JPH02174998A - Mixing aerator for aeration tank - Google Patents
Mixing aerator for aeration tankInfo
- Publication number
- JPH02174998A JPH02174998A JP63331698A JP33169888A JPH02174998A JP H02174998 A JPH02174998 A JP H02174998A JP 63331698 A JP63331698 A JP 63331698A JP 33169888 A JP33169888 A JP 33169888A JP H02174998 A JPH02174998 A JP H02174998A
- Authority
- JP
- Japan
- Prior art keywords
- aerator
- waterway
- flow velocity
- peripheral side
- mounting angle
- 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.)
- Granted
Links
- 238000005273 aeration Methods 0.000 title claims abstract description 30
- 238000005276 aerator Methods 0.000 title claims abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- 230000002093 peripheral effect Effects 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract description 6
- 239000002351 wastewater Substances 0.000 description 6
- 238000009434 installation Methods 0.000 description 5
- 239000010802 sludge Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000010564 aerobic fermentation Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 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)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は無終端水路を形成した曝気槽において、汚水を
均一に混合して効率的、均一な曝気を行なう装置に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for uniformly mixing wastewater and performing efficient and uniform aeration in an aeration tank having an endless waterway.
下水汚水、産業廃棄汚水等の有機物を含有する汚水の処
理に際しては長円形の循環水路、二重円形水路の如く無
紋・端水路を形成した曝気槽に曝気機を設置し、該槽内
の汚水中に空気すなわち空気中の酸素を連続的に供給し
つつ汚水を混合撹拌して暢気すなわち好気性発酵処理を
行なう方法が提案されている。When treating sewage containing organic matter such as sewage sewage and industrial waste sewage, an aeration machine is installed in an aeration tank that has an oval circulation waterway or a double circular waterway with no markings or end channels. A method has been proposed in which wastewater is mixed and stirred while continuously supplying air, that is, oxygen in the air, to carry out an aerobic fermentation treatment.
〔発明が解決しようとする[1118)無終幼水路を有
する二重円形曝気槽において、該槽の中心を通す直線に
対し直交する方向に2台の嘩気機を互いに平行にして設
置し、そしてこの1ft気9機B置位置より1.80度
より少し旋回した位置で水路の内周側より外周側に向か
って所要間隔毎に流速計を投置して曝気機を運転しつつ
水路内の各点における流速を計測した。[To be solved by the invention [1118] In a double circular aeration tank having an endless nursery channel, two aerators are installed parallel to each other in a direction perpendicular to a straight line passing through the center of the tank, Then, at a position a little more than 1.80 degrees turned from the 1ft aerator B position, flowmeters were placed at required intervals from the inner circumference to the outer circumference of the waterway, and while the aerator was running, it was inside the waterway. The flow velocity at each point was measured.
第1図a、l)t C1dの各測定点における計測結
束は第2図(1)に示すように水路の内周側が遅く、外
周になる程流速が速くなることが判明した。As shown in FIG. 2 (1), it was found that the flow velocity at each measurement point in FIG. 1 a, l) t C1d was slow at the inner circumference of the waterway, and faster toward the outer circumference.
このように水路における流速の不均等はいかに曝気を行
なっても良好な曝気を行なえず、スワール現象が生じて
水路の内周側に汚泥が堆積し、この堆積汚泥が腐敗し、
水質を悪化させる新たな問題が生じる。In this way, the uneven flow velocity in the waterway makes it impossible to achieve good aeration no matter how much aeration is performed, and a swirl phenomenon occurs, causing sludge to accumulate on the inner circumference of the waterway, and this accumulated sludge rots.
New problems arise that degrade water quality.
本発明はこれに鑑みて曝気すべき無終端水路の形状、大
きさに応じて曝気機による水路内側の流速を外周側に比
べて増大させるようにして曝気機を設置し、水路全体に
亘って流速の均一化を図り少ない動力で均一に混合し、
汚泥堆積、水a悪化を未然に防止し、効率的なlE!気
を行なうことを目的とする。In view of this, the present invention installs an aerator so that the flow velocity inside the waterway by the aerator is increased compared to the outer circumferential side according to the shape and size of the endless waterway to be aerated, and the aerator is installed throughout the waterway. Uniform flow rate allows for uniform mixing with less power,
Efficient lE that prevents sludge accumulation and water aggravation! The purpose is to practice qi.
曝気すべき無21%端水路の形状9 大きさに応して曝
気機による水路内周側の流速を外周側に比べて増大させ
るようにスクリュー形曝気機の水平取付角調整可能にし
て取り付け、水路全体に亘って流速の均一化を図り水路
を均一に混合する。Shape of 21% end waterway to be aerated 9 Install the screw type aerator so that the horizontal mounting angle can be adjusted so that the flow velocity on the inner circumferential side of the waterway by the aerator is increased compared to the outer circumferential side according to the size. Equalize the flow velocity throughout the waterway and mix the waterway uniformly.
無終端水路に設とされる曝気機を該水1烙の内周(1!
l流速をその外周よりも増大させるようにスクリュー形
曝気機を前記漕の水路に対し水平取付角を変えて!2g
tすることにより水路内における汚水は均一に混合され
、スワール現象が防止される。これにより汚泥の堆積や
水質悪化の問題をも解決することができる。An aerator installed in an endless waterway is installed around the inner circumference of the water (1!
l Change the horizontal installation angle of the screw type aerator with respect to the waterway of the tank so that the flow rate is increased more than its outer circumference! 2g
By doing so, the wastewater in the waterway is mixed uniformly, and the swirl phenomenon is prevented. This also solves the problems of sludge accumulation and water quality deterioration.
以下本発明16気槽に於ける均一混合曝気装置を図示の
実施例にもとづいて説明する。The homogeneous mixing aeration device in the 16-air tank of the present invention will be explained below based on the illustrated embodiment.
第1図のものは無終端水路が円形をなした二重円形曝気
槽を用いた実施例である。The one in FIG. 1 is an embodiment using a double circular aeration tank with a circular endless water channel.
1は二重円形曝気槽で、これは小径の円周壁11と大径
の外周壁12を同心上にして2毅し。1 is a double circular aeration tank, which has a small diameter circumferential wall 11 and a large diameter outer circumferential wall 12 arranged concentrically.
この内外両周壁11,121!8に所要幅と深さを有す
る循環水路ユ23を形成する。A circulation waterway unit 23 having a required width and depth is formed on both the inner and outer circumferential walls 11, 121!8.
2はスクリュー形曝気機で、第5図に詳示するようにモ
ータ直結の中空シャフトとスクリューとにより構成され
、スクリューの回転により水流を起こすと共に、それに
伴って発生ずるスクリュー先端部の負圧を利用して空気
を中空シャフトを介して吸引し、汚水中に微細気泡とし
て供給させ、気泡を水中に効率的に溶は込むようになし
たものである。2 is a screw type aerator, which, as shown in Figure 5, consists of a hollow shaft directly connected to a motor and a screw.The rotation of the screw generates a water flow, and the resulting negative pressure at the tip of the screw is reduced. Air is sucked in through a hollow shaft and supplied into the wastewater as fine bubbles, so that the bubbles are efficiently dissolved into the water.
曝気機2は取付フレーム21にモータ22を固定し、こ
のモータ22に中空シャフト23を直結し、このモータ
及び中空シャフトをカバー24にて覆い、このカバーを
介してモータ等をフレームに取り付けるが、この場合取
付角度調整器25を介して水路に対し曝気機の水平取付
角度を任意に調整可能とし、かつ前記中空シャフト先端
に所要形状のスクリュー26を設けて成る。In the aerator 2, a motor 22 is fixed to a mounting frame 21, a hollow shaft 23 is directly connected to the motor 22, the motor and the hollow shaft are covered with a cover 24, and the motor etc. are attached to the frame through this cover. In this case, the horizontal mounting angle of the aerator relative to the waterway can be arbitrarily adjusted via a mounting angle adjuster 25, and a screw 26 of a desired shape is provided at the tip of the hollow shaft.
そしてこの各曝気機2の槽に対する水平取付角度すなわ
ち二重円形曝気if 1に対しその接線方向の角度をそ
れぞれ調整可能として取り付ける1例えば内側の曝気機
の水平取付角度をα、外側の曝気機の水平取付角度なβ
とし、(1)α=0° β=O。Then, the horizontal installation angle of each aerator 2 with respect to the tank, that is, the angle in the tangential direction to the double circular aeration if 1, can be adjusted respectively 1. For example, the horizontal installation angle of the inner aerator is α, Horizontal installation angle β
and (1) α=0° β=O.
(2) α = 9″、 β = 6゜(3)α=9
°、βa耘せず
(4) αR転せず、 β=i39
(5) β=45″
の各取付角度での暢気機2台を用いて運転した。(2) α = 9″, β = 6° (3) α = 9
It was operated using two free-air machines at each mounting angle: °, βa did not change (4) αR did not change, β = i39 (5) β = 45''.
夫々の運転状態における水g13内の流速を曝気機2の
設定位置より180度以上旋回した位置に、かつ底部よ
り10(1)の高さに流速計a、 b。Current velocity meters a and b are placed at a position 180 degrees or more from the set position of the aerator 2 and at a height of 10 (1) from the bottom to measure the flow velocity in the water g13 in each operating state.
c、 dを設置して計測し、その結果を第2図に示す
。c and d were installed and measured, and the results are shown in Figure 2.
これからもヤ」るようにα二9″、 β=6°及びα=
9°、β運転せずの場合、水路]3の内周側と外周側と
がその流速はほぼ均一化されている。これは曝気機2の
水平取付角を内側に向けて12五して運転することによ
り循環水路13の内周側流速が外周側J、り流速を増大
しているものである。From now on, α29″, β=6° and α=
9°, β When the operation is not performed, the flow velocity on the inner circumferential side and the outer circumferential side of the water channel] 3 is almost equalized. This is because the flow velocity on the inner circumferential side of the circulation waterway 13 increases compared to the flow velocity on the outer circumferential side J by operating the aerator 2 with its horizontal mounting angle facing inward.
また第3図に示すものは長円形の11気槽3を示すもの
である。この実施例では曝気装置2を循環水路33の直
線位置に2台設置する。この直線+路に長1−輪心に対
し、内側に設置した曝気装置の中心線を少し内側に向く
ようにして内周0tll流速を増大させる。他力外側に
設置した曝気装置は中心線を少し外側に向くようにして
設置して、内外周壁近傍の流速を中央部に比べて上げる
ようにする。このようにすれば、水g槙所面における流
速は直線部においても均一化され、更に旋回部において
も均一化を図ることがi′11′能である。Moreover, what is shown in FIG. 3 shows eleven oval air tanks 3. In this embodiment, two aeration devices 2 are installed in a straight line position of the circulation waterway 33. In this straight + path, the center line of the aeration device installed on the inside of the long 1-wheel center is directed slightly inward to increase the inner periphery 0tll flow velocity. The aeration devices installed on the outside are installed with their center lines facing slightly outward to increase the flow velocity near the inner and outer peripheral walls compared to the center. In this way, the flow velocity on the water flow surface can be made uniform not only in the straight section but also in the swirling section.
また第4図は二重円形曝気槽において曝気装置のJ9置
方法を変化させた異なる実施例を示すが、(A)は−台
の曝気装置を流路中央部よりも内周側に配置した例であ
り、(B)は水流方向を内側に向けた例であり、(C)
は外側の曝気装置に比べて、容量能力の大きい曝気装置
を内側に配して内周側流速を増大するようにした例を夫
々示している。Furthermore, Fig. 4 shows a different embodiment in which the aeration device J9 placement method was changed in a double circular aeration tank, but (A) shows a different example in which the aeration device J9 was placed closer to the inner circumference than the center of the flow path. This is an example, (B) is an example where the water flow direction is directed inward, and (C)
1 and 2 show examples in which an aeration device having a larger capacity than an outside aeration device is arranged inside to increase the flow velocity on the inner peripheral side.
本発明は曝気すべき無終端水路の形状、大きさに応じて
@紙機による水路内側の流速をダ周側に比べて増大させ
るように曝気機をその水平取付角度を内側に向くように
毅けているので水路全体に亘って流速の均一化を図り水
路全体を均一に混合され、スワール現象を防止し、かつ
水路幅方向に亘って汚水を均一に混合できるので汚水を
安定してかつ効率的、均一な曝気を行なうことができ、
しかもスクリュー形曝気機により空気を自吸でき、装置
が簡易となる利点がある。In accordance with the shape and size of the endless waterway to be aerated, the present invention is designed so that the horizontal installation angle of the aerator is directed inward so that the flow velocity inside the waterway due to the paper machine is increased compared to the periphery side. This allows the flow velocity to be uniform throughout the waterway, ensuring uniform mixing throughout the waterway, preventing swirl phenomena, and allowing wastewater to be mixed uniformly across the width of the waterway, ensuring stable and efficient flow of wastewater. Targeted and uniform aeration can be performed.
Moreover, the screw type aerator allows air to be self-suctioned, which has the advantage of simplifying the equipment.
図面は本発明@低重ζこ於ける均一混合@′A装置を示
す一実施例で、第1図は二重円形曝気槽の平面図、第2
図は水路各点における流速値を示したグラフ図、第3図
は長円形曝気槽の111面図、第4図は異なりたる実施
例の説明図、第5因は曝気機の説明図である。
1は二重円形曝気槽、2は@紙機、3は長円形@iA僧
。The drawings show one embodiment of the present invention @low-weight ζ homogeneous mixing @'A device. Figure 1 is a plan view of a double circular aeration tank, and Figure 2 is a plan view of a double circular aeration tank.
The figure is a graph showing flow velocity values at each point in the waterway, Figure 3 is a 111-view diagram of an oblong aeration tank, Figure 4 is an explanatory diagram of different embodiments, and the fifth factor is an explanatory diagram of an aerator. . 1 is a double circular aeration tank, 2 is @ paper machine, and 3 is oval @ iA monk.
Claims (2)
気機による水路内周側の流速を外周側に比べて増大させ
るようにスクリュー形曝気機の水平取付角調整可能にし
て取り付けることを特徴とする曝気槽に於ける混合曝気
装置。(1) The horizontal mounting angle of the screw type aerator can be adjusted and installed so that the flow velocity of the aerator on the inner circumferential side of the waterway is increased compared to the outer circumferential side according to the shape and size of the endless waterway to be aerated. A mixed aeration device in an aeration tank characterized by:
置における水路曲線の接線方向から水路内周側に所定の
角度を有することを特徴とする第1項記載の曝気槽に於
ける混合曝気装置。(2) Mixed aeration in the aeration tank according to item 1, wherein the horizontal mounting angle of the screw type aerator has a predetermined angle from the tangential direction of the waterway curve at the mounting position to the inner circumferential side of the waterway. Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63331698A JPH0763709B2 (en) | 1988-12-28 | 1988-12-28 | A uniform mixing aerator for aeration tank consisting of double circular circulation channels |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63331698A JPH0763709B2 (en) | 1988-12-28 | 1988-12-28 | A uniform mixing aerator for aeration tank consisting of double circular circulation channels |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02174998A true JPH02174998A (en) | 1990-07-06 |
JPH0763709B2 JPH0763709B2 (en) | 1995-07-12 |
Family
ID=18246586
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63331698A Expired - Fee Related JPH0763709B2 (en) | 1988-12-28 | 1988-12-28 | A uniform mixing aerator for aeration tank consisting of double circular circulation channels |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0763709B2 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5979294U (en) * | 1982-11-19 | 1984-05-29 | 住友重機械エンベイロテック株式会社 | Circulating waterway type wastewater treatment equipment |
JPS6021397U (en) * | 1983-07-22 | 1985-02-14 | 日立プラント建設株式会社 | rotary aeration device |
JPS6067196U (en) * | 1983-10-17 | 1985-05-13 | 丸誠重工業株式会社 | Sewage treatment equipment |
-
1988
- 1988-12-28 JP JP63331698A patent/JPH0763709B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5979294U (en) * | 1982-11-19 | 1984-05-29 | 住友重機械エンベイロテック株式会社 | Circulating waterway type wastewater treatment equipment |
JPS6021397U (en) * | 1983-07-22 | 1985-02-14 | 日立プラント建設株式会社 | rotary aeration device |
JPS6067196U (en) * | 1983-10-17 | 1985-05-13 | 丸誠重工業株式会社 | Sewage treatment equipment |
Also Published As
Publication number | Publication date |
---|---|
JPH0763709B2 (en) | 1995-07-12 |
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