KR102408977B1 - Water treatment method using high efficiency large-capacity ozone generator - Google Patents

Abstract

In a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention, the first step of collecting waste water that has passed through the microfilter from the distribution tank to the flow rate control unit, and the main line unit, the miscellaneous waste water in the flow rate control unit to the line mixer unit A second step of transferring, a third step of generating the first mixed water in which ozone and ultra-fine bubbles are mixed through the gas-liquid mixing unit, a fourth step of supplying the first mixed water generated by the gas-liquid mixing unit to the main line unit, A fifth step of mixing the miscellaneous wastewater introduced into the line mixer unit and the first mixed water, a sixth step of transferring the second mixed water mixed by the line mixer unit to the catalytic oxidation reaction unit, the second mixed water introduced into the catalytic oxidation reaction unit It may include a seventh step of treating the oxidation reaction and an eighth step of discharging the treated water treated in the catalytic oxidation reaction unit to the outside.

Description

Water treatment method using high efficiency large-capacity ozone generator

The present invention relates to a water treatment method using a high-efficiency large-capacity ozone generator, and more particularly, a water treatment system capable of generating ozone in a large capacity and supplying it to the system when treating miscellaneous wastewater collected from a distribution tank through a microfilter to a flow rate control tank It relates to a water treatment method using a high-efficiency, large-capacity ozone generator using

In general, as a water treatment technology for purifying wastewater, physicochemical treatment methods such as filtration, precipitation, and adsorption, and biological treatment methods using microorganisms are mainly used.

The physical and chemical treatment method has the disadvantages of requiring a large amount of chemicals and high operating cost. Although the biological treatment method using microorganisms is an eco-friendly treatment technology, the process is complicated and large-scale aeration tanks and sedimentation tanks are required, so a lot of facility space is required. In recent years, advanced oxidation treatment technology is being used because it is required, it takes a lot of time and money to construct, and it is not possible to easily purify the recalcitrant organic components of sewage and wastewater.

Advanced Oxidation Process (AOP) is a technology that decomposes organic compounds contained in wastewater into harmless compounds such as CO2, H2O, or O2 by generating OH radicals. Various types of technologies such as oxidation and oxidation by catalyst materials have been developed.

Advanced Oxidation Process (AOP) includes ozone(O3)/UV AOP(Advanced Oxidation Process), ozone(O3)/hydrogen peroxide(H2O2)(Peroxone AOP), hydrogen peroxide(H2O2)/UV AOP(Advanced Oxidation Process) ), AOP (Advanced Oxidation Process) using photocatalyst, ozone (O3)/High PH AOP (Advanced Oxidation Process), and hydrogen peroxide/iron salt AOP (Advanced Oxidation Process) technologies have been developed.

Meanwhile, among the advanced oxidation treatment technologies described above, the water treatment technology using ozone (O3)/hydrogen peroxide (H2O2) (Peroxone AOP) has excellent oxidizing power of relatively difficult-to-decompose organic substances, and the ozone remaining in the treatment process is combined with hydrogen peroxide (H2O2). Therefore, it has the characteristic of accelerating ozone decomposition and is widely used.

Korean Patent Registration No. 10-2169383

It is an object of the present invention to provide a water treatment method using a high-efficiency large-capacity ozone generator using a water treatment system using a high-efficiency large-capacity ozone generator that treats wastewater collected from a distribution tank through a microfilter to a flow rate control tank.

In a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention, a flow rate control unit for collecting miscellaneous wastewater, connected to the flow rate control unit, and mixing microbubbles including ozone and miscellaneous wastewater moved from the flow rate control unit A line mixer unit, a main line unit connecting the flow rate adjustment unit and the line mixer unit, a gas-liquid mixing unit supplying mixed water in which ozone and ultrafine bubbles are mixed to the main line unit, and ozone are generated, and the generated ozone is mixed with the gas-liquid unit High-efficiency, large-capacity using a water treatment system using a high-efficiency, large-capacity ozone generator including an ozone generating unit supplied to the unit and a catalytic oxidation reaction unit for oxidizing and treating contaminants in the mixed water moved from the line mixer while connected to the line mixer unit In the water treatment method using an ozone generator, a first step of collecting waste water passing through a microfilter from a distribution tank to the flow rate adjusting unit, a second step of transferring the miscellaneous waste water in the flow rate adjusting unit through the main line unit to the line mixer unit , a third step of generating a first mixed water in which ozone and ultrafine bubbles are mixed through the gas-liquid mixing unit, a fourth step of supplying the first mixed water generated by the gas-liquid mixing unit to the main line unit, the line A fifth step of mixing the miscellaneous wastewater introduced into the mixer unit and the first mixed water, a sixth step of transferring the second mixed water mixed by the line mixer to the catalytic oxidation reaction unit, a second step introduced into the catalytic oxidation reaction unit It may include a seventh step of oxidizing the mixed water and an eighth step of discharging the treated water treated in the catalytic oxidation reaction unit to the outside.

The gas-liquid mixing unit of the water treatment method using the high-efficiency large-capacity ozone generator according to an embodiment of the present invention includes a mixing pump unit for mixing the ozone moved from the ozone generator and the treated water moved from the catalytic oxidation reaction unit; Ultra-fine bubble generation for generating the first mixed water, which is the secondary mixed water, by mixing ultra-fine bubbles with the primary mixed water moved from the mixing pump unit while being disposed between the mixing pump unit and the main line unit The third step comprises: a 3-1 step of transferring the treated water from the catalytic oxidation reaction unit to the mixing pump unit; a 3-2 step of transferring ozone from the ozone generating unit to the mixing pump unit; Step 3-3 of mixing the ozone and the treated water introduced by the mixing pump unit, Step.3-4 of transferring the primary mixed water mixed by the mixing pump unit to the ultrafine bubble generating unit, the Step 3-5 of mixing ultra-fine bubbles with the primary mixed water introduced into the ultra-fine bubble generating unit, and Step 3-6 of transferring the secondary mixed water mixed by the ultra-fine bubble generating unit to the main line unit may include

The water treatment system using the high-efficiency large-capacity ozone generator of the water treatment method using the high-efficiency large-capacity ozone generator according to an embodiment of the present invention is disposed between the flow rate adjustment unit and the line mixer unit, and is moved through the line mixer unit. Further comprising an ejector unit for mixing miscellaneous wastewater and ozone moved from the ozone generating unit, wherein the second step is a 2-1 step of transferring the miscellaneous wastewater in the flow rate adjusting unit through the main line unit to the ejector unit, the ozone generation A second step of transferring ozone generated from the unit to the ejector unit, a second step of 2-3 mixing the waste water and ozone by the ejector unit, and a first step of transferring the mixed waste water mixed by the ejector unit to the line mixer unit 2-4, wherein the ozone generating unit may supply a first portion of the generated ozone to the ejector unit, and the remaining second portion of the first portion may be supplied to the mixing pump unit.

The first part of the water treatment method using the high-efficiency large-capacity ozone generator according to an embodiment of the present invention may be 3.7/5.5 of the generated ozone, and the second part may be 1.8/5.5 of the generated ozone.

In the water treatment system using the high-efficiency large-capacity ozone generator of the water treatment method using the high-efficiency large-capacity ozone generator according to an embodiment of the present invention, the catalytic oxidation reaction unit and the mixing pump unit are connected to each other, and the treatment in the catalytic oxidation reaction unit A first inflow pipe for allowing a portion of water to flow into the mixing pump unit, and connecting the ozone generating unit and the mixing pump unit to allow the second portion of ozone generated from the ozone generating unit to flow into the mixing pump unit. and a pipe and a mixing pipe connecting the mixing pump unit and the main line unit, wherein the mixing pump unit includes a first pump and a second pump, and the discharge pipe includes the catalytic oxidation reaction unit and the first a first discharge pipe connecting the pump and a second discharge pipe branching from the first discharge pipe and connected to the second pump, wherein the first inlet pipe includes a first first connecting the ozone generator and the second pump a first inlet pipe and a 1-2 inlet pipe branched from the 1-1 inlet pipe and connected to the first pump, wherein the mixing pipe includes a first first pump connecting the first pump and the main line a mixing pipe and a second mixing pipe connecting the second pump and the main line part, wherein the ultrafine bubble generating unit is installed in the first mixing pipe and moved from the first pump to the main line part A first bubble generating piece that mixes ultra-fine bubbles with the primary mixed water and a second bubble that is installed in the second mixing pipe to mix ultra-fine bubbles with the primary mixed water that is moved from the second pump to the main line unit A production piece is provided, and the step 3-1 includes the step 3-1-1 and the second step of transferring a portion of the treated water in the catalytic oxidation reaction unit to the first pump through the first discharge pipe. and a 3-1-2 step of transferring a portion of the treated water in the catalytic oxidation reaction unit to the second pump through a discharge pipe, wherein the 3-2 step is performed through the 1-1 inlet pipe Step 3-2-1 of transferring a portion of ozone generated from the ozone generator to the second pump; and and a 3-2-2 step of transferring a portion of the ozone generated from the ozone generating unit to the first pump through the 1-2 inlet pipe, wherein the 3-4 step includes the first Step 3-4-1 of transferring the primary mixed water mixed by the pump to the first bubble generating piece through the first mixing pipe and the primary mixed water mixed by the second pump, the and a step 3-4-2 of transferring the second bubble generating piece to the second bubble generating piece through a second mixing pipe, wherein the 3-6 step is the second mixing water mixed by the first bubble generating piece. A third step of transferring the secondary mixed water mixed by the second bubble generating piece to the main line unit through the second mixing pipe in a third step 3-6-1 of transferring to the main line part through the first mixing pipe -6-2 may be included.

The ejector part of the water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention includes a plurality of ejector pieces, and the gas-liquid mixing unit includes a plurality of gas-liquid numbers corresponding to each of the plurality of ejector pieces on a one-to-one basis. It is composed of a mixing piece, and the ozone generating unit may supply the generated ozone to the plurality of ejector pieces and the plurality of gas-liquid mixing pieces.

The line mixer part of the water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention is composed of a first line mixer piece, a second line mixer piece, and a third line mixer piece connected in parallel with the flow rate adjusting unit, , The ejector unit includes a first ejector piece disposed between the flow rate adjusting unit and the first line mixer piece, a second ejector piece disposed between the flow rate adjusting unit and the second line mixer piece, and the flow rate adjusting unit and the third Consisting of a third ejector piece disposed between the line mixer pieces, the water treatment system using the high-efficiency large-capacity ozone generator connects the ozone generator and the mixing pump to remove the ozone generated from the ozone generator. and a second inlet pipe for allowing one portion to be introduced into the plurality of ejector pieces, wherein in step 2-2, a portion of ozone generated from the ozone generating unit is transferred to the first ejector through the second inlet pipe. Step 2-2-1 of transferring to one side, step 2-2-2 of transferring a part of ozone generated from the ozone generator to the second ejector piece through the second inlet pipe, and the ozone generator It may include a step 2-2-3 of transferring a portion of ozone generated from the second inlet pipe to the third ejector piece.

The water treatment system using the high-efficiency large-capacity ozone generator of the water treatment method using the high-efficiency large-capacity ozone generator according to an embodiment of the present invention is disposed between the flow rate adjusting unit and the line mixer, and from the flow rate adjusting unit to the line mixer A pressurized dissolution pump unit implementing the movement of miscellaneous waste to the unit, and a flow rate measuring unit disposed between the pressurized dissolving pump unit and the line mixer unit to measure the flow rate of miscellaneous waste water moved to the line mixer unit by the pressurized dissolution pump unit further Including, wherein the pressure dissolution pump unit, A first pressure dissolving pump piece disposed between the flow rate adjusting unit and the first line mixer piece, and a second pressure dissolving pump piece disposed between the flow rate adjusting unit and the second line mixer piece and a third pressurized dissolution pump piece disposed between the flow rate adjusting unit and the third line mixer piece, and the miscellaneous waste water collected in the flow rate adjusting unit is branched into each line mixer piece by each pressurized dissolving pump piece. Moving, the flow rate measurement unit is disposed between the first pressure dissolving pump piece and the first line mixer piece disposed between the first flow rate measuring piece, the second pressure dissolving pump piece and the second line mixer piece A second flow rate measurement piece and a third flow rate measurement piece disposed between the third pressure dissolution pump piece and the third line mixer piece, the water treatment system using the high-efficiency large-capacity ozone generator, Further comprising a control unit for changing the ozone supply amount from the ozone generating unit to the first line mixer piece, the second line mixer piece, and the third line mixer piece based on the flow rate information measured by the ozone generator, The unit generates ozone of a preset capacity, and the step 2-2 includes a step 2-2a of measuring the flow rate of miscellaneous wastewater moving to the first line mixer piece through the first flow rate measurement piece, the step 2-2a, the Step 2-2b of measuring the flow rate of the miscellaneous waste water moving to the second line mixer piece through the second flow rate measuring piece, the flow rate of the miscellaneous waste water moving to the third line mixer piece through the third flow rate measuring piece Step 2-2c of measuring and the first flow obtained by the first flow measurement piece in the ozone generating unit to obtain a quantity value, a second flow rate value obtained by the second flow rate measurement piece, and a third flow rate value obtained by the third flow rate measurement piece, and match the ratio of the obtained flow rate values A 2-2d step of dividing the first portion of the generated ozone may be included.

The control unit of the water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention includes, based on the flow rate information measured by the flow rate measurement unit, the first mixing pump piece, the second a first main line piece connecting the flow rate adjusting unit and the first line mixer piece, the flow rate adjusting unit and the second It consists of a second main line piece connecting the line mixer piece and a third main line piece connecting the flow rate adjusting unit and the third line mixer piece, wherein the gas-liquid mixing unit supplies mixed water to the first main line piece. a first gas-liquid mixing piece, a second gas-liquid mixing piece for supplying mixed water to the second main line piece, and a third gas-liquid mixing piece for supplying mixed water to the third main line piece, the first gas-liquid mixing piece The mixing piece includes a first mixing pump piece and a first ultra-fine bubble generating piece, the second gas-liquid mixing piece includes a second mixing pump piece and a second ultra-fine bubble generating piece, and the third gas-liquid mixing piece The mixing piece includes a third mixing pump piece and a third ultra-fine bubble generating piece, and in step 3-2, the flow rate of miscellaneous wastewater moved to the first line mixer piece through the first flow rate measuring piece Step 3-2a of measuring 3 A 3-2c step of measuring the flow rate of the miscellaneous wastewater moving to the line mixer piece, and a first flow rate value obtained by the first flow rate measurement piece, a second flow rate value obtained by the second flow rate measurement piece, and the a 3-2d step of acquiring a third flow rate value obtained by the third flow rate measurement piece, and dividing the second portion of the ozone generated by the ozone generator to match the ratio of the obtained flow rate value can do.

In the water treatment system using the high-efficiency large-capacity ozone generator of the water treatment method using the high-efficiency large-capacity ozone generator according to an embodiment of the present invention, the mixing tank unit in which the treated water purified by the catalytic oxidation reaction unit is collected and the catalytic oxidation reaction It is disposed between the unit and the mixing tank, and further includes a water level control unit for adjusting the water level of the catalytic oxidation reaction unit, wherein the catalytic oxidation reaction unit includes a water tank unit in which the mixed water moved from the line mixer is accommodated, the water tank unit A first cylindrical portion formed in a cylindrical shape with an open upper portion, disposed on the lower side of the cylindrical portion, and providing a passage for discharging a portion of the treated water oxidized in the water tank to the water level control portion A passage providing unit, disposed on the lower side of the cylindrical portion, a second passage providing portion providing a passage for discharging a portion of the oxidized treated water in the water tank to the gas-liquid mixing unit, and an upper side of the water tank and a scup removal unit for removing the floating scum generated by the oxidation reaction of the mixed water in the water tank unit, wherein the water level control unit includes a receiving unit for receiving the treated water discharged from the passage providing unit, the passage agent It has a treated water inlet that allows the treated water to flow into the accommodating part while connected to the study and a treated water outlet that allows the treated water to flow out into the blending tank while connected to the mixing tank, and the treatment treated in the catalytic oxidation reaction unit A ninth step of transferring water to the water level control unit and a tenth step of transferring the treated water in the water level control unit to the mixing tank may be further included.

According to the present invention, it is possible to supply ozone to sewage treatment devices connected in parallel through one high-efficiency and large-capacity ozone generator, and to implement purification of wastewater using ozone.

In addition, by distributing ozone generated from the ozone generator to an ejector or a gas-liquid mixing pump, it is possible to implement sewage treatment by ozone with an optimized system.

In addition, it is possible to reduce unnecessary use of ozone and to utilize ozone more efficiently by changing the amount of ozone according to the flow rate of the introduced miscellaneous wastewater.

1 is a flowchart for explaining a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention.
2 is a piping and instrumentation diagram illustrating a water treatment system using a high-efficiency large-capacity ozone generator used in a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention.
3 is a piping and instrumentation diagram illustrating a part of a water treatment system using a high-efficiency large-capacity ozone generator used in a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention.
4 is a schematic diagram for explaining a control unit of a water treatment system using a high-efficiency large-capacity ozone generator used in a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention;
5 is a schematic view showing a catalytic oxidation reaction part of a water treatment system using a high-efficiency large-capacity ozone generator used in a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention;
6 is a schematic diagram showing a line mixer of a water treatment system using a high-efficiency large-capacity ozone generator used in a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention;

Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings. However, the spirit of the present invention is not limited to the presented embodiments, and those skilled in the art who understand the spirit of the present invention may add, change, delete, etc. other elements within the scope of the same spirit, and may use other degenerative inventions or the present invention. Other embodiments included within the scope of the invention may be easily proposed, but this will also be included within the scope of the invention.

In addition, components having the same function within the scope of the same idea shown in the drawings of each embodiment will be described using the same reference numerals.

Water treatment system using high-efficiency large-capacity ozone generator

2 is a piping and instrumentation diagram showing a water treatment system using the high-efficiency large-capacity ozone generator of the present invention, and FIG. 3 is a piping and instrumentation diagram illustrating a part of the water treatment system using the high-efficiency large-capacity ozone generator of the present invention.

In addition, Figure 4 is a block diagram for explaining the control unit of the water treatment system using the high-efficiency large-capacity ozone generator of the present invention.

2 to 4 , a water treatment system 1 using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention is a high-efficiency, large-capacity ozone for treating miscellaneous wastewater collected from a distribution tank through a microfilter to a flow rate control tank. It is a water treatment system (1) using a generator.

The water treatment system 1 using the high-efficiency large-capacity ozone generator includes a flow rate adjustment unit 10, a line mixer unit 20, a main line unit (ML), a gas-liquid mixing unit 30, an ozone generating unit 40, and contact oxidation. It may include a reaction unit 50 , a pressure dissolution pump unit 60 , a flow rate measurement unit 70 , and an ejector unit 80 .

The flow rate adjusting unit 10 is a kind of water tank that forms an accommodating space therein while being formed of a PVC material, and miscellaneous water can be collected.

Here, the miscellaneous wastewater may be sewage that has been subjected to a microfilter in the raw water treated with secondary precipitation received in the distribution tank.

The line mixer unit 20 is connected to the flow rate adjusting unit 10 , and may mix the miscellaneous waste water moved from the flow rate adjusting unit 10 and ultra-fine bubbles including ozone. Here, ozone may be supplied from the ozone generator 40 .

The line mixer unit 20 generates ultra-fine bubbles to increase the surface area and quantity of bubbles, and increases the dissolved amount, and the ultra-fine bubbles, unlike coarse bubbles, have a very slow floating speed, so the contact time increases as the residence time increases. This increases so that the oxidation effect is increased even when the same amount of ozone bubbles are mixed in water.

The main line unit ML may connect the flow rate adjusting unit 10 and the line mixer unit 20 . The main line unit ML may be a pipe that moves the miscellaneous waste water in the flow rate adjusting unit 10 to the line mixer unit 20 .

The gas-liquid mixing unit 30 may supply mixed water in which ozone and ultrafine bubbles are mixed to the main line unit ML.

The gas-liquid mixing unit 30 supplies mixed water to the front end of the line mixer unit 20, so that miscellaneous water and mixed water moving through the main line unit ML are mixed, and the line mixer unit 20 ) can be moved to

The gas-liquid mixing unit 30 may include a mixing pump unit 31 and an ultrafine bubble generating unit 33 .

The mixing pump unit 31 may mix the ozone transferred from the ozone generator 40 and the treated water transferred from the catalytic oxidation reaction unit 50 .

The mixing pump unit 31 is a device for injecting ozone into the liquid, and by injecting a gas, that is, ozone, into the pumped liquid at high speed and high pressure, a large amount of ozone is injected and mixed, so that organic substances in water quality In addition to making it possible to make good contact with the water, it is possible to maximize the water treatment efficiency by increasing the dissolution rate of ozone in water by generating microbubbles.

The ultra-fine bubble generating unit 33 is disposed between the mixing pump unit 31 and the main line unit ML, and ultra-fine bubbles are added to the primary mixed water moved from the mixing pump unit 31 . It may be provided with an ultra-fine bubble generating unit 33 for generating secondary mixed water by mixing.

The mixed water supplied to the line mixer 20 by the gas-liquid mixing unit 30 is the secondary mixed water that has passed through the ultrafine bubble generating unit 33 . In addition, the primary mixed water is mixed water in which the treated water moved from the catalytic oxidation reaction unit 50 and the ozone moved from the ozone generator 40 are mixed.

The ozone generating unit 40 may generate ozone and supply the generated ozone to the gas-liquid mixing unit 30 . The ozone generator 40 may generate ozone by discharging oxygen supplied in a discharge tube type.

In addition, the ozone generator 40 preferably generates ozone with a large capacity of up to 16.5 kg/hr, and may generate ozone with a capacity smaller than 16.5 kg/hr according to a user's setting.

The catalytic oxidation reaction unit 50 may oxidize the contaminants in the mixed water moved from the line mixer unit 20 while being connected to the line mixer unit 20 . The catalytic oxidation reaction unit 50 will be described in detail below with reference to FIG. 5 .

The pressurized dissolution pump unit 60 is disposed between the flow rate adjusting unit 10 and the line mixer unit 20 to implement the movement of miscellaneous waste water from the flow rate adjusting unit 10 to the line mixer unit 20 . .

The flow rate measurement unit 70 is disposed between the pressure dissolution pump unit 60 and the line mixer unit 20, and is moved to the line mixer unit 20 by the pressure dissolution pump unit 60 It is possible to measure the flow rate of miscellaneous wastewater.

The ejector unit 80 is disposed between the pressurized dissolution pump unit 60 and the line mixer unit 20, and the miscellaneous wastewater moved by the pressurized dissolution pump unit 60 and the ozone generating unit 40 Ozone transferred from can be mixed.

The ozone generating unit 40 may supply a first portion of the generated ozone to the ejector unit 80 , and the remaining second portion of the first portion may be supplied to the mixing pump unit 31 .

Specifically, the ozone generating unit 40 generates ozone of a preset capacity within a predetermined time, and at this time, a first portion of the total ozone generated for a predetermined time is supplied to the ejector unit 80 , and out of the total ozone A second portion other than the first portion may be supplied to the mixing pump unit 31 .

Preferably, the first portion may be 3.7 / 5.5 of the generated ozone, and the second portion may be 1.8 / 5.5 of the generated ozone.

In addition, the water treatment system 1 using the high-efficiency large-capacity ozone generator of the present invention may further include an outlet pipe (OP), a first inlet pipe (IP-1), and a mixing pipe (MP).

The discharge pipe OP connects the catalytic oxidation reaction unit 50 and the mixing pump unit 31 so that a portion of the treated water in the catalytic oxidation reaction unit 50 is transferred to the mixing pump unit 31 . can be brought in.

The first inlet pipe IP-1 connects the ozone generating unit 40 and the mixing pump unit 31 so that the second portion of ozone generated from the ozone generating unit 40 is mixed. It may be introduced into the pump unit 31 .

The mixing pipe MP may connect the mixing pump 31 and the main line ML.

The mixing pump unit 31 may include a first pump 311 and a second pump 312 .

The discharge pipe (OP) is branched from the first discharge pipe (OP-1) and the first discharge pipe (OP-1) connecting the catalytic oxidation reaction unit (50) and the first pump (311). 2 A second discharge pipe OP-2 connected to the pump 312 may be provided.

The treated water discharged from the catalytic oxidation reaction unit 50 flows into the first pump 311 through the first discharge pipe OP-1, and through the second discharge pipe OP-2, the second It flows into the pump 312 .

The first inlet pipe (IP-1) includes a 1-1 inlet pipe (IP-1a) and a 1-1 inlet pipe (IP-1a) connecting the ozone generator 40 and the second pump 312 ( A 1-2 inlet pipe (IP-1b) branched from IP-1a) and connected to the first pump 311 may be provided.

The ozone generator 40 supplies 1/2 of the second portion of the generated ozone to the 1-1 inlet pipe (IP-1a), and the other 1/2 is the 1-2 inflow pipe ( IP-1b) is supplied. Preferably, the ozone generator 40 supplies 0.9 / 5.5 to the 1-1 inlet pipe IP-1a, and 0.9 / 5.5 to the 1-2 inlet pipe IP-1b. can supply

The mixing pipe MP includes a first mixing pipe MP-1 connecting the first pump 311 and the main line part ML, and the second pump 312 and the main line part ML. ) may be provided with a second mixing pipe (MP-2) for connecting the.

The ultrafine bubble generating unit 33 is installed in the first mixing pipe MP-1, and superfines the primary mixed water moved from the first pump 311 to the main line unit ML. It is installed in the first bubble generating piece 331 and the second mixing pipe MP-2 for mixing the fabric, and is supplied to the primary mixed water moving from the second pump 312 to the main line part ML. A second bubble generating piece 332 for mixing ultra-fine bubbles may be provided.

On the other hand, the ejector unit 80 may be composed of a plurality of ejector pieces.

The gas-liquid mixing unit 30 may be composed of a plurality of gas-liquid mixing pieces in a number corresponding to each of the plurality of ejector pieces one-to-one.

The gas-liquid mixing unit 30 is configured to supply mixed water to the first gas-liquid mixing piece 30a for supplying mixed water to the first main line piece ML-1, and the second main line piece ML-2. It may be composed of a second gas-liquid mixing piece 30b and a third gas-liquid mixing piece 30c for supplying mixed water to the third main line piece ML-3.

The main line part ML includes a first main line piece ML-1 connecting the first line mixer piece 20a and the first gas-liquid mixing piece 30a, and the second line mixer piece 20b. ) and a second main line piece ML-2 connecting the second gas-liquid mixing piece 30b, and a third main connecting the third line mixer piece 20c and the third gas-liquid mixing piece 30c. It may be composed of a line piece ML-3.

The first gas-liquid mixing piece 30a includes a first mixing pump piece 31a and a first ultrafine bubble generating piece 33a, and the second gas-liquid mixing piece 30b includes a second mixing pump piece. 31b and a second ultrafine bubble generating piece 33b, wherein the third gas-liquid mixing piece 30c includes a third mixing pump piece 31c and a third ultrafine bubble generating piece 33c can do.

The line mixer unit 20 may include a first line mixer piece 20a , a second line mixer piece 20b , and a third line mixer piece 20c connected in parallel with the flow rate adjusting unit 10 . .

The ozone generator 40 may supply the generated ozone to the plurality of ejector pieces and the plurality of gas-liquid mixing pieces.

The pressure dissolution pump unit 60 includes a first pressure dissolution pump piece 60a disposed between the flow rate adjusting unit 10 and the first line mixer piece 20a, the flow rate adjusting unit 10 and the second A second pressure dissolution pump piece 60b disposed between the line mixer pieces 20b and a third pressure dissolution pump piece 60c disposed between the flow rate adjusting unit 10 and the third line mixer piece 20c. can be configured.

The miscellaneous waste water collected in the flow rate adjusting unit 10 may be branched and moved to each line mixer piece by each pressurized dissolution pump piece. At this time, the miscellaneous waste water may pass through each ejector piece before being moved to each line mixer piece.

The ejector part 80 includes a first ejector piece 80a and a second pressure dissolution pump piece 60b disposed between the first pressurized dissolution pump piece 60a and the first line mixer piece 20a. and a second ejector piece 80b disposed between the second line mixer piece 20b and a third ejector piece disposed between the third pressure dissolution pump piece 60c and the third line mixer piece 20c. (80c) may consist of.

The water treatment system 1 using the high-efficiency large-capacity ozone generator of the present invention may further include a second inlet pipe IP-2.

The second inlet pipe IP-2 connects the ozone generating unit 40 and the mixing pump unit 31 so that the first part of the ozone generated from the ozone generating unit 40 is divided into a plurality of units. It can be made to flow into the ejector side.

The ozone generator 40 generates ozone of a preset capacity, and transfers the first portion of the generated ozone to the first ejector piece 80a, the second ejector piece 80b, and the third ejector piece. (80c) can be divided and supplied.

The second inlet pipe IP-2 is branched to the first ejector piece 80a, the second ejector piece 80b, and the third ejector piece 80c to supply ozone.

The flow rate measuring unit 70 includes a first flow rate measuring piece 70a and a second pressure dissolving pump piece disposed between the first pressure dissolving pump piece 60a and the first line mixer piece 20a ( 60b) and a second flow rate measurement piece 70b disposed between the second line mixer piece 20b, and the third pressure dissolution pump piece 60c and the third line mixer piece 20c disposed between the second piece 20c. It may be composed of three flow measurement pieces (70c).

The water treatment system 1 using the high-efficiency large-capacity ozone generator of the present invention may further include a control unit 95 .

The control unit 95 includes the first line mixer piece 20a and the second line mixer piece 20b from the ozone generator 40 based on the flow rate information measured by the flow rate measurement unit 70 . ) and the amount of ozone supplied to the third line mixer piece 20c can be changed.

The ozone generator 40 may generate ozone of a preset capacity.

The control unit 95 is configured to match the ratio of the flow rate values measured by the first flow rate measurement piece 70a, the second flow rate measurement piece 70b, and the third flow rate measurement piece 70c, so that the ozone The ozone generated by the generator 40 may be divided and supplied to the first ejector piece 80a, the second ejector piece 80b, and the third ejector piece 80c.

Meanwhile, the water treatment system 1 using the high-efficiency large-capacity ozone generator of the present invention may further include a mixing tank 91 and a water level adjusting unit 92 .

In the mixing tank unit 91 , the treated water purified by the catalytic oxidation reaction unit 50 may be collected.

The water level control unit 92 may adjust the water level of the catalytic oxidation reaction unit 50 while being disposed between the catalytic oxidation reaction unit 50 and the mixing tank unit 91 .

The catalytic oxidation reaction unit 50 includes a first oxidation reaction piece 50a connected to the first line mixer piece 20a, and a second oxidation reaction piece 50b connected to the second line mixer piece 20b. ) and a third oxidation reaction piece 50c connected to the third line mixer piece 20c.

The water level control unit 92 includes a first water level control piece 92a disposed between the first oxidation reaction piece 50a and the mixing tank unit 91, the second oxidation reaction piece 50b and the mixture. It may be composed of a second water level adjusting piece 92b disposed between the tank parts 91 and a third water level adjusting piece 92c disposed between the third oxidation reaction piece 50c and the mixing tank part 91 . .

The water treatment system 1 using the high-efficiency large-capacity ozone generator of the present invention is disposed between the first water level control piece 92a and the mixing tank 91, and is moved from the first water level control piece 92a. It may further include a filter media contact unit 93 for purifying the treated water through the received contact media.

The filter media contact unit 93 may purify the treated water moved through the accommodated media. Here, the filter medium may be silica (SiO2), alumina (Al2O3), loess, and the like.

In addition, the filter media exhibits functions such as substitution and adsorption of oxidized ions, adsorption and removal of fine particles, a binder role and ion substitution function to maintain the wet strength of the filter itself, alkalinizing acidic wastewater/wastewater, It has functions such as neutralizing function expression and foaming agent for forming micropores.

5 is a schematic diagram illustrating a catalytic oxidation reaction unit of a water treatment system using the high-efficiency, large-capacity ozone generator of the present invention.

Referring to FIG. 5 , the catalytic oxidation reaction unit 50 of the water treatment system 1 using the high-efficiency large-capacity ozone generator of the present invention includes a water tank unit 51 , a cylindrical unit 53 , and a first passage providing unit 55 . ), a second passage providing unit 57 , a scum removal unit 58 and an exhaust ozone treatment unit 59 may be provided.

The water tank 51 may receive the mixed water moved from the line mixer 20 .

The cylindrical part 53 is located in the water tank part 51, and may be formed in a cylindrical shape with an open top.

The mixed water moved to the catalytic oxidation reaction unit 50 through the line mixer unit 20 may be introduced from the open upper part of the cylindrical part 53 toward the bottom surface of the cylindrical part 53 . .

The mixed water introduced into the cylindrical part 53 is reflected on the bottom surface of the cylindrical part 53 , and discharged to the open outside of the cylindrical part 53 , and is accommodated in the water tank 51 and comes into contact with it. An oxidation reaction may be performed in the oxidation reaction unit 50 . Here, the cylindrical part 53 may ensure a residence time in the water tank part 51 of the mixed water introduced into the water tank part 51 .

The first passage providing part 55 is disposed on the lower side of the cylindrical part 53 and discharges a portion of the treated water oxidized in the water tank 51 to the water level adjusting part 92 . can provide a pathway to

The second passage providing part 57 is disposed on the lower side of the cylindrical part 53 and discharges a portion of the treated water oxidized in the water tank 51 to the gas-liquid mixing part 30 . can provide a pathway to

The scum removal unit 58 is located on the upper side of the water tank unit 51 , and may remove scum floating due to oxidation reaction of the mixed water in the water tank unit 51 .

The ozone treatment unit 59 may be formed on the upper side of the water tank 51 to discharge the ozone in the water tank 51 to the outside.

The water level control unit 92 may include a receiving unit 921 , a treated water inlet 923 , and a treated water outlet 925 .

The accommodating part 921 may receive the treated water discharged from the passage providing part.

The treated water inlet 923 may allow the treated water to flow into the receiving portion 921 while being connected to the passage providing unit.

The treated water outlet 925 may allow the treated water to flow out into the mixing tank 91 while being connected to the mixing tank 91 .

6 is a schematic diagram illustrating a line mixer of a water treatment system using the high-efficiency large-capacity ozone generator of the present invention.

Referring to FIG. 6 , the line mixer 20 of the water treatment system 1 using the high-efficiency large-capacity ozone generator of the present invention, the line mixer 20 includes ozone, ultra-fine bubbles and miscellaneous water introduced into the inlet. It may be composed of a plurality of curved pipes to be mixed.

The plurality of bent pipes is composed of a direction reversing pipe 211 for reversing the direction, and a composite reversing pipe 213 for reversing the direction and lowering the height, three direction reversing pipes 211a, 211b, 211c and It may be composed of two composite inverting pipes (213a, 213b).

Accordingly, in the line mixer unit 20, while the plurality of curved pipes are formed in three stages, the miscellaneous wastewater introduced from the upper part moves downward while passing through the direction reversing pipe 211 and the complex reversing pipe 213. It can be mixed with ozone and ultra-fine bubbles in the process.

Water treatment method using high-efficiency large-capacity ozone generator

1 is a flowchart illustrating a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention.

Referring to FIG. 1 , a water treatment method using a high-efficiency large-capacity ozone generator according to an embodiment of the present invention may be implemented using a water treatment system 1 using a high-efficiency large-capacity ozone generator.

The water treatment system 1 using the high-efficiency large-capacity ozone generator may be the water treatment system 1 using the high-efficiency large-capacity ozone generator described with reference to FIGS. 2 to 6 .

The sewage treatment method of the present invention may include a first step (S1) to an eighth step (S8).

The first step (S1) is a step of collecting in the flow rate adjusting unit 10 miscellaneous wastewater that has passed through the microfilter from the distribution tank.

The second step (S2) is a step of transferring the waste water in the flow rate adjusting unit 10 to the line mixer unit 20 through the main line unit.

The second step (S2) may include steps 2-1 to 2-4.

The step 2-1 is a step of transferring the waste water in the flow rate adjusting unit 10 through the main line unit to the ejector unit 80 .

Step 2-2 is a step of transferring ozone generated from the ozone generating unit 40 to the ejector unit 80 .

In addition, step 2-2 may include steps 2-2-1 to 2-2-3.

Step 2-2-1 is a step of transferring a portion of ozone generated from the ozone generator 40 to the first ejector piece 80a through the second inlet pipe.

Step 2-2-2 is a step of transferring a portion of ozone generated from the ozone generator 40 to the second ejector piece 80b through the second inlet pipe.

Step 2-2-3 is a step of transferring a portion of ozone generated from the ozone generator 40 to the third ejector piece 80c through the second inlet pipe.

In addition, step 2-2 may include steps 2-2a to 2-2d.

The step 2-2a is a step of measuring the flow rate of the miscellaneous waste water moving to the first line mixer piece 20a through the first flow rate measuring piece 70a.

The step 2-2b is a step of measuring the flow rate of the miscellaneous wastewater moving to the second line mixer piece 20b through the second flow rate measuring piece 70b.

The step 2-2c is a step of measuring the flow rate of the miscellaneous wastewater moving to the third line mixer piece 20c through the third flow rate measuring piece 70c.

The step 2-2d includes a first flow rate value obtained by the first flow rate measurement piece 70a, a second flow rate value obtained by the second flow rate measurement piece 70b, and the third flow rate measurement piece Obtaining the third flow rate value obtained in step 70c, and dividing the first portion of the ozone generated by the ozone generator 40 so as to match the ratio of the obtained flow rate value.

Step 2-3 is a step of mixing miscellaneous wastewater and ozone by the ejector unit 80 .

The step 2-4 is a step of transferring the miscellaneous waste water mixed by the ejector unit 80 to the line mixer unit 20 .

The third step (S3) is a step of generating the first mixed water in which ozone and ultra-fine bubbles are mixed through the gas-liquid mixing unit 30 .

The third step S3 may include steps 3-1 to 3-6.

Step 3-1 is a step of transferring treated water from the catalytic oxidation reaction unit 50 to the mixing pump unit 31 .

In addition, in step 3-1, a portion of the treated water in the catalytic oxidation reaction unit 50 is transferred to the first pump 311 through the first discharge pipe OP-1. Step 1 and Step 3-1-2 of transferring a portion of the treated water in the catalytic oxidation reaction unit 50 to the second pump 312 through the second discharge pipe OP-2. have.

Step 3-2 is a step of transferring ozone from the ozone generating unit 40 to the mixing pump unit 31 .

In addition, in step 3-2, a portion of ozone generated from the ozone generator 40 is transferred to the second pump 312 through the 1-1 inlet pipe IP-1a. Step 3-2-1 and a 3-2 step in which a part of ozone generated from the ozone generator 40 is transferred to the first pump 311 through the 1-2 inlet pipe IP-1b -2 may be included.

In addition, step 3-2 may include steps 3-2a to 3-2d.

The step 3-2a is a step of measuring the flow rate of the miscellaneous wastewater moving to the first line mixer piece 20a through the first flow rate measuring piece 70a.

The step 3-2b is a step of measuring the flow rate of the miscellaneous wastewater moving to the second line mixer piece 20b through the second flow rate measuring piece 70b.

The step 3-2c is a step of measuring the flow rate of the miscellaneous waste water moving to the third line mixer piece 20c through the third flow rate measuring piece 70c.

The step 3-2d includes a first flow rate value obtained by the first flow rate measurement piece 70a, a second flow rate value obtained by the second flow rate measurement piece 70b, and the third flow rate measurement piece Obtaining the third flow rate value obtained by step (70c), and dividing the second portion of the ozone generated by the ozone generator 40 so as to match the ratio of the obtained flow rate value.

Step 3-3 is a step of mixing the ozone and the treated water introduced by the mixing pump unit 31 .

Step 3-4 is a step of transferring the primary mixed water mixed by the mixing pump unit 31 to the ultrafine bubble generating unit 33 .

In addition, in step 3-4, the primary mixed water mixed by the first pump 311 is transferred to the first bubble generating piece 331 through the first mixing pipe MP-1. The first mixing water mixed by the step 3-4-1 and the second pump 312 is transferred to the second bubble generating piece 332 through the second mixing pipe MP-2. Step 3-4-2 may be included.

Step 3-5 is a step of mixing ultra-fine bubbles with the primary mixing water introduced into the ultra-fine bubble generating unit 33 .

Step 3-6 is a step of transferring the secondary mixed water mixed by the ultrafine bubble generating unit 33 to the main line unit.

In addition, in step 3-6, the secondary mixed water mixed by the first bubble generating piece 331 is transferred to the main line part through the first mixing pipe MP-1. -1 and a 3-6-2 step of transferring the secondary mixed water mixed by the second bubble generating piece 332 to the main line part through the second mixing pipe MP-2 can

The fourth step (S4) is a step of supplying the first mixed water generated by the gas-liquid mixing unit 30 to the main line unit.

The fifth step (S5) is a step of mixing the miscellaneous waste water introduced into the line mixer unit 20 and the first mixed water.

The sixth step S6 is a step of transferring the second mixed water mixed by the line mixer 20 to the catalytic oxidation reaction unit 50 .

The seventh step ( S7 ) is a step of oxidizing the second mixed water introduced into the catalytic oxidation reaction unit 50 .

The eighth step (S8) is a step of discharging the treated water treated in the catalytic oxidation reaction unit 50 to the outside.

In the above, the configuration and features of the present invention have been described based on the embodiments according to the present invention, but the present invention is not limited thereto, and it is understood that various changes or modifications can be made within the spirit and scope of the present invention. It is intended that such changes or modifications will be apparent to those skilled in the art, and therefore fall within the scope of the appended claims.

S1: first step
S2: second step
S3: Step 3
S4: Step 4
S5: Step 5
S6: Step 6
S7: Step 7
S8: Step 8
1: Water treatment system using high-efficiency large-capacity ozone generator
10: flow control unit
20: line mixer unit
ML: Main line
OP: exhaust pipe
IP-1: first inlet pipe
IP-2: 2nd inlet pipe
MP: Mixed pipe
30: gas-liquid mixing unit
40: ozone generating unit
50: catalytic oxidation reaction unit
60: pressure dissolution pump unit
70: flow measurement unit
80: ejector unit
91: mixed grandfather
92: water level control unit
921: receptacle
923: treated water inlet
925: treated water outlet
93: media contact part
95: control unit

Claims (10)

A flow rate adjusting unit for collecting waste water, a line mixer connected to the flow rate adjusting unit, and mixing ultra-fine bubbles including ozone and the miscellaneous waste water moved from the flow rate adjusting unit, a main line unit connecting the flow rate adjusting unit and the line mixer, the A gas-liquid mixing unit supplying mixed water in which ozone and ultrafine bubbles are mixed to the main line unit and an ozone generating unit supplying ozone and supplying the generated ozone to the gas-liquid mixing unit and connected to the line mixer unit, the line mixer unit A water treatment method using a high-efficiency large-capacity ozone generator using a water treatment system using a high-efficiency large-capacity ozone generator including a catalytic oxidation reaction unit for oxidizing and treating contaminants in mixed water transferred from
A first step of collecting waste water that has passed through the microfilter from the distribution tank to the flow rate adjusting unit;
a second step of transferring miscellaneous waste water in the flow rate adjustment unit to the line mixer unit through the main line unit;
a third step of generating a first mixed water in which ozone and ultra-fine bubbles are mixed through the gas-liquid mixing unit;
a fourth step of supplying the first mixed water generated by the gas-liquid mixing unit to the main line unit;
a fifth step of mixing the miscellaneous wastewater introduced into the line mixer and the first mixed water;
a sixth step of transferring the second mixed water mixed by the line mixer to the catalytic oxidation reaction unit;
a seventh step of oxidizing the second mixed water introduced into the catalytic oxidation reaction unit; and
An eighth step of discharging the treated water treated in the catalytic oxidation reaction unit to the outside;
The gas-liquid mixing unit,
a mixing pump unit for mixing the ozone moved from the ozone generator and the treated water moved from the catalytic oxidation reaction unit; and
Ultra-fine bubble generation for generating the first mixed water, which is the secondary mixed water, by mixing ultra-fine bubbles with the primary mixed water moved from the mixing pump unit while being disposed between the mixing pump unit and the main line unit have wealth,
The third step is
Step 3-1 of transferring the treated water from the catalytic oxidation reaction unit to the mixing pump unit;
A 3-2 step of transferring ozone from the ozone generating unit to the mixing pump unit;
Step 3-3 of mixing the treated water and ozone introduced by the mixing pump unit;
A step 3-4 of transferring the primary mixed water mixed by the mixing pump unit to the ultrafine bubble generating unit;
Steps 3-5 of mixing ultra-fine bubbles with the first mixing water introduced into the ultra-fine bubble generating unit; and
Steps 3-6 of transferring the secondary mixed water mixed by the ultrafine bubble generating unit to the main line unit,
The water treatment system using the high-efficiency large-capacity ozone generator,
It is disposed between the flow rate adjustment unit and the line mixer unit, and further comprises an ejector unit for mixing miscellaneous waste water moved through the line mixer unit and ozone moved from the ozone generating unit,
The second step is
Step 2-1 of transferring miscellaneous waste water in the flow rate adjustment unit to the ejector unit through the main line unit;
A 2-2 step of transferring the ozone generated from the ozone generating unit to the ejector unit;
Step 2-3 of mixing miscellaneous wastewater and ozone by the ejector unit; and
A step 2-4 of transferring the miscellaneous waste water mixed by the ejector unit to the line mixer unit,
The ozone generator,
A first portion of the generated ozone is supplied to the ejector unit, and the remaining second portion of the first portion is supplied to the mixing pump unit,
The ejector unit is composed of a plurality of ejector pieces,
The gas-liquid mixing unit is composed of a plurality of gas-liquid mixing pieces of a number corresponding to each of the plurality of ejector pieces one-to-one,
The ozone generator,
A water treatment method using a high-efficiency large-capacity ozone generator, characterized in that the generated ozone is supplied to the plurality of ejector pieces and the plurality of gas-liquid mixing pieces.
delete delete According to claim 1,
The first part is
3.7 / 5.5 of generated ozone,
The second part is
A water treatment method using a high-efficiency large-capacity ozone generator, characterized in that 1.8 / 5.5 of the generated ozone.
According to claim 1,
The water treatment system using the high-efficiency large-capacity ozone generator,
a discharge pipe connecting the catalytic oxidation reaction unit and the mixing pump unit so that a portion of the treated water in the catalytic oxidation reaction unit flows into the mixing pump unit;
a first inlet pipe connecting the ozone generator and the mixing pump to allow the second portion of ozone generated from the ozone generator to flow into the mixing pump; and
Further comprising a mixing pipe connecting the mixing pump unit and the main line unit,
The mixing pump unit is composed of a first pump and a second pump,
The exhaust pipe is
A first discharge pipe connecting the catalytic oxidation reaction unit and the first pump and a second discharge pipe branching from the first discharge pipe and connected to the second pump,
The first inlet pipe,
and a 1-1 inlet pipe connecting the ozone generator and the second pump and a 1-2 inlet pipe branching from the 1-1 inlet pipe and connected to the first pump,
The mixing pipe is
a first mixing pipe connecting the first pump and the main line unit and a second mixing pipe connecting the second pump and the main line unit;
The ultrafine bubble generating unit,
A first bubble generating piece installed in the first mixing pipe to mix ultrafine bubbles with the primary mixed water moving from the first pump to the main line unit and installed in the second mixing pipe, the second pump and a second bubble generating piece for mixing ultra-fine bubbles in the primary mixing water moved from the main line part,
The step 3-1 is,
Step 3-1-1 so that a portion of the treated water in the catalytic oxidation reaction unit is transferred to the first pump through the first discharge pipe; and
and a 3-1-2 step of transferring a portion of the treated water in the catalytic oxidation reaction unit to the second pump through the second discharge pipe,
The 3-2 step is,
Step 3-2-1 so that a portion of ozone generated from the ozone generator is transferred to the second pump through the 1-1 inlet pipe; and
and a 3-2-2 step of transferring a portion of the ozone generated from the ozone generator to the first pump through the 1-2 inlet pipe,
Steps 3-4 are,
A 3-4-1 step of transferring the primary mixed water mixed by the first pump to the first bubble generating piece through the first mixing pipe; and
A step 3-4-2 of transferring the primary mixed water mixed by the second pump to the second bubble generating piece through the second mixing pipe,
Steps 3-6 are,
Step 3-6-1 of transferring the secondary mixed water mixed by the first bubble generating piece to the main line part through the first mixing pipe; and
Water treatment using a high-efficiency large-capacity ozone generator, characterized in that it comprises a 3-6-2 step of transferring the secondary mixed water mixed by the second bubble generating piece to the main line part through the second mixing pipe. Way.
delete According to claim 1,
The line mixer unit,
It consists of a first line mixer piece, a second line mixer piece and a third line mixer piece connected in parallel with the flow rate adjusting unit,
The ejector unit,
A first ejector piece disposed between the flow rate adjusting unit and the first line mixer piece, a second ejector piece disposed between the flow rate adjusting unit and the second line mixer piece, and between the flow rate adjusting unit and the third line mixer piece Consists of a third ejector piece disposed,
The water treatment system using the high-efficiency large-capacity ozone generator,
and a second inlet pipe connecting the ozone generator and the mixing pump to allow the first portion of ozone generated from the ozone generator to flow into a plurality of ejector pieces,
The 2-2 step is,
A step 2-2-1 of transferring a portion of the ozone generated from the ozone generator to the first ejector piece through the second inlet pipe;
a step 2-2-2 of transferring a portion of the ozone generated from the ozone generator to the second ejector piece through the second inlet pipe; and
and a 2-2-3 step of transferring a portion of the ozone generated from the ozone generator to the third ejector piece through the second inlet pipe.
8. The method of claim 7,
The water treatment system using the high-efficiency large-capacity ozone generator,
A pressurized dissolution pump unit disposed between the flow rate adjusting unit and the line mixer unit to implement miscellaneous drainage movement from the flow rate adjusting unit to the line mixer unit; and
It is disposed between the pressure dissolution pump unit and the line mixer unit, further comprising a flow rate measuring unit for measuring the flow rate of miscellaneous waste water moved to the line mixer unit by the pressure dissolution pump unit,
The pressure dissolution pump unit,
A first pressurized dissolving pump piece disposed between the flow rate adjusting unit and the first line mixer piece, a second pressurized dissolving pump piece disposed between the flow rate adjusting unit and the second line mixer piece, and the flow rate adjusting unit and the third line Consists of a third pressure dissolving pump piece disposed between the mixer pieces,
Miscellaneous wastewater collected in the flow rate adjustment unit,
It is branched and moved to each line mixer piece by each pressurized dissolution pump piece,
The flow measurement unit,
A first flow rate measuring piece disposed between the first pressurized dissolving pump piece and the first line mixer piece, a second flow rate measuring piece disposed between the second pressurized dissolving pump piece and the second line mixer piece, and the second 3 Consists of a third flow rate measurement piece disposed between the pressure dissolution pump piece and the third line mixer piece,
The water treatment system using the high-efficiency large-capacity ozone generator,
Based on the flow rate information measured by the flow rate measurement unit, further comprising a control unit for changing the ozone supply amount from the ozone generating unit to the first line mixer piece, the second line mixer piece, and the third line mixer piece and
The ozone generating unit generates ozone of a preset capacity,
The 2-2 step is,
Step 2-2a of measuring the flow rate of miscellaneous wastewater moving to the first line mixer piece through the first flow rate measurement piece;
A 2-2b step of measuring the flow rate of miscellaneous wastewater moving to the second line mixer piece through the second flow rate measurement piece,
A step 2-2c of measuring the flow rate of miscellaneous wastewater moving to the third line mixer piece through the third flow rate measuring piece; and
obtaining a first flow rate value obtained by the first flow rate measurement piece, a second flow rate value obtained by the second flow rate measurement piece, and a third flow rate value obtained by the third flow rate measurement piece; and a 2-2d step of dividing the first portion of the ozone generated by the ozone generator so as to match the ratio of the flow rate value.
delete 8. The method of claim 7,
The water treatment system using the high-efficiency large-capacity ozone generator,
a mixing tank in which the treated water purified by the catalytic oxidation reaction unit is collected; and
It is disposed between the catalytic oxidation reaction part and the mixing tank part, and further comprises a water level control part for adjusting the water level of the catalytic oxidation reaction part,
The catalytic oxidation reaction unit,
a water tank in which the mixed water moved from the line mixer is accommodated;
A cylindrical part positioned in the water tank part, and formed in a cylindrical shape with an open upper part,
A first passage providing part which is disposed on the lower side of the cylindrical part and provides a passage for discharging a portion of the oxidized treated water in the water tank to the water level adjusting part;
a second passage providing portion disposed on the lower side of the cylindrical portion and providing a passage for discharging a portion of the oxidized treated water in the water tank to the gas-liquid mixing portion; and
It is located on the upper side of the water tank, and includes a scup removal unit for removing the floating scum generated by the oxidation reaction of the mixed water in the water tank,
The water level control unit,
a receiving unit in which the treated water discharged from the passage providing unit is accommodated;
A treated water inlet unit for allowing the treated water to flow into the receiving unit while being connected to the passage providing unit; and
and a treated water outlet for allowing the treated water to flow out into the mixing tank while being connected to the mixing tank;
a ninth step of transferring the treated water treated in the catalytic oxidation reaction unit to the water level control unit; and
A water treatment method using a high-efficiency large-capacity ozone generator further comprising; a tenth step of transferring the treated water in the water level control unit to the mixing tank unit.

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