KR20110015914A - Purification bottle with active radical generator - Google Patents

Purification bottle with active radical generator Download PDF

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Publication number
KR20110015914A
KR20110015914A KR1020090073363A KR20090073363A KR20110015914A KR 20110015914 A KR20110015914 A KR 20110015914A KR 1020090073363 A KR1020090073363 A KR 1020090073363A KR 20090073363 A KR20090073363 A KR 20090073363A KR 20110015914 A KR20110015914 A KR 20110015914A
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KR
South Korea
Prior art keywords
active radical
radical generator
electrodes
electrode
reactor
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KR1020090073363A
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Korean (ko)
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박정일
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박정일
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Priority to KR1020090073363A priority Critical patent/KR20110015914A/en
Publication of KR20110015914A publication Critical patent/KR20110015914A/en

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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/46109—Electrodes
    • C02F2001/46133—Electrodes characterised by the material
    • C02F2001/46138—Electrodes comprising a substrate and a coating

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE: A purification bottle with an active radical generator is provided to improve sterilization and deodorization functions by contacting a mesh-type electrode with an amount of water in the purification bottle. CONSTITUTION: A purification bottle comprises an active radical generator(310). Contaminated gas or liquid flows into an inlet pipe(211) and is discharged through an outlet pipe(212). The active radical generator is inserted into the bottom of a first reactor(220). An upper electrode(311) and a lower electrode(312) are arranged in the active radical generator at an uniform interval. A power supply unit applies power to the upper and lower electrodes.

Description

Purification bottle with active radical generator

The present invention relates to a purifier having an active radical generating device that provides a function of deodorizing the smell of a contaminated gas or liquid using sterilizing water containing a large amount of active radicals, and more particularly, sterilizing in an active radical generating device. By making water and making the path of contact with sterilizing water as long as possible in the double structure of filtration tank to increase odor removal effect and making space in the lower part of active radical generator, creating circulation of sterilization water in doubling structure of sterile water It relates to a canister configured to provide the effect of odor removal.

 The present invention relates to a purification to remove or sterilize a polluted gas or liquid, and when water is used to purify indoor air, the used water becomes contaminated and the pollutant is discharged again. At present, such a problem occurs in the use of a general humidifier, and there are many problems in the food processor, not only the smell, but also the bacteria propagation in the processor.

The usual method is to remove the moisture by putting a separate disinfectant cleaner in the water or by installing a dryer in the food processor. This is due to the extra cost of buying a separate disinfectant cleaner and the use of the dryer. There is a disadvantage in that it can attack at any time because it can multiply, and there is currently no purifier in the market that can remove odor and sterilize and disinfect.

The present invention has been proposed to solve and supplement the above disadvantages,

By making sterilized water and making contact with and reacting with contaminated gas or liquid, it removes the smell of contaminated gas or liquid, and uses it in a safe place where necessary to create a pleasant environment, and replaces only active radical generating device to reduce manufacturing cost. The purpose is to lower the cost.

Purification container having a function of deodorizing with sterilizing water containing a large amount of active radicals according to the present invention for achieving the above object, in the purifying tank provided with an active radical generating device,

Purification container 210 is composed of the upper lid 100 and the power supply connection 150, the contaminated gas or fluid through the inlet pipe 211 is configured to flow through the outlet pipe 212, the purification tank of the dual structure 210,

 Primary reaction space in which primary contact and reaction occur in the dual structure purifier 210 and the dual structure purifier 210 so that the introduced gas or fluid is in natural contact and reaction with the sterilizing water generating active radicals. (221) the first reactor 220 and the first reaction space 221 and the second reaction space 231 connecting pipe 222 and the outlet 222 and 180 degrees opposite the outlet And a secondary reactor 230 having a secondary reaction space 231 in which secondary contact and reaction occur while turning left and right along the outer wall of the primary reactor 220 in the direction of the tube 212.

In the outer wall of the primary reactor 220, many holes having a diameter of 3 mm are formed in the primary reactor 220 and the secondary reactor 230 in the flow of sterilized water by microbubbles generated in the active radical generator 310. Exchange and circulating action therebetween occur, creating a space under the pair of electrodes 311 and 312 of the active radical generating device 310 for the sterilizing water between the secondary reactor 230 and the primary reactor 220. It allows the flow to complete the large cycle between the two reactors.

It is inserted into the lower portion of the primary reactor 220 in which the water treatment process proceeds, the power is supplied to at least one pair of electrodes including the upper electrode 311 and the lower electrode 312 and to maintain the predetermined interval and the pair of electrodes In the purifying container 210 having an active radical generator, characterized in that it comprises a power supply 400 for applying a

The active radical generator is selected from the group consisting of carbon, titanium nitride (titanium nitride), ceramics, tantalum, nickel, tin, palladium, rhodium, ruthenium, or a combination thereof. It is configured to include a purifying tank 210 having a.

The purifying container 210 has an inlet pipe 211 and an outlet pipe 212 are formed in the upper lid 100 and there are many holes in the outer wall of the primary reactor 220 so that the secondary reactor 230 is micro. The sterilizing water flows upward by the bubble and then flows to the secondary reactor 230, and creates a space under the lower electrode 312 in the pair of electrodes 311 and 312 in the secondary reactor 230. Induces a smooth flow of sterilization water to the primary reactor 220 to complete a large circulation, arranged to be similar to the flow direction of the sterilization water generated from a pair of electrodes.

The active radical generator 310 mounted below the primary reactor 220 of the septic tank 210 is configured to sterilize bacteria or contaminants contained in the water by using an electrolysis method. When the electrolysis reaction proceeds, the reaction of directly oxidizing bacteria and microorganisms contained in the water and generating various active radicals such as chlorine, ozone, OH radical and oxygen radical, indirect oxidation and sterilization, Accordingly, since the sterilized water including active radicals and the contaminated gas and liquid are in contact with each other in the first reactor 220 and the second reactor 230 to sterilize and deodorize by direct or indirect oxidation, the contaminated gas and liquid are purified. do.

The active radical generator 310 is configured by inserting the lower portion of the primary reactor 220 of the clarification tank 210 performing the water treatment process. The clarification tank 210 provides a space between the primary reactor 220 and the secondary reactor 230 in which a water treatment process for changing general tap water into sterilized water is performed. The purifying container 210 includes a pair of electrodes 311 and 312 to allow an electrolysis reaction to occur. The electrolysis reaction is generated by supplying a direct current to the pair of electrodes 311 and 312.

The DC current is supplied by the power supply unit 400. In the active radical generator 310 according to a specific embodiment of the present invention, it has been described that the DC current is supplied by the power supply unit 400, but the power supplied by the power supply unit 400 is necessarily a DC voltage. It is not limited. That is, the power supply unit 400 supplies not only a direct current voltage but also a pulse voltage, a square wave pulse voltage, a pulse voltage controlled by time division, and an alternate pulse voltage to the electrodes 311 and 312. By doing so, an electrolysis reaction can occur.

The pair of electrodes 311 and 312 receiving power from the power supply unit 400 is formed in a plate shape having a relatively thin thickness. The pair of electrodes 311 and 312 may include a positive electrode 311 and a negative electrode 312, and the shapes of the positive electrode 311 and the negative electrode 312 may be symmetrical with faces facing each other. A plurality of holes 315 are formed in the positive electrode 311 and the negative electrode 312 at regular intervals. The plurality of holes 315 flows the water in the primary reactor 220 of the septic tank 210 to the secondary reactor 230 through a plurality of holes in the outer wall of the primary reactor 220. And this flow serves as a passage for a large circulation back to the primary reactor 220 through the space in the lower portion of the pair of electrodes (311,312), thereby improving the effect of the electrolysis reaction. In a specific embodiment of the present invention, the electrodes 311 and 312 have been described as being flat plates having a plurality of holes, but are not necessarily limited thereto. That is, the electrodes 311 and 312 may be formed in a mesh shape or a cylindrical shape in which a plurality of holes are formed.

The pair of electrodes 311 and 312 are formed at intervals of 0.9 to 1.1 mm. The gap between the electrodes 311 and 312 is maintained by the support member 317. In addition, the support member 317 forms a gap as described above while the pair of electrodes 311 and 312 are rotated by 90 degrees while having a shape.

Then, the pair of electrodes 311 and 312 are mounted to the clarification tank 210 by using the support member 317 and the electrode bolt 313, and a power supply unit to the electrode bolt 313 through the power connection unit 150. Supply DC power made in 400).

The coating layer is formed on a part or the whole of the surface of the electrode (311, 312). The coating layer is formed of a component selected from the group consisting of platinum compounds, iridium compounds, tin compounds, titanium compounds, palladium compounds, tantalum compounds, rhodium compounds, ruthenium compounds, or a combination thereof. At this time, the thickness of the coating layer is formed within 5㎛ to prevent the occurrence of wear, and to prevent the desorption of the coating layer by the droplets of the electrode surface.

The power supply unit 400 is driven by a control board. And it is provided with a control pad or an operation button for driving the power supply 400 separately. In addition, in order to solve the problem of erosion of the electrodes (311, 312) it can be driven to alternate the direction of the current through the control board.

Purification container 210 according to the present invention, because it is possible to deodorize the contaminated gas or liquid can be used in a place where the odor removal is necessary, can reduce the manufacturing cost and maintenance by replacing only the active radical generating device There is an advantage that it is easy.

Purification container 210 according to the present invention has a dual structure of the primary reactor 220 and the secondary reactor 230 to increase the deodorizing effect and effectively suppress the bacteria and microorganisms generated inside the purification vessel 210 It can be used to disinfect tap water in a simple way. In addition, the use of a mesh-type electrode increases the electrode surface area than when using an electrode having a conventional shape, and thus allows a larger amount of water to be sterilized at the same time since it can be contacted with a larger amount of water in the clarifier 210. Turns into a number Therefore, there is an effect that the sterilization and deodorization function is further improved.

A filter having a function of deodorizing with sterilizing water containing a large amount of active radicals according to the present invention for achieving the above object, in the filter comprising an active radical generator,

Purification container 210 is composed of the upper lid 100 and the power supply connection 150, the contaminated gas or fluid through the inlet pipe 211 is configured to flow through the outlet pipe 212, the purification tank of the dual structure 210,

 The primary reaction space in which the primary contact and reaction takes place in the dual structure purification vessel 210 and the dual structure purification vessel 210 so that the introduced gas or fluid is in natural contact and reaction with the sterilizing water generating active radicals ( 221 of the primary reactor 220 and the primary reaction space 221 and the secondary reaction space 231 with the 221 and the outlet pipe 212 opposite the connector 222 180 degrees And a secondary reactor 230 having a secondary reaction space 231 in which secondary contact and reaction occur while turning left and right along the outer wall of the primary reactor 220 in the) direction.

Many holes having a diameter of 3 mm on the outer wall of the primary reactor 220 direct the flow of sterilized water by micro bubbles generated in the active radical generator 310 to the primary reactor 220 and the secondary reactor 230. It is a structure to exchange and circulate with

A space is placed under the pair of electrodes of the active radical generator 310 to create a flow of sterilizing water between the secondary reactor 230 and the primary reactor 220 to complete a large circulation between the two reactors. Structure.

It is inserted into the lower portion of the primary reactor 220 in which the water treatment process proceeds, the power is supplied to at least one pair of electrodes including the upper electrode 311 and the lower electrode 312 and to maintain the predetermined interval and the pair of electrodes In the purifying container 210 having an active radical generating device 310, characterized in that it comprises a power supply 400 for applying a

The active radical generator is selected from the group consisting of carbon, titanium nitride (titanium nitride), ceramics, tantalum, nickel, tin, palladium, rhodium, ruthenium, or a combination thereof. It is configured to include a purifying tank 210 having a (310).

The purification vessel 210 is the inlet pipe 211 and the outlet pipe 212 is configured in the upper lid 100 and there are a number of holes in the outer wall of the primary reactor 220 there is a micro reactor secondary 230 The sterilizing water flows upward by the bubble and then flows to the secondary reactor 230, and creates a space under the lower electrode 312 in the pair of upper and lower electrodes 311 and 312. In addition, the secondary reaction furnace 230 induces a smooth flow of sterilization water from the first reactor 220 to complete a large circulation, and is arranged to be similar to the flow direction of the sterilization water generated from the pair of electrodes.

Hereinafter, with reference to the accompanying drawings will be described an embodiment of the purifying tank 210 to deodorize the contaminated gas or liquid with sterile water containing an active radical according to the present invention.

1 is a plan view showing a pair of electrodes constituting a specific embodiment of the present invention. It is a block diagram showing the schematic structure of an active radical generating device 310 including a pair of upper electrodes 311 and lower electrodes 312 mounted below the primary reactor 220 of the septic tank 210.

It is configured to sterilize bacteria or contaminants contained in the water by using an electrolysis method of the active radical generator 310 mounted below the primary reactor 220 of the clarification tank 210. When the electrolysis reaction proceeds, the reaction of directly oxidizing bacteria and microorganisms contained in the water and generating various active radicals such as chlorine, ozone, OH radical and oxygen radical, indirect oxidation and sterilization, Accordingly, since the sterilized water including active radicals and the contaminated gas and liquid are in contact with each other in the first reactor 220 and the second reactor 230 to sterilize and deodorize by direct or indirect oxidation, the contaminated gas and liquid are purified. do. Detailed structure and operation principle of the active radical generating device 310 will be described in detail with reference to the drawings.

As shown in FIG. 1, an active radical generating device 310 according to a specific embodiment of the present invention is configured by being inserted into a lower portion of a primary reactor 220 of a septic tank 210 performing a water treatment process. The clarification tank 210 provides a space between the primary reactor 220 and the secondary reactor 230 in which a water treatment process for changing general tap water into sterilized water is performed. The purifying container 210 includes a pair of electrodes 311 and 312 to allow an electrolysis reaction to occur. The electrolysis reaction is generated by supplying a direct current to the pair of electrodes 311 and 312.

The DC current is supplied by the power supply 400. In the active radical generator 310 according to a specific embodiment of the present invention, it has been described that the direct current is supplied by the power supply unit 400, but the power supplied by the power supply unit 400 must be a direct current voltage. It is not limited. That is, the power supply unit 400 supplies not only a direct current voltage but also a pulse voltage, a square wave pulse voltage, a pulse voltage controlled by time division, and an alternate pulse voltage to the electrodes 311 and 312. By doing so, an electrolysis reaction can occur.

As shown in FIG. 1, the pair of electrodes 311 and 312 that receive power from the power supply unit 400 may have a plate shape having a relatively thin thickness. The pair of electrodes 311 and 312 may include a positive electrode 311 and a negative electrode 312, and the shapes of the positive electrode 311 and the negative electrode 312 may be symmetrical with faces facing each other. A plurality of holes 315 are formed in the positive electrode 311 and the negative electrode 312 at regular intervals. The plurality of holes 315 are secondary reactors 230 through a plurality of holes in the outer wall of the primary reactor 220 by the microbubble of the sterilization water in the primary reactor 220 of the clarification tank 210. ) And this flow acts as a passage for a large circulation, which flows back to the primary reactor 220 through the space under the pair of electrodes 311 and 312, thereby improving the effect of the electrolysis reaction. Let's do it. In a specific embodiment of the present invention, the electrodes 311 and 312 have been described as being flat plates having a plurality of holes, but are not necessarily limited thereto. That is, the electrodes 311 and 312 may be formed in a mesh shape or a cylindrical shape in which a plurality of holes are formed.

The pair of electrodes 311 and 312 are formed at intervals of 0.9 to 1.1 mm. The gap between the electrodes 311 and 312 is maintained by the support member 317. In addition, the support member 317 forms a gap as described above while the pair of electrodes 311 and 312 are rotated by 90 degrees while having a shape.

In addition, the pair of electrodes 311 and 312 may be mounted on the septic tank 210 using the support member 317 and the electrode bolt 313, and a power supply unit may be connected to the electrode bolt 313 through a power connection unit 150. Supply the DC power made in 400).

The coating layer is formed on a part or the whole of the surface of the electrode (311, 312). The coating layer is formed of a component selected from the group consisting of platinum compounds, iridium compounds, tin compounds, titanium compounds, palladium compounds, tantalum compounds, rhodium compounds, ruthenium compounds, or a combination thereof. At this time, the thickness of the coating layer is formed within 5㎛ to prevent the occurrence of wear, and to prevent the desorption of the coating layer by the droplets of the electrode surface.

The power supply unit 400 is driven by a control board. And it is provided with a control pad or an operation button for driving the power supply 400 separately. In addition, in order to solve the problem of erosion of the electrodes (311, 312) it can be driven to alternate the direction of the current through the control board.

In a specific embodiment of the present invention, it has been described that a pair of electrodes 311 and 312 are provided. However, the present invention is not limited thereto and may be constituted by one or more pairs of electrodes according to design conditions and water treatment processes.

Hereinafter will be described in detail the operation of the specific embodiment of the present invention having the configuration as described above.

The action of the active radical generating device 310 according to the specific embodiment of the present invention is explained by Bubble Mechanism.

First, the DC voltage Vd supplied from the power supply unit 400 is applied to the pair of electrodes 311 and 312. That is, the power supply unit 400 applies cathode power to the cathode electrode 312 and anode power to the anode electrode 311. At this time, the positive electrode 311 and the negative electrode 312 are submerged in water in a state spaced apart from each other at intervals of d (mm), the electric field is formed when the voltage Vd is applied by the power supply 400. .

If the electric field formed exceeds the threshold of the Avalanche mechanism, the ionized impurities at the electrode points, the OH ?? Etc. form a key generation site in the cell region of the cathode electrode 312.

Next, an extremely high electric field region is formed locally, which causes local heating to form fine bubbles as the water molecules evaporate. The fine bubbles extend from the cathode electrode 312 in the direction of the anode electrode 311 to form an electrically conductive path between the two electrodes 311 and 312.

Subsequently, water molecules are decomposed by the conduction path of electricity formed between the two electrodes 311 and 312 so that the O ? , OH ?? , O 3 ?? Fungicides and oxidants such as HOCl and H 2 O 2 are produced.

Microorganisms present in water are inactivated or removed by the oxidant produced. That is, bacteria are removed by electrosorption, and other microorganisms e . It is removed by direct electrolysis by reaction with.

By this reaction, it is possible to suppress and remove the generation of microorganisms and bacteria in the clarification container 210, and while the electrolysis reaction proceeds, the chlorine, ozone, OH as well as the reaction of the direct oxidation of the bacteria and microorganisms contained in the water Various active radicals, such as radicals and oxygen radicals, are generated to indirectly oxidize and sterilize the reaction simultaneously, thus contaminating with sterilized water including active radicals in the primary reactor 220 and the secondary reactor 230. Purifies contaminated gas and liquid because gas and liquid come into contact with each other to sterilize and deodorize by direct and indirect oxidation.

 Sterilization water having such a function and contaminated gas or liquid induce a constant flow through the primary reaction space 221, the connecting pipe 222, and the secondary reaction space 231, and contact with the sterilizing water and reaction time Was increased for sterilization and deodorization.

The rights of the present invention are not limited to the embodiments described above, but are defined by the claims, and those skilled in the art can make various modifications and adaptations within the scope of the claims. It is self-evident.

1 is a block diagram showing a schematic configuration of a purification vessel having an active radical generator according to a specific embodiment of the present invention.

2 is a plan view showing a pair of electrodes constituting a specific embodiment of the present invention.

Figure 3 is a schematic exploded view of parts of the purification vessel having an active radical generating device according to a specific embodiment of the present invention.

* Description of the symbols for the main parts of the drawings *

100: upper lid 150: power connection

210: purifier

211: inlet pipe 212: outlet pipe

220: first reactor 221: first reaction space

222: connector 223: hole

224: lower passage

230: secondary reactor 231: secondary reaction space

310: active radical generator

311: upper electrode 312: lower electrode

313: electrode bolt

315: hole 317: support member

400: power supply

Claims (9)

In the purification tank 210 having the active radical generator 310, Purification container 210 is configured to enter the contaminated gas or liquid into the inlet pipe 211 to the outlet pipe 212, and It is inserted into the lower portion of the primary reactor 220 in which the water treatment process proceeds, the power is supplied to at least one pair of electrodes including the upper electrode 311 and the lower electrode 312 and to maintain the predetermined interval and the pair of electrodes In the purifying container 210 having an active radical generating device 310, characterized in that configured to be connected to the power supply unit 400 for applying a The active radical generator is selected from the group consisting of carbon, titanium nitride (titanium nitride), ceramics, tantalum, nickel, tin, palladium, rhodium, ruthenium, or a combination thereof. It is configured to include a purifying tank 210 having a. The method of claim 1, The purifying tank 210 is the inlet pipe 211 and the outlet pipe 212 is configured in the upper lid 100 and there are many holes in the outer wall of the primary reactor 220 there is a sterilized water upwards by micro bubbles And flows to the secondary reactor 230 through the holes of the primary reactor 220 and flows below the lower electrode 312 in the pair of upper and lower electrodes 311 and 312. Create a space in the part to induce a smooth flow of sterilized water from the secondary reactor 230 to the primary reactor 220 to complete a large circulation, so as to be similar to the flow direction of the sterilized water generated from a pair of electrodes Purification tank equipped with an active radical generator, characterized in that the two reactors arranged. The method of claim 1, The primary reaction space in which the primary contact and reaction takes place in the dual structure purification vessel 210 and the dual structure purification vessel 210 so that the introduced gas or fluid is in natural contact and reaction with the sterilizing water generating active radicals ( Primary reactor 220 having a 221 and a connector 222 connecting the primary reactor 220 and the secondary reactor 230 and an outlet 180 degrees opposite the connector 222 The dual structure of the secondary reactor 230 having a secondary reaction space 231 in which the secondary contact and reaction takes place while turning left and right along the outer wall of the primary reactor 220 in the direction of the tube 212 Purification tank provided with an active radical generator, characterized in that. The method of claim 1, A coating layer is formed on part or all of the surface of the electrode, and a component of the coating layer is composed of a platinum compound, an iridium compound, a tin compound, a titanium compound, a palladium compound, a tantalum compound, a rhodium compound, a ruthenium compound, or a combination thereof. Purification tank with an active radical generator, characterized in that selected from. The method of claim 2 The thickness of the coating layer of the electrode is in the range of 1 to 5㎛, the interval between the pair of electrodes is in the range of 0.9 to 1.1mm purification tank with an active radical generator. The method of claim 2 The shape of the electrode is one and the 90 degree rotation is mounted so as to face each other, and the purifying tank with an active radical generator characterized in that the shape of the support member and the structure of the electrode for this. The method according to any one of claims 1 to 5. Wherein the electrode is a purifying tank with an active radical generator, characterized in that any one of the form of a plate-like, mesh-shaped, cylindrical having a plurality of holes. The method according to any one of claims 1 to 5. And the power supply unit applies any one of a DC voltage, a pulse voltage, a square wave pulse voltage, a time division control pulse voltage, and an alternating pulse voltage to the pair of electrodes. The method of claim 8 The power supply unit is a purifying tank with an active radical generator, characterized in that it comprises a control panel or an operation button for applying power to the pair of electrodes.
KR1020090073363A 2009-08-10 2009-08-10 Purification bottle with active radical generator KR20110015914A (en)

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Application Number Priority Date Filing Date Title
KR1020090073363A KR20110015914A (en) 2009-08-10 2009-08-10 Purification bottle with active radical generator

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Application Number Priority Date Filing Date Title
KR1020090073363A KR20110015914A (en) 2009-08-10 2009-08-10 Purification bottle with active radical generator

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KR20110015914A true KR20110015914A (en) 2011-02-17

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KR1020090073363A KR20110015914A (en) 2009-08-10 2009-08-10 Purification bottle with active radical generator

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