JP2014113549A - Ozone water generator - Google Patents

Abstract

To provide an ozone water generating device capable of generating high concentration ozone water with a relatively simple device configuration.
An ozone water generator 1 for generating ozone water by dissolving ozone gas generated by electrolysis of water into water, comprising an ozone generator 21, wherein the ozone gas generated by the ozone generator 21 is converted into water. An electrolytic cell 2 for generating ozone water by being dissolved in the water, a supply channel 3 for supplying water to the electrolytic cell 2, a water discharge channel 4 for discharging the ozone water generated in the electrolytic cell 2, and the electrolytic cell 2 Degassing means 5 for reducing the dissolved gas in the water supplied to the water, the water in which the dissolved gas is reduced by the degassing means 5 is supplied to the electrolytic cell 2 through the supply path 3, Let the ozone water produced | generated in the said electrolytic vessel 2 be the ozone water production | generation apparatus 1 from which the water discharge channel 4 discharges.
[Selection] Figure 1

Description

  The present invention relates to an ozone water generator.

  Ozone water is widely used in fields such as sterilization, bleaching, and decomposition of organic substances. In addition, as a means for generating ozone, for example, a discharge method and an electrolysis method are known, but the electrolysis method requires only water, and features such as being able to obtain a relatively high concentration ozone gas, It is used in ozone water generators for cleaning.

  Specifically, for example, Patent Document 1 describes an ozone water generating device (deodorizing / sterilizing device) that can generate high-concentration ozone water. In this ozone water generating apparatus, ozone water having a predetermined concentration is generated by circulating ozone water generated by electrolysis by a reflux means.

  Moreover, the electrolytic ionic water production | generation apparatus of patent document 2 is known as a technique relevant to the production | generation of ozone water. In Patent Document 2, when carbonic acid is contained in raw water that is electrolyzed in an electrolytic cell, there is a problem that pH change is suppressed by the reaction of carbonic acid and ionic water, resulting in a decrease in electrolysis efficiency. Have been described. Furthermore, in order to solve this problem, the solubility of carbonic acid in the raw water is reduced by stirring the raw water with the stirring means to gasify and release the carbonic acid, or operating the negative pressure means and the pressurizing means. Thus, a method for releasing and removing gasified carbonic acid has been proposed.

JP 2008-61700 A JP-A-7-265857

  However, for example, in the ozone water generating device of Patent Document 1, it is necessary to provide a reflux means in order to obtain high-concentration ozone water, and there is a problem in that an increase in cost due to complication of the device cannot be avoided.

  On the other hand, the electrolytic ionic water generator of Patent Document 2 aims to suppress the reaction between carbonic acid and ionic water, and does not suggest any configuration for increasing the dissolved concentration of ozone gas.

  This invention is made | formed in view of the above situations, and makes it a subject to provide the ozone water production | generation apparatus which can produce | generate ozone water of high concentration with the structure of a comparatively simple apparatus.

  In order to solve the above-mentioned problems, an ozone water generator of the present invention is an ozone water generator that generates ozone water by dissolving ozone gas generated by electrolysis of water in water, and includes an ozone generator. , An electrolytic tank for generating ozone water by dissolving ozone gas generated by the ozone generator, a supply path for supplying water to the electrolytic tank, and a water discharge path for discharging the ozone water generated in the electrolytic tank And degassing means for reducing dissolved gas in the water supplied to the electrolytic cell, and water in which dissolved gas is reduced by the degassing means is supplied to the electrolytic cell via the supply path. The ozone water generated in the electrolytic cell is discharged from the discharge channel.

  In this ozone water generator, the deaeration means is preferably at least one of an ultrasonic vibration device, a heating device, and an inert gas supply device.

  According to the ozone water generator of the present invention, high-concentration ozone water can be generated with a relatively simple device configuration.

It is the schematic which illustrated 1st Embodiment of the ozone water generating apparatus of this invention. It is the schematic which illustrated 2nd Embodiment of the ozone water generating apparatus of this invention. It is the schematic which illustrated 3rd Embodiment of the ozone water generating apparatus of this invention.

  In the case of the conventional ozone water generating apparatus such as Patent Document 1, for example, the present inventors have dissolved various gases in water supplied into the electrolytic cell. It was considered that the amount of ozone gas generated in the electrolytic cell was limited. Therefore, the present inventors have obtained a new idea that high-concentration ozone water can be obtained by reducing the dissolved gas contained in the water supplied into the electrolytic cell and increasing the amount of ozone gas dissolved, thereby achieving the present invention. It was.

  FIG. 1 is a schematic view illustrating a first embodiment of an ozone water generator according to the present invention. The arrows in FIG. 1 illustrate the flow of water (ozone water).

  The ozone water generator 1 generates ozone water by dissolving ozone gas generated by electrolyzing water (pure water, tap water, etc.) in water, and includes an electrolytic cell 2, a supply path 3, It has a water discharge channel 4 and a deaeration means 5.

  The electrolytic cell 2 includes an ozone generator 21 and a dissolving part 22. The specific configuration of the ozone generator 21 is not particularly limited, and an electrolytic system that electrolyzes water through an electrode to generate ozone gas can be appropriately employed. More specifically, for example, the ozone generator 21 can be exemplified by one having a structure in which the anode 21a and the cathode 21b connected to a power source (not shown) are partitioned by the polymer membrane M. As such a polymer membrane M, a known ion exchange membrane having ozone resistance can be adopted as appropriate. Specifically, for example, an ion exchange membrane based on polytetrafluoroethylene or the like is exemplified. can do. The two electrodes (anode and cathode) can be used in combination with an appropriate anode 21a and cathode 21b suitable for generating ozone water. Specifically, examples of the material of the anode 21a include diamond, gold, and platinum, and examples of the material of the cathode 21b include diamond, stainless steel, gold, silver, platinum, and titanium. . Among these, a diamond electrode is particularly preferable because it can suppress generation of hydrogen and oxygen generated by electrolysis and can efficiently generate ozone water.

  In the ozone water generator 1, water is supplied to the electrolytic cell 2 through the supply path 3. The supply path 3 is provided with an ultrasonic vibration device 51 as the deaeration means 5, and the ultrasonic vibration device 51 is connected to the electrolytic cell 2 through the connection portion 6.

  Specifically, the ultrasonic vibration device 51 includes a first partition wall 51a extending downward from the upper end portion and a second partition wall 51b extending upward from the lower end portion, and the introduction tank A from the upstream side. An intermediate tank B and a discharge tank C are formed. The introduction tank A and the intermediate tank B communicate with each other below the first partition wall 51a, and the intermediate tank B and the discharge tank C communicate with each other above the second partition wall 51b. Further, above the intermediate tank B and the discharge tank C, an atmosphere release portion 51c that is in communication with the outside and capable of releasing gas into the atmosphere via a valve is disposed.

  Furthermore, ultrasonic elements S are disposed on the inner wall surface of the introduction tank A and the inner wall surface of the intermediate tank B. With the ultrasonic element S, ultrasonic vibration can be applied to the water passing through the ultrasonic vibration device 51. The ultrasonic element S is not particularly limited as long as it generates ultrasonic vibration, and a known configuration can be appropriately employed.

  Water that is a raw material for electrolysis is introduced from above the introduction tank A of the ultrasonic vibration device 51 through the supply path 3. And the water in the introduction tank A receives ultrasonic vibration by the ultrasonic element S, and dissolved dissolved gas (for example, oxygen, hydrogen, carbon dioxide, etc.) is gasified, and gas-liquid separation is promoted. . Furthermore, the water that descends the introduction tank A rises in the intermediate tank B through the lower part of the first partition wall 51a. In the intermediate tank B, the ultrasonic vibration by the ultrasonic element S is received again, and the dissolved gas dissolved in the water is gasified to promote gas-liquid separation. Further, in the intermediate tank B, bubbles rise on the water surface of the gasified gas due to the rising water flow, so that gas-liquid separation is further promoted. The gas gas-liquid separated from the water and separated into gas and liquid can be discharged from the upper atmosphere release part 51c, and the water in which the dissolved gas is reduced is discharged through the discharge tank C, and the electrolytic cell is connected through the connection part 6. 2 is supplied.

  In the electrolytic cell 2, the water supplied via the supply path 3 and the ultrasonic vibration device 51 is electrolyzed by the ozone generator 21, and the ozone gas generated from the anode 21 a of the ozone generator 21 is dissolved in the water by the dissolving part 22. By doing so, ozone water is generated. The ozone water generated in the electrolytic cell 2 is discharged to the outside through a water discharge channel 4 communicating with the electrolytic cell 2.

  The ozone water generating device 1 has a room for the ozone gas to be dissolved in water because the dissolved gas in the water supplied to the electrolytic cell 2 by the ultrasonic vibration device 51 is reduced, so that the ozone gas is dissolved in water. The amount is increasing. For this reason, the generation efficiency of ozone water in the electrolytic cell 2 is high, and high-concentration ozone water can be generated. Moreover, since the ozone water generating apparatus 1 only has to arrange the ultrasonic vibration device 51 upstream (supply path 3) of the electrolytic cell 2, the configuration of the apparatus is simple and the cost can be kept low. The high-concentration ozone water generated by the ozone water generator can be suitably used as, for example, ozone water for cleaning.

  In addition, the specific structure of the supply path 3 and the water discharge path 4 is not specifically limited. For example, water pumped from a water supply source (not shown) is continuously supplied into the electrolytic cell 2 through the supply path 3 to generate ozone water, and this ozone water is continuously discharged from the water discharge path 4. It is preferable that it is possible.

  FIG. 2 is a schematic view illustrating a second embodiment of the ozone water generator of the present invention. Parts common to the first embodiment are denoted by the same reference numerals, and a part of the description is omitted below.

  In the ozone water generator 1, a heating unit 52 as a deaeration unit 5 is disposed in the supply path 3. The heating means 52 only needs to be able to heat the water supplied to the electrolytic cell 2 to a desired temperature. For example, known means such as an electric heater can be employed.

  By heating the water supplied to the electrolytic cell 2 by the heating means 52, the solubility of water is lowered and gasification of the dissolved gas in water is promoted, so that the dissolved gas in water is reduced. Therefore, the temperature of the water heated by the heating means 52 can illustrate preferably the range of about 40 degreeC-80 degreeC, for example. Moreover, the gas recovered by gasification from the water can be discharged to the outside by an appropriate method upstream of the electrolytic cell 2.

  Then, the water whose dissolved gas is reduced by the heating means 52 is supplied to the electrolytic cell 2 through the supply path 3. At this time, the water heated by the heating means 52 is preferably cooled to about room temperature. In the electrolytic cell 2, the supplied water is electrolyzed by the ozone generator 21 to generate ozone water.

  The ozone water generating device 1 has less room for the ozone gas to be dissolved in water because the dissolved gas in the water supplied to the electrolytic cell 2 by the heating means 52 is reduced, so the amount of ozone gas dissolved in the water is reduced. It has increased. For this reason, the generation efficiency of ozone water in the electrolytic cell 2 is high, and high-concentration ozone water can be generated. Moreover, since the ozone water production | generation apparatus 1 only needs to arrange | position the heating means 52 in the upstream (supply path 3) of the electrolytic cell 2, the structure of an apparatus is simple and it can suppress cost low.

  FIG. 3 is a schematic view illustrating a third embodiment of the ozone water generator of the present invention. Parts common to the first embodiment are denoted by the same reference numerals, and a part of the description is omitted below.

  In the ozone water generator 1, an inert gas supply device 53 as a deaeration unit 5 is disposed in the supply path 3. The inert gas supply device 53 is not particularly limited as long as the inert gas can be supplied to the water supplied to the electrolytic cell 2. Specifically, for example, an inert gas such as nitrogen can be taken into the water in the supply path 3 by using a negative pressure due to a water flow of water supplied via the ejector 7 or the like. Thereby, since the solubility of water falls, the gasification of the dissolved gas in water is accelerated | stimulated, and the dissolved gas in water reduces. The gas or the inert gas recovered by gasification from the water can be discharged to the outside by an appropriate method upstream of the electrolytic cell 2.

  Then, the water whose dissolved gas is reduced by the inert gas supply device 53 is supplied to the electrolytic cell 2 through the supply path 3.

  In the electrolytic cell 2, the supplied water is electrolyzed by the ozone generator 21 to generate ozone water.

  The ozone water generating device 1 has a room for the ozone gas to be dissolved in water because the dissolved gas in the water supplied to the electrolytic cell 2 by the inert gas supply device 53 is reduced. The amount of dissolution is increasing. For this reason, the generation efficiency of ozone water in the electrolytic cell 2 is high, and high-concentration ozone water can be generated. Moreover, since the ozone water production | generation apparatus 1 should just arrange | position the inert gas supply apparatus 53 in the upstream (supply path 3) of the electrolytic cell 2, the structure of an apparatus is simple and it can hold down cost low. .

  The ozone water generator of the present invention is not limited to the above form. For example, the deaeration means does not necessarily have to be disposed in the supply path, and it is sufficient if the dissolved gas in the water supplied to the electrolytic cell upstream of the electrolytic cell can be reduced. Specifically, for example, the deaeration means can be disposed in a water storage tank connected to the supply path. Furthermore, the deaeration means can be provided by combining a plurality of devices such as an ultrasonic vibration device, a heating device, and an inert gas supply device.

DESCRIPTION OF SYMBOLS 1 Ozone water production | generation apparatus 2 Electrolysis tank 21 Ozone generator 3 Supply path 4 Water discharge path 5 Deaeration means 51 Ultrasonic vibration apparatus 52 Heating means 53 Inert gas supply apparatus 7 Ejector

Claims (2)

An ozone water generator for generating ozone water by dissolving ozone gas generated by water electrolysis in water,
An electrolyzer equipped with an ozone generator and generating ozone water by dissolving ozone gas generated by the ozone generator in water;
A supply path for supplying water to the electrolytic cell;
A water discharge channel for discharging ozone water generated in the electrolytic cell;
Deaeration means for reducing dissolved gas in water supplied to the electrolytic cell;
With
Ozone having dissolved gas reduced by the deaeration means is supplied to the electrolytic cell through the supply channel, and ozone water generated in the electrolytic cell is discharged from the water discharge channel. Water generator. The ozone water generation apparatus according to claim 1, wherein the deaeration means is at least one of an ultrasonic vibration device, a heating device, and an inert gas supply device.

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