JP7145256B2 - Water treatment system and method for improving water treatment system - Google Patents
Water treatment system and method for improving water treatment system Download PDFInfo
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- JP7145256B2 JP7145256B2 JP2021029134A JP2021029134A JP7145256B2 JP 7145256 B2 JP7145256 B2 JP 7145256B2 JP 2021029134 A JP2021029134 A JP 2021029134A JP 2021029134 A JP2021029134 A JP 2021029134A JP 7145256 B2 JP7145256 B2 JP 7145256B2
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 91
- 238000000034 method Methods 0.000 title claims description 24
- 238000005273 aeration Methods 0.000 claims description 290
- 238000005276 aerator Methods 0.000 description 39
- 239000007789 gas Substances 0.000 description 37
- 239000010802 sludge Substances 0.000 description 12
- 238000004088 simulation Methods 0.000 description 7
- 238000013019 agitation Methods 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 238000009434 installation Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Activated Sludge Processes (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
本発明は、液体中に微細な気泡を分散させるための曝気装置を備える水処理システム及び曝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曝気槽に用いる曝気装置を備える水処理システム及び水処理システムの改良方法に関するものである。 The present invention relates to a water treatment system with an aerator for dispersing fine air bubbles in a liquid and a method of arranging the aerator. More particularly, the present invention relates to a water treatment system equipped with an aerator used in an aeration tank for treating wastewater and the like, and a method for improving the water treatment system.
下水や汚水等の排水を処理する方法として、排水処理装置に曝気槽を設け、この曝気槽内に曝気装置を設置し、この曝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。曝気装置は、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曝気槽内に供給し、被処理水中の溶存酸素量を高めるものである。曝気装置には、全面曝気式、旋回流式などが知られている。 As a method for treating wastewater such as sewage and sewage, there is a method in which an aeration tank is installed in the wastewater treatment equipment, an aeration device is installed in this aeration tank, and the air is dispersed in the wastewater as fine bubbles by this aeration device. . The aerator converts oxygen or the like supplied by the blower into fine bubbles and supplies them into the aeration tank to increase the amount of dissolved oxygen in the water to be treated. As aeration equipment, a full aeration type, a swirling flow type, and the like are known.
全面曝気式は、曝気槽全体に曝気されるため、曝気効率(処理効率)が高いという特徴があるが、曝気槽底部に汚泥が堆積しやすいという面がある。一方、旋回流式は、旋回流によって曝気槽底部の汚泥も撹拌されるため、全面曝気式と比べて曝気槽底部への汚泥の堆積という問題は少ないが、曝気効率が劣るという面がある。 The full-surface aeration type is characterized by high aeration efficiency (treatment efficiency) because the entire aeration tank is aerated, but sludge tends to accumulate on the bottom of the aeration tank. On the other hand, in the swirling flow type, the sludge at the bottom of the aeration tank is agitated by the swirling flow, so the problem of sludge accumulation on the bottom of the aeration tank is less than in the full-surface aeration type, but the aeration efficiency is inferior.
例えば、特許文献1には、曝気効率の向上及び曝気槽底部の汚泥の撹拌を目的とした全面曝気式及び旋回流式の曝気装置を備える水処理システムが記載されている。
特許文献1には、水処理システムの具体例として、仕切り壁を設けた曝気槽内の一方側の中段に第1の曝気装置及び第1の制御装置を備え、更に曝気槽内の底部に第2の曝気装置及び第2の制御装置を備えることが記載されており、中段に設けられた第1の曝気装置が旋回流式、底部に設けられた第2の曝気装置が全面曝気式であることが記載されている。
また、特許文献1には、曝気装置を備えた既存の水処理システムに、更に曝気装置を加えて配置することで、曝気効率を上げることも記載されている。
For example, Patent Literature 1 describes a water treatment system equipped with a full aeration type and a swirl type aerator for the purpose of improving the aeration efficiency and agitating the sludge at the bottom of the aeration tank.
In Patent Document 1, as a specific example of a water treatment system, a first aeration device and a first control device are provided in the middle stage on one side of an aeration tank provided with a partition wall, and a second aeration device and a first control device are provided at the bottom of the aeration tank. It is described that two aeration devices and a second control device are provided. is stated.
Moreover, Patent Document 1 also describes increasing the aeration efficiency by adding an aerator to an existing water treatment system equipped with an aerator.
特許文献1に記載の水処理システムは、曝気槽内に設置高さの異なる複数の曝気装置を設け、更に曝気装置ごとに制御装置を付設し、制御するようになっているため、水処理システム全体として規模が大きく、設置コストや維持コストが掛かるものである。 In the water treatment system described in Patent Document 1, a plurality of aeration devices with different installation heights are provided in the aeration tank, and a control device is attached to each aeration device to control the water treatment system. As a whole, the scale is large, and the installation and maintenance costs are high.
そこで、本発明は、全面曝気式の曝気装置を備える水処理装置において、簡素な構造物で、曝気槽内の撹拌効率を向上することを目的とする。 SUMMARY OF THE INVENTION Accordingly, it is an object of the present invention to improve the stirring efficiency in an aeration tank with a simple structure in a water treatment apparatus equipped with a full-surface aeration type aerator.
本発明者は、上記課題について鋭意検討した結果、全面曝気式の曝気装置を備える水処理システムにおいて、曝気による下降流の一部が曝気装置の下側へ通過するように曝気装置を配置することにより、異なる高さに複数の曝気装置を設けることなく曝気装置の下側にまで流れが生じ、曝気槽内の撹拌効率が上がることを見出して本発明の水処理システムを完成させた。
また、既設の全面曝気式の曝気装置を備える水処理システムに対して、一部下降流が曝気装置の下側へ通過するように曝気装置を配置する方法を適用することにより、曝気装置の下側にまで流れが生じ、曝気槽内の撹拌効率を上げることが可能となることを見出して本発明の水処理システムの改良方法を完成させた。
具体的には、本発明は、以下の曝気装置を備える水処理システム及び水処理システムの改良方法である。
As a result of intensive studies on the above problems, the inventors of the present invention have found that, in a water treatment system equipped with a full-surface aeration type aerator, the aerator is arranged so that part of the downward flow caused by aeration passes through the lower side of the aerator. As a result, without providing a plurality of aerators at different heights, a flow is generated to the lower side of the aerator, and the agitation efficiency in the aeration tank is improved, and the water treatment system of the present invention was completed.
In addition, by applying the method of arranging the aerator so that the downward flow partially passes through the lower side of the aerator to the water treatment system equipped with the existing full-surface aeration type aerator, The present inventors have found that a flow occurs even to the side of the aeration tank, making it possible to increase the agitation efficiency in the aeration tank, and have completed the method for improving the water treatment system of the present invention.
Specifically, the present invention is a water treatment system having the following aerator and a method for improving the water treatment system.
上記課題を解決するための本発明の水処理システムは、曝気槽の略全面に曝気装置を備える水処理システムであって、前記曝気装置は、曝気槽の幅方向の略全幅に曝気体を配した全幅曝気ユニットと、曝気槽の幅方向の一部に曝気体を配した部分曝気ユニットとを組み合わせてなることを特徴とするものである。 A water treatment system of the present invention for solving the above problems is a water treatment system comprising an aeration device substantially over the entire surface of an aeration tank, wherein the aeration device distributes the aeration gas substantially across the entire width of the aeration tank. It is characterized by combining a full-width aeration unit and a partial aeration unit in which the aeration gas is distributed partially in the width direction of the aeration tank.
本発明の水処理システムによれば、部分曝気ユニットが設置された領域に下降流が通過する下降流スペースが形成される。この下降流スペースによって、システム全体を大きくすることなく、かつ全面曝気式曝気装置の曝気効率を下げることなく、曝気装置を設けた面の下にも水流を発生することができる。この結果、曝気槽底部の撹拌が可能となり、曝気槽底部への汚泥の堆積を防ぐ効果を奏する。 According to the water treatment system of the present invention, a downward flow space through which the downward flow passes is formed in the area where the partial aeration unit is installed. This downward flow space allows water flow to be generated below the surface where the aerator is installed without increasing the size of the overall system and without reducing the aeration efficiency of the aerator of the general aeration type. As a result, it becomes possible to agitate the bottom of the aeration tank, which has the effect of preventing the accumulation of sludge on the bottom of the aeration tank.
更に、本発明の水処理システムの一形態としては、前記部分曝気ユニットは、曝気槽の幅方向中心側に偏在して配した複数の曝気体からなり、前記曝気装置は、前記全幅曝気ユニットと前記部分曝気ユニットとを交互に配置することを特徴とするものである。
この特徴によれば、曝気槽内に一定間隔で下降流スペースが設けられることになるため、曝気槽底部において良好な撹拌状態が形成される。
Furthermore, as one form of the water treatment system of the present invention, the partial aeration unit comprises a plurality of aeration gases unevenly distributed on the center side in the width direction of the aeration tank, and the aeration device comprises the full width aeration unit and It is characterized by arranging the partial aeration units alternately.
According to this feature, since downward flow spaces are provided at regular intervals in the aeration tank, a good agitation state is formed at the bottom of the aeration tank.
また、上記課題を解決するための本発明の水処理システムの改良方法は、曝気槽の略全面に曝気装置を備える既設の水処理システムの改良方法であって、曝気槽の幅方向の略全幅に曝気体を配した全幅曝気ユニットから曝気体を取り外し、曝気槽の幅方向の一部に曝気体を配した部分曝気ユニットとすることを特徴とするものである。 Further, a method for improving a water treatment system of the present invention for solving the above problems is a method for improving an existing water treatment system in which an aeration device is provided over substantially the entire surface of the aeration tank, wherein substantially the entire width of the aeration tank in the width direction The aeration gas is removed from the full-width aeration unit in which the aeration gas is placed in the aeration tank, and a partial aeration unit in which the aeration gas is placed in a part of the width direction of the aeration tank is provided.
また、上記課題を解決するための本発明の水処理システムの改良方法は、曝気槽の略全面に曝気装置を備える既設の水処理システムの改良方法であって、曝気槽の幅方向の略全幅に曝気体を配した全幅曝気ユニットにおいて、一部の曝気体への送気を停止して、曝気槽の幅方向の一部に曝気体を配した部分曝気ユニットとすることを特徴とするものである。 Further, a method for improving a water treatment system of the present invention for solving the above problems is a method for improving an existing water treatment system in which an aeration device is provided over substantially the entire surface of the aeration tank, wherein substantially the entire width of the aeration tank in the width direction In a full-width aeration unit in which the aeration gas is arranged in the aeration tank, the supply of air to a part of the aeration gas is stopped, and a partial aeration unit in which the aeration gas is arranged in a part of the width direction of the aeration tank is formed. is.
これらの本発明の水処理システムの改良方法によれば、既設の全面曝気式曝気装置に対して、他の付設設備を設けることなく、かつ曝気効率を下げることなく、曝気装置を設けた面の下にも水流が生じるような曝気装置の配置が可能となる。この結果、曝気槽底部の撹拌を可能とし、曝気槽底部への汚泥の堆積を防ぐ効果を奏する。 According to these methods for improving the water treatment system of the present invention, the surface on which the aeration device is installed can be improved without providing additional equipment to the existing full surface aeration type aeration device and without lowering the aeration efficiency. It is possible to arrange the aerator so that the water flow also occurs below. As a result, it is possible to agitate the bottom of the aeration tank and prevent the deposition of sludge on the bottom of the aeration tank.
本発明の水処理システムによれば、曝気装置を設けた面に曝気による下降流が通過する下降流スペースが形成されることで、システム全体を大きくすることなく、かつ全面曝気式曝気装置の曝気効率を下げることなく、曝気装置を設けた面の下にも水流が生じる。この結果、曝気槽底部の撹拌を可能とし、曝気槽底部への汚泥の堆積を防ぐ効果を奏する。 According to the water treatment system of the present invention, the downflow space through which the downflow due to aeration passes is formed on the surface where the aerator is provided, so that the entire system can be aerated without increasing the size of the whole system. Water flow also occurs under the surface where the aerator is installed without reducing efficiency. As a result, it is possible to agitate the bottom of the aeration tank and prevent the deposition of sludge on the bottom of the aeration tank.
また、本発明の水処理システムの改良方法によれば、既設の全面曝気式曝気装置に対して、他の付設設備を設けることなく、かつ曝気効率を下げることなく、曝気装置を設けた面の下にも水流が生じるような曝気装置の配置が可能となる。この結果、曝気槽底部の撹拌を可能とし、曝気槽底部への汚泥の堆積を防ぐ効果を奏する。 In addition, according to the method for improving the water treatment system of the present invention, the surface on which the aeration device is installed can be improved without installing other attached equipment to the existing full surface aeration type aeration device and without lowering the aeration efficiency. It is possible to arrange the aerator so that the water flow also occurs below. As a result, it is possible to agitate the bottom of the aeration tank and prevent the deposition of sludge on the bottom of the aeration tank.
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曝気装置を有する排水処理装置等に利用するものである。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曝気槽に用いる曝気装置を備える水処理システムに利用される。 INDUSTRIAL APPLICABILITY The water treatment system of the present invention is used in a wastewater treatment apparatus or the like having an aerator for dispersing fine air bubbles in a liquid. Preferably, it is used in a water treatment system equipped with an aerator used in an aeration tank for biologically treating wastewater or the like with activated sludge.
本発明の水処理システムは、曝気槽の略全面に曝気装置を備える水処理システムであって、前記曝気装置は、曝気槽の幅方向の略全幅に曝気体を配した全幅曝気ユニットと、曝気槽の幅方向の一部に曝気体を配した部分曝気ユニットとを組み合わせてなることを特徴とする。 The water treatment system of the present invention is a water treatment system comprising an aeration device substantially over the entire surface of an aeration tank, the aeration device comprising: a full-width aeration unit in which aeration gas is distributed substantially across the width of the aeration tank; It is characterized in that it is combined with a partial aeration unit in which an aeration gas is distributed partially in the width direction of the tank.
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, embodiments of the present invention will be described in detail with reference to attached screens. It should be noted 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曝気槽2内に曝気装置1aが設置され、曝気装置1aは曝気槽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曝気体3からなる曝気ユニットAUを有し、これらの曝気ユニットAUにブロワーBから空気が供給されることにより、曝気ユニットAUから処理水W中に気泡を発生させて曝気を行う。
[First embodiment]
FIG. 1 is a schematic explanatory diagram showing the configuration of the water treatment system of the first embodiment of the present invention. (a) It is the 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 this invention. (c) It is a side view of the water treatment system of the 1st Embodiment of this invention. (Arrow view of II in FIG. 1b)
As shown in FIG. 1, in the water treatment system 10 of the present embodiment, an aeration device 1a is installed in an aeration tank 2 of a water treatment facility using activated sludge, for example. It is immersed in W (mixture of water to be treated and activated sludge) and has an aeration unit AU composed of a plurality of aeration gases 3 connected to a blower B, and air is supplied from the blower B to these aeration units AU. As a result, air bubbles are generated in the treated water W from the aeration unit AU for aeration.
曝気装置1aの曝気ユニットAUは、曝気槽2内で曝気槽2の幅方向(図1bの上下方向;以下、単に「幅方向」という)の略全幅に曝気体3を並設した全幅曝気ユニット4と、幅方向の部分的に曝気体3を配した部分曝気ユニット5aからなるものである。この全幅曝気ユニット4及び部分曝気ユニット5aは、曝気槽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、それぞれ複数並設置されている。 The aeration unit AU of the aeration device 1a is a full-width aeration unit in which the aeration gas 3 is arranged side by side in substantially the entire width of the aeration tank 2 in the width direction (the vertical direction in FIG. 1b; hereinafter simply referred to as the "width direction"). 4 and a partial aeration unit 5a in which the aeration gas 3 is partially distributed in the width direction. A plurality of full-width aeration units 4 and partial aeration units 5a are arranged in parallel along the length direction of the aeration tank 2 (horizontal direction in FIG. 1b; hereinafter simply referred to as "longitudinal direction").
(曝気槽)
曝気槽2は、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、外部には曝気装置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、曝気槽2内部には、曝気槽2の底部の略全面に曝気装置1aが設けられている。曝気槽2の深さ方向における曝気装置1aの位置は、特に制限されないが、通常、曝気槽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、曝気装置1aを比較的高い位置に設置してもよい。
(aeration tank)
The aeration tank 2 has an upper haunch Hu and a lower haunch Hs in a substantially rectangular parallelepiped tank, and is provided outside with a blower B for supplying oxygen-containing air to the aerator 1a. Inside the aeration tank 2, an aeration device 1a is provided on substantially the entire bottom of the aeration tank 2. As shown in FIG. The position of the aeration device 1a in the depth direction of the aeration tank 2 is not particularly limited, but it is usually installed near the bottom of the aeration tank 2. Considering the restriction of the discharge pressure of the blower B and the balance with the existing facilities, the aeration device 1a may be installed at a relatively high position.
(曝気ユニット)
曝気ユニットAUは、曝気槽2の幅方向に配設した複数の曝気体3と、曝気体3上で幅方向に延在し曝気体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7とを有している。また、ブロワーBからの空気は、送気管8を通じてヘッダ管7に供給されている。
(aeration unit)
The aeration unit AU includes a plurality of aeration gases 3 arranged in the width direction of the aeration tank 2, and a header which is an air supply pipe extending in the width direction above the aeration gas 3 and allowing airtight communication between the insides of the aeration gases 3. a tube 7; Also, the air from the blower B is supplied to the header pipe 7 through the air pipe 8 .
図1a及び図1bに示されるように、曝気ユニットAUは、曝気体3が幅方向の全幅に対して配置され、長さ方向の中心軸CLに対して線対称かつ等間隔に並設される全幅曝気ユニット4と、曝気体3が幅方向片側に偏在して並設される部分曝気ユニット5a、部分曝気ユニット5aと曝気体3の偏在方向を逆にした部分曝気ユニット5a’とがある。この全幅曝気ユニット4及び部分曝気ユニット5aを曝気槽2の長さ方向に沿って並設する。なお、第1の実施形態では、全幅曝気ユニットの配置は、中心軸CLに対して線対称かつ等間隔に並設しているが、全幅曝気ユニットの配置は、略全幅に配置されていればよい。例えば、中心軸CLに対して線対称でなくてもよく、また、等間隔に並設しなくてもよい。 As shown in FIGS. 1a and 1b, the aeration unit AU has the aeration gas 3 arranged over the entire width in the width direction, and arranged in parallel at equal intervals and line symmetrical with respect to the central axis CL in the length direction. There are a full-width aeration unit 4, a partial aeration unit 5a in which the aeration gas 3 is unevenly distributed on one side in the width direction, and a partial aeration unit 5a' in which the direction of uneven distribution of the aeration gas 3 is opposite to that of the partial aeration unit 5a. The full width aeration unit 4 and the partial aeration unit 5a are arranged side by side along the length direction of the aeration tank 2. As shown in FIG. In the first embodiment, the full-width aeration units are arranged in line symmetrically and at equal intervals with respect to the central axis CL. good. For example, they may not be line-symmetrical with respect to the central axis CL, and may not be arranged side by side at regular intervals.
この構成により、曝気装置1aの配置平面に、曝気が行われない下降流スペース6が形成される。図1cに示すように、曝気の際に、曝気による上昇流が水面まで到達し、下降流となって曝気装置1aまで戻って来た際に、この下降流スペース6を通じて、曝気装置1aの下側にも水流が生じ、曝気槽2の底部の撹拌が可能となる。 With this configuration, a downward flow space 6 in which no aeration is performed is formed in the plane of arrangement of the aeration device 1a. As shown in FIG. 1c, during aeration, when the upward flow due to aeration reaches the water surface and returns to the aeration device 1a as a downward flow, through this downward flow space 6, A water flow is also generated on the side of the aeration tank 2, making it possible to agitate the bottom of the aeration tank 2.
全幅曝気ユニット4及び部分曝気ユニット5aの数の比率は、特に制限されず、全幅曝気ユニット4及び部分曝気ユニット5aの数を同数としてもよいし、異数としてもよい。曝気量を確保するという観点から、部分曝気ユニット5aの数より全幅曝気ユニット4の数を多く設置することが好ましい。
また、全幅曝気ユニット4及び部分曝気ユニット5aの配置は、特に制限されず、交互に配列してもよいし、ランダムに配列してもよい。
The ratio of the numbers of the full-width aeration units 4 and the partial aeration units 5a is not particularly limited, and the numbers of the full-width aeration units 4 and the partial aeration units 5a may be the same or different. From the viewpoint of securing the amount of aeration, it is preferable to install more full-width aeration units 4 than partial aeration units 5a.
Further, the arrangement of the full-width aeration units 4 and the partial aeration units 5a is not particularly limited, and they may be arranged alternately or randomly.
部分曝気ユニットにおける曝気体の位置は、特に制限されず、例えば、曝気槽2の幅方向の片側に偏在してもよいし、幅方向中心側に偏在してもよいし、幅方向の両方の外側に偏在してもよい。 The position of the aerated gas in the partial aeration unit is not particularly limited. It may be unevenly distributed on the outside.
なお、第1の実施形態における部分曝気ユニット5a、5a’は、ヘッダ管7の長さが全幅曝気ユニット4よりも短くすることにより、下降流スペース6を形成する構成であるが、部分曝気ユニットは、全幅曝気ユニットの一部の曝気体3の散気孔を塞ぐことにより構成してもよい。 The partial aeration units 5a and 5a' in the first embodiment are configured to form the downward flow space 6 by making the length of the header pipe 7 shorter than that of the full width aeration unit 4, but the partial aeration unit may be configured by blocking the diffusion holes for a part of the aeration gas 3 of the full-width aeration unit.
また、本発明の本質は、曝気槽の略全面に配置した曝気装置の一部の領域において曝気を止め、下降流スペースを形成することである。全幅曝気ユニットおよび部分曝気ユニットが一体として構成されていてもよい。例えば、曝気槽の長さ方向に延伸した曝気体を用いて、所定の間隔で散気孔を塞ぐことにより下降流スペースを形成してもよい。 Further, the essence of the present invention is to stop the aeration in a partial region of the aeration device arranged over substantially the entire surface of the aeration tank to form a downward flow space. A full-width aeration unit and a partial aeration unit may be configured as one piece. For example, the downward flow space may be formed by closing the diffuser holes at predetermined intervals using the aeration gas extending in the length direction of the aeration tank.
曝気装置1aを平面視した際の下降流スペース6の位置は、特に制限されず、ランダムに配置されても、規則的に配置されてもよい。良好な下降流を形成するという観点から、下降流スペースは規則的に配置されることが好ましく、曝気槽2の幅方向の両側に規則的に配置されることがより好ましい。なお、「規則的」とは、曝気槽2の長さ方向に対して、繰り返し構造を有するものを意味する。 The position of the downward flow space 6 when the aeration device 1a is viewed from above is not particularly limited, and may be arranged randomly or regularly. From the viewpoint of forming a good downward flow, the downward flow spaces are preferably regularly arranged, and more preferably regularly arranged on both sides of the aeration tank 2 in the width direction. In addition, "regularly" means having a repeating structure in the length direction of the aeration tank 2 .
また、下降流スペース6の大きさは、特に制限されないが、曝気槽の幅方向の長さに対する下降流スペースの幅方向の長さが、好ましくは2/3以下であり、より好ましくは1/3以下である。なお、「下降流スペースの幅方向の長さ」とは、図1(b)の両方向矢印Pに示すように、曝気装置のない領域の幅方向の長さを示し、一つの部分曝気ユニットにおいて下降流スペースが複数ある場合(例えば図3の「部分曝気ユニット5b)には、その合計とする。また、曝気槽の長さ方向に下降流スペースが複数存在する場合には、上記「曝気槽の幅方向の長さに対する下降流スペースの幅方向の長さ」は、その平均値で表す。
また、曝気槽の長さ方向のおける曝気装置全体の長さに対する一又は複数の下降流スペースの長さの合計は、好ましくは1/3以下である。なお、この曝気槽の長さ方向における「下降流スペースの長さ」は、図1(b)の両方向矢印Qに示すように、曝気装置のない領域の長さを示す。
The size of the downflow space 6 is not particularly limited, but the length in the width direction of the downflow space with respect to the length in the width direction of the aeration tank is preferably 2/3 or less, and more preferably 1/3. 3 or less. In addition, the "length in the width direction of the downward flow space" indicates the length in the width direction of the area without an aeration device, as indicated by the double-headed arrow P in Fig. 1(b). When there are a plurality of descending spaces (for example, the "partial aeration unit 5b" in Fig. 3), the sum of them is used. The widthwise length of the downflow space with respect to the widthwise length of the " is represented by its average value.
Also, the total length of the downdraft space or spaces with respect to the length of the entire aeration device in the longitudinal direction of the aeration tank is preferably ⅓ or less. The "length of the downflow space" in the longitudinal direction of the aeration tank indicates the length of the region without the aerator, as indicated by the double-headed arrow Q in FIG. 1(b).
(曝気体)
本発明の曝気体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曝気管であり、「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。曝気体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曝気管であってもよい。また、曝気体3は、角型、丸型などの板状部材からなる曝気板であってもよい。
(Aeration gas)
The aeration gas 3 of the present invention is an aeration pipe made of a tubular member wrapped with a membrane having fine air diffusion holes through which air passes, and is also called a "membrane pipe type ultrafine bubble air diffusion pipe". The aeration gas 3 may be a diffuser tube made of porous synthetic resin or ceramic, or an aeration pipe made of a tubular member such as a flexible tube provided with a large number of slits. Also, the aeration gas 3 may be an aeration plate made of a plate-shaped member such as a rectangular or round shape.
〔第2の実施形態〕
図2は、本発明の第2の実施形態の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の実施形態の曝気装置1bでは、第1の実施形態の部分曝気ユニット5aに代えて、曝気体3が幅方向中心側に偏在して並設される部分曝気ユニット5bとしたものである。曝気装置1bは、全幅曝気ユニット4及び部分曝気ユニット5bを曝気槽2の長さ方向に対して交互に延在するように配置されている。
[Second embodiment]
FIG. 2 is a schematic explanatory diagram showing the water treatment system of the second embodiment of the present invention. FIG. 2(a) is a plan view of the water treatment system of the second embodiment of the present invention, and FIG. 2(b) is a side view of the water treatment system of the second embodiment of the present invention. (II-II arrow view in Fig. 2a)
In the aeration apparatus 1b of the second embodiment, instead of the partial aeration unit 5a of the first embodiment, a partial aeration unit 5b in which the aerated gas 3 is unevenly distributed on the center side in the width direction is provided. . The aeration device 1b is arranged so that the full width aeration unit 4 and the partial aeration unit 5b are alternately extended in the length direction of the aeration tank 2. As shown in FIG.
図2aに示されるように、全幅曝気ユニット4及び部分曝気ユニット5bにより形成される下降流スペース6が規則的に曝気装置1bの配置面に設けられることになる。この曝気装置1bによれば、曝気装置1bの配置面の下側に一定間隔で水流が発生することになり、定常的に曝気槽2底部の撹拌が可能となる。 As shown in FIG. 2a, downdraft spaces 6 formed by full-width aeration units 4 and partial aeration units 5b will be provided regularly in the plane of installation of the aerator 1b. According to this aeration device 1b, a water flow is generated at regular intervals under the installation surface of the aeration device 1b, and the bottom of the aeration tank 2 can be constantly agitated.
〔第3の実施形態〕
図3は、本発明の第3の実施形態の水処理システムを示す概略説明図である。図3(a)は、本発明の第3の実施形態の水処理システムの平面図であり、図3(b)は、本発明の第3の実施形態の水処理システムの側面図である。(図3a中のIII-III矢視図)
第3の実施形態の曝気装置1cでは、第2の実施形態の全幅曝気ユニット4及び部分曝気ユニット5bに加えて、曝気体3が幅方向曝気槽壁面の両側に偏在して並設される部分曝気ユニット5cを備えるものである。曝気装置1cは、全幅曝気ユニット4及び部分曝気ユニット5b、5cを曝気槽2の長さ方向に対して延在するように配置されている。なお、図3aでは、全幅曝気ユニット4、部分曝気ユニット5b、全幅曝気ユニット4、部分曝気ユニット5c、全幅曝気ユニット4となるように配置している。
[Third embodiment]
FIG. 3 is a schematic explanatory diagram showing a water treatment system according to a third embodiment of the invention. Fig.3 (a) is a top view of the water treatment system of 3rd Embodiment of this invention, FIG.3(b) is a side view of the water treatment system of 3rd Embodiment of this invention. (View from the arrow III-III in Fig. 3a)
In the aeration device 1c of the third embodiment, in addition to the full width aeration unit 4 and the partial aeration unit 5b of the second embodiment, the aeration gas 3 is unevenly distributed on both sides of the width direction aeration tank wall surface. It has an aeration unit 5c. The aeration device 1c is arranged so that the full-width aeration unit 4 and the partial aeration units 5b, 5c extend in the longitudinal direction of the aeration tank 2. As shown in FIG. 3a, the full width aeration unit 4, the partial aeration unit 5b, the full width aeration unit 4, the partial aeration unit 5c, and the full width aeration unit 4 are arranged.
図3aに示されるように、全幅曝気ユニット4及び部分曝気ユニット5b、5cにより形成される下降流スペース6が曝気槽2の長さ方向中心軸CL側と曝気槽2の壁面の両側に設けられることになる。この曝気装置1cによれば、曝気槽2の長さ方向中心軸CL側からの下降流及び壁面側からの下降流が曝気装置1cの下側に誘導され、曝気槽2底部の撹拌を可能とする。 As shown in FIG. 3a, downdraft space 6 formed by full-width aeration unit 4 and partial aeration units 5b, 5c is provided on both sides of the longitudinal central axis CL side of aeration tank 2 and the wall surface of aeration tank 2. It will be. According to this aeration device 1c, the downward flow from the longitudinal center axis CL side of the aeration tank 2 and the downward flow from the wall surface side are guided to the lower side of the aeration device 1c, making it possible to agitate the bottom of the aeration tank 2. do.
[水処理システムの改良方法]
本発明の水処理システムの改良方法は、曝気槽の略全面に曝気装置を備える既設の水処理システムにおいて、曝気槽の幅方向の略全面に曝気体を配した既設の全幅曝気ユニットのうちの一部を、曝気槽の幅方向の一部に曝気体を配した部分曝気ユニットとなるようにして、曝気装置の配置面において曝気による下降流が通過する下降流スペースが形成されるようにすればよい。
具体的には、曝気体が幅方向に均等配置された既設の曝気装置において、上記下降流スペースが形成されるように、曝気体の一部を取り外したり、一部の曝気を停止したりするようにすればよい。
この水処理システムの改良方法により、全面曝気式の曝気装置を備えた既設の水処理システムにおいて、新たな付設装置を設けることなく、かつ既設の曝気装置の全てを交換する必要がなく、曝気槽底部の十分な撹拌が可能な曝気装置を備えた水処理システムとすることができる。
[Method for improving water treatment system]
The method for improving a water treatment system of the present invention is an existing water treatment system in which an aeration device is provided over substantially the entire surface of an aeration tank. A portion of the aeration tank is configured to be a partial aeration unit in which the aeration gas is arranged in a portion of the aeration tank in the width direction, so that a downward flow space through which the downward flow due to aeration passes is formed on the arrangement surface of the aeration device. Just do it.
Specifically, in an existing aeration device in which the aerated gas is evenly distributed in the width direction, part of the aerated gas is removed or a part of the aeration is stopped so that the downward flow space is formed. You should do it like this.
According to this water treatment system improvement method, in an existing water treatment system equipped with a full aeration type aeration device, there is no need to install a new attached device and replace all of the existing aeration device, and the aeration tank It can be a water treatment system with an aerator capable of sufficient agitation at the bottom.
<曝気装置の底部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底部流速シミュレーションを行った。曝気ユニットAUの配置は、上記第2の実施形態に倣い、曝気ユニットAUを構成する曝気体3を10本としてシミュレーションを行った。その結果を図4aに示す。
なお、図4bは、曝気体を均等配置した従来の全面曝気式の曝気装置における底部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4a及び図4bの曝気体の数は同一としている。
<Simulation of flow velocity at the bottom of the aerator>
A bottom flow velocity simulation was performed for the water treatment system of the present invention. The arrangement of the aeration unit AU followed the second embodiment, and the simulation was performed with ten aeration gases 3 constituting the aeration unit AU. The results are shown in FIG. 4a.
In addition, FIG. 4b shows the results of a bottom flow velocity simulation in a conventional full-surface aeration type aeration apparatus in which the aerated gas is evenly distributed. In this simulation, the number of aeration gases in Figures 4a and 4b 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 result shown in FIG. 4 is the result of execution for an aeration tank width of 5.5 m, tank length of 8.6 m, tank water depth of 5.0 m, and aeration equipment installed water depth of 4.0 m, but it is only an example. It does not limit the shape of the tank, the depth of water in which the aerator is installed, the layout of the aerator, or the like.
図4aから、本発明の水処理システムでは、曝気槽2底部において、曝気槽2の壁面側にある下降流スペース6の下側から曝気槽2の長さ方向中心軸CLに向かって一定方向の流れが形成されていることがわかる。一方、図4bから、従来の曝気装置においては曝気槽2底部の流れは一定の方向にはなっていないことがわかる。 From FIG. 4a, in the water treatment system of the present invention, at the bottom of the aeration tank 2, from the lower side of the downward flow space 6 on the wall side of the aeration tank 2 toward the longitudinal central axis CL of the aeration tank 2, It can be seen that a flow is formed. On the other hand, from FIG. 4b, it can be seen that the flow at the bottom of the aeration tank 2 does not have a constant direction in the conventional aerator.
図5には、本発明の第2の実施形態の水処理システムと、全面曝気式の曝気装置を備えた従来の水処理システムにおける底部平均流速の比較したグラフを示した。
底部流速の平均値を比較すると、本発明の曝気装置における底部平均流速は、従来の全面曝気式の曝気装置における底部平均流速よりも2.2倍速くなった。
FIG. 5 shows a graph comparing bottom average flow velocities in the water treatment system of the second embodiment of the present invention and in a conventional water treatment system provided with a full aeration type aerator.
Comparing the average bottom flow velocities, the bottom average flow velocity in the aerator of the present invention was 2.2 times higher than that in the conventional full aeration type aerator.
図4、5の結果から、複数の曝気体からなる曝気ユニットを備える全面曝気式の曝気装置において、曝気による下降流が通過する下降流スペースを設けることにより、曝気槽の底部に十分な速さの一定方向の流れが生じ、曝気槽内の効果的な撹拌が可能となる。 From the results of Figures 4 and 5, in a full-surface aeration type aeration device equipped with an aeration unit consisting of a plurality of aeration gases, by providing a downflow space through which the downflow due to aeration passes, sufficient speed can be achieved at the bottom of the aeration tank. A unidirectional flow of water is generated, enabling effective agitation in the aeration tank.
本発明の水処理システムは、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。 INDUSTRIAL APPLICABILITY The water treatment system of the present invention can be used in aerobic microbial treatment tanks for organic sludge in sewage treatment plants and organic wastewater in food factories, pharmaceutical factories and the like, and methods for treating the same.
本発明の水処理システムの改良方法は、既設の曝気装置を利用して本発明の水処理システムを導入することができる方法を提供することができる。 The method for improving the water treatment system of the present invention can provide a method for introducing the water treatment system of the present invention using an existing aerator.
1a、1b、1c 曝気装置、2 曝気槽、3 曝気体、4 全幅曝気ユニット、5a、5a’、5b、5c 部分曝気ユニット、6 下降流スペース、7 ヘッダ管、8 送気管、10 水処理システム、AU 曝気ユニット、Hu 上部ハンチ、Hs 下部ハンチ、B ブロワー、W 処理水 1a, 1b, 1c aerator, 2 aeration tank, 3 aeration gas, 4 full width aeration unit, 5a, 5a', 5b, 5c partial aeration unit, 6 downflow space, 7 header pipe, 8 air pipe, 10 water treatment system , AU aeration unit, Hu upper haunch, Hs lower haunch, B blower, W treated water
Claims (2)
前記部分曝気ユニットは、曝気槽の幅方向曝気槽壁面の両側に偏在して並設される曝気体からなることを特徴とする、水処理システムの改良方法。 A method for improving an existing water treatment system having an aeration device substantially over the entire surface of the aeration tank, wherein the aeration is performed by removing the aeration gas from a full-width aeration unit in which the aeration gas is arranged substantially across the width of the aeration tank. A partial aeration unit in which the aeration gas is arranged partially in the width direction of the tank ,
A method for improving a water treatment system, wherein the partial aeration unit comprises an aeration gas arranged unevenly on both sides of the aeration tank wall surface in the width direction of the aeration tank .
前記部分曝気ユニットは、幅方向曝気槽壁面の両側に偏在して並設される曝気体からなることを特徴とする、水処理システムの改良方法。 A method for improving an existing water treatment system having an aeration device substantially over the entire surface of the aeration tank, wherein in a full-width aeration unit in which the aeration gas is arranged substantially in the width direction of the aeration tank, air is supplied to a part of the aeration gas. By stopping the
A method for improving a water treatment system, wherein the partial aeration unit comprises aeration gas unevenly distributed on both sides of the wall surface of the aeration tank in the width direction .
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| JPH0418720Y2 (en) * | 1986-08-05 | 1992-04-27 | ||
| JP2604745Y2 (en) * | 1993-08-16 | 2000-06-05 | 栗田工業株式会社 | Activated sludge treatment equipment |
| JP3171555B2 (en) * | 1996-04-12 | 2001-05-28 | 日本碍子株式会社 | Deep tank aeration device |
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| US5013493A (en) | 1990-01-22 | 1991-05-07 | Environmental Dynamics, Inc. | Staggered diffuser arrangement for waste water treatment systems |
| JP2001504754A (en) | 1996-11-12 | 2001-04-10 | アクアテック―マクソン ピーティーワイ.リミティッド | A diffuser that aerates fluid |
| JP2004041928A (en) | 2002-07-11 | 2004-02-12 | Sumitomo Heavy Ind Ltd | Diffusion method and diffusion system |
| JP2005262090A (en) | 2004-03-18 | 2005-09-29 | Kurita Water Ind Ltd | Aeration tank |
| JP2006198478A (en) | 2005-01-18 | 2006-08-03 | Kurimoto Ltd | Aerator and method for operating aeration tank |
| JP2006263585A (en) | 2005-03-24 | 2006-10-05 | Ngk Insulators Ltd | Method for preventing clogging of air diffuser and method for operating air diffuser using this method |
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