KR101070172B1 - purification device - Google Patents

Abstract

The present invention is a volume control tank, decomposition tank, reagent tank, sedimentation tank, flotation tank, stabilizer tank, oxygen supply tank, filtration tank, water storage tank, volume control tank, advanced treatment filtration tank and treated water storage tank, volume control tank, decomposition tank, The present invention relates to a purification apparatus using a water decomposition method that allows for a quick and economical purification by completely processing the functions of a reagent tank, a precipitation tank, a flotation tank, and a stabilizer tank by a single device.

According to the present invention,

A first control valve and a pump are installed in the raw water inlet pipe of the centrifugal volume regulator in which raw water is introduced through the raw water inlet pipe.

At the lower end of the centrifugal volume regulator having a discharge port formed at an upper end thereof, a return port provided with a second control valve is installed.

In the upper part of the first decomposition purification pressurization chamber connected through the first supply port in the centrifugal volume regulator, an aeration flow acceleration motor is installed to allow the vanes to rotate inside, thereby forming an aeration mechanism at the bottom thereof.

Sides of the plurality of decomposed pentagonal bodies installed in multiple stages inside the first decomposed purification buoyancy chamber are alternately formed with anion and cationic grilles, and an alternating electromagnet is mounted on the outside of the first decomposed purification buoyancy chamber by magnetic force. The inner diaphragm and the outer diaphragm formed on a plurality of disassembled pentagrams cause the fixed piece to vibrate,

A supply cylinder is installed at an upper end of the first decomposition purification pressurization chamber to supply a substituted aggregated adsorbent,

A magnetic separation network is installed at the center of the inside while installing a water wall composition part having a heat generator at the lower end of the treated water purification stable chamber.

The sludge outlet is installed at the lower part of the treated water purification stability chamber in which the ion exchange separation network is installed therein, and the sludge collection chamber is connected to the upper part through the collecting port.

Anion oxygen group aeration air stone is installed at the lower end of the second decomposition purification pressurization chamber, and a plurality of magnetization ion exchange decomposition pentagons are arranged up and down at the center.

The second decomposition purification pressurization chamber provided with an anion sprayer on the upper surface is characterized in that configured to connect to the upper portion of the treated water collection chamber through the extraction port.

Centrifugation volume adjustment, decomposition and purification pressurization, circulating, decomposition pentagon, alternating electromagnet, diaphragm, treatment water purification stability, water wall composition, magnetization separation, sludge collection, treatment water collection

Description

Purification device using water decomposition method

The present invention relates to a purification apparatus using a water decomposition method, and in detail, a water control tank, a decomposition tank, a reagent tank, a precipitation tank, a flotation tank, a stabilizer tank, an oxygen supply tank, a filtration tank, a water quality storage reservoir, a volume control tank, and an altitude. Purification using the water decomposition method that enables quick and economical purification by completely processing the functions of volume control tank, digestion tank, reagent tank, settling tank, flotation tank and stabilizer tank in treated filtration tank and treated water reservoir Relates to a device.

In general, since a lot of wastes such as garbage and other wastes are emitted from general homes, factories, and farms, water with self-cleaning ability is also heavily polluted and cannot be directly used for drinking water, as well as damaging many ecosystems such as rivers and seas Is already well known.

And once polluted water is used for the purification process to clean the water, various apparatuses and methods are used a lot, and research for more efficient water purification is still being conducted.

Looking at some methods of integers known to date, some of them use or study biological methods using activated sludge or microorganisms, chemical methods using chemical reactions, and physical methods using electrons or ultrasonic waves.

However, according to the conventional waste water purification method as described above, not only stable and complete water purification is performed, but also high operating costs required for water purification cannot increase water purification efficiency.

In other words, conventional biological methods using activated sludge or microorganisms are used in many countries internationally to decompose contaminants by microorganisms, but since they have a limit of effective concentration in digestive substances of microorganisms, they contain high concentrations of waste. In the state, the treatment is insufficient, and in the case of alkaline or acidic wastewater, pretreatment is required, and it is affected by the environment such as time and temperature. there was.

In addition, the chemical treatment method has the advantage of fast reaction speed and simple process, while the cost of installation and maintenance are too high to treat wastewater by itself even if it is difficult to decompose organic matters by biological treatment. There was a drawback of being used only as a pretreatment or aftertreatment.

In addition, the physical method using electrons or ultrasonic waves is applied to the process of decomposing hardly decomposable substances such as benzene compounds and halogen compounds, which are difficult to process by biological methods or chemical methods, but they are not widely used because their effects are insignificant compared to the huge facility and maintenance costs. There was a disadvantage.

Accordingly, the applicant has proposed a patent application No. 10-1999-0037763 dated September 6, 1999 (wastewater treatment system using molecular decomposition method),

This, after the waste water collected in the storage tank goes through the PH adjustment tank, and moves to the pre-treatment and flotation separation tank to treat the suspended matter for purification,

Next, the contaminants contained in the waste water are oxidized and decomposed while passing through the digestion tank, the flocculation tank, and the immersion tank several times, and the separated contaminants are suspended or suspended while being removed.

It increases dissolved oxygen in oxygen supply tank and removes fine contaminants while passing through filtration tank, adsorption tank, and substitution tank in order to completely decontaminate contaminants by physical energy rather than conventional biological treatment method. The original stable material was converted to positive water with excellent self-cleaning ability.

However, in the wastewater treatment system using the conventional molecular decomposition method as described above, the contaminants are removed by passing through the decomposing tank, the flocculating tank, and the settling tank several times, but the efficiency is not maximized by the general structure. There was a problem in that the economic feasibility was not supported due to the high cost of treating wastewater.

Therefore, the present invention is to solve the conventional problems as described above, water volume control tank, decomposition tank, reagent tank, sedimentation tank, flotation tank, stabilizer tank, oxygen supply tank, filtration tank, water storage tank, volume control tank, altitude Purification using the water decomposition method that enables quick and economical purification by completely processing the functions of volume control tank, digestion tank, reagent tank, settling tank, flotation tank and stabilizer tank in treated filtration tank and treated water reservoir It is an object to provide a device.

Purification apparatus using the water decomposition method of the present invention for achieving the above object is provided with a first control valve and a pump in the raw water inlet pipe of the centrifugal volume regulator in which raw water is introduced through the raw water inlet pipe,

At the lower end of the centrifugal volume regulator having a discharge port formed at an upper end thereof, a return port provided with a second control valve is installed.

In the upper part of the first decomposition purification pressurization chamber connected through the first supply port in the centrifugal volume regulator, an aeration flow acceleration motor is installed to allow the vanes to rotate inside, thereby forming an aeration mechanism at the bottom thereof.

Sides of the plurality of decomposed pentagonal bodies installed in multiple stages inside the first decomposed purification buoyancy chamber are alternately formed with anion and cationic grilles, and an alternating electromagnet is mounted on the outside of the first decomposed purification buoyancy chamber by magnetic force. The inner diaphragm and the outer diaphragm formed on a plurality of disassembled pentagons vibrate the stationary piece,

A supply cylinder is installed at an upper end of the first decomposition purification pressurization chamber to supply a substituted aggregated adsorbent,

A magnetic separation network is installed at the center of the inside while installing a water wall composition part having a heat generator at the lower end of the treated water purification stable chamber.

The sludge outlet is installed at the lower part of the treated water purification stability chamber in which the ion exchange separation network is installed therein, and the sludge collection chamber is connected to the upper part through the collecting port.

Anion oxygen group aeration air stone is installed at the lower end of the second decomposition purification pressurization chamber, and a plurality of magnetization ion exchange decomposition pentagons are arranged up and down at the center.

The second decomposition purification pressurization chamber provided with an anion sprayer on the upper surface is characterized in that configured to connect to the upper portion of the treated water collection chamber through the extraction port.

In the purification apparatus using the water decomposition method of the present invention as described above, the first water inlet pipe of the centrifugal water inlet regulator through which the raw water is introduced through the raw water inlet pipe, the first control valve and the pump to adjust the amount of water,

On the upper surface of the first decomposition purification pressurization chamber connected through the first supply port in the centrifugal volume regulator, an aeration return acceleration motor is installed to allow the wings to rotate inside, together with the air aerated in the aerator at the bottom. Vortices and injuries,

Sides of the plurality of decomposed pentagonal bodies installed in multiple stages inside the first decomposed purification buoyancy chamber are alternately formed with anion and cationic grilles, and an alternating electromagnet is mounted on the outside of the first decomposed purification buoyancy chamber by magnetic force. The inner diaphragm and the outer diaphragm formed on the plurality of disassembled pentagonal bodies vibrate the fixing piece to the axis so that the sludge can be smoothly disassembled,

At the lower end of the treated water purification stable chamber, a water wall composition part having a heat generator is installed, and a magnetization separation network is installed at the center thereof to form a water wall by floating force.

Anion oxygen group aeration air stone is installed at the lower end of the second decomposition purification pressurization chamber, and a plurality of magnetization ion exchange decomposition pentagons are arranged up and down at the center to be purified again by water decomposition and collected in the treatment water collection chamber. It is effective to make.

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

Purifier using the water decomposition method according to the present invention

A first control valve 3 and a pump 4 are installed in the raw water inlet pipe 2 of the centrifugal volume regulator 1 through which the raw water is introduced through the raw water inlet pipe 2, and then the first decomposition purification pressurization unit The state of supply of raw water is controlled by the water level sensor 9 installed in the loss chamber 10,

The raw water flowing into the centrifugal volume regulator 1 above an appropriate capacity is an additional amount or more of the amount adjusted through the second regulating valve 5 through the circulating hole 6 (not shown in the drawing). Return to the

Raw water inlet pipe (2) is formed on the side of the eccentric position of the centrifugal volume regulator (1) so that the raw water rotates while vortexing inside,

As the raw water rotates in the centrifugal volume regulator (1), the pollutant with a high concentration in the water phase is naturally centrifuged and separated through the side of the centrifugal volume regulator (1) and descends downward. Combination with the bubble to rise above the centrifugal volume regulator (1) to be discharged through the discharge pipe (7),

The raw water from which some sludge or contaminants have been removed by centrifugation and specific gravity separation such as flotation in the centrifugal volume regulator 1 is first decomposed and purified through the first supply port 11. To get into,

The raw water introduced into the first decomposition purification pressurization chamber 10 is gradually appropriate inside the first decomposition purification pressurization chamber 10 by the blade 13 rotating by the aeration flow acceleration motor 12. To flow at speed,

The circulating raw water is caused to vortex while hitting a plurality of decomposition pentagonal body 14 built in a multi-step inside the first decomposition purification pressurization chamber 10,

The raw water by oxidative decomposition is introduced into the air through the opening 22 of the lower end of the first decomposition purification pressurization chamber 10,

By forming an anion grill 15 on the side of the decomposition pentagon 14 to draw the cationic contaminants of the contaminants and to push out the anionic contaminants to have an effect of decomposition and purification,

On the other side of the decomposition pentagonal body 14 to form a cationic grill 16 to pull out the anionic contaminants, and away from the cationic contaminants to decompose contaminants of the powerful complex macromolecules,

The internal diaphragm 18 formed on the lower surface and the upper surface of the plurality of decomposition pentagonal bodies 14 by magnetic force according to the polarity of the alternating electromagnet 17 mounted on the outside of the first decomposition purification pressurization chamber 10. ) And the external diaphragm 19 to reciprocate the fixed piece 20, 21 axially,

The ionization port 27 is formed at an upper end of the first decomposition purification pressurization chamber 10 while an aeration apparatus 22 is provided at the upper end thereof to receive an anion, a cationic oxygen, and an ozone group.

The sludge discharge port 24 is formed in the lower concave portion 23 of the first decomposition purification pressurization chamber 10 to discharge the collected sludge,

A supply cylinder 25 is installed at an upper end of the first decomposition purification pressurization chamber 10 to supply a substituted coagulant adsorbent,

The raw water purified in the first decomposition purification pressurization chamber 10 is introduced into the treated water purification stable chamber 30 through the treated water outlet 26, and the raw water is not purified. To be reduced to the first decomposition purification pressurization chamber (10),

An underwater separation wall is formed by the anion oxygen and ozone groups aerated in the water wall composition part 31 installed at the lower end of the treated water purification stability chamber 30 to interact with the heat generator 32 of the water wall composition part 31. To cause a severe double-sided convection phenomenon centering on the magnetization separation network (33),

The sedimentary sludge separated by the ion exchange separation network 35 from the raw water entering the treatment water purification stability chamber 30 is discharged through the lower sludge outlet 34 of the water wall composition part 31 and the floating sludge After being separated into a plurality of sludge collection chamber 40 through the collecting port 41, it is to be removed through the sludge discharge port 42,

The raw water purified by convection in the internal stable chamber of the treated water purification stability chamber 30 and the specific oxygen separation and aeration of the anion oxygen group are aerated increases the second supply port 51. Through the second decomposition purification pressurization chamber 50 to enter,

The raw water introduced into the second decomposition purification pressurization chamber 50 and purified is saturated with dissolved oxygen (DO) by the anion oxygen group, which is aerated in large quantities through the anion oxygen group aeration air stone 52, As a result, a number of magnetization ion exchange decomposition pentagrams 53 are used to purify the pyramid energy by focusing and net collision purification, oxidative purification, ion exchange purification, and rotational twist (by pyramid twist configuration). To be completely disintegrated and purified,

The negative ions in the upper surface of the second decomposition purification pressurization chamber (50) to generate negative ions inside,

The anion sprinkler 55 has an electric discharge unit (not shown) to produce cations and anions, and the cations interact with tourmaline, precious stones, and gelatin to deodorize, while the anion is water. Melted and sprinkled on the upper surface of the second decomposition purification pressurization chamber 50 together with water so as to generate a soot and oxidative purification effect,

The sludge contained in the treated water while being purified by the second decomposition purification pressurization chamber 50 is floated by the air aerated in large quantities in the air stone 52 at the bottom, and the second decomposition purification pressurization chamber 50 is provided. While the treated water of the rises to draw the raw water of the treated water purification stability chamber 30 through the water wall composition part 31,

Sludge rises due to the rise to enter the upper portion of the treatment water collection chamber 60 through the treatment water extraction port 54 with the purified treatment water,

On the other hand, in the treated water purification stable chamber 30 in conjunction with the air bubbles continuously aerated through the water wall composition part 31 to the magnetized ion exchange decomposition pentagon 53 with the sludge by the ion exchange separation network (35). The sludge separated by this is configured to be collected and removed by a plurality of sludge collection chambers 40 formed on both sides of the magnetization separation net 33.

Purification apparatus using the water decomposition method of the present invention configured as described above,

A first control valve 3 and a pump 4 are installed in the raw water inlet pipe 2 of the centrifugal volume regulator 1 through which the raw water is introduced through the raw water inlet pipe 2, and then the first decomposition purification pressurization unit The state of supply of raw water is controlled by the water level sensor 9 installed in the loss chamber 10.

The supplied raw water is to remove large dirt, objects or sludge with a screen (not shown) installed in the front of the raw water inlet pipe (2).

When the raw water is introduced into the centrifugal volume regulator 1 when the raw water flows into the proper capacity by the pump 4, the surplus water is added more than the amount regulated through the second control valve 5 formed at the bottom. The amount is to be returned to the raw water tank of the front end through the return hole (6).

The raw water flowing into the centrifugal volume regulator 1 through the raw water inlet pipe 2 continuously by the pumping pressure of the pump 4 is introduced into the raw water inlet pipe 2 located on the side in an eccentric position. By the pressure to rotate while vortexing inside the centrifuge controller (1).

As the raw water rotates in the centrifugal volume regulator (1), the pollutant with a high concentration in the water phase is naturally centrifuged and separated through the side of the centrifugal volume regulator (1) and descends downward. Combination with the bubble to rise above the centrifugal volume regulator 1 to be discharged through the discharge pipe (7).

The raw water from which some sludge or contaminants are removed by centrifugation and specific gravity separation such as flotation in the centrifugal volume regulator 1 is discharged through the first supply port 11. To get into

If the diameter of the first supply port 11 of the first disintegration replacement pressure inlet chamber 10 is small, the flow rate may be increased to disperse the aggregated sludge. (2) Larger and wider to prevent dispersion.

The raw water introduced into the first decomposition purification pressurization chamber 10 is gradually appropriate inside the first decomposition purification pressurization chamber 10 by the blade 13 rotating by the aeration flow acceleration motor 12. Return to speed.

The circulating raw water is caused to vortex while hitting a plurality of decomposition pentagonal body 14 built in a multi-stage inside the first decomposition purification pressurization chamber (10).

The centrifugal force is applied during the flow of the vortex to cause a vortex phenomenon. The rotating raw water strikes a plurality of decomposed pentagons 14 and vortex vortex phenomena opposite to the flow direction of the plurality of decomposed pentagons 14. This will cause a binding collision phenomenon, such as a strong decomposition of water phenomena occurs to purify the raw water.

At this time, when the aeration flow acceleration motor 12 operates, the raw water is sent to the lower end of the first decomposition purification pressurization chamber 10 while rapidly rotating a plurality of decomposition pentagrams 14 by the lower wing 13. Since the amount is large, a large amount of air is sucked together with the plurality of decomposition pentagonal bodies 14 and mixed with the air introduced through the lower opening 22 to purify the raw water by oxidative decomposition.

In the first decomposition purification pressurizing chamber 10, a large amount of air is gradually introduced into the plurality of decomposition pentagrams 14 by the operation of the aeration flow acceleration motor 12, and the first decomposition purification pressurizing chamber at an appropriate speed ( 10) while entering or passing through the anion grille 15 of the plurality of decomposition pentagrams 14 while hitting the plurality of decomposition pentagrams 14 formed therein, the cationic contaminants of the contaminants are pulled out and the anionic contaminants are pushed out for purification. To have an effect.

In addition, at this time, the cationic grille 16 is formed on the other side of the plurality of decomposed pentagrams 14 to pull out the anionic contaminants and away from the cationic contaminants to decompose the contaminants of the strong complex macromolecules.

In the above decomposition process, contaminants are associated with them by ion exchange oxidative decomposition and the like by decomposing and phenomena through the supply of oxygen group, thereby decomposing and decomposing with amazing performance.

In this process, a radical group is naturally generated in the water, and the purification of the plurality of decomposed pentagrams 14 is synergistically accelerated by the strong and delicate oxidation of the radical group.

At this time, the internal diaphragm 18 formed on the lower surface and the upper surface of the plurality of decomposition pentagonal bodies 14 by the magnetic force according to the polarity of the alternating electromagnet 17 mounted on the outside of the first decomposition purification pressurization chamber 10 is changed. Pulsating, waving, and magnetizing a plurality of decomposed pentagonal bodies 14 by reciprocating vibrations of the external diaphragm 19) and the outer diaphragm 19. Maximize oxidative decomposition of oxygen group and radical group.

The reciprocating vibration of the diaphragm 18 and 19 is to maximize the purification phenomenon by various ion exchange by the anion grill 15 and the cation grill 16 constituted in a plurality of decomposition pentagonal body 14.

By the action of the alternating electromagnet 17, a plurality of decomposed pentagrams 14 are magnetized, and the inner diaphragm 18 and the outer diaphragm 19 vibrate in a reciprocating manner, thereby making the particle motion of raw water extremely intense and contaminating molecules. The combined enddal of is disrupted by vibrating magnetization to maximize the effect of various modifications.

The inner diaphragm 18 and the outer diaphragm 19 vibrate and shake the upper pole around the lower fixing piece 20, 21 to generate an energy source of some longwave, longwave, shortwave, ultrashort, and sound waves. The sources are very effective in decomposing the contaminants in the water, and at the same time, synergistically with all the purifying actions occurring in the first decomposition purification pressurization chamber 10.

Molecular motion and bubbles inside the first decompression-purifying pressurizing chamber 10 including the action of the aeration flow and the alternating electromagnet 17 and the action of the internal diaphragm 18 and the external diaphragm 19 by the aeration flow acceleration motor 12. The decomposition by the parametric energy concentration of a plurality of decomposition pentagram 14 introduced into the alternating electromagnet 17 by the rising of these, etc. are made.

A plurality of decomposition pentagonal body 14 rotated by the raw water flowing through the aeration of the air through the aeration mechanism 22 at the bottom and the anion supplied through the ion inlet 27 at the top and aeration of cationic oxygen, ozone group It is made in water to increase the amount of dissolved oxygen (DO) and to oxidatively combine the contaminants to purify a large number of decomposition pentagones (14).

When the contaminated sludges are collected and become larger during the above process, the contaminated sludge accumulated in the water after being precipitated in the lower concave portion 23 by centrifugal force and internal decomposition is discharged through the lower sludge outlet 24.

A supply cylinder 25 is installed at the upper end of the first decomposition purification pressurization chamber 10 to supply a substituted agglomerated adsorbent, so as to be diluted in the plurality of decomposed pentagonal bodies 14 to adsorb and replace contaminated components, and to substitute agglomerated substitutes. The adsorbent becomes agglomerate nuclei to aggregate contaminants.

The substituted adsorbent is crushed zeolite, magnetite ore and activated carbon to the size of 1mm or less, and then bonded and bonded while mixing each of 30% by weight, 30% by weight and 40% by weight to form a diameter of 3 to 8cm by specific gravity 1, 8 to 2.2 or more of the first decomposition purification pressurizing chamber 10 while purifying by the adsorption of contaminants, the internal pores and the floating bubbles with the decomposition of the pentagonal body 14 very slowly. While staying in the decomposed pentagonal body 14 for a long time, the water treatment purification effect by substitution adsorption flocification is maximized.

The plurality of decomposed pentagonal bodies 14 have a pyramidal shape in a plurality of stages in the first decomposed pentagonal chamber 10, the inner angle of which is configured to have a twisted shape for each layer by 60 ° and the lower end of one decomposed pentagonal body 14. By arranging the plurality of decomposition pentagonals 14 up and down in such a manner that a part of the other decomposition pentagonal bodies 14 is inserted into the upper and lower parts, the pyramid energy concentration of the rotating pentagonal body 14 rotated by a twisting configuration enables high efficiency and high performance decomposition purification. Make it happen.

The lower decomposition pentagonal body 14 has a part of a vertex inserted into the upper decomposition pentagonal body 14 so that pyramidal energy concentration can be minimized and decomposed and purified by a plurality of decomposition pentagonal bodies 14 with high performance and high efficiency. Attached to the cation grill 16 of the diaphragm 19 performs the function of the cation magnetization vibrating plate and attached to the anion grill 15 by the linkage action with the decomposition pentagonal body 14 while performing the function of the anion magnetization vibrating plate. Water treatment decomposition and purification to complete deodorization.

In the first decomposition purification pressurization chamber 10, various kinds of water treatments are performed, and the odor causing components of the wastewater are completely decomposed and oxidized by decomposition by magnetization, energy sources, concentration of energy focus, and oxidation of oxygen group. It can be seen that the odor odor is removed to the extent that it can.

This comprehensive magnetization, energy source, radical, oxidation, energy focusing, underwater underwater and ion exchange purify the water, and all the water pollution such as pollutant sludge and odors. The state wastewater is to be purified by water treatment.

The structure of the first decomposition purification pressurization chamber 10 is in the form of a hexagonal column for maximizing the purification function of the polarity of the electromagnet and increasing the hexagonal structure and the purification efficiency of water.

In the raw water to be purified, a plurality of decomposed pentagrams 14 rotate slowly in the interior of the first decomposed purification buoyancy chamber 10 and continue to purify and strengthen continuously and repeatedly, and the purified water having a large specific gravity increases in the lower portion. In this case, the aeration flow acceleration motor 12 is pushed in and pulled by the air bubbles in the bubble so as to flow into the treatment water purification stability chamber 30 through the treatment water outlet 26.

Magnetization in the first decomposition purification pressurization chamber (10). Ion exchange. Radical oxidation. Oxygen group oxidation. Water vapor. Floor. Water that has been purified by substitution adsorption and by substitution adsorption, while convection is caused by floating force in the bubble group, good water is collected in the lower part by the underwater gravity separation phenomenon of the treated water through the treated water outlet 26. Enter the purification stability room (30).

This bad water is introduced into the first decomposition purification pressurization chamber 10 through the discharge return water inlet 28 during the water treatment purification process of the low system, and is repeatedly purified.

The raw water entering the treated water purification stability chamber 30 is a magnetized separation network by the underwater separation wall acting as a heat dissipation device of the water wall composition part 31 by the anion oxygen and ozone groups aerated in the water wall composition part 31. It causes severe double-sided convection phenomena centering on (33) and the raw water on the left and right sides can pass through the rise of bubble group and the vertical rise of the hot water with high relative water temperature in the treated water purification stability room 30. Forms a water wall.

This water wall plays a very important role in water treatment purification. First of all, when the water wall is formed, the aeration in the water wall composition part 31 causes a small difference due to the heating of the internal heat generator 32, but the water temperature of the upper surface of the heat generator 32 is small but the specific gravity is lowered. The left and right sides of the heat generator 32 rise due to the bubble rising force of the raw waters due to the aeration, but the water heated by the heat generator 32 has a low specific gravity so that the rising speed is faster than the left and right rises, and the rapid rotation convection. Water wall composition part 31 to form a water wall separating the water on both sides.

The raw water of the treated water purification stable chamber 30 before the first decomposition purification pressurization chamber 10 enters the treated water purification stable chamber 30 is water-treated and suspended sludge becomes suspended in the treated water purification stable chamber 30. The heavy sedimentary sludge, which is discharged from the upper surface and collected in the alicyclic adsorbent, is discharged through the sludge discharge port 24, and the raw water enters the treated water purification stable chamber 30.

Raw water entered into the treatment water purification stable chamber 30 is a radical oxidative decomposition, anion oxygen group by the magnetization separation network 33 on the left side of the inside of the treatment water purification stable chamber 30 by the action of most water wall composition part 31. Purification and purification by collision with magnetization collision, while descending during convection, it collides with ion exchange separation network (35), and purification is carried out by purifying ion exchange of cations and anions. The floating SS below the composition part 31 is separated and removed in a plurality of sludge collection chambers 40.

Some of the purified water moves through the water wall to the right side of the water wall to convection in the stable chamber of the treated water purification stability chamber 30, and the specific gravity is separated and the dissolved oxygen amount (DO) is increased by the aeration oxygen group. While the purified water is to enter the second decomposition purification pressurization chamber 50 through the second supply port (51).

Purified water introduced into the second decomposition purification pressurization chamber 50 is saturated with dissolved oxygen (DO) by the anion oxygen group which is aerated in large quantity through the anion oxygen group aeration air stone 52, As it rises, a number of decomposition pentagons (53) provides perfect accurate purification by purging by pyramid energy concentration focusing, net collision purification, oxidative purification, ion exchange purification, and rotary twist (by pyramid twist configuration). To be completely decomposed and purified.

Anion is generated inside the negative ionizer 55 on the upper surface of the second decomposition purification pressurization chamber 50.

The anion sprinkler 55 has an electric discharge unit (not shown) to produce cations and anions, and the cations interact with tourmaline, precious stones, and gelatin to deodorize, while the anion is water. It is melted in water and sprayed on the upper surface of the second decomposition purification pressurization chamber 50 together with water so that the scouring and oxidation purification effect occurs.

The sludge contained in the treated water while being purified by the second decomposition purification pressurization chamber 50 is floated by the air aerated in large quantities in the air stone 52 at the bottom, and the second decomposition purification pressurization chamber 50 is provided. While the treated water of the rise up to draw the raw water of the treated water purification stability chamber 30 through the water wall composition part 31 to flow.

The sludge floated by the rise enters the upper portion of the treatment water collection chamber 60 through the treatment water extraction port 54 together with the purified treatment water.

On the other hand, in the treated water purification stable chamber 30 in conjunction with the air bubbles continuously aerated through the water wall composition part 31 to the magnetized ion exchange decomposition pentagon 53 with the sludge by the ion exchange separation network (35). The sludge separated by this is configured to be collected and removed by a plurality of sludge collection chambers 40 formed on both sides of the magnetization separation net 33.

That is, the raw water is partially purified by the purifying action of the treated water purification stability chamber 30 such as ion exchange, and part of the raw water flows into the first decomposing purification pressurization chamber 10 to continue the first decomposition purifying pressurization by the purifying action. The chamber 10 is purged continuously by returning to the loss chamber 10, the treatment water purification stable chamber 30, the second decomposition purification pressurization chamber 50, the treatment water collection chamber 60, and the first decomposition purification pressurization chamber 10. .

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, but many variations and modifications may be made without departing from the scope of the invention. It will be understood by those skilled in the art that various changes and modifications may be made without departing from the spirit and scope of the invention as defined by the appended claims.

1 is a front view showing the overall configuration of the present invention.

2 is a cross-sectional view schematically showing the internal configuration of the present invention.

3 is a plan sectional view showing a configuration of the present invention.

Figure 4 is a front view showing the configuration of the present invention decomposition pentahedron.

4 is a plan view showing the constitution of the present invention.

Explanation of symbols on the main parts of the drawings

1: Centrifuge Volume Adjuster 10: 1st Resolution Purification Pressurization Loss

12: aeration flow acceleration motor 14, 53: decomposition pentahedron

15 Anion Grill 16 Cationic Grill

17: alternating electromagnet 18, 19: diaphragm

22: aeration apparatus 30: treated water purification stable chamber

31: water wall composition part 33: magnetization separation network

40: sludge collection chamber 50: second decomposition purification pressurization chamber

60: treatment water collection room

Claims (1)

A first control valve 3 and a pump 4 are installed in the raw water inlet pipe 2 of the centrifugal volume regulator 1 through which the raw water is introduced through the raw water inlet pipe 2, At the lower end of the centrifugal volume regulator 1 having a discharge port 7 formed at an upper end thereof, a return hole 6 having a second control valve 5 is installed. The raw water inlet pipe (2) is formed on the side which is the eccentric position of the centrifugal volume regulator 1 so that the raw water rotates while vortexing inside, A water level sensor 9 is installed in the first decomposition purification pressurization chamber 10 connected to the centrifugal volume regulator 1 through a first supply port 11, An aeration aeration acceleration motor 12 is installed on the upper surface of the first decomposition purification pressurization chamber 10 so that the wing 13 rotates inside, and an aeration mechanism 22 is formed at the lower end thereof. The first decomposition purification pressurization chamber 10 has a plurality of decomposition pentagonal body 14 in a multi-stage, The anion grill 15 and the cation grill 16 are alternately formed on the side surface of the decomposition pentagonal body 14, and an alternating electromagnet 17 is mounted on the outside of the first decomposition purification pressurization chamber 10. The inner diaphragm 18 and the outer diaphragm 19 formed on the pentagonal body 14 to vibrate the fixing pieces 20, 21 axially, A sludge discharge port 24 is formed in the lower concave portion 23 of the first decomposition purification pressurization chamber 10 having an ion inlet 27 formed at an upper end thereof. A supply cylinder 25 is installed at an upper end of the first decomposition purification pressurization chamber 10 to supply a substituted coagulant adsorbent, The first decomposition purification pressurization chamber 10 through the return water inlet 28 while connecting the treatment water purification stability chamber 30 through the treatment water outlet 26 in the first decomposition purification pressurization chamber 10. To be connected to, At the lower end of the treated water purifying stable chamber 30, a magnetic separation separation network 33 is installed at the center of the water wall composition unit 31 having a heat generator 32. A plurality of sludge collection chambers 40 are installed through a collecting port 41 on the upper portion of the treatment water purification stable chamber 30 having an ion exchange separation network 35 installed therein, and a sludge discharge port 34 on the upper portion thereof. To connect, A second decomposition purification pressurization chamber 50 is connected to the treated water purification stability chamber 30 through a second supply port 51. Anion oxygen group aeration air stone 52 is installed at the lower end of the second decomposition purification pressurization chamber 50, and a plurality of magnetized ion exchange decomposition pentagons 53 are arranged up and down at the center. The second decomposition purification pressurization chamber (50) having an anion sprayer (55) installed on an upper surface thereof is characterized in that the water decomposition method is configured to enter the upper portion of the treated water collection chamber (60) through the extraction port (54). Used purifier.

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