JPH08197081A - Biological treatment utilizing carrier with microorganism stuck thereto and device therefor - Google Patents

Abstract

PURPOSE: To provide biological treatment and device therefor without causing a nonuniform distribution of the carrier concn. in an aeration tank and without the carrier being deposited on the bottom of the aeration tank. CONSTITUTION: This biological treating device is provided with the aeration tank 1 having a raw water inlet 2, a return sludge feed pipe 9, a waste water outlet pipe 3 and an aerating means 5 and wherein activated sludge and a carrier 6 to which a microorganism is stuck are suspended by the aerating means 5. A pipe or plate 7 inclined downward in the flow direction is set in multiple stages on the vertical section in the flow direction in the tank 1 to float and separate the carrier 6, and the sp.gr. of the carrier 6 is preferably controlled to 0.8 to 1.0.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biological treatment method for organic waste water, and more particularly to a novel biological treatment method and apparatus for suspending and flowing a microorganism-attached carrier together with activated sludge in an aeration tank.

[0002]

2. Description of the Related Art Recently, polyethylene glycol gel, polyacrylamide gel, polyvinyl alcohol gel, etc. have a specific gravity of 1 or more (about 1.02 to 1.04) as an effective measure for improving the nitrification reaction in activated sludge treatment.
Attention has been focused on the method for adhering microorganisms, in which nitrifying bacteria are supported on the settling granular gel of (1), and the suspension is allowed to flow together with activated sludge in an aeration tank. However, the inventor of the present invention has encountered the following major problems in the course of improvement research of this method. That is, as shown in FIG. 2, the carrier flows down along with the water flow in the aeration tank, resulting in a decrease in the carrier amount at the front and middle portions of the aeration tank and an increase in the carrier concentration at the terminal portion, resulting in a nitrification function. The problem is that it causes a significant decrease in Also,
In order to prevent such bias of carrier concentration, we tried to pump the carrier back from the end of the aeration tank to the tip, but the strength of the gel carrier was weak, so the carrier was strongly sheared when passing through the pump. There was also the problem of destruction by force. Also, the pump power cost was not negligible. Furthermore, since the specific gravity of the carrier is 1 or more,
There is also a drawback that some carriers precipitate on the bottom of the region of the aeration tank where the aeration strength is weak.

[0003]

DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems, does not cause uneven distribution of carrier concentration in the aeration tank, makes it unnecessary to pump the carrier back, and allows the carrier to reach the bottom of the aeration tank. An object of the present invention is to provide a new biological treatment method and apparatus capable of preventing carrier deposition.

[0004]

In order to solve the above problems, the present invention provides a biological treatment method for sewage, which is performed in an aeration tank having activated sludge and a microorganism-adhering carrier while the carrier is suspended and flowing by aeration. The microbial adherent carrier is settled and separated by an inclined tube or an inclined plate provided in a multi-stage in a vertical cross section so as to incline downward in the flow direction of the aeration tank,
The carrier is designed so as not to move over the inclined tube or the inclined plate. Further, in the present invention, a living organism having a raw water inflow pipe, a returning sludge supply pipe, a drainage outflow pipe, and an aeration means, and an aeration tank holding the activated sludge and the microorganism-attached carrier in a floating state by the aeration means. In the processing apparatus, inclined pipes or inclined plates inclined downward in the flow direction for floating and separating the microorganism-attached carrier are installed in a multi-stage manner in a vertical cross section in the flow direction in the aeration tank.

Next, the present invention will be described in detail with reference to FIG. FIG. 1 is a schematic sectional configuration diagram of a biological treatment apparatus of the present invention. In FIG. 1, 1 is an aeration tank and 2 is raw water such as sewage. Numeral 3 is the effluent water that flows out after being subjected to biological treatment, and is usually guided to the settling basin 8 for solid-liquid separation of the activated sludge. Reference numeral 4 is aeration air, and 5 is an aeration means such as an air diffuser. 6 is one of the points of the present invention, and the specific gravity is 0.
It is a granular material (having a particle size of about 1 to 3 mm) of polyethylene, polypropylene or the like, which has an extremely high strength adjusted to 8 to 1 (does not break at all even when pumped) and acts as a carrier for adhering microorganisms such as nitrifying bacteria. Reference numeral 7 denotes an inclined tube or an inclined plate (hereinafter abbreviated as an inclined tube) for floating and separating the carrier.

In the present invention, because the floating separation of the carrier is important, it is not at a position where downward flow does not occur at the position of the inclined pipe (that is, not on the upstream side of each compartment (compartment) in the aeration tank caused by the inclined pipe). It is advisable to dispose an air diffusing pipe, etc. It is important that the inclined pipe and the inclined plate 7 are inclined downward with respect to the water flow direction as shown in FIG. Etc. 7 has an inclination angle, spacing and length that allow the carrier to be floated and separated. 9 is activated sludge returned from the settling tank. BOD and ammonia of the raw water are removed by the biological action of both the microorganisms that are not attached) and the microorganisms (nitrifying bacteria, etc.) attached to the carrier.

[0007]

In FIG. 1, since there is a water flow (corresponding to the flow of a river) from the left side to the right side, both the activated sludge and the carrier try to move to the right side by riding on the water flow. Since a slant pipe is provided in the vertical cross section of 1 and only the carrier is floated and separated while the water passes through this slant pipe and the activated sludge is allowed to pass as it is, the carrier moves to the downstream side along with the water flow. Without compartments A to D
You can stay inside. On the other hand, since the activated sludge does not float, the activated sludge is not floated and separated by the slant pipe 7 or the like, rides on the water flow as it is, passes through each of the sections A to D, and is settled and separated in the settling tank 8 together with the outflow water. Further, since the diameter of the inclined tube is as large as about 10 cm, clogging troubles due to impurities in the raw water do not occur unlike the method of separating the carrier by providing a screen. 10 is clear treated water. That is, the inclined pipe 7 has a function of skillfully classifying the both by utilizing the floating property of the carrier and the sedimentation property of the activated sludge. By the above action, the carrier is evenly distributed in each section A to D in the aeration tank without being biased toward the outflow water 3 side.

The suspension concentration of the carrier is preferably set to about 5 to 40% by volume. This is because if the carrier suspension concentration is too low, the biological reaction rate will decrease, and if it is too high, the suspension will not flow smoothly due to aeration. In the present invention, the specific gravity of the carrier is extremely important.
When it was 80 or less, it was confirmed that the floatability was so large that the carrier floated to be in a fixed layer state, and it was difficult to uniformly suspend and flow the aerated tank even by aeration. In the present invention, it is important that the floatable carrier is not used in the state of a fixed bed, but is made to flow in a substantially uniform manner throughout the aeration tank. Otherwise, activated sludge SS
Are trapped in the floating fixed layer portion of the carrier and cause clogging. When the specific gravity of the carrier is larger than that of water, some carriers partially settle at the bottom of the aeration tank. In order to adjust the specific gravity of the carrier within this range, it is possible to easily adjust it by adding clay particles or the like to polyethylene or polypropylene and performing melt granulation.

[0009]

EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited thereto. Example 1 Using the apparatus of FIG. 1, biological treatment was performed under the following treatment conditions. (A) Raw water: BOD removed from the group groundwater in advance by the biological denitrification section. (B) Aeration tank volume: 10 m ³ , Dimensions: Water depth 2 m x Width 1 m x Length 5 m, (c) Residence time: 4 hours,

[0010 (d) The average flow rate ... 1.25 m / hr in the horizontal direction of the water flow in the aeration tank, (e) aeration process ... diffuser aeration by plates, aeration amount sewer 1 m ³ per 7m ^3. (F) Inclined tube installation method: Installed as shown in Fig. 1 at 1m intervals in the horizontal direction of the aeration tank. The inclination angle is 60 degrees, the diameter of one inclination pipe is 10 cm, and the inclination pipe length is 40 cm. (G) Microorganism-attached carrier: Polyethylene pellets having a particle size of 2.5 to 3 mm to which nitrifying bacteria are attached, specific gravity of 0.
96, carrier suspension concentration 20% volume. (H) Activated sludge MLSS ... 2000-2500 mg
/ L, (i) Settling basin water area load ... 25 m / d,

As a result of operating under the above conditions, when no aeration was carried out, the carrier floated to the surface of the water and became in a fixed bed state, but when aeration was started, the fixed bed state was broken and the carrier was suspended very smoothly and uniformly in the aeration tank. It became cloudy. Further, the carrier quickly floated and separated at the inflow end of the slant pipe, and only activated sludge passed through the slant pipe. As a result, it was confirmed that the carrier was not biased toward the outflow side of the aeration tank. Further, since the carrier has a floating property, there was no problem that the carrier sinks to the bottom of the aeration tank. The ammoniacal nitrogen (18-22 mg / liter) in the raw water was almost completely nitrified, and the ammoniacal nitrogen in the effluent was stable at 1 mg / liter or less.

[0012]

According to the present invention, the following effects can be obtained. (1) In a biological treatment apparatus that uses a microorganism-attached carrier, deviation of the carrier in the aeration tank toward the downstream side does not occur. (2) A pump for returning the carrier from the end of the aeration tank to the tip is unnecessary. (3) There is no problem that the carrier sinks to the bottom of the aeration tank. (4) Since the strength of the carrier is very large, there is no destruction of the carrier. (5) Since it is not necessary to use a separate screen for separating the carrier, clogging troubles due to impurities in the raw water do not occur.

[Brief description of drawings]

FIG. 1 is a schematic sectional configuration diagram of a biological treatment apparatus of the present invention.

FIG. 2 is a schematic explanatory view of a conventional aeration tank.

[Explanation of symbols]

1: Aeration tank, 2: Raw water, 3: Outflow water, 4: Air, 5: Air diffuser, 6: Microorganism-attached carrier, 7: Inclined tube, 8: Sedimentation tank,
9: returned sludge, 10: treated water, 11: excess sludge, 12:
screen,

Claims (3)

[Claims] 1. A biological treatment method for sewage in an aeration tank having activated sludge and a carrier having attached microorganisms, wherein the carrier is suspended and flowed by aeration, and a vertical cross section is inclined downward in the flow direction of the aeration tank. An organism using a microorganism-attached carrier characterized in that the microorganism-attached carrier is floated and separated by a tilted tube or a tilted plate provided in a multi-step manner so that the carrier does not move over the tilted tube or the tilted plate. Processing method. 2. The biological treatment method using the microorganism-attached carrier according to claim 1, wherein the carrier has a specific gravity of 0.8 to 1.0. 3. A biological treatment having a raw water inflow pipe, a returning sludge supply pipe, a drainage outflow pipe, and an aeration means, and an aeration tank holding the activated sludge and the microorganism-supporting carrier in a floating state by the aeration means. In the apparatus, a microorganism adhering carrier characterized in that a slant pipe or a slant plate inclined downward in the flow direction for floating and separating the microorganism adhering carrier in a vertical cross section in the flow direction in the aeration tank is installed in multiple stages Biological treatment equipment.