WO2017077774A1

WO2017077774A1 - Settling tank and method for operating same

Info

Publication number: WO2017077774A1
Application number: PCT/JP2016/077634
Authority: WO
Inventors: 哲清水
Original assignee: 栗田工業株式会社
Priority date: 2015-11-02
Filing date: 2016-09-20
Publication date: 2017-05-11
Also published as: JP2017087091A; TW201722532A; JP6269635B2

Abstract

Provided are a settling tank having a simple structure and excellent maintainability and a method for operating the same. A settling tank 1 according to this embodiment is provided with a tank body 2 and a raw water introducing unit 10 for introducing raw water in the lower part within the tank body 2. The tank body 2 has a cylindrically shaped peripheral wall part 2a and a tapered part 2c connected on the bottom side of the peripheral wall part 2a, with the diameter thereof decreasing toward the lower side. The angle of elevation of the tapered part 2c with respect to a horizontal plane is 50 - 70°.

Description

Precipitation tank and its operation method

The present invention relates to a sedimentation tank for separating fine suspended substances and the like from water to be treated and an operation method thereof.

Conventionally, in activated sludge treatment equipment, coagulation sedimentation treatment equipment, etc., sedimentation separation using a solid-liquid separation tank (precipitation tank) is widely adopted as means for separating the sludge mixed liquid into treated water and sludge. As this sedimentation separation, a sludge zone (sludge blanket layer) is formed in the sedimentation tank in order to efficiently remove turbidity and fine SS in the sludge mixture and obtain good treated water. There is a sludge blanket filtration method in which turbidity and fine SS in the sludge mixed solution are filtered and separated by flowing the gas from the distributor into the lower part of the sludge zone and passing through the sludge zone (for example, Patent Documents 1 and 2).

In the sedimentation tank of Patent Document 1, a tubular distributor extends in the radial direction from the lower end of the feed well, and a large number of openings are provided at intervals on the side of the distributor, and the raw water (sludge mixture) is supplied to the opening. Spill through.

In Patent Document 2, a rectangular frame-shaped distributor having a straight tubular side is installed at the bottom of the settling tank, and a liquid outflow opening extending in the longitudinal direction of each side is provided on the bottom surface of the distributor.

Since the conventional distributor has a complicated structure, the opening for raw water outflow may be clogged with sludge and foreign substances, and the maintenance is troublesome.

Japanese Patent Laid-Open No. 10-202009 JP 2014-1000066 A

The present invention has been made in view of the above-described conventional situation, and an object thereof is to provide a sedimentation tank having a simple structure and good maintainability and an operation method thereof.

The precipitation tank of the present invention (first invention) is a precipitation tank comprising a tank body and a raw water introduction part for introducing raw water into the lower part of the tank body, the tank body having a cylindrical peripheral wall part, In a sedimentation tank having a tapered portion connected to the lower side of the peripheral wall portion and having a smaller diameter on the lower side, the elevation angle of the tapered portion with respect to the horizontal plane is 50 ° to 70 °.

In the settling tank according to one aspect of the first invention, the tapered portion is continuous with the bottom surface of the tank body, the raw water introduction portion has a discharge port for discharging raw water toward the bottom surface, and the diameter of the bottom surface is It is larger than the diameter of the discharge port.

In this case, the apparatus further includes a stirring body provided between the bottom surface of the tank body and the raw water introduction section, and the stirring body is connected to a rotating shaft arranged in the vertical direction in the tank body, The rotating shaft may be disposed through the raw water introduction portion.

Furthermore, the raw water introduction section has an insertion hole through which the rotating shaft is inserted, and a passage hole through which the stirring body passes when the stirring body is disposed to be lowered from above the tank body toward the bottom surface. And an elastic cover may be provided in the insertion hole and the passage hole.

The operation method of the settling tank of the present invention (the second invention) is a method for operating the settling tank of the first invention, wherein a sludge blanket is formed in the tank body, and the raw water is introduced from the raw water introduction section into the tank body. The flow rate is 0.35 m / s or less.

In the present invention, since the elevation angle with respect to the horizontal surface of the tapered portion connected to the lower side of the peripheral wall portion of the tank body is 50 ° to 70 °, the raw water discharged from the raw water introduction portion hits the bottom surface of the tank body, and along the tapered portion. An upward flow is formed, and a uniform upward flow as a whole can be passed through the sludge blanket. The raw water introduction part can be a simple configuration that discharges raw water to the bottom surface of the tank body, and a sedimentation tank with good maintainability can be obtained.

It is a longitudinal cross-sectional view of the sedimentation tank which concerns on embodiment. It is a perspective view of a raw water introduction part. It is a perspective view of the raw | natural water introducing | transducing part which attached the elastic cover. 4a to 4c are diagrams for explaining a method of installing the stirring member. It is a longitudinal cross-sectional view of the sedimentation tank which concerns on another embodiment.

Hereinafter, embodiments of the present invention will be described with reference to FIGS.

The sedimentation tank 1 is provided in the tank body 2, the raw water introduction part 10 installed in the lower part (near the bottom) in the tank body 2, and the middle part in the vertical direction of the peripheral wall part 2a of the tank body 2 or slightly higher than that. The outlet 3, the receiving tank 4 communicating with the tank body 2 through the outlet 3, the stirring device 5 provided in the tank body 2, the upper part in the tank body 2, and the sludge blanket S The trough 6 etc. which take out the treated water (supernatant water) which was turbidized when passing through. The inside of the receiving tank 4 is the receiving chamber 4a. The concentrated sludge is taken out from the lower part of the receiving tank 4.

The peripheral wall 2a of the tank body 2 is cylindrical, and the axial direction is the vertical direction. The lower end of the taper part 2c continues to the periphery of the bottom surface 2b of the tank body 2, and the upper end of the taper part 2c continues to the lower end of the peripheral wall part 2a. The tapered portion 2c has a smaller diameter toward the lower side. Accordingly, the inner diameter D ₁ of the cylindrical part of the tank body 2 is larger than the diameter D ₂ of the bottom surface 2b.

The elevation angle θ of the tapered portion 2c with respect to the horizontal plane is 50 ° to 70 °, and preferably 55 ° to 70 °. Considering the production of the sedimentation tank 1, the elevation angle θ is preferably 55 ° to 65 °, particularly about 60 °.

The agitating device 5 is arranged vertically on a drive unit 5a such as a motor, the shaft center part of the tank body 2, and is rotationally driven by the drive unit 5a, and is attached to the lowermost end of the rotation shaft 5b. 1 stirrer 5c, and second and third stirrers 5d and 5e attached higher than that. The stirring bodies 5d and 5e are paddle blades composed of a plurality of blades extending in the radial direction from the rotating shaft 5b. For example, the stirring bodies 5d and 5e extend in the four radiation directions. On the other hand, the stirring member 5c is a single paddle blade that extends from the lowermost end of the rotating shaft 5b in a direction perpendicular to the axial direction.

The stirring body 5c is disposed below the discharge port 10c of the raw water introduction unit 10, for example, directly above the bottom surface 2b. The stirring bodies 5d and 5e are arranged above the raw water introduction unit 10. The uppermost stirring body 5e is positioned below the lower edge of the outlet 3. Stirrer 5d, 5e turning diameter is preferably about 50 to 95% of the inner diameter (diameter) _{D 1} of the cylindrical part of the tank body 2. The turning diameter of the stirring body 5c is preferably about 80 to 95% of the diameter D2 of the bottom surface 2b of the tank body ₂ .

The raw water introduction part 10 has a straight pipe part 10a that penetrates the taper part 2c of the tank body 2 and extends in the horizontal direction, and a bent part 10b that is located on the distal end side of the straight pipe part 10a and bent downward (see FIG. 2 and 3). The opening at the lower end of the bent portion 10b is a discharge port 10c that discharges raw water toward the bottom surface 2b. Discharged from the discharge port 10c raw water dispersed, and in order to sludge deposition area is not too large, the diameter D ₂ of the bottom surface 2b, 1.15 ~ 3 times the diameter D ₃ of the discharge port 10c It is preferable that

The raw water flow rate (raw water introduction flow rate) introduced into the tank body 2 from the raw water introduction unit 10 is preferably 0.35 m / s or less, and more preferably 0.22 m / s or less. The raw water introduction flow rate is preferably 0.01 m / s or more.

The raw water discharged from the discharge port 10c hits the bottom surface 2b and is dispersed. If the height H ₁ to the discharge port 10c of the raw water inlet portion 10 from the bottom surface 2b of the tank body 2 is too small, lateral discharge flow rate is increased, it becomes difficult to uniformly disperse the raw water. On the other hand, if the height H ₁ is too large, the dead space below the tank body 2 increases. Therefore, the height H ₁ is preferably about the same as the diameter D ₃ of the discharge port 10 c, for example, about 0.8 to 1.2 times the diameter D ₃ .

From the discharge port 10c of the raw water inlet portion 10, the height H ₂ of to the top of the tapered portion 2c (lower part of the peripheral wall 2a) is the height required for uniform dispersion of the raw water, the raw water inlet portion 10 installation height The elevation angle θ of the tapered portion 2c with respect to the horizontal plane, the inner diameter D _{1 of the} tank body 2, and the diameter D _{2 of the} bottom surface 2b are determined.

From the top of the tapered portion 2c (lower part of the peripheral wall 2a), the height H ₃ to the lower edge of the outlet 3, taking into account the clarification of raw water, it is preferably 400mm or more.

In order to prevent the floc from being sucked into the treated water side near the trough 6, the height H ₄ from the lower edge of the outlet 3 to the water surface of the treated water is set to the inner diameter D ₁ of the cylindrical portion of the tank body 2. It is preferably 0.5 times or more.

In order to enable the sedimentation tank 1 to be transported by a truck or the like with the stirring device 5 installed, the height H ₅ of the tank body 2 is preferably 2500 mm or less.

The rotating shaft 5b of the agitator 5 and the bent portion 10b of the raw water introduction portion 10 are both disposed at the axial center of the tank body 2, and the rotating shaft 5b is inserted into the bent portion 10b as shown in FIG. An insertion hole 10d is provided. When the stirring member 5c is installed from the bent portion 10b to the discharge port 10c, a passage hole 10e through which the stirring member 5c passes is formed in a slit shape extending in the vertical direction. The upper part of the passage hole 10e is connected to the insertion hole 10d.

As shown in FIG. 3, the insertion hole 10d is provided with a cover 11 that closes the space between the peripheral edge of the insertion hole 10d and the rotation shaft 5b when the rotation shaft 5b is inserted. The cover 11 is an elastic cover made of a material having elasticity such as rubber. The cover 11 is provided along the periphery of the insertion hole 10d, and an opening 11a through which the rotation shaft 5b is inserted is provided at the center. The cover 11 is provided with a slit 11b so as to be connected to a slit 12c described later.

Covers 12a and 12b are provided so as to close the passage hole 10e. A slit 12c is provided between the cover 12a and the cover 12b. The covers 12a and 12b are elastic covers made of a material having elasticity such as rubber.

When installing the stirring device 5, as shown in FIG. 4a, the rotating shaft 5b is lowered from above the tank body 2 toward the bottom surface 2b. At this time, the positions of the rotating shaft 5b and the insertion hole 10d are aligned, and the extending direction of the stirring member 5c is aligned with the passage hole 10d. Even if the position of the rotating shaft 5b is slightly deviated from the position of the opening 11a of the cover 11, the cover 11 has elasticity, so the rotating shaft 5b in contact with the cover 11 is guided to the opening 11a.

Since the covers 11, 12a and 12b have elasticity, as shown in FIG. 4b, the rotating shaft 5b descends while the stirring member 5c passes through the slits 11b and 12c. As shown in FIG. 4c, when the stirring member 5c reaches below the raw water introduction part 10, the passage hole 10e is closed by the covers 12a and 12b. The insertion hole 10d is closed by the cover 11 and the rotating shaft 5b. Therefore, it can suppress that raw | natural water leaks from the insertion hole 10d and the passage hole 10e.

It is preferable to use a material having good slidability with the stirring member 5c as the material of the covers 11, 12a, 12b. Of the covers 11, 12 a, 12 b, a member having good slidability with the stirrer 5 c may be provided in a portion in contact with the stirrer 5 c.

The raw water is discharged downward at a slow flow rate from the discharge port 10c of the raw water introduction section 10, hits the bottom surface 2b of the tank body 2, forms an upward flow along the tapered portion 2c, and becomes a uniform upward flow as a whole. Pass the sludge blanket S. When the agitation bodies 5c to 5e agitate the sludge blanket S, the aggregated floc is adsorbed on the pellets of the sludge blanket S and is compacted by the collision of the pellets.

Raw water flows out of the trough 6 as treated water that has been turbidized when passing through the sludge blanket S. Since the suspended substance is adsorbed by the flocs in the sludge blanket S, the blanket interface rises. When the interface reaches the height of the outlet 3, the floc in the sludge blanket S flows out from the outlet 3 to the receiving chamber 4a. The sludge accumulated and concentrated in the receiving chamber 4a is taken out from the bottom of the receiving chamber 4a.

Stirring by the stirring body 5c is preferably such that the stirring strength in the space from the bottom surface 2b of the tank body 2 to the discharge port 10b of the raw water introduction section 10 is 0.01 to 0.5 s ^{−1 in} terms of G value. An average speed gradient value (G value) represented by the following formula is used as an indicator of the stirring intensity of the stirring and mixing by the stirring blades, and is determined by the size, the number of the stirring blades, and the number of rotations.
G = √ (g · w / μ)
g: Gravitational acceleration (= 9.8) (m / s2)
w: Work per unit time, unit volume (kg · m / m3 · s)
μ: Water viscosity coefficient (kg / m · s)

When stirring is performed with this stirring strength, sludge staying near the bottom surface 2b of the tank body 2 is prevented. Since sludge does not stay near the bottom surface 2b, the sludge is prevented from being spoiled and fermented, and gases such as methane and hydrogen sulfide are not generated. For this reason, the sludge rise resulting from gas adhesion is prevented and the quality of treated water becomes good.

Stirring by the stirring bodies 5e and 5d is preferably such that the stirring strength in the space from the raw water introduction part 10 to the lower edge of the outlet 3 is 2 to 50 s ^{−1 in} terms of G value. The agitation with this agitation strength promotes the growth of flocs of the sludge blanket S.

In the sedimentation tank 1 according to the present embodiment, the raw water introduction unit 10 has a simple structure for discharging raw water downward, and a distributor having a complicated structure having a large number of openings is unnecessary. Therefore, apparatus cost can be suppressed and maintainability can be improved.

In the sedimentation tank 1 shown in FIG. 1, the raw water introduction part 10 is provided in the tank lower part, and the straight pipe part 10a penetrates the taper part 2c of the tank body 2, but like the precipitation tank 1A shown in FIG. The raw water introduction part 10 may be provided in the upper part of the tank, and the straight pipe part 10 a may penetrate the peripheral wall part 2 a of the tank body 2.

The peripheral wall 2a of the tank body 2 is not limited to a cylindrical shape, and may be a rectangular tube with a polygonal cross section.

Hereinafter, the present invention will be described more specifically with reference to examples.
[Example 1]
In treating raw water using the sedimentation tank 1 shown in FIG. 1, whether or not a circulating flow can be formed by the tapered portion 2c and whether or not a sludge blanket S can be formed were examined by CFD analysis. As the analysis program, “ANSY CFX” manufactured by ANSYS was used.

The simulation conditions are as follows.
Raw water SS concentration: 100mg / L
Raw water flow rate: 10m ³ / hr
Raw water discharge flow rate: 0.16m / s
SS sedimentation speed: 55.2 · exp (−0.07 · X) [m / hr] X is the raw water SS concentration The inner diameter D ₁ of the cylindrical portion of the tank body 2: 1000 mm
The diameter of the bottom 2b _D 2: 400mm
Diameter D ₃ of the discharge port 10c of the raw water introduction part 10: 150 mm
Height H ₁ from the bottom surface 2b of the tank body 2 to the discharge port 10c of the raw water introduction part 10: 150 mm
Height H ₃ from the upper part of the taper part 2c to the lower edge of the outlet ₃ : 700 mm
Agitation intensity (G value) by the agitator 5c: 0.03 s ⁻¹
Agitation strength (G value) by the agitators 5d and 5e: 2.1 s ⁻¹

The simulation was performed with the elevation angle θ of the tapered portion 2c with respect to the horizontal plane in increments of 5 ° from 45 ° to 80 °. The results are as follows.

A blanket can be formed by setting the elevation angle θ to 50 ° to 70 °, and blanket formation can be improved by setting the elevation angle θ to 55 ° to 70 °.

[Example 2]
The diameter D ₃ and the raw water discharge flow rate of the discharge port 10c is varied, and whether the sludge blanket S can be formed was examined by CFD analysis. The elevation angle θ of the tapered portion 2c with respect to the horizontal plane was 60 °. Other simulation conditions were the same as those in Example 1. The results are as follows.

A blanket can be formed by setting the discharge flow rate to 0.35 m / s or less, and blanket formation is improved by setting the discharge flow rate to 0.22 m / s or less.

Although the present invention has been described in detail using specific embodiments, it will be apparent to those skilled in the art that various modifications can be made without departing from the spirit and scope of the invention.
This application is based on Japanese Patent Application No. 2015-215806 filed on Nov. 2, 2015, which is incorporated by reference in its entirety.

1, 1A Precipitation tank 2 Tank body 3 Outlet 4 Receiving tank 5 Stirrer 6 Trough 10 Raw water introduction part

Claims

A sedimentation tank comprising a tank body and a raw water introduction part for introducing raw water into the lower part of the tank body,
The tank body
A cylindrical peripheral wall,
A taper portion that is continuous with the lower side of the peripheral wall portion and has a smaller diameter toward the lower side;
In a settling tank having
The settling tank, wherein an elevation angle of the tapered portion with respect to a horizontal plane is 50 ° to 70 °.
In Claim 1, the taper portion continues to the bottom surface of the tank body,
The raw water introduction part has a discharge port for discharging raw water toward the bottom surface,
A sedimentation tank, wherein a diameter of the bottom surface is larger than a diameter of the discharge port.
In claim 2, further comprising a stirring body provided between the bottom surface of the tank body and the raw water introduction portion,
The stirrer is connected to a rotating shaft arranged in the vertical direction in the tank body,
The rotary tank is disposed through the raw water introduction part.
In Claim 3, The said stirring body passes in the said raw | natural water introducing | transducing part, when the said rotating shaft is penetrated and the said stirring body descend | falls from the said tank body toward the said bottom face, and arrange | positions it. And a through hole to be provided,
A settling tank, wherein the insertion hole and the passage hole are provided with an elastic cover.
It is a method of operating the sedimentation tank of any one of Claim 1 thru | or 4, Comprising: A sludge blanket is formed in the said tank body, and the raw | natural water introduction flow velocity from the said raw water introduction part to a tank body is 0.35 m / s or less A method for operating a sedimentation tank, characterized in that