JPS638467Y2 - - Google Patents
Info
- Publication number
- JPS638467Y2 JPS638467Y2 JP1982175324U JP17532482U JPS638467Y2 JP S638467 Y2 JPS638467 Y2 JP S638467Y2 JP 1982175324 U JP1982175324 U JP 1982175324U JP 17532482 U JP17532482 U JP 17532482U JP S638467 Y2 JPS638467 Y2 JP S638467Y2
- Authority
- JP
- Japan
- Prior art keywords
- waterway
- aerator
- wall
- flow
- wastewater treatment
- 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
Links
- 238000005276 aerator Methods 0.000 claims description 19
- 238000004065 wastewater treatment Methods 0.000 claims description 10
- 238000005273 aeration Methods 0.000 description 6
- 238000005192 partition Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
Description
【考案の詳細な説明】
本考案は循環水路式排水処理装置に関し、詳し
くは、整流板により曝気水路の偏流を矯正した循
環水路式排水処理装置に関する。[Detailed Description of the Invention] The present invention relates to a circulating waterway type wastewater treatment device, and more particularly, to a circulating waterway type wastewater treatment device in which the uneven flow of an aeration channel is corrected by a rectifying plate.
たとえば、第1図および第2図に示すように、
循環水路式曝気槽11の中央長手方向に水路内壁
(仕切壁)13を設け、この内壁13の両側で流
れ方向が反対となるように循環曝気水路を形成
し、下水、汚水などの排水を曝気処理する循環水
路式排水処理装置が従来から知られている。縦軸
エアレータ15は水路内の混合液に酸素を供給す
る他に、水路内の混合液に流れを生じせしめ、混
合、撹拌する役割を果たすものである。 For example, as shown in Figures 1 and 2,
A waterway inner wall (partition wall) 13 is provided in the central longitudinal direction of the circulation waterway type aeration tank 11, and a circulation aeration waterway is formed so that the flow direction is opposite on both sides of this inner wall 13, and wastewater such as sewage and sewage is aerated. Circulating waterway type wastewater treatment devices have been known for a long time. The vertical aerator 15 serves not only to supply oxygen to the mixed liquid in the water channel but also to create a flow in the mixed liquid in the water channel, thereby mixing and agitating the mixed liquid in the water channel.
しかしながら、従来の循環水路式排水処理装置
では、第1図に水流を矢印で示すように、水路内
に均等かつ十分な流れを生じさせられないという
点で問題を残していた。すなわち、エアレータ1
5の回転速度を大きくすればする程、外壁11側
の流速のみが卓越する偏流傾向が強まる。他方、
中央壁(仕切壁)13寄りはむしろ流れが停滞あ
るいは逆流する現象がみられ、その結果、中央壁
底部に汚泥等の堆積が生じやすくなる欠点を有し
ていた。 However, the conventional circulating waterway type wastewater treatment apparatus has a problem in that it is not possible to generate an even and sufficient flow in the waterway, as shown by the arrows in FIG. That is, aerator 1
The higher the rotational speed of the outer wall 11, the stronger the tendency for the flow to be uneven, where only the flow velocity on the outer wall 11 side is predominant. On the other hand,
On the contrary, near the center wall (partition wall) 13, the flow stagnates or flows backwards, which has the disadvantage that sludge and the like tend to accumulate at the bottom of the center wall.
本考案は、上記の如き従来技術の欠点を解消す
るためになされたものであり、曝気水路における
偏流を矯正し、水路底部への汚泥等の堆積を防止
することのできる排水処理装置を提供することを
目的とする。 The present invention has been made in order to eliminate the above-mentioned drawbacks of the conventional technology, and provides a wastewater treatment device that can correct the unbalanced flow in the aeration waterway and prevent the accumulation of sludge and the like on the bottom of the waterway. The purpose is to
そこで、本考案は、縦軸エアレータを備えた循
環水路式排水処理装置において、該エアレータの
流出水路側の近傍に、該エアレータから流出水路
外壁方向に押し出される流れを受けて該水路内壁
方向に向けるように1または複数の整流板を配設
したことを特徴とする。 Therefore, the present invention provides a circulating waterway type wastewater treatment device equipped with a vertical aerator, in which a flow pushed out from the aerator toward the outer wall of the waterway is directed toward the inner wall of the waterway in the vicinity of the outflow waterway side of the aerator. It is characterized by disposing one or more rectifying plates as shown in FIG.
以下、本考案の一実施例について第3図および
第4図を参照して説明する。 An embodiment of the present invention will be described below with reference to FIGS. 3 and 4.
第3図は縦軸エアレータ15付近の一部平面
図、第4図はその断面図である。ここでは曝気水
路の流出水路側12aであつて縦軸エアレータ1
5の近傍に整流板17が、縦軸エアレータ15か
ら押し出される流れ(図中、点線で示した)を水
路内壁(仕切壁)13に向けるように配設されて
いる。このように整流板17はエアレータにより
押し出され外壁11へ向う流れを内側へそらすも
のであるので、エアレータ15の近傍に設けら
れ、好ましくは流出水路12bのほぼ中央であつ
て、エアレータ15との距離は整流板17のエア
レータ側端部がエアレータ直径(φ1)の1〜3
倍となるような位置に設けられる。また、整流板
17としては、幅0.5φ〜1.0φで高さがほぼ水路水
深に等しい程度のものが好ましい。 FIG. 3 is a partial plan view of the vicinity of the vertical axis aerator 15, and FIG. 4 is a sectional view thereof. Here, it is the outflow channel side 12a of the aeration channel, and the vertical axis aerator 1
A rectifying plate 17 is disposed near the vertical aerator 15 so as to direct the flow (indicated by dotted lines in the figure) from the vertical aerator 15 toward the inner wall (partition wall) 13 of the water channel. In this way, the rectifier plate 17 deflects the flow pushed out by the aerator toward the outer wall 11 inward, so it is provided near the aerator 15, preferably at approximately the center of the outflow channel 12b, and at a distance from the aerator 15. The aerator side end of the rectifier plate 17 is 1 to 3 of the aerator diameter (φ 1 ).
It is placed in such a position that it doubles. Further, the current plate 17 preferably has a width of 0.5φ to 1.0φ and a height approximately equal to the water depth of the channel.
第3図および第4図に示した実施例では、軸受
などにより回動自在に枢支された軸19に、鋼鉄
製あるいはその他の材料からなる平板の整流板1
7が取り付けられ、整流板17は方向指定レバー
21により任意の方向に回動させ(第3図中、矢
印←→で示してある。)レバー21を固定すること
により角度設定ができるようになつている。この
ような可動整流板を用いることにより、現場の状
況に即応して整流板の傾きを設定し内壁方向の流
量を増加させることができるが、勿論、整流板は
固定式のものでもよい。 In the embodiment shown in FIGS. 3 and 4, a flat rectifying plate 1 made of steel or other material is attached to a shaft 19 rotatably supported by a bearing or the like.
7 is attached, and the rectifying plate 17 can be rotated in any direction using the direction specifying lever 21 (indicated by the arrow ←→ in FIG. 3). By fixing the lever 21, the angle can be set. ing. By using such a movable current plate, the inclination of the current plate can be immediately set in response to the situation at the site, and the flow rate toward the inner wall can be increased, but of course, the current plate may be of a fixed type.
また、第5図に示すように、複数の整流板17
a,17b,17cを設けてもよい。 Further, as shown in FIG. 5, a plurality of rectifier plates 17
a, 17b, and 17c may be provided.
本考案によれば、エアレータから外壁に向かつ
て押し出された水量の一部(典型的には1/5〜1/3
程度)が整流板により受けとめられ、水路中央よ
り内側へとそらされる。その結果、水路断面にお
ける流速分布が均一化し、特に循環槽の中央分離
壁寄りの流速を増大することができる。たとえば
本考案者らの実験によれば、第3図に示した可動
整流板を用いることにより外壁へ向かう流れの1/
5〜1/3を受けとめたところ、整流板を用いなかつ
た場合には10cm/秒であつた中央分離壁寄りの流
れが倍以上に速くなり、その付近の底部への汚泥
の沈積を防止する結果が得られた。 According to the present invention, a portion (typically 1/5 to 1/3
degree) is received by the current plate and deflected inward from the center of the waterway. As a result, the flow velocity distribution in the cross section of the water channel becomes uniform, and the flow velocity near the central separation wall of the circulation tank can be increased in particular. For example, according to experiments conducted by the present inventors, by using the movable rectifying plate shown in Figure 3, 1/2 of the flow toward the outer wall can be reduced.
When 5 to 1/3 of the amount was received, the flow toward the central separation wall, which was 10 cm/sec when no current plate was used, became more than twice as fast, preventing sludge from depositing on the bottom near that area. The results were obtained.
第1図は循環水路式排水処理装置について示す
平面図、第2図はその縦断面図である。第3図お
よび第5図は本考案の循環水路式排水処理装置の
エアレータ付近の一部拡大図であり、第4図は第
3図に係る断面図である。
10……循環水路式曝気槽、11……水路外
壁、13……水路内壁(仕切壁)、15……(縦
軸)エアレータ、17,17a,17b,17c
……整流板。
FIG. 1 is a plan view of a circulating waterway type wastewater treatment device, and FIG. 2 is a longitudinal sectional view thereof. 3 and 5 are partially enlarged views of the vicinity of the aerator of the circulating waterway type wastewater treatment apparatus of the present invention, and FIG. 4 is a sectional view of FIG. 3. 10... Circulating waterway type aeration tank, 11... Waterway outer wall, 13... Waterway inner wall (partition wall), 15... (vertical axis) aerator, 17, 17a, 17b, 17c
……rectifier.
Claims (1)
置において、該エアレータの流出水路側の近傍
に、該エアレータから流出水路外壁方向に押し出
される流れを受けて該水路内壁方向に向けるよう
に1または複数の整流板を配設したことを特徴と
する循環水路式排水処理装置。 In a circulating waterway type wastewater treatment device equipped with a vertical axis aerator, one or more are installed near the outflow waterway side of the aerator so as to receive the flow pushed out from the aerator toward the outer wall of the outflow waterway and direct it toward the inner wall of the waterway. A circulating waterway type wastewater treatment device characterized by a rectifying plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982175324U JPS5979294U (en) | 1982-11-19 | 1982-11-19 | Circulating waterway type wastewater treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982175324U JPS5979294U (en) | 1982-11-19 | 1982-11-19 | Circulating waterway type wastewater treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5979294U JPS5979294U (en) | 1984-05-29 |
JPS638467Y2 true JPS638467Y2 (en) | 1988-03-14 |
Family
ID=30381465
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1982175324U Granted JPS5979294U (en) | 1982-11-19 | 1982-11-19 | Circulating waterway type wastewater treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5979294U (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0790236B2 (en) * | 1988-12-28 | 1995-10-04 | 日立機電工業株式会社 | Uniform mixed aeration method for aeration tank consisting of double circular circulation channels |
JPH0763709B2 (en) * | 1988-12-28 | 1995-07-12 | 日立機電工業 株式会社 | A uniform mixing aerator for aeration tank consisting of double circular circulation channels |
JPH0677746B2 (en) * | 1989-12-11 | 1994-10-05 | 日立機電工業株式会社 | Operating method of agitator and aerator in endless waterway |
JP5223687B2 (en) | 2009-01-09 | 2013-06-26 | ソニー株式会社 | Stereoscopic glasses |
JP5839439B2 (en) * | 2011-02-01 | 2016-01-06 | 住友重機械エンバイロメント株式会社 | Impeller guide plate and aeration stirrer |
JP2019005728A (en) * | 2017-06-28 | 2019-01-17 | オルガノ株式会社 | Aeration agitating device and oxidation ditch |
-
1982
- 1982-11-19 JP JP1982175324U patent/JPS5979294U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5979294U (en) | 1984-05-29 |
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