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JP2006198478A - Aerator and method for operating aeration tank - Google Patents

Aerator and method for operating aeration tank Download PDF

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JP2006198478A
JP2006198478A JP2005010564A JP2005010564A JP2006198478A JP 2006198478 A JP2006198478 A JP 2006198478A JP 2005010564 A JP2005010564 A JP 2005010564A JP 2005010564 A JP2005010564 A JP 2005010564A JP 2006198478 A JP2006198478 A JP 2006198478A
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air
aeration
diffuser
tank
pipe
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Ryota Omatsu
良太 尾松
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Kurimoto 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

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  • Treatment Of Sludge (AREA)
  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To diffuse sludge sediment on the bottom part of a tank by cheap means in an overall aeration method. <P>SOLUTION: An air diffuser 10 in the aeration tank 1 is divided into one diffusion part 10b and another diffusion part 10a, and a flexible pipe joint 17 having an on-off valve function is provided through a lateral pipe 11 on the border of both the diffusion parts. Normally, as shown by a solid line, both the diffusing parts 10a and 10b are made into a horizontal state, air is supplied to all diffusion parts to be diffused over the whole area of the tank 1, and the overall aeration is carried out. When the sludge is settled on the bottom part of the tank, one diffusion part 10b is elected as shown by a chain line, air distribution to the diffusion part 10b is cut off by the on-off valve function of the flexible pipe joint 17 due to the election. Thus, air is introduced only into another diffusion part 10a, swirling flow is generated to agitate the sludge settled on the bottom part of the aeration tank. If there is no sludge sediment on the bottom part of the aeration tank 1 (diffuse), one diffusion part 10b is laid down and returned to a horizontal state to transfer to the overall aeration. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、下水処理場における曝気槽、活性汚泥法用曝気槽、家畜糞尿貯留槽用曝気槽等において、その曝気を全面曝気とするとともに、その槽底部に堆積した汚泥を攪拌して円滑に槽全体に拡散するようにした曝気装置及びその曝気槽の運転方法に関するものである。   In the aeration tank in the sewage treatment plant, the aeration tank for the activated sludge method, the aeration tank for the livestock manure storage tank, etc., the aeration is made to be the entire aeration, and the sludge accumulated at the bottom of the tank is stirred smoothly. The present invention relates to an aeration apparatus that diffuses throughout the tank and a method for operating the aeration tank.

下水処理場における曝気槽は、その槽内に散気装置を設けて、その散気装置の散気管から散気し、槽内の好気性微生物を利用して曝気処理するものが一般的である。
この好気性処理を行う曝気槽における曝気方法として、旋回流式、全面曝気式、水中攪拌式等の種々のものが採用されているが、普及度では、旋回流式と全面曝気式の2つが主流となっている。
An aeration tank in a sewage treatment plant is generally provided with an air diffuser in the tank, diffused from the air diffuser of the air diffuser, and aerated using an aerobic microorganism in the tank. .
As an aeration method in the aeration tank for performing the aerobic treatment, various methods such as a swirling flow method, a full aeration method, and an underwater agitation method are adopted. It has become mainstream.

上記旋回流式の曝気方法は、曝気槽内の一側に散気装置を設け、その散気装置の散気管から散気して、その散気による上昇流により、槽内に旋回流を生じさせ、旋回流によって、槽内全域を攪拌するとともに曝気するものである(特許文献1参照)。
全面曝気式の曝気方法は、曝気槽内底部に散気装置を設置し、その散気装置の散気管から槽内全面に散気して曝気するものである(特許文献1、2参照)。
特開平9−276891号公報 特開平9−174066号公報
The above-described swirling flow type aeration method is provided with a diffuser on one side of the aeration tank, diffuses from the diffuser pipe of the diffuser, and creates a swirling flow in the tank by the upward flow caused by the diffused air. The entire area in the tank is stirred and aerated by the swirling flow (see Patent Document 1).
In the aeration method of the entire surface aeration method, an aeration device is installed at the bottom of the aeration tank, and the entire surface of the tank is diffused and aerated from the aeration pipe of the aeration device (see Patent Documents 1 and 2).
Japanese Patent Laid-Open No. 9-276891 JP-A-9-174066

また、曝気槽には、下水処理場の曝気槽に比べて高濃度の屎尿を投入して活性汚泥法によってその屎尿を処理するものもある。この曝気槽にも、上記旋回流式、全面曝気式、水中攪拌式等の種々のものが採用されているが、同様に、普及度では、旋回流式と全面曝気式の2つが主流となっている。   In addition, some aeration tanks have a higher concentration of manure compared to an aeration tank in a sewage treatment plant and treat the manure by an activated sludge method. In this aeration tank, various types such as the swirling flow method, the entire surface aeration method, and the underwater agitation method are adopted, but similarly, the swirling flow method and the entire surface aeration method become mainstream in the degree of spread. ing.

さらに、乳牛尿などの家畜糞尿は貯留することによって大腸菌群数が減少し、さらに曝気することにより、硫化水素臭が減少してアンモニア臭のみとなる。この曝気槽にも、同様に、上記旋回流式、全面曝気式、水中攪拌式等の種々のものが採用されている。   Furthermore, by storing livestock manure such as dairy cow urine, the number of coliforms decreases, and further aeration reduces the hydrogen sulfide odor and only the ammonia odor. Similarly, various types of aeration tanks such as the swirling flow type, the entire aeration type, and the underwater agitation type are employed.

全面曝気式は、槽全域に円滑に散気されるため、曝気効率(処理効率)が高い利点はあるが、槽底部に汚泥(SS等の沈降物)が沈降して堆積する。この汚泥の堆積は、腐敗して悪臭(硫化水素)が発生するため、浚渫や引き抜きが必要である。しかし、それらの作業を軽減するため、従来から、その堆積した汚泥を攪拌して槽内に拡散させている。従来では、その拡散を攪拌翼などによる機械的手段によって行なっている。
旋回流式は、旋回流によって槽底部の汚泥も攪拌するため、上記全面曝気式における汚泥堆積の問題は少ない。しかし、全面曝気式に比べて、曝気効率が劣る。
The whole surface aeration type has an advantage of high aeration efficiency (treatment efficiency) because it is smoothly diffused throughout the tank, but sludge (sediment such as SS) settles and accumulates at the bottom of the tank. This sludge accumulation needs to be dredged and pulled out because it rots and produces a bad odor (hydrogen sulfide). However, in order to reduce such work, conventionally, the accumulated sludge is stirred and diffused in the tank. Conventionally, the diffusion is performed by mechanical means such as a stirring blade.
In the swirling flow method, the sludge at the bottom of the tank is also agitated by the swirling flow. However, the aeration efficiency is inferior compared to the full aeration type.

このため、全面曝気式と旋回流式を選択的に切り換え、その旋回流によって槽底部の堆積汚泥を拡散するようにした技術がある(特許文献1 段落0012、図3、段落0013 図4参照)。
しかし、この技術は、複数の散気装置を設けて、その各散気装置の個々に制御装置を付設し、その制御装置によって、各散気装置を個々に制御して散気するようにしている。このため、曝気装置としては高価なものとなっている。
For this reason, there is a technique that selectively switches between the whole surface aeration type and the swirling flow type, and diffuses the sludge accumulated at the bottom of the tank by the swirling flow (see Patent Document 1, paragraph 0012, FIG. 3, paragraph 0013, FIG. 4). .
However, in this technique, a plurality of air diffusers are provided, and a control device is attached to each of the air diffusers, and each air diffuser is controlled individually by the control device to diffuse air. Yes. For this reason, it is expensive as an aeration apparatus.

また、槽底部に散気装置を設け、その散気装置の全散気管から散気することにより全面曝気するとともに、その一部の散気管から散気して旋回流を生じさせて、添加物の滞留を防止した技術もある(特許文献2 段落0009〜0010)。   In addition, an air diffuser is provided at the bottom of the tank, and the entire surface is aerated by aeration from the entire air diffuser of the air diffuser. There is also a technique that prevents the stagnation (Patent Document 2, paragraphs 0009 to 0010).

この発明は、全面曝気式において、槽底部の汚泥堆積を安価な手段によって拡散(攪拌)させることを課題とする。   This invention makes it a subject to diffuse (stir) the sludge deposit of a tank bottom part by an inexpensive means in a whole surface aeration type.

上記の課題を達成するために、この発明は、上記特許文献2の旋回流による攪拌作用を採用して、全面曝気を行う散気管の一部から散気することにより、旋回流を生じさせて槽底部の堆積汚泥を拡散するようにしたのである。
このように、全面曝気を行う散気管の一部からの散気によって旋回流を生じさせて攪拌すれば、特許文献1記載技術のように、全面曝気用の散気装置とは別に、旋回流を生じさせるための散気装置を設ける場合に比べて安価となる。
In order to achieve the above-mentioned problem, the present invention adopts the stirring action by the swirling flow of the above-mentioned Patent Document 2 and generates a swirling flow by diffusing from a part of the diffusing tube that performs aeration on the entire surface. The sediment sludge at the bottom of the tank was diffused.
In this way, if the swirl flow is generated by aeration from a part of the diffuser tube that performs aeration of the entire surface, the swirl flow is separated from the aeration device for the entire surface aeration as in the technique described in Patent Document 1. Compared to the case where an air diffuser is provided to cause the problem, the cost is low.

つぎに、この発明は、弁の切換によって、全面曝気と旋回流の生成を切換えるように、例えば、散気用空気供給管からそれぞれ分岐したライザー管によって全面曝気時の空気供給と旋回流時の空気供給を行い、その切り換えを前記空気供給管と両分岐ライザー管の間に設けた弁により行なうこととしたのである。
このように、一の空気供給管によって全面曝気時の空気供給と旋回流時の空気供給を行い、かつ、その切り換えを弁で行うようにすれば、構造も簡単であり、安価なものとし得る。
Next, according to the present invention, for example, a riser pipe branched from the air supply pipe for aeration is used to switch between the generation of the entire aeration and the swirling flow by switching the valve. The air supply is performed, and the switching is performed by a valve provided between the air supply pipe and both branch riser pipes.
In this way, if the air supply during the entire aeration and the air supply during the swirling flow are performed by one air supply pipe and the switching is performed by a valve, the structure can be simplified and the cost can be reduced. .

この発明は、以上のようにしたので、安価にして、槽底部の汚泥の堆積をなくしつつ、全面曝気によって効率の高い曝気を行うことができる。   Since the present invention is configured as described above, it is possible to perform aeration with high efficiency by aeration over the entire surface while reducing the cost and eliminating the accumulation of sludge at the bottom of the tank.

上記課題を達成するこの発明に係る曝気槽の運転方法は、下水処理場における曝気槽、活性汚泥法用曝気槽、家畜糞尿貯留槽用曝気槽等に採用でき、その実施形態としては、曝気槽内の散気装置からの散気によって曝気する方法において、通常は、前記散気装置の全ての散気管に空気を送り込むことによって全面曝気を行い、曝気槽底部に汚泥が堆積した場合には、散気装置の一部の散気管のみに空気を送り込むことにより、旋回流を生じさせて曝気槽底部に堆積した汚泥を攪拌する構成を採用できる。   The operation method of the aeration tank according to the present invention that achieves the above object can be employed in an aeration tank in an sewage treatment plant, an aeration tank for an activated sludge method, an aeration tank for livestock manure storage tanks, etc. In the method of aeration by aeration from the inside of the aeration device, normally, the entire aeration is performed by sending air to all the aeration tubes of the aeration device, and when sludge is accumulated at the bottom of the aeration tank, It is possible to adopt a configuration in which the sludge accumulated in the bottom of the aeration tank is agitated by sending air to only a part of the air diffuser of the air diffuser.

このとき、上記散気装置の一部の散気管と他の散気管の間に上下方向の仕切り壁を設けたものとすれば、その仕切り壁によって槽内を上昇流域と下降流域とに分けることができて上記旋回流が生じ易くなるため、上記攪拌作用も円滑となる。
また、上記他の散気管はその一側でもって起伏自在として、上記旋回流を生じさせる際には、その他の散気管を起立させるようにすれば、その他の散気管が上記仕切り壁の役目を果たすと共に、旋回流の邪魔とならず、円滑に旋回流が生じる。
At this time, if a vertical partition wall is provided between some of the diffuser pipes and the other diffuser pipes, the inside of the tank is divided into an upflow area and a downflow area by the partition walls. Since the swirl flow is easily generated, the stirring action is also smoothed.
In addition, the other air diffuser can be raised and lowered on one side thereof, and when the swirl flow is generated, if the other air diffuser is raised, the other air diffuser can serve as the partition wall. At the same time, the swirl flow is smoothly generated without disturbing the swirl flow.

上記課題を達成する曝気槽に関するこの発明の実施形態としては、曝気槽内に散気装置を設け、その散気装置の全部の散気管又は一部の散気管のみに空気を選択的に供給可能とし、通常は、前記散気装置の全ての散気管に空気を送り込むことによって全面曝気を行い、前記曝気槽底部に汚泥が堆積した場合には、前記散気装置の一部の散気管のみに空気を送り込むことにより、旋回流を生じさせて前記曝気槽底部に堆積した汚泥を攪拌する構成を採用することができる。   As an embodiment of the present invention relating to an aeration tank that achieves the above-mentioned problems, an air diffuser is provided in the aeration tank, and air can be selectively supplied to all or only some of the air diffusers of the air diffuser. Ordinarily, the entire surface is aerated by sending air to all the diffuser pipes of the diffuser, and if sludge accumulates at the bottom of the aeration tank, only a part of the diffuser pipes of the diffuser It is possible to employ a configuration in which the sludge accumulated in the bottom of the aeration tank is stirred by generating a swirling flow by feeding air.

この構成における散気装置への空気供給構造としては、上記一部の散気管と他の散気管に、空気供給管からそれぞれ分岐したライザー管を設けてそのライザー管によって両散気管にそれぞれ空気を供給可能とするとともに、前記空気供給管と両分岐ライザー管の間に設けた弁によって両散気管又は一部の散気管のみに選択的に空気を供給可能とする構成を採用できる。   As an air supply structure to the diffuser in this configuration, a riser pipe branched from the air supply pipe is provided in the above-mentioned part of the diffuser pipes and other diffuser pipes, and air is supplied to both diffuser pipes by the riser pipes. It is possible to employ a configuration in which air can be supplied and air can be selectively supplied only to both the diffuser pipes or only a part of the diffuser pipes by a valve provided between the air supply pipe and both branch riser pipes.

これらの構成において、上記他の散気管をその一側でもって起伏自在にして、上記旋回流の形成時には、その他の散気管を起立させるようにすれば、旋回流を生じさせた場合に、その他の散気管は起立しているため、その旋回流の邪魔にならず、その流れが円滑になされるとともに、その起立した他の散気管は上記仕切り壁の作用も少なからず行う。   In these configurations, the other air diffuser can be raised and lowered on one side thereof, and when the swirl flow is formed, the other air diffuser can be erected. Since the diffusing pipe is standing, it does not interfere with the swirling flow, and the flow is made smooth, and the other diffusing pipe that stands up performs the action of the partition wall.

この他の散気管を起伏自在とした構成において、上記一部の散気管と他の散気管に、空気供給管からそれぞれ分岐したライザー管を設けてそのライザー管によって両散気管にそれぞれ空気を供給可能とするとともに、他の散気管に至るライザー管に自在管継手を介設してその他の散気管を起伏自在とし、前記自在管継手は開閉弁機能を有したものとすることができる。
また、上記空気供給管からのライザー管、ラテラル管によって一部の散気管から他の散気管に連続して空気を供給可能とし、その両散気管の境のラテラル管に自在管継手を介設し、その自在管継手は開閉弁機能を有したものとすることもできる。
これらの構成とすれば、上記旋回流を生じさせる際、上記他の散気管を前記自在管継手を介して起立させると、その開閉弁機能によって他の散気管への空気供給を遮断するようにすることができる。
In this configuration where the other diffusing pipes can be raised and lowered, the above-mentioned part of the diffusing pipes and other diffusing pipes are provided with riser pipes branched from the air supply pipes, and air is supplied to both of the diffusing pipes by the riser pipes In addition, a universal pipe joint is interposed in a riser pipe that reaches another diffuser pipe so that the other diffuser pipe can be raised and lowered, and the universal pipe joint can have an on-off valve function.
In addition, it is possible to supply air continuously from some diffuser pipes to other diffuser pipes by the riser pipes and lateral pipes from the above air supply pipes, and a universal pipe joint is provided in the lateral pipes at the boundary between both diffuser pipes. In addition, the universal pipe joint may have an on-off valve function.
With these configurations, when the above-mentioned swirling flow is generated, when the other air diffuser is raised via the universal pipe joint, the air supply to the other air diffuser is cut off by the opening / closing valve function. can do.

上記他の散気管を起伏させる手段としては、その散気管から上記曝気槽の上面に導いたワイヤーによって行う、その散気管の他側にエアバックを設け、そのエアバックに空気を供給することにより膨張させて、そのエアバックの浮力により行う等を採用できる。このとき、他の散気管の他側に倒伏状態への復帰用重りを設けて、全面曝気時の態様に円滑に復帰できるようにすることができる。   As means for raising and lowering the other diffuser pipe, an air bag is provided on the other side of the diffuser pipe by a wire led from the diffuser pipe to the upper surface of the aeration tank, and air is supplied to the airbag. For example, it is possible to employ inflating and performing the buoyancy of the airbag. At this time, it is possible to provide a weight for returning to the fallen state on the other side of the other air diffusing tubes so that the entire surface can be smoothly returned to the state during aeration.

これらの曝気槽は、上記運転方法によって円滑な曝気を行うことができ、同様に、上記散気装置の一部の散気管と他の散気管の間に上下方向の仕切り壁を設けて、攪拌作用を円滑にすることができる。   These aeration tanks can perform smooth aeration by the above operation method, and similarly, a partition wall in the vertical direction is provided between a part of the air diffuser and another air diffuser, and stirring is performed. The action can be made smooth.

一実施例を図1及び図2に示し、この実施例は、平面視長方状の曝気槽1の底面長さ方向に沿って散気装置10を水平状態に設けている。各散気装置10は、略中央において2つの散気部10a、10bに分割されており、各散気部は、ラテラル管11の両側に超微細気泡型の散気管12を設けた同一面上となったものであり、それぞれサポート用架台13で槽1の底に50cm程度の間隙をもって支持されている。   One embodiment is shown in FIGS. 1 and 2, and in this embodiment, the diffuser 10 is provided in a horizontal state along the bottom surface length direction of the aeration tank 1 having a rectangular shape in plan view. Each air diffuser 10 is divided into two air diffusers 10a and 10b at substantially the center, and each air diffuser is on the same surface provided with the ultrafine bubble diffuser 12 on both sides of the lateral tube 11. Each of them is supported on the bottom of the tank 1 by a support base 13 with a gap of about 50 cm.

各散気部10a、10bのラテラル管11には一の空気供給管14から分岐させたライザー管15が接続されており、このライザー管15を介して各ラテラル管11に空気供給管14から空気が供給されて、各散気管12から超微細気泡が吐出して槽1の全域に散気され、その散気によって槽1内が曝気される。
各ライザー管15には開閉弁16がそれぞれ介設されており、この開閉弁16の開閉によって、各散気部10a、10bに選択的に空気が供給される。
A riser pipe 15 branched from one air supply pipe 14 is connected to the lateral pipe 11 of each of the air diffusers 10a and 10b, and air is supplied from the air supply pipe 14 to each lateral pipe 11 via the riser pipe 15. Is supplied, and ultrafine bubbles are discharged from each diffuser tube 12 and diffused over the entire area of the tank 1, and the inside of the tank 1 is aerated by the diffused air.
Each riser pipe 15 is provided with an open / close valve 16, and air is selectively supplied to the air diffusers 10 a and 10 b by opening and closing the open / close valve 16.

この実施例は以上の構成であり、通常、各開閉弁16を開放して全ての散気部10a、10b(全ての散気装置10)に空気を供給して槽1内全域に散気して全面曝気を行う。
槽1底部に汚泥が堆積した場合には、各散気装置10の一方の散気部(散気管)10a又は10bに接続のライザー管15の開閉弁16を閉じ、他の散気部10b又は10aの散気管12のみに空気を送り込むことにより、旋回流を生じさせて曝気槽1底部に堆積した汚泥を攪拌する。
This embodiment has the above-described configuration. Normally, each on-off valve 16 is opened and air is supplied to all the air diffusers 10a and 10b (all air diffusers 10) to diffuse the entire area in the tank 1. Aeration.
When sludge is accumulated at the bottom of the tank 1, the open / close valve 16 of the riser pipe 15 connected to one of the air diffusers (air diffuser pipes) 10a or 10b of each air diffuser 10 is closed, and the other air diffuser 10b or By sending air only to the diffuser pipe 12 of 10a, the sludge accumulated in the bottom part of the aeration tank 1 by a swirling flow is stirred.

この旋回流による汚泥攪拌は、目視により、汚泥の堆積を確認した都度、開閉弁16を操作して行ったり、一定時間毎に開閉弁16を自動操作して行う。その一定時間は実験・実操業に基づき適宜に設定する。また、汚泥堆積量をセンサーで検出し、その検出信号に基づきその操作をすることもできる。旋回流の操作時間も、実験・実操業に基づく堆積量に応じて適宜に設定する。   The sludge agitation by the swirl flow is performed by operating the on-off valve 16 or automatically operating the on-off valve 16 every predetermined time each time the sludge accumulation is visually confirmed. The fixed time is set appropriately based on experiments and actual operations. Moreover, the amount of sludge accumulation can be detected by a sensor, and the operation can be performed based on the detection signal. The operation time of the swirling flow is also set appropriately according to the amount of accumulation based on the experiment and actual operation.

図3、図4に示す実施例は、各散気装置10の一方の散気部10b(「請求の範囲」で言う「他の散気管」)をその一側でもって起伏自在にしたものであり、上記空気供給管14からの一本のライザー管15、ラテラル管11によって他方の散気部10a(「請求の範囲」で言う「一部の散気管」)から一方の散気部10bに連続して空気を供給可能としている。
その両散気部10a、10bの境のラテラル管11にスイベル継手等の自在管継手17を介設し、その自在管継手17は開閉弁機能を有したものとする。
In the embodiment shown in FIG. 3 and FIG. 4, one air diffuser 10 b of each air diffuser 10 (“other air diffuser” referred to in “Claims”) can be raised and lowered on one side. There is a single riser pipe 15 and lateral pipe 11 from the air supply pipe 14 to the other air diffuser 10a ("part of air diffuser" in the "claims") to one air diffuser 10b. Air can be supplied continuously.
It is assumed that a universal pipe joint 17 such as a swivel joint is interposed in the lateral pipe 11 at the boundary between the diffusers 10a and 10b, and the universal pipe joint 17 has an on-off valve function.

図3の実施例は、一方の散気部10bの一側縁にはワイヤー18及び重り19が設けられ、ワイヤー18は曝気槽1の上面に導かれており、このワイヤー18を引くことにより、図示鎖線のように、一方の散気部10bが起立する。
ワイヤー18を緩めれば、重り19及び自重によって一方の散気部10bは倒伏して水平状態(実線状態)に復帰する。
In the embodiment of FIG. 3, a wire 18 and a weight 19 are provided on one side edge of one air diffuser 10 b, and the wire 18 is led to the upper surface of the aeration tank 1, and by pulling the wire 18, As shown by the chain line in the figure, one air diffuser 10b stands up.
If the wire 18 is loosened, the one air diffuser 10b falls down due to the weight 19 and its own weight and returns to the horizontal state (solid line state).

図4の実施例は、一方の散気部10bの他側にエアバック20を設け、そのエアバック20に空気供給用ホース21を接続しており、そのホース21に介在した弁22を適宜に開閉することにより、ホース21を介してエアバック20に空気を供給して膨張させると、図示鎖線のように、そのエアバック20の浮力により、一方の散気部10bが起立する。
一方、弁22の適宜な開閉により、ホース21を介してエアバック20内の空気を抜けば、重り19及び自重によって一方の散気部10bは倒伏して水平状態(実線状態)に復帰する。
In the embodiment of FIG. 4, an air bag 20 is provided on the other side of one air diffuser 10 b, an air supply hose 21 is connected to the air bag 20, and a valve 22 interposed in the hose 21 is appropriately set. When air is supplied to the airbag 20 via the hose 21 and expanded by opening and closing, the one air diffuser 10b stands up due to the buoyancy of the airbag 20 as shown by the chain line in the figure.
On the other hand, if the air in the airbag 20 is removed through the hose 21 by appropriately opening and closing the valve 22, the one air diffuser 10b falls down due to the weight 19 and its own weight and returns to the horizontal state (solid line state).

この両実施例も、通常は、各図実線のごとく、各散気装置10の両散気部10a、10bを水平状態にして全ての散気部10a、10b(全ての散気装置10)に空気を供給して槽1内全域に散気して全面曝気を行う。
槽1底部に汚泥が堆積した場合には、一方の散気部10bを鎖線のごとく起立させ、その起立による自在管継手17の開閉弁機能によってその散気部10bへの空気流通を遮断する。これにより、他方の散気部10aにのみに空気が送り込まれることとなって、旋回流が生じて曝気槽1底部に堆積した汚泥を攪拌する。
この空気供給は、散気部10bの起立作用時も継続していてもよいが、空気供給を一時停止し、散気部10bの起立後に空気供給をすることもできる。
In both of these embodiments, normally, as shown in the solid lines in the figure, all the air diffusers 10a and 10b (all air diffusers 10) are placed with the air diffusers 10a and 10b of each air diffuser 10 in a horizontal state. Air is supplied and diffused over the entire area of the tank 1 to perform aeration on the entire surface.
When sludge is accumulated at the bottom of the tank 1, one air diffuser 10b is erected as shown by a chain line, and the air flow to the air diffuser 10b is blocked by the open / close valve function of the universal pipe joint 17 by the erection. Thereby, air will be sent only into the other aeration part 10a, and a swirl flow will arise and the sludge accumulated in the bottom part of the aeration tank 1 will be stirred.
This air supply may be continued during the standing action of the air diffuser 10b. However, the air supply may be temporarily stopped and the air supplied after the air diffuser 10b is raised.

この旋回流によって、曝気槽1底部の汚泥堆積が無くなれば(拡散すれば)、一方の散気部10bを倒伏させて水平状態に復帰させ、全面曝気に移行する。
この旋回流による汚泥攪拌は、上記と同様に、目視により、汚泥の堆積を確認した都度、一方の散気部10bを起立操作して行ったり、一定時間毎にその起立を自動操作して行い、その一定時間は実験・実操業に基づき適宜に設定する。また、汚泥堆積量をセンサーで検出し、その検出信号に基づきその操作をすることもできる。旋回流の操作時間も、実験・実操業に基づく堆積量に応じて適宜に設定する。
When the swirl flow eliminates sludge accumulation at the bottom of the aeration tank 1 (if it diffuses), one of the air diffusers 10b is laid down and returned to the horizontal state, and the entire surface is aerated.
The sludge agitation by the swirl flow is performed by standing up one of the air diffusers 10b every time the sludge accumulation is confirmed by visual observation, or by automatically operating the standing up at regular intervals. The fixed time is appropriately set based on experiments and actual operations. Moreover, the amount of sludge accumulation can be detected by a sensor, and the operation can be performed based on the detection signal. The operation time of the swirling flow is also set appropriately according to the amount of accumulation based on the experiment and actual operation.

上記各実施例において、上記散気装置10の一方の散気部10bと他方の散気部10aの間に、例えば、図1(b)の鎖線で示すように、上下方向の仕切り壁30を設けることができる。このようにすれば、その仕切り壁30によって槽1内を上昇流域と下降流域とに分けることができて上記旋回流が生じ易くなって、上記攪拌作用も円滑となる。その仕切り壁30は、上方のみ、下方のみでもよい。   In each of the above embodiments, the partition wall 30 in the vertical direction is provided between the one air diffuser 10b and the other air diffuser 10a of the air diffuser 10 as shown by the chain line in FIG. Can be provided. If it does in this way, the inside of the tank 1 can be divided into an upflow area and a downflow area by the partition wall 30, it becomes easy to produce the said turning flow, and the said stirring action also becomes smooth. The partition wall 30 may be only upward or downward.

上記各実施例は、一の空気供給管14によって各散気装置10に空気供給を行っているため、その設備も安くなり、また、その制御、例えば、全面曝気時と旋回流時の空気供給量を適宜に変動させること等も容易である。
また、旋回流によって、槽1底部の堆積汚泥を攪拌するようにしたので、各散気装置10の位置も槽1の底面から比較的高い位置にすることができ、高くなれば、圧力損失も少なくなるとともに空気供給圧も小さくし得るため、供給空気能力との関係では有利である。このため、水深:8〜10m程度の深層曝気槽1においても、この発明を採用することによって、円滑な曝気作用を得ることができる。例えば、散気装置10を槽1の水深の中程に設置し得る。
In each of the above embodiments, since air is supplied to each diffuser 10 by one air supply pipe 14, the equipment is also cheaper, and the control thereof, for example, air supply during full aeration and swirl flow It is easy to change the amount appropriately.
Further, since the accumulated sludge at the bottom of the tank 1 is agitated by the swirling flow, the position of each air diffuser 10 can also be set to a relatively high position from the bottom of the tank 1, and if it becomes higher, the pressure loss is also increased. Since the air supply pressure can be reduced while decreasing, it is advantageous in relation to the supply air capacity. For this reason, even in the deep aeration tank 1 having a water depth of about 8 to 10 m, by adopting the present invention, a smooth aeration action can be obtained. For example, the air diffuser 10 can be installed in the middle of the water depth of the tank 1.

なお、各実施例において、各弁16、22は、三方弁等を使用して、一の弁で、両散気部10a、10b等への選択的な空気供給・排気を行なうようにすることもできる。
また、図1〜図2の実施例においても、槽1底面に平行なライザー管15の途中に上記自在管継手17を介在し、その他方の散気部10bの起立によって、その散気部10bへの空気供給を遮断するようにすることもできる。
In each embodiment, each of the valves 16 and 22 uses a three-way valve or the like, and performs selective air supply / exhaust to both the air diffusers 10a and 10b by using one valve. You can also.
Also in the embodiment of FIGS. 1 to 2, the universal pipe joint 17 is interposed in the middle of the riser pipe 15 parallel to the bottom of the tank 1, and the air diffuser 10 b is raised by standing the other air diffuser 10 b. It is also possible to cut off the air supply to the.

因みに、上記各実施例において、旋回流による曝気作用を行う場合には、上記槽底部の堆積汚泥の攪拌作用、例えば、図1の実施例では、各散気装置10の一方の散気部(散気管)10a又は10bに接続のライザー管15の開閉弁16を閉じ、他の散気部10b又は10aのみに空気を送り込むことにより、旋回流を生じさせて行う。この旋回流による曝気は、冬季の硝化抑制時に採用することができるが、冬季に限らず、任意であって、全面曝気と適宜に切り換えることができる。   Incidentally, in each of the above embodiments, when the aeration action by the swirl flow is performed, the stirring action of the accumulated sludge at the bottom of the tank, for example, in one embodiment of FIG. (Aeration tube) The on-off valve 16 of the riser pipe 15 connected to the air diffuser 10a or 10b is closed, and air is sent only to the other air diffuser 10b or 10a to generate a swirling flow. The aeration by the swirling flow can be employed when suppressing nitrification in winter, but is not limited to the winter and is optional and can be appropriately switched to full-surface aeration.

また、旋回流の発生時、各弁16等を適宜に開閉して、散気装置10の一方の散気部10bと他方の散気部10aへの空気供給を交互に繰り返し、旋回流の向きの変更及び散気管12からの散気・その停止を繰り返すことによるエアブロー効果により、散気管12の目詰りを解消・防止できる。   Further, when the swirl flow is generated, the valves 16 and the like are appropriately opened and closed, and the air supply to the one air diffuser 10b and the other air diffuser 10a of the air diffuser 10 is alternately repeated, and the direction of the swirl flow The clogging of the air diffuser 12 can be eliminated and prevented by the air blowing effect by repeating the above change and the air diffused from the air diffuser 12 and the stop thereof.

上記実施例は、下水処理場における曝気槽の場合であったが、高濃度の屎尿を投入して活性汚泥法によってその屎尿を処理する曝気槽、また、曝気することにより、硫化水素臭が減少してアンモニア臭のみとする家畜糞尿貯留槽用曝気槽等にも、この発明を採用できることは勿論であり、その場合、上記実施例の各態様を採用できる。   The above example was the case of an aeration tank in a sewage treatment plant, but an aeration tank in which high-concentration manure was introduced and the manure was treated by the activated sludge method, and the hydrogen sulfide odor decreased by aeration. Of course, the present invention can be applied to an aeration tank for a livestock excrement storage tank that has only an ammonia odor, and in this case, each aspect of the above embodiment can be used.

一実施例を示し、(a)は同実施例の平面図、(b)は同切断右側面図、(c)は(b)の切断要部右側面図1 shows an embodiment, (a) is a plan view of the embodiment, (b) is a right side view of the same cut, (c) is a right side view of the main cutting section of (b). 同実施例の概略斜視図Schematic perspective view of the embodiment 他の実施例の概略切断側面図Schematic cut side view of another embodiment 他の実施例の概略切断側面図Schematic cut side view of another embodiment

符号の説明Explanation of symbols

1 曝気槽
10 散気装置
10a 他方の散気部(一部の散気管)
10b 一方の散気部(他の散気管)
11 ラテラル管
12 散気管
14 空気供給管
15 ライザー管
16、22 開閉弁
17 自在管継手
18 ワイヤー
19 重り
20 エアバック
21 空気供給用ホース
30 仕切り壁
1 Aeration tank 10 Air diffuser 10a The other air diffuser (part of the air diffuser)
10b One air diffuser (other air diffuser)
11 Lateral pipe 12 Air diffuser pipe 14 Air supply pipe 15 Riser pipe 16, 22 Open / close valve 17 Universal pipe joint 18 Wire 19 Weight 20 Air bag 21 Air supply hose 30 Partition wall

Claims (14)

下水処理場における曝気槽1内に散気装置10を設けて、その散気装置10からの散気によって曝気する方法であって、
通常は、上記散気装置10の全ての散気管12に空気を送り込むことによって全面曝気を行い、上記曝気槽1底部に汚泥が堆積した場合には、前記散気装置10の一部の散気管12のみに空気を送り込むことにより、旋回流を生じさせて前記曝気槽1底部に堆積した汚泥を攪拌することを特徴とする曝気槽の運転方法。
A method of providing an aeration device 10 in an aeration tank 1 in a sewage treatment plant, and aeration by aeration from the aeration device 10,
Usually, when aeration is performed on the entire surface by sending air to all of the air diffusers 12 of the air diffuser 10, and sludge accumulates on the bottom of the air tank 1, a part of the air diffuser 10 of the air diffuser 10 is used. 12. A method of operating an aeration tank, characterized in that a swirl flow is generated by feeding air only to 12 and the sludge accumulated at the bottom of the aeration tank 1 is agitated.
活性汚泥法用曝気槽1内に散気装置10を設けて、その散気装置10からの散気によって曝気する方法であって、
通常は、上記散気装置10の全ての散気管12に空気を送り込むことによって全面曝気を行い、前記曝気槽1底部に汚泥が堆積した場合には、前記散気装置10の一部の散気管12のみに空気を送り込むことにより、旋回流を生じさせて前記曝気槽1底部に堆積した汚泥を攪拌することを特徴とする曝気槽の運転方法。
A method in which an aeration device 10 is provided in the activated sludge method aeration tank 1, and aeration is performed by the aeration from the aeration device 10.
In general, when aeration is performed on the entire surface by sending air to all of the air diffusers 12 of the air diffuser 10, and sludge accumulates on the bottom of the aeration tank 1, a part of the air diffuser 10 of the air diffuser 10 is used. 12. A method of operating an aeration tank, characterized in that a swirl flow is generated by feeding air only to 12 and the sludge accumulated at the bottom of the aeration tank 1 is agitated.
家畜糞尿貯留槽を曝気して硫化水素臭を減少させる曝気槽1内に散気装置10を設けて、その散気装置10からの散気によって曝気する方法であって、
通常は、上記散気装置10の全ての散気管12に空気を送り込むことによって全面曝気を行い、上記曝気槽1底部に汚泥が堆積した場合には、前記散気装置10の一部の散気管12のみに空気を送り込むことにより、旋回流を生じさせて前記曝気槽1底部に堆積した汚泥を攪拌することを特徴とする曝気槽の運転方法。
The aeration apparatus 10 is provided in the aeration tank 1 for aeration of the livestock manure storage tank to reduce the hydrogen sulfide odor, and the aeration is performed by the aeration from the aeration apparatus 10.
Usually, when aeration is performed on the entire surface by sending air to all of the air diffusers 12 of the air diffuser 10, and sludge accumulates on the bottom of the air tank 1, a part of the air diffuser 10 of the air diffuser 10 is used. 12. A method of operating an aeration tank, characterized in that a swirl flow is generated by feeding air only to 12 and the sludge accumulated at the bottom of the aeration tank 1 is agitated.
上記散気装置10の一部の散気管と他の散気管の間に上下方向の仕切り壁30を設けて上記旋回流を生じ易くしたことを特徴とする請求項1乃至3の何れかに記載の曝気槽の運転方法。   4. A vertical partition wall 30 is provided between a part of the air diffuser and another air diffuser to facilitate the swirling flow. How to operate the aeration tank. 上記他の散気管はその一側でもって起伏自在として、上記旋回流を生じさせる際には、その他の散気管を起立させるようにしたことを特徴とする請求項1乃至3の何れかに記載の曝気槽の運転方法。   4. The air diffuser according to claim 1, wherein the other air diffuser can be raised and lowered on one side thereof, and when the swirl flow is generated, the other air diffuser is erected. How to operate the aeration tank. 請求項1乃至3の何れかに記載の曝気槽の運転方法を行う曝気装置であって、
上記曝気槽1内に散気装置10を設け、その散気装置の全部の散気管又は一部の散気管のみに空気を選択的に供給可能とし、通常は、前記散気装置10の全ての散気管に空気を送り込むことによって全面曝気を行い、前記曝気槽1中に汚泥が堆積した場合には、前記散気装置10の一部の散気管のみに空気を送り込むことにより、旋回流を生じさせて前記曝気槽1中に堆積した汚泥を攪拌することを特徴とする曝気装置。
An aeration apparatus for performing the operation method of the aeration tank according to claim 1,
The air diffuser 10 is provided in the aeration tank 1 so that air can be selectively supplied to all or only a part of the air diffuser of the air diffuser. When the entire surface is aerated by sending air into the aeration tube, and sludge accumulates in the aeration tank 1, a swirl flow is generated by sending air only to some of the aeration tubes of the aeration device 10. The aeration apparatus characterized by stirring the sludge accumulated in the aeration tank 1.
上記一部の散気管と他の散気管に、空気供給管14からそれぞれ分岐したライザー管15を設けてそのライザー管15によって両散気管にそれぞれ空気を供給可能とするとともに、前記空気供給管14と両分岐ライザー管15の間に設けた弁16によって両散気管又は一部の散気管のみに選択的に空気を供給可能としたことを特徴とする請求項6に記載の曝気装置。   A riser pipe 15 branched from the air supply pipe 14 is provided in the part of the diffuser pipes and the other diffuser pipes so that air can be supplied to both of the diffuser pipes by the riser pipe 15. The aeration apparatus according to claim 6, wherein air can be selectively supplied to both of the diffuser pipes or only a part of the diffuser pipes by a valve 16 provided between the first and second branch riser pipes 15. 上記一部の散気管以外の他の散気管を起伏自在とし、旋回流を生じさせる際には、その他の散気管を起立させることを特徴とする請求項6又は7に記載の曝気装置。   The aeration apparatus according to claim 6 or 7, wherein other aeration tubes other than the part of the aeration tubes are allowed to be raised and lowered, and the other aeration tubes are erected when the swirling flow is generated. 上記一部の散気管と他の散気管に、空気供給管14からそれぞれ分岐したライザー管15を設けてそのライザー管15によって両散気管にそれぞれ空気を供給可能とするとともに、上記他の散気管に至るライザー管15に自在管継手17を介設してその他の散気管を起伏自在とし、前記自在管継手17は開閉弁機能を有して、上記旋回流を生じさせる際には、前記他の散気管を前記自在管継手17を介して起立させ、その開閉弁機能によって他の散気管への空気供給を遮断するようにしたことを特徴とする請求項6に記載の曝気装置。   A riser pipe 15 branched from the air supply pipe 14 is provided in the part of the diffuser pipes and the other diffuser pipes so that air can be supplied to both of the diffuser pipes by the riser pipe 15 and the other diffuser pipes. A riser pipe 15 is provided with a universal pipe joint 17 so that other diffuser pipes can be raised and lowered. The universal pipe joint 17 has an on-off valve function, and when the above-mentioned swirl flow is generated, the other The aeration apparatus according to claim 6, wherein the air diffusion pipe is erected through the universal pipe joint 17 and the air supply to the other air diffusion pipes is shut off by the open / close valve function. 上記空気供給管14からのライザー管15、ラテラル管11によって一部の散気管10aから他の散気管10bに連続して空気を供給可能とし、その両散気管10a、10bの境のラテラル管11に自在管継手17を介設してその他の散気管10bを起伏自在とし、前記自在管継手17は開閉弁機能を有して、上記旋回流を生じさせる際には、前記他の散気管10bを前記自在管継手17を介して起立させ、その開閉弁機能によって他の散気管10bへの空気供給を遮断するようにしたことを特徴とする請求項6に記載の曝気装置。   The riser pipe 15 and the lateral pipe 11 from the air supply pipe 14 can continuously supply air from a part of the diffuser pipes 10a to the other diffuser pipes 10b, and the lateral pipe 11 at the boundary between the diffuser pipes 10a and 10b. The other diffuser pipe 10b can be raised and lowered with a universal pipe joint 17 interposed therebetween, and the universal pipe joint 17 has an open / close valve function. When the swirl flow is generated, the other diffuser pipe 10b is provided. The aeration apparatus according to claim 6, wherein the aeration apparatus is erected through the universal pipe joint 17, and the air supply to the other air diffuser pipe 10 b is shut off by the open / close valve function. 上記他の散気管10bの起立をその散気管10bから上記曝気槽1の上面に導いたワイヤー18によって行うことを特徴とする請求項8乃至10の何れかに記載の曝気装置。   The aeration apparatus according to any one of claims 8 to 10, wherein the other aeration pipe 10b is erected by a wire 18 led from the aeration pipe 10b to the upper surface of the aeration tank 1. 上記他の散気管10bの他側にエアバック20を設け、そのエアバック20に空気を供給することにより膨張させて、そのエアバック20の浮力により、前記他の散気管10bを起立させるようにしたことを特徴とする請求項8乃至10の何れかに記載の曝気装置。   An air bag 20 is provided on the other side of the other air diffuser 10b, and the air diffuser 10b is inflated by supplying air to the air bag 20, and the other air diffuser 10b is erected by the buoyancy of the air bag 20. The aeration apparatus according to any one of claims 8 to 10, wherein 上記他の散気管10bの他側に倒伏状態への復帰用重り19を設けたことを特徴とする請求項8乃至12の何れかに記載の曝気装置。   The aeration apparatus according to any one of claims 8 to 12, wherein a weight 19 for returning to a lying state is provided on the other side of the other diffuser tube 10b. 上記散気装置10の一部の散気管と他の散気管の間に上下方向の仕切り壁30を設けたことを特徴とする請求項6乃至13の何れかに記載の曝気装置。   The aeration apparatus according to any one of claims 6 to 13, wherein a partition wall 30 in the vertical direction is provided between a part of the air diffuser and another air diffuser.
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US8002246B2 (en) 2006-10-27 2011-08-23 Aura Tec Co., Ltd. Aeration apparatus
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8002246B2 (en) 2006-10-27 2011-08-23 Aura Tec Co., Ltd. Aeration apparatus
JP2009101269A (en) * 2007-10-22 2009-05-14 Sharp Corp Odor treatment method, malodor treatment system and breeding system
JP2010158626A (en) * 2009-01-08 2010-07-22 Sumitomo Heavy Industries Environment Co Ltd Air diffuser
JP2016153118A (en) * 2015-02-16 2016-08-25 栗田工業株式会社 Biological treatment tank, method for operating the tank, and method for treating organic waste water
WO2016132881A1 (en) * 2015-02-16 2016-08-25 栗田工業株式会社 Biological treatment tank, method for operating same and method for treating organic wastewater
JP2018023931A (en) * 2016-08-10 2018-02-15 栗田工業株式会社 Operation method of biological treatment tank
CN111573864A (en) * 2020-05-26 2020-08-25 王炳东 Aeration tank for sewage treatment based on sludge siltation prevention
JP2021090966A (en) * 2021-02-25 2021-06-17 住友重機械エンバイロメント株式会社 Water treatment system and method for improving water treatment system
JP7145256B2 (en) 2021-02-25 2022-09-30 住友重機械エンバイロメント株式会社 Water treatment system and method for improving water treatment system
CN114192538A (en) * 2021-12-03 2022-03-18 上海康恒环境修复有限公司 Horizontal aerobic aeration system of household garbage rigid landfill

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