KR20200099646A - Recycling and water quality purification treatment system of livestock manure - Google Patents

Abstract

The present invention relates to a treatment system equipment facility for purifying and treating livestock manure wastewater slurries generated in livestock houses such as pig farms. The first object (resourceization) of the present invention is to convert high concentration fermentation, odorless liquid manure and organic compost as resources through a rapid oxidation fermentation and odorless treatment system device. The second object (circulated recycling) of the present invention is to recycle the bio-filtered water through the NPR sprinkling filter upper filtration device of the system treatment system and recycle the same to the bio-filtered water in the wastewater slurry storage tank at the bottom of a pig house. The third purpose (advanced purification treatment) of the present invention separates a non-degradable solid substance contained in livestock wastewater by sequentially passing through a system treatment process in which the final treated water is recycled or discharged as cleaning water, agricultural water, etc., through advanced purification treatment of excess biological filtration water, performs oxidation, fermentation, decomposition and removal of organic suspended matter through the metabolic function of complex microorganisms, and completely destroys and removes hydrogen sulfide, ammonia, etc., which are the cause of odor generation in the process of natural decomposition of organic substances. The recycling system for recycling and purifying livestock wastewater according to the present invention completely removes nitrogen, phosphorus, and residual organic matter contained in wastewater, harmful bacteria, nitrogen, phosphorus, heavy metals, and pigment components, which are causes of eutrophication.

Description

Recycling and water quality purification treatment system of livestock manure}

The present invention provides system equipment and facilities in the process of treating high-concentration livestock manure wastewater slurry (hereinafter referred to as "wastewater") discharged from the manure wastewater storage tank of a pig farm, especially a pig farm pig house (hereinafter referred to as "wastewater") according to a purification system. In addition to physical treatment functions such as agitation and aeration of wastewater, the active function of complex microorganisms added to the oxidation decomposition and removal treatment of organic substances, nitrogen, phosphorus, etc. contained in the wastewater, and to reduce odor and activate the removal function Wastewater treatment water (hereinafter referred to as "treatment water") from which wastewater is rapidly oxidized/fermented by the biological treatment used and odor-removed wastewater treated water (hereinafter referred to as "treatment water") is converted into odorless fermented fermented liquid manure or organic compost, and then the excess treated water is systematically treated In the meantime, part of the treated water activated by complex microorganisms is returned to the wastewater slurry collection tank and the first flow control storage tank, and circulates and recycles as a donor of complex microorganisms to remove odors and oxidize fermentation of the livestock wastewater slurry that is continuously introduced. Softening and homogenization through anaerobic digestion and decomposition of the wastewater of the storage tank by returning the flow rate corresponding to the discharged flow rate to the storage tank of the livestock house by returning the treated water (biofilter water) treated through the biowood chip sprinkling filter stage of the process to the complex microbial donor. And odor reduction or removal function, and the overall treatment efficiency is improved by significantly reducing the capacity of wastewater treated water in the subsequent system treatment, and then the surplus treated water (biofiltration water) is recycled and discharged through advanced purification treatment. It relates to a recycling system for recycling and recycling livestock wastewater from pig farms for sequential purification through step-by-step system treatment according to the Ministry of Environment notification standard).

The technology for composting and liquefying livestock manure has been published in detail in Registration Patent Publication No. 10-0921194, but generally, the type of composition of the pig farm livestock wastewater treatment facility is livestock wastewater that stores and stores pig manure wastewater slurry generated from the livestock house. It consists of a storage tank, a contaminant separation device equipped with a solid-liquid separator that separates and extracts contaminants (feed skin, hair, etc.) of a certain size or more contained in the wastewater, and an aeration tank that oxidizes and decomposes organic substances. Stored in farmland and grassland, or mixed with sawdust and rice husk for composting, the excess is transported to external treatment facilities such as livestock wastewater public treatment plants for purification.

In such a process, due to the lack of engineering technology, the treatment function and efficiency are low in operation, so that it cannot be properly treated and a severe odor is generated, and liquid manure and compost that have not been normally fermented and ripened are sprayed or discharged without permission to farmland, etc. Due to a number of problems such as destruction of the surrounding ecological environment, civil complaints are frequent, and the resulting problem has emerged as a chronic challenge for the central government and local governments across the country, and many of the facilities are suspended or left as useless due to strengthened enforcement. to be.

It is an emergency that the foundation of the pig farm's livestock industry itself may collapse without solving the fundamental problems as the environmental destruction and pollution caused by the volatilization of odors generated during the pig farm livestock wastewater treatment process, the unauthorized spraying of immature fermentation and poor liquid manure, etc. In one situation, there is an urgent need to develop a pig farm livestock wastewater treatment facility facility with more environmentally friendly, low-cost, high-efficiency, and consistently stable engineering technology.

In addition, since livestock wastewater contains a large amount of organic matter, nitrogen, phosphorus, etc., since the C/N ratio is low, an external carbon source such as methanol is required to completely oxidize and remove nitrogen with nitrogen gas.

In addition, the livestock wastewater must undergo a denitrification process to remove nitrate nitrogen contained in organic matter, a nitrification process to nitrify ammonia nitrogen, and a dephosphorization process to remove phosphorus.

Conventional techniques related to the above-described denitrification process are divided into heterotrophic denitrification and autotrophic denitrification.

The heterotrophic denitrification method is further subdivided into pre-denitrification and post-denitrification according to the position of the anoxic tank. The heterotrophic denitrification method uses organic matter in wastewater, so it is a method that can reduce the cost of using external carbon sources. A tank and a settling tank are installed in order to perform denitrification.

At this time, in the oxygen-free tank, the denitrification reaction and organic matter decomposition occur mainly, and the organic matter decomposition and nitrification reaction occur in the oxidation tank. The intermediate treated water that has been nitrified in the nitrification tank is returned to the anoxic tank to perform a denitrification reaction in the anoxic tank.

In the heterotrophic post-denitrification method described above, an external carbon source with a high price and a concentration suitable for the concentration of nitrate nitrogen must be introduced into the nitrified wastewater, and a nitrate nitrogen monitoring system and a system that automatically inputs an external carbon source corresponding to the concentration Required.

If an external carbon source suitable for the concentration of nitrate nitrogen cannot be added, there is a problem that the external carbon source remaining in the effluent must be treated again.

The heterotrophic denitrification is performed by a reaction by a nutrient-requiring denitrification bacteria that reduces nitric acid or nitrite nitrogen to nitrogen gas using organic matter as an electron donor in an anaerobic state.

However, in industrial wastewater such as nitrogen and phosphoric fertilizer manufacturing, plywood manufacturing, pesticide manufacturing, leather manufacturing, etc., and leachate generated from landfills, the concentration of organic matter is relatively low compared to the concentration of nitrogen. Since it is necessary to perform a post-denitrification process inducing a denitrification reaction by adding the same organic matter, in the case of treating a large amount of wastewater, there is a disadvantage in that the cost of adding organic matter is more difficult, so it is difficult to expect effectiveness.

In order to solve the above problems, many studies have been conducted on an independent nutrition denitrification method, particularly a denitrification method using sulfur. The sulfur denitrification method has a decent denitrification effect in terms of economy and stable treatment efficiency, but there is a problem that the pH is lowered due to the destruction of alkalinity due to hydrogen ions generated during the denitrification process.When 1 mg of nitrogen is denitrified during autotrophic denitrification, calcium carbonate (CaCO3) about 5mg is consumed.

Therefore, in order to maintain the pH in the neutral band (6-8), a plan was attempted to supplement the alkalinity by filling the reaction tank with limestone, etc., but in the case of wastewater containing high concentration of nitrogen such as leachate, factory wastewater, and livestock wastewater. It is virtually difficult to compensate for alkalinity only with limestone.

When a high concentration of nitrate nitrogen is treated, a high concentration of sulfate ions is generated as a by-product. Sulfate ions generated as a result of metabolism of sulfuric acid denitrification microorganisms are not regulated in the effluent quality standards, and are defined as aesthetically influencing substances in the drinking water quality standards. In terms of drinking water quality, Korea regulates it to not exceed 200 ppm, and WHO regulates it at 400 ppm.

Commonly used processes to remove nitrogen in wastewater include Badenpo 4-stage process, oxidation hole process, A2O process, Badenpo 5-stage process, UCT process, VIP process, P/L process, SBR, intermittent aeration method, comprehensive fixation. There are chemical methods, but since all of the above methods use heterotrophic denitrifying microorganisms, it is difficult to apply when the C/N ratio of the influent is low, and since an anaerobic tank must be added to biologically remove phosphorus (P), a larger site is required. . Among the water treatment technologies for removing phosphorus, the coagulation precipitation method is commonly used, but it has the disadvantage of high chemical treatment cost and large amount of slurry generation.

Examples of the nitrogen removal method from conventional livestock wastewater include methods such as using an external carbon source, ammonia stripping, struvite sedimentation, and RO membrane, but it is very expensive and economically difficult in livestock farms, rather than the concept of effectively treating livestock wastewater. It has been consumed by storing it for a certain period of time and then simply processing it, then making compost and liquid manure and spraying it on farmland.

As described above, livestock wastewater is often treated in a microbial reaction tank after pretreatment such as centrifugation or flotation separation, but livestock wastewater after pretreatment has a low C/N ratio and cannot be completely denitrified as it is. There is a problem that an organic carbon source such as methanol must be continuously supplied from the outside, and thermal energy must be continuously supplied from the outside in order to perform anaerobic fermentation at medium temperature.

In conclusion, livestock wastewater or slurries are often treated in a microbial reactor after pretreatment such as centrifugation or flotation of non-degradable substances, chromaticity, residual nutrients and suspended substances contained in biologically and chemically treated water. As described above, since the C/N ratio of livestock wastewater is low, it is difficult to completely denitrate it as described above. Therefore, organic carbon sources such as methanol and acetate must be continuously supplied from the outside for complete denitrification. Therefore, difficult to decompose livestock wastewater and slurry are economically and efficiently used. There is a need for a solution that can continuously purify in large quantities.

The solution to implement the first object of the present invention is,

The wastewater slurry discharged from the livestock storage tank is stored and stored and stirred with an aeration type stirring device that operates intermittently by an automatic control device to prevent slurry precipitation and solidification, and to anaerobic digestion and smooth homogenization of the wastewater slurry in the second flow control tank. A collection and storage tank (10) for oxidizing and decomposing, reducing and removing odors, and discharging wastewater that exceeds a certain level in comparison with the amount of inflow through an underwater pump by activating complex microorganisms included in the treated water returned and flowing;

The wastewater slurry transported from the collection and storage tank 10 is filtered out of inorganic solid contaminants contained in the wastewater slurry through a detailed screen of a certain standard, compressed by a pressing screw, and discharged separately, and the slurry solution desorbed in this process is removed. 1 and the impurity separation device 11 discharged to the flow control storage tank 20;

Stores the slurry aqueous solution desorbed by the impurities separation device 11, and intermittently agitates the stored water in an aeration method under the control of an automatic control device through an aeration-type stirring device to prevent precipitation and solidification of the slurry while anaerobic digestion. , Oxidation decomposition, odor reduction, removal treatment, and a first flow rate adjustment storage tank (20) for discharging a certain amount of overwater to the first rapid oxidation and fermentation tank (30a) in comparison to the inflow amount through the water pump;

Accepts the treated water introduced from the first flow rate control storage tank 20, and includes it in the treated water through a rapid oxidation/fermentation device and an NPR bioreactor mounted inside the first rapid oxidation and fermentation tank 30a. It is equipped with a foam removal device (see Fig. 13) to rapidly oxidize and ferment the organic suspended matter, and remove a large amount of foam generated in this process, and adsorb/parasitic on the media filled in the NPR bioreactor (BIO REACTOR). As the dominant species of complex microorganisms increase or decrease by themselves according to the flow rate/characteristic of the treated water, organic matter decomposition/removal treatment and oxidation fermentation are generated through vigorous activation, generating heat of fermentation of about 50℃ or higher. A first rapid oxidation and fermentation tank (30a) for discharging the overwater to the second rapid oxidation and fermentation tank (30b) through the NPR-simplified filtration device (33) installed on the inner wall of the tank and most of the odor of the tank;

The second rapid oxidation and fermentation tank (30a) has the same configuration and function as the first rapid oxidation and fermentation tank (30a) to re-treat the treated water flowing from the first rapid oxidation and fermentation tank (30a) in the same process while discharging the excess water to the biooxidation reactor (40). A rapid oxidation and fermentation tank (30b);

Dominant species of complex microorganisms adsorbing/parasitic to the media of the NPR bioreactor through intermittent air aeration by an air aeration device installed inside the tank and receiving the treated water discharged from the second rapid oxidation and fermentation tank 30b Biooxidation that discharges excess water through the NPR-simplified filtration device 43 installed on the inner wall of the tank while decomposing and removing organic substances contained in the treated water by actively promoting the metabolism of the treated water. A reaction tank 40;

The treated water discharged from the biooxidation reaction tank 40 is stabilized so as to be precipitated, and the precipitated treated water (activated sludge) in which the complex microorganisms are activated using an air lift transfer device is collected and stored in a collection tank 10 and a first flow control tank ( 20), and supply it to the active microorganism donor for anaerobic digestion, oxidative decomposition, odor reduction and removal of wastewater, and discharge it to the outside as a high concentration liquid manure if necessary, or selectively discharge the precipitated treated water to the compost stage 300 Therefore, it is mixed and fermented with organic compost materials such as sawdust, rice husk, and rice straw to make organic compost.In this case, the treated water is also used as a moisture control agent for compost materials such as sawdust, and the treatment flow rate decreases in the subsequent system treatment. It may appear as an increasing effect, and the surplus water is characterized in that it is implemented by the second flow control storage tank 50 discharged to the solid-liquid separation device 60 or the biowood chip sprinkling filter top 70.

The solution according to the second and third objects of the present invention is,

The sediment water settled at the bottom of the tank of the second flow control storage tank 50 is separated into solid-liquid through a solid-liquid separator to discharge the solids and convert them into organic compost material, and the sap component is discharged to the biowood chip sprinkling filter top (70). A solid-liquid separation device 60;

The treated water discharged from the solid-liquid separation device 60 is stored on one side of the partitioned tank, and the treated water stored through a sprinkling device (spraying nozzle, sprinkling pipe) is sprayed onto the NPR biowood chip filling layer in which complex microorganisms are adsorbed and cultured. While the treated water is retained/filtered through the biowood chip layer, it continuously decomposes and removes by adsorbing organic suspended matter contained in the treated water, and discharges the treated biological filtrate to the third flow control storage tank 80. A biowood chip sprinkling filter top 70;

The bio-filtered water discharged from the biowood chip sprinkling filter stage 70 is stored in a stable manner and the stored bio-filtered water is discharged to convert it into a low-concentration liquid fertilizer or, if necessary, through a transfer pump device, in response to the discharge of the wastewater storage tank under the livestock house. It is returned to the active microbial filtrate of the lower storage tank, and accordingly, the treatment capacity is significantly reduced in the subsequent system treatment by circulating and recycling the wastewater treated water, and the treatment efficiency can be significantly increased.The excess overwater is the first unit. A third flow control storage tank 80 transferred to the biooxidation reaction tank 90a;

It accommodates the treated water transferred from the third flow control storage tank 80, and intermittently supplies air into the NPR bioreactor through an air aeration device installed inside the tank to promote the metabolism of dominant species complex microorganisms. A first aerobic biooxidation reactor (90a) for discharging the treated water with activated complex microorganisms through the NPR-simplified filtration device 93 installed on the inner wall of the tank while decomposing and removing residual organic matter contained in the treated water. ;

The second aerobic bio-oxidation reactor reprocessing the treated water discharged from the first aerobic bio-oxidation reactor 90a with the same configuration and function as the first aerobic bio-oxidation reactor 90a and discharged through the NPR-simplified filtration device ( 90b) and;

The treated water discharged from the second aerobic biooxidation reactor (90b) is treated by spraying it on the NPR biowood chip filling layer where the complex microorganisms are cultivated/adsorbed through a sprinkling device and air is intermittently supplied through the aeration device. The organic material oxidation bio that the water retains and filters the biowood chip layer, absorbs/decomposes/removes organic residual suspended matters remaining in the treated water, and discharges the filtered treated water to the 4th flow control storage tank 109. A filtration tank 100;

In order to store the treated water discharged from the organic material oxidation biofiltration tank 100 to be stabilized and to discharge the stored treated water as a resource as a low-concentration liquid manure, or to use it as the storage water (bio-filtration water) of the wastewater storage tank at the lower part of the house (1) A fourth flow adjustment storage tank 109 for discharging excess overwater to the first advanced treatment tank 110a while transferring a certain amount to the lower storage tank of the house 1 through a transfer pump device as needed;

An NPR-REACTOR (NPR reactor) by an air diffuser that is installed inside the tank to supply air intermittently while storing the treated water transferred from the fourth flow control storage tank 109, and air intermittently supplied by the air diffuser. ) The NPR block filled inside, the advanced treatment MEDIA composed of natural minerals and the treated water are contacted and aerated. In this process, the components of the NPR block and advanced treatment media are finely dissolved in the treated water, and residual organic matter contained in the treated water, The first that adsorbs/decomposes/removes harmful bacteria, nitrogen, phosphorus, heavy metals, and pigment components, and discharges overwater to the second advanced treatment tank 110b through the NPR-simplified filtration device 113 installed on the inner wall of the tank. An advanced treatment tank 110a;

In the same configuration and function as the first advanced treatment tank 110a, the second treatment water discharged from the first advanced treatment tank 110a is reprocessed in the same process and the overwater is discharged through the NPR-simplified filtration device. An advanced treatment tank 110b;

Equipped with a media layer for advanced treatment composed of NPR biowood chips, NPR blocks, and natural minerals, and an aeration device for supplying air into the filter material layer, and spray the treated water discharged from the second advanced treatment tank 110b. Water is sprayed to the top of the filter media layer through the device to absorb/decompose/remove residual organic matter, harmful bacteria, nitrogen, phosphorus, heavy metals, and pigment components remaining in the treated water while the treated water stays and passes through the media layer, and is filtered. An NPR biofiltration tank 120 for discharging the treated water to the sterilization and sterilization tank 130;

A sterilization and sterilization tank 130 for discharging overwater to the decolorization filtration tank 140 while sterilizing/sterilizing through a sterilization/sterilization device installed to be immersed in the treated water discharged from the NPR biofiltration tank 120 (optional configuration according to need), and ;

While receiving the treated water introduced from the sterilization and disinfection tank 130, while staying and passing through the multistage filter chamber filled with granular activated carbon and NPR blocks, the residual chromaticity remaining in the treated water is completely decolorized, and residual harmful bacteria A decolorization filtration tank 140 for sterilizing/sterilizing the treated water and discharging the treated water to the treated water storage tank 150 under natural flow;

It is characterized by consisting of a treated water storage tank 150 that stores the treated water discharged from the decolorization filtration tank 140 and transfers it so that it can be recycled as agricultural water and cleaning water through a transfer pump, and discharges excess excess water through a discharge pipe. have.

The present invention relates to a storage tank (1), a collecting storage tank (10), a contaminant removal device (11), a first flow adjustment storage tank (20), a second rapid oxidation and fermentation tank (30a), a second rapid oxidation and fermentation tank (30b), and biooxidation. It can be converted into resources (liquid manure or compost) through the processing system of the reaction tank 40, the second flow control storage tank 50 and the solid-liquid separation device 60,

Biowood chip sprinkling filter top (70), the third flow adjustment storage tank (80), the first aerobic biooxidation tank (90a), the second biooxidation tank (90b), the organic material oxidation biofiltration tank (100), the fourth flow rate The system of the controlled storage tank 109, the first advanced treatment tank 110a, the second advanced treatment tank 110b, the NPR bio filtration tank 120, the sterilization and sterilization tank 130, the bleaching filter tank 140, and the treated water storage tank 150 In the 3rd flow adjustment storage tank and the 4th flow adjustment storage tank, the collection storage tank (10), the impurities removal device (11), the first flow adjustment storage tank (20) by the complex microbial filtrate returned to the wastewater storage tank below the house. , By periodically supplying the donor while increasing the microbial activity of the second rapid oxidation and fermentation tank (30a), the second rapid oxidation and fermentation tank (30b), and the biooxidation reactor (40), it is not used for the livestock wastewater without using an external carbon source for denitrification. It separates and treats contaminants such as non-degradable inorganic solids and removes odors (ammonia, hydrogen sulfide) generated in the process of oxidation, fermentation, decomposition and removal of organic suspended substances through the metabolic function of complex microorganisms, and natural decomposition of organic substances. It is completely extinct and removed from the treatment system, and it can remove nitrogen, phosphorus and residual organic matter contained in wastewater, harmful bacteria, nitrogen, phosphorus, heavy metals, and pigment components in medium to medium water quality.

Therefore, the solution of the first object of the present invention, that is, recycling of resources into high concentration odorless, fermented liquid manure and organic compost through a rapid oxidation fermentation and odorless treatment system, and recycling recycling, which is the second objective , The best objective effect is to convert a large amount of wastewater treated water (biofiltered water) into a wastewater storage tank at the bottom of the house while recycling and recycling the biological filtrate to a low-concentration odorless liquid ratio through the NPR sprinkling filter upper filtration device as a resource and as an active microorganism donor in the first flow control storage tank. The purification system is connected to the water quality that can recycle or discharge the final treated water as cleaning water or agricultural water through advanced purification treatment, that is, the advanced purification treatment of surplus biological filtration water, which is a solution to the third purpose of recycling and recycling as reservoir water. It is implemented as an enemy. In addition, if necessary, the final treated water can be sterilized and sterilized to be recycled as drinking water for both pig farms.

1 is a configuration diagram of a system for recycling livestock manure and water purification treatment according to the present invention,
FIG. 2 is a cross-sectional view showing the main parts of the collection storage tank and the first flow control storage tank shown in FIG. 1, respectively.
FIG. 3 is a cross-sectional view showing main portions of the first and second rapid oxidation and fermentation tanks shown in FIG. 1, respectively.
FIG. 4 is a cross-sectional view showing the main portions of the biooxidation reactor and the second flow control storage tank shown in FIG. 1, respectively.
5 is a cross-sectional view showing the main parts of the biowood chip sprinkling filter top and the third flow control storage tank shown in FIG.
6 is a cross-sectional view showing the main portions of the first and second aerobic biooxidation reactors shown in FIG. 1, respectively.
7 is a cross-sectional view showing the main parts of the organic material oxidation biofiltration tank and the fourth flow control storage tank shown in FIG.
FIG. 8 is a cross-sectional view showing main portions of the first and second advanced treatment tanks shown in FIG. 1, respectively.
9 is a cross-sectional view showing the main parts of the NPR biofiltration tank and the sterilization and disinfection tank shown in FIG.
10 is a cross-sectional view showing the main parts of the decolorization filtration tank and the treated water storage tank shown in FIG.
11 is a perspective view showing a circuit control device (MCC control panel panel) according to the present invention.

Hereinafter, a preferred embodiment according to the system for recycling livestock manure and water purification treatment system according to the present invention will be described in detail with reference to the accompanying drawings.

1 is a block diagram illustrating a system for recycling livestock manure and water purification treatment according to the present invention. As shown in Fig. 1, the water purification treatment system includes a storage tank 1, a collection storage tank 10, a contaminant removal device 11, a first flow adjustment storage tank 20, and a second rapid oxidation and fermentation tank 30a provided in the lower part of the barn, as shown in FIG. , The second rapid oxidation and fermentation tank (30b), the biooxidation reaction tank (40), the second flow adjustment storage tank (50), the solid-liquid separation device (60), the biowood chip spray filter stage (70), the third flow adjustment storage tank (80) ), the first aerobic biooxidation reactor (90a), the second aerobic biooxidation reactor (90b), the organic material oxidation biofiltration tank (100), the fourth flow control storage tank (109), the first advanced treatment tank (110a), the second It is a treatment system consisting of an advanced treatment tank 110b, an NPR biofiltration tank 120, a sterilization and sterilization tank 130, a bleaching filter tank 140, and a treated water storage tank 150.

The means for implementing the first object (recycling of resources) according to the present invention is a collection storage tank 10, a contaminant removal device 11, a first flow adjustment storage tank 20, a second rapid oxidation and fermentation tank 30a, and a second rapid oxidation. It is implemented by a treatment system leading to the fermentation tank 30b, the biooxidation reactor 40, and the second flow rate adjustment storage tank 50,

The means for implementing the second purpose (recycling and recycling of biological filtrate water in the wastewater storage tank at the bottom of the barn) are the second flow adjustment storage tank 50, the solid-liquid separation device 60, the biowood chip sprinkling filter top 70, and the third flow adjustment storage tank 80. ), the first aerobic biooxidation reactor (90a), the second aerobic biooxidation reactor (90b), the organic material oxidation biofiltration tank (100), and the fourth flow control storage tank (109).

The means for implementing the third purpose (high purification treatment, circulation recycling and discharge) are the first advanced treatment tank 110a, the second advanced treatment tank 110b, the NPR bio filtration tank 120, the sterilization and sterilization tank 130, and the bleaching filter tank ( 140), implemented by a treatment system leading to the treated water storage tank 150.

As shown in FIGS. 1 and 2, the above-described collection and storage tank 10 stores and stores the manure wastewater slurry discharged from the wastewater storage tank 1 of the house, while agitating the stored slurry, in an air pump A1. An air stirring device (not shown in the drawing, hereinafter referred to as "aerated agitating device") for blowing the generated air into water is installed, and the impurity removing device 11 described later by the transfer pump P1 Transfer to.

The above-described aeration type stirring device prevents precipitation and solidification of the slurry by stirring the wastewater by continuously blowing air into the collecting water 10. The above-described transfer pump P1 pumps and transfers wastewater to the impurity removing device 11.

The above-described impurity removing device 11 is equipped with a detailed screen (not shown in the drawing) of a certain standard.

Therefore, the wastewater transferred by the above transfer pump (P1) consists of a drum, an inclined screen (fine screen), and a screw compactor (not shown in the drawing) to filter out various inorganic solid impurities such as pig hair and feed skin. After being compressed, it is separated and discharged to the outside, and only the sap desorbed during this process is discharged to the first flow control storage tank 20.

As shown in FIG. 2, the first flow adjustment storage tank 20 is equipped with an aeration type stirring device for injecting air supplied by the air pump A2 and a submersible pump P2, like the aeration type stirring device described above. Air is injected into the water to agitate the wastewater, and when the water level reaches a certain level, the submersible pump (P2) operates to transfer the wastewater to the first rapid oxidation and fermentation tank (30a), and when the water level falls below the set value, the submersible pump ( The flow rate is controlled in such a way that P2) is stopped.

The first rapid oxidation and fermentation tank 30a above has an NPR bioreactor 32 (BIO REACTOR) immersed in the tank as shown in FIG. 3, and a rapid oxidation/fermentation high pressure agitation aeration pump device is installed under the tank. And, a foam removal device and an NPR-simple filtration device 33 are installed on one side wall of the bath.

The NPR bioreactor (32, BIO REACTOR) is a stainless perforated plate sieve filled with biowood chips, bio blocks (filter material), oyster shells and volcanic stone as shown in FIG. 3, and an air diffuser is installed under the laminated filter material to be automatically controlled. The air pump (A3) under the control of the device operates intermittently to maintain the activity of the complex microorganism.

In the first rapid oxidation and fermentation tank 30a, a high-pressure agitating aeration pump device 34 for rapid oxidation/fermentation is installed into the stored wastewater, so that the aeration pump (not shown in the drawing) sucks and discharges the wastewater and at the same time, the air intake pipe ( In the drawing, air is sucked in and the inhaled wastewater and air are mixed and injected into the wastewater at high pressure, and by this process, the wastewater is rapidly oxidized/decomposed/fermented. In this rapid oxidation fermentation process, the internal temperature of the wastewater treated water is about 50℃ or higher due to the rapid oxidation/fermentation of organic matter, and the fermentation heat, the treated water that is stirred and sprayed at high pressure, and the supply of air through the air diffuser are NPR. The dominant compound microorganism in the bioreactor 32 naturally increases or decreases according to the flow rate and properties of the treated water, and the treated water is rapidly oxidized/fermented/decomposed by vigorous organic matter decomposition activities, thereby becoming odorless.

In addition, in this process, a large amount of bubbles are floating on the water surface, and the floating bubbles are removed through the above-described bubble removal device 35, and the overwater is separated by the NPR-simplified filtration device 33 partitioned by the partition wall 31. It is discharged to the second rapid oxidation and fermentation tank 30b to be described later while filtering through.

The above-described NPR-simplified filtration device 33 is filtered by a filter medium filled with oyster shells, volcanic stones, anthracite, biowood chips, etc., so that only the filtered water is discharged.

Since the second rapid oxidation and fermentation tank 30b has the same configuration and operation as the above-described first rapid oxidation and fermentation tank 30a, a description thereof will be omitted.

The first and second rapid oxidation and fermentation tanks 30a and 30b described above have the same function by the same configuration. The reason for dividing both fermenters 30a and 30b is to rapidly decompose and oxidize organic matter. That is, when both fermenters (30a) (30b) are integrated, treatment efficiency cannot be rapidly increased as the incoming treated water is frequently added during the fermentation and maturation process, so rapid oxidation and fermentation time of organic matter relative to the same quantity takes more than 72 hours. , By dividing the treatment tank, the fermentation aging degree of the treated water is subdivided and the rapid oxidation/fermentation time is shortened within 72 hours.Therefore, there is an effect of increasing the efficiency of wastewater treatment and capacity, and also lowering the operating load in the subsequent treatment system. The efficiency of purification treatment can be increased. In FIG. 3, reference numeral A4 denotes an air pump.

The overwater treated in the second rapid oxidation and fermentation tank 30b is discharged to the biooxidation reactor 40 through the NPR-simplified filtration device (not shown) described above.

The biooxidation reactor 40 is a treatment tank that stores the treated water discharged from the second rapid oxidation and fermentation tank 30b as shown in FIG. 4, and the NPR bioreactor 42 is installed so as to be immersed in water. , In the lower part of the NPR bioreactor 42, an air diffuser (not shown) is installed to blow air into the treated water through the air pump A5, and the aforementioned NPR-simplified filtration device ( The same NPR-simplified filtration system (not shown in the drawing) as in 43) is partitioned and installed by a partition wall (not shown in the drawing).

Therefore, in the biooxidation reactor 40, the metabolism of the dominant species complex microorganisms adsorbed and parasitic on the biowood chips, bioblocks, oyster shells, and volcanic rocks filled in the NPR bioreactor 42 by the air intermittently supplied by the aeration device As it progresses actively, residual organic substances are decomposed and removed in more detail, and most of the odors of treated water are removed and treated through the decomposition and removal treatment of residual organic substances by this treatment system.

The treated overwater is discharged to the second flow control storage tank 50 through the NPR-simplified filtration device 33 described above.

As shown in FIG. 4, the second flow control storage tank 50 stabilizes and precipitates the treated water flowing in the biooxidation tank 40 and intermittently activates the complex microorganisms through the air lift transfer device 51. The treated water is periodically returned to the aforementioned collection and storage tank 10 and the first flow rate adjustment storage tank 20. In FIG. 4, reference numeral A6 denotes an air pump for blowing air into the air lift conveying device 51 at a predetermined period.

Through periodic conveyance and supply through an air lift, a certain amount of the treated water activated by high-concentration complex microorganisms is returned to the collection and storage tank 10 and the first flow control and storage tank 20, and thus the collection and storage tank 10 and the first flow control and storage tank 20 ) Anaerobic digestion and decomposition of wastewater treated water, reduction of odor, and removal treatment are activated.

Therefore, by lowering the treatment load in the treatment system leading from the first rapid oxidation and fermentation tank (30a) to the biooxidation reactor (40), the treatment efficiency is increased, the treatment time can be further shortened, and the residence time and flow rate are controlled. have.

The second flow control storage tank 50 is a settling tank that stabilizes the treated water discharged from the biooxidation reaction tank 40, and transfers the stored water deposited in the lower portion of the tank to a solid-liquid separation device 60 (see FIG. 5) to separate solid-liquid. After the process, the separated solids are discharged to the compost bed to be converted into organic compost as resources, and the sap component is discharged to the biowood chip trickling filter stage 70.

Accordingly, the aforementioned collection and storage tank 10, the contaminant removal device 11, the first flow control storage tank 20, the first rapid oxidation and fermentation tank 30a, the second rapid oxidation and fermentation tank 30b, the biooxidation reactor 40 And there is no problem in using the treated water modified by the treatment system of the second flow control storage tank 50 as high-quality liquid manure.

On the other hand, the present invention sequentially performs the following treatment system in order to finally purify the treated water in which the complex microorganisms treated by the second flow rate adjustment storage tank 50 are activated at a high concentration to the quality of medium water.

The stored water stored in the above-described second flow control storage tank 50 is transferred to the solid-liquid separation device 60 through a submersible pump P3 as shown in FIGS. 1 and 5 to separate the solid and liquid, and then the separated solid is , The organic compost material is discharged to the compost stage to convert it into a resource, and the sap component is discharged to the biowood chip watering filter stage 70 (FIG. 5).

The biowood chip sprinkling filter top 70 stores the treated water discharged from the solid-liquid separation device in one space 71 divided inside as shown in FIG. 5, and the stored water is transferred to the transfer pump P4. Thus, it is sprayed from the top of the biowood chip sprinkling filter top 70 through the sprinkling device 73.

In the biowood chip sprinkling filter top 70, a diffuser (not shown in the drawing) that blows air into the air pump A7 is installed, and biowood chips are stacked in large/medium/small sizes based on the top. In the lowermost layer, a filter material layer 72 in which oyster shells, volcanic stone, and anthracite are deposited are stacked to a predetermined height.

Therefore, in the biowood chip watering filter stage 70, the complex microorganisms adsorbed and cultured on the NPR biowood chip 72 by the air supplied by the air pump A7 are energetically activated in metabolism and proliferation. While the organic suspended matter contained in the treated water passes through the NPR biowood chip 72, it is adsorbed, decomposed/removed, and the treated biological filtrate is discharged to the third flow control storage tank 80.

As shown in FIG. 5, the third flow adjustment storage tank 80 injects air supplied by the air pump A8 in order to intermittently aerated the introduced treated water (biofilter water) (not shown in the drawing). In order to convert the stored biological filtrate into a low-concentration liquid fertilizer as a resource with an underwater pump (P5), or if necessary, a certain amount can be returned to the wastewater storage tank (1) of the livestock house, and periodically to the aforementioned collection and storage tank (10). While conveying a certain amount, the overwater is discharged to the first aerobic biooxidation reactor 90a.

The above-described collection storage tank 10 promotes anaerobic digestion, oxidation, fermentation, and decomposition of wastewater by the complex microorganisms activated and contained in the biological filtrate returned from the third flow control storage tank 80, thereby improving the treatment efficiency of the subsequent treatment system. Can be enhanced.

The first aerobic biooxidation reactor 90a is a treatment tank that oxidizes, fermentes, and decomposes organic substances remaining in the treated water through the activation of aerobic microorganisms, and air is sprayed through the air pump A9 to the lower part of the tank. An apparatus (not shown in the drawing) and an NPR bioreactor 92 are installed so as to be immersed thereon, and an NPR-simplified filtration device 93 partitioned by a partition wall 91 is installed on one side of the inner wall.

Therefore, in the first aerobic biooxidation reactor (90a), the air supplied intermittently by the air pump (A9) is adsorbed to the filter material (biowood chips, bioblocks, volcanic rocks, oyster shells) filled in the NPR bioreactor 92. As the active metabolism of the cultured dominant species of complex microorganisms takes place, residual organic substances contained in the treated water are oxidized, fermented, decomposed and removed, and the treated water in which the complex microorganisms are activated is the aforementioned NPR-simplified filtration device (drawing code (Not shown) is discharged to the second aerobic biooxidation tank 90b.

As shown in Fig. 6, the second aerobic biooxidation reactor 90b has the same configuration as the first aerobic biooxidation reactor 90a and provides the same effect.

The double arrangement of the first and second aerobic biooxidation reactors 90a and 90b having the same structure is related to treatment efficiency and treatment time as described above. That is, when the amount of wastewater is large, it is to improve the efficiency of decomposition and removal of organic matter in the wastewater and to make it faster.

The treated water treated in the second aerobic biooxidation tank 90b is discharged to the organic material oxidation biofiltration tank 100 in the same manner as in the first aerobic biooxidation tank 90a. In FIG. 6, reference numeral A10 denotes an air pump.

The organic material oxidation biofiltration tank 100 has NPR biowood chips 101a to 101c and oyster shells, volcanic stone, and anthracite 101d stacked 101 as shown in FIG. 7, and a sprinkling device ( 102), an air diffuser 103 (air pump) for intermittently supplying air into the biowood chip is installed in the lower part.

Therefore, when the treated water discharged from the second aerobic biooxidation reactor 90b is sprinkled onto the NPR biowood chip layer through the sprinkler, the organic residue remaining in the treated water during the process of staying and passing through the NPR biowood chip. When the filtered treated water reaches a certain level while adsorbing/decomposing/removing suspended substances, it is transferred to the fourth flow control storage tank 109 by driving a transfer pump (not shown in the drawing).

In the above-described stacked 101 section, the size of the biowood chips is large/medium/small from top to bottom. In this way, the efficiency of adsorption/decomposition/removal of organic residual suspended matter is better when the treated water stays and passes through the stacking 101 section.

The fourth flow adjustment storage tank 109 is a treatment tank that stores the inflow treated water to be stabilized, as shown in FIG. 7, and discharges the treated water stored through the submersible pump P6 to the outside to convert it into a low-concentration liquid manure as a resource, or In response to the discharge of the wastewater storage tank, the biological filtrate is returned to the wastewater storage tank at the bottom of the house through a transfer pump (not shown in the drawing), and the active microbial filtrate in the collection and storage tank 10 through an air lift device (not shown in the drawing). The overwater is transferred to the first advanced treatment tank 110a while being returned to the furnace at regular intervals.

The first advanced treatment tank 110a is equipped with an air diffuser (not shown) that injects air supplied by the air pump A12 in the lower part of the tank, and an NPR block (Ball type), which is a media filter for advanced treatment, is installed at the bottom of the tank. ) And ceramic balls, volcanic stone, and oyster shells are sequentially filled with an NPR reactor 112 is immersed, and an NPR-simplified filtration device 113 partitioned by a partition 111 is installed on one inner wall.

In the first advanced treatment tank 110a, while being aerated by air intermittently supplied by the air pump A12, the components of the media are dissolved in the treated water by abandoning the contact between the media for advanced treatment and the treated water. Adsorption, decomposition and removal of included residual organic matter, harmful bacteria, nitrogen, phosphorus, heavy metals, and pigment components, and the treated overwater is discharged to the second advanced treatment tank 110b via the NPR-simplified filtration device 113 do. In FIG. 8, reference numeral 111 denotes a partition wall.

As shown in FIG. 8, the second advanced treatment tank 110b is a treatment tank that reprocesses with the same configuration and function as the first advanced treatment tank 110a, and the processed overwater is a simple filtration device (not shown in the drawing). It is filtered through, and when the filtered water reaches a certain level, the transfer pump P7 is operated to spray water from the top of the NPR-biofiltration tank 120.

As shown in FIG. 9, the NPR biofiltration tank 120 has biowood chips, NPR blocks, and advanced processing media made of various natural minerals in the tank.

Therefore, the sprinkled treated water is residual organic matter remaining in the treated water while staying and passing through the media filter layer 121 in which complex microorganisms activated by air intermittently supplied by the air pump A14 are adsorbed/cultivated, It adsorbs, decomposes, removes, and treats harmful bacteria, nitrogen, phosphorus, heavy metals, and pigment components, and the filtered treated water is transferred to the sterilization and sterilization tank 130 through the transfer pump P8. At this time, 98% of organic matter remaining in the treated water, about 80% or more of nitrogen and phosphorus are removed, more than 99% of heavy metals are removed, and 95% or more of pigments are removed.

As shown in FIG. 9, the sterilization and sterilization tank 130 is installed so that a sterilization means such as an ultraviolet sterilizer 131 or a sterilizer is immersed, and after sterilizing and disinfecting the introduced treated water, the overwater is decolorized and filtered under natural flow. To discharge.

As shown in FIG. 10, the decolorization filtration tank 140 is equipped with a multistage filtering chamber (not shown) connected to each other in a zigzag manner, and granular activated carbon and NPR blocks are mixed in a 2:1 ratio in the filter chamber. It is filled.

Therefore, 99.9% of various bacteria and fungi are removed from the treated water flowing into the decolorization filtration tank 140 while slowly staying and passing through the multi-stage filter chamber, and the turbidity is purified to the water quality of heavy water (urban reuse water based on the Ministry of Environment notification). And the overwater is transferred to the treated water storage tank 150 through natural flow.

As shown in FIG. 10, the treated water storage tank 150 is recycled as cleaning water and agricultural water through the water supply pump P9 while storing the treated water treated with the medium water quality discharged from the above-described decolorization filtration tank 140. , Pig farming drinking water can be recycled and recycled, and excess excess water can be discharged to the outside.

FIG. 11 is an MCC control panel 200 for controlling components operated by each treatment tank or reaction tank included in the treatment tank or reaction tank, various transfer pumps, or power sources operated as described above with an electric circuit. , If a person having ordinary knowledge in the technical field to which the present invention belongs can sufficiently understand the MCC control panel 200, and a configuration that can be implemented, a more detailed description will be omitted.

All of the above-described NPR-simplified filtration devices are filled with filtering media such as oyster shells, volcanic stone, and anthracite.

In addition, "NPR" as defined in the present invention is the English initial of a reactor for removing nitrogen and phosphorus, and registered trademark 4008407090000 (trade name: NPR, designated product: manufactured with oyster shell for manure filtration equipment) Filter materials, etc.).

As described above, according to the present invention, the high-concentration livestock wastewater slurry discharged from the livestock house can be rapidly oxidized and fermented to become a resource as liquid manure or compost, and in connection with the system purification treatment, the filtered water of complex microorganisms is used in the pig farm. By circulating and recycling into the storage water in the lower wastewater storage tank, it activates the microorganisms in the slurry storage water and reduces the load and homogenization of the wastewater slurry through the anaerobic digestion function, while reducing and removing odors generated from the wastewater slurry, significantly in subsequent system treatment. It can reduce the treatment capacity and significantly improve the operating load and treatment efficiency, and the high-concentration livestock manure wastewater is purified to the medium water quality (urban reuse water quality based on the Ministry of Environment notification) through the advanced purification treatment of the surplus treated water. Recycling can be recycled or excess water can be discharged.

10: collection and storage tank 11: contaminant separation device
20: first flow adjustment storage tank 30a: second rapid oxidation and fermentation tank
30b: second rapid oxidation and fermentation tank 40: biooxidation reactor
50: second flow adjustment storage tank 60: solid-liquid separation device
70: top of biowood chip sprinkling filter 80: 3rd flow control storage tank
90a: No. 1 biooxidation reactor 90b: No. 2 biooxidation reactor
100: organic material oxidation biofiltration tank 109: 4th flow control storage tank
110a: the first advanced treatment tank 110b: the second advanced treatment tank
120: NPR biofiltration tank 130: sterilization and sterilization tank
140: decolorization filtration tank 150: treated water storage tank

Claims (3)

Storage and storage of the livestock manure wastewater slurry discharged from the livestock wastewater storage tank (1) and agitating it through an aerated stirrer to prevent slurry precipitation and solidification and malignant anaerobicity, smoothing and homogenizing wastewater above a certain level through an underwater pump A collection and storage tank 10 for discharging;
The wastewater slurry conveyed from the collection and storage tank 10 is filtered out of inorganic solid contaminants through a detailed screen of a certain standard, and the filtered contaminants are compressed by a pressing screw and discharged separately, and the sap desorbed in this process is the first flow rate. An impurity separation device 11 discharged to the controlled storage tank 20;
Stores the sap desorbed by the contaminant separation device 11, and intermittently agitates the stored water through an aeration-type stirring device to prevent precipitation and solidification of the slurry, as well as malignant anaerobicity, while preventing the precipitation and solidification of the slurry, as well as the first overwater through an underwater pump. A first flow rate adjustment storage tank 20 discharged to the rapid oxidation and fermentation tank 30a;
Organic suspended matter contained in the stored water through the rapid oxidation/fermentation device and NPR bioreactor installed inside the first rapid oxidation/fermentation tank 30a to receive the treated water introduced from the first flow rate adjustment storage tank 20 It is equipped with a foam removal device to rapidly oxidize/ferment the water and remove a large amount of foam generated during this process, and complex microorganisms of dominant species adsorbing/parasitic to the media filled in the NPR bioreactor are applied to the flow rate and properties of the treated water. As a result, it naturally increases and decreases, and functions to decompose and remove organic substances. In this process, self-fermentation heat of 50°C or higher is generated, and odors are decomposed and removed along with organic substances through the rapid oxidation and fermentation of organic substances. A first rapid oxidation and fermentation tank (30a) for discharging the overwater to the second rapid oxidation and fermentation tank (30b) through an NPR-simplified filtration device installed on the side wall;
Reprocessing the treated water flowing from the first rapid oxidation and fermentation tank 30a with the same function by the same configuration and function as the first rapid oxidation and fermentation tank 30a, while discharging the excess water to the biooxidation reactor 40 2 rapid oxidation and fermentation tank (30b);
By accommodating the treated water discharged from the second rapid oxidation and fermentation tank (30b), and intermittently supplying air through an aeration device mounted inside the tank, the metabolism of the dominant species parasitic in the NPR bioreactor is actively promoted. A bio-oxidation reactor (40) for discharging excess water through an NPR-simplified filtration device installed on the inner wall of the tank while decomposing and removing organic substances contained in the treated water;
The treated water discharged from the biooxidation reaction tank 40 is stabilized so as to precipitate, and the treated water, in which the complex microorganisms are activated through the air lift transfer device, is transferred to the collection and storage tank 10 and the first flow control storage tank 20 as a donor of the complex microorganism. While periodically conveying a certain amount, the treated water is selectively discharged to the composting stage 300, mixed and fermented with organic compost materials such as sawdust, rice husk, and rice straw to make organic compost. The second flow adjustment storage tank 50 discharged to the watering filter top (70)
A system for recycling and recycling livestock wastewater to be used as a resource and for purification and treatment. While storing the treated water discharged from the second flow control storage tank 50 described in Paragraph 1, the sediment water precipitated at the bottom of the tank is separated into solid and liquid through a solid-liquid separator to discharge the solids and convert them into organic compost materials. A solid-liquid separation device 60 for discharging the components to the biowood chip sprinkling filter top 70;
While the treated water discharged from the solid-liquid separation device 60 is stored in a partitioned tank, the treated water stored through the sprinkling device is sprinkled on the NPR biowood chip in which the complex microorganisms are adsorbed and cultured, and the treated water stays and passes through A biowood chip sprinkling filter stage (70) for adsorbing organic suspended matter contained in the treated water during continuous decomposition and removal treatment, and discharging the treated biological filtrate to the third flow control storage tank (80);
The bio-filtered water discharged from the biowood chip watering filter top (70) is stored in a stable manner, and the stored bio-filtered water is discharged and converted into a low-concentration liquid manure, or periodically returned to the collection and storage tank (10) through an airlift conveying device to provide a complex microbial donor. A third flow rate control storage tank 80 which can be supplied to and optionally supplied to an active microbial donor of the wastewater storage tank at the lower part of the house through a transfer pump, and transfers overwater to the first aerobic biooxidation tank 90a;
The treated water transferred from the 3rd flow control storage tank 80 is received, and air is supplied into the bioreactor through an air diffuser installed inside the tank to actively promote the metabolism of the dominant species complex microorganisms. A first aerobic biooxidation reactor (90a) for discharging the treated water in which the complex microorganisms are activated while decomposing and removing residual organic matter through an NPR-simplified filter installed on the inner wall of the tank;
The second aerobic bio-oxidation reactor reprocessing the treated water discharged from the first aerobic bio-oxidation reactor 90a with the same configuration and function as the first aerobic bio-oxidation reactor 90a and discharged through the NPR-simplified filtration device ( 90b) and;
The treated water discharged from the second aerobic biooxidation reactor 90b is sprinkled on the layer of NPR biowood chips where complex microorganisms are cultivated/adsorbed through a sprinkling device and air is intermittently supplied through the aeration device. An organic material oxidation biofiltration tank 100 for adsorbing/decomposing/removing organic residual suspended matter remaining in the treated water while remaining in the bed and passing through the treated water and discharging the filtered treated water to the fourth flow control storage tank 109;
An airlift conveying device for storing the treated water discharged from the organic material oxidation biofiltration tank 100 to be stabilized and discharging the stored treated water as a resource as a low-concentration liquid manure or using it as a biofiltration water (donor) of the collection and storage tank 10 A certain amount of odors generated in the lower wastewater storage tank of the livestock can be reduced and removed by returning a certain amount to the collection and storage tank 10 through a transfer pump or by circulating and recycling the storage water in the lower wastewater storage tank of the livestock house through a transfer pump. In the system treatment that follows through recycling, the treatment capacity and operating load are drastically reduced to increase the treatment efficiency, and as a result, the flow rate of the final treated effluent can be drastically reduced, while the surplus overwater is reduced to the first advanced treatment tank (110a). To the fourth flow adjustment storage tank 109 discharged to the,
A system for recycling and recycling livestock wastewater as a resource and purification treatment, characterized in that it is configured. An air diffuser device installed inside the tank to supply air while storing the treated water transferred from the fourth flow control storage tank 109 described in paragraph 2, and the NPR reactor filled inside the NPR reactor by air supplied by the air diffuser device. NPR block and MIDEA for advanced treatment composed of natural minerals and aerated to adsorb/decompose/remove residual organic matter, harmful bacteria, nitrogen, phosphorus, heavy metal, chromaticity components, etc. contained in the treated water, and remove excess water into the tank. A first advanced treatment tank 110a for discharging to the second advanced treatment tank 110b through an NPR-simplified filtration device installed on the side wall;
With the same configuration and function as the first advanced treatment tank 110a, the second advanced treatment tank for reprocessing the treated water flowing from the first advanced treatment tank 110a and discharging the excess water through the NPR-simplified filtration device ( 110b);
Equipped with a media layer for advanced treatment consisting of NPR biowood chips, NPR blocks, and natural minerals, and an aeration device for supplying air into the filter media layer, and spray the treated water discharged from the second advanced treatment tank 110b. Water is sprayed to the top of the filter media layer through the device to adsorb/decompose/remove residual organic matter, harmful bacteria, nitrogen, phosphorus, heavy metals, and pigment components remaining in the treated water while the treated water stays and passes through the media layer, and is filtered. An NPR biofiltration tank 120 for discharging the water to the sterilization and sterilization tank 130;
A sterilization and sterilization tank 130 for discharging the overwater to the bleaching filtration tank 140 while sterilizing/sterilizing through a sterilization and sterilization device installed to be immersed in the treated water introduced from the NPR bio-filtration tank 120;
While receiving the treated water discharged from the sterilization and disinfection tank 130, while staying and passing through a multistage filter chamber filled with granular activated carbon and NPR blocks, the treated water is decolorized/sterilized/sterilized, and the treated water flows naturally. A decolorization filtration tank 140 discharged to the furnace treated water storage tank 150;
It is characterized by consisting of a treated water storage tank 150 that discharges and discharges excess water through a discharge pipe while storing the treated water discharged from the bleaching filter tank 140 and recycling it as agricultural water and cleaning water through a transfer pump. Livestock wastewater recycling and purification treatment circulation recycling system.

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