KR20000033325A - United water-purifier tank of high efficiency - Google Patents

Abstract

PURPOSE: A water-purifier tank is provided, which is characterized in that a main tank is divided into an anaerobic tank, an anoxic tank, aerobic tank, a settling tank, and a storage tank so that highly concentrated sewage can be disposed effectively. CONSTITUTION: United water-purifier tank of high efficiency (1) is composed of a main body (5), a cover (7), an anaerobic tank (10), an anoxic tank (30), an aerobic tank (50), a sedimentation tank (70), and a concentrating tank (90). Wastewater flow into first anaerobic tank (12a), then, flow through second (12b), third (12c), and fourth anaerobic tank (12d). A lower part of all of anaerobic tanks is opened, so sludge flows to concentrating tank (90). So, treatment of sludge is simplified. Wastewater flows over partition walls in anaerobic tank (10), so, load of treatment is reduced. Denitrification is happened using lower molecule of carbon produced at anaerobic tank (10), and treated water is recycled from sedimentation tank (70). Microorganism can remove phosphorus.

Description

High efficiency merger septic tank

The present invention relates to a combined septic tank for treating manure and sewage from the source, more specifically, excellent in coping capacity with fluctuations in inflow flow, stable treatment of influent sewage with a high concentration of load, and removal efficiency of nitrogen and phosphorus. This is an excellent high efficiency merger septic tank.

In general, the septic tank is divided into a single septic tank and a merged septic tank, and a general septic tank is mostly a single septic tank, which is installed in single and shared (multi-family) houses with flush toilets to purify sewage (manure) from the toilet. In addition, a merger septic tank (aka, high efficiency sewage septic tank) refers to a facility that simultaneously treats manure and household wastewater (kitchen, laundry, toilet, bath sewage, etc.).

In the case of the single septic tank, the treatment efficiency is low enough to reach 150 to 200ppm BOD concentration of the effluent after treatment, despite the treatment of manure only. In addition, nitrogen and phosphorus treatment is rarely performed, and thus, eutrophication of rivers and lakes is accelerating, and pollution problems in the near sea are also raised. In recent years, however, legislation has been announced for the establishment of merger and purification tanks, and regulations on nitrogen and phosphorus are beginning to be introduced.

On the other hand, conventionally, the activated sludge process has been widely used as a biological wastewater / wastewater process, and a fixed biofilm process has recently emerged. As a process for simultaneously removing nitrogen and phosphorus by the activated sludge process, processes such as A / O, A ² / O, Bardenpho, UCT, and VIP have been developed. In addition, these processes are capable of treating not only organic matter but also nitrogen / phosphorus, which is the main culprit of aquatic eutrophication, with the proper placement of anaerobic, anaerobic and aerobic tanks and the internal transport of mixed liquids.

In the nitrogen / wastewater removal mechanism, ammonia is nitrified by nitrifying microorganisms in an aerobic tank (see Eq. 1), and the nitrate is recycled to an anoxic tank by internal transport and converted to nitrogen gas by denitrifying microorganisms (Equation 2). Reference)

^{_{NH 4 + + 2O 2 → NO}} 3 - + H 2 O + 2H + ( Equation 1)

5C (organic ^{_{carbon) + 4NO 3 - + 2H 2}} O → 2N 2 + 4OH - + 5CO 2 ( Equation 2)

On the other hand, the phosphorus removal mechanism is complex but, briefly mentioned, is removed due to phosphorus release / excess intake by microorganisms under anaerobic / aerobic conditions.

In addition, the fixed biofilm method using various kinds of carriers can maintain a large number of microorganisms compared to activated sludge method and easily remove nutrients due to the presence of various microbial phases (anaerobic / anaerobic / aerobic). In addition, relatively stable water quality can be obtained under high organic load.

To date, many patents and utility model registrations related to septic tanks have been reported, but many of them focus on anaerobic tanks and aeration tanks for septic tanks alone. The situation is being exposed.

Korean Patent Publication No. 98-1875, Utility Model Registration Publication No. 98-8135, 97-62317, 96-17556 and the like disclose a contact aeration type single purification tank, and Patent Publication No. 97- Nos. 6201, 93-4208, 93-19568, and Utility Model Publication No. 97-5787, etc., suggest an anaerobic monolithic purification tank, but these are only organic matters removed. Removal is not done. In addition, Utility Model Publication No. 97-58369 has an anaerobic and aerated form, but there is no internal transport of nitride for denitrification, and it does not have a proper countermeasure against fluctuations in inflow flow.

In addition, the Utility Model Registration Publication No. 96-34557 also has insufficient measures against flow fluctuations, and there is a problem that such a denitrification reaction cannot be properly performed because there is an internal return of nitride but an anaerobic tank for denitrification is not properly provided. This is expected. In Patent Publication No. 95-23604, a merger septic tank using a ciliary contact material is proposed to give flow control to anaerobic tank 2, but these are not effective, and the septic tank itself has a horizontal cylindrical structure, so that the piping line is It is complicated and it is difficult to draw waste sludge. In addition, in the case of various merger and purification tanks proposed in the premises and overseas (Japan) other than the proposed structure, most of them have a horizontal cylindrical structure, and thus have similar problems as described above.

The present invention has been proposed in order to solve the conventional problems as described above, the object of which is to cope with the fluctuation of the inflow flow rate, it is possible to reliably treat the influent sewage with a high concentration load, the removal of nitrogen and phosphorus Its purpose is to provide a highly efficient combined septic tank that is excellent in efficiency and structurally stable while maintaining a compact size.

1 is a cross-sectional view showing a vertically divided structure as a flat cross-sectional view of the high-efficiency merger septic tank according to the present invention;

Figure 2 is a longitudinal sectional view showing a high efficiency merger septic tank according to the present invention;

3 is a view for explaining the processing operation of the high-efficiency merger septic tank according to the present invention, the operation explanatory diagram of the structure shown in FIG.

Figure 4 is a block diagram showing an air lift pipe of the high efficiency combined septic tank according to the present invention;

Figure 5 is a detailed view showing the settling tank of the high efficiency combined septic tank according to the present invention;

Figure 6 is a block diagram showing that the lower portion of the concentrated storage tank of the high efficiency combined septic tank according to the present invention is penetrated with the anaerobic tank;

7 is a block diagram of an diffuser provided in a merger septic tank according to the present invention;

8 is a perspective view showing a mounting configuration of a partition provided in a merger septic tank according to the present invention;

Figure 9 is a block diagram of the filter medium provided in the anaerobic tank and the aerobic tank of the combined septic tank according to the present invention.

Explanation of symbols on the main parts of the drawings

5 ..... Body 7 ..... Cover

10 .... anaerobic tank 30 .... anaerobic tank

33 .... Weir 50 ....

54 .... diffuser 70 .... sedimentation tank

90 .... Concentrated Storage Tank

The present invention to achieve the above object,

In the combined septic tank for treating manure and sewage from the source having a hollow body and a cover covering the anaerobic tank, anoxic tank, aerobic tank, sedimentation tank and concentrated storage tank, the concentrated storage tank is disposed in the center of the body The anaerobic tank, the anaerobic tank, the aerobic tank and the settling tank are disposed radially around the concentrated storage tank so as to vertically divide the space between the concentrated storage tank and the body.

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

The high efficiency combined septic tank 1 according to the present invention has a structure of a vertical cylindrical (or vertical hollow polygon) structure as shown in a planar cross section in FIG. As the structure is compact, it can be made simply and structurally stable.

The high efficiency combined purification tank 1 according to the present invention has an anaerobic tank 10, anoxic tank 30, an aerobic tank 50, and a settling tank as shown in FIGS. 1 to 3, inside the body 5 and the cover 7. 70 and a concentrated storage tank 90, the concentrated storage tank 90 is disposed in the center of the body 5, the anaerobic tank 10, the anaerobic tank 30, around the concentrated storage tank 90, The aerobic tank 50 and the settling tank 70 are arranged radially to divide vertically the space between the concentrated storage tank 90 and the body 5, and each reaction tank (anaerobic tank 10) in the body (5) In addition, it is convenient to manufacture and transport by having a structure in which the partitions partitioning the oxygen-free tank 30, the aerobic tank 50, the settling tank 70 and the concentrated storage tank 90 can be separately separated and assembled.

The anaerobic tank 10 has an anaerobic tank 12a equipped with a wastewater inlet 11, an anaerobic tank 2a 12b, an anaerobic tank 3a 12c, and an anaerobic tank 4a 12d. The tank 12a has a minimum water level 14 of about 1/2 to 5/6 of the highest water level 16, and partitions partitioning between the anaerobic tank 12a and the anaerobic tank 12b ( p1) connects the inner surface of the body 5 and the outer surface of the concentrated storage tank 90, the lower edge p1 'of which is 1/20 to the highest water level 16 from the bottom 5a surface of the body 5; 1/2, preferably 1/7 to 1/5 is installed in a floating state, partition wall (p2) partitioning between the anaerobic tank 2 (12b) and the anaerobic tank 3 (12c) is the body 5 It connects the inner surface and the outer surface of the concentrated storage tank 90, the lower edge p2 'of which is 1/40 to 1/5 of the highest water level 16 from the bottom 5a surface of the body 5, preferably 1 / 20 to 1/10, with the top edge up (p2 ") The partition wall p2 is emptied to about 1/2 to 1/6 of the highest water level 16 so as to overflow the sewage and facilitate the formation of upflow.

In addition, between the anaerobic tank 3 (12c) and anaerobic tank 4 (12d), the partition wall (p3) for the downflow, the lower edge (p3 ') is 1/20 to 1 from the bottom (5a) of the body (5) / 3, preferably raised to a degree of 1/10 to 1/5. Further, the anaerobic tank 12d is adjacent to the anoxic tank 30 through the partition wall p4, and at the rear end of the anaerobic tank 12d, a certain amount of sewage is collected using an air lift pump 19. Movement of the sludge due to the partition wall p5 is further provided with a partition p5 partitioning the anaerobic tank 12d at the bottom to supply the anoxic tank 30 adjacent to the anaerobic tank 4d 12d. To prevent.

The lower edges of the concentrated storage tank 90 adjacent to the partition p6 of the anaerobic tank 12a, anaerobic tank 12b, anaerobic tank 12c and anaerobic tank 12d are shown in FIGS. As shown in 6, a sludge inlet 21 is formed so as to form a lower portion of the bulkhead p6 of the anaerobic tank 12a, the anaerobic tank 12b, the anaerobic tank 12c and the anaerobic tank 12d. Deposited sludge (S) is configured to flow into the concentrated storage tank (90).

On the other hand, the anaerobic tank 4 (12d) adjacent to the anaerobic tank 30 is equipped with a plurality of media to be removable in the circumferential direction of the body (5) inside the flow of waste, waste water in the anaerobic tank 30 upflow In order to repeat the flow down and down, the inflow of wastewater into the anaerobic tank 30 from the anaerobic tank 4 (12d) is made by using an air lift pump (19). As shown in FIG. 4, the air lift pump 19 is a vertical air lift pipe having an air injection pipe 23 connected to a pneumatic pump 27 and a tip of the air injection pipe 23 inserted therein. Pumping, sludge head pipe (25), the air is injected into the inside of the air lift pipe (25) through the air inlet (23a) located near the lower end of the air inlet pipe (23).

Therefore, when the air is supplied to the air lift pump 19, water and air are mixed to form a mixture having a specific gravity smaller than that of water, and the floating force of the air is applied to the water in the air lift pipe 25. The air lift pump 19 extending to the entrance side of the anaerobic tank 30 starts to pump from the anaerobic tank 12d to the anaerobic tank 30 by being discharged to the position higher than this partition p4.

The wastewater introduced into the anoxic tank 30 flows through the lower edge of the first filter material K1 to the second filter material K2 and flows over the second filter material K2 to the third filter material K3. After passing through the lower edge of the third filter material K3, the gas flows through the discharge ware 33 of the partition p7 of the anaerobic tank 30 formed adjacent to the body 5 to the aerobic tank 50 adjacent thereto.

The aerobic tank 50 is equipped with a plurality of media (K4) (K5) (K6) therein in the radial direction of the body (5) to repeat the flow of waste water, up and down flow, diffuser (54) In order to blow air through the air) to contact the air, the diffuser (50) is located on the lower surface of the aerobic tank (50) is located and is connected to the pneumatic pump (27) by the diffuser The air is supplied to the wastewater and wastewater which is repeatedly flowed up and down through the media K4, K5 and K6 through a plurality of air holes provided in the 54. Then, the wastewater flowing through the inside of the exhalation tank 50 passes through the lower edge of the first media K4 of the exhalation tank 50 and flows to the second media K5, and rides over the second media K5. The sedimentation tank 70 which flows to the 3rd filter material K6 and passes through the bottom edge of the 3rd filter material K6 and through the discharge weir 58 of the partition p8 of the aerobic tank 50 adjacent to the concentrated storage tank 90 side, is adjacent to it. Go to).

The media K1, K2, K3, K4, K5, and K6 provided in the anoxic tank 30 and the aerobic tank 50 each have a structure as shown in FIG. It is formed by filling the particles 62 made of a polymer-based, ceramic-based or other composite materials, the height, size and arrangement of the media (K1) (K2) (K3) (K4) (K5) (K6) Each can be changed according to the capacity of the merger purification tank 1 of this invention.

And, the settling tank 70, as shown in FIG. 5, the bulkhead (p9) for separating the treated water introduced from the aerobic tank 50 into the supernatant and the settling sludge (S), and the purified treated water to overflow The sludge S separated from the treated water in the space between the partition p9 and the concentrated storage tank 90 is equipped with a weir 75 for discharging, and the concentrated storage tank 90 next to it by the air lift pump 79. ), Some of the treated water is passed over the weir 75 and discharged through the outflow pipe 85, and the other part is returned to the anoxic tank 30 by the air lift pump 87.

Since the settling tank 70 is adjacent to the concentrated storage tank 90, it can be easily transported, and the advantage of the septic tank 1 having such an upright vertically divided structure is that the sludge (S) is an air lift pump (79). ), There is no fear of clogging due to the lack of conveying piping.

Meanwhile, air is supplied to the air lift pump 19 of the anaerobic 4 tank 12d and the plurality of air lift pumps 79 and 87 of the settling tank 70 and the diffuser 54 of the aerobic tank 50. The pneumatic pump 27 can simplify the configuration of the equipment by supplying air through the common pipe 27a as shown in Figs. The barrier ribs p1 to p9 respectively form upper and lower length guides and grooves 92 on the inner circumferential surface of the body 5 and the outer surface of the concentrated storage tank 90, respectively, as shown in FIG. In addition, the barrier ribs p1 to p9 are inserted into the guide and the grooves 92 to be assembled, and the guides and the grooves 92 are formed at respective heights to assemble the barrier ribs p1 to p9. It is configured to.

The merger septic tank 1 of the present invention configured as described above is slowly introduced into the anaerobic tank 1 12a through the inlet pipe 11 through the inlet pipe 11, followed by the anaerobic tank 2 (12b) and the anaerobic tank 3 ( 12c), the sludge through the concentrated storage tank (90) as the lower portion of the anaerobic tanks 1 to 4 (12a)-(12d) are drilled to communicate with the central concentrated storage tank (90). At the same time withdrawal of S), sludge S can be taken out at the same time. In the anaerobic 1 to 4 tanks (12a)-(12d), the flow of sewage is repeatedly flowed down and upstream due to a plurality of partitions p1, p2, and p3. Minimization of mixing is to be minimized, and most of the sludge (S) in the lower portion is to be moved sequentially.

On the other hand, through the anaerobic tank 1 (12a) to the anaerobic tank 4 (12d), the precipitation of solids, the decomposition of organic matter and the low molecular weight of the polymer material is made. The wastewater supplied to the anaerobic tank 30 from the anaerobic tank 12d through the air lift pump 19 is treated using a low molecular carbon source made in the anaerobic tank 10 and returned from the settling tank 70. Denitrification of nitrates in wastewater and wastewater is carried out using. Wherein the filter medium (K1) (K2) (K3) in the form of a plate (horizontal or vertical) or block in the form of a fixed or fluidized bed to increase the activity and denitrification efficiency of the microorganism, through the flow through the weir 33 The wastewater which has passed to the aerobic tank 50 is nitrified by ammonia by the acid pipe 54 installed in the lower part while passing through the filter media K4, K5 and K6, and organic matter is removed, and excess by the microorganism of phosphorus Intake takes place.

Filling media (K4) (K5) (K6) in the above can be used to fill the fixed bed or the fluid bed in the horizontal (Bed Type) or vertical (Sheet type), the treated water passed in the aerobic tank 50 is settling tank ( Some of the purified water separated into the supernatant and the settling sludge (S) in 70) is discharged through the outlet pipe 85, the other part is returned to the anoxic tank 30 by the air lift pump 87, the precipitated sludge S is conveyed to the concentrated storage tank 90 next to it via the air lift pump 79.

Since the settling tank 70 is adjacent to the concentrated storage tank 90, the sludge S can be easily transported. Therefore, an advantage of the septic tank 1 having such an upright vertically divided structure is that when the sludge S is transferred as the air lift pump 79, there is no fear of clogging because there is no conveying piping.

As described above, according to the present invention, by adjusting the flow rate of the wastewater in the anaerobic 1 to 4 tanks (12a)-(12d) by the upstream and downstream flows repeatedly, the flow rate adjustment function is strengthened to prevent overloading in the morning and evening. The treatment burden can be reduced, and when the sludge S generated from the aerobic tank 50 is transferred from the sedimentation tank 70 to the concentrated storage tank 90, the transfer line becomes unnecessary so that no clogging in the transfer pipe occurs. Will not. And, since the regular drawing of the sludge (S) is made at a time in the concentrated storage tank 90 located in the center has the advantage that the treatment of the sludge (S) is very convenient.

Therefore, the present invention is excellent in the ability to cope with the fluctuation of the inflow flow rate due to the upright cylindrical structure, can stably process the influent sewage with a high concentration load, excellent removal efficiency of nitrogen and phosphorus, while maintaining a small structure It is also possible to obtain a stable effect.

Claims (6)

It has a hollow body (5) and a cover (7) covering it, and inside the anaerobic tank (10), anaerobic tank (30), aerobic tank (50), sedimentation tank (70) and concentrated storage tank (90), etc. In the combined septic tank 1 which processes wastewater from a generation source, the said concentrated storage tank 90 is arrange | positioned in the center of the body 5, and the anaerobic tank 10, the anaerobic tank 30, around the said concentrated storage tank 90, The aeration tank (50) and the settling tank (70) is disposed radially merged septic tank, characterized in that configured to vertically divide the space between the concentrated storage tank (90) and the body (5). The anaerobic tank (10) according to claim 1, wherein the anaerobic tank (10) is equipped with a wastewater inlet (11), an anaerobic tank (12a), adjacent to the anaerobic tank (12b), an anaerobic tank (12c) and an anaerobic tank (12d) The partition wall p1 partitioning between the anaerobic tank 12a and the anaerobic tank 12b has a lower edge p1 'from the bottom 5a surface of the body 5 to be the highest water level 16. ) Is 1/20 to 1/2, and the partition wall p2 partitioning between the anaerobic tank 12b and the anaerobic tank 12c has a bottom edge p2 'of the bottom of the body 5 5a) is 1/40 to 1/5 of the highest water level 16 of the anaerobic tank 10, and at the same time, the upper edge p2 " is also emptied to about 1/2 to 1/6 of the highest water level 16, The partition p3 between the anaerobic tank 3c and the anaerobic tank 12d has a bottom edge p3 'of 1/20 to 1 of the highest water level 16 from the bottom 5a of the body 5. Merger septic tank characterized by the structure emptied to / 3. The partition p1, which partitions between the anaerobic tank 12a and the anaerobic tank 12b, has a bottom edge p1 'of which is the highest from the bottom 5a surface of the body 5. 1/7 to 1/5 of the water level 16 is floated, and the partition wall p2 partitioning between the anaerobic tank 12b and the anaerobic tank 3c 12c has a lower edge p2 'of the body. (5) is floated about 1/20 to 1/10 of the highest water level 16 from the bottom 5a surface, and at the same time the upper edge p2 "is also about 1/2 to 1/6 of the highest water level 16 It is a structure emptied up to, the partition p3 between the anaerobic tank 3 (c) 12c and the anaerobic tank 4 (12d) has a lower edge p3 'from the bottom 5a of the body 5 to 1/10 to 1 / Merger septic tank characterized by being raised to 5 degrees. According to claim 2 or 3, wherein the partitions are formed on the inner circumferential surface of the body (5) and the outer surface of the concentrated storage tank (90), respectively, the upper and lower longitudinal guides and grooves (92), respectively, the guide and groove (92) Merged septic tank, characterized in that the partition is inserted into the) prefabricated. The anaerobic tank (10) according to claim 1, wherein the anaerobic tank (10) is a concentrated storage tank (90) adjacent to a partition (p5) of an anaerobic tank (12a), an anaerobic tank (12b), an anaerobic tank (12c), and an anaerobic tank (12d). Sludge inlet 21 is formed at the bottom edge of the bottom) and is deposited on the bottom side of the bulkhead (p5) of the anaerobic tank 1 (12a), anaerobic tank 2 (12b), anaerobic tank 3 (12c) and anaerobic tank 4 (12d). Sludge (S) to be introduced into the concentrated storage tank (90) and merged septic tank, characterized in that configured to be discharged at one time through the concentrated storage tank (90). The method of claim 1, wherein the settling tank (70) is a partition (p9) for separating the treated water introduced from the aerobic tank 50 into the supernatant and the settling sludge (S), and for flowing over the discharged purified water The wear 75 is provided, and a part of the treated water is discharged through the outflow pipe 85 by passing the wear 75, and the other part is returned to the anoxic tank 30 by the air lift pump 87, and the partition wall p The sludge S separated from the treated water in the space between the tank and the concentrated storage tank 90 is transferred to the concentrated storage tank 90 next to it by the air lift pump 79 so that the transfer pipe is blocked by the sludge S. Merged septic tank, characterized in that there is no configuration.