank 1 and acid making electrolysis trough 9 are connected is through 6 solenoid valve and salt water peristaltic pump R1 24 intercommunication, salt water peristaltic pump R1 and 5 solenoid valve intercommunication and through 7 solenoid valve and 3 solenoid valve intercommunication, 8 solenoid valve and the water inlet end intercommunication of clean water tank 14, the rear end intercommunication on the top right side of salt dissolving tank 1 communicates with RO water machine 13's output, the front end on salt dissolving tank 1 top right side communicates with the water outlet end of salt water tank 4, the water inlet end of salt water tank 4 communicates with the water outlet end of salt dissolving tank 1 bottom, the inside of salt water tank 4 sets up water-stop, immersible pump and concentration detector respectively, this equipment is by splendid attire electrolyte, water inlet dissolving zone, buffer filter zone, splendid attire electrolyte zone, circulation system five modules are made by titanium steel as the substrate, make 80 x 11 x 0.5 platinum gold titanium electrode slices, pole piece horizontal distance 20mm,0.5A or 0.2A constant current power supply, it gathers organic salt under organic salt different concentration conditions such as NaCL or potassium chloride, corresponding organic salt concentration of operation such as NaCL or potassium chloride.
In the working process of the acid making electrolytic tank 9, alkaline water is generated while acid water is generated, the alkaline water is not pumped away, but overflows to the wastewater tank 25 from the alkaline water tank 5 through the wastewater overflow pipeline 26 after being accumulated, in the working process of the alkali making electrolytic tank 10, acid water is also generated while the alkaline water is generated, the acid water is not pumped away, but overflows to the wastewater tank 25 from the acid water tank 6 through the wastewater overflow pipeline 26 after being accumulated, and the wastewater tank 25 in the RO water machine 13 is used for supplying wastewater to the RO water machine 13 for purifying so as to realize wastewater treatment and reutilization.
Working principle: starting a power switch of equipment, observing a water purifying tank upper water level gauge 15 and a water purifying tank lower water level gauge 16 of the external water level of a water purifying tank 14, starting a RO water machine 13 power supply by a water purifying tank lower water level gauge 16 lamp, starting an electromagnetic valve group 19 of a water inlet end of the water purifying tank 14, turning on a water purifying tank upper water level gauge 15 lamp, closing the electromagnetic valve group 19 of the water inlet end of the water purifying tank 14, observing a brine tank upper water level gauge 2 and a brine tank lower water level gauge 3 of the external water level of a brine tank 4, starting the RO water machine 13 power supply by the brine tank lower water level gauge 3 lamp, starting the electromagnetic valve group 19 of the water inlet end of the salt dissolving tank 1, turning on the brine tank upper water level gauge lamp, closing the electromagnetic valve group 19 of the water inlet end of the salt dissolving tank 1, and detecting salt concentration: starting a salt concentration detection device when the electromagnetic valve group 19 at the water inlet end of the salt dissolving tank 1 is started, starting a submersible pump when the salt concentration device is higher than 5V, prompting that electrolyte is added, continuously running the equipment, starting B2 when the water level meter 8 under the acid water tank is on, stopping running the submersible pump when the electromagnetic valve group 19 at the water inlet end of the salt dissolving tank 1 is closed, detecting a TDS signal of the RO water machine 13, prompting that the electromagnetic valve group 19 is higher than a specified value, prompting that the RO filter element is replaced, continuously running the equipment, starting/stopping an acid switch, starting an acid key lamp, starting a No. 3 electromagnetic valve, a No. 4 electromagnetic valve and a No. 7 electromagnetic valve of the electromagnetic valve group 19, starting a pump after 3 seconds, starting an electrolytic tank A power supply after 3 seconds of R1, starting a No. 3 electromagnetic valve and No. 7 electromagnetic valve when the water level meter 7 on the acid water tank is on, powering down the No. 3 electromagnetic valve and the No. 7 electromagnetic valve on the acid making electrolytic tank 9, namely powering down the electrolytic tank A, the electromagnetic valve No. 3 and the electromagnetic valve No. 7 are powered off 10 seconds after the electromagnetic valve No. 4 is powered off, when the water level meter No. 8 lamp under the acid water tank is powered off, the electromagnetic valve No. 3, the electromagnetic valve No. 4 and the electromagnetic valve No. 7 are started again, then the pump is started again, the power supply of the electrolytic tank A is started after the three pumps R1 are 3 seconds, weak, medium and strong keys are selected, the currents corresponding to the acid making electrolytic tank 9 and the alkali making electrolytic tank 10 are 15A/20A respectively, the acid key is stopped, the acid key lamp is turned off, the electromagnetic valve No. B2, the electromagnetic valve No. 3 and the electromagnetic valve No. 7 are powered off, the electromagnetic valve No. 4 and the electrolytic tank A are powered off after the electromagnetic valve No. 3 and the electromagnetic valve No. 7 are powered off for 10 seconds, the alkali key lamp is started, the electromagnetic valve No. 2, the electromagnetic valve No. 5 and the electromagnetic valve No. 6 are started again, the power supply of the electrolytic tank B is started after the three pumps R1 are started after the three pumps are 3 seconds, when the water level meter 18 lamp under the acid water tank is powered on, and B1 is started, when a water level gauge 17 on an alkali water tank is on, a No. 5 electromagnetic valve and a No. 6 electromagnetic valve are powered off, a No. 2 electromagnetic valve and an electrolytic tank B are powered off after a No. 5 electromagnetic valve and a No. 6 electromagnetic valve are powered off, when a water level gauge 18 under the alkali water tank is powered off, a No. 2 electromagnetic valve, a No. 5 electromagnetic valve and a No. 6 electromagnetic valve are started again, a pump is started again after three pumps R1 are started for 3 seconds, a power supply of the electrolytic tank B is started, weak, medium and strong keys are selected, currents corresponding to an acid making electrolytic tank 9 and an alkali making electrolytic tank 10 are 15A/18A/21A respectively, an alkali key is stopped, the alkali key lamp is powered off, a No. B1 electromagnetic valve, a No. 5 electromagnetic valve and a No. 6 electromagnetic valve are powered off, and a No. 2 electromagnetic valve and an electrolytic tank B are powered off after the No. 5 electromagnetic valve and the No. 6 electromagnetic valve are powered off.
Example 2
Logical relationship of the present application:
1. starting a power switch of the equipment: 1. detecting a water tank high-low liquid level meter Y1/Y2, turning on an RO machine power supply by a Y2 lamp, turning on an electromagnetic valve 8, turning on a Y1 lamp, turning off the electromagnetic valve 8.2, detecting a brine tank high-low liquid level meter Y3/Y4, turning on the RO machine power supply by a Y4 lamp, turning on the electromagnetic valve 1, turning on a Y3 lamp, and turning off the electromagnetic valve 1. 3. Detecting salt concentration: when the electromagnetic valve 1 is started, a salt concentration detection device is started, when the salt concentration device is higher than 5V, the submersible pump is started, and the 'please add electrolyte' is prompted, so that the equipment can continue to operate. When the salt concentration device is lower than 5V, and the electromagnetic valve 1 is closed, the submersible pump stops running. 4. Detecting RO water TDS signal, which is higher than the appointed value, reminding 'please replace RO filter core', the equipment can continue to operate.
2. Starting/stopping an acid switch 1, starting an acid bond, turning on an acid bond lamp, starting electromagnetic valves 3,4 and 7, starting pumps B3 and 400mL, and starting a power supply of an electrolytic tank A after three pumps R1 are 3 seconds; when the Y6 lamp is on, starting B2; when the Y5 lamp is on, the electromagnetic valves 3, 7 and 400mL pump and the electrolytic tank A are powered off, and the electromagnetic valve 4 is powered off 10 seconds after the electromagnetic valves 3 and 7 are powered off. When the Y6 lamp is turned off, the electromagnetic valves 3,4 and 7 are started again, then the B3 and 400mL pumps are started again, the power supply 2 of the electrolytic tank A is started after 3 seconds of the three pumps R1, weak, medium and strong keys are selected, and the corresponding currents for the electrolytic tank are 15A/18/20A respectively. 3. Stopping acid bond, turning off the acid bond lamp, B2, powering off the electromagnetic valves 3 and 7, and powering off the electromagnetic valve 4 and the electrolytic tank A10 seconds after the electromagnetic valves 3 and 7 are powered off.
3. Starting and stopping an alkali switch 1, starting an alkali key, turning on an alkali key lamp, starting electromagnetic valves 2, 5 and 6, starting pumps B3 and 400mL, and starting a power supply of an electrolytic tank B3 seconds after three pumps R1; when the Y8 lamp is on, the B1 is started, when the Y7 lamp is on, the electromagnetic valves 5 and 6 are powered off, and after the electromagnetic valves 5 and 6 are powered off, the electromagnetic valve 2 and the electrolytic tank B are powered off for 10 seconds. When the Y8 lamp is turned off, the electromagnetic valves 2, 5 and 6 are started again, then the B3 and 400mL pumps are started again, the power supply 2 of the electrolytic tank B is started after 3 seconds by the three pumps R1, weak, medium and strong keys are selected, and the corresponding currents for the electrolytic tank are 15A/18/21A respectively. 3. And stopping the alkali key, turning off the alkali key lamp, and turning off the B1, the electromagnetic valves 5 and 6, and turning off the electromagnetic valve 2 and the electrolytic tank B10 seconds after the electromagnetic valves 5 and 6 are turned off.
4. Special definition 1 peristaltic pump R1 flow is controlled at 30 ml/min.
The salt dissolving system consists of five modules of an electrolyte bearing area, a water inlet dissolving area, a buffer filtering area, an electrolyte bearing area and a circulating system, and the principle is as follows: titanium steel is used as a base material, platinum is coated on the surface of the base material, 80 x 11 x 0.5 platinum titanium electrode plates are manufactured, the horizontal distance of the electrode plates is 20mm, constant current power supply is carried out on the electrode plates at 0.5A or 0.2A, working voltages of the electrode plates under the conditions of different concentrations of NaCL are collected, and corresponding NaCL concentrations are calculated.
The acid making electrolytic cell and the alkali making electrolytic cell electrolyze saline water by adopting a diaphragm method to generate acid hypochlorous acid and strong alkaline oil removal water, and then the diaphragm-free electrolytic cell is used for improving the PH and the effective chlorine concentration of the acid hypochlorous acid water. The principle of the method is that dilute saline solution is introduced into a diaphragm electrolytic tank, and the saline solution reacts respectively under the action of an anode and a cathode and an ion membrane as follows: anode: 2 Cl-2e=cl 2 ↑，Cl 2 +H 2 O=hcl+hclo; and (3) cathode: 2h++ 2e=h 2 ∈, ±na+=naoh. At this time, the effluent of the anode in the diaphragm electrolytic tank is acidic hypochlorous acid water, and the effluent of the cathode is strongly alkaline sodium hydroxide water. The main ions contained in the hypochlorous acid water are cl-, clo-, H+ and Na+. The acidic hypochlorous acid water is led into a diaphragm-free electrolytic tank for electrolysis, and the following reaction occurs: 2 hcl=h2 ≡+Cl2↑，2NaCl+2H 2 O＝2NaOH+H 2 ↑+Cl 2 ，2NaOH+Cl 2 ＝NaCl+NaClO+H 2 O。
From the above equation, the diaphragm-free electrolytic cell consumes hydrochloric acid and sodium chloride in acidic hypochlorous acid water, producing hydrogen and sodium hypochlorite. The PH of the solution will start to rise as the strongly acidic hydrochloric acid is consumed and the sodium chloride is consumed and the available chlorine concentration in the solution will rise. According to the working principle, the hypochlorous acid water with corresponding PH and effective chlorine concentration can be produced. The strong alkaline water generated from the diaphragm electrolyzer is generated by electrolysis, and at the moment, the water in the solution can be converted into small molecular water, and the strong alkaline substance of sodium hydroxide exists, so that the oil removing effect is remarkable. The pH and the effective chlorine concentration of the hypochlorous acid water generated by the method can be adjusted by changing the concentration and the water flow of the brine, and the greater the concentration of the brine, the greater the concentration of the pH and the effective chlorine; the smaller the water flow, the greater the pH and available chlorine concentration. Embodiment 1: 2L/min of 0.6% dilute brine is introduced into the diaphragm electrolytic cell, the anode of the diaphragm electrolytic cell generates hypochlorous acid with PH=3 and effective chlorine of 80ppm, and the cathode generates strongly alkaline water with PH=11.2. And introducing hypochlorous acid water of the anode into a diaphragm-free electrolytic tank for electrolysis to generate slightly acidic hypochlorous acid water with PH=6 and 120ppm of available chlorine. Embodiment 2: 2L/min of 1% dilute brine is introduced into the diaphragm electrolytic cell, the anode of the diaphragm electrolytic cell generates hypochlorous acid with the pH of=2.8 and the available chlorine of 120ppm, and the cathode generates strongly alkaline water with the pH of=11.5. And introducing hypochlorous acid water of the anode into a diaphragm-free electrolytic tank for electrolysis to generate slightly acidic hypochlorous acid water with PH=5.5 and 180ppm of available chlorine. Embodiment 3: 4L/min of 1% dilute brine is introduced into the diaphragm electrolytic tank, the anode of the diaphragm electrolytic tank generates hypochlorous acid with PH=3.4 and 90ppm of available chlorine, and the cathode generates strongly alkaline water with PH=11. And introducing hypochlorous acid water of the anode into a diaphragm-free electrolytic tank for electrolysis to generate slightly acidic hypochlorous acid water with PH=6 and 150ppm of available chlorine.
The foregoing is only a preferred embodiment of the present utility model, but the scope of the present utility model is not limited thereto, and any person skilled in the art, who is within the scope of the present utility model, should make equivalent substitutions or modifications according to the technical scheme of the present utility model and the inventive concept thereof, and should be covered by the scope of the present utility model.
Claims (10)
1. The utility model provides an equipment of electrolysis production acid-base water, includes RO water machine (13), its characterized in that, the output intercommunication of RO water machine (13) has clean water tank (14), the pipeline intercommunication of RO water machine (13) output has soluble salt case (1), the output intercommunication of soluble salt case (1) has brine tank (4), the output intercommunication of clean water tank (14) has acid-making electrolysis tank (9), the pipeline intercommunication of clean water tank (14) output has alkali-making electrolysis tank (10), an output and acid tank (6) of acid-making electrolysis tank (9) and alkali-making electrolysis tank (10) are linked together, another output and alkaline water tank (5) of acid-making electrolysis tank (9) and alkali-making electrolysis tank (10) are linked together, the output intercommunication of brine tank (4) has brine pump R1 (24), brine peristaltic pump R1 (24) are linked together with acid-making electrolysis tank (9) and alkali-making electrolysis tank (10) respectively through the pipeline, the bottom of acid-making electrolysis tank (9) and alkali-making electrolysis tank (10) have electric wire (23), the electric wire of acid-making electrolysis tank (10) is linked together.
2. The equipment for generating acid-base water through electrolysis according to claim 1, wherein a brine tank upper water level gauge (2) is fixedly arranged at the top end of the outside of the brine tank (4), and a brine tank lower water level gauge (3) is fixedly arranged at the bottom end of the outside of the brine tank (4).
3. The device for generating acid-base water through electrolysis according to claim 1, wherein an acid tank upper water gauge (7) is fixedly arranged at the top end of the outer part of the acid tank (6), and an acid tank lower water gauge (8) is fixedly arranged at the bottom end of the outer part of the acid tank (6).
4. An apparatus for electrolytically generating sour and alkaline water according to claim 1, characterized in that the top outside the clean water tank (14) is fixedly equipped with a clean water tank upper water gauge (15), and the bottom outside the clean water tank (14) is fixedly equipped with a clean water tank lower water gauge (16).
5. The device for generating acid-base water by electrolysis according to claim 1, wherein an upper water level meter (17) of the base water tank is fixedly arranged at the top end of the outer part of the base water tank (5), and a lower water level meter (18) of the base water tank is fixedly arranged at the bottom end of the outer part of the base water tank (5).
6. The device for generating acid-base water by electrolysis according to claim 1, wherein a main control board (20) is connected between the brine tank (4), the alkaline water tank (5), the acid water tank (6), the RO water machine (13) and the water purifying tank (14) through line wires.
7. The device for generating acid-base water by electrolysis according to claim 6, wherein the input end of the main control board (20) is connected with a control power supply (12) through wires, and the output end of the main control board (20) is connected with a display board (21) through wires.
8. The equipment for generating acid-base water through electrolysis according to claim 1, wherein the pipelines of the salt dissolving tank (1), the water purifying tank (14), the acid making electrolytic tank (9) and the alkali making electrolytic tank (10) are fixedly provided with electromagnetic valve groups (19).
9. The equipment for generating acid-base water through electrolysis according to claim 1, wherein the rear end of the right side of the top of the salt dissolving tank (1) is communicated with the output end of the RO water machine (13), the front end of the right side of the top of the salt dissolving tank (1) is communicated with the water outlet end of the salt dissolving tank (4), and the water inlet end of the salt dissolving tank (4) is communicated with the water outlet end of the bottom of the salt dissolving tank (1).
10. The device for generating acid-base water by electrolysis according to claim 1, wherein a water stop plate, a submersible pump and a concentration detector are respectively arranged in the brine tank (4).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220244828 | 2022-01-29 | ||
| CN2022202448281 | 2022-01-29 |
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| CN218951506U true CN218951506U (en) | 2023-05-02 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114314960A (en) * | 2022-01-29 | 2022-04-12 | 多特姆节能环保科技(大连)有限公司 | Equipment for generating acid-base water by electrolysis |
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2023
- 2023-01-03 CN CN202320005620.9U patent/CN218951506U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114314960A (en) * | 2022-01-29 | 2022-04-12 | 多特姆节能环保科技(大连)有限公司 | Equipment for generating acid-base water by electrolysis |
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