KR200182581Y1 - A waste water disposal apparatus - Google Patents

Abstract

The present invention provides a screen for filtering large contaminants, a flow regulating tank for adjusting the flow rate of influent sewage, a flow regulating foot, a contact aeration tank containing a microbial contact material, a sedimentation tank for removing suspended solids in the treated water treated by the contact aeration tank, and a discharge. Between the tank, a thickening tank for storing the solids precipitated by the settling tank, a thickening tank for condensing the solids stored in the thickening tank, a broa for supplying air in the contact aeration tank, a diffuser for small dispersion of the air supplied by the broa, and each treatment tank. A sewage treatment apparatus composed of a transfer pump that is responsible for the transfer of sewage, the contact aeration tank comprising: a first contact aeration tank having a residence time of about 22-26 hours and a second contact aeration tank having a residence time of 1 hour to 3 hours. It is composed of stages, the settling tank is installed in the next stage of the first settling tank and the second contact aeration tank installed after the first contact aeration tank The sewage treatment apparatus, characterized in that it consists of two sets of the second settling tank, the sewage treatment apparatus of the present invention is highly efficient so that the treated water BOD and SS is 5ppm or less without additional physical and chemical treatment equipment, respectively This has the advantage of being able to perform sewage treatment.

Description

Sewage Treatment Equipment {A WASTE WATER DISPOSAL APPARATUS}

The present invention relates to a sewage treatment apparatus using a two-stage contact aeration tank, and more specifically, a BOD in sewage, including a first contact aeration tank having a residence time of 22-26 hours and a second contact aeration tank having a residence time of 1-3 hours, The present invention relates to a sewage treatment apparatus which can reduce SS to 5 ppm or less.

Recently, the pollution of rivers and lakes caused by domestic sewage has become a serious problem, and the standard of discharged water quality has been strengthened. Specifically, among the parameters for evaluating the degree of pollution of sewage, the most important BOD (biochemical oxygen demand) and SS (float amount) are treated to be discharged to 10 ppm or less. Therefore, there is an urgent need for the development of a sewage treatment apparatus having a high treatment capacity capable of easily operating a facility and treating BOD and SS of discharged water to 10 ppm or less without requiring separate maintenance.

Among the sewage treatment methods, the chemical treatment method using chemicals has received much attention because biological treatment methods cause additional pollution. Currently, activated sludge process, catalytic oxidation method and rotating disc method are mainly used as biological sewage treatment methods. Among them, activated sludge process is excellent in treated water quality, but requires sophisticated technology to maintain the concentration of suspended microorganisms and side effects such as bulking phenomenon. Due to this problem, there is an inadequate limit to small-scale sewage treatment facilities such as restaurants and inns.

On the other hand, the catalytic oxidation method is a method of aeration by putting a microorganism contact material that can be attached and grown microorganisms in the microbial culture tank, there is little sludge generation, simple equipment and easy maintenance, but the BOD of the treated water is 20 to 30ppm In order to meet the effluent water quality standards, it is disadvantageous to use a combination of physical and chemical treatment methods such as sand filter, activated carbon adsorption tower, ozone oxidation treatment and chemical flocculation treatment. However, these physical and chemical treatment facilities are usually expensive, expensive to maintain and complicated to operate, so there is a problem in that they cannot operate properly without a manager who has expertise.

It is an object of the present invention to provide a sewage treatment apparatus having a very good treatment capacity capable of treating BOD and SS of sewage to 5 ppm or less with only a contact aeration tank having simple facilities and simple maintenance in biological treatment facilities.

That is, one aspect of the present invention is a screen for filtering large contaminants, a flow regulating tank for adjusting the flow rate of influent sewage and a flow regulating foot, a contact aeration tank including a microbial contact material, and suspended matter in the treated water treated by the contact aeration tank. Sedimentation tank for discharging water, discharge tank, concentration tank for storing solid precipitated by sedimentation tank, concentration storage tank for condensing solids stored in concentration tank, broach for supplying air in contact aeration tank, diffuser for small air scattered by broa And a transfer pump that is responsible for the transfer of wastewater between the respective treatment tanks, wherein the contact aeration tank has a first contact aeration tank having a residence time of about 22-26 hours and a residence time of 1 hour to 3 hours. It consists of two stages of a 2nd contact aeration tank, and the said 1st precipitation tank and the 2nd contact width which the said precipitation tank was installed in the next stage of a 1st contact aeration tank. To provide a sewage treatment apparatus, characterized in that consists of twos, section 2 of the second settling tank is installed in the following stage.

1 is a schematic view of a sewage treatment apparatus having a two-stage contact aeration tank of the present invention,

FIG. 2A is a side view illustrating a method for installing microbial contact material and diffuser in a first contact aeration tank of the sewage treatment apparatus of FIG. 1; FIG.

Figure 2b is a cross-sectional view illustrating the installation of microorganism contact material and diffuser in the first contact aeration tank of the sewage treatment apparatus of Figure 1,

3 is a structural diagram of a second contact aeration tank of the sewage treatment apparatus of FIG. 1.

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

Sewage treatment apparatus using a two-stage contact aeration tank of the present invention is configured as shown in FIG. That is, the sewage treatment apparatus of the present invention includes a screen (1), a flow regulating tank (2), a flow adjusting feet (3), a first contact aeration tank (4), a first precipitation tank (5), a second contact aeration tank (6), and a first It consists of two settling tanks (7), a discharge tank (8), a concentration tank (9), a concentrated storage tank (10), a broa (11), a microbial contact material (12), an acid pipe (13), and a transfer pump (14). .

Screen (1) of the device of the present invention is a device for filtering large contaminants in consideration of the inflow degree and size of the contaminants, and use a bar screen and a sieve screen of a certain grid.

The flow rate adjusting tank 2 installed at the next stage of the screen 1 is an apparatus for sending the incoming sewage to the first contact aeration tank 4 evenly. In case of 6 hours, it should have a volume that stays for more than 15 hours, and in order to prevent anaerobic, inject 1㎥ / min of air per 1㎥ of crude volume and mix it evenly.

The flow adjusting feet 3 are devices for allowing the wastewater of the flow adjusting tank 2 to be conveyed to the first contact aeration tank 4 by a predetermined amount, and return to the V-shaped groove and the flow adjusting tank 2 for measuring the amount of conveyed water. A switchgear is provided.

The sewage treatment apparatus of the present invention is characterized in that the contact aeration tank is composed of two stages: a first contact aeration tank having a residence time of 22 to 26 hours and a second contact aeration tank having a residence time of 1-3 hours. Microbial contact material 12 for microbial attachment is installed, the amount of microbial contact material is installed in the first contact aeration tank 30 to 80m of microbial contact material is installed per aeration tank volume, the second contact aeration tank of 100 to 400m per volume of aeration tank Microbial contact materials are installed.

Specifically, the volume of the first contact aeration tank 4 is such that the retention time of the sewage is 22-26 hours, and in order to prevent the impact load on the BOD load, the chamber is divided into two, three, or four chambers. good. In case of dividing into two rooms, 60% of the first room and 40% of the second room should be divided into 50% of the first room, 30% of the second room, and 20% of the third room. In case of dividing into four rooms, it is preferable that the first room is 40%, the second room is 30%, the third room is 15%, and the fourth room is 15%.

The method for installing the microbial contact material in the first contact aeration tank 4 and the method for installing the diffuser are schematically shown in FIG. In the case of installing the microbial contact material in the first contact aeration tank, in order to prevent the blockage of the microbial contact material 12 and the resulting decay, it is necessary to walk a predetermined distance between the contact aeration tank and the microbial contact material in the up and down direction. good. For example, the distance (a) between the wall of the first contact aeration tank and the microbial contact material needs to be 300-500 mm, and the microbial contact material is installed at a distance (b) of 300-500 mm under water in the first contact aeration tank. It is desirable to be. In addition, the microbial contact material is preferably installed at a predetermined distance (c), preferably 400-700mm from the bottom, and, if the diffuser is installed between the microbial contact materials (d) ) Needs to be secured about 600-1000 mm.

The microbial contact material 12 installed in the first and second contact aeration tanks of the sewage treatment apparatus of the present invention is the most important factor in determining the removal efficiency of the contaminants in the contact aeration tank. In order to improve the treatment efficiency, it is recommended to use a surface area of 1.0 m2 or more per unit length. Synthetic fibers having high chemical resistance and durability such as nylon and polyvinylidene chloride are preferable.

The first contact aeration tank 4 is a main device for removing BOD and SS in the sewage, and about 90 to 95% of the BOD is removed. In general, since the BOD and SS of the raw sewage water are about 200 ppm, the BOD and SS of the treated water having passed through the first contact aeration tank 4 are about 10 to 20 ppm.

The first settling tank 5 is a device for removing suspended matter in the treated water treated in the first contact aeration tank, and its water surface load is suitably 30 m 3 / m 2 .day. Here, the solids settle to the bottom and the treated water is transferred to the next treatment through the weir. Solids settled in the lower part are periodically transferred to the concentration tank (9).

The main feature of the present invention is the second contact aeration tank 6, which is about 1/10 the capacity of the first contact aeration tank 4, which is used to remove residual BOD and SS that have not been treated in the first contact aeration tank 4. It is to be able to process below 5ppm. The capacity of the second contact aeration tank 6 is such that the residence time is 1-3 hours and constitutes one chamber. In the second contact aeration tank 6, as in the first contact aeration tank, a microbial contact material 12 is installed, preferably 100 to 400 m of microbial contact material per aeration tank volume. In addition, as shown in Figure 3, the microbial contact material 12 is installed on the front of the second contact aeration tank (6) to act as a biofilter and to install the diffuser 13 to the front aeration. When the second contact aeration tank 6 is operated for a predetermined time, clogging due to biofiltering is generated, thereby reducing processing efficiency. In this case, the diffuser 13 may be used to remove the clogging. In the second contact aeration tank 6, the diffuser 13 serves as the original diffuser when air is injected at a weak pressure, but is excessively attached when strongly blowing air to remove a clogging phenomenon. It acts as a desorption device to desorb the microorganisms. The bottom of the second contact aeration tank of the present invention is configured to be inclined to collect and remove the detached microorganism toward the transfer pump (14). The desorbed microorganisms collected along the inclined plane toward the transfer pump are taken out to the concentration tank 9 by the transfer pump 14 which functions as the desorption microorganism removal device. As described above, in the present invention, the second contact aeration tank 6 serves to completely remove residual BOD and SS that are not decomposed in the first contact aeration tank 4 and the BOD of the treated water passing through the second contact aeration tank 6. And SS is 5 ppm or less.

Like the first precipitation tank 5, the second precipitation tank 7 serves to remove the desorbed microorganisms, and the solids settled to the lower portion are periodically transferred to the concentration tank 9. The water treated in this way is disinfected through the discharge tank 8 and then discharged.

And the concentration tank (9) serves to store the solids submerged in the first settling tank (5) and the second settling tank (7), it is preferable to install the concentrated storage tank (10) in order to concentrate the stored solids once again. In addition, the supernatant of the concentration tank (9) is connected to the pipe so as to pass to the flow adjustment tank (2).

The broa (11) is a device for supplying air into the contact aeration tank, between the first contact aeration tank (4) in the flow rate adjustment tank (2), the concentration tank (9) in the second contact aeration tank (6), and the concentration storage tank (10) in the concentration tank. The sewage or treated water is transferred to the transfer pump 14 and the rest uses a natural flow method due to water level difference.

The sewage treatment apparatus of the present invention including a two-stage contact aeration tank is capable of treating BOD and SS to 5ppm or less using only a contact oxidation apparatus using microorganisms, and it is excellent in treatment efficiency and does not require an additional physical and chemical treatment apparatus. In addition, it has the advantages of simple maintenance, low maintenance cost, low sludge generation and no bulking phenomenon, and can perform sewage treatment with high efficiency.

Claims (2)

Screens for filtering large contaminants, flow regulating tanks and flow adjusting feet to control the flow of influent sewage, contact aeration tanks containing microbial contact materials, sedimentation tanks, discharge tanks, and sedimentation tanks to remove suspended matter in the treated water by the contact aeration tanks. Condensation tanks for storing solids precipitated by the condensation tank, condensing storage tanks for condensing the solids stored in the condensing tanks, broa for supplying air into the contact aeration tanks, diffusers for small air scattering of the air supplied by broa, and sewage between each treatment tank. A sewage treatment apparatus composed of a transfer pump in charge of a transfer, the contact aeration tank comprising two stages of a first contact aeration tank having a residence time of about 22-26 hours and a second contact aeration tank having a residence time of 1 hour to 3 hours. And a second needle installed in the stage next to the first precipitation tank and the second contact aeration tank installed at the stage next to the first contact aeration tank. Sewage treatment apparatus according to claim 2, which consists of sets of twos. The wastewater treatment apparatus according to claim 1, wherein the first contact aeration tank is provided with a microorganism contact material of 30 to 80 m per volume of aeration tank, and the second contact aeration tank is provided with a microbial contact material of 100 to 400 m per volume of aeration tank.