KR20090054263A - Method for recycling and purifying livestock wastewater or high concentration wastewater by microbial high rate reactor - Google Patents

Abstract

The present invention relates to a method for the recycling and purification of livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer, the method comprising a pretreatment step, a first biological treatment step, a solid-liquid separation step, a second biological treatment step, a chemical treatment step and It includes a recycling step, by using a high rate microbial reaction stirrer in common in the liquid fertilizer production facilities and purification treatment, the livestock waste water can be recycled or purified as needed in a single facility, and the second flow rate after the first biological treatment step The installation cost can be reduced by separating the wastewater stored in the adjusting tank into sludge and wastewater using the centrifuge used in the pretreatment step.

High Rate Microbial Reaction Agitator, Centrifuge, Wastewater

Description

METHODO FOR RECYCLING AND PURIFYING LIVESTOCK WASTEWATER OR HIGH CONCENTRATION WASTEWATER BY MICROBIAL HIGH RATE REACTOR}

The present invention relates to a method of recycling and purifying livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer, and more particularly, by using a high rate microbial reaction stirrer in common in a liquid fertilizer production facility and a purification process, The present invention relates to a method for recycling and purifying livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer capable of recycling or purifying livestock wastewater.

In general, the organic wastewater is treated by solid-liquid separation through screen separation, sedimentation, and the like, and then discharged after biological treatment combined with an aerobic processor, anaerobic processor, and anoxic processor. By the above method, various organic substances which are food sources of microorganisms dissolved in waste water, nitrogen compounds resulting from decomposition of proteins, phosphorus compounds derived from fats, and the like can be removed.

However, while hydrocarbons, which are a food source for microorganisms, are relatively easily removed by microorganisms, nitrogen and phosphorus compounds are not easily removed, and researches for biologically removing them have been conducted for a long time. In the case of biological nitrogen removal, it was confirmed that nitrification and denitrification can be performed in the activated sludge process, and the removal process of biological phosphorus compounds also removes phosphorus compounds by the biochemical action of microorganisms by changing the environmental conditions of the reactor. Many treatments have been proposed.

By the way, the microbial treatment method as described above shows an excellent effect on the living sewage with a relatively low content of organic nitrogen, but in the case of livestock wastewater, nitrogen compounds are continuously released as the sludge produced from the livestock manure continues to decompose. Increasingly, there is a problem that the facility to deal with this has to be huge, and there is a problem that the processing time is also prolonged, which is not practically applied.

The removal of biological nitrogen is a method that induces cell synthesis and nitrification and denitrification reactions by the assimilation of microorganisms and converts them into nitrogen gas and removes them. The ammonia nitrogen compound is an assimilation of microorganisms such as nitrosomonas and nitrobacter. To nitrogen nitrate. At this time, the nitrogen nitrate is changed from the oxygen-free state to the nitrogen gas state by the organic carbon source as an electron donor by heterotropes, which are random heterotrophic microorganisms.

A treatment method developed using the above principle includes a biological nutrient removal (BNR) process, which induces nitrification by maintaining aerobic inside the reactor, and denitrification of nitrified nitrogen under semi-anaerobic conditions. It depends on the arrangement of aerobic and semi-anaerobic reactors, and the research is conducted based on this BNR process, and the Bardenpho process, A / O process, A2 / O process, University of capetown process, Biodeny Biodenipho (Biodenipho; Biological Denitrification Phosphorus) process, BB (Bunnik Bunschoten) process, Carrousel process, Oxidation ditch process, etc. have been developed.

In general, livestock wastewater is purified by using microbial treatment and chemical treatment, and solid wastes in livestock wastewater are solid composted and liquids are fertilized by liquid fertilization.

However, in the past, the recycling and purification treatment facilities are commonly used to remove solids from livestock wastewater and solid compost, but the liquid fertilizer production process and purification treatment process are installed separately or only one process is selected for purification. In the case of producing liquid fertilizer in the treatment facility, there is a problem of installing a separate new process or installing a separate facility for the entire process when purifying the liquid fertilizer production process.

In addition, in the case of the conventional liquid fertilizer production technology, many nutrients are removed due to aerobic aeration for a long time, there is a problem that it is impossible to control the nitrogen component important in the nature of the liquid fertilizer.

The present invention is to solve the problems of the prior art as described above,

An object of the present invention can efficiently and simultaneously perform a process for producing a liquid fertilizer and a pretreatment process for the purification treatment, and to adjust the nitrogen concentration of the liquid ratio as necessary by adjusting the gas discharge amount of the high rate microbial reaction stirrer Providing a method for recycling and purifying livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer that can secure high quality liquid waste by removing only unnecessary substances in the liquid fertilizer and preserving it without destroying nutrients through a short residence time. will be.

One aspect of the present invention for achieving the above object is

Large contaminants contained in the livestock wastewater or high concentration wastewater are filtered out with a contaminant processor, and the wastewater filtered in the contaminant handler is collected and pumped from a collector, and the fine solids contained in the pumped wastewater are separated by a centrifuge. Pretreatment step;

Decomposing a high concentration of nutrients contained in the wastewater passed through the pretreatment step using a high rate microbial reaction stirrer, wherein the step of storing the wastewater filtered out the contaminants and fine solids in the pretreatment step in a first flow rate adjustment tank, A first biological treatment step comprising the step of purifying the stored waste water by reacting with oxygen using microorganisms inside by a high rate microbial reaction stirrer, and then storing the discharged waste water in a second flow control tank;

Separating the wastewater stored in the second flow adjusting tank into sludge and wastewater using a centrifuge used in the pretreatment step;

Storing the wastewater that has undergone the solid-liquid separation in a third flow control tank;

A second biological treatment step of decomposing organic matter and nitrogen contained in the waste water stored in the third flow regulating tank by a biological treatment facility;

A chemical treatment step of decomposing the hardly decomposable substance and chromaticity contained in the wastewater which passed through the second biological treatment step by a chemical treatment facility; And

Animal wastewater using a high rate microbial reaction agitator, characterized in that the wastewater stored in the second flow rate adjustment tank is recycled into an open-air liquid ratio, or the wastewater stored in the third flow rate adjustment tank is used as a facility farm liquid ratio. The present invention relates to a method for recycling and purifying high concentration wastewater.

Recycling and purifying livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer according to the present invention can efficiently perform a process for producing liquid fertilization and a pretreatment process for purifying treatment, the gas of the high rate microbial reaction stirrer It is possible to control the nitrogen concentration in liquid liquefaction by adjusting the discharge amount as needed, and it is possible to secure high quality liquid ratio by removing only unnecessary substances in the liquid ratio and preserving it without destroying nutrients through the short residence time.

In addition, the method according to the present invention can reduce the installation cost by changing the operating time of the centrifuge to perform the role of the existing centrifuge and the centrifugal separator only by the centrifuge of the front end except the centrifugal dehydrator of the rear end of the high rate microbial reaction agitator. In addition, high-rate microbial reaction stirrer effluent can be produced in the liquid ratio required for the open field, and the plant liquid liquor for which the solid content (SS) should be low is produced through a centrifugal separator, and the concentration of the most important nitrogen in the liquid ratio can be arbitrarily controlled. It can provide a liquid fertilizer production process that can flexibly respond to the site conditions.

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

1 is a system diagram for treatment of livestock wastewater or high concentration wastewater according to the present invention. As shown in FIG. 1, the method for recycling and purifying livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer according to the present invention includes a pretreatment step (A), a first biological treatment step (B), and a solid-liquid separation step (C). ), A storage step (D), a second biological treatment step (E), a chemical treatment step (F) and a resourceization step (G). 2 is a process chart of the livestock wastewater or high concentration wastewater according to an embodiment of the present invention, Figure 3 is a process chart of the livestock wastewater or high concentration wastewater according to another embodiment of the present invention, Figure 4 is an embodiment of the present invention An example is the livestock wastewater or high concentration wastewater treatment process chart. As shown in Figures 2 to 4, the method for the recycling and purification of livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer according to the present invention is a large-scale contaminants contained in the livestock wastewater or high concentration wastewater. Pre-treatment step (A) of filtering the wastewater filtered by the contaminant treatment unit (10) and collecting and pumping the wastewater from the collector (12), and then separating the fine solids contained in the pumped wastewater by the centrifuge (14). );

Decomposing high concentration of nutrients contained in the wastewater passed through the pretreatment step (A) by using a high rate microbial reaction stirrer (22), wherein the step is wastewater from which the contaminants and fine solids are filtered out in the pretreatment step (A) Is stored in the first flow rate adjustment tank 20, the stored waste water is reacted with oxygen using the microorganisms inside the high rate microbial reaction stirrer 22 to purify and discharged, and the discharged waste water is discharged to the second flow rate adjustment tank. A first biological treatment step (B) comprising storing in (26);

(C) solid-liquid separation of the wastewater stored in the second flow rate adjusting tank (26) into sludge and wastewater using the centrifuge (14) used in the pretreatment step (A);

Storing (D) the wastewater having passed through the solid-liquid separation step (C) in a third flow rate adjustment tank (29);

A second biological treatment step (E) for decomposing, by a biological treatment facility, organic matter and nitrogen contained in the wastewater stored in the third flow regulating tank (29);

A chemical treatment step (F) for decomposing the hardly decomposable substance and the chromaticity contained in the wastewater having passed through the second biological treatment step (E) by a chemical treatment facility; And

The step (G) of recycling the wastewater stored in the second flow rate adjustment tank 26 as a liquid waste for the field or the wastewater stored in the third flow rate adjustment tank 29 as a facility farming liquid ratio.

At this time, the contaminant processing unit 10 is a known device to filter out relatively large contaminants contained in the wastewater, such as manure, nutrients, livestock wastewater, domestic wastewater. And the collector 12 is provided for collecting and pumping wastewater from which some of the large contaminants filtered out from the contaminant treatment unit 10.

5 is a structural diagram of a centrifuge according to the present invention. The centrifuge 14 rotates at a high speed and forms a centrifugal force field to settle the contaminants having a greater specific gravity than the waste water therein, and simultaneously transports and discharges the sediment from the sediment to the outlet, and flows the separated waste water to the contrary. Device.

As shown in FIG. 5, the centrifuge 14 rotates the rotary cylinder 123 at a high speed in the case 120 about the rotation shafts 121 and 122 on both sides by a driving means, and therein. The feed screw 124 is rotatably formed coaxially.

In addition, the rotary cylinder 123 is a wastewater supply pipe 125 for supplying the wastewater filtered out a relatively large contaminant is located at the end side, the external wastewater is introduced into the transfer screw 124, this wastewater injected As the centrifugal force by the high-speed rotation of the transfer screw 124 is placed on the inner wall of the rotary cylinder 123 in the order of high specific gravity, solid-liquid separation is made in a stacked form.

At this time, through the hole (not shown) formed in the front side of the rotary tube 123, the contaminants of the waste water exits to the contaminant outlet 126 of the case 120. In addition, the relatively clear and clean supernatant of the waste water is transferred in the rotary cylinder 123 by the transfer screw 124, and a plurality of separation liquid discharge ports 127 formed at the end of the case 120 through the holes of the rotary cylinder 123. To be discharged.

In addition, the separation liquid of the wastewater discharged through the separation liquid outlet 127 is dispersed in the atomization state by the centrifugal force by the high-speed rotation of the rotary cylinder 123, the gas having an ammonia nitrogen component contained in the separation liquid The degassing phenomenon from the separation solution will occur.

On the other hand, the centrifuge 14 may be used in common in the pre-treatment step (A) and the solid-liquid separation step (C) with a stepwise time. That is, the centrifuge 14 separates the sludge and the wastewater in the activated wastewater of the high rate microbial reaction stirrer 22 which will be described later. As an example, the centrifuge is operated as a pretreatment for removing fine contaminants during the 8 hours a day, and the remaining 4 hours is the sludge of the wastewater discharged from the high rate microbial reaction stirrer. It can be used for the purpose of separating wastewater. Each operating time can be adjusted to the site conditions.

The first biological treatment step (B) is a high flow rate microorganism reaction stirrer 22 for reacting the wastewater filtered out of the contaminants in the pretreatment step (A) with the first flow rate adjusting tank 20 and reacting the wastewater with oxygen to activate the microorganisms therein. And a second flow rate adjusting tank 26 for storing the wastewater activated by the microorganisms.

The first flow rate adjustment tank 20 is provided to store the wastewater and to stably supply the wastewater to the high rate microbial reaction stirrer 22. Wastewater stored in the first flow rate adjustment tank 20 is supplied to the microbial reaction stirrer 22 continuously or intermittently.

Figure 6 is a plan view of a high rate microbial reaction stirrer according to the present invention, Figure 7 is a longitudinal sectional view of a high rate microbial reaction stirrer according to the present invention. As shown in Figure 6 and 7, the high-rate microbial reaction stirrer 22 is a denitrification tank 212, the activation tank 214, the nitrification tank in which a plurality of reaction tanks are connected in a horizontal direction to contact the contaminant and the microorganisms. A plurality of reactors comprising 216; Raw water inlet pipe 220 for supplying livestock wastewater or high concentration wastewater to the upper portion of the denitrification tank 212; An internal conveying pipe 230 for conveying the livestock wastewater or the high concentration wastewater in the nitrification reaction tank 216 to the denitrification reaction tank 212; An ejector (240) installed between the raw water inlet pipe (220) and the denitrification reactor (212) to maximize oxygen dissolution efficiency; A plurality of air inlet pipes 250, 250a, 250b for supplying air into each of the plurality of reaction tanks; A gas discharge pipe 260 which discharges gas to the top of the plurality of reaction tanks, respectively; A treatment liquid discharge tube 270 integrally connected to one side of the gas discharge tube 260 and the nitrification tank 216 to discharge the purified wastewater treatment liquid; A plurality of underwater air pumps (2121, 2141, 2161) respectively installed under the plurality of reaction tanks; Air inlet hoses (2123, 2143, 2163) connected to the plurality of air pumps (2121, 2141, 2161) from the plurality of air inlet pipes (250, 250a, 250b); And sludge discharge ports 2125 and 2165 for discharging sludge in the lower portion of the denitrification reaction tank 212 and the nitrification reaction tank 216.

Looking at the method for the recycling and purification of livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer according to the present invention, the wastewater supplied to the microbial reaction stirrer 22 is denitrification tank ( 212), it is processed through the activation tank 214 and the nitrification reaction tank 216 and discharged to the outside, and a part of the treatment liquid is returned internally from the nitrification reaction tank 216 to the denitrification reaction tank 212.

The air is introduced into the reactor through the ejector 240 and the air inlet hoses 2123, 2143, and 2163 using the underwater air pumps 2121, 2141, and 2161 for a predetermined time to decompose organic matter and decompose ammonia nitrogen. Nitrify. In FIG. 7, a broken arrow shows a path through which wastewater moves.

After a certain period of time, the inflow of the denitrification tank 212 is blocked, and the inside is stirred using a submersible air pump (2121, 2141, 2161) to nitrify the nitrogen nitrate, which is internally conveyed, and the organic material in the inflowing raw water. To denitrate. After denitrification, air is introduced again and the process is repeated for a certain time.

In addition, sludge discharge ports 2125 and 2165 for discharging sludge are formed at the lower portions of the denitrification reaction tank 212 and the nitrification reaction tank 216.

The wastewater discharged from the above is stored in the second flow adjustment tank 26, which may be supplied to the liquid ratio for the open field or may be stably transferred to the centrifuge for a predetermined time.

The high rate microbial reaction stirrer 22 may adjust the gas discharge amount to adjust the concentration of nitrogen in the resourced liquid ratio. That is, a large amount of ammonia gas is contained in the gas discharged to the outside, and the nitrogen content in the liquid ratio can be easily adjusted to 0.3 to 0.5% by adjusting the amount of exhaust gas using the gas discharge pipe 260.

The hydraulic retention time of the wastewater in the high rate microbial reaction stirrer 22 in the first biological treatment step (B) is preferably 12 to 24 hours. This is to secure high-quality liquid ratio by preserving nutrients necessary for the soil by preserving hard-degradable organic matters that are beneficial to the soil while maximally decomposing the degradable organic matter harmful to the soil through a short time treatment.

In addition, the temperature inside the high rate microorganism reaction stirrer 22 is preferably maintained at 50 ~ 60 ℃, which is to kill E. coli and pathogenic microorganisms.

On the other hand, solid-liquid separation step (C) is a solid-liquid separation of the wastewater stored in the second flow rate adjustment tank 26 into sludge and wastewater using the centrifuge 14 used in the pretreatment step (A). In the conventional high rate microbial reaction stirrer, a centrifuge for separating fine solids and a centrifugal dehydrator for separating sludge and waste water from the wastewater discharged from the high rate microbial reaction stirrer were used separately, and in the present invention, the operation time of the centrifuge was used. By doing so, only the centrifuge can perform the role of the existing centrifuge and the centrifugal dehydrator at the same time can reduce the installation cost.

The storage step (D) stores the wastewater that passed through the solid-liquid separation step (C) in the third flow rate adjusting tank 29, which may be supplied to the facility farm liquid ratio or transferred to the rear end facility stably for a continuous time.

Meanwhile, the wastewater stored in the third flow adjusting tank 29 is discharged through the second biological treatment step E and the chemical treatment step F as shown in FIGS. 2 to 4. The second biological treatment step (E) decomposes organic matter and nitrogen contained in the waste water stored in the third flow regulating tank 29 by a biological treatment facility, and the chemical treatment step (F) comprises the second biological treatment step. The hardly decomposable substance and chromaticity contained in the wastewater which passed through (E) are decomposed by a chemical treatment facility.

The aeration tank 30, the settling tank 32 shown in FIG. 3 or the anaerobic tank 34, the anaerobic tank 35, the aerobic tank 36 and the settling tank 37 shown in FIG. 4 are preferred in the second biological treatment step (E). An example is shown.

The aeration tank 30 removes organic substances using aerobic microorganisms while receiving air, and the first precipitation tank 32 is a facility for separating wastewater and sludge treated in the aeration tank 30 through the precipitation action.

In addition, anaerobic tank 34, anoxic tank 35, aerobic tank 36, precipitation tank 37 is a technique for removing nitrogen and phosphorus in addition to the organic material. The anaerobic tank 34 does not supply air so that the microorganisms adsorb the phosphorus to remove the phosphorus, and the oxygen-free tank 35 does not supply oxygen to convert nitrogen nitrated in the aerobic tank 36 to nitrogen gas using the microorganism. To remove nitrogen. The aerobic tank 36 supplies oxygen to convert organic matter and convert ammonia nitrogen to nitrate nitrogen, and return some treated wastewater to the anaerobic tank 34 or anoxic tank 35. The settling tank 37 is a facility for separating the wastewater and sludge treated in the aerobic tank 36 through the settling action.

On the other hand, the chemical coagulation tank 40, the second precipitation tank 42 and the ozone contact tank 44 shown in Figure 4 shows a preferred embodiment of the chemical treatment step (F).

The chemical coagulation tank 40 is a technique for coagulating the hardly decomposable substance and various contaminants by using an inorganic coagulant or an organic coagulant, and sedimentation and treatment of the aggregate and the treated wastewater in the second precipitation tank 42. In addition to the chemical coagulation technology, the ozone contacting tank 44 can be used to inject oxidizing ozone into the wastewater to treat hardly decomposable substances and various pollutants. The sludge discharged from the second settling tank 42 is dewatered and caked.

In Figures 2 to 4 the overall movement with respect to the flow of air, the return flow of excess sludge, the flow of solids and the flow of other waste water is represented by arrows.

Recycling step (G) is to recycle the wastewater stored in the second flow control tank 26 of the first biological treatment step (B) to the off-site liquid ratio or stored in the third flow control tank 29 of the storage step (D) The waste water is recycled as liquid for plant farming.

Although the present invention has been described in connection with the above-mentioned preferred embodiments, it is possible to make various modifications or variations without departing from the spirit and scope of the invention. Accordingly, the appended claims include such modifications and variations as fall within the spirit of the invention.

1 is a system diagram for treatment of livestock wastewater or high concentration wastewater according to the present invention.

2 is a process chart of the livestock wastewater or high concentration wastewater according to an embodiment of the present invention.

3 is a process chart of livestock wastewater or high concentration wastewater according to another embodiment of the present invention.

4 is a process chart of the livestock wastewater or high concentration wastewater according to an embodiment of the present invention.

5 is a structural diagram of a centrifuge according to the present invention.

6 is a plan view of a high rate microbial reaction stirrer according to the present invention.

7 is a longitudinal sectional view of a high rate microbial reaction stirrer according to the present invention.

<Explanation of symbols for the main parts of the drawings>

A pretreatment step B first biological treatment step

C: solid-liquid separation step D: storage step

E: second biological treatment step F: chemical treatment step

G: Resourceization Step

10: dust collector 12: water collector (pumping tank)

14 centrifuge 20 first flow rate adjusting tank

22 high rate microorganism reaction stirrer 26 second flow rate adjusting tank

29: third flow rate adjustment tank 30: aeration tank

32: first settling tank 34: anaerobic tank

36: aerobic tank 35: anaerobic tank

37: sedimentation tank 40: chemical flocculation tank

42: second precipitation degree 44: ozone contact tank

120: case

121, 122: rotating shaft 123: rotating cylinder

124: transfer screw 125: waste water supply pipe

126: foreign matter discharge port 127: separation liquid discharge port

212 denitrification tank 214 activation tank

216: nitrification tank

220: raw water inlet pipe 230: internal return pipe

240: ejector 250, 250a, 250b: air inlet pipe

260: gas discharge pipe 270: treatment liquid discharge pipe

2121, 2141, 2161: Submersible air pump 2123, 2143, 2163: Air inlet hose

2125, 2165: sludge outlet

Claims (7)

Large contaminants contained in the livestock wastewater or high concentration wastewater are filtered out with a contaminant processor, and the wastewater filtered in the contaminant handler is collected and pumped from a collector, and the fine solids contained in the pumped wastewater are separated by a centrifuge. Pretreatment step; Decomposing a high concentration of nutrients contained in the wastewater passed through the pretreatment step using a high rate microbial reaction stirrer, wherein the step of storing the wastewater filtered out the contaminants and fine solids in the pretreatment step in a first flow rate adjustment tank, A first biological treatment step comprising the step of purifying the stored waste water by using a microorganism inside with a high rate microbial reaction stirrer, purifying and discharging the waste water, and storing the discharged waste water in a second flow control tank; Separating the wastewater stored in the second flow adjusting tank into sludge and wastewater using a centrifuge used in the pretreatment step; Storing the wastewater that has undergone the solid-liquid separation in a third flow control tank; A second biological treatment step of decomposing organic matter and nitrogen contained in the waste water stored in the third flow regulating tank by a biological treatment facility; A chemical treatment step of decomposing the hardly decomposable substance and the chromaticity contained in the wastewater having passed through the second biological treatment step by a chemical treatment facility; And Livestock wastewater or high concentration using a high rate microbial reaction stirrer, characterized in that the wastewater stored in the second flow rate adjustment tank to the wastewater ratio for the open field or the wastewater stored in the third flow rate adjustment tank to the facility farm liquid ratio; Method of recycling and purification of waste water. The method according to claim 1, wherein the centrifugal separator is commonly used in the pretreatment step and the solid-liquid separation step in stepwise time. The method of claim 1, wherein the high rate microbial reaction stirrer controls the concentration of gas to adjust the concentration of nitrogen in the recycled liquid ratio. The method of claim 1, wherein the residence time of the wastewater in the high rate microbial reaction stirrer in the first biological treatment step is 12 to 24 hours, the resource and purification of livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer Treatment method. The method of claim 1, wherein the second biological treatment step comprises: an aeration tank step of supplying air and removing organic substances contained in the wastewater by using aerobic microorganisms; And A first sedimentation tank stage for separating the wastewater and sludge treated in the aeration tank through sedimentation, The chemical treatment step may include a chemical coagulation step of agglomerating a hardly decomposable substance using an inorganic coagulant or an organic coagulant; And And a second precipitation tank step of separating the aggregates and the wastewater aggregated in the chemical coagulation tank step. The method for treating and purifying livestock wastewater or high concentration wastewater using a high rate microbial reaction stirrer. The method of claim 1, wherein the second biological treatment step comprises: an anaerobic tank step of adsorbing phosphorus using microorganisms; An anoxic tank step of removing nitrogen by denitrifying nitric acid and nitrite nitrogen in an aerobic tank using microorganisms; An aerobic tank step of supplying oxygen to decompose organic substances and convert ammonia nitrogen to nitrate nitrogen; And A sedimentation tank stage for separating the wastewater and sludge treated in the aerobic tank, The chemical treatment step is a resource treatment and purification method of livestock wastewater or high concentration wastewater using a high rate microbial reaction agitator, characterized in that it comprises an ozone contact tank step of injecting ozone into the wastewater through an ozone generator. According to claim 1, wherein the high rate microbial reaction stirrer includes a plurality of reaction tank including a denitrification reaction tank, the activation tank, the nitrification reaction tank in which a plurality of reaction vessels are connected in a horizontal direction to contact the pollutant and the microorganism; Raw water inlet pipe for supplying livestock wastewater or high concentration wastewater to the upper portion of the denitrification reactor; An internal conveying pipe for returning livestock wastewater or high concentration wastewater in the nitrification tank to the denitrification tank; An ejector installed between the raw water inlet pipe and the denitrification reactor to maximize oxygen dissolution efficiency; A plurality of air inlet pipes supplying air into each of the plurality of reaction tanks; A gas discharge pipe for discharging the gas to the top of the plurality of reaction tanks, respectively; A treatment liquid discharge tube connected to one side of the gas discharge tube and the nitrification tank to discharge the purified wastewater treatment liquid; A plurality of underwater air pumps each installed at a lower portion of the plurality of reaction tanks; An air inlet hose connected to the plurality of underwater air pumps from the plurality of air inlet pipes; And And a sludge discharge port for discharging sludge in the lower part of the denitrification tank and the nitrification tank.

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