The present disclosure relates to an electrolyzed ozone water generator composed of coated titanium anodes, which belongs to the technical field of electrolytic electrolysis ozone water generators.
At present, electrolyzed ozone generators that use electrolyzed water to generate ozone mostly use lead dioxide as the anode material. Because lead dioxide is easily poisoned that reduces its catalytic activity, tap water cannot be used directly as electrolyzed water, but ultrapure water can only be used as electrolyzed water to keep the generator performance stable. In many applications, pure water is electrolyzed to produce ozone gas and then mixed with ordinary water to produce ozone water through mixing technology, which also increases the complexity of ozone equipment. Furthermore, because of the use of lead dioxide as the anode, the electrolyzed ozone generator of such material will denature the surface of lead dioxide and thereby losing catalytic activity of lead dioxide due to the reverse movement of hydrogen ions when exchanging status of turning on and off frequently. Therefore, it is necessary to find a way to generate ozone water that directly uses tap water as electrolyzed water.
The purpose of the present disclosure is to overcome the shortcomings of the prior art and provide an electrolyzed ozone water generator composed of coated titanium anodes. The present disclosure directly uses tap water as water for electrolysis to directly produce ozone water, to solve the problem of catalyst poisoning of the lead dioxide catalyst thereby losing catalytic activity and environmental pollution of lead, and low cost, simple process operation, easy to scale production, easy to replace the generator, easy to operate and use.
The technical solution provided by the present disclosure is as follows:
the beneficial effects of the present disclosure are:
1. In the present disclosure, the tin dioxide coating layer is used as the material of anodes to solve the problem of catalyst poisoning of the lead dioxide catalyst thereby losing catalytic activity and environmental pollution of lead, and the tin dioxide is low cost.
2. The electrolytic ozone water generator of the present disclosure is connected to a constant direct current, the water is electrolyzed under the action of an electric field, and the oxygen ions generate ozone microbubbles under the action of the anode catalyst. The ozone microbubbles are quickly dissolved into the water to directly generate ozone water. The step of producing ozone gas and then mixing with water to produce ozone water, which is currently commonly used, is omitted, and the product made by the present disclosure has a simple structure and low cost.
3. The process of the present disclosure is simple to operate and easy to scale production.
4. The electrolyzed ozone water generator constructed by the present disclosure is easy to replace and convenient to operate and use.
The specific embodiments of the present invention will be described in detail below with reference to the drawings.
A 1 mm thick punched titanium plate of 1000 cm2 with a diameter of 3 mm and a hole density of 1 per square centimeter is taken to sandblasted and roughened, and then the sandblasted and roughened punched titanium plate is placed in a hydrochloric acid aqueous solution with a volume percentage concentration of 30% and heated to 90° C. to be etched for 5 minutes. The etched punched titanium plate is rinsed with pure water and stored in a hydrochloric acid aqueous solution with a volume percentage concentration of 3% for use.
30 grams of tin chloride pentahydrate, 3.9 grams of ruthenium chloride containing 37% ruthenium, and 1.13 grams of nickel chloride hexahydrate is taken to be dissolved in a solution containing 30.9 ml of butyl titanate, 9 ml of nitric acid and 300 ml of ethanol to form into a tin dioxide coating solution doped with ruthenium and nickel.
The punched titanium plate is taken out and dried.
The above-mentioned tin dioxide coating solution doped with ruthenium and nickel is smeared evenly on the punched titanium plate, dried in an infrared oven at 120° C. for 6 minutes, and placed in a high temperature furnace at 420° C. for 10 minutes to thermally decompose the coating material. The steps of smearing, drying and high-temperature thermal decomposition are repeated 8 times, and the furnace temperature is adjusted to 500° C. for the last time and kept for 2 hours before being taken out. The tin dioxide coated titanium anode is produced and ready for use.
A 0.6 mm thick punched titanium plate of 1000 cm2 is taken to sandblasted and roughened, and then the sandblasted and roughened punched titanium plate is placed in a hydrochloric acid aqueous solution with a volume percentage concentration of 20% and heated to 90° C. to be etched for 8 minutes. The etched punched titanium plate is rinsed with pure water and stored in a hydrochloric acid aqueous solution with a volume percentage concentration of 2% for use.
30 grams of tin chloride pentahydrate, 3 grams of ruthenium chloride containing 37% ruthenium, and 0.5 grams of nickel chloride hexahydrate is taken to be dissolved in a solution containing 20 ml of butyl titanate, 5 ml of nitric acid and 300 ml of ethanol to form into a tin dioxide coating solution doped with ruthenium and nickel.
The punched titanium plate is taken out and dried.
The above-mentioned tin dioxide coating solution doped with ruthenium and nickel is smeared evenly on the punched titanium plate, dried in an infrared oven at 130° C. for 3 minutes, and placed in a high temperature furnace at 400° C. for 15 minutes to thermally decompose the coating material. The steps of smearing, drying and high-temperature thermal decomposition are repeated 12 times, and the furnace temperature is adjusted to 480° C. for the last time and kept for 3 hours before being taken out. The tin dioxide coated titanium anode is produced and ready for use.
A 4×6 mm stretched titanium mesh plate of 1000 cm2 after flattening treatment is taken to sandblasted and roughened, and then the sandblasted and roughened stretched titanium mesh plate is placed in a hydrochloric acid aqueous solution with a volume percentage concentration of 10% and heated to 90° C. to be etched for 8 minutes. The etched stretched titanium mesh plate is rinsed with pure water and stored in a hydrochloric acid aqueous solution with a volume percentage concentration of 1% for use.
30 grams of tin chloride pentahydrate, 2.34 grams of ruthenium chloride containing 37% ruthenium, and 0.204 grams of nickel chloride hexahydrate is taken to be dissolved in a solution containing 9.09 ml of butyl titanate, 3 ml of nitric acid and 300 ml of ethanol to form into a tin dioxide coating solution doped with ruthenium and nickel.
The titanium mesh plate is taken out and dried.
The above-mentioned tin dioxide coating solution doped with ruthenium and nickel is smeared evenly on the titanium plate, dried in an infrared oven at 90° C. for 10 minutes, and placed in a high temperature furnace at 450° C. for 8 minutes to thermally decompose the coating material. The steps of smearing, drying and high-temperature thermal decomposition are repeated 5 times, and the furnace temperature is adjusted to 520° C. for the last time and kept for 1 hours before being taken out. The tin dioxide coated titanium anode is produced and ready for use.
As shown in
At first, the anodes and the cathodes of the electrolyzed ozone water generator composed of coated titanium anodes is immersed into water with a conductivity greater than 30 μs/cm. Then, the anodes and the cathodes are powered by a constant current at a power supply voltage ranging between 3.5V and 12V, the water with a conductivity greater than 30 μs/cm passes through the water inlet (1-1-1) and into the inside of the generator. The positive and negative electrodes that supply power to the generator provide constant current power supply to the generator through the cathode conductive stud (1-8) and the anode conductive stud (1-9) at a power supply voltage ranging between 3.5V and 12V. The water with a conductivity greater than 30 μs/cm is electrolyzed under the action of an electric field, and the ozone microbubbles are generated via oxygen ions under the action of the anode catalyst. The ozone microbubbles are quickly dissolved into the water to directly generate the ozone water. The ozone water passes through a water outlet (1-1-2) for the use of removing the biofilm on the pipe wall and sterilizing the pipe water.