KR20220049160A - Continuous electric discharge water generation system - Google Patents

Abstract

The present invention relates to a continuous electric discharge water generation system. The continuous electric discharge water generation system of the present invention includes: a gas supply unit (100) that supplies gas; a plurality of plasma gas generation units (200) that generate plasma gas by receiving the gas from the gas supply unit and are connected in series; a water supply unit (300) that supplies water; and a water tank (400) that receive the plasma gas from the plasma gas generation unit (200) and receives the water from the water supply unit (300) to generate electric discharge water by dissolving the plasma gas in the water. According to the present invention, it is possible to sufficiently increase the concentration of a NO group.

Description

Continuous electric discharge water generation system

The present invention relates to a continuous electric discharge water generating system.

Recently, consumers' interest in fresh agricultural products is increasing, and according to this trend, interest in cleanliness and sanitary management of agricultural products is also rapidly increasing. Therefore, various studies are being conducted on methods for washing while controlling harmful microorganisms in agricultural products and minimizing residual pesticides.

Currently, chlorine disinfection is mainly used as a method of washing agricultural products, but there is a risk of discoloration if washing is incomplete or the concentration is not appropriate after treatment, and there is also a problem that residual chlorine is toxic. Therefore, in order to replace chlorine disinfection, it is confirmed that the possibility of using ozone water is large.

As disclosed in the patent documents of the following prior art documents, research and development of a method for manufacturing washing water containing ozone is continuously being made. In particular, research is being conducted on a method of producing washing water by generating ozone using a plasma generator. However, the method for producing washing water containing ozone according to the prior art has a limit in maintaining the concentration of NO groups constant or increasing the concentration as necessary.

KR 10-2012-0052524 A

The present invention is to solve the problems of the prior art described above, and one aspect of the present invention is to have a homeostasis to maintain the NO group concentration at a certain concentration or to sufficiently increase it by providing a plurality of plasma gas generating means or water tanks. It relates to a continuous electric discharge water generating system.

The continuous electric discharge water generating system according to an embodiment of the present invention comprises a gas supply means for supplying gas, a plasma gas generator by receiving gas supplied from the gas supply means, a plurality of plasma gas generators connected in series, and water. a water supply unit for supplying the water; and a water tank receiving plasma gas from the plasma gas generating unit, receiving water from the water supply unit, and dissolving the plasma gas in water to generate electric discharge water.

A continuous electric discharge water generating system according to an embodiment of the present invention includes a gas supply means for supplying a gas, a plasma gas generator by receiving gas supplied from the gas supply means, a plurality of plasma gas generator means, and water supply. a water supply means, and a plurality of them are connected in series, receive water from the water supply means and are sequentially delivered to each, and receive plasma gas from each of the plasma gas generating means, respectively, to supply plasma gas to the water and a water tank for dissolving and generating electric discharge water.

In addition, in the continuous electric discharge water generating system according to an embodiment of the present invention, the plurality of water tanks are sequentially connected by a connecting pipe, and the diameter of the connecting pipe is smaller than the diameter of the water tank.

In addition, in the continuous electric discharge water generating system according to the embodiment of the present invention, the gas supply means is an air pump (air pump).

In addition, in the continuous electric discharge water generating system according to an embodiment of the present invention, the cooling means provided in the water tank to lower the temperature of the water tank further includes.

In addition, in the continuous electric discharge water generating system according to an embodiment of the present invention, the cooling means includes a cooling pipe extending helically in the longitudinal direction of the water tank and the cooling water flowing therein.

In addition, in the continuous electric discharge water generating system according to an embodiment of the present invention, the filter unit for receiving the plasma gas that is not dissolved in water from the water tank to remove moisture or ozone is further included.

In addition, in the continuous electric discharge water generating system according to an embodiment of the present invention, the filter unit includes a silica filter that removes moisture and a manganese filter that removes ozone.

In addition, in the continuous electric discharge water generation system according to an embodiment of the present invention, the water supply means includes a first circulation water tank that receives and stores water and supplies water to the water tank, and the electric discharge water from the water tank. a second circulation water tank for receiving and storing, and discharging the electric discharge water to the outside, and a transfer pipe for transferring the electric discharge water from the second circulation water tank to the first circulation water tank, from the second circulation water tank The electric discharge water transferred to the first circulation water tank is supplied to the water tank.

In addition, in the continuous electric discharge water generating system according to an embodiment of the present invention, the water supply means further includes an auxiliary plasma gas generator for supplying the plasma gas to the second circulation water tank.

The features and advantages of the present invention will become more apparent from the following detailed description taken in conjunction with the accompanying drawings.

Prior to this, the terms or words used in the present specification and claims should not be construed in a conventional and dictionary meaning, and the inventor may properly define the concept of the term to describe his invention in the best way. Based on the principle that there is, it should be interpreted as meaning and concept consistent with the technical idea of the present invention.

According to the present invention, there is an advantage in that the concentration of NO group and the like can be sufficiently increased by providing a plurality of plasma gas generating means or water tanks.

1 is a perspective view of a continuous electric discharge water generating system according to a first embodiment of the present invention;
2 to 3 are graphs showing the dissolved NO group concentration according to the number of plasma gas generating means connected in series;
4 is a graph showing the concentration of dissolved NO groups according to time in the experimental water tanks at 10 ° C and 15 ° C;
5 is a perspective view of a continuous electric discharge water generating system according to a second embodiment of the present invention;
6 is a graph showing the concentration of dissolved NO groups when four water tanks and a static mixer are connected in series;
7 is a perspective view of a continuous electric discharge water generating system according to a third embodiment of the present invention.

The objects, specific advantages and novel features of the present invention will become more apparent from the following detailed description taken in conjunction with the accompanying drawings and preferred embodiments. In the present specification, in adding reference numbers to the components of each drawing, it should be noted that only the same components are given the same number as possible even though they are indicated on different drawings. Also, terms such as “first” and “second” are used to distinguish one component from another, and the component is not limited by the terms. Hereinafter, in describing the present invention, detailed descriptions of related known technologies that may unnecessarily obscure the gist of the present invention will be omitted.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

1 is a perspective view of a continuous electric discharge water generating system according to a first embodiment of the present invention.

As shown in Fig. 1, the continuous electric discharge water generating system according to this embodiment generates plasma gas by receiving gas from a gas supplying means 100 for supplying a gas, a gas supplying means 100, and a plurality of The dog is supplied with plasma gas from the plasma gas generating means 200 connected in series, the water supplying means 300 for supplying water, and the plasma gas generating means 200, and water is supplied from the water supplying means 300, and a water tank 400 for generating electric discharge water by dissolving plasma gas in water.

The gas supply means 100 serves to continuously supply gas to the plasma gas generator 200 , and may supply air or oxygen to the plasma gas generator 200 . Here, the gas supply means 100 is not particularly limited, but may be an air pump or an air compressor. In this case, the gas supply means 100 may be, for example, a UF-1000GN of United (united). On the other hand, the flow rate at which the gas supply means 100 supplies gas is not particularly limited, but may be, for example, 8 to 12L/min, preferably 10L/min.

The plasma gas generating means 200 serves to generate plasma gas by receiving gas (air or oxygen) from the gas supply means 100 . Here, the plasma gas generating means 200 may be a plasma generator. At this time, the plasma generator is provided with an electrode plate based on aluminum (Al) and aluminum oxide (Al ₂ O ₃ ), and the air introduced into the microchannel passage between the electrode plates by the generated microplasma is converted into ozone or the like. For example, the plasma generator may be an MP1 Series 1001 manufactured by EP Purification. On the other hand, a plurality of plasma gas generating means 200 may be connected in series. That is, when one plasma gas generating means 200 generates plasma gas, it is supplied to the other plasma gas generating means 200, so that the other plasma gas generating means 200 can generate a higher concentration of plasma gas. there is. As a result, by connecting the plurality of plasma gas generating means 200 in series, the concentration of the plasma gas can be increased. In particular, it is possible to increase the concentration of NO groups in the plasma gas. For example, four plasma gas generating means 200 may be connected in series. That is, the plasma gas generating means 200 includes a first plasma gas generating means 200a, a second plasma gas generating means 200b, a third plasma gas generating means 200c, and a fourth plasma gas generating means 200d. may include, and they may be connected in series.

As described above, in order to confirm the effect of the plasma gas generating means 200 connected in series, while changing the number of plasma gas generating means 200 connected in series, it is dissolved in an experimental water tank containing 2.5L and 4L tap water. The dissolved NO group concentration was measured every 20 minutes up to a maximum of 60 minutes. At this time, 10L/min of air was constantly maintained in the plasma gas generating means 200 . As shown in FIG. 2 , when there is one or two plasma gas generating means 200 in the 2.5L experimental water tank, the NO group concentration is rather decreased, but the number of plasma gas generating means 200 connected in series increases. It can be seen that the concentration of NO group increases as When four plasma gas generating means 200 are connected in series compared to one, it can be seen that there is a difference of about two times based on 60 minutes of measurement time (one: 127 μM Vs. four: 248 μM). As shown in FIG. 3 , in the 4L experimental water tank, the NO concentration difference was more clearly confirmed according to the number of plasma gas generating means 200 . As the number of plasma gas generating means 200 increases, it can be seen that the NO group concentration increases by about 40 μM or more. When four plasma gas generating means 200 are connected in series compared to one, it can be seen that there is a difference of about 2.5 times based on 60 minutes of measurement time (one: 104 μM Vs. four: 242 μM).

After all, it can be clearly confirmed that the concentration of the dissolved NO group is increased even through an experiment when a plurality of plasma gas generating means 200 are provided and connected in series.

Meanwhile, the plasma gas generating means 200 may continuously supply the generated plasma gas to the water tank 400 through the plasma gas supply line 210 . In this case, the plasma gas supply line 210 is provided with an air flow meter 215 to measure the flow rate of the plasma gas supplied to the water tank 400 .

Additionally, in order to supply power to the plasma gas generating means 200, a rectifier 220, a rectifier, an IGBT-based power supply (230, power supply based on IGBT, including a function generator function), and a flyback power supply 240, flyback power supply) and the like may be provided. Here, the rectifier 220 serves to convert an externally applied AC voltage into a DC voltage using a diode and a capacitor. In addition, the IGBT-based power supply 230 performs the functions of the IGBT and the function converter at the same time to convert the rectified DC voltage into an AC voltage having an adjustable frequency and duty cycle. Then, the flyback power supply 240 receives the changed AC voltage from the IGBT-based power supply 230 and amplifies it to 3kV and supplies it to the plasma gas generating means 200 .

The water supply means 300 serves to continuously supply water to the water tank 400 . Here, the water supply means 300 may supply water to the water tank 400 through the water supply line 310 , and the water supply means 300 is not particularly limited, but may be, for example, a water pump. can

The water tank 400 receives plasma gas continuously from the plasma gas generating means 200 and continuously receives water from the water supply means 300 to dissolve the plasma gas in water to generate electric discharge water. carry out Specifically, plasma gas may be supplied to the water tank 400 through the plasma gas supply line 210 , and water may be supplied to the water tank 400 through the water supply line 310 . At this time, the plasma gas supply line 210 is connected to the lower side of the water tank 400 , and the plasma gas is supplied to the lower end of the water accommodated in the water tank 400 , so that it can be effectively dissolved in water. As such, when the plasma gas is dissolved in water, electric discharge water is generated, and the generated electric discharge water may be discharged through the outlet 405 provided at one side of the water tank 400 . Meanwhile, a bubble generator may be provided at the end of the plasma gas supply line 210 in order to supply the plasma gas to the tank 400 in the form of bubbles.

Additionally, a cooling means 420 provided in the water tank 400 to lower the temperature of the water tank 400 may be provided. The dissolution rate of plasma gas is different depending on the temperature of the water tank 400. In order to confirm this, the concentration of NO groups dissolved in the experimental water tank containing 4L of tap water maintained at 10°C and 15°C is set at 5 minute intervals up to 180 minutes. was repeated three times. As shown in FIG. 4 , it can be confirmed that the dissolution rate of the plasma gas at 10° C. is larger than the dissolution rate of the plasma gas at 15° C. The time to reach the saturation concentration for each temperature was after about 60 minutes at 10°C and after about 90 minutes at 15°C. Therefore, in order to increase the dissolution rate of the plasma gas in the water tank 400, the temperature of the water tank 400 should be lowered. However, the plasma gas supplied from the plasma gas generating means 200 has a relatively high temperature, and by increasing the overall temperature of the water tank 400 , the dissolution rate of the plasma gas may be slowed. In particular, when a plurality of plasma gas generating means 200 are connected in series, the temperature of the plasma gas becomes higher, and there is a fear that the dissolution rate of the plasma gas becomes slower. To prevent this, a cooling means 420 is provided in the water tank 400 , and the water tank 400 maintains a relatively low temperature by the cooling means 420 , thereby increasing the dissolution rate of the plasma gas. Specifically, the cooling means 420 may include a cooling pipe 423 and a cooler 425 . Here, the cooling pipe 423 extends spirally in the longitudinal direction of the water tank 400 , and the cooling water flows therein. In this way, since the cooling tube 423 extends spirally, it is possible to uniformly cool the water tank 400 . In addition, the cooler 425 is to circulate the cooling water inside the cooling tube 423, for example, LK lab's "Circulating Water Bath" product can be used.

Meanwhile, a data logger 430 capable of measuring and recording the temperature of the water tank 400 may be connected to the water tank 400 . Accordingly, the temperature of the water tank 400 may be detected through the data logger 430 , and the temperature of the water tank 400 may be adjusted through the cooling means 420 . In this case, the data logger 430 is not particularly limited, but Agilent's "34970A" product may be used. In addition, a dissolved ozone meter for measuring the ozone concentration of the generated electric discharge water may be connected to the water tank 400 . In this case, the dissolved ozone meter is not particularly limited, but TOA-DKK's "OZ-21P" product may be used.

In addition, the plasma gas not dissolved in water in the water tank 400 may be exhausted to the outside through the exhaust port 407 formed on one side of the water tank 400 . As such, the plasma gas exhausted without being dissolved in water is transferred from the water tank 400 to the filter unit 440 . Here, the filter unit 440 may receive the plasma gas to remove moisture or ozone. Specifically, the filter unit 440 may include a silica filter 443 for removing moisture and a manganese oxide filter 445 for removing ozone.

Referring to FIG. 1 , an operation process of the continuous electric discharge water generating system according to the present embodiment will be described.

First, when air or oxygen is supplied from the gas supplying means 100 to the plasma gas generating means 200 , the plasma gas generating means 200 generates plasma gas. At this time, a plurality of plasma gas generating means 200 may be connected in series to increase the dissolved NO group. The plasma gas generating means 200 continuously supplies the generated plasma gas to the water tank 400 through the plasma gas supply line 210 . In this case, the plasma gas supply line 210 is provided with a flow meter 215 to measure the flow rate of the plasma gas supplied to the water tank 400 . At the same time, the water supply means 300 continuously supplies water to the water tank 400 through the water supply line 310 .

As a result, plasma gas and water are continuously supplied to the water tank 400 , and the plasma gas is supplied in the form of bubbles through a bubble generator and dissolved in water, thereby generating electric discharge water. The dissolution rate of the plasma gas can be increased by maintaining the water tank 400 at a low temperature by the cooling means 420 while generating the electric discharge water in the water tank 400 . In this case, the temperature of the water tank 400 may be measured and recorded using the data logger 430 . The electric discharge water generated in the water tank 400 may be discharged to the outside through the outlet 405 .

Meanwhile, the plasma gas that is not dissolved in water in the water tank 400 may be transferred to the filter unit 440 through the exhaust port 407 to remove moisture and remove ozone.

5 is a perspective view of a continuous electric discharge water generating system according to a second embodiment of the present invention.

As shown in FIG. 5 , the continuous electric discharge water generating system according to the present embodiment includes most of the same configuration as the continuous electric discharge water generating system according to the first embodiment, but the plasma gas generating means 200 . and the water tank 400 are different. Therefore, in the continuous electric discharge water generating system according to the present embodiment, overlapping contents with the continuous electric discharge water generating system according to the first embodiment are omitted, and the plasma gas generating means 200 and the water tank 400 are mainly used. to be described as

The plasma gas generating means 200 serves to generate plasma gas by receiving gas (air or oxygen) from the gas supplying means 100 , and a plurality of plasma gas generating means 200 are provided. The plurality of plasma gas generating means 200 are respectively connected to the plurality of water tanks 400 . That is, each of the plasma gas generating means 200 is connected to each of the tanks 400 , and each of the plasma gas generating means 200 supplies the plasma gas to each of the tanks 400 . Meanwhile, the plurality of plasma gas generating means 200 may receive gas from one gas supplying means 100 .

The water tank 400 receives plasma gas continuously from the plasma gas generating means 200 and continuously receives water from the water supply means 300 to dissolve the plasma gas in water to generate electric discharge water. carry out Here, the plurality of water tanks 400 are connected in series, receive water from the water supply means 300 and sequentially deliver to each, and each water tank 400 is plasma from each plasma gas generating means 200 . The gas is supplied and the plasma gas is dissolved in water to generate electric discharge water. That is, when water and plasma gas are supplied from one tank 400 to generate electric discharge water, it is supplied to the other water tank 400 to dissolve the plasma gas again, thereby sequentially generating higher concentration of electric discharge water. can As a result, the concentration of the electric discharge water can be increased by connecting the plurality of water tanks 400 in series and supplying the plasma gas to the plasma gas generating means 200 to each of the water tanks 400 . In particular, it is possible to increase the concentration of NO groups in the electric discharge water. For example, four water tanks 400 may be connected in series, and four plasma gas generating means 200 may be respectively connected to the four water tanks 400 . That is, the water tank 400 includes a first water tank 400a, a second water tank 400b, a third water tank 400c, and a fourth water tank 400d, and the plasma gas generating means 200 is a first plasma. It may include a gas generating means 200a, a second plasma gas generating means 200b, a third plasma gas generating means 200c, and a fourth plasma gas generating means 200d. At this time, the first water tank 400a, the second water tank 400b, the third water tank 400c, and the fourth water tank 400d are connected in series, and the first plasma gas generating means ( 200a) is connected, the second plasma gas generating means 200b is connected to the second water tank 400b, the third plasma gas generating means 200c is connected to the third water tank 400c, and the fourth water tank ( The fourth plasma gas generating means 200d may be connected to 400d). Accordingly, the concentration of the electric discharge water may be sequentially increased while passing through the first water tank 400a -> the second water tank 400b -> the third water tank 400c -> the fourth water tank 400d.

As described above, in order to confirm the effect of the water tank 400 connected in series, four water tanks 400 connected in series (the plasma gas generating means 200 is connected to each water tank 400) and a static mixer When 60 L of electric discharge water was generated using a (static mixer), the dissolved NO group concentration of the electric discharge water was measured. As shown in FIG. 6 , it can be seen that when four tanks 400 connected in series are used, about 8 μM is higher than when a static mixer is used (four tanks: 78 μM Vs. Static mixer: 70 μM). As a result, when four tanks 400 connected in series are used according to the present embodiment, it is possible to generate electric discharge water at a level exceeding that of a currently commercialized and used static mixer.

On the other hand, the plurality of water tanks 400 may be sequentially connected in series by the connection pipe (410). For example, between the first water tank 400a and the second water tank 400b, between the second water tank 400b and the third water tank 400c, and between the third water tank 400c and the fourth water tank 400d Each may be connected by a connector 410 . In this case, the diameter of the connection pipe 410 may be smaller than the diameter of the water tank 400 . Accordingly, as the electric discharge water passes through the connecting pipe 410 with a relatively small diameter, the pressure of the fluid instantly drops and the flow rate increases, so that the plasma gas is bubbled into a small size, so that the dissolution can proceed more easily and quickly.

More specifically, the connection pipe 410 may be connected to the upper side of one water tank 400 and the lower side of the next water tank 400 , and the plasma gas supply line 210 may be connected to the lower side of the water tank 400 . Therefore, after the plasma gas is dissolved in water in one water tank 400 to generate electric discharge water, the electric discharge water is transferred to the lower side of the next water tank 400, and the plasma gas supplied to the lower side of the next water tank 400 is By further dissolving in the electric discharge water, the concentration of the electric discharge water can be continuously increased.

7 is a perspective view of a continuous electric discharge water generating system according to a third embodiment of the present invention.

As shown in FIG. 7 , the continuous electric discharge water generating system according to the present embodiment includes most of the same configuration as the continuous electric discharge water generating system according to the second embodiment, but the water supply means 300 is different Accordingly, in the continuous electric discharge water generating system according to the present embodiment, content overlapping with the continuous electric discharge water generating system according to the second embodiment will be omitted, and the water supply means 300 will be mainly described.

The water supply means 300 serves to continuously supply water to the water tank 400 and to circulate the electric discharge water generated in the water tank 400 . Here, the water supply means 300 may include a first circulation water tank 320 , a second circulation water tank 330 , a transfer pipe 340 , a water pump 345 , and the like. Specifically, the first circulation water tank 320 receives water and stores a certain amount, supplies water to the water tank 400 through the water pump 345 , and the second circulation water tank 330 is supplied from the water tank 400 . It receives the electric discharge water, stores a certain amount, and discharges the electric discharge water to the outside. That is, the first circulation water tank 320 stores water and supplies water to the water tank 400 , and the second circulation water tank 330 stores the electric discharge water and discharges it to the outside. However, the first circulation water tank 320 and the second circulation water tank 330 are connected by a transfer pipe 340 , and the electric discharge water may be transferred from the second circulation water tank 330 to the first circulation water tank 320 . (When the level of the electric discharge water in the second circulation water tank 330 is equal to or higher than a predetermined value, it may be transferred to the first circulation water tank 320). As described above, the electric discharge water transferred from the second circulation water tank 330 to the first circulation water tank 320 is again supplied to the water tank 400 to dissolve the plasma gas, so that the concentration of the electric discharge water can be further increased. By continuously circulating the electric discharge water through the first circulation water tank 320 , the second circulation water tank 330 , and the connection pipe 410 , the dissolution time is sufficiently secured and the plasma gas is continuously supplied, and the electric discharge water concentration can be increased.

In fact, the concentration of dissolved NO groups in the electric discharge water was measured every 20 minutes up to 60 minutes, and as a result, it was measured to be 82 μM at 20 minutes, 86 μM at 40 minutes, and 92 μM at 60 minutes. Through these results, it can be clearly confirmed that the concentration of dissolved NO groups in the electric discharge water increases when the electric discharge water is circulated.

Additionally, the water supply means 300 may include an auxiliary plasma gas generator 350 . Here, the auxiliary plasma gas generating means 350 is connected to the second circulation water tank 330 to supply the plasma gas to the second circulation water tank 330 . Accordingly, the plasma gas generated by the auxiliary plasma gas generating means 350 is additionally supplied to the electric discharge water stored in or circulating in the second circulation water tank 330 , thereby further increasing the concentration of the electric discharge water. On the other hand, an auxiliary gas supply means 360 for supplying gas (air or oxygen) to the auxiliary plasma gas generating means 350 may be additionally provided.

For reference, in the continuous electric discharge water generating system according to the second and third embodiments of the present invention, the flow meter, rectifier, IGBT-based power supply, and fly of the continuous electric discharge water generating system according to the first embodiment of the present invention Although the back power supply, data logger, filter unit (silica filter, manganese filter), etc. are not shown (refer to FIGS. 5 and 7), the configurations are continuous electric discharge water according to the second and third embodiments of the present invention Of course, the same can be applied to the generation system.

Although the present invention has been described in detail through specific examples, it is intended to describe the present invention in detail, and the present invention is not limited thereto. It is clear that the modification or improvement is possible.

All simple modifications or changes of the present invention fall within the scope of the present invention, and the specific scope of protection of the present invention will be made clear by the appended claims.

100: gas supply means 200: plasma gas generating means
200a-d: first to fourth plasma gas generating means
210: plasma gas supply line 215: flow meter
220: rectifier 230: IGBT based power supply
240: flyback power supply 300: water supply means
310: water supply line 320: first circulation water tank
330: second circulation water tank 340: transfer pipe
350: auxiliary plasma gas generating means 360: auxiliary gas supply means
400: water tank 400a-d: first to fourth water tanks
405: exhaust port 407: exhaust port
410: connector 420: cooling means
423: cooling tube 425: cooler
430: data logger 440: filter unit
443: silica filter 445: manganese filter

Claims (10)

gas supply means for supplying gas;
Plasma gas generating means receiving the gas from the gas supply means to generate plasma gas, a plurality of plasma gas generating means connected in series;
water supply means for supplying water; and
a water tank receiving plasma gas from the plasma gas generating means, receiving water from the water supplying means, and dissolving the plasma gas in water to generate electric discharge water;
A continuous electric discharge water generating system comprising a.
gas supply means for supplying gas;
Plasma gas generating means provided with a plurality of generating plasma gas by receiving the gas from the gas supply means;
water supply means for supplying water; and
A plurality of them are connected in series, receive water from the water supply means and are sequentially delivered to each, each receive plasma gas from each of the plasma gas generating means, dissolve the plasma gas in water to generate electric discharge water generating tank;
A continuous electric discharge water generating system comprising a.
3. The method according to claim 2,
A plurality of the water tanks are sequentially connected by a connecting pipe, and the diameter of the connecting pipe is smaller than the diameter of the water tank.
The method according to claim 1 or 2,
The gas supply means is an air pump (air pump) continuous electric discharge water generating system.
The method according to claim 1 or 2,
a cooling means provided in the water tank to lower the temperature of the water tank;
A continuous electric discharge water generating system further comprising a.
6. The method of claim 5,
The cooling means,
a cooling pipe extending spirally in the longitudinal direction of the water tank and through which cooling water flows;
A continuous electric discharge water generating system comprising a.
The method according to claim 1 or 2,
a filter unit that receives plasma gas that is not dissolved in water from the water tank and removes moisture or ozone;
A continuous electric discharge water generating system further comprising a.
8. The method of claim 7,
The filter unit,
Silica filter to remove moisture; and
Manganese filter to remove ozone;
A continuous electric discharge water generating system comprising a.
The method according to claim 1 or 2,
The water supply means,
a first circulation water tank receiving and storing water and supplying water to the water tank;
a second circulation water tank receiving and storing the electric discharge water from the water tank; and
a transfer pipe for transferring the electric discharge water from the second circulation water tank to the first circulation water tank;
including,
The electric discharge water transferred from the second circulation water tank to the first circulation water tank is supplied to the water tank.
10. The method of claim 9,
The water supply means,
auxiliary plasma gas generating means for supplying plasma gas to the second circulation water tank;
A continuous electric discharge water generating system further comprising a.

Images