JPS6216157B2 - - Google Patents
Info
- Publication number
- JPS6216157B2 JPS6216157B2 JP55091911A JP9191180A JPS6216157B2 JP S6216157 B2 JPS6216157 B2 JP S6216157B2 JP 55091911 A JP55091911 A JP 55091911A JP 9191180 A JP9191180 A JP 9191180A JP S6216157 B2 JPS6216157 B2 JP S6216157B2
- Authority
- JP
- Japan
- Prior art keywords
- cylindrical body
- water
- aeration device
- conical lid
- deep water
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
- B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
- B01F23/23231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
- B01F23/232311—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit the conduits being vertical draft pipes with a lower intake end and an upper exit end
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/45—Mixing liquids with liquids; Emulsifying using flow mixing
- B01F23/454—Mixing liquids with liquids; Emulsifying using flow mixing by injecting a mixture of liquid and gas
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
【発明の詳細な説明】
本発明はダム又は湖沼などの水深部の水質を改
善することを目的とした水深部ばつ気装置に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a deep water aeration device for the purpose of improving water quality in deep water areas such as dams or lakes.
従来湖沼の水質改善については、水中に直立設
置した筒体内へ、加圧空気を間欠的に吹き出すこ
とにより水中に上下方向の対流を発生させ、水面
付近の水を深部に導いて全体の容存酸素量を増大
させる方法(特許第499563号)、水底に敷設した
パイプに設けた多数の小孔から空気を噴出せる方
法又は深部より汲み上げた水を水面上へ撒布する
方法などが知られている。前記加圧空気による対
流方法は有効であるけれども、水中の浅層又ま深
層に限定されることはなく、全体に対流を発生さ
せるので、比較的水深の大きい湖沼において、深
水層を形成する場合に、深水層のみの水質改善に
ついては最良とはいゝ難い。また水底に敷設した
パイプから微細気泡を噴出させる方法又はポンプ
で汲み上げた水を水面上で撒布する方法は、比較
的水量の少ない例えば貯水槽などにおける水質改
善には有効であるとしても水量の著しく多い湖沼
又はダムなどにおいては厖大な設備費を要し、実
用性がきわめて低いという問題点があつた。然し
て比較的水深の大きい湖沼又はダムなどにおいて
水底全域に気泡発生パイプを敷設することは実用
上不可能であり、水深変動のある湖沼又はダムに
おいては、水を汲み上げて水面上に撒布する方法
は事実上採用し難いものである。 Conventionally, water quality in lakes and marshes has been improved by intermittently blowing pressurized air into a cylinder placed vertically in the water to generate vertical convection in the water, guiding water near the surface to the depths and improving overall storage capacity. Known methods include increasing the amount of oxygen (Patent No. 499563), blowing out air from a number of small holes in pipes laid on the bottom of the water, and spraying water pumped from deep onto the surface of the water. . Although the above-mentioned convection method using pressurized air is effective, it is not limited to shallow or deep underwater layers, and convection is generated throughout the water, so it is useful when forming deep water layers in lakes and marshes with relatively large water depths. Furthermore, it is difficult to say that it is the best method for improving water quality only in the deep water layer. Furthermore, although methods of ejecting microbubbles from pipes laid at the bottom of the water or methods of sprinkling pumped water on the water surface are effective for improving water quality in relatively small amounts of water, such as water storage tanks, The problem was that it required huge equipment costs and was extremely impractical in areas where there were many lakes or dams. However, in lakes and dams with relatively large water depths, it is practically impossible to lay a bubble generating pipe over the entire water bottom, and in lakes and dams where the water depth fluctuates, there is no method to pump up water and sprinkle it on the water surface. In fact, it is difficult to adopt.
然るに本発明は水中へ鉛直に設置した筒体の下
部から微細気泡を噴出させ、前記筒体の下側部か
ら流入する水と気泡とを混合させると共、筒体の
上部において気液分離を行い、筒体の側方(水平
方向)へ水を放出し、上方へ空気を放出するよう
に構成したので、所望の深度で横方向に広範囲に
亘り対流を生起させることができる。従つて著し
く単純かつ小設備で所望の水深以下における水質
を効率よく改善することに成功し、前記従来の問
題点を解決したのである。然して前記筒体中へ適
量の微粒子凝集剤を注入することによつて、深水
層に浮遊する微粒固形物を団粒化して沈降させ、
濁水処理を行うことができるなど、従来著しく困
難とされていたダム底付近における濁水層の改善
も可能にしたのである。 However, in the present invention, fine air bubbles are ejected from the lower part of a cylinder installed vertically into water, and the air bubbles are mixed with water flowing in from the lower side of the cylinder, and gas-liquid separation is performed at the upper part of the cylinder. Since the structure is configured to release water to the sides (horizontal direction) of the cylinder and release air upward, convection can be generated over a wide range in the lateral direction at a desired depth. Therefore, it was possible to efficiently improve the water quality below a desired water depth with extremely simple and small equipment, and the above-mentioned conventional problems were solved. By injecting an appropriate amount of particulate flocculant into the cylinder, the particulate solids floating in the deep water layer are aggregated and settled,
It has also made it possible to treat turbid water and improve the turbid water layer near the bottom of a dam, which was previously considered extremely difficult.
即ち本発明を実施例について説明すれば、合成
樹脂製又は金属製の有底円筒体1の底板2より若
干上部に、多孔性の仕切盤3を設けて空気室4を
形成し、空気室4はコンプレツサー5と送気ホー
ス6で連結する。前記空気室4の上部の円筒体1
の側壁には、下方の水を流入させる流入パイプ7
の基部が連結してある。前記円筒体1の上端部に
は環状鍔8を水平に張出して設け、環状鍔8の上
方には小間隙9において、円錐蓋10の周縁を対
向させ、円錐蓋10の中央部には萩気パイプ11
の基部を連結し、円錐蓋10の内側であつて、前
記円筒体の上方には弧状の阻流板12を設けてあ
る。前記排気パイプ11の周囲には浮子13を固
定し、円筒体1の下端には鎖体14を介して重錘
15を連結したものである。前記実施例において
は、円筒体および円錐蓋を用いたが、角筒体およ
び角錐蓋でもよいことは勿論である。また下方の
水の流入については必ずしも流入パイプ7を必要
としない。例えば円筒体の側壁へ単に流入口を穿
設することもできる。更に環状鍔8を水平に設け
ることなく、テーパー状(斜上向又は下向)に設
けたり、又は環状鍔8を設けない場合も考えられ
る。前記阻流板12は、上昇混合流体(水と空気
の混合)を受けて方向変換させ、側方流動力を付
与すると共に、気液の分離を容易にさせる為に設
けたものであつて、一枚に限定されることなく、
複数枚の阻流板に小間隙を介し鱗状に配置するこ
ともできる。また阻流板12をパンチングメタル
板又は網板として気液分離を更に有効にすること
もできる。 That is, to explain the present invention with reference to an embodiment, a porous partition plate 3 is provided slightly above the bottom plate 2 of a bottomed cylindrical body 1 made of synthetic resin or metal to form an air chamber 4. is connected to the compressor 5 by an air supply hose 6. Cylindrical body 1 in the upper part of the air chamber 4
An inflow pipe 7 for introducing water from below is provided on the side wall of the
The bases of the two are connected. An annular flange 8 is provided horizontally extending from the upper end of the cylindrical body 1. Above the annular flange 8, a small gap 9 is provided between the circumferential edges of a conical lid 10 to face each other. pipe 11
An arc-shaped baffle plate 12 is provided inside the conical lid 10 and above the cylindrical body. A float 13 is fixed around the exhaust pipe 11, and a weight 15 is connected to the lower end of the cylindrical body 1 via a chain body 14. In the above embodiment, a cylindrical body and a conical lid were used, but it goes without saying that a prismatic cylinder and a pyramidal lid may also be used. Furthermore, the inflow pipe 7 is not necessarily required for the inflow of water from below. For example, it is also possible to simply drill an inlet into the side wall of the cylinder. Furthermore, it is also conceivable that the annular collar 8 is not provided horizontally but in a tapered shape (diagonally upward or downward), or that the annular collar 8 is not provided. The baffle plate 12 is provided to receive and change the direction of the rising mixed fluid (mixture of water and air), apply lateral flow force, and facilitate separation of gas and liquid. Not limited to one piece,
It is also possible to arrange a plurality of baffle plates in a scale-like manner with small gaps between them. Further, the baffle plate 12 may be a punched metal plate or a mesh plate to further enhance gas-liquid separation.
次に第2図の実施例は、円筒体1の流入パイプ
連結部の上部へ凝集剤流入用の注入パイプ16を
直径的に設置したもので、注入パイプ16の一端
は送液ホース17を介してポンプ18と連結して
ある。前記各実施例の装置は、例えばムダ19の
深水層20内へ設置する。前記各実施例におい
て、円錐蓋に排気パイプを連設したが、排気パイ
プによることなく、複数の排気口を設けてもよい
ことは勿論である。上記における円錐蓋は放出水
の上昇を防止すると共に、気液を分離することを
目的としたものである。従つてこの目的に合致す
る範囲において錐状蓋を適宜設計することは当然
考えられる所である。 Next, in the embodiment shown in FIG. 2, an injection pipe 16 for coagulant inflow is diametrically installed at the upper part of the inflow pipe connection part of the cylindrical body 1, and one end of the injection pipe 16 is connected via a liquid feeding hose 17. and is connected to the pump 18. The apparatus of each of the embodiments described above is installed, for example, in the deep water layer 20 of the waste 19. In each of the embodiments described above, an exhaust pipe is connected to the conical lid, but it goes without saying that a plurality of exhaust ports may be provided instead of using an exhaust pipe. The conical lid mentioned above is intended to prevent the discharged water from rising and to separate gas and liquid. Therefore, it is natural to design the conical lid appropriately within a range that meets this purpose.
第1および第4図の状態において送気ホース6
により空気室4内へ加圧空気を送入すれば、空気
室4内の気圧上昇により仕切盤3の細孔から矢示
21のように小気泡が上昇するので、これにつれ
て流入パイプ7の下端からも矢示22のように下
方の水を吸い上げ、気泡と共に筒体内を矢示23
のように上昇する。この場合に気泡は微細である
から、気泡中の酸素は可及的に水中へ溶解し、混
合する。前記のようにして上昇した気液混合物は
阻流板12に衝突し、矢示24のように側方へ流
動する。一方分離された気泡は円錐蓋10の下面
に付着し、又はそのまゝ浮上して排気パイプ11
から矢示25のように上昇し水面外へ排出され
る。前記のようにして側方へ流動した水は暫く深
水層上面に近い付近を矢示26のように流動した
後沈降し、矢示27,28のように環流すること
になる。何故ならば、円筒内を上昇した水の水温
は深水層上部の水温より若干低いが、矢示26の
ように放出されると、放出付近の水と混合して、
その水温差が小さくなるので、比重差による沈降
が緩慢となり、放出直後その直下に沈降するおそ
れはない。従つて比較的水平方向流動距離が長く
なり、環流範囲が拡大される。また第2図の実施
例のように凝集剤(例えば硫酸ばん土又は高分子
凝集剤)を注入すると、円筒体内で或程度混合し
たまゝ円筒体の上部から側方へ放出される為に、
前記深水層中に拡散することになる。従つて深水
層内の固形微粒子が団粒化し、濁水は環流中に固
液比重分離が行われ、濁水を処理することができ
る。 Air supply hose 6 in the state shown in Figs. 1 and 4
When pressurized air is fed into the air chamber 4, small air bubbles rise from the pores of the partition panel 3 as shown by the arrow 21 due to the rise in the air pressure inside the air chamber 4, so that the lower end of the inflow pipe 7 The water is sucked up from below as shown by arrow 22, and the water flows inside the cylinder along with air bubbles as shown by arrow 23.
rise like. In this case, since the bubbles are fine, the oxygen in the bubbles dissolves and mixes into the water as much as possible. The gas-liquid mixture that has risen as described above collides with the baffle plate 12 and flows laterally as shown by the arrow 24. On the other hand, the separated air bubbles adhere to the lower surface of the conical lid 10 or float up as they are to the exhaust pipe 11.
From there, it rises as shown by arrow 25 and is discharged out of the water. The water that has flowed laterally as described above flows for a while near the upper surface of the deep water layer as shown by arrow 26, then settles and flows back as shown by arrows 27 and 28. This is because the temperature of the water that has risen inside the cylinder is slightly lower than the water temperature at the top of the deep water layer, but when it is released as shown by arrow 26, it mixes with the water near the release.
Since the difference in water temperature becomes smaller, sedimentation due to the difference in specific gravity becomes slower, and there is no risk of sedimentation directly below the water immediately after release. Therefore, the horizontal flow distance is relatively long, and the reflux range is expanded. In addition, when a flocculant (for example, sulfuric acid salt or polymer flocculant) is injected as in the embodiment shown in Fig. 2, the flocculant remains mixed to some extent within the cylinder and is released laterally from the top of the cylinder.
It will diffuse into the deep water layer. Therefore, the solid particles in the deep water layer are aggregated, and the turbid water undergoes solid-liquid specific gravity separation during reflux, allowing the turbid water to be treated.
即ち本発明によれば、深水層内へ鉛直筒体の下
部より微気泡を上昇させ、筒体の下部より吸入し
た水に気泡を混入させながら上昇させ、筒体上部
で気液分離して側方へ放出するので、筒体を深水
層へ設置すれば、該部において比較的広範囲に亘
つて対流を生起し、深水層中に空気中の酸素を溶
出して該部の溶存酸素量を好適に調節する効果が
ある。また凝集剤を注入することもできるので、
深部に生じた濁水層を効率よく改善し得る効果も
ある。然して筒体と、送気装置と、気泡発生装置
と気液分離装置を連結したもので、水中設置部に
動力装置は皆無であるから故障のおそれなく、長
く同一効率で連続運転し得る効果もある。 That is, according to the present invention, microbubbles are allowed to rise into the deep water layer from the lower part of the vertical cylinder, and the bubbles are mixed with the water sucked in from the bottom of the cylinder, and the air and liquid are separated at the upper part of the cylinder. Therefore, if the cylinder is installed in the deep water layer, convection will occur over a relatively wide area in the deep water layer, eluting oxygen from the air into the deep water layer and adjusting the amount of dissolved oxygen in the area to an appropriate level. It has the effect of adjusting. It is also possible to inject a flocculant, so
It also has the effect of efficiently improving the turbid water layer that has formed deep within. However, since the cylinder body, air supply device, bubble generator, and gas-liquid separation device are connected, there is no power unit installed in the underwater installation part, so there is no risk of failure and it is possible to operate continuously with the same efficiency for a long time. be.
第1図は本発明の実施例の設置状態における一
部断面した正面図、第2図は同じく他の実施例の
一部を断面した正面図、第3図は同じく第1図中
A―A断面図、第4図は同じく本発明の装置をダ
ムに設置した際の正面図である。
1……円筒体、3……仕切盤、4……空気室、
5……コンプレツサー、6……送気ホース、7…
…流入パイプ、8……環状鍔、10……円錐蓋、
11……排気パイプ、12……阻流板、13……
浮子、15……重錘、16……注入パイプ、17
……送液ホース、18……ポンプ、19……ダ
ム、20……深水層。
Fig. 1 is a partially sectional front view of an embodiment of the present invention in an installed state, Fig. 2 is a partially sectional front view of another embodiment, and Fig. 3 is the same as A-A in Fig. 1. The sectional view and FIG. 4 are also front views when the device of the present invention is installed in a dam. 1... Cylindrical body, 3... Partition board, 4... Air chamber,
5...Compressor, 6...Air supply hose, 7...
... Inflow pipe, 8 ... Annular collar, 10 ... Conical lid,
11...Exhaust pipe, 12...Break plate, 13...
Float, 15... Weight, 16... Injection pipe, 17
...Liquid supply hose, 18...Pump, 19...Dam, 20...Deep water layer.
Claims (1)
して空気室を設け、空気室へ送気ホースを連設
し、前記筒体の下部側壁へ流入口が設けてあり、
前記筒体の上方へ所定の間隙を介して錐状蓋を被
冠し、錐状蓋には排気口を設け、前記筒体の上方
に浮子を固定し、下方に重錘を固定したことを特
徴とする水深部ばつ気装置。 2 錐状蓋は円錐状又は角錐状であつてその下部
内側へ凸弧状の阻流板を設けたことを特徴とする
特許請求の範囲第1項記載の水深部ばつ気装置。 3 仕切盤は多数の並列小孔を密接して設けた陶
器製又は合成樹脂製としたことを特徴とする特許
請求の範囲第1項記載の水深部ばつ気装置。 4 錐状蓋に浮子を固定し、筒体の下端に重錘を
固定して筒体を水中へ鉛直に設置した特許請求の
範囲第1項記載の水深部ばつ気装置。 5 筒体の下部に小孔を有する仕切盤を介して空
気室を設け、空気室へ加圧空気の供給ホースを連
設し、前記筒体の下部側壁へ流入パイプが連結し
てあり、前記筒体の上部外側へ環状鍔を設けると
共に、環状鍔の上方へ所定の間隔を介して錐状蓋
を被冠し、錐状蓋へ排気口を連設し、筒体の上方
に浮子を固定し、下方に重錘を固定し、前記筒体
の下部内側へ薬剤注入パイプを設置し、前記薬剤
注入パイプを薬剤ホースと連結したことを特徴と
する水深部ばつ気装置。 6 薬剤注入パイプは、流入パイプの流入口より
若干上方の筒体内へ直径的に横架し、その上側壁
に多数の透孔を設けたことを特徴とする特許請求
の範囲第5項記載の水深部ばつ気装置。 7 流入パイブは凸弧状に湾曲させ、その下端は
下向とした特許請求の範囲第6項記載の水深部ば
つ気装置。[Claims] 1. An air chamber is provided in the lower part of the cylindrical body through a partition panel having a large number of small holes, an air supply hose is connected to the air chamber, and an inlet is provided in the lower side wall of the cylindrical body. There is,
A conical lid is placed above the cylindrical body through a predetermined gap, an exhaust port is provided in the conical lid, a float is fixed above the cylindrical body, and a weight is fixed below. Features a deep water aeration device. 2. The deep water aeration device according to claim 1, wherein the conical lid has a conical or pyramidal shape, and a convex arc-shaped baffle plate is provided inside the lower part of the conical lid. 3. The deep water aeration device according to claim 1, wherein the partition panel is made of ceramic or synthetic resin and has a large number of parallel small holes arranged closely together. 4. The deep-water aeration device according to claim 1, wherein a float is fixed to the conical lid, a weight is fixed to the lower end of the cylindrical body, and the cylindrical body is installed vertically into the water. 5. An air chamber is provided in the lower part of the cylindrical body through a partition panel having small holes, a pressurized air supply hose is connected to the air chamber, and an inflow pipe is connected to the lower side wall of the cylindrical body, An annular flange is provided on the outside of the upper part of the cylindrical body, a conical lid is placed above the annular flange at a predetermined interval, an exhaust port is connected to the conical lid, and a float is fixed above the cylindrical body. A deep water aeration device characterized in that a weight is fixed below, a drug injection pipe is installed inside the lower part of the cylindrical body, and the drug injection pipe is connected to a drug hose. 6. The drug injection pipe according to claim 5, wherein the drug injection pipe is diametrically suspended in a cylindrical body slightly above the inlet of the inflow pipe, and has a large number of through holes in its upper wall. Deep water aeration device. 7. The deep water aeration device according to claim 6, wherein the inflow pipe is curved into a convex arc shape, and the lower end thereof is directed downward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9191180A JPS5719093A (en) | 1980-07-04 | 1980-07-04 | Deep-layer aerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9191180A JPS5719093A (en) | 1980-07-04 | 1980-07-04 | Deep-layer aerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5719093A JPS5719093A (en) | 1982-02-01 |
| JPS6216157B2 true JPS6216157B2 (en) | 1987-04-10 |
Family
ID=14039756
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9191180A Granted JPS5719093A (en) | 1980-07-04 | 1980-07-04 | Deep-layer aerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5719093A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4747006B2 (en) * | 2006-03-02 | 2011-08-10 | 独立行政法人水資源機構 | Submerged combined aeration equipment |
| JP4866777B2 (en) * | 2007-04-23 | 2012-02-01 | 独立行政法人水資源機構 | Submerged combined aeration equipment |
| JP5296565B2 (en) * | 2009-01-28 | 2013-09-25 | 株式会社 米崎 | Stirrer |
| JP5296646B2 (en) * | 2009-09-15 | 2013-09-25 | 株式会社 米崎 | Stirring device having an air lift pump |
| JP5597496B2 (en) * | 2010-09-16 | 2014-10-01 | 株式会社丸島アクアシステム | Deep aeration equipment |
| JP6402023B2 (en) * | 2014-12-17 | 2018-10-10 | 東亜建設工業株式会社 | Air lift pump device and method for removing contaminants in water |
| JP6604676B1 (en) * | 2019-01-11 | 2019-11-13 | 株式会社アクアトリム | Waterway device |
-
1980
- 1980-07-04 JP JP9191180A patent/JPS5719093A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5719093A (en) | 1982-02-01 |
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