JPH0534798Y2 - - Google Patents
Info
- Publication number
- JPH0534798Y2 JPH0534798Y2 JP1987095106U JP9510687U JPH0534798Y2 JP H0534798 Y2 JPH0534798 Y2 JP H0534798Y2 JP 1987095106 U JP1987095106 U JP 1987095106U JP 9510687 U JP9510687 U JP 9510687U JP H0534798 Y2 JPH0534798 Y2 JP H0534798Y2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- plate
- air diffuser
- tank body
- inclined guide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000005273 aeration Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000002351 wastewater Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000010802 sludge Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005276 aerator Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Activated Sludge Processes (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
本考案は、下水処理場等において有機性廃水の
処理に用いられる曝気槽の改良に関するものであ
る。[Detailed Description of the Invention] (Field of Industrial Application) The present invention relates to the improvement of an aeration tank used for treating organic wastewater in sewage treatment plants and the like.
(従来の技術)
有機性廃水の処理には、廃水を曝気槽に入れ活
性汚泥を加えたうえで散気装置によつて空気を吹
込み、槽内に旋回流を生じさせて攪拌を行わせる
とともに空気中の酸素によつて活性汚泥中の好気
性微生物の活性度を高め、有機物の生物処理を行
わせる活性汚泥法が最も多く採用されている。こ
のために従来から第3図及び第4図に示されるよ
うに、槽体11を垂直なバツフル板3により2分
し、その片側の水深が4〜5mの中段位置に散気
装置12を設けた曝気槽が用いられている。この
ような曝気槽の内部では散気装置12から発生す
る気泡の浮力によつて矢印方向の旋回流が形成さ
れるのであるが、水流は槽体1の壁付近を中心と
して流れるためにその流速分布を測定すると例え
ば第3図のようになり、中央のバツフル板13に
近い部分では逆方向の流れさえ生じて均一な旋回
流が形成されていないことが判明した。またこの
結果、DO(溶存酸素)濃度の分布を測定すると
第4図のように槽の中央付近の領域ではDO値が
低く、この領域では酸素が不足して生物処理が有
効に行われないデツドゾーンとなつていることも
判明した。(Conventional technology) To treat organic wastewater, wastewater is placed in an aeration tank, activated sludge is added thereto, and air is blown into the tank using an aeration device to create a swirling flow in the tank and agitate the tank. The activated sludge method, in which the activity of aerobic microorganisms in activated sludge is increased by oxygen in the air to perform biological treatment of organic matter, is most commonly adopted. For this purpose, conventionally, as shown in FIGS. 3 and 4, the tank body 11 is divided into two parts by a vertical buttful plate 3, and an air diffuser 12 is installed in the middle position of one side of the tank body at a water depth of 4 to 5 m. Aerated tanks are used. Inside such an aeration tank, a swirling flow in the direction of the arrow is formed due to the buoyancy of the bubbles generated from the aeration device 12, but since the water flow is centered near the wall of the tank body 1, the flow velocity is low. When the distribution was measured, the result was as shown in FIG. 3, for example, and it was found that even a flow in the opposite direction occurred in a portion near the center baffle plate 13, and a uniform swirling flow was not formed. Furthermore, as a result, when measuring the distribution of DO (dissolved oxygen) concentration, as shown in Figure 4, the DO value is low in the area near the center of the tank, which is a dead zone where oxygen is insufficient and biological treatment cannot be performed effectively. It was also found that
(考案が解決しようとする問題点)
本考案は上記のような従来の問題点を解決し、
槽内の全領域にわたつてできるだけ均一な旋回流
を形成することにより酸素不足の領域が発生する
ことを防止し、これによつて槽内の全域にわたつ
て好気性微生物による生物処理が活発に行われる
ようにした曝気槽を目的として完成されたもので
ある。(Problems that the invention attempts to solve) This invention solves the conventional problems as mentioned above,
By creating a swirling flow that is as uniform as possible throughout the entire area of the tank, the formation of oxygen-deficient areas is prevented, and as a result, biological treatment by aerobic microorganisms is activated throughout the entire area of the tank. It was completed with the purpose of creating an aeration tank for this purpose.
(問題点を解決するための手段)
本考案は、槽体を垂直なバツフル板により2分
してその片側に散気装置を設けるとともに、バツ
フル板を挟んで散気装置とは反対側の中央付近の
水面よりもやや下方位置に、水平方向の流れを下
向きに偏向させる傾斜案内板をバツフル板とは独
立に設けたことを特徴とするものである。(Means for solving the problem) The present invention is to divide the tank body into two by a vertical buttful plate, provide an air diffuser on one side, and place the air diffuser in the center on the opposite side of the aerator with the buttfull plate in between. It is characterized by having an inclined guide plate, which deflects the horizontal flow downward, installed at a position slightly below the nearby water surface, independent of the baffle plate.
(実施例)
次に本考案を図示の実施例について詳細に説明
する。(Embodiments) Next, the present invention will be described in detail with reference to illustrated embodiments.
第1図及び第2図において、1は例えば深さが
10m、幅が10m、紙面方向の長さが数十m程度の
深槽曝気槽の槽体、2はその片側の水深が4〜
5m付近の中段位置に設けられた散気装置、3は
槽体1の中央部に垂直に設けられて槽体1の内部
を2分するバツフル板である。また4はバツフル
板3を挟んで散気装置2が設けられている側とは
反対側の中央付近の水面よりもやや下方位置にバ
ツフル板3とは独立させて固定された傾斜案内板
である。この傾斜案内板4は散気装置2から発生
する気泡の浮力によつて形成される旋回流のう
ち、バツフル板2の上方部分を水平方向に通過し
てきた流れを下向きに偏向させるためのものであ
り、実施例ではバツフル板3の上端と水面との間
が2mとされており、傾斜案内板4はその上端が
水面下1m、その下端が水面下2mに位置するよう
に45°の角度で固定されている。なお、傾斜案内
板4はタービンブレードのようにゆるやかにわん
曲した断面形状を持たせてもよく、また複数枚を
適当な間隔で取付けてもよい。更にまた、第1図
に想像線で示すように槽体1の上部傾斜部5をわ
ん曲させたり、散気装置2の上方にも同様の傾斜
案内板6を設ければより好ましい結果を得ること
ができる。 In Figures 1 and 2, 1 is, for example, a depth
The tank body of a deep aeration tank is 10 m long, 10 m wide, and several tens of meters long in the paper direction.
The air diffuser 3, which was installed at a middle position at around 5 m, is a baffle plate that is vertically installed in the center of the tank 1 and divides the inside of the tank 1 into two. Reference numeral 4 designates an inclined guide plate that is fixed independently of the full board 3 at a position slightly below the water surface near the center on the opposite side of the full board 3 from the side where the air diffuser 2 is installed. . This inclined guide plate 4 is for deflecting downward the flow that has passed horizontally through the upper part of the bubble plate 2 out of the swirling flow formed by the buoyancy of bubbles generated from the air diffuser 2. In the example, the distance between the upper end of the vertical board 3 and the water surface is 2 m, and the inclined guide plate 4 is installed at an angle of 45° so that its upper end is located 1 m below the water surface and its lower end is located 2 m below the water surface. Fixed. Incidentally, the inclined guide plate 4 may have a gently curved cross-sectional shape like a turbine blade, or a plurality of inclined guide plates 4 may be attached at appropriate intervals. Furthermore, more preferable results can be obtained by bending the upper inclined portion 5 of the tank body 1 as shown by imaginary lines in FIG. 1, or by providing a similar inclined guide plate 6 above the air diffuser 2. be able to.
(作用)
このように構成されたものは、槽体1内に廃水
を満たしたうえでバツフル板3の片側中段の散気
装置2から圧縮空気を多数の気泡として水中に噴
出させ、その浮力によつて槽内に図示のような旋
回流を発生させて槽内の廃水の攪拌を行わせると
同時に酸素の供給を行い、これにより活性汚泥法
による有機廃水の処理を行わせることは従来のも
のと同様である。しかし本考案においては、槽体
1のバツフル板3を挟んで散気装置2が設けられ
た側とは反対側の中央付近の水面よりもやや下方
位置にバツフル板3とは独立させて傾斜案内板4
を設けてあるので、槽中央のバツフル板3の上部
を水平方向に流れてきた水流のうち水面直下の水
流は従来と同様に槽体1の壁面に沿つて流れる
が、より低い部分を水平方向に流れる水流はこの
領域案内板4によつて下向きに偏向され、槽内の
バツフル板3に近い領域においても旋回流が形成
される。この結果、本考案の曝気槽内の流速分布
は例えば第1図に示すとおりとなり、これを従来
の曝気槽内の流速分布を示す第3図と比較する
と、流速のばらつきが極めて小さくなり、全領域
にわたつて均一な旋回流が形成されたことが分か
る。(Function) In this structure, after the tank body 1 is filled with waste water, compressed air is ejected into the water as a large number of bubbles from the air diffuser 2 located in the middle of one side of the full plate 3, and the buoyancy of the air is used to Therefore, the conventional method is to generate a swirling flow in the tank as shown in the figure to stir the wastewater in the tank and at the same time supply oxygen, thereby treating organic wastewater using the activated sludge method. It is similar to However, in the present invention, an inclined guide is provided at a position slightly below the water surface near the center of the tank body 1 on the side opposite to the side where the air diffuser 2 is provided, with the buttful plate 3 interposed therebetween. Board 4
, the water flow directly below the water surface that flows horizontally over the upper part of the buttful plate 3 in the center of the tank flows along the wall surface of the tank body 1 as before, but the lower part flows horizontally. The water flow flowing through the tank is deflected downward by the area guide plate 4, and a swirling flow is also formed in the area close to the baffle plate 3 in the tank. As a result, the flow velocity distribution in the aeration tank of the present invention is as shown in Figure 1, for example. Comparing this with Figure 3, which shows the flow velocity distribution in the conventional aeration tank, the variation in flow velocity is extremely small, and the overall It can be seen that a uniform swirling flow was formed over the area.
またこの結果、本考案の曝気槽の内部には流速
の小さいデツドゾーンが形成されにくくなるの
で、DO濃度の分布は第2図のようになり、従来
例を示す第4図の値と比較すると槽内の全領域に
わたつてほぼ均一なDO濃度が得られることが明
らかである。 As a result, it becomes difficult to form a dead zone with a low flow rate inside the aeration tank of the present invention, so the DO concentration distribution becomes as shown in Figure 2. It is clear that a nearly uniform DO concentration can be obtained over the entire area.
(考案の効果)
本考案は以上の説明からも明らかなように、バ
ツフル板により2分された槽体内のバツフル板を
挟んで散気装置とは反対側の中央部分に傾斜案内
板を設けて槽内の中央部分にも旋回流を生じさ
せ、これによつて槽内の流速分布及びDO濃度分
布を均一化して槽内の全域にわたつて好気性微生
物による生物処理を活発に行わせることに成功し
たものである。従つて本考案によれば槽内の全領
域を有効に利用できるので同一サイズの槽体であ
ればその処理能力を向上させることができ、また
処理能力を一定とすれば槽体のサイズを小型化す
ることができる。よつて本考案は従来の問題点を
一掃した曝気槽として、産業の発展に寄与すると
ころは極めて大である。(Effects of the invention) As is clear from the above explanation, the present invention provides an inclined guide plate in the central part on the opposite side of the air diffuser across the double plate inside the tank, which is divided into two by the double plate. A swirling flow is also generated in the center of the tank, which equalizes the flow velocity distribution and DO concentration distribution within the tank, allowing aerobic microorganisms to actively perform biological treatment throughout the tank. It was a success. Therefore, according to the present invention, the entire area inside the tank can be used effectively, so if the tank is the same size, the processing capacity can be improved, and if the processing capacity is constant, the tank size can be reduced. can be converted into Therefore, the present invention will greatly contribute to the development of industry as an aeration tank that eliminates the problems of the conventional system.
第1図は本考案の実施例の曝気槽内の流速分布
を示すベクトル線図、第2図は同じくDO濃度の
分布図、第3図は従来の曝気槽内の流速分布を示
すベクトル線図、第4図はそのDO濃度の分布図
である。
1……槽体、2……散気装置、3……バツフル
板、4……傾斜案内板。
Figure 1 is a vector diagram showing the flow velocity distribution in the aeration tank according to the embodiment of the present invention, Figure 2 is a DO concentration distribution diagram, and Figure 3 is a vector diagram showing the flow velocity distribution in the conventional aeration tank. , FIG. 4 is a distribution map of the DO concentration. 1...tank body, 2...aeration device, 3...buttful board, 4...inclined guide plate.
Claims (1)
の片側に散気装置2を設けるとともに、バツフル
板3を挟んで散気装置2とは反対側の中央付近の
水面よりもやや下方位置に、水平方向の流れを下
向きに偏向させる傾斜案内板4をバツフル板3と
は独立に設けたことを特徴とする曝気槽。 The tank body 1 is divided into two parts by a vertical butt-full plate 3, and the air diffuser 2 is installed on one side of the tank body, and the air diffuser 2 is installed at a position slightly below the water surface near the center on the opposite side of the air diffuser 2 across the butt-full plate 3. An aeration tank characterized in that an inclined guide plate 4 for deflecting a horizontal flow downward is provided independently of a buttful plate 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1987095106U JPH0534798Y2 (en) | 1987-06-19 | 1987-06-19 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1987095106U JPH0534798Y2 (en) | 1987-06-19 | 1987-06-19 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS641797U JPS641797U (en) | 1989-01-06 |
JPH0534798Y2 true JPH0534798Y2 (en) | 1993-09-02 |
Family
ID=30959263
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1987095106U Expired - Lifetime JPH0534798Y2 (en) | 1987-06-19 | 1987-06-19 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0534798Y2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2663327B2 (en) * | 1993-05-20 | 1997-10-15 | 哲夫 西田 | Culture treatment tank and water treatment facility with it |
US8307856B2 (en) * | 2007-11-07 | 2012-11-13 | Tdw Delaware Inc. | Double block and bleed plug |
JP4994349B2 (en) * | 2008-12-01 | 2012-08-08 | メタウォーター株式会社 | Nitrification carrier circulation method in deep tank aeration tank |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5439341Y2 (en) * | 1975-02-25 | 1979-11-21 |
-
1987
- 1987-06-19 JP JP1987095106U patent/JPH0534798Y2/ja not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS641797U (en) | 1989-01-06 |
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