KR20190079270A - System of purifying rain using ozone - Google Patents

Abstract

A system for purifying rainwater by using ozone according to the present invention comprises: a rainwater intake device for intaking rainwater; a rainwater purification device for physically purifying rainwater supplied from the rainwater intake device; an ozone water purification device for sterilizing the rainwater physically purified in the rainwater purification device by using ozone; and a storage water supply device for supplying storage water stored in a separate storage space to the rainwater purification device, wherein the ozone water purification device includes a housing forming an appearance; a cluster separation unit for separating a cluster of water introduced by a pump by an electric field; a backflow prevention unit for introducing ozone gas from an ozone generator and preventing backflow of raw water; a gas-liquid mixing unit for mixing water which has passed through the cluster separation unit with the ozone gas which is introduced through the backflow prevention unit; and a gas-liquid mixing line mixing device for promoting mixing of the ozone gas and supplying mixed water which has passed through the gas-liquid mixing unit. Thus, according to the present invention, it is possible to purify rainwater by using ozone, minimize excess ozone gas, and maximize the solubility of ozone water, thereby purifying rainwater by using ozone to the extent to be drunk.

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to an ozone purification system using Information and Communications Technologies (ICT)

The present invention relates to a system for purifying stormwater, and more particularly to a system for purifying stormwater using ozone.

Ozone is a highly potent antimicrobial substance that can be usefully used in the food industry by inactivating microorganisms through oxidation and decomposing into harmless oxygen.

Ozone has high oxidizing power after fluorine and has high reactivity with organic and inorganic materials and has a sterilizing, deodorizing and decolorizing effect, so that microorganisms are killed much faster than chlorine, there is no need to adjust the pH during the treatment and ozone sterilization This method is more inexpensive than other processing methods, and can be sterilized not only on the surface of the food but also on the surface of the food.

Despite the function of ozone water, ozone has a microbial sterilization effect, and even when the concentration of ozone gas is 0.1 ppm, irritating nose and throat, and toxicity that can cause headache at 1 ppm, It is because the ozone generator should be equipped with an ozone gas decomposition device and a lid of ozone water washing tank so that the concentration of ozone gas in the workplace increases.

For this reason, technologies for converting ozone gas into ozonated water and using it in domestic and industrial facilities have been developed.

However, according to the existing ozonated water production method, the dissolution rate is only about 7 to 30%, so that a lot of surplus ozone gas is generated and unnecessary human and other substances are adversely affected due to strong oxidizing power of ozone .

On the other hand, there is a case where the development is not progressed and the rainwater is gathered and used as the drinking water as it is in the area where the drinking water is lacking. If the uncleaned rainwater is consumed, it may be exposed to various bacterial diseases, The factor is increasing.

In addition, although the ozonated water system requires proper management at an appropriate time, there is a limit to the management of the ozonated water system because the manager can not reside when the facility is installed at a remote place.

The present invention has been devised to solve the problems described above. The present invention is to purify ozone by using ozone, and by applying ICT (Information and Communications Technologies) technology, it is possible to check the operation state of equipment even at a long distance, The notification function is activated, the drinking can be stopped immediately, the action can be taken, and the ozone gas can be minimized and the ozone water dissolution rate can be maximized to provide an excellent purification system capable of purifying the ozone to such an extent that the ozone can be consumed. It has its purpose.

The excellent purification system using ozone according to the present invention is characterized in that it comprises an excellent water intake apparatus for taking rainwater, an excellent purification apparatus for physically purifying storm water supplied from the above excellent water intake apparatus, An ozone water purifying device for sterilizing the ozone water by using ozone, and a storage water supplying device for supplying the storage water stored in a separate storage space to the ozonized water purifying device, wherein the ozonated water purifying device comprises: A cluster separating unit for separating clusters of water introduced by the pump by an electric field, a reverse flow preventing unit for introducing ozone gas from the ozone generator and preventing reverse flow of raw water, water passing through the cluster separating unit, A gas-liquid mixing section for mixing the incoming ozone gas and a gas- One can mix and a liquid mixture line for supplying the mix apparatus to promote the mixing of the ozone gas.

The gas-liquid mixed line mixer includes a cylindrical housing and a plurality of mixing members inserted into the central axis of the cylindrical housing, wherein the mixing member includes a perforated plate and a vane member.

The perforated plate includes a symmetrical perforated plate having symmetrical holes formed in the disk, and an asymmetric perforated plate having holes formed asymmetrically in the disk.

Here, the vane member is a flex vane having a plurality of blades and including a flat vane or a straight vane or a round vane type blade.

Further, the vane member is disposed at the rear end of the perforated plate.

The gas-liquid mixing unit may include a supply unit for supplying a mixture of water and ozone gas, a main body for forming an outer shape, a first jetting unit disposed in the main body, for supplying and discharging the mixture from the supply unit, A bubble generating unit for generating bubbles by spraying the mixture at a first spraying unit; and a spraying unit for spraying the mixed water, which is generated through the foam generating unit, into the mixed water and the converted mixed water to the inner surface of the main body, And a discharge unit for discharging mixed water sprayed through the second spray unit to the main body, wherein the foam is converted into bubbles through the foam generating unit, and the contact area To increase the amount of dissolved gas.

The ozonated water purification apparatus may further include a plurality of sensors and a separate database for storing data collected from the plurality of sensors, wherein measurement data can be transmitted remotely by the plurality of sensors.

According to the present invention,

First, the stormwater can be used for drinking by cleansing stormwater by high concentration ozone water.

Secondly, it is possible to utilize the surface water and the groundwater in addition to excellent quality by purifying them.

Third, purification efficacy can be further improved by eliminating initial storms.

Fourth, the excellent purification system is modularized so that the storm collected from the roof can be purified, which is efficient.

Fifth, since the modularized stormwater purification system is composed of a folding solar panel, it can be used in a narrow space and can be operated by a solar panel.

Sixth, it can monitor and control the necessity of maintenance in remote place by real-time monitoring and control of the purification process and facilities status of the storm, so that the replacement period notification due to differential pressure of filter, normal operation of ozonizer, , It is possible to make the quality of water quality maintenance free, such as real-time measurement of ozone water concentration through mounting, change of raw water and treated water through electric conductivity and temperature sensor.

BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 shows an exemplary purification system in accordance with the present invention.
FIG. 2 shows an ozonated water purification apparatus of an excellent purification system according to the present invention.
FIG. 3 is a schematic view showing the internal structure of the ozonated water purification apparatus according to the present invention.
FIG. 4 is a bottom view of the ozonated water purification apparatus according to the present invention.
FIGS. 5 to 16 show another configuration of the ozonated water purification apparatus according to the present invention.
17 is a schematic view of a solar cell canopy device according to the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described more specifically with reference to the accompanying drawings, but the description of the already known techniques will be omitted.

FIG. 1 shows an excellent purification system using ozone according to the present invention. Referring to FIG. 1, the excellent purification system using ozone according to the present invention includes an excellent water intake apparatus 20, an excellent purification apparatus 30, a stored water supply apparatus 40, and an ozonated water purification apparatus 10.

The storm water intake system is a system for taking rainwater. The system is constructed in an area where the water supply facility is insufficient, so that the stormwater can be taken by the storm water intake system to clean the stormwater to enable drinking.

The storm water intake system is equipped to receive stormwater, and supplies the stormwater stormwater to the stormwater purification system.

The stormwater purification apparatus 30 is divided into a filtering tank 31 and a storage tank 32 to physically purify storm water.

The filtering tank 31 allows the contaminants contained in the storm to be filtered by the plurality of screens, and the thus filtered storm is stored in the storage tank 32.

After storing a predetermined amount or more of the rainwater stored in the reservoir 32, the rainwater is supplied to the ozonated water purifier 10 according to the operation of the pump or the like, and is chemically purified by ozone in the ozonated water purifier 10 to be used.

The storage water supply device 40 stores the surface water, the ground water or the purified water and supplies the water to the storage tank 32 of the stormwater purification apparatus 30 in order to use the purified water by the ozonated water purification apparatus 10, Groundwater, groundwater, or water wells are stored.

By selectively operating it, complex and continuous supply of drinking water can be made possible.

3 is a schematic view showing the internal construction of the ozonated water purifying apparatus according to the present invention, and Fig. 4 is a sectional view of the ozonated water purifying apparatus according to the present invention, FIG.

2 to 4, an ozonated water purification apparatus 10 according to an embodiment of the present invention includes a housing H, an ozone generator O, a filtering unit 100, a cluster separation unit 200, a pump P, Liquid mixing unit 300, a backflow prevention unit, a gas-liquid mixing line mixer, a ozone treatment unit 160, and a control unit C, and the like.

The housing H forms an outer appearance and includes a filtering unit 100, a cluster separating unit 200, a pump P, a gas-liquid mixing unit 300, a backflow preventing unit, a gas-liquid mixing line mixer, And an operation switch S is provided on the outside.

The ozone generator O is a structure for supplying ozone gas into the housing H in a configuration for generating ozone gas.

The filtering unit 100 contained in the housing H may be provided in a plurality of ways. In order to purify the wastewater, the inflow water may pass through the filtering unit 100. In an environment in which purified water is introduced, .

The pump P operates in accordance with the signal of the controller C under the control of the operation switch S to draw water and supply it to the gas-liquid mixer 300. The cluster separator 200 has a gas- (300), and reduces the cluster unit of water supplied.

Water is formed by a large number of water molecules forming clusters. Studies have shown that as the cluster size gets smaller, the water tastes better, and the solubility, osmolality, and vitality become better. In this work, water is not simply combined with ozone gas, but the clusters are reduced by the cluster separator, and the intensity of the electric field in contact with the water and the contact time are maximized to change the inherent physical properties such as minerals contained in the water And maximize the function of ozone water by increasing the solubility, metabolism, osmotic power, activation power and so on.

Referring to FIG. 5, the cluster separator includes a separator plate 210, a booster 220, an electrode bar 230, and the like.

The separation plate 210 is formed in a horizontal direction in the path of the water for forcing the strength of the electric field in contact with the water by forcing the path of the water flowing through the flow path.

The positive pole of the booster 220 is connected to the electrode rod 230 and the negative pole of the booster 220 is connected to the cluster separator to boost the common electricity 220V to a high voltage, It causes a classic badge. The electrode bar 230 is composed of a stainless steel bar to which the positive pole of the booster 220 is electrically connected, and a ceramic layer that surrounds the stainless steel bar. The electrode bar 230 is spaced apart from the inner surface of the cluster separator and is disposed so as not to be in contact with the separator plate 210. The electrode bar 230 may be formed in a simple bar shape, And has a substantially L-shaped or L-shaped or more bent shape.

The gas-liquid mixing unit 300 is configured to mix the ozone gas supplied from the ozone generator O and the water that has passed through the cluster separation unit 200 at a high concentration, and the ozone gas is supplied through the backflow prevention unit.

The backflow prevention portion includes the backflow prevention valve 410, the auxiliary backflow prevention unit 420, and the bypass means.

The check valve 410 is provided to prevent the raw water from flowing back to the supply pipe to which the gas is supplied. 6 and 7, but the present invention is not limited thereto.

The body 411 has a generally cylindrical outer shape with a stepped cylindrical shape and a receiving space 412 is formed in the upper end and a loading port 430 which is smaller in inner diameter than the receiving space 412 is connected to the receiving space 412 at the lower end .

A male thread is formed on the upper and lower parts of the body 411, and the lower part of the body 411 is threadedly engaged with the line through which the raw water passes.

The head portion 440 has a substantially cylindrical outer shape with an upper end opened and a lower portion formed with a female screw so as to be screwed on the upper portion of the body 411. A female screw is connected to the opening in the body 411 An inlet is formed. Accordingly, when the head part 440 is coupled to the body 411, the opening of the head part 440, the inlet port, the receiving space 412, and the inlet port 430 are connected in order.

Here, the cap 450 may be screwed to the upper end of the head part 440 so as to be connected to a supply pipe for supplying gas.

And includes a moving piece 460 and a spring 470 for opening and closing the inlet.

The moving piece 460 is formed to have a substantially hemispherical shape with an outer diameter corresponding to the inner diameter of the accommodation space 412 and a lower end formed to be smaller than the outer diameter of the upper end. One passage 460a is formed.

The moving piece 460 is inserted into the receiving space 412 and moves up and down.

Accordingly, when the moving piece 460 is inserted into the accommodation space 412, the inlet port and the inlet port 430 are connected to each other by the passage 460a formed in the moving piece 460. [

The spring 470 is fitted to the lower end of the moving piece 460 and inserted into the receiving space 412.

Accordingly, the spring 470 pushes the moving piece 460 upward, so that the moving piece 460 normally keeps the inlet port shut off.

Here, the moving piece 460 may be formed such that the surface area of the lower end is larger than the surface area of the upper end, and grooves are further formed at the lower end of the moving piece 460. When the raw water is filled in the receiving space 412 in a state where the moving piece 460 is in close contact with the inlet, the upper and lower sides of the moving piece 460 are pressure balanced. This is because the raw water is also filled in the upper part of the moving piece 460 through the passage 460a of the moving piece 460. At this time, since the surface area of the lower end of the moving piece 460 is larger than the upper surface area of the moving piece 460, the raw water pushes the moving piece 460 upward so that the moving piece 460 moves downward.

If the surface area of the upper end of the moving piece 460 is larger than the surface area of the lower end portion, the pressing force of the raw water lower than the force pushing the moving piece 460 upward becomes larger so that the moving piece 460 instantaneously moves downward The inlet may be opened instantaneously by movement.

However, in the present invention, since the surface area of the lower end of the moving piece 460 is larger than the surface area of the upper end, the force of pushing the raw material upward above the force of pushing the moving piece 460 downward is large.

Further, since the outer diameter of the moving piece 460 corresponds to the inner diameter of the receiving space 412, it is possible to prevent the moving piece 460 from flowing back and forth, right and left. Accordingly, even if an impact or vibration is applied from the outside, the moving piece 460 is prevented from flowing back and forth, right and left, thereby making it possible to firmly block the opening of the inlet.

6, the auxiliary backflow prevention unit 420 is connected to the ozone gas supply O to supply the gas to the backflow prevention valve 410, maintains the pressure of the supplied gas at a constant level The main body 421 and the buoyancy valve 422. The main body 421 and the buoyancy valve 422 serve to shut off the reverse flow of the raw water to the gas supply means.

The main body 421 has a substantially long tank having an internal space of a predetermined size formed therein and a gas inflow portion 423 through which gas is injected to be connected to the ozone gas supply O is provided at an upper end thereof, A gas supply part 424 is provided to be connected to the valve 410.

The main body 421 is provided with a raw water inflow portion 425 connected to a line at a lower end of the main body 421 so that raw water flows into the lower portion of the main body 421, An overflow portion 426 for discharging raw water out of the main body 421 is provided. Accordingly, due to the overflow portion, a certain range of pressure can be formed inside the main body 421, so that the gas can be supplied smoothly.

The buoyancy valve 422 is formed in a substantially spherical shape of a light material floating in water and inserted into the interior of the main body 421.

When the raw water flows into the lower end of the main body 421, the buoyancy valve 422 is lifted by the raw water. When a predetermined amount of raw water flows into the main body 421, the raw water is supplied through the overflow portion 426 And discharged out of the main body 421.

When the pressure of the raw water suddenly increases, the raw water rapidly rises to the inside of the main body 421, and the buoyancy valve 422 is brought into close contact with the upper end of the main body 421 to cut off the upper end of the main body 421. Therefore, by blocking the upper end of the main body 421, the buoyancy valve 422 can prevent the raw water from flowing back to the gas supply means.

If the pressure of the gas suddenly increases, the raw water is discharged out of the main body 421, the buoyancy valve 422 moves downward, and the gas can be discharged out of the main body 421 through the overflow portion 426 have. Accordingly, it is possible to prevent the inside of the main body 421 from being damaged due to the high pressure.

The overflow unit 426 uses a well-known technique, and a detailed description thereof will be omitted.

The bypass means includes a check valve 480 and a bypass valve 490 formed at the front end and the rear end of the check valve 410. In order to actively regulate the concentration and capacity of the ozonated water, the water is bypassed by shutting off the flow by a check valve (480) and forming a bypass pipe between the bypass valve (480).

9 to 13 show the gas-liquid mixing unit 300, wherein the gas-liquid mixing unit 300 mixes the introduced water and the ozone gas at a high concentration.

Liquid mixing unit 300 includes a main body 310, a supply unit 320, a mixed aquatic function unit 330, a discharge unit 340, a bubble generation unit 350, a pressure measurement unit 360, a pressure reducing valve 370, .

The main body 310 has a substantially cylindrical shape with a closed upper end and a lower end, and a valve V is installed at the lower end to remove the residues therein.

The supply unit 320 includes a supply pipe 321, a pressurizing pump 322, and a flow control unit 323.

The supply pipe 321 is installed horizontally through the main body 310 and the body 331 to be described later in a substantially pipe shape. At this time, a valve (not shown) may be installed at the end of the supply pipe 321 to remove the pressure of the supply pipe 321 when the pressure of the supply pipe 321 rises above the allowable pressure.

The pressurizing pump 322 is connected to the supply pipe 321 and is disposed outside the body 331 and supplies a mixture of water and ozone gas to the supply pipe 321.

The flow rate regulator 323 is connected to the supply pipe 321 and is disposed between the pressurizing pump 322 and the main body 310 and adjusts the supply amount of the mixture and the injection pressure of the mixture.

The mixed aquatic function portion 330 includes a body 331, a foam generating portion 332, a first jetting portion 333, a perforated plate 334, a leg 335 and a second jetting portion 336.

The body 331 is formed in a substantially cylindrical shape having a closed upper end and a lower end and is smaller than the body 310 and is disposed inside the body 310. A leg 335 is provided between the lower end of the body 331 and the body 310, And is disposed in the middle of the inside of the main body 310.

The foam generating portion 332 is provided on the inner ceiling of the body 331 with a mesh M of a substantially cylindrical shape. A description thereof will be described later.

Here, the foam generating unit 332 may be a perforated plate (not shown), which uses the mesh M but has the same hole or holes of different sizes.

The first jetting section 333 is configured such that a vertical tube 333a connected to the supply tube 321 is disposed inside the body 331 and a rotary nozzle 333b is provided at the upper end of the vertical tube 333a, The nozzle 333b is inserted into the center of the mesh M. At this time, when the mixture is supplied to the mesh (M) by receiving the mixture from the supply pipe (321), the mixture passes through the mesh (M) and bubbles are generated. As a result, the contact area of the mixture becomes large, and the ozone gas dissolves well in water.

The perforated plate 334 is formed with a plurality of holes in a substantially disc shape, is fitted in the vertical tube 333a, and is provided at the lower end of the mesh M. That is, the bubble generated in the bubble generator 332 falls down through the hole of the perforated plate 334, so that the residence time of the bubble can be extended, and the bubble fades to generate mixed water. Thus, by extending the bonding time between the gas and the liquid, the gas is well dissolved in the liquid.

The second jetting section 336 is disposed below the body 331, and a plurality of the second jetting sections 336 are provided around the body 331. That is, the mixed water dropped through the perforated plate 334 is collected at the bottom of the body 331, and the mixed water collected at the bottom is injected into the bubble generating unit 350 to be described later through the second jetting unit 336. A description thereof will be described later.

Here, the second jetting part 336 may be formed with a plurality of jetting nozzles or a slit shape in the vertical direction in order to widen the jetting range. In addition, the second jetting section 336 may be formed toward the bubble generating section 350, which will be described later.

One end of the discharge part 340 is installed around the lower part of the main body 310, connected to the main body 310, and bent upward. The discharge unit 340 is provided with an exhaust unit 341 at an upper end of the discharge unit 340 to discharge surplus gas remaining in the body 310.

The bubble generating unit 350 includes a plurality of holes formed in a rectangular perforated panel and a plurality of holes are provided around the upper portion of the body 331 to correspond to the second jetting unit 336. As a result, the mixed water sprayed from the second jetting part 336 collides to generate bubbles, and the contact area of the mixed water increases, so that the gas melts once more into the mixed water, thereby producing high-quality mixed water.

The pressure measuring unit 360 is installed at the upper end of the main body 310 and measures the internal pressure of the main body 310.

The pressure reducing valve 370 is disposed outside the main body 310 and has one end connected to the upper end of the main body 310 and the other end connected to the supply pipe 321 to open and close the upper connecting portion of the main body 311. That is, when the pressure measured by the pressure measuring unit 360 exceeds the set pressure 4K, the pressure reducing valve 370 is opened to allow the internal pressure of the main body 310 to be bypassed to the supply pipe 321, The pressure drops.

In addition, the ozone treatment unit 160 is further configured to minimize excess ozone gas discharged through the exhaust port 341 of the discharge unit 340 described above.

16, the ozone treatment section 160 includes an ultraviolet ray contact section 161, an ozone destruction filtering medium section 162, an electric control section 163, and a discharge section 164.

The present invention minimizes the emission of harmful gas by passing ozone gas that is vulnerable to ultraviolet rays to an ultraviolet lamp of 254 nm and passing ozone-destroying filter medium 162-1 having a property of decomposing ozone. That is, the ultraviolet ray contact portion 161 is constituted by an external appearance of a stainless steel material that surrounds an exhaust pipe (not shown) formed from the exhaust port 341, and constitutes an ultraviolet lamp inside thereof, Ultraviolet rays are emitted from the ultraviolet lamp by breaking the ozone passing through the space between the quartz tube 161-1 and the ozone-destroying filter medium part 162, so that the ozone gas is decomposed by contacting with ultraviolet rays.

The ultraviolet ray contact portion 161 is composed of an ultraviolet lamp and a quartz tube 161-1 that surrounds the ultraviolet ray lamp 161. The ultraviolet ray contact portion 161 communicates with the ozone destructive filter portion 162 through two pores at the lower end of the quartz tube 161-1.

The ultraviolet lamp is connected to an electric control unit 163 located at the lower end to supply power to the ultraviolet light contact unit 161, and is illuminated only when the entire system is operating. The ozone gas is decomposed to the maximum by applying light of 32 watts / 254 nm, and the ozone gas is destroyed again by passing through the ozone-destroying filter medium portion 162 disposed at the rear end of the ozone gas, .

Excess ozone gas passed through the ultraviolet ray contact portion 161 and the ozone destruction filter portion 162 is finally discharged to the outside through the discharge portion 163 naturally.

On the other hand, as shown in FIG. 11, the second jetting section 336 may be inclined toward the bubble generating section. Accordingly, the ozone water sprayed from the second sprayer 336 is uniformly sprayed to the bubble generator 350.

Here, as shown in FIG. 12, the perforated plate 334 may have a plurality of holes having different sizes. Accordingly, the mixed water and bubbles generated through the mesh can stay together with the perforated plate 334 while descending.

As shown in FIG. 13, a plurality of holes having different sizes may be formed in the bubble generator 350. As a result, the mixed water and the foam sprayed from the second sprayer 336 pass through the bubble generator 350, and the mixed water bubbles once again, and the sprayed foam passes as it is to maximize the contact area, A larger amount of residual gas gas can be melted to produce a high quality mixed water.

The ozonated water thus mixed is passed through a gas-liquid mixing line mixer and then stored in an internal or external reservoir or supplied directly.

14 and 15, the gas-liquid mixing line mixing apparatus includes a cylindrical housing 510 and a plurality of mixing members.

The gas-liquid mixing line mixer further enhances the ozone gas dissolution rate of the ozonated water mixed through the gas-liquid mixing section. The ozonated water mixes the ozone gas through the plurality of mixing members and increases the contact area and the contact time, .

That is, a plurality of mixing members are fitted to the central axis of the gas-liquid mixed-line mixer for this purpose, and the plurality of mixing members include the symmetrical perforated plate 520, the asymmetric perforated plate 530 and the vane member.

The symmetrical perforated plate 520 and the asymmetric perforated plate 530 pass through the holes formed in the disk and dissolve well and are further mixed by rotation. The vane member can extend the contact area and contact time so that the ozone gas can be dissolved well in water by the rotation of the blade.

Symmetrical perforated plate 520 is formed symmetrically around perimeter of perforated plate 521. Asymmetric perforated plate 530 is formed with asymmetric holes arranged on the disk, And the smaller holes 532 are formed asymmetrically.

The symmetrical perforated plate 520 and the asymmetric perforated plate 530 are both roughened so that the flow direction of the mixed water is blocked and changed, and mixing is performed more well.

In addition, the symmetrical perforated plate 520 and the asymmetric perforated plate 530 can be arranged in plural.

The following vane member is provided at the rear end of the perforated plate for promoting mixing by inducing the rotation of the mixed water passing through the perforated plate in the radial direction on the end face of the housing 510. In the example of Fig. 14, And the example of FIG. 15 corresponds to a flex vane 550 composed of a plurality of rounded blades.

As described above, the excellent or surface water, ground water or purified water is purified by using high concentration of ozone, so that it can be purified to the extent that it can be used as drinking water even in areas where drinking water is insufficient.

Further, the superior purification device and the ozonated water purification device may be packaged in the purifying chamber 1 as shown in FIG. 17, or may be modularized and manufactured as a set so that they can be disposed more conveniently and conveniently in the corresponding area.

This provides a power supply to provide the power needed for the storm water purification system and the ozonated water purification system and allows the storage facility to be protected from external environmental hazards.

In addition, various sensors and photographing means are provided inside and outside the purifying chamber 1 so as to monitor the operation of the devices and the water quality state so that the purified water to be used as potable water can be thoroughly managed so as not to be exposed to danger, And the devices can be controlled remotely through a separate control means according to the monitoring result.

In other words, it is possible to measure the equipment aspect of the apparatus and the water quality of the ozonated water by using the water intake sensor of an excellent water intake device, the water level sensor in the ozonated water purification device, the pressure sensor of the pump,

The measured data can be stored in a separate database, thereby making it possible to utilize the data.

In addition, the collected data can be monitored through the web or mobile through the linkage API.

On the other hand, the roof of the purifying chamber 1 is provided with a solar cell canopy device 2 to which a solar cell is attached, so that the energy collected by the solar cell can be used for power supply.

The solar cell shading device 2 is provided so as to be able to spread on the hinge by a motorized method when necessary as shown in the drawing, thereby enabling more efficient condensation, and also capable of shielding the sunlight shining on the purifying chamber 1 as much as possible The facility can play a role at the same time.

While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is to be understood that the invention is not limited to the disclosed exemplary embodiments. And the scope of the present invention should be understood as the following claims and their equivalents.

20: Excellent water intake system
30: Excellent purification device
40: Stored water supply device
10: ozonated water purification device
1: Clean room
2: Solar cell awnings

Claims (7)

An excellent water intake system for taking rainwater;
An excellent purification device for physically purifying stormwater supplied from the storm water taking-in device;
An ozonated water purifier for physically purifying the stormwater in the stormwater purification system using sterilization using ozone; And
And a storage water supply device for supplying storage water stored in a separate storage space to the stormwater purification apparatus,
The ozonated water purification apparatus includes:
A housing defining an appearance;
A cluster separator for separating clusters of water introduced by the pump by an electric field;
A backflow prevention part for introducing ozone gas from the ozone generator and preventing reverse flow of raw water;
A gas-liquid mixing unit for mixing water having passed through the cluster separating unit and ozone gas flowing through the backflow preventing unit; And
And a gas-liquid mixed line mixer for mixing and supplying the mixed water having passed through the gas-liquid mixer to the ozone gas mixer. The method according to claim 1,
The gas-liquid mixed line mixer includes:
A cylindrical housing;
And a plurality of mixing members inserted into and inserted into the central axis of the cylindrical housing,
Wherein the mixing member comprises a perforated plate and a vane member. The method of claim 2,
Wherein the perforated plate comprises: a symmetrical perforated plate having symmetrical holes formed in a disk; And an asymmetric perforated plate formed asymmetrically with the hole in the disk. The method of claim 2,
Characterized in that said vane member is a flex vane comprising a plurality of blades and comprising a straight vane comprising a flat blade or a round vane shaped blade. The method of claim 4,
Wherein the vane member is disposed at a rear end of the perforated plate. The method of claim 2,
The gas-
A supply part for supplying a mixture of water and ozone gas;
A body forming an outer shape;
A foam generating unit disposed in the main body and generating a foam by injecting the mixture in the first jetting unit; An ozonated water generating part having at least one second injection part for converting the bubbles into mixed water and injecting the converted mixed water to the inner surface of the main body and raising the internal pressure of the main body; And
And a discharge portion for discharging the mixed water sprayed through the second spray portion to the main body,
Wherein the bubble generating unit converts the mixture into bubbles to increase the contact area to increase the amount of dissolved gas. The method of claim 2,
Wherein the ozone water purification apparatus is provided with a plurality of sensors and a separate database for storing data collected from the plurality of sensors is provided and the measurement data can be transmitted remotely by the plurality of sensors. Superior purification system using.

Images