KR200357623Y1 - Advanced treatment system for foul water of middle.small size village by using a media - Google Patents

Abstract

The present invention relates to a medium and small scale sewage treatment system using a media, and the conventional sewage treatment apparatus is capable of treating organic substances at a certain concentration, but is not easily removed from nitrogen and phosphorus (TP) and requires a lot of operating costs. There is this.

The present invention has a flow rate adjusting tank when the sewage treatment system 110 is composed of a collecting tank 110, a flow adjusting tank 120, an aeration tank 130, a sedimentation tank 140, a filtration tank 150, a parcel and a discharge tank 160. The microorganism growth tank 170 in which the media 172 is stacked is formed at one side in the 120, and an anaerobic tank 180 and an anaerobic tank 190 are installed between the flow rate adjusting tank 120 and the aeration tank 130, and the aeration tank is installed. The media 132 is stacked in the 130, and a circulation water tank 200 is provided between the aeration tank 130 and the precipitation tank 140 to re-supply a portion of the treated water to the oxygen-free tank 190. By filling the media 152 for culturing microorganisms and returning the backwash water of the filtration tank 150 to the aeration tank 130, the present invention changes the flow of water by stacking a large amount of media in the microbial growth tank and the aeration tank and the filtration tank. It is possible to stably grow microbial culture in spite of inflow quantity change and water quality variation. Since the entire system excellent in nitrogen and phosphorus removal efficiencies will have highly processable on low cost.

Description

Advanced treatment system for foul water of middle.small size village by using a media}

The present invention relates to a medium and small scale sewage treatment system using media, and more specifically, by using the biopurification principle of the natural ecosystem food chain, the aerobic microorganisms are increased in cultivation efficiency and nitrogen contained in sewage / sewage (TN). The present invention relates to a medium and small scale sewage treatment system using medium, which is economical due to its high efficiency in removing TP and phosphorus, and low cost of facilities and maintenance.

In general, in Korea, the pollutant characteristics of various sewage, industrial and livestock wastewater and domestic sewage (hereinafter referred to as “sewage / sewage”) are quite complicated due to the unauthorized discharge of pollutants such as homes, small household industries, and livestock farms. These sewage / sewage contain large amounts of nitrogen (TN) and phosphorus (TP).

In addition, long research has shown that nitrogen (T-N) and phosphorus (T-P) contained in sewage / sewage are the main culprit causing red tide and water pollution. Therefore, sewage / sewage should always be treated with purified water and discharged with BOD (Bio Oxygen Demand: BOD) as low as possible to avoid violation of relevant regulations.

In other words, the various sewage / sewages contain large amounts of organic substances nitrogen (TN) and phosphorus (TP) that contaminate rivers and shores, and contain large amounts of chromaticity. Due to the fact that the ecosystem is seriously destroyed, such as the death of the lice, the water quality standards of the effluent are gradually being strengthened.

For example, sewage treatment plants have regulated nitrogen (TN) and phosphorus (TP) since 1996, and are expected to be applied to sewage treatment in the future, and BOD (biological oxygen demand) and SS, nitrogen and phosphorus (TP) It can be interpreted as irrelevant, but water quality analysis shows that nitrogen and phosphorus (TP) increase simultaneously when BOD and SS are high.

Therefore, the existing treatment process such as activated sludge requires excessive aeration tank capacity to remove nutrients such as nitrogen and phosphorus (TP), and has a limit in the ability to cope with sudden load fluctuations. There are many difficulties in management.

In addition, it is widely known that the improvement of final treatment efficiency and performance in biological sewage treatment can improve the final treatment efficiency by increasing the concentration of microorganisms. It should be maintained more than 5,000mg / ℓ in the existing activated sludge treatment process is a problem that the separation of microorganisms in the sedimentation tank is not a good result.

In order to solve these problems, methods of using various growth-grown microorganisms have been steadily studied.However, the water quality standards for effluents until 1999 were regulated to BOD 80mg / l or less except for the protected water source. It is gradually strengthened to less than 10mg / ℓ, the advanced treatment is required.

To solve this problem, currently developed and used biological treatment methods using the sewage / sewage purification treatment system include Patent No. 272758 and Utility Model 190709, and Chemical Treatment Method includes Patent No. 278798.

However, the treatment methods are capable of treating a certain concentration of organic material, but the nitrogen (T-N) and phosphorus (T-P) components, which are always a problem when purifying sewage / sewage, are not effectively removed.

In addition, even though the development of treatment technology complementing this is being actively researched or developed, it is not practically used in the field due to the high facility cost, high operating cost, and economic feasibility. Accordingly, a considerable amount of nitrogen (TN) and phosphorus (TP) Actual countermeasures have not been established for the treatment of sewage / sewage containing large amounts of components.

Therefore, the present invention was developed to solve the above-mentioned conventional problems after long experience and research in the field, and an object of the present invention is to rapidly culture aerobic microorganisms that lower BOD of sewage / sewage. Medium and small sized media that can be operated unattended (TN), phosphorus (TP), BOD, COD, SS have good processing efficiency, low construction cost and maintenance cost, and suitable for medium and small capacity. It is to provide village sewerage altitude treatment system.

1 is a block diagram showing a process of the present invention

2 is a processing system diagram showing a processing procedure of the present invention.

Explanation of symbols for main parts of the drawings

120: flow adjustment tank 121,131: air supply pipe

130: aeration tank 132,152,172: media

140: sedimentation tank 150: filtration tank

170: microbial growth tank 180: anaerobic tank

190: anoxic tank 200: circulation tank

210: caustic soda chemical tank 220: PAC chemical tank

Hereinafter, described in detail by the accompanying drawings the technical configuration and operation of the preferred embodiment that can effectively achieve the above object of the present invention.

1 is a block diagram showing a treatment process of the present invention, Figure 2 is a process flow diagram showing the treatment process of the present invention, the sewage / sewage is collected in the collecting tank 110, then the flow adjustment tank 120, aeration tank 130 , Through the sedimentation tank 140, the filtration tank 150 in order to be discharged through the defoaming and discharge tank 160 can be said to be the same as the conventional configuration.

The present invention is to form a microbial growth tank 170 in which the media (172) is stacked in a portion in the flow control tank 120 is supplied air through the air supply pipe 121 connected to the blower (B) Characterized in that, between the flow control tank 120 and the aeration tank 130, the anaerobic tank 180 for releasing phosphorus (TP) and nitrogen oxides to nitrogen gas while the absorption of organic matter by the microorganism occurs in the nitrogen gas (190) It is characterized by the installation.

In addition, the air supply pipe 131 connected to the blower (B) is installed on the floor, the usual aeration tank 130 is also characterized in that the media 132 is stacked and installed, between the aeration tank 130 and the settling tank 140 The circulating water tank 200 is installed to remove nitrogen and phosphorus by adjusting the concentration of dissolved oxygen (DO) and to re-supply some of the treated water to the oxygen-free tank 190.

In addition, the treated water line between the circulation water tank 200 and the settling tank 140 is connected to the supply line of the caustic soda drug tank 210 and the PAC drug tank 220, characterized in that the phosphorus flocculant is supplied when necessary do.

And the filtration tank 150 is the air supply pipe 151 connected to the blower (B) is installed on the bottom, the microorganism group is deposited aging with the sludge generation amount is reduced by filling the media 152 cultivated by contacting the microorganism on the top The microorganisms that induce dropout and have good activity are characterized in that they are formed to be returned to the aeration tank 130 through the backwash line 153.

In the drawing, reference numeral P1 denotes a pump for pumping and supplying sewage / sewage of the flow adjusting tank 120 to the anaerobic tank 180, and P2 recirculates the treated water of the circulation tank 200 to the anaerobic tank 190. Pump (P3) is a pump for supplying the settling sludge (sludge) of the settling tank 140 to the sludge concentration tank 230 or the anaerobic tank 180, (P4) is a sludge concentration tank (230) bottom of the sludge tank It is a pump to be sent to 240, (P5) is a pump to send the treated water of the defoaming and discharge tank 160 to the aeration tank 130 to be sprayed.

The sewage / sewage that is discharged through the defoaming and discharge process after going through each treatment process such as flow control process, aeration process, sedimentation process, and filtration process of the sewage / sewage collected in the collection tank among the process by the treatment system of the present invention Can be said to be the same as the conventional method. A feature of the present invention is to change the flow of water flowing into the water collecting tank 110 by the media 172 filled therein before performing the flow adjusting process in the flow adjusting tank 120 to multiply a large amount of microorganisms to improve the sewage / sewage. The microbial growth step is carried out to allow the flow to enter the flow control tank in the first purified state. The present invention formed as described above is because the media 172 is stacked in the microbial growth tank 170 in the flow control tank 120, the water flow chart By changing the media 172, a large number of microorganisms are proliferated, and are resistant to inflow quantity changes and water quality (load) variations. In particular, since the microorganism growth tank 170 serves as a high tide and low tide when the sewage / sewage flow into the flow adjustment tank 120, the purification is primarily performed on the same principle as when the natural tidal flat is purified.

The present invention is characterized in that it precedes the anaerobic treatment step for the absorption of organic matter by the microorganisms of the sewage / sewage and the anoxic treatment step for changing nitrogen oxides into nitrogen gas before performing the aeration process. When the sewage / sewage containing a large amount of microorganisms in the microorganism growth tank 170 in the adjustment tank 120 flows into the anaerobic tank 180, the anaerobic tank 180 is absorbed by the microorganisms and the phosphorus contained in the sewage / sewage ( TP) component is well released, and in the anoxic tank 190, nitrogen oxide is changed to nitrogen gas in anoxic state so that phosphorus (TP) removal is prevented from interfering with the release of phosphorus component with nitrogen removal throughout the system. Effectively done

And when the media 132 is stacked in the aeration tank 130 through which the air is supplied to the sewage / sewage through the air supply pipe 131, the attachment and desorption of microorganisms sensitive to water temperature is periodically performed (7-10 days: slightly depending on the growth of microorganisms). Of the microorganisms are stable, and the growth of the microorganisms is stable, and the growth of microorganisms is stable. Accordingly, in the aeration tank 130, organic matter decomposition and nitrification occur simultaneously. Sufficient intake of phosphorus (TP) will occur.

In addition, the present invention precedes the step of adjusting the dissolved oxygen (DO) concentration and recirculating some of the treated water in the anaerobic treatment step before the precipitation process, and in the filtration process using the media, the microorganisms have a large amount of microorganisms while filtering the sewage / sewage. And carrying out the step of returning the contained backwash water to the aeration process. In this way, in the circulating water tank 200 into which the sewage / sewage is introduced, nitrogen (T-N) and phosphorus (T-P) removal efficiency may be improved by adjusting dissolved oxygen (DO) concentration in the entire system.

And when the phosphorus of the sewage / sewage flowing into the sedimentation tank 140 from the circulation water tank 200 is not sufficiently made, caustic soda and phosphorus flocculant through the caustic soda drug tank 210 and PAC drug tank 220 and Since the PAC chemicals can be added to increase the cohesion of phosphorus in the settling tank 140, such chemicals of the phosphorus flocculant should be used only in an emergency where phosphorus removal is not sufficient.

In addition, in the settling tank 140, the sludge generation amount can be said to be considerably less than that of the conventional treatment method because the sludge rich in dissolved oxygen (DO) in the sedimentation state is lowered to the outside.

In addition, the aeration tank 150 is also attached to the filled media (152), aerobic microorganisms are cultured to remove a significant amount of sludge, making the sludge generated by the sludge insignificant, the aging deposited microbial group induces dropout and activity Some of the good microorganisms are returned to the aeration tank 130 together with backwashing water, thereby increasing the removal efficiency of nitrogen, phosphorus and COD components throughout the system.

As described above, the treatment system of the present invention changes the flow chart by stacking a large amount of media in the microbial growth tank, the aeration tank, and the filtration tank in the flow control tank, and stably propagates the microbial culture even in the inflow amount change and the water quality fluctuation. It has excellent effect of removing impurities such as (TN) and phosphorus (TP), and it is possible to perform advanced treatment of sewage / sewage generated in small and medium-sized villages.

In addition, the structure is simple compared to the prior art, the facility cost is low, but the operation according to the process is simple and economical due to the low maintenance costs, it is easy to cope with the load fluctuations and there is less effect on the climate.

In addition, the sludge generation amount is small, and sludge conveyance may be intermittently carried out, and the sewage / sewage generated in the small and medium-sized villages can be processed at high altitude, and the operation can be performed without permission, thereby reducing the cost.

Claims (2)

Sewage / sewage is collected in the sump (110) and then discharged through the parcel and discharge tank 160 through the flow adjustment tank 120, aeration tank 130, sedimentation tank 140, filtration tank 150 in order. In constructing the processing system, The microorganism propagation tank 170 in which the media 172 is stacked is installed at one portion in the flow control tank 120 through which air is supplied, and the organic matter absorption by the microorganism is between the flow control tank 120 and the aeration tank 130. Install an anaerobic tank 180 to occur and an oxygen-free tank 190 to change the nitrogen oxides into nitrogen gas in sequence, The median 132 is stacked and filled in the aeration tank 130, and between the aeration tank 130 and the precipitation tank 140, a dissolved oxygen (DO) concentration adjustment and a recirculating water tank for supplying a part of the treated water to the anoxic tank 190 ( 200), The filtration tank 150 fills the media 152 for culturing microorganisms on the air supply pipe 151 installed on the bottom, and the medium and small town using media, characterized in that backwash water is returned to the aeration tank 130. Sewage Advanced Treatment System. The method of claim 1, Median characterized in that the phosphorus flocculant is supplied when necessary by connecting the supply line of the caustic soda drug tank 210 and the PAC drug tank 220 to the treated water supply line between the circulation tank 200 and the sedimentation tank 140 Medium and small town sewage altitude treatment system using