JP2018164894A - Arrangement method of water treatment system and diffuser - Google Patents

Arrangement method of water treatment system and diffuser Download PDF

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JP2018164894A
JP2018164894A JP2017063489A JP2017063489A JP2018164894A JP 2018164894 A JP2018164894 A JP 2018164894A JP 2017063489 A JP2017063489 A JP 2017063489A JP 2017063489 A JP2017063489 A JP 2017063489A JP 2018164894 A JP2018164894 A JP 2018164894A
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air
diffuser
side wall
air diffuser
treatment system
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JP6912236B2 (en
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祐子 松▲崎▼
Yuko Matsuzaki
祐子 松▲崎▼
鈴木 茂
Shigeru Suzuki
鈴木  茂
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Sumitomo Heavy Industries Environment Co Ltd
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Sumitomo Heavy Industries Environment Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PROBLEM TO BE SOLVED: To provide a water treatment system equipped with a diffuser capable of generating a strong swirling flow in a tank to enhance air lift effect.SOLUTION: There is provided a water treatment system equipped with a diffusion tank and a diffuser arranged adjacent to one side wall of the diffusion tank while forming a gap with the other side wall of the diffusion tank, wherein the diffuser gradually decreases or increases the amount of diffusion as extending from the other side wall of the diffusion tank toward the one side wall thereof. This water treatment system can prevent scum deposition on a water surface by generating a strong swirling flow on the water surface.SELECTED DRAWING: Figure 1

Description

本発明は、液体中に微細な気泡を分散させるための散気装置を備える水処理システム及び散気装置を配置する方法に関するものである。更に詳しくは、排水等を水処理するための散気槽に用いる散気装置を備える水処理システム及び散気装置の配置方法に関するものである。   The present invention relates to a water treatment system including an air diffuser for dispersing fine bubbles in a liquid and a method for arranging the air diffuser. More specifically, the present invention relates to a water treatment system including an air diffuser used for an air diffuser for treating wastewater and the like, and an arrangement method of the air diffuser.

下水や汚水等の排水を処理する方法として、排水処理装置に散気槽を設け、この散気槽内に散気装置を設置し、この散気装置により空気を微細な気泡として排水中に分散する方法がある。散気装置は、ブロワーにより供給された酸素等を微細な気泡に変えて散気槽内に供給し、被処理水中の溶存酸素量を高めるものである。特に、処理効率に関わる酸素移動効率を向上させるための散気装置が広く用いられている。   As a method of treating wastewater such as sewage and sewage, an air diffuser is installed in the wastewater treatment device, and an air diffuser is installed in the air diffuser, and this diffuser disperses air into the wastewater as fine bubbles. There is a way to do it. The air diffuser converts oxygen or the like supplied by the blower into fine bubbles and supplies the air into the air diffusion tank to increase the amount of dissolved oxygen in the water to be treated. In particular, a diffuser for improving the oxygen transfer efficiency related to the processing efficiency is widely used.

例えば、特許文献1には、散気装置としてメンブレン式散気装置を設けた水処理システムが記載されている。
特許文献1には、メンブレン式散気装置を用いた散気において、メンブレン式散気装置への通気量を所定値以下に設定することで、気泡径を小さくし、気泡径の分布幅を狭くすることができるため、高い酸素移動効率を達成し、水処理効率を高めることが記載されている。
For example, Patent Document 1 describes a water treatment system provided with a membrane-type air diffuser as an air diffuser.
In Patent Document 1, in air diffusion using a membrane air diffuser, the air flow rate to the membrane air diffuser is set to a predetermined value or less, thereby reducing the bubble diameter and narrowing the bubble diameter distribution width. Therefore, it is described that high oxygen transfer efficiency is achieved and water treatment efficiency is increased.

特開2008−221158号公報JP 2008-221158 A

特許文献1に記載されるメンブレン式散気装置のような超微細気泡散気装置では、気泡径を小さくすることにより酸素移動効率を高めることができる。しかし、気泡によるエアリフト効果が小さくなるため、槽内に強い旋回流を発生させることが困難となる。その結果、水面での流速が低下して、スカムが水面に留まりやすくなるという問題が生じる。   In the ultrafine bubble diffuser such as the membrane diffuser described in Patent Document 1, the oxygen transfer efficiency can be increased by reducing the bubble diameter. However, since the air lift effect due to the bubbles is reduced, it is difficult to generate a strong swirling flow in the tank. As a result, the flow velocity at the water surface is lowered, and there arises a problem that the scum tends to stay on the water surface.

そこで、本発明の課題は、エアリフト効果が高められ、槽内に強い旋回流を発生させることが可能な散気装置を備えた水処理システムを提供することである。   Then, the subject of this invention is providing the water treatment system provided with the diffuser which can raise the air lift effect and can generate a strong swirl flow in a tank.

本発明者は、上記課題について鋭意検討した結果、散気装置を散気槽の一方の側壁に寄せて配置する散気装置を備えた水処理システムにおいて、局所的に散気密度が高くなるように散気装置の散気量を減少あるいは増加させることで、水面での強い流れが生じ、水面でのスカム堆積防止が可能となることを見出して本発明を完成させた。
具体的には、本発明は、以下の水処理システム及び散気装置の配置方法である。
As a result of earnestly examining the above problems, the present inventor seems to locally increase the aeration density in the water treatment system including the aeration apparatus that places the aeration apparatus close to one side wall of the aeration tank. In addition, the present inventors have found that by reducing or increasing the amount of air diffused by the air diffuser, a strong flow occurs on the water surface, and scum accumulation can be prevented on the water surface.
Specifically, this invention is the arrangement | positioning method of the following water treatment systems and aeration apparatuses.

上記課題を解決するための本発明は、散気槽と、前記散気槽の一方の側壁に近接し、前記散気槽の他方の側壁との間に間隙を形成して設置された散気装置を備える水処理システムであって、前記散気装置は、前記他方の側壁から前記一方の側壁に向かうに従い、散気量が次第に減少あるいは増加することを特徴とするものである。   The present invention for solving the above-mentioned problems is an air diffuser installed near a diffuser tank and one side wall of the diffuser tank with a gap formed between the other side wall of the diffuser tank. A water treatment system including an apparatus, wherein the air diffuser is configured such that the amount of air diffused gradually decreases or increases from the other side wall toward the one side wall.

本発明の水処理システムによれば、散気装置は、散気槽の他方の側壁から一方の側壁に向かうに従い、散気量が次第に減少あるいは増加するように構成されているため、局所的にエアリフト効果の高い領域が生じ、散気槽内に強い旋回流が生じる。その結果、水面の流速が上昇し、水面でのスカム堆積を防ぐ効果を奏する。   According to the water treatment system of the present invention, the air diffuser is configured so that the amount of air diffused gradually decreases or increases from the other side wall of the air diffusion tank toward the one side wall. A region having a high air lift effect is generated, and a strong swirling flow is generated in the air diffusion tank. As a result, the flow velocity on the water surface increases, and the effect of preventing scum accumulation on the water surface is achieved.

更に、本発明の散気装置を備える水処理システムの一形態としては、散気装置は、前記他方の側壁から前記一方の側壁に向かうに従い、散気量が次第に増加することを特徴とするものである。
この特徴によれば、散気槽の側壁により近い側の散気密度が高まるため、散気装置に近接する一方の側壁付近で強い上昇流が発生する。この上昇流は、水面において他方の側壁に向かう流れとなり、他方の側壁付近で下降流となる。すなわち、散気槽全体を旋回する旋回流が形成される。この旋回流は、散気量が均等になるように配置された散気装置に比べて、水面の流速が格段に上昇するため、水面でのスカム堆積をより確実に防止することができる。
Furthermore, as one form of a water treatment system provided with the air diffusing device of the present invention, the air diffusing device gradually increases the amount of air diffusing as it goes from the other side wall to the one side wall. It is.
According to this feature, the density of the air diffuser closer to the side wall of the air diffusion tank is increased, so that a strong upward flow is generated in the vicinity of one side wall close to the air diffuser. This upward flow becomes a flow toward the other side wall on the water surface, and becomes a downward flow near the other side wall. That is, a swirl flow that swirls the entire diffusion tank is formed. This swirl flow can prevent scum accumulation on the water surface more reliably, since the flow velocity on the water surface is remarkably increased compared to the air diffuser arranged so that the amount of air diffused becomes uniform.

更に、本発明の散気装置を備える水処理システムの一形態としては、散気装置は、複数の散気体からなり、前記散気体は、前記一方の側壁に向かうに従い、密集するように配置されていることを特徴とするものである。
この特徴によれば、散気装置に供給する空気量を一定にした状態で、散気槽の側壁により近い側の散気密度を高め、水面での強い流れを生じさせることができる。
Furthermore, as one form of a water treatment system provided with the air diffusing device of the present invention, the air diffusing device is composed of a plurality of air diffusing gas, and the air diffusing gas is arranged so as to be closely packed toward the one side wall. It is characterized by that.
According to this feature, in a state where the amount of air supplied to the air diffuser is constant, the air diffuser density closer to the side wall of the air diffuser can be increased, and a strong flow on the water surface can be generated.

また、上記課題を解決するための本発明は、散気槽に、複数の散気体からなる散気装置を配置する方法であって、前記散気装置は、前記散気槽の一方の側壁に近接し、前記散気槽の他方の側壁との間に間隙を形成して設置され、前記散気体は、前記一方の側壁に向かうに従い、密集するように配置されていることを特徴とするものである。   Moreover, this invention for solving the said subject is a method of arrange | positioning the diffuser which consists of a several diffused gas to a diffuser tank, Comprising: The said diffuser is provided in one side wall of the said diffuser tank. Proximity is installed with a gap between the other side wall of the air diffuser and the air diffused gas is arranged so as to be densely packed toward the one side wall. It is.

本発明の散気装置の配置方法によれば、簡易的に上述の水処理システムを構築し、散気槽内の水面の流速を上昇させることができる。   According to the arrangement method of the aeration apparatus of the present invention, the above-described water treatment system can be simply constructed, and the flow velocity of the water surface in the aeration tank can be increased.

本発明の散気装置を備える水処理システムによれば、エアリフト効果が高められ、槽内に強い旋回流を発生させることが可能な散気装置を備えた水処理システムを提供することができる。   According to the water treatment system provided with the air diffusing device of the present invention, it is possible to provide a water treatment system provided with an air diffusing device that can enhance the air lift effect and can generate a strong swirling flow in the tank.

本発明の第1の実施形態の水処理システムの構成を示す概略説明図である。(a)本発明の第1の実施形態の水処理システムの概略斜視図である。(b)本発明の第1の実施形態の水処理システムの平面図である。(c)本発明の第1の実施形態の水処理システムの側面図である。(図1b中のI−I矢視図)It is a schematic explanatory drawing which shows the structure of the water treatment system of the 1st Embodiment of this invention. (A) It is a schematic perspective view of the water treatment system of the 1st Embodiment of this invention. (B) It is a top view of the water treatment system of the 1st embodiment of the present invention. (C) It is a side view of the water treatment system of the 1st embodiment of the present invention. (I-I arrow view in FIG. 1b) 本発明の第2の実施形態の水処理システムの構成を示す概略説明図である。(a)本発明の第2の実施形態の水処理システムの平面図である。(b)本発明の第2の実施形態の水処理システムの側面図である。(図2a中のII−II矢視図)It is a schematic explanatory drawing which shows the structure of the water treatment system of the 2nd Embodiment of this invention. (A) It is a top view of the water treatment system of the 2nd Embodiment of this invention. (B) It is a side view of the water treatment system of the 2nd Embodiment of this invention. (II-II arrow view in FIG. 2a) 水面流速シミュレーションの結果を示した図である。(a)本発明の第1の実施形態の水処理システムにおける結果を示した図である。(b)散気体を等間隔で配置した従来の旋回式の散気装置を備える水処理システムにおける結果を示した図である。It is the figure which showed the result of the water surface flow velocity simulation. (A) It is the figure which showed the result in the water treatment system of the 1st Embodiment of this invention. (B) It is the figure which showed the result in the water treatment system provided with the conventional turning-type aeration apparatus which arranged the aeration gas at equal intervals. 本発明の第1の実施形態の水処理システムと、散気体を等間隔で配置した従来の旋回式の散気装置を備えた水処理システムにおける水面平均流速の比較したグラフである。It is the graph which compared the water surface average flow velocity in the water treatment system of the water treatment system of the 1st Embodiment of this invention, and the water treatment system provided with the conventional swirl type diffuser which arrange | positioned the diffused gas at equal intervals.

本発明の水処理システムは、液体中に微細な気泡を分散させるための散気装置を有する排水処理装置等に利用するものである。特に好ましくは、排水等を活性汚泥により生物学的水処理するための散気槽に用いる超微細気泡散気装置を備える水処理システムに利用される。   The water treatment system of the present invention is used for a waste water treatment apparatus having an air diffuser for dispersing fine bubbles in a liquid. Particularly preferably, it is used in a water treatment system provided with an ultrafine bubble diffuser used in an aeration tank for biologically treating wastewater or the like with activated sludge.

本発明の散気装置を備える水処理システムは、散気槽と、前記散気槽の一方の側壁に近接し、前記散気槽の他方の側壁との間に間隙を形成して設置された散気装置を備える水処理システムであって、前記散気装置は、前記他方の側壁から前記一方の側壁に向かうに従い、散気量が次第に減少あるいは増加することを特徴とする。   A water treatment system including an air diffuser according to the present invention is installed in a space between an air diffuser and one side wall of the air diffuser and between the other side wall of the air diffuser. A water treatment system including an air diffuser, wherein the air diffuser gradually decreases or increases as it goes from the other side wall to the one side wall.

以下、本発明の実施形態を、添付画面を参照して詳細に説明する。なお、この実施形態は、本発明を限定するものではない。   Hereinafter, an embodiment of the present invention will be described in detail with reference to the attached screen. Note that this embodiment does not limit the present invention.

〔第1の実施形態〕
図1は、本発明の第1の実施形態の散気装置を備える水処理システムの構成を示す概略説明図である。(a)本発明の第1の実施形態の水処理システムの全体概略斜視図である。(b)本発明の第1の実施形態の水処理システムの平面図である。(c)本発明の第1の実施形態の水処理システムの側面図である。(図1b中のI−I矢視図)
図1に示すように、本実施形態の水処理システム10は、例えば活性汚泥を用いた水処理施設の散気槽2内に散気装置1aが設置され、散気装置1aは散気槽2内の処理水W(処理対象水と活性汚泥との混合液)に浸漬するとともに、ブロワーBに接続された複数の散気体3からなる散気ユニット4を有し、これらの散気ユニット4にブロワーBから空気が供給されることにより、散気ユニット4から処理水W中に気泡を発生させて散気を行う。
[First Embodiment]
FIG. 1 is a schematic explanatory diagram illustrating a configuration of a water treatment system including an air diffuser according to a first embodiment of the present invention. (A) It is a whole schematic perspective view of the water treatment system of the 1st Embodiment of this invention. (B) It is a top view of the water treatment system of the 1st embodiment of the present invention. (C) It is a side view of the water treatment system of the 1st embodiment of the present invention. (I-I arrow view in FIG. 1b)
As shown in FIG. 1, in the water treatment system 10 of the present embodiment, an air diffuser 1a is installed in an air diffuser 2 of a water treatment facility using activated sludge, for example, and the air diffuser 1a is an air diffuser 2 It has a diffuser unit 4 composed of a plurality of diffused gases 3 connected to the blower B, and is immersed in the treated water W (mixed liquid of treated water and activated sludge). When air is supplied from the blower B, air bubbles are generated in the treated water W from the air diffusion unit 4 to perform air diffusion.

(散気槽)
散気槽2は、側壁2a、2bを有する略直方体状の槽に上部ハンチHu及び下部ハンチHsを有しており、外部には散気装置1aに酸素を含む空気を供給するブロワーBを備えている。
また、散気槽2の内部には、散気槽2の底部と略平行に散気装置1aが設けられている。散気槽2の深さ方向における散気装置1aの位置は、特に制限されないが、通常、散気槽2の底部近傍に設置される。ブロワーBの吐出圧力の制約や既設施設とのバランスを考慮して、散気装置1aを比較的高い位置に設置してもよい。
(Aeration tank)
The air diffuser 2 has an upper hunch Hu and a lower haunch Hs in a substantially rectangular parallelepiped tub having side walls 2a and 2b, and a blower B for supplying air containing oxygen to the diffuser 1a outside. ing.
An air diffuser 1 a is provided inside the air diffuser 2 so as to be substantially parallel to the bottom of the air diffuser 2. The position of the air diffuser 1 a in the depth direction of the air diffuser 2 is not particularly limited, but is usually installed near the bottom of the air diffuser 2. In consideration of the restriction on the discharge pressure of the blower B and the balance with existing facilities, the air diffuser 1a may be installed at a relatively high position.

(散気装置)
散気装置1aは、散気槽2内で散気槽2の幅方向(図1bの上下方向;以下、単に「幅方向」という。)に並設された散気体3からなる散気ユニット4を有するものである。散気ユニット4は、散気槽2の長さ方向(図1bの左右方向;以下、単に「長さ方向」という)に沿って複数並設されている。
(Air diffuser)
The air diffuser 1a includes an air diffuser unit 4 composed of an air diffuser 3 arranged in parallel in the width direction of the air diffuser 2 (the vertical direction in FIG. 1b; hereinafter simply referred to as “width direction”). It is what has. A plurality of aeration units 4 are arranged in parallel along the length direction of the aeration tank 2 (left-right direction in FIG. 1b; hereinafter, simply referred to as “length direction”).

散気装置1a全体としては、散気槽の一方の側壁2aに近接して配置され、他方の側壁2bとの間に間隙Gを形成している。そのため、散気装置1aから発生した気泡は、散気槽1aの領域に上昇流を発生し、上昇流は、他方の側壁2bに向かって流れ、間隙Gの領域に下降流を形成する。   The entire air diffuser 1a is disposed close to one side wall 2a of the air diffusion tank, and a gap G is formed between the other side wall 2b. Therefore, the bubbles generated from the air diffuser 1a generate an upward flow in the region of the air diffusion tank 1a, the upward flow flows toward the other side wall 2b, and forms a downward flow in the region of the gap G.

散気装置1aを配置する領域(一方の側壁2aから散気ユニット4の間隙G側の最端部までの領域)は、散気槽2の幅方向の70%以下であることが好ましい。この範囲に散気装置1aを設けることにより、間隙Gの領域に十分な下降流が発生し、散気槽2全体を循環する旋回流が形成される。
また、散気装置1aを配置する領域は、散気槽2の幅方向の50%以上であることが好ましい。散気装置1aを設けることにより、散気装置1aの配置された領域から発生する上昇流と、間隙Gの領域に発生する下降流のバランスがよく、散気槽2全体に良好な旋回流が形成される。
The region in which the air diffuser 1a is disposed (the region from one side wall 2a to the outermost end on the gap G side of the air diffuser unit 4) is preferably 70% or less in the width direction of the air diffuser 2. By providing the diffuser 1a in this range, a sufficient downward flow is generated in the region of the gap G, and a swirl flow that circulates the entire diffuser tank 2 is formed.
Moreover, it is preferable that the area | region which arrange | positions the diffuser 1a is 50% or more of the width direction of the diffuser tank 2. By providing the air diffuser 1a, the balance between the upward flow generated from the region where the air diffuser 1a is arranged and the downward flow generated in the region of the gap G is good, and a good swirl flow is present in the entire diffuser tank 2. It is formed.

(散気ユニット)
散気ユニット4は、散気槽2の幅方向に配設した複数の散気体3と、散気体3上で幅方向に延在し散気体3の内部同士を気密に連通させる空気供給管であるヘッダ管6とを有している。また、ブロワーBからの空気は、送気管7を通じてヘッダ管6に供給されている。
(Aeration unit)
The diffuser unit 4 is a plurality of diffused gases 3 arranged in the width direction of the diffuser tank 2 and an air supply pipe that extends in the width direction on the diffused gas 3 and communicates the inside of the diffused gas 3 in an airtight manner. And a certain header pipe 6. The air from the blower B is supplied to the header pipe 6 through the air supply pipe 7.

図1a及び図1bに示されるように、散気ユニット4は、散気槽2の一方の側壁2aに近接し、散気槽の他方の側壁2bとの間に間隙Gを形成するように配置されている。また、一方の側壁2aに向かうに従い、散気体3の設置間隔が密集するように配置される。この散気ユニット4は、散気槽2の長さ方向に沿って、複数並設されている。   As shown in FIGS. 1a and 1b, the air diffusion unit 4 is disposed so as to be close to one side wall 2a of the air diffusion tank 2 and to form a gap G between the other side wall 2b of the air diffusion tank. Has been. Moreover, it arrange | positions so that the installation space | interval of the diffused gas 3 may become dense as it goes to one side wall 2a. A plurality of the air diffusion units 4 are arranged in parallel along the length direction of the air diffusion tank 2.

このような散気ユニット4の構成によれば、図1cに示すように、散気体3が密に設けられた散気槽側壁2a側からの散気密度が高くなる。そのため、散気槽側壁2a付近において、より強い上昇流が生じ、この上昇流が水面まで到達し、水面上のスカムSを散気槽側壁2b側へ押し流した後、下降流となって間隙Gを通過する。そして、下降流は、散気槽2の底部を流れて、散気槽側壁2b側から散気槽側壁2aへと向かい、散気槽2全体に旋回流が生じることとなる。   According to such a configuration of the air diffusion unit 4, as shown in FIG. 1c, the air diffusion density from the side of the air diffusion tank side wall 2a where the air diffusion 3 is densely provided becomes high. Therefore, a stronger upward flow is generated in the vicinity of the air diffusion tank side wall 2a, and this upward flow reaches the water surface. After the scum S on the water surface is pushed toward the air diffusion tank side wall 2b, it becomes a downward flow and becomes a gap G. Pass through. And a downward flow flows through the bottom part of the air diffusion tank 2, goes to the air diffusion tank side wall 2a from the air diffusion tank side wall 2b side, and a swirl flow will arise in the air diffusion tank 2 whole.

このようにして形成された旋回流は、散気量が均等になるように配置された散気装置に比べて、水面における流速が格段に上昇するため、水面でのスカム堆積をより確実に防止することができる。   The swirling flow formed in this way can prevent scum accumulation on the water surface more reliably because the flow velocity on the water surface is dramatically increased compared to the air diffuser arranged so that the amount of air diffused is uniform. can do.

なお、散気密度を調整するための手段としては、特に制限されず、第1の実施形態のように、散気体3の設置間隔を調整して、散気体3を密集するように配置する手段の他、例えば、散気体に供給する空気量を調整する手段や、散気体に形成されている散気孔やスリット等の散気口の数又は大きさを調整する手段等でもよい。均等な径を有する微細気泡を散気装置全体に形成しつつ、散気密度を調整できるという点で、散気体を密集するように配置する手段や、散気体に形成されている散気口の数を調整する手段が好ましい。   In addition, it does not restrict | limit especially as a means for adjusting a diffused density, The means which arrange | positions the diffused gas 3 densely by adjusting the installation space | interval of the diffused gas 3 like 1st Embodiment. In addition, for example, means for adjusting the amount of air supplied to the air diffuser, means for adjusting the number or size of the air diffuser holes and slits formed in the air diffuser, and the like may be used. Means for arranging the air diffused densely and the air diffuser port formed in the air diffused in that the air diffuse density can be adjusted while forming fine bubbles having a uniform diameter throughout the air diffuser. Means for adjusting the number are preferred.

また、散気槽側壁2b側から散気槽側壁2aへと向かうに従い、散気量が次第に減少してもよい。これにより、散気槽側壁2b側の散気体3における散気密度が高まるため、水面における流速を上昇することができる。散気槽2全体に良好な旋回流を形成するという観点から、第1の実施形態のように、散気槽側壁2b側から散気槽側壁2aへと向かうに従い、散気量が次第に増加することが好ましい。   Further, the amount of air diffusion may gradually decrease from the side of the air diffusion tank side wall 2b toward the air diffusion tank side wall 2a. Thereby, since the diffuse density in the diffused gas 3 by the side of the diffuser tank side wall 2b increases, the flow velocity on the water surface can be increased. From the viewpoint of forming a favorable swirling flow in the entire air diffusion tank 2, the amount of air diffusion gradually increases from the air diffusion tank side wall 2b side toward the air diffusion tank side wall 2a as in the first embodiment. It is preferable.

散気量を次第に減少あるいは増加する構成としては、散気槽側壁2b側から散気槽側壁2aへと向かうに従い、連続的に散気量が減少あるいは増加する構成としても、断続的に散気量が減少あるいは増加する構成としてもよい。   As a configuration for gradually decreasing or increasing the amount of air diffused, even if the configuration in which the amount of air diffused continuously decreases or increases from the side of the air diffuser tank side wall 2b to the side of the air diffuser tank side wall 2a, the air diffuser is intermittently diffused. A configuration may be adopted in which the amount decreases or increases.

(散気体)
本発明の散気体3は、空気を通過する微細な散気孔を有するメンブレンが巻かれた管状部材からなる散気管であり、「メンブレンパイプ式超微細気泡式散気管」とも呼ばれるものである。散気体3は、多孔質の合成樹脂又はセラミックからなる散気筒や多数のスリットを設けたフレキシブルチューブのような管状部材からなる散気管であってもよい。また、散気体3は、角型、丸型などの板状部材からなる散気板であってもよい。
(Spread gas)
The air diffuser 3 of the present invention is an air diffuser tube made of a tubular member around which a membrane having fine air diffuser holes passing through air is wound, and is also referred to as a “membrane pipe ultrafine bubble air diffuser tube”. The diffused gas 3 may be a diffused tube made of a tubular member such as a diffused cylinder made of a porous synthetic resin or ceramic or a flexible tube provided with a large number of slits. Further, the air diffuser 3 may be a diffuser plate made of a plate-shaped member such as a square shape or a round shape.

〔第2の実施形態〕
図2は、本発明の第2の実施形態の散気装置を備える水処理システムを示す概略説明図である。図2(a)は、本発明の第2の実施形態の水処理システムの平面図であり、図2(b)は、本発明の第2の実施形態の水処理システムの側面図である。(図2a中のII−II矢視図)
第2の実施形態の散気装置1bでは、第1の実施形態の散気体3を、排出する空気量がそれぞれ異なるようにした散気体5a、5b、5c、5d、5e、5fに代えたものである。
[Second Embodiment]
FIG. 2 is a schematic explanatory view showing a water treatment system including an air diffuser according to a second embodiment of the present invention. Fig.2 (a) is a top view of the water treatment system of the 2nd Embodiment of this invention, FIG.2 (b) is a side view of the water treatment system of the 2nd Embodiment of this invention. (II-II arrow view in FIG. 2a)
In the air diffuser 1b according to the second embodiment, the air diffuser 3 according to the first embodiment is replaced with air diffusers 5a, 5b, 5c, 5d, 5e, and 5f that have different amounts of air to be discharged. It is.

散気体5a、5b、5c、5d、5e、5fは、それぞれ排出される空気量が異なるような構造を選択する。例えば、散気体5a、5b、5c、5d、5e、5fは空気を排出する散気口(スリット、孔)の数や大きさが異なる構造としてもよいし、供給する空気量を個々に調整する流量制御機構を設けてもよい。また、図2aに示すように、散気体5a、5b、5c、5d、5e、5fの長さが異なる構造としてもよい。更に、散気体5a、5b、5c、5d、5e、5fとして、それぞれ異なる形態のものを用いてもよい。例えば、管状部材と板状部材の組み合わせであってもよい。   As the diffused gas 5a, 5b, 5c, 5d, 5e, and 5f, a structure is selected in which the amount of air discharged is different. For example, the diffused gas 5a, 5b, 5c, 5d, 5e, and 5f may have a structure in which the number and size of air diffusers (slits and holes) for discharging air are different, and the amount of air to be supplied is individually adjusted. A flow rate control mechanism may be provided. Further, as shown in FIG. 2a, the lengths of the diffused gases 5a, 5b, 5c, 5d, 5e, and 5f may be different. Further, different forms may be used as the diffused gases 5a, 5b, 5c, 5d, 5e, and 5f. For example, a combination of a tubular member and a plate member may be used.

図2bに示されるように、散気の際に、散気体5a、5b、5c、5d、5e、5fの順に排出される空気量を減少させることで、散気槽側壁2a側から強い上昇流が生じ、この上昇流が水面まで到達し、水面上のスカムSを散気槽側壁2b側へ押し流した後、下降流となって間隙Gを通過し、散気槽側壁2b側から散気槽2の底部に向かう旋回流が生じることとなる。   As shown in FIG. 2b, when the air is diffused, the amount of air discharged in the order of the diffused gas 5a, 5b, 5c, 5d, 5e, and 5f is reduced to increase the strong upward flow from the diffuser tank side wall 2a side. This upward flow reaches the water surface, pushes the scum S on the water surface toward the diffuser tank side wall 2b, then flows downward through the gap G, and from the diffuser tank side wall 2b side to the diffuser tank A swirling flow toward the bottom of 2 is generated.

[散気装置の配置方法]
本発明の散気装置の配置方法は、複数の散気体からなる散気装置を配置する方法であって、前記散気装置は、前記散気槽の一方の側壁に近接し、前記散気槽の他方の側壁との間に間隙を形成して設置され、前記散気体は、前記一方の側壁に向かうに従い、密集するように配置し、前記散気装置からの散気量が散気槽の他方の側壁から一方の側壁に向かうに従い、次第に増加するようにすればよい。
具体的には、散気槽の側壁2a寄りの散気体3を密に配置し、側壁2b寄りになるに従い、散気体3の配置間隔が疎になるように配置する。
この散気装置の配置方法により、超微細気泡散気装置のように供給する空気量を比較的少なくして酸素移動効率を向上させる散気装置において、酸素移動効率を低下させることなく強い旋回流を発生させ、水面のスカムの堆積を防ぐことが可能となる。
[Arrangement method of air diffuser]
The arrangement method of the air diffuser according to the present invention is a method of arranging an air diffuser comprising a plurality of air diffusers, wherein the air diffuser is adjacent to one side wall of the air diffuser and the air diffuser The air diffuser is disposed so as to be densely packed toward the one side wall, and the amount of air diffused from the air diffuser is What is necessary is just to make it increase gradually as it goes to one side wall from the other side wall.
Specifically, the diffused gas 3 close to the side wall 2a of the air diffusion tank is arranged densely, and the arrangement interval of the diffused gas 3 is arranged so as to become sparse as it approaches the side wall 2b.
With this air diffuser arrangement method, a strong swirl flow without reducing the oxygen transfer efficiency in an air diffuser that improves the oxygen transfer efficiency by relatively reducing the amount of air supplied as in the ultrafine bubble diffuser. It is possible to prevent the accumulation of scum on the water surface.

<散気装置の水面流速シミュレーション>
本発明の水処理システムについて水面流速シミュレーションを行った。散気体3の配置は、上記第1の実施形態に倣い、散気ユニット4を構成する散気体3を7本としてシミュレーションを行った。その結果を図3aに示す。
なお、図3bは、散気体を等間隔で配置した従来の散気装置における水面流速シミュレーションの結果である。このシミュレーションにおいて、図3a及び図3bの散気体の数は同一としている。
<Water surface velocity simulation of diffuser>
A water flow velocity simulation was performed on the water treatment system of the present invention. The arrangement of the diffused gas 3 was simulated in the same manner as in the first embodiment with seven diffused gases 3 constituting the diffused unit 4. The result is shown in FIG.
FIG. 3b shows a result of a water surface flow velocity simulation in a conventional air diffuser in which the air diffused is arranged at equal intervals. In this simulation, the number of diffused gas in FIGS. 3a and 3b is the same.

シミュレーションはANSYS社の汎用流体シミュレーション用ソフト「フルーエント」を用いて行った。図4で示した計算結果は曝気槽幅が5.5m、槽長が8.6m、槽水深が5.0m、曝気装置設置水深が4.0mに対して実施した結果であるが、あくまでも一例であり、槽形状、曝気装置設置水深、曝気装置レイアウト等を限定するものではない。   The simulation was performed using ANSYS general-purpose fluid simulation software “Fluent”. The calculation results shown in FIG. 4 are the results of an aeration tank width of 5.5 m, a tank length of 8.6 m, a tank water depth of 5.0 m, and an aeration apparatus installation water depth of 4.0 m. The tank shape, the aeration device installation water depth, the aeration device layout, etc. are not limited.

図3aから、本発明の水処理システムでは、水面において、一方の側壁から他方の側壁に向かって一定方向の強い流れが形成されていることがわかる。一方、図3bから、散気体を等間隔で配置した従来の散気装置においては、水面における流れが全体的に拡散していることがわかる。   It can be seen from FIG. 3a that in the water treatment system of the present invention, a strong flow in a certain direction is formed from one side wall to the other side wall on the water surface. On the other hand, it can be seen from FIG. 3b that in the conventional diffuser in which the diffused gas is arranged at equal intervals, the flow on the water surface is diffused as a whole.

また、図4には、本発明の第1の実施形態の水処理システムと、散気体を等間隔で配置した従来の旋回式の散気装置を備えた水処理システムにおける水面平均流速の比較したグラフを示した。
本発明の散気装置における水面平均流速が、散気体を等間隔に配置した散気装置における水面平均流速よりも1.5倍速くなった。
Moreover, in FIG. 4, the water surface average flow velocity in the water treatment system of the 1st Embodiment of this invention and the water treatment system provided with the conventional swirling diffuser which arranged the diffused gas at equal intervals was compared. The graph is shown.
The water surface average flow velocity in the air diffuser of the present invention was 1.5 times faster than the water surface average flow velocity in the air diffuser in which the air diffused was arranged at equal intervals.

図3、4の結果から、散気装置からの散気量が散気槽の一方の側壁から他方の側壁に向かうに従い、次第に減少あるいは増加させるようにすることにより、散気槽の水面に十分な速さの一定方向の流れが発生する。この結果、水面のスカムを押し流し、スカム堆積を防ぐことが可能となる。   From the results of FIGS. 3 and 4, the amount of air diffused from the air diffuser gradually decreases or increases from one side wall of the air diffusion tank toward the other side wall. A constant direction of flow is generated. As a result, the scum on the water surface can be washed away and scum accumulation can be prevented.

本発明の水処理システム及び散気装置の配置方法は、下水処理場等の有機性汚泥や、食品工場や医薬品工場等の有機性排水の好気性微生物処理槽及びその処理方法に使用することができる。   The water treatment system and the arrangement method of the air diffuser according to the present invention can be used in an aerobic microorganism treatment tank for organic sludge such as a sewage treatment plant or an organic wastewater such as a food factory or a pharmaceutical factory, and a treatment method thereof. it can.

1a、1b 散気装置、2 散気槽、2a、2b 側壁、3 散気体、4 散気ユニット、5a、5b、5c、5d、5e、5f 散気体、6 ヘッダ管、7 送気管、10 水処理システム、G 間隙、Hu 上部ハンチ、Hs 下部ハンチ、B ブロワー、W 処理水、S スカム

1a, 1b Air diffuser, 2 Air diffuser, 2a, 2b Side wall, 3 Air diffuser, 4 Air diffuser unit, 5a, 5b, 5c, 5d, 5e, 5f Air diffuser, 6 Header tube, 7 Air supply tube, 10 Water Treatment system, G gap, Hu upper hunch, Hs lower hunch, B blower, W treated water, S scum

Claims (4)

散気槽と、前記散気槽の一方の側壁に近接し、前記散気槽の他方の側壁との間に間隙を形成して設置された散気装置を備える水処理システムであって、前記散気装置は、前記他方の側壁から前記一方の側壁に向かうに従い、散気量が次第に減少あるいは増加することを特徴とする、水処理システム。   A water treatment system comprising an air diffuser installed near a side wall of the air diffuser and the other side wall of the air diffuser to form a gap between the air diffuser, The air diffusion device is characterized in that the amount of air diffusion gradually decreases or increases from the other side wall toward the one side wall. 前記散気装置は、前記他方の側壁から前記一方の側壁に向かうに従い、散気量が次第に増加することを特徴とする、請求項1に記載の水処理システム。   2. The water treatment system according to claim 1, wherein the air diffuser gradually increases in the amount of air diffused from the other side wall toward the one side wall. 前記散気装置は、複数の散気体からなり、前記散気体は、前記一方の側壁に向かうに従い、密集するように配置されていることを特徴とする、請求項2に記載の水処理システム。   The water treatment system according to claim 2, wherein the air diffuser includes a plurality of air diffused gas, and the gas diffused gas is arranged so as to be concentrated toward the one side wall. 散気槽に、複数の散気体からなる散気装置を配置する方法であって、前記散気装置は、前記散気槽の一方の側壁に近接し、前記散気槽の他方の側壁との間に間隙を形成して設置され、前記散気体は、前記一方の側壁に向かうに従い、密集するように配置されていることを特徴とする、散気装置の配置方法。

A method of disposing an air diffuser comprising a plurality of air diffusers in an air diffuser, wherein the air diffuser is adjacent to one side wall of the air diffuser and is connected to the other side wall of the air diffuser. A method for arranging a diffuser, wherein the diffuser is arranged so as to form a gap therebetween, and the diffused gas is arranged so as to be densely packed toward the one side wall.

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