KR100637920B1 - Secondary settling basin for biological wastewater treatment facilities - Google Patents

Abstract

The present invention relates to a secondary sedimentation basin for biological sewage and wastewater treatment plants, and more particularly, floc formation for improving sedimentation of sludge by increasing the number of collisions and the number of collisions between suspended particles and cohesive sludge flocs. The present invention relates to a secondary sedimentation basin for biological sewage and wastewater treatment plants.

Secondary sedimentation basin for biological sewage and wastewater treatment plant according to the present invention, the sludge mixture flowing from the reaction tank is pipe-shaped distribution pipe formed with a slit of a predetermined width in the longitudinal direction so as to flow out evenly in the width direction of the sedimentation tank; An inlet pipe which communicates with one end of the reactor and the other end communicates with a central portion of the distribution pipe and supplies the sludge mixture of the reactor to the distribution pipe; It consists of a plurality of vertical batches spaced apart at predetermined intervals downstream of the distribution pipe to guide the flow of the sludge mixture flowing out from the slit of the distribution pipe in the vertical direction to collide between the floating particles and the floating particles and sticky sludge floc Characterized in that it comprises a floc forming unit for increasing the chance and number of times.

Settling basin, floc, flocculation, baffle, settling tank, sludge, distribution pipe, slit

Description

Secondary settling basin for biological wastewater treatment facilities

1 is a schematic conceptual view showing the basic configuration of a biological sewage and wastewater treatment plant,

Figure 2 is a side cross-sectional view showing an example of a secondary sedimentation basin according to the prior art,

3 and 4 is a side cross-sectional view showing a preferred embodiment of the secondary settler according to the present invention,

5 is a perspective view showing an example of a distribution pipe according to the present invention;

6 is a cross-sectional view illustrating a state in which the distribution pipe illustrated in FIG. 5 is cut along a line A-A;

7 is a partial perspective view showing an example of the floc forming part according to the present invention;

8a to 8c is a partial side cross-sectional view showing various modified embodiments of the secondary sedimentation basin according to the present invention,

9 is a side cross-sectional view showing another embodiment of a secondary sedimentation basin according to the present invention;

10 and 11 are side cross-sectional view showing another embodiment of the secondary sedimentation basin according to the present invention;

12a to 12c is a partial side cross-sectional view showing various modified embodiments of the secondary sedimentation basin according to the present invention,

13 and 14 are a side cross-sectional view and a partially enlarged view showing a preferred embodiment of a circular secondary sedimentation basin according to the present invention,

15 is a partially enlarged view showing another embodiment of a circular secondary sedimentation basin according to the present invention.

**** Description of the symbols for the main parts of the drawings *****

2: sludge collector 3: settling tank

5: sludge mixture inlet 7: supernatant outlet

9: sludge outlet 10: secondary sedimentation basin

21: inlet pipe 22: distribution pipe

23: Slit 24: Reflector

60: floc forming part 61, 62, 63, 64, 65: vertical baffle

70: vertical baffle lifting means 90: flocculant input means

100: round secondary clarifier 122: distribution tube

123: slit 130: double tube

132: outer hollow 140: inlet tank

160: floc forming part 240: vertical inlet water tank

260: floc forming portion 660: second floc forming portion

The present invention relates to a secondary sedimentation basin for biological sewage and wastewater treatment plants, and more particularly, floc formation for improving sedimentation of sludge by increasing the number of collisions and the number of collisions between suspended particles and cohesive sludge flocs. The present invention relates to a secondary sedimentation basin for biological sewage and wastewater treatment plants.

In general, sewage and wastewater treatment plants use aerobic microorganisms present in nature to remove suspended organic matter contained in sewage or wastewater. This biological sewage and wastewater treatment plant is composed of a primary sedimentation basin, a reaction tank, and a secondary sedimentation basin, as shown in FIG. The primary sedimentation basin performs the role of pretreatment for biological treatment by sedimentation and removal of solid particles contained in influent, that is, sewage or wastewater (hereinafter referred to as 'sewage').

The reactor is a reactor that blows air into the sewage and stirs it to form a cohesive floc. The floc floc is also called activated sludge, and is composed of microorganisms such as various bacteria, protozoa, and welfare animal, and non-organic inorganic and organic matter. That is, when activated sludge, which is a microbial mass, is stirred with oxygen, the activated activated sludge adsorbs suspended organic substances in sewage and is oxidized or assimilated according to the metabolic function of microorganisms to remove them.

Subsequently, the secondary sedimentation basin is gravity precipitated from the activated sludge mixed solution (active sludge + sewage) discharged from the reaction tank and separated into activated sludge and supernatant. The separated supernatant is discharged as treated water, and some of the precipitated and concentrated activated sludge is returned to the reactor as return sludge and used again for biological sewage treatment, and the remaining activated sludge is disposed of as excess sludge.

Therefore, secondary sedimentation basins in biological sewage and wastewater treatment plants are an important process for determining the quality of treated water and the amount and character of excess sludge. Therefore, it is very important to reduce the suspended particles in the treated water and to improve the density and dehydration of the excess sludge in order to increase the treatment efficiency and economic efficiency of the whole sewage and wastewater treatment plant.

Accordingly, the present invention is a flocculation process of forming a flocculant floc having a particle size that can be precipitated by colliding floating particles with each other in a secondary sedimentation basin for gravity-sedimentation and solid-liquid separation of activated sludge mixture flowing from a reaction tank. ) To provide. This 'flocculation' is achieved through interparticle collisions or enmeshment of particles caused by the mixing effect and molecular motion of the fluid.

In general, floc formation in the primary sedimentation basin of sewage and wastewater treatment plants or in the sedimentation basin of water treatment plants is carried out through a two-step process: coagulation and flocculation. In other words, in order for the colloidal particles to settle, the size of the particles must be increased due to the aggregation between the particles. In general, the floating particles have a repulsive force due to the charge on the surface. A condensation process is preceded by neutralizing the surface charge to remove the repulsive force. In other words, the coagulation is performed by chemical and physical interactions between the colloidal particles charged with (-) and the flocculant with the (+) charge.

However, the condensation process can be omitted because the influent (sludge mixture) flowing into the secondary sedimentation basin of the biological sewage and wastewater treatment plant contains a large amount of tacky activated sludge. That is, since activated sludge is a sticky floc made of various microorganisms and organic macromolecules released from these microorganisms, it is possible to agglomerate the suspended particles simply by increasing the collision chance and the number of times between the suspended particles and the sticky sludge floc.

On the other hand, Figure 2 is a schematic side cross-sectional view showing an example of a secondary sedimentation basin according to the prior art. As shown, the sedimentation basin 1 has a rectangular sedimentation tank 3 of a predetermined size, a sludge mixture inlet portion 5 formed on an upstream side of the sedimentation tank 3, and formed on an upper side of a downstream side of the sedimentation tank 3 and symbolized. Sludge which is formed in the sewage sludge discharge portion 7 through which the water is discharged, the sludge discharge portion 9 formed at the downstream side of the sedimentation tank 3, and the sludge discharged portion is driven in the sedimentation tank 3. Sludge collector (2), which is scraped by the drawer (9), formed on one side of the sedimentation tank (3), the sludge suction pipe (41), sludge drawing pump (42) and conduit and pump chamber (4) are installed. do.

In addition, the sludge mixture inlet portion 5 installed at an upstream side of the settling tank 3 and into which the sludge mixture is introduced is composed of an inlet tank 51, a distribution channel 53, and a process flow plate 54 having a predetermined size. The inflow water tank 51 is formed in a relatively small size so that the sludge mixture flowing from the reaction tank (not shown) can temporarily flow out into the distribution water flow passage 53, and the distribution water flow passage 53 is the flow-through flow plate ( 54 and together with the width of the settling tank 3 so that the sludge mixture supplied from the inlet tank 51 can be evenly distributed in the width direction of the settling tank 3. At this time, the flow-flow plate 54 is formed with a plurality of permeation holes to evenly distribute the sludge mixture into the settling tank 3 to form a low-speed laminar flow inside the settling tank (3).

Therefore, the conventional secondary sedimentation basin 1, in which the distribution channel 53 and the eutectic flow plate 54 are installed, smoothly precipitates the settling flocs contained in the sludge mixture because low-speed laminar flow is formed inside the sedimentation tank 3. It can be effective. On the other hand, the conventional secondary sedimentation basin 1 has a disadvantage in that floc formation is not active because low-speed laminar flow is formed in the sedimentation tank 3 so that the floating particles do not have a chance to collide. Therefore, the floating particles that do not form a precipitated floc before entering the sedimentation tank (3) is discharged to the symbolic water outlet (7) with the symbolic water has a problem of deteriorating the water quality of the treated water.

In order to solve this problem, the conventional secondary sedimentation basin 1 is provided with an agitator 55 in an inlet tank 51 and a distribution channel 54 to agitate the sludge mixed liquid introduced thereto, as shown in FIG. 2. The solution was presented. However, the stirrer 55 has a problem in that maintenance costs increase by increasing the amount of electricity used, and in order to sufficiently agitate the sludge mixture, an inlet tank 51 and a distribution channel 54 having a predetermined size should be provided. As the size of the settler is increased, the required land area is widened and the effective settling tank is reduced.

The present invention has been made to solve this problem, the main object of the present invention, by installing a floc forming portion in the inlet of the sludge mixture of the secondary sedimentation basin to the front and back and / or up and down the flow of the sludge mixture flowing into the secondary sedimentation basin It is to provide a secondary sedimentation basin for biological sewage and wastewater treatment plant which greatly improves the sedimentation of the sludge by increasing the chance and number of collisions between the floating particles or between the floating particles and the sticky flocs.

The present invention also provides a sludge mixture inlet of the secondary sedimentation basin without the use of a power floc forming part to increase the possibility of collision and the number of times between suspended particles or suspended particles and cohesive sludge flocs with no power. To provide a secondary sedimentation basin for biological sewage and wastewater treatment plants.

In addition, the present invention not only enlarges the effective area of the sedimentation basin by installing a predetermined distribution plate and a plurality of vertical baffles in place of the inflow water tank, the distribution channel and the eutectic flow plate which were installed in the sludge mixture inlet of the conventional secondary sedimentation basin. It is to provide a secondary sedimentation basin for biological sewage and wastewater treatment plants that can reduce the cost of constructing concrete structures.

In order to achieve the above object of the present invention, the secondary sedimentation basin for biological sewage and wastewater treatment plant according to the present invention is installed in the sludge mixture inlet horizontally in the width direction of the sedimentation tank and the sludge mixture introduced from the reaction vessel is the width of the sedimentation tank. One end portion is in communication with the reaction tank to guide the pipe-shaped distribution pipe formed with a predetermined slit along the longitudinal direction so as to flow out evenly in the direction, and to guide the sludge mixed liquid flowing from the reaction tank to the center portion of the distribution pipe. The other end part comprises an inlet pipe installed to be orthogonal to the distribution pipe.

In addition, the secondary sedimentation basin for biological sewage and wastewater treatment plant according to the present invention, a plurality of vertical installed vertically at predetermined intervals downstream of the distribution pipe to induce the flow of the sludge mixture flowing out from the distribution pipe in the vertical direction It is configured to include a floc-shaped voice composed of baffles.

In addition, the secondary sedimentation basin for biological sewage and wastewater treatment plant according to the present invention, a double pipe formed perpendicular to the center of the circular sedimentation tank, an inlet pipe for introducing the sludge mixture to the upper portion of the double pipe, and the sludge mixture supplied from the inlet pipe Spiral inlet tank formed in the double pipe and vertically installed on the inlet tank so as to guide the lower side to guide the flow of the sludge mixture in the vertical direction to collide with the floating particles or between the floating particles and the sticky floc and It includes a plurality of vertical baffles to increase the number of times to greatly improve the sedimentation of the sludge.

Hereinafter, a preferred embodiment of the secondary sedimentation basin for biological sewage and wastewater treatment plants according to the present invention will be described in detail.

First, Figures 3 and 4 is a cross-sectional view showing a secondary sedimentation basin for biological sewage and wastewater treatment plant according to the present invention. As shown in the drawings, the secondary sedimentation basin 10 (hereinafter referred to as 'secondary sedimentation basin') for biological sewage and wastewater treatment plants according to the present invention is a rectangular sedimentation tank 3 and an upstream side of the sedimentation tank 3. Sludge mixture inlet formed in the inlet portion 5, formed on the downstream side of the sedimentation tank 3, the symbolic water outlet portion 7 is discharged from the symbol water, is formed in the lower downstream side of the sedimentation tank 3 is sludge is withdrawn Sludge collector (9), the sludge collector (2) which is operably installed in the settling tank (3) to collect the sludge collected in the sludge withdrawal unit (9), and formed on one side of the settling tank (3) The sludge suction pipe 41, the sludge drawing pump 42 and the conduit and the conduit and the pump chamber (4) is installed including a conduit.

The structure of this secondary sedimentation basin 10 is similar to the conventional secondary sedimentation basin 1 shown in FIG. Therefore, the same parts as the conventional secondary sedimentation basin 1 are given the same reference numerals, and detailed description thereof will be omitted.

Again, an example of the secondary sedimentation basin 10 according to the present invention will be described with reference to 3 and 4. As shown, the sludge mixture inlet portion 5 of the secondary settler 10 according to the present embodiment is different from the structure of the sludge mixture inlet portion 5 of the secondary settler 1 according to the prior art. That is, the secondary sedimentation basin 10 according to the present embodiment is an inflow water tank 51, a distribution channel 53, and a eutectic flow plate 54 installed in the sludge mixed liquid inlet 5 of the conventional secondary sedimentation basin 1. Instead of), a distribution pipe 22 of a predetermined diameter is installed.

In addition, the secondary sedimentation basin 10 according to the present invention is different from the conventional secondary sedimentation basin 1 by inducing the flow of the sludge mixture introduced from the sludge mixture inlet portion 5 into the sedimentation tank 3 in the vertical direction. A floc forming part 60 is provided which increases the possibility of collision and the number of times between oily particles and suspended particles and sticky sludge flocs.

At this time, the floc forming part 60 is formed of a plurality of vertical baffles, and installed in the front of the sludge collector 2 as shown in Figure 3 and as shown in Figure 4, is installed in the sludge collector 2 There is a form. Since this is arbitrarily selected according to the shape and function of the settling tank 3 and the sludge collector 2, this invention is not limited to either.

First, the distribution pipe 22 installed in the sludge mixture inlet portion 5 will be described. As shown in FIG. 5, the distribution pipe 22 is a circular pipe installed horizontally in the width direction of the settling tank 3, and a slit 23 having a predetermined height is formed in the longitudinal direction thereof. In addition, the circular inlet pipe 21 is coupled to the center portion of the distribution pipe 22. One end of the inlet pipe 21 is connected to a reaction tank (aeration tank or inlet water tank) not shown, and the other end is welded to the distribution pipe 22.

Therefore, the sludge mixture of the reaction tank is introduced into the distribution pipe 22 through the inlet pipe 21. At this time, the sludge mixed liquid introduced into the distribution pipe 22 hits the inner circumferential surface of the distribution pipe 22 and is distributed in the width direction of the settling basin 3. And the sludge mixed liquid distributed from side to side in the distribution pipe 22 is discharged to the settling tank 3 through the slit 23. As described above, the secondary sedimentation basin 10 of the present invention performs the same function instead of omitting the inflow water tank 51, the distribution channel 53 and the eutectic flow plate 54 of the sedimentation basin 1 according to the prior art. The distribution pipe 22 is installed.

As shown in Fig. 5 and 6, the distribution pipe 22 is the slit 23 is opened in the direction in which the inlet pipe 21 is installed, that is, the direction in which the sludge mixture is introduced. At this time, the height of the slit 23 is increased toward the left and right side with respect to the center portion in which the inlet pipe 21 is installed. In addition, the slit 23 is not formed to the left and right from the center portion in which the inflow pipe 21 is welded. Therefore, the sludge mixed liquid introduced into the distribution pipe 22 along the inflow pipe 21 hits the inner circumferential surface of the distribution pipe 22 and flows backward and flows in the left and right directions.

Therefore, the sludge mixed liquid flowing into the distribution pipe 22 moves in the left and right directions and is discharged in the reverse flow direction (rear) through the slit 23. At this time, since the height of the slit 23 is lower in the middle and higher toward both ends, the amount of the sludge mixed liquid discharged through the slit 23 is equalized in the width direction of the settling tank 3. As described above, the distribution pipe 22 simplifies the structure of the inlet of the sludge mixture and increases the number of collisions between the suspended particles and the suspended particles and the sticky sludge floc by counterflowing and distributing the flow of the sludge mixture.

In addition, as shown in Figure 6, the sludge mixture is preferably discharged backward through the slit (23) hits the vertical wall 13 of the settling tank 3, the flow of the sludge mixture is changed again. As described above, the secondary sedimentation basin 10 may allow the sludge 23 formed in the distribution pipe 22 to flow backward so that the flow of the sludge mixture may flow back through the secondary. That is, the flow of the sludge mixture supplied from the reaction tank first flows back into the distribution pipe 22 and then collides again with the vertical wall 13 of the settling tank 3 and flows back to the secondary, thereby allowing the suspended particles contained in the sludge mixture to flow back. To increase the likelihood and number of collisions between hepatic or suspended particles and cohesive sludge flocs.

As described above, the secondary sedimentation basin 10 of the present invention opens the slit 23 formed in the distribution pipe 22 toward the rear so that the flow of the sludge mixture is repeatedly flowed back and forth in the forward and backward directions, so that the floating particles may collide. And increasing the number of times is characterized by improving the sedimentation of the sludge.

That is, the sludge mixture (biologically treated water) flowing out of the reaction tank (aeration tank) contains a mixture of suspended particles (pin flocs), which do not easily precipitate depending on the size of the particles, and settling flocs that precipitate well. As such, the floating particles and the settling flocs are sticky particles and flocs composed of various microorganisms and organic polymers released from the microorganisms. Therefore, increasing the collision chance and the number of times between the floating particles and the settling flocs can greatly improve the cohesion rate and lower the concentration of the floating particles.

Therefore, as shown in the present embodiment, by installing the distribution pipe 22 having the slit 23 formed at the tip of the settling tank 3, increasing the chance of collision and the number of times between the suspended particles and the sticky sludge floc greatly improves the sedimentation of the sludge You can.

Next, the floc forming unit 60 in which a plurality of vertically baffled channels are formed will be described with reference to FIGS. 3, 4, and 7. As shown in the figure, the upstream side of the settling tank 3 is provided with a floc forming part 60 that forms a plurality of vertical baffle channels by a plurality of vertical baffles 61, 62, 63, 64.

As shown in FIG. 7, the vertical baffles 61, 62, 63, and 64 are plate bodies of a predetermined thickness, and both ends thereof are fixed to both side walls 14 of the settling basin 3. The vertical baffles 61, 62, 63, and 64 are spaced at regular intervals, and vertical baffle channels are formed between the neighboring vertical baffles to allow the sludge mixture to flow in a vertical direction.

For example, a lower end of the first vertical baffle 61 is located close to the bottom surface of the settling tank 3, and an upper end thereof is installed below the water surface of the settling tank 3. Therefore, the sludge mixture supplied from the distribution pipe 22 moves to the next vertical baffle channel through the top of the first vertical baffle 61 while forming a flow of upflow.

More preferably, as shown in Figure 6, when the reflection plate 24 of a predetermined curvature is installed on the front of the vertical wall 13 of the settling tank 3, it flows out through the slit 23 of the distribution pipe 22 The sludge mixture can be induced to flow naturally. In addition, the lower end of the first vertical baffle 61 is spaced apart from the bottom of the settling tank 3 by a predetermined height so that the settling sludge deposited on the bottom of the settling tank 3 can move downstream along the flow of the sludge mixture.

Subsequently, the lower end of the second vertical baffle 62 is spaced apart from the bottom of the reactor 3 by a predetermined distance, and the upper end is located near the water surface. Therefore, the sludge mixture liquid passed through the upper end of the first vertical baffle 61 forms a downward flow and then moves to the next vertical baffle channel through the lower end of the second vertical baffle 62. At this time, the upper end of the second vertical baffle 62 must be located below the surface of the settling tank 3 so that the scum floating on the surface of the settling tank 3 can be removed using a scum removing scraper.

When the third vertical baffle 63 and the fourth vertical baffle 64 are provided in the same manner, an upward vertical baffle channel is formed between the second vertical baffle 62 and the third vertical baffle 63. A vertical vertical baffle channel is formed between the three vertical baffles 63 and the fourth vertical baffle 64. Therefore, the sludge mixture flowing into the settling zone of the settling tank 3 through the lower end of the fourth vertical baffle 64 moves downstream while forming a flow of upflow to form a low-speed laminar flow.

Therefore, the sludge mixture liquid repeatedly moving up and down through a plurality of channels formed between the first vertical baffle 61 and the fourth vertical baffle 64 has an extended movement path and a collision opportunity between the floating particles and the sticky floc. The number of times increases so that the suspended particles aggregate. The aggregated sludge floc is settled in the precipitation zone after the fourth vertical baffle 64. In addition, the precipitated sludge is removed from the settling tank in the same manner as the conventional method.

As such, the secondary sedimentation basin 10 according to the present invention has a floc forming part 60 composed of a plurality of vertical baffles downstream of the distribution pipe 22 and flows of the sludge mixed liquid introduced through the distribution pipe 22. By increasing the vertical direction, the movement path of the sludge mixture is extended, and the collision chance and the number of times between the suspended particles and the adhesive sludge flocs contained in the sludge mixture are increased to increase the possibility of trapping of the suspended particles in the floc.

On the other hand, the sludge precipitated in the floc forming part 60 is moved downstream along the flow of the sludge mixed liquid flowing down the bottom of each vertical baffle. And the sediment sludge transported downstream is collected downstream by the settling tank 3 by the blades of the sludge collector 2 and then discharged to the outside through the sludge take-out part 9. In addition, the scum floated in the floc forming part 60 is removed through the scum lead-out (not shown) by moving along the flow of the sludge mixture or the scraper of the scum remover flowing upwards of the top of each vertical baffle.

Preferably, as shown in Figure 4, by installing the blades of the sludge collector 2 to pass through the lower and upper ends of the floc forming unit 60 it is possible to more easily remove the sludge sludge and scum.

Hereinafter, various modifications of the floc forming part 60 according to the present invention will be described. FIG. 8A is a partial side cross-sectional view of the secondary sedimentation basin 10, and in particular, elevating means 70 is provided to elevate up and down the fourth vertical baffle 64 installed downstream of the last end of the floc forming part 60. If it is. The lifting means 70 can freely adjust the height between the bottom of the vertical baffle and the bottom surface of the settling tank (3). Therefore, the fourth vertical baffle 64 can freely adjust the flow direction and flow rate of the sludge mixture introduced into the settling tank 3.

To this end, the elevating means 70 is a power transmission means (not shown) for transferring a predetermined drive motor 71 and the rotational force of the drive motor 71 to the fourth vertical baffle 64 by converting it into vertical motion. It is configured to include a guide roller 72 for guiding the lifting of the fourth vertical baffle (64). At this time, the power transmission means may be a power transmission means that can change the rotational motion such as chain and sprocket, rack and pinion to vertical motion.

8b shows another embodiment of the secondary sedimentation basin 10 according to the present invention. In particular, the fifth vertical baffle 65 is further installed downstream of the floc forming part 60. The lower end of the fifth vertical baffle 65 is installed close to the bottom surface, and the upper end is sufficiently spaced from the water surface so that the sludge mixed liquid introduced through the fifth vertical baffle 65 is bottomed from the water side of the settling tank 3. To flow toward the side. In this way, by inducing the flow of the sludge mixture toward the bottom of the settling tank can minimize the rise of the sludge due to the water temperature rise. In this case, it is preferable to provide a lifting means in the fifth vertical baffle 65 to freely adjust the height between the top of the vertical baffle and the water surface.

8c shows another embodiment of the secondary sedimentation basin 10 according to the present invention, in which a flow-through flow plate 60 having a plurality of permeable holes is further provided downstream of the floc forming part 60. The process flow plate 60 smoothly settles the settling sludge floc by equally distributing the sludge mixture flowing out into the settling tank and minimizing turbulence.

On the other hand, the secondary sedimentation basin 10 according to the present invention can change the number, position and height of the vertical baffle according to the situation of the sedimentation tank. Therefore, the present invention has been described by way of example the floc forming portion 60 consisting of four vertical baffles vertically baffle of the floc forming portion 60 according to the present invention is not limited to the number or position shown.

And Figure 9 is a side cross-sectional view showing another embodiment of a secondary sedimentation basin 10 according to the present invention. As shown, the present embodiment is a case where the flocculant input means 90 is further installed so that the flocculant can be injected into the sludge mixture flowing into the settling tank 3 through the distribution pipe 22. The coagulant injecting means 90 is configured to include a mixing tank 91 installed in communication with the inlet pipe (21). In addition, the mixing tank 91 is provided such that a treated water feed pipe 93 for circulating and supplying treated water and a treated water feed pump 92 provided on the treated water feed pipe 93 communicate with each other.

Therefore, the flocculant supplied to the mixing tank 91 is stirred with the treated water and then introduced into the inlet pipe 21. Then, the sludge mixture into which the flocculant is added is stirred again in the distribution pipe 22 and the floc forming part 60 to condense the floating particles to facilitate the formation of the precipitated floc. As described above, the secondary sedimentation basin 10 according to the present invention improves the cohesiveness between the suspended particles by administering a predetermined amount of flocculant to the sludge mixture which flows into the distribution pipe 22 and the floc forming part 60, thereby precipitating the precipitate. Increase and improve dewatering of excess sludge. At this time, the dosage of the flocculant is preferably limited to a range that does not adversely affect the activated sludge returned to the reaction tank (aeration tank).

Next, another embodiment of the secondary settling basin 10 according to the present invention will be described with reference to FIGS. 10, 11 and 12. As shown, the secondary sedimentation basin 10 according to the present embodiment is formed in the sludge discharge portion is discharged upstream side of the sedimentation tank (3), the sludge mixture inlet portion of the secondary sedimentation basin (1) according to the prior art It has a structure similar to the sludge mixture inlet portion (5).

That is, the secondary sedimentation basin 10 is formed of a rectangular sedimentation tank 3 and an upstream side of the sedimentation tank 3, and is composed of a sludge mixed liquid consisting of an inflow water tank 51, a distribution channel 53, and a eutectic flow plate 54. The inlet part 5, the symbol water outlet part 7 which is formed in the upper part of the downstream side of the sedimentation tank 3, and discharges the symbol water, is formed in the lower part of the upstream side of the sedimentation tank 3, and the sludge withdrawal part which the sludge is drawn out ( 91), a sludge collector 2 which is operably installed in the sedimentation tank 3 to scrape the sediment sludge toward the sludge withdrawal part 91, formed in the lower part of the sludge mixture liquid inlet part 5, and not shown in the sludge suction It comprises a cavity ball and a pump chamber 44 in which piping, a sludge drawing pump, an electric conduit, etc. are installed.

Referring to FIG. 10, the secondary sedimentation basin 10 of the present embodiment has the same structure as the conventional sludge mixture inlet 5, but has a plurality of vertical baffles 61, 62, 63, in the distribution channel 53. It is characterized in that the floc forming part 60 composed of 64 is formed. By installing the floc forming part 60 in the distribution channel 53 in this way, not only the settling efficiency of the settling tank 3 is increased but also the effective area of the settling tank 3 is widened.

At this time, the vertical baffles 61, 62, 63, 64 of the floc forming part 60 are plate bodies, and both ends thereof are fixed to both side walls of the distribution channel 53. The vertical baffles 61, 62, 63, and 64 are spaced apart from each other to form a vertical channel between neighboring vertical baffles. Therefore, the sludge mixed liquid forms flocs before flowing into the settling tank 3, and the flocs introduced into the settling tank 3 are precipitated and discharged to the sludge withdrawal unit 91 installed upstream of the settling tank 3. At this time, it is also possible to omit the flow-flow plate 54 provided downstream of the distribution channel (53).

Next, FIG. 11 is an embodiment in which the distribution channel 53 is provided with a distribution pipe 22 shown in FIG. 5 at the tip. Therefore, the sludge mixed liquid of the inflow water tank 51 (or the reaction tank) is introduced into the distribution pipe 22 through the inflow pipe 21, and the sludge mixed liquid introduced into the distribution pipe 22 is formed in the distribution pipe 22. After impinging on the inner circumferential surface and is distributed, it flows out into the distribution channel 53 through the slit 23. In addition, the sludge mixed solution flowing out of the distribution pipe 22 sequentially passes through the vertical channel of the floc forming part 60. As such, by forming the distribution pipe 22 at the front end of the floc forming part 60, the flocculation efficiency can be increased by further increasing the possibility of collision and the number of times between the floating particles or the floating particles and the sticky sludge floc.

Referring back to FIG. 113, a second floc forming part 660 is further provided inside the settling tank 3. The second floc forming part 660 has the same configuration as the floc forming part 60 described above. The second floc forming part 660 may agglomerate the sludge mixture liquid that is not processed by the floc forming part 60 installed in the distribution channel 53. As such, by providing the floc forming parts 60 and 660 in the distribution channel 53 and the settling tank 3, respectively, more enhanced sedimentation efficiency can be obtained.

In this case, the second floc forming part 660 is composed of a plurality of vertical baffles 661, 662, 663 and 664 installed downstream of the sludge drawing part 91. Both ends of each vertical baffle are fixed to both side walls of the sedimentation basin 3, and the vertical baffles 661, 662, 663 and 664 are spaced apart from each other to form a plurality of vertical channels.

12A, 12B and 12C are side cross-sectional views showing various modifications of the secondary settling basin 10 according to the present invention.

First, FIG. 12A shows a secondary sedimentation basin 10 having a floc forming part 60 composed of a plurality of vertical baffles not only in the distribution channel 53 but also in the inflow tank 51. As such, when the floc forming part 60 is provided in the inflow water tank 51, the second floc forming part 660 installed in the settling tank 3 may be omitted. 12b and 12c show the secondary sedimentation basin 10 using mechanical rotary mixing or air mixing instead of installing a vertical baffle in the distribution channel 53 (or the inlet tank 51). That is, in FIG. 12B, a floc is formed by installing a rotary stirrer 555 having a plurality of rotary blades in the distribution channel 53 and the inflow tank 51. In addition, in FIG. 12C, an air diffuser 700 is installed in the distribution channel 53 and the inflow water tank 51 to form a floc by using a circulation flow caused by air bubbles injected from the air diffuser 700. Thus, when using the rotary stirrer 555 and the diffuser 700, it is preferable to provide the 2nd floc formation part 660 in the settling tank 3. As shown in FIG. Other configurations are the same as those of the secondary sedimentation basin 10 described above, and thus a detailed description thereof will be omitted.

Meanwhile, FIGS. 13 and 14 are side cross-sectional views and enlarged views showing a circular secondary sedimentation basin 100 having a floc forming part according to the present invention. As shown, in the circular secondary sedimentation basin 100 according to the present invention, the sludge mixture inlet 105 is formed at the center of the circular sedimentation tank 103. In addition, the inlet pipe 121 which communicates with the reaction tank and introduces the sludge mixture is installed at the upper portion of the double pipe 130 formed at the center of the circular precipitation tank 103. The inner hollow portion 131 of the double pipe 130 is provided with a rotating shaft 112 for rotating the sludge collector 102 installed on the bottom surface of the circular sedimentation tank 103, the outer bulge of the double pipe 130 ( 132 is provided with a spiral inlet water tank 140 to guide the sludge mixture supplied through the inlet pipe 121 to the bottom. The inflow tank 140 is formed by a spiral bottom plate 141 welded to the outer hollow portion 132 of the double pipe 130. Reference numeral 107 denotes a symbolic water outlet, 109 a sludge outlet, and 104 a sludge suction pipe.

Subsequently, the inflow tank 140 converts the flow of the sludge mixture flowing downward to increase the chance and number of collisions between the floating particles or the floating particles and the sticky flocs, thereby greatly increasing the settling properties of the sludge. The unit 160 is provided. The floc forming part 160 includes a plurality of vertical baffles 161, 162, 163, 164, and 165 spaced apart at predetermined intervals along the inflow water tank 140. The vertical baffles 161 to 165 are alternately installed at a lower end thereof adjacent to the spiral bottom plate 141 and installed at a predetermined distance away from the bottom plate 141 to repeatedly change the flow of the sludge mixture in the vertical direction. To be possible. At this time, the bottom and top of each vertical baffle (161 ~ 165) is installed to be spaced apart from the spiral bottom plate 141 by a predetermined interval to prevent the settling sludge and scum. In addition, the plurality of vertical baffles (161, 162, 163, 164, 165) are installed on the outer inner circumferential surface of the double tube 130 and the inner outer circumferential surface of the double tube 130, respectively, alternately spaced downward flow of the sludge mixture It is also possible to repeatedly switch to the left and right directions.

On the other hand, the bottom of the outer hollow portion 132 of the double pipe 130 is provided with a flow-flow plate 166 is formed with a plurality of perforation holes. The process flow plate 166 smoothly settles the settling sludge floc by equally distributing the sludge mixture flowing along the inflow water tank 140 and minimizing turbulence. As such, the circular secondary sedimentation basin 100 according to the present invention forms a spiral inlet water tank 140 in the sludge mixture inlet 105, and a plurality of vertical baffles 161 to 165 in the inlet water tank 140. By increasing the flow path of the sludge mixture and by repeatedly changing the flow direction of the sludge mixture up and down to increase the chance of collision between the suspended particles and the sticky sludge floc to improve the sludge sedimentation.

In addition, Figure 15 is an enlarged view showing another embodiment of a circular secondary sedimentation basin 100 with a floc forming portion according to the present invention. As shown, the upper portion of the double pipe 130 formed perpendicular to the center of the circular settling tank 103 is installed at the tip of the inlet pipe 121 to distribute the sludge mixture evenly in the circumferential direction of the double pipe (130) The ring-shaped distribution pipe 122 in which the slit 123 of predetermined width is formed so that it may be provided is provided. In addition, a vertical inflow water tank 240 is formed at the outer hollow portion 132 of the double pipe 130 so as to guide the sludge mixed liquid flowing out from the distribution pipe 122 downward. In addition, a floc forming portion 260 is formed in the vertical inflow tank 240 inclined downward at a predetermined angle to change the flow direction of the sludge mixed liquid downward. . For example, annular baffles (261, 263, 265) provided on the outer inner circumferential surface of the double tube 130 and annular baffles (262, 264) provided on the inner outer circumferential surface of the double tube 130 are alternately spaced to form a zigzag inflow tank. do. In addition, a bottom surface of the double pipe 130 may be further provided with a flow plate 266 is formed a plurality of permeable holes.

As such, the circular secondary sedimentation basin 100 according to the present embodiment distributes the sludge mixture flowing through the ring-shaped distribution pipe 122 evenly in the circumferential direction of the double pipe 130 and at the same time the flow of the sludge mixture is switched. do. In addition, the present invention extends the flow path by converting the sludge mixture flowing downward through the plurality of annular baffles (261 ~ 265) to the left and right, while stirring the sludge mixture and the chance of collision between the suspended particles and sticky sludge floc and Increase the number of times to improve the sedimentation of the sludge.

Although the preferred embodiments of the rectangular secondary settler and the circular secondary settler according to the present invention has been described above, one of ordinary skill in the art will be able to implement various modifications according to the technical idea of the present invention. The scope of the right is not limited by this embodiment.

As described above, the secondary sedimentation basin according to the present invention by repeatedly converting the flow of the sludge mixture flowing through the distribution pipe in the front and rear and up and down direction and the collision opportunities between the suspended particles and the sticky floc contained in the sludge mixture Increasing the number of times increases the possibility of trapping of suspended particles in the floc, thereby improving the sedimentation property of the sludge.

In addition, the present invention by converting the flow of the sludge mixture flowing through the inlet pipe into a non-power using a distribution pipe and a plurality of vertical baffles to improve the sedimentation of the sludge to improve the water quality of the treated water, as well as conventional secondary sedimentation basin Compared to this, it is possible to reduce energy consumption and to increase effective sedimentation area.

In addition, the present invention by administering a small amount of flocculant to the sludge mixture flowing through the inlet pipe and stirred through the distribution pipe or floc forming unit to improve the sedimentation and dehydration of the sludge to improve the water quality of the treated water and the water content of the excess sludge By lowering the processing cost can be reduced.

Claims (20)

A sedimentation tank, a sludge mixture inlet formed at an upstream side of the sedimentation tank, a symbolic water outlet formed at an upper portion of the downstream side of the sedimentation tank, a sludge withdrawal portion formed at a lower side of the sedimentation tank, and a sludge collector installed at the sedimentation tank. In the secondary sedimentation basin for biological sewage and wastewater treatment apparatus, including The secondary sewage treatment apparatus for biological sewage and wastewater treatment equipment, characterized in that a floc forming part formed of a plurality of vertical baffles spaced apart from each other is installed in the sedimentation tank so as to induce the flow of the sludge mixture flowing from the reaction tank (aeration tank) in the vertical direction. Sedimentation basin. A sedimentation tank, a sludge mixture inlet formed at an upstream side of the sedimentation tank, a symbolic water outlet formed at an upper portion of the downstream side of the sedimentation tank, a sludge withdrawal portion formed at a lower side of the sedimentation tank, and a sludge collector installed at the sedimentation tank. In the secondary sedimentation basin for biological sewage and wastewater treatment apparatus, including A distribution pipe installed horizontally in the sludge mixture inlet in the width direction of the settling tank and having a slit formed in the longitudinal direction so that the sludge mixed solution introduced from the reaction tank (aeration tank) can be equally discharged in the width direction of the settling tank, and introduced from the reaction tank In order to guide the sludge mixture to the middle portion of the distribution pipe, one end is in communication with the reaction vessel and the other end is configured for biological sewage and wastewater treatment apparatus comprising an inlet pipe installed to be orthogonal to the distribution pipe. Sedimentation basin. A sedimentation tank, a sludge mixture inlet formed at an upstream side of the sedimentation tank, a symbolic water outlet formed at an upper portion of the downstream side of the sedimentation tank, a sludge withdrawal portion formed at a lower side of the sedimentation tank, and a sludge collector installed at the sedimentation tank. In the secondary sedimentation basin for biological sewage and wastewater treatment apparatus, including A pipe-shaped distribution pipe having slits formed in the longitudinal direction so that the sludge mixture liquid introduced from the reaction tank (aeration tank) can be evenly discharged in the width direction of the settling tank; An inlet pipe having one end connected to the reaction tank and the other end communicating with the distribution pipe to supply the sludge mixture of the reaction tank to the distribution pipe; Secondary sedimentation basin for biological sewage and wastewater treatment apparatus comprising a floc forming portion composed of a plurality of vertical baffles spaced apart to induce the flow of the sludge mixture flowing out from the slit of the distribution pipe in the vertical direction. The method according to claim 2 or 3, Slit formed in the distribution pipe is the secondary sludge pond for biological sewage and wastewater treatment apparatus, characterized in that the sludge mixture is opened toward the inflow side of the sludge mixture flowing through the inlet pipe flows back. The method according to claim 2 or 3, The distribution pipe is installed near the vertical wall of the sedimentation tank and the sludge mixture flowing out through the distribution pipe hits the vertical wall of the sedimentation tank, the flow of the secondary sedimentation basin, characterized in that the flow back. The method of claim 4, wherein The height of the slit formed in the distribution pipe becomes larger toward the left and right from the inlet pipe into which the sludge mixture is introduced, so that the sludge mixture is distributed evenly in the width direction of the sedimentation tank secondary sedimentation basin for biological sewage treatment apparatus. The method according to claim 1 or 3, The plurality of vertical baffles are spaced apart from each other to form a plurality of vertical baffle channels, both ends of each vertical baffle is sedimentary for biological sewage treatment apparatus, characterized in that fixed to both side surfaces of the settling tank. The method according to claim 1 or 3, The plurality of vertical baffles secondary sedimentation basin for biological sewage and wastewater treatment apparatus, characterized in that the height is alternately changed so that the flow of the sludge mixture can be repeatedly converted in the vertical direction. The method according to claim 1 or 3, Secondary sedimentation basin for biological sewage and wastewater treatment apparatus, characterized in that the elevating means is installed in the vertical baffle located downstream of the rear end of the floc forming unit. The method according to claim 1 or 3, Secondary sedimentation basin for biological sewage and wastewater treatment apparatus, characterized in that the flow-flow flow plate is formed downstream of the floc forming portion is formed with a plurality of permeable holes. The method according to claim 1 or 3, The inlet pipe is a secondary sedimentation basin for biological sewage and wastewater treatment apparatus, characterized in that a flocculant administration means for administering a flocculant is installed. The method according to claim 2 or 3, Secondary sedimentation basin for biological sewage and wastewater treatment device, characterized in that the reflector is further installed on the vertical wall of the settling tank to reflect the sludge mixture liquid discharged from the distribution pipe. A sludge mixture inlet consisting of a sedimentation tank, an inflow water tank and a distribution water provided upstream of the sedimentation tank, a supernatant water outlet formed in an upper portion of the downstream side of the sedimentation tank, and a sludge withdrawal portion formed in an upstream side of the sedimentation tank; In the secondary sedimentation basin for biological sewage and wastewater treatment device comprising a sludge collector installed in the sedimentation tank, In the distribution channel of the sludge mixture inlet, the sludge mixture is spaced apart from each other so as to induce the flow of the sludge mixture introduced from the reactor (aeration tank) or the inlet tank in the vertical direction, and forms a plurality of vertical baffle channels. A secondary sedimentation basin for biological sewage and wastewater treatment equipment, which is fixed to the side wall and has a floc forming part formed of a plurality of vertical baffles, the height of which is alternately changed. A sludge mixture inlet consisting of a sedimentation tank, an inflow water tank and a distribution water provided upstream of the sedimentation tank, a supernatant water outlet formed in an upper portion of the downstream side of the sedimentation tank, and a sludge withdrawal portion formed in an upstream side of the sedimentation tank; In the secondary sedimentation basin for biological sewage and wastewater treatment apparatus comprising a sludge collector installed in the sedimentation tank, The sludge mixture inlet is formed spaced apart from each other so as to guide the flow of the sludge mixture in the reaction tank (aeration tank) or the inlet tank in the vertical direction to form a plurality of vertical baffle channels, both ends of the distribution channel A first floc forming portion fixed to the side wall surface, the first floc forming portion having a plurality of vertical baffles installed so that the heights thereof are alternately changed; It is installed spaced apart from each other in the settling tank so as to induce the flow of the sludge mixed liquid flowing out from the floc forming part again up and down to form a plurality of vertical baffle channels, both ends are fixed to both sidewalls of the settling tank, The secondary sedimentation basin for biological sewage and wastewater treatment apparatus, comprising a second floc forming part composed of a plurality of vertical baffles installed alternately. The method according to claim 13 or 14, A distribution pipe installed horizontally in the distribution channel of the sludge mixture inlet and having a slit formed in the longitudinal direction so that the sludge mixture obtained from the reactor can flow out evenly in the width direction of the distribution channel; Biological sewage and wastewater treatment apparatus, characterized in that it comprises an inlet pipe is installed so that one end is in communication with the reaction tank and the other end is orthogonal to the distribution pipe in order to guide the sludge mixture from the distribution pipe to the center portion of the distribution pipe. Secondary settling basin. The method according to claim 13 or 14, The inlet tank is spaced apart from each other so as to induce the flow of the sludge mixture flowing from the reaction tank (aeration tank) in the vertical direction, forming a plurality of vertical baffle channels, both ends are fixed to both sidewalls of the inlet tank, the height of the The secondary sedimentation basin for biological sewage and wastewater treatment equipment, characterized in that the floc forming portion is formed of a plurality of vertical baffles installed alternately. The method according to claim 13 or 14, Secondary sedimentation basin for biological sewage and wastewater treatment apparatus, characterized in that the inlet tank is provided with a stirring device or an acid generator to form a floc. A sludge mixture inlet consisting of a sedimentation tank, an inflow water tank and a distribution water provided upstream of the sedimentation tank, a supernatant water outlet formed in an upper portion of the downstream side of the sedimentation tank, and a sludge withdrawal portion formed in an upstream side of the sedimentation tank; In the secondary sedimentation basin for biological sewage and wastewater treatment apparatus comprising a sludge collector installed in the sedimentation tank, In the distribution channel and the inlet tank of the sludge mixed liquid inlet, an agitator or an air diffuser is installed, and inside the settling tank, spaced apart from each other to guide the flow of the sludge mixed liquid in the vertical direction to form a plurality of vertical baffle channels. Both ends are fixed to both sidewalls of the settling tank, the secondary sedimentation basin for biological sewage and wastewater treatment apparatus comprising a second floc forming part composed of a plurality of vertical baffles installed so that the height is alternately changed. A circular sedimentation tank, a sludge mixed liquid inlet formed in the center of the circular sedimentation tank, a symbolic water outlet formed in the outer periphery of the circular sedimentation tank, a sludge withdrawal unit formed in the lower center of the circular sedimentation tank, and a rotation in the bottom of the circular sedimentation tank. In the secondary sedimentation basin for biological sewage and wastewater treatment apparatus comprising a sludge collector which is possibly installed, A double pipe formed perpendicularly to the center of the circular sedimentation tank, an inlet pipe installed at an upper portion of the double pipe to introduce a sludge mixed liquid from the reaction tank, and a spiral formed in the double pipe so as to guide the sludge mixed liquid supplied from the inlet pipe downward; A secondary sedimentation basin for biological sewage and wastewater treatment apparatus, comprising: a floc forming part comprising a mold inflow tank and a plurality of vertical baffles installed vertically on the inflow tank. A circular sedimentation tank, a sludge mixed liquid inlet formed in the center of the circular sedimentation tank, a symbolic water outlet formed in the outer periphery of the circular sedimentation tank, a sludge withdrawal unit formed in the lower center of the circular sedimentation tank, and a rotation in the bottom of the circular sedimentation tank. In the secondary sedimentation basin for biological sewage and wastewater treatment apparatus comprising a sludge collector which is possibly installed, A double pipe formed perpendicularly to the center of the circular sedimentation tank, an inlet pipe installed at an upper portion of the double pipe to introduce a sludge mixed solution from the reaction tank, and installed at the tip of the inlet pipe to distribute the sludge mixed solution evenly in the circumferential direction of the double pipe. A ring-shaped distribution pipe formed with a slit so as to be slit, a vertical inflow water tank formed at an outer hollow of the double pipe so as to guide the sludge mixed liquid flowing out of the distribution pipe downward, and installed downwardly inclined to the vertical inflow water tank A secondary sedimentation basin for biological sewage and wastewater treatment apparatus, comprising a floc forming part composed of a plurality of annular baffles for changing the flow direction of the sludge mixture.

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