JPS60193592A - Aeration apparatus for water treatment - Google Patents
Aeration apparatus for water treatmentInfo
- Publication number
- JPS60193592A JPS60193592A JP59049884A JP4988484A JPS60193592A JP S60193592 A JPS60193592 A JP S60193592A JP 59049884 A JP59049884 A JP 59049884A JP 4988484 A JP4988484 A JP 4988484A JP S60193592 A JPS60193592 A JP S60193592A
- Authority
- JP
- Japan
- Prior art keywords
- water
- aeration
- aeration vessel
- aeration tank
- vessel
- 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.)
- Pending
Links
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】
本発明け、曝気槽内の処理水及び活性汚泥をその曝気槽
内の水面上方に揚送吐出するポンプ付管路を設け、その
管路に酸素含有ガスを供給する給気装置を設けた曝気装
置の改良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a pipe with a pump for pumping and discharging treated water and activated sludge in the aeration tank above the water surface in the aeration tank, and supplies oxygen-containing gas to the pipe. This invention relates to improvement of an aeration device equipped with an air supply device.
従来、第6図に示すように、−Fl&(2)から吐出さ
れる処理水を曝気槽ill内の水11ii(5)に衝突
させ、給気装置(4)からの酸素含有ガスを可及的に長
時間水中に保持させ、酸素供給速麿を大きくしようとし
ていた。 しかし、管路(2)からの処理水が水面位に
衝突するに際し、周囲の大気を巻込んで、水面位上で激
しく発泡し、曝気槽(1)からあふれた泡や汚泥によシ
設備が汚染される欠点があった。 また、曝気槽(1)
内の生物反応に伴う発熱は曝気排ガスによって持去られ
るだけであるため、殊に夏期に高濃変有機廃水を大量6
理する場合、曝気槽(1)内の水温が高温になり過ぎて
、活性汚泥の活動が鈍化しやすい欠点があり、また、曝
気槽(11に冷凍機を付設すると、イニシャルコスト及
びランニングコストの而で不利になる欠点があった。Conventionally, as shown in Fig. 6, the treated water discharged from -Fl & (2) is made to collide with the water 11ii (5) in the aeration tank ill, and the oxygen-containing gas from the air supply device (4) is released as much as possible. In order to increase the rate of oxygen supply, the researchers tried to keep the water in water for a long time to increase the rate of oxygen supply. However, when the treated water from the pipe (2) collides with the water level, it entrains the surrounding air and foams violently above the water level. It had the disadvantage that it could be contaminated. Also, aeration tank (1)
Since the heat generated by the biological reactions in the water is only carried away by the aeration exhaust gas, large amounts of highly concentrated denatured organic wastewater are used, especially in the summer.
If a refrigerator is installed in the aeration tank (11), the water temperature in the aeration tank (1) becomes too high, which tends to slow down the activity of activated sludge. However, there were drawbacks that put it at a disadvantage.
本発明の目的は、酸素供給速麿を十分に大にしながら、
曝気槽内での発泡及び水温上昇を十分に抑制できるよう
にする点にある。The object of the present invention is to sufficiently increase the oxygen supply rate while
The aim is to sufficiently suppress foaming and water temperature rise in the aeration tank.
本発明による曝気装置の特徴構成は、曝気槽から活性汚
泥き共に揚送され、かつ、給気装置からの酸素含有ガス
が混入された状態で、ポンプ付管路から吐出される処理
水を衝突させる分散具を、その衝突面が曝気槽内の水面
上方に位置するように、かつ、衝突面からの飛散水が曝
気槽内に落下す”るように配置したことにあり、その作
用効果は次の通りである。The characteristic configuration of the aeration device according to the present invention is that activated sludge is pumped together from the aeration tank, and treated water discharged from a pipe with a pump is collided with oxygen-containing gas from the air supply device. The effect is that the dispersing device is arranged so that its collision surface is located above the water surface in the aeration tank, and so that the water scattered from the collision surface falls into the aeration tank. It is as follows.
つまシ、処理水を分散具に衝突させて微細な水滴として
飛散させることによって、処理水中の溶解しなかったガ
スや活性汚泥に付着した窒素ガスや炭酸ガス等の気泡を
、処理水から十分に遊離できると共に、飛散に伴って水
滴表面からの十分な酸素吸収及び放熱を行わせることが
でき、その上、水滴の水面への衝突エネルギーを十分小
さくできる。By colliding the treated water with a dispersion tool and scattering it as fine water droplets, the undissolved gas in the treated water and bubbles of nitrogen gas, carbon dioxide gas, etc. attached to the activated sludge are thoroughly removed from the treated water. In addition to being able to release water, sufficient oxygen absorption and heat radiation from the water droplet surface can be performed as the water droplets scatter, and furthermore, the impact energy of the water droplets on the water surface can be sufficiently reduced.
したがって、余分な気泡の持込み及び水面でのガス巻込
みを十分に抑制して、曝気槽内での泡立ちを効果的に防
止でき、良好な運転を行えるようになった。Therefore, the introduction of excess air bubbles and the entrainment of gas on the water surface can be sufficiently suppressed, and bubbling in the aeration tank can be effectively prevented, allowing good operation.
また、水滴からの放熱によって、たとえ夏期に高濃廣有
機廃水を大量処理したとしても、曝気槽内の水温を、特
別な冷凍機を付設すること無く、40℃程度以下の活性
汚泥の活発な活動に好適な範囲に維持でき、良好な水処
理を低コストで81実に行えるようになった。In addition, by heat radiation from water droplets, even if a large amount of Kounohiro organic wastewater is treated in the summer, the water temperature in the aeration tank can be kept at around 40℃ or less without the need for a special refrigerator. It has become possible to maintain water within a range suitable for activities, and to perform good water treatment at low cost.
もちろん、酸素供給速度も十分に大きくでき、実験的に
確認したところ、循環水量l−当りの酸素吸収量が、従
来装置では0.08即であるに比して本発明装置でf″
i()、05)fとなり、むしろ酸素供給速度を一層増
大して、高負荷処理性能においても優れていることが判
った。 ・
要するに、高性能でトラブルが少く、さらに経済性に優
れた、全体として極めて優秀な曝気装置を提供できるよ
うになった。Of course, the oxygen supply rate can also be made sufficiently large, and it was experimentally confirmed that the amount of oxygen absorbed per liter of circulating water was 0.08 in the conventional device, whereas in the device of the present invention, the amount of oxygen absorbed per liter of circulating water was f″.
i(),05)f, and it was found that the oxygen supply rate was further increased and the high-load processing performance was also excellent. - In short, we have now been able to provide an extremely excellent overall aeration system that has high performance, fewer troubles, and is more economical.
次に、第1図によ#)実施例を示す。Next, an example will be shown in FIG.
密閉型曝気槽fi+の下部に吸込側を接続したポンプi
PI付管路(2)の吐出口(2a)を、曝気槽(11内
の水面6■上方に下向き配置し、流量調節弁M付吸気路
(3)からの外気を水流によって吸引するエゼクタ−(
4)を管路t21 K設け、曝気槽11+力為らの処理
水及び活性汚泥を、エゼクタ−(4)によって空気を混
入した状態で曝気槽(1)上部に揚送吐出するように構
成しである。Pump i with the suction side connected to the bottom of the closed aeration tank fi+
The discharge port (2a) of the pipe line (2) with PI is arranged downward above the water surface 6 in the aeration tank (11), and the ejector sucks the outside air from the intake line (3) with flow rate adjustment valve M by water flow. (
4) is provided in the pipe t21K, and the treated water and activated sludge from the aeration tank 11 + force are pumped and discharged to the upper part of the aeration tank (1) with air mixed in by the ejector (4). It is.
吐出口(2a)からの処理水を衝突させる分散共(5)
を、その衝突面(5a)が曝気槽f、11内の水面(資
)上刃に位置するように曝気槽11+内上部に配置し、
微細な水滴になった衝突面(5a)力為らの飛散水力(
曝気槽(1)内の水面側に分散落下するように構成し、
処理水の脱泡や冷却等を行えるようにしである。Dispersion cooperator (5) that collides the treated water from the discharge port (2a)
is arranged in the upper part of the aeration tank 11+ so that its collision surface (5a) is located at the upper blade of the water surface in the aeration tank f, 11,
Collision surface (5a) that has turned into minute water droplets Splashing water force (
It is configured so that it disperses and falls on the water surface side in the aeration tank (1),
This allows for defoaming and cooling of the treated water.
曝気槽fl+の上部に、外気導入路(6)及び杉ト風機
(7)付グクト(8)を接続して、臭気の脱臭処理や集
中放出を行えるようにしである。An outside air introduction path (6) and a gasket (8) with a cedar blower (7) are connected to the upper part of the aeration tank fl+, so that odor deodorization processing and concentrated release can be performed.
次に、別の実施例を示す。Next, another example will be shown.
曝気槽fi+を、第2図及び第5図に示すように上部開
放型に形成してもよい。The aeration tank fi+ may be formed into an open top type as shown in FIGS. 2 and 5.
管路(2)に供給するガスは、例えば酸素富化した空気
や純酸素、その他であってもよく、要するに酸素含有ガ
スであればよい。 また、第8図及び第4図に示すよう
に送圃機(9)で管w!I(21内に唆素含有ガスを押
込んでもよく、その他適当な給気構成を利用でき、それ
らを給気装置[41,telと総称する。The gas supplied to the pipe line (2) may be, for example, oxygen-enriched air, pure oxygen, or others, and in short, any gas containing oxygen may be used. In addition, as shown in Fig. 8 and Fig. 4, the farm feeder (9) is used to produce pipes w! The ion-containing gas may be forced into the air supply system [41, tel.
分散共(6)の配置や形状、その龍の構成を適宜変更で
き、例えば、第2図に示すように、分散共(5)を、そ
の全周に水滴を飛散するように曝気。The arrangement and shape of the disperser (6) and the configuration of its dragon can be changed as appropriate. For example, as shown in FIG. 2, the disperser (5) is aerated to scatter water droplets all around it.
槽(1)の中央側に配置したり、第8図及び第4図に示
すように、水面側全体に分散して水滴を落下させるよう
に、E向き吐出口(2a)の上方に分散具(5)を配置
したり、第4図及び第51ffiに示すように、水滴の
微細化を助長するように、分散J、f5+ヲモータ1M
で駆動回転されるものにする等が可能である。A dispersing device may be placed at the center of the tank (1), or above the E-direction outlet (2a) so that the water droplets are dispersed and dropped over the entire water surface, as shown in Figures 8 and 4. (5), dispersion J, f5 + motor 1M to promote the miniaturization of water droplets, as shown in Fig. 4 and 51ffi.
It is possible to use a device that is driven and rotated by a motor.
処理水は、し尿や高濃度有機件産業廃水、下水、その他
いかなるものでもよい。The treated water may be human waste, highly concentrated organic industrial wastewater, sewage, or any other source.
第1図は、本発明の実施例を示す概略断面図、第2図な
いし第5図は、本発明の各別の実施例を示す概略断面図
である。 @6図は従緊例の概略断面図である。
(1)・・・・・・曝気槽、(2)・・・・・・管路、
+411 +91・・・・・・給気装置、(6)・・・
・・・分散具、(5a)・・・・・・衝突面、(P)・
・・・・・ポンプ、醐水面。
代理人 弁理士 北 村 修
第1図
第2垣 阿3図FIG. 1 is a schematic cross-sectional view showing an embodiment of the present invention, and FIGS. 2 to 5 are schematic cross-sectional views showing different embodiments of the present invention. Figure @6 is a schematic cross-sectional view of a conventional example. (1)...Aeration tank, (2)...Pipe line,
+411 +91... Air supply device, (6)...
... Dispersion tool, (5a) ... Collision surface, (P)
...Pump, water surface. Agent Patent Attorney Osamu Kitamura Figure 1 Figure 2 Figure A3
Claims (1)
fil内の水面位上方に揚送吐出するポンプ(Pl付管
路(2)を設け、その管路(2)に酸素含有ガスを供給
する給気装置+41 ’、 191を設けた曝気装置で
あって、前記管路(2)から吐出される処理水を衝突さ
せる分散具(6)を、その衝突面(5a)が前記曝気槽
[11内の水面(イ)上方に位置するように、かつ、そ
の衝突面(5a)からの飛散水がその曝気槽(1)内に
落下するように配置しである水処理用曝気装置。 ■ 前記分散具(6)が駆動回転されるものである特許
請求の範囲第0項に記載の装置。[Claims] ■ A pump (pipe line (2) with Pl is provided, which pumps and discharges the treated water and activated sludge in the aeration tank +11 above the water level in the aeration tank fil, and the pipe line (2) The aeration device is equipped with an air supply device +41', 191 for supplying oxygen-containing gas to the pipe line (2), and a dispersion device (6) for colliding the treated water discharged from the pipe (2) with its colliding surface (5a). ) is located above the water surface (a) in the aeration tank [11], and the water splashed from the collision surface (5a) falls into the aeration tank (1). Aeration device for treatment. (1) The device according to claim 0, wherein the dispersing tool (6) is driven and rotated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59049884A JPS60193592A (en) | 1984-03-14 | 1984-03-14 | Aeration apparatus for water treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59049884A JPS60193592A (en) | 1984-03-14 | 1984-03-14 | Aeration apparatus for water treatment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60193592A true JPS60193592A (en) | 1985-10-02 |
Family
ID=12843461
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59049884A Pending JPS60193592A (en) | 1984-03-14 | 1984-03-14 | Aeration apparatus for water treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60193592A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01114099U (en) * | 1988-01-29 | 1989-08-01 | ||
KR100363199B1 (en) * | 2000-04-20 | 2002-12-05 | 주식회사 태백종합환경기술단 | mixed oxygen supply device and agitator of using injector |
KR102019195B1 (en) * | 2018-05-29 | 2019-09-06 | 창원환경산업 주식회사 | Apparatus for on-site treating night soil in vessels |
KR102026130B1 (en) * | 2018-11-08 | 2019-09-27 | 주식회사 호두 | Wastewater treatment apparatus for ships |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS541096B2 (en) * | 1975-05-19 | 1979-01-20 | ||
JPS5725797B2 (en) * | 1977-03-18 | 1982-06-01 |
-
1984
- 1984-03-14 JP JP59049884A patent/JPS60193592A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS541096B2 (en) * | 1975-05-19 | 1979-01-20 | ||
JPS5725797B2 (en) * | 1977-03-18 | 1982-06-01 |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01114099U (en) * | 1988-01-29 | 1989-08-01 | ||
KR100363199B1 (en) * | 2000-04-20 | 2002-12-05 | 주식회사 태백종합환경기술단 | mixed oxygen supply device and agitator of using injector |
KR102019195B1 (en) * | 2018-05-29 | 2019-09-06 | 창원환경산업 주식회사 | Apparatus for on-site treating night soil in vessels |
KR102026130B1 (en) * | 2018-11-08 | 2019-09-27 | 주식회사 호두 | Wastewater treatment apparatus for ships |
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