JPH0131957B2 - - Google Patents

Info

Publication number
JPH0131957B2
JPH0131957B2 JP61095961A JP9596186A JPH0131957B2 JP H0131957 B2 JPH0131957 B2 JP H0131957B2 JP 61095961 A JP61095961 A JP 61095961A JP 9596186 A JP9596186 A JP 9596186A JP H0131957 B2 JPH0131957 B2 JP H0131957B2
Authority
JP
Japan
Prior art keywords
air
opening
discharge
discharge port
slide gate
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
Application number
JP61095961A
Other languages
Japanese (ja)
Other versions
JPS62250996A (en
Inventor
Ryoji Suzuki
Masatsugu Yamada
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dengyosha Machine Works Ltd
Original Assignee
Dengyosha Machine Works Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dengyosha Machine Works Ltd filed Critical Dengyosha Machine Works Ltd
Priority to JP61095961A priority Critical patent/JPS62250996A/en
Publication of JPS62250996A publication Critical patent/JPS62250996A/en
Publication of JPH0131957B2 publication Critical patent/JPH0131957B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2336Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer
    • B01F23/23362Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer the gas being introduced under the stirrer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2334Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer
    • B01F23/23341Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer with tubes surrounding the stirrer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/25Mixers with both stirrer and drive unit submerged in the material being mixed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/112Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
    • B01F27/1125Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、汚水処理施設における撹拌曝気によ
る好気性処理および低速撹拌による嫌気性処理の
双方に性能を切り換えて使用することのできる水
中撹拌装置に関するものである。
Detailed Description of the Invention (Field of Industrial Application) The present invention provides an underwater stirring device that can be used for both aerobic treatment using stirring aeration and anaerobic treatment using low-speed stirring in sewage treatment facilities, with the performance switched. It is related to.

(従来の技術) 近年、小規模汚水処理方式の1つとして回分式
活性汚泥処理法が脚光を浴びつつある。この処理
方法は、次の4つの工程を1つのサイクルとして
いる。
(Prior Art) In recent years, a batch activated sludge treatment method has been attracting attention as one of the small-scale sewage treatment methods. This processing method includes the following four steps as one cycle.

高速の撹拌曝気による好気性処理における
BOD除去と硝化処理および活性汚泥内への燐
の過剰取り込み工程。
In aerobic treatment using high-speed stirring aeration
BOD removal, nitrification treatment and excessive phosphorus incorporation into activated sludge.

低速撹拌による嫌気性処理における脱窒工
程。
Denitrification process in anaerobic treatment using low-speed stirring.

静置による活性活泥の沈殿工程。 Sedimentation process of activated mud by standing still.

上澄水の排出および余剰汚泥の引き抜き工
程。
Discharge of supernatant water and extraction of excess sludge.

ところで、上記好気性処理を行うための撹拌曝
気装置として、従来は機械式と散気式のものが用
いられている。機械式の装置としては、水面近く
で撹拌翼を回転させて空気を巻き込んで水流を起
こすもの、またはポンプの吐出噴射孔に空気管を
連通させたエジエクターを設けて、ポンプの噴流
に空気を混入しながら水流を起こすもの等があ
る。散気式の装置としては、水槽の底部に散気管
や散気板などの気泡発生装置を設けて空気源と連
通させ、空気源から大量の空気を供給して気泡の
上昇により水流を起こすもの等がある。
By the way, mechanical type and aeration type have been conventionally used as stirring aeration devices for performing the above-mentioned aerobic treatment. Mechanical devices include those that rotate a stirring blade near the water surface to draw in air to create a water flow, or an ejector that connects an air pipe to the pump's discharge injection hole to mix air into the jet of the pump. There are some that cause water flow while doing so. An air diffuser type device is one in which a bubble generator such as an air diffuser pipe or plate is installed at the bottom of the aquarium and communicates with an air source, and a large amount of air is supplied from the air source to cause water flow as the air bubbles rise. etc.

これらの撹拌曝気装置は、好気性処理を行なう
には好適であつても、極力空気との接触を絶ち低
速撹拌のみの嫌気性処理を行うには不適当であ
る。このため、好気性処理を行う撹拌曝気装置と
は別に、嫌気性処理のための低速撹拌装置が設け
られている。
Although these stirring aeration devices are suitable for performing aerobic treatment, they are not suitable for performing anaerobic treatment using only low-speed stirring by cutting off contact with air as much as possible. For this reason, a low-speed stirring device for anaerobic treatment is provided separately from the stirring and aeration device for performing aerobic treatment.

(発明が解決しようとする問題点) 上記のごとく、回分式活性汚泥処理法におい
て、従来の撹拌曝気装置は、嫌気性処理の工程に
不適当であり、別途に嫌気性処理の工程のための
低速撹拌装置が必要であり、それだけ設備が高価
なものになるという問題点があつた。また、従来
の撹拌曝気装置で機械式の撹拌翼のものは、稼動
部が水面上で騒音を発するとともに汚水槽の底部
が曝気しにくいという不具合がある。また、機械
式のポンプの吐出噴流によるものは、吐出流速が
極めて速く強い乱流が生じてエネルギー損失が大
きいとともに微生物フロツクの破壊を生じ易いと
いう不具合がある。さらに、散気式のものは、十
分な撹拌を行うために槽底の広範囲に気泡発生装
置が必要であるとともに多量の空気が必要であ
り、空気源等を含む設備が高価であり、しかも、
撹拌曝気の停止時に汚泥の沈殿により散気孔が目
詰まりを生じ易いという不具合がある。
(Problems to be Solved by the Invention) As mentioned above, in the batch activated sludge treatment method, the conventional stirring aeration equipment is unsuitable for the anaerobic treatment process, and a separate There was a problem in that a low-speed stirring device was required, which made the equipment that much more expensive. In addition, conventional stirring aeration devices using mechanical stirring blades have problems in that the moving parts generate noise above the water surface and it is difficult to aerate the bottom of the sewage tank. In addition, the discharge jet of a mechanical pump has the disadvantage that the discharge flow rate is extremely high and strong turbulence occurs, resulting in large energy loss and easy destruction of microbial flocs. Furthermore, the aeration type requires a bubble generator over a wide area at the bottom of the tank to achieve sufficient agitation, requires a large amount of air, and the equipment including the air source is expensive.
There is a problem in that the aeration holes tend to become clogged due to sedimentation of sludge when stirring aeration is stopped.

本発明の目的は、上記した事情に鑑みてなされ
たもので、撹拌曝気と低速撹拌の双方に性能を切
り換えて使用することのできる水中撹拌装置を提
供しようとすることにある。
The object of the present invention was made in view of the above-mentioned circumstances, and it is an object of the present invention to provide an underwater stirring device that can be used for both stirring aeration and low-speed stirring by switching its performance.

(問題点を解決するための手段) かかる目的を達成するために、本発明の水中撹
拌装置は、外胴ケーシングに内装された竪軸軸流
ポンプの吐出側に、軸方向に対して放射状に流路
を形成する截頭円錐形の吐出しコーンを設け、こ
の吐出しコーンと前記外胴ケーシングの端部との
間に円周状の吐出口を形成し、この吐出口の開閉
および開度調整できるように前記外胴ケーシング
に軸方向に摺動自在な環状のスライドゲートを設
け、前記吐出しコーンに前記流路に臨んで散気孔
を設け、この散気孔を開閉弁を介在させた空気管
により空気源に連通し、前記吐出口の開度を大と
するとともに前記開閉弁を開いて撹拌曝気による
好気性処理を行ない、前記吐出口の開度を小とす
るとともに前記開閉弁を閉じて低速撹拌による嫌
気性処理を行ない得るように構成されている。
(Means for Solving the Problems) In order to achieve the above object, the underwater agitation device of the present invention has a vertical shaft axial flow pump that is housed in an outer casing, and on the discharge side of the vertical shaft axial flow pump, a A truncated cone-shaped discharge cone forming a flow path is provided, and a circumferential discharge port is formed between the discharge cone and the end of the outer casing, and the opening/closing and opening degree of the discharge port is controlled. An annular slide gate slidable in the axial direction is provided in the outer body casing so as to be adjustable, and an air diffuser hole is provided in the discharge cone facing the flow path, and an opening/closing valve is interposed in the air diffuser hole. Communicating with an air source through a pipe, increasing the opening of the discharge port and opening the on-off valve to perform aerobic treatment by stirring aeration, reducing the opening of the discharge port and closing the on-off valve. The structure is such that anaerobic treatment can be performed using low-speed stirring.

(作用) 竪軸軸流ポンプの吐出側に截頭円錐形の吐出し
コーンを設けて流路を末広がりに軸方向に対して
放射状とし、この流路の円周状の吐出口をスライ
ドゲートで開閉および開度調整できるようにした
ので、スライドゲートの開度を調整することで吐
出口の流体抵抗が調整されて吐出流量を調整する
ことができる。そして、吐出流量の調整により吐
出流速が増減して、流路に臨んで設けた散気孔か
ら吸気される吸気量が増減される。さらに、開閉
弁を閉じて散気孔と空気源を遮断すれば、散気孔
から気泡が水中に混入されない。したがつて、ス
ライドゲートにより吐出口の開度を大とするとと
もに開閉弁を開けば、大きな吐出流量に多量な気
泡が混入されて撹拌曝気による好気性処理が行な
われ、吐出口の開度を小とするとともに開閉弁を
閉じれば、小さな吐出流量で気泡は混入されずに
低速撹拌による嫌気性処理が行なわれる。
(Function) A truncated cone-shaped discharge cone is provided on the discharge side of the vertical shaft axial flow pump, the flow path is widened at the end and radial in the axial direction, and the circumferential discharge opening of this flow path is connected with a slide gate. Since opening/closing and the opening degree can be adjusted, by adjusting the opening degree of the slide gate, the fluid resistance of the discharge port can be adjusted and the discharge flow rate can be adjusted. Then, by adjusting the discharge flow rate, the discharge flow rate is increased or decreased, and the amount of intake air taken in from the air diffuser holes provided facing the flow path is increased or decreased. Furthermore, if the on-off valve is closed to shut off the air diffuser hole and the air source, air bubbles will not be mixed into the water from the air diffuser hole. Therefore, by increasing the opening of the discharge port using a slide gate and opening the on-off valve, a large amount of air bubbles are mixed into the large discharge flow rate, and aerobic treatment is performed by stirring aeration, which increases the opening of the discharge port. By setting the flow rate to be small and closing the on-off valve, anaerobic treatment can be performed by low-speed stirring without mixing air bubbles with a small discharge flow rate.

(実施例) 以下、本発明の実施例につき第1図ないし第3
図を参照して説明する。第1図は、本発明の水中
撹拌装置の一実施例の断面図であり、第2図は、
第1図のスライドゲートの開度の調整機構の一例
の説明図であり、第3図は、スライドゲートの開
度の調整による吐出流量の特性図である。
(Example) Hereinafter, Figures 1 to 3 will be described for examples of the present invention.
This will be explained with reference to the figures. FIG. 1 is a sectional view of an embodiment of the underwater stirring device of the present invention, and FIG.
FIG. 3 is an explanatory diagram of an example of a mechanism for adjusting the opening degree of the slide gate shown in FIG. 1, and FIG. 3 is a characteristic diagram of the discharge flow rate by adjusting the opening degree of the slide gate.

第1図において、水中モータ1により回転駆動
される軸流羽根車2が外胴ケーシング3にリブ
4,4による支持で内装されて竪軸軸流ポンプ5
が構成されている。この竪軸軸流ポンプ5の吸込
側の外胴ケーシング3の端部はベル状に開いて吸
込口6が形成されている。さらに、吐出側の外胴
ケーシング3の端部は、吐出流を斜め外方に偏向
させて末広がりに軸方向に対して放射状となる流
路を形成する截頭円錐形の吐出しコーン7に間隔
を保つて放射リブ8,8……で支持され、吐出し
コーン7と外胴ケーシング3の端部との間に円周
状の吐出口9が形成されている。この吐出しコー
ン7の底部に鏡板10を設けて吐出しコーン7の
内部は中空室11が形成され、この中空室11か
ら吐出口9に臨んで多数の小孔の散気孔12,1
2……が円周状に配置されて穿設されている。こ
の中空室11に空気管13の一端が開口し、開閉
弁22を介して図示しない空気源若しくは外気に
連通されている。さらに、外胴ケーシング3の外
周に環状のスライドゲート14が軸方向に摺動自
在に嵌合して設けられ、このスライドゲート14
により吐出口9の開閉および開度調整がなされ
る。そして、吐出口9がスライドゲート14で閉
じられたときに、散気孔12,12……の開口に
スライドゲート14が当接して散気孔12,12
……が閉塞される。なお、吐出しコーン7の鏡板
10の外周に複数の脚部15,15……が設けら
れ、これらの脚部15,15……で槽底に装置が
固定されている。
In FIG. 1, an axial flow impeller 2 rotationally driven by a submersible motor 1 is installed inside an outer body casing 3 supported by ribs 4, and a vertical shaft axial flow pump 5 is installed.
is configured. The end of the outer body casing 3 on the suction side of the vertical shaft axial flow pump 5 is opened in a bell shape to form a suction port 6. Further, the end of the outer body casing 3 on the discharge side is formed with a truncated cone-shaped discharge cone 7 at intervals which deflects the discharge flow diagonally outward and widens at the end to form a flow path radial with respect to the axial direction. A circumferential discharge port 9 is formed between the discharge cone 7 and the end of the outer casing 3. A mirror plate 10 is provided at the bottom of the discharge cone 7, and a hollow chamber 11 is formed inside the discharge cone 7. From this hollow chamber 11, facing the discharge port 9, a large number of small aeration holes 12, 1 are formed.
2... are arranged and drilled in a circumferential manner. One end of an air pipe 13 opens into the hollow chamber 11 and communicates with an air source (not shown) or the outside air via an on-off valve 22 . Further, an annular slide gate 14 is provided on the outer periphery of the outer casing 3 so as to be slidable in the axial direction.
The opening/closing and opening degree adjustment of the discharge port 9 is performed by this. When the discharge port 9 is closed by the slide gate 14, the slide gate 14 comes into contact with the opening of the air diffuser holes 12, 12...
...is blocked. A plurality of legs 15, 15, .

スライドゲート14の開度の調整機構は、第2
図のごとく、外胴ケーシング3に設けた支点16
に操作アーム17を揺動自在に設け、この操作ア
ーム17の一端が操作ロツド18を介してスライ
ドゲート14に連結され、操作アーム17の他端
が駆動ロツド19を介して水槽上部の架台等に設
置した電動装置20および手動装置21に連結さ
れている。この電動装置20ではリミツトスイツ
チ等により、また手動装置21ではストツパ等に
よりスライドゲート14が摺動できる範囲を適宜
に制限し、その範囲内でスライドゲート14は任
意に吐出口9の開度を設定できる。
The mechanism for adjusting the opening degree of the slide gate 14 is the second one.
As shown in the figure, a fulcrum 16 provided on the outer casing 3
An operating arm 17 is swingably provided at the aquarium, and one end of the operating arm 17 is connected to the slide gate 14 via an operating rod 18, and the other end of the operating arm 17 is connected via a driving rod 19 to a pedestal, etc. at the top of the aquarium. It is connected to the installed electric device 20 and manual device 21. The electric device 20 uses a limit switch or the like, and the manual device 21 uses a stopper or the like to appropriately limit the sliding range of the slide gate 14, and within that range, the slide gate 14 can arbitrarily set the opening degree of the discharge port 9. .

かかる構成において、スライドゲート14が吐
出口9を大きく開いていれば、吐出口9の流体抵
抗は小さく、第3図の実線のごとく、竪軸軸流ポ
ンプ5から大きな吐出流量が外方へ放射状に吐き
出され、広い範囲に水流を起こすことができる。
また、スライドゲート14が吐出口9を小さく開
いていれば、第3図の破線のごとく、小さな吐出
流量が吐き出されて狭い範囲にしか水流を起こさ
ない。また、開閉弁22を開いて、中空室11が
空気源若しくは外気に連通していれば、流速が速
いときにはそれだけエジエクター効果で散気孔1
2,12……より多量の空気を吸込んで多量の気
泡を水中に巻き込むことができ、流速が遅いとき
には少量の気泡が水中に巻き込まれる。さらに、
開閉弁22を閉じて中空室11を空気源若しくは
外気から遮断すれば、散気孔12,12……から
の気泡の巻き込みは生じない。
In this configuration, if the slide gate 14 opens the discharge port 9 widely, the fluid resistance of the discharge port 9 is small, and a large discharge flow rate is radially outward from the vertical axial flow pump 5, as shown by the solid line in FIG. It can be spewed out and create water currents over a wide area.
Furthermore, if the slide gate 14 opens the discharge port 9 to a small extent, a small discharge flow rate is discharged and the water flow is generated only in a narrow range, as shown by the broken line in FIG. In addition, if the on-off valve 22 is opened and the hollow chamber 11 is in communication with the air source or the outside air, when the flow velocity is high, the ejector effect will increase the air diffusion hole 1.
2, 12...A larger amount of air can be sucked in and a larger amount of bubbles can be drawn into the water, and when the flow rate is slow, a smaller amount of air bubbles can be drawn into the water. moreover,
If the on-off valve 22 is closed to isolate the hollow chamber 11 from the air source or the outside air, air bubbles from the air diffusion holes 12, 12, . . . will not be trapped.

そこで、スライドゲート14を調整して吐出口
9を大きく開くとともに開閉弁22を開いて中空
室11を空気源若しくは外気に連通させること
で、多量の気泡が巻き込まれた多量の吐出流量で
十分な撹拌曝気による好気性処理を行なうことが
できる。また、吐出口9の開きを小さくするとと
もに、開閉弁22を閉じれば、吐出流量が小さく
気泡が混入せずに低速撹拌による嫌気性処理を行
なうことができる。なお、スライドゲート14で
吐出口9を閉じれば、散気孔12,12……はス
ライドゲード14で閉塞されて活性汚泥の沈殿等
で目詰まりを生じない。
Therefore, by adjusting the slide gate 14 to widen the discharge port 9 and opening the on-off valve 22 to communicate the hollow chamber 11 with the air source or the outside air, a large amount of discharge flow rate containing a large amount of air bubbles is sufficient. Aerobic treatment by stirring and aeration can be performed. Further, by reducing the opening of the discharge port 9 and closing the on-off valve 22, anaerobic treatment can be performed by low-speed stirring with a small discharge flow rate and no air bubbles mixed in. Note that if the discharge port 9 is closed by the slide gate 14, the air diffusion holes 12, 12, .

第4図は、本発明の水中撹拌装置の他の実施例
の部分図である。第4図において、外胴ケーシン
グ3に軸方向に摺動自在に設けられたスライドゲ
ート30に、散気孔12,12……から水中に巻
き込まれた気泡の一部を溜める気泡溜め込み室3
1が設けられ、この気泡溜め込み室31には排気
弁32が設けられている。この排気弁32は、ス
ライドゲート30が所定の高さに浮き上がると外
胴ケーシング3に設けたストツパ33に当接して
開成されて、気泡溜め込み室31の空気が排出さ
れるように構成されている。さらに、スライドゲ
ート30の散気孔12,12……への当接部にパ
ツキング34が設けられている。
FIG. 4 is a partial diagram of another embodiment of the underwater stirring device of the present invention. In FIG. 4, an air bubble storage chamber 3 that stores some of the air bubbles drawn into the water from the air diffuser holes 12, 12, etc. is placed in a slide gate 30 that is slidably provided in the outer body casing 3 in the axial direction.
1 is provided, and this bubble storage chamber 31 is provided with an exhaust valve 32. This exhaust valve 32 is configured so that when the slide gate 30 rises to a predetermined height, it comes into contact with a stopper 33 provided on the outer body casing 3 and is opened, so that the air in the bubble storage chamber 31 is discharged. . Furthermore, packing 34 is provided at the portion of the slide gate 30 that comes into contact with the air diffuser holes 12, 12, . . . .

かかる構成により、気泡溜め込み室31に空気
が溜まつて浮力が強くなるとスライドゲート30
は上昇してより吐出流量が増大し、強い撹拌曝気
がなされる。そして、所定の高さまで上昇すると
排気弁32が開成されて、気泡溜め込み室31の
空気が排出されてスライドゲート30は下降し、
吐出流量が減少して弱い撹拌曝気となる。このよ
うにして、自動的に交互に一定周期で強弱の撹拌
曝気がなされる。なお、停止時には、スライドゲ
ート30はパツキング34により散気孔12,1
2……を確実に閉塞して、逆流等による目詰まり
が防止される。
With this configuration, when air accumulates in the bubble storage chamber 31 and the buoyancy becomes strong, the slide gate 30
increases, the discharge flow rate increases, and strong stirring and aeration is performed. Then, when it rises to a predetermined height, the exhaust valve 32 is opened, the air in the bubble storage chamber 31 is exhausted, and the slide gate 30 is lowered.
The discharge flow rate decreases, resulting in weak stirring aeration. In this way, strong and weak stirring aeration is automatically performed alternately at a constant period. In addition, when the slide gate 30 is stopped, the air diffusion holes 12 and 1 are closed by the packing 34.
2... is reliably closed to prevent clogging due to backflow, etc.

第5図は、本発明の水中撹拌装置のさらに他の
実施例の部分図である。第5図において、散気孔
12,12……を覆うように一端部が固定されて
パツキング35が設けられている。このパツキン
グ35はリード弁として作用し、吐出流速に応じ
て散気孔12,12……から吸気される際には開
口を開き、停止時にはスライドゲート14の当接
部がこのパツキング35を介して開口に当接して
確実な閉塞がなされる。
FIG. 5 is a partial diagram of still another embodiment of the underwater stirring device of the present invention. In FIG. 5, a packing 35 is provided with one end fixed so as to cover the air diffuser holes 12, 12, . This packing 35 acts as a reed valve, and opens when air is taken in from the air diffuser holes 12, 12, depending on the discharge flow rate, and when stopped, the abutting part of the slide gate 14 opens through this packing 35. A reliable closure is achieved by contacting the

上記した本発明の水中撹拌装置を比較的大きな
水槽に複数台設置する場合には、第6図のごと
く、駆動装置40,40で駆動される回転軸4
1,41の回転を変換装置42,42……で直線
の上下運動に変換し、それぞれの水中撹拌装置の
第2図の駆動ロツド19を同時に調整してスライ
ドゲート14,30を調整するように構成するこ
とができる。そして、それぞれの水中撹拌装置の
撹拌曝気を原水流入側で強く、後流側で弱くする
等の調整を行なつても良い。
When a plurality of the underwater stirring devices of the present invention described above are installed in a relatively large water tank, as shown in FIG.
1, 41 is converted into linear vertical movement by converters 42, 42..., and the slide gates 14, 30 are adjusted by simultaneously adjusting the drive rods 19 in FIG. 2 of each underwater stirring device. Can be configured. Then, adjustments may be made such as making the stirring aeration of each underwater stirring device stronger on the raw water inflow side and weaker on the downstream side.

なお、上記実施例にあつては、吐出しコーン7
に吐出口9に臨んで散気孔12,12……が設け
られたが、これに限られず、エジエクター効果で
水中に気泡が巻き込まれるならば、流路に臨んで
吐出しコーン7のいずれの位置に散気孔12,1
2……を穿設しても良い。さらに、本発明の水中
撹拌装置は、回分式活性汚泥法のみならず、各種
水槽内の撹拌用ならびに曝気用として使用できる
ことは勿論である。
In addition, in the above embodiment, the discharge cone 7
Although the air diffuser holes 12, 12... are provided facing the discharge port 9, the invention is not limited to this, and if air bubbles are drawn into the water due to the ejector effect, any position of the discharge cone 7 facing the flow path is provided. Diffusion hole 12,1
2... may be provided. Furthermore, it goes without saying that the underwater stirring device of the present invention can be used not only for the batch activated sludge method but also for stirring and aeration in various water tanks.

(発明の効果) 以上説明したように、本発明に係わる水中撹拌
装置によれば、吐出口の開度を大とするとともに
開閉弁を開くことで、多量の気泡が混入された大
きな吐出流量により、撹拌曝気の好気性処理を行
なうことができる。また、吐出口の開度を小とす
るとともに開閉弁を閉じることで、気泡の混入さ
れない小さな吐出流量により、低速撹拌の嫌気性
処理を行なうことができる。したがつて、1台の
装置を撹拌曝気と低速撹拌とに性能を切り換える
ことができるので、1台の装置で好気性処理と嫌
気性処理の2つの工程を行なうことができ、設備
が安価なものになるという優れた効果を奏する。
(Effects of the Invention) As explained above, according to the underwater agitation device according to the present invention, by increasing the opening degree of the discharge port and opening the on-off valve, a large discharge flow rate containing a large amount of air bubbles can be produced. , aerobic treatment with stirring and aeration can be performed. Furthermore, by reducing the opening degree of the discharge port and closing the on-off valve, anaerobic treatment with low-speed stirring can be performed with a small discharge flow rate that does not introduce air bubbles. Therefore, since the performance of one device can be switched between stirring aeration and low-speed stirring, one device can perform two processes, aerobic treatment and anaerobic treatment, and the equipment is inexpensive. It has the excellent effect of becoming something.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明の水中撹拌装置の一実施例の
断面図であり、第2図は、第1図のスライドゲー
トの開度の調整機構の一例の説明図であり、第3
図は、スライドゲートの開度の調整による吐出流
量の特性図であり、第4図は、本発明の水中撹拌
装置の他の実施例の部分図であり、第5図は、本
発明の水中撹拌装置のさらに他の実施例の部分図
であり、第6図は、本発明の水中撹拌装置を水槽
に複数台設置するときのスライドゲートの開度の
調整機構の一例を示す図である。 3:外胴ケーシング、5:竪軸軸流ポンプ、
7:吐出しコーン、9:吐出口、12:散気孔、
13:空気管、14,30:スライドゲート、2
2:開閉弁、31:空気溜め込み室、32:排気
弁、34,35:パツキング。
1 is a sectional view of one embodiment of the underwater stirring device of the present invention, FIG. 2 is an explanatory diagram of an example of the mechanism for adjusting the opening degree of the slide gate in FIG.
The figure is a characteristic diagram of the discharge flow rate by adjusting the opening degree of the slide gate, FIG. 4 is a partial diagram of another embodiment of the underwater stirring device of the present invention, and FIG. FIG. 6 is a partial view of still another embodiment of the stirring device, and FIG. 6 is a diagram showing an example of a mechanism for adjusting the opening degree of the slide gate when a plurality of underwater stirring devices of the present invention are installed in an aquarium. 3: Outer casing, 5: Vertical axial flow pump,
7: Discharge cone, 9: Discharge port, 12: Diffusion hole,
13: Air pipe, 14, 30: Slide gate, 2
2: Open/close valve, 31: Air storage chamber, 32: Exhaust valve, 34, 35: Packing.

Claims (1)

【特許請求の範囲】 1 外胴ケーシングに内装された竪軸軸流ポンプ
の吐出側に、軸方向に対して放射状に流路を形成
する截頭円錐形の吐出しコーンを設け、この吐出
しコーンと前記外胴ケーシングの端部との間に円
周状の吐出口を形成し、この吐出口の開閉および
開度調整できるように前記外胴ケーシングに軸方
向に摺動自在な環状のスライドゲートを設け、前
記吐出しコーンに前記流路に臨んで散気孔を設
け、この散気孔を開閉弁を介在させた空気管によ
り空気源に連通し、前記吐出口の開度を大とする
とともに前記開閉弁を開いて撹拌曝気による好気
性処理を行ない、前記吐出口の開度を小とすると
ともに前記開閉弁を閉じて低速撹拌による嫌気性
処理を行ない得るようにしたことを特徴とする水
中撹拌装置。 2 前記吐出コーンに前記吐出口に臨んで散気孔
を設けたことを特徴とする特許請求の範囲第1項
記載の水中撹拌装置。 3 前記スライドゲートで前記吐出口が閉じられ
たときに、前記散気孔の開口に前記スライドゲー
トが当接して閉塞するように構成したことを特徴
とする特許請求の範囲第2項記載の水中撹拌装
置。 4 前記スライドゲートがパツキングを介して前
記散気孔の開口に当接するように構成したことを
特徴とする特許請求の範囲第3項記載の水中撹拌
装置。 5 前記スライドゲートに前記散気孔からの気泡
の一部を溜める気泡溜め込み室を設けるととも
に、この気泡溜め込み室の浮力で前記スライドゲ
ートが所定の高さに浮き上がると前記気泡溜め込
み室の空気を排出する排気弁を設けたことを特徴
とする特許請求の範囲第1項ないし第4項記載の
いずれかの水中撹拌装置。
[Claims] 1. A truncated cone-shaped discharge cone forming a flow path radially in the axial direction is provided on the discharge side of a vertical shaft axial flow pump housed in an outer casing. A circumferential discharge port is formed between the cone and the end of the outer casing, and an annular slide is slidable in the axial direction on the outer casing so that the discharge port can be opened/closed and the degree of opening can be adjusted. A gate is provided, an air diffuser hole is provided in the discharge cone facing the flow path, and the air diffuser hole is communicated with an air source through an air pipe with an opening/closing valve interposed therebetween, and the opening degree of the discharge port is increased. The underwater system is characterized in that the opening/closing valve is opened to perform aerobic treatment by stirring and aeration, and the opening degree of the discharge port is reduced and the opening/closing valve is closed to perform anaerobic treatment by low-speed stirring. Stirring device. 2. The underwater stirring device according to claim 1, wherein the discharge cone is provided with aeration holes facing the discharge port. 3. The underwater agitation according to claim 2, wherein when the discharge port is closed by the slide gate, the slide gate contacts and closes the opening of the air diffuser hole. Device. 4. The underwater agitation device according to claim 3, wherein the slide gate is configured to abut against the opening of the air diffusion hole through packing. 5. A bubble storage chamber is provided in the slide gate to collect some of the bubbles from the air diffuser hole, and when the slide gate rises to a predetermined height due to the buoyancy of the bubble storage chamber, the air in the bubble storage chamber is discharged. An underwater stirring device according to any one of claims 1 to 4, characterized in that an exhaust valve is provided.
JP61095961A 1986-04-25 1986-04-25 Underwater stirrer Granted JPS62250996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61095961A JPS62250996A (en) 1986-04-25 1986-04-25 Underwater stirrer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61095961A JPS62250996A (en) 1986-04-25 1986-04-25 Underwater stirrer

Publications (2)

Publication Number Publication Date
JPS62250996A JPS62250996A (en) 1987-10-31
JPH0131957B2 true JPH0131957B2 (en) 1989-06-28

Family

ID=14151817

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61095961A Granted JPS62250996A (en) 1986-04-25 1986-04-25 Underwater stirrer

Country Status (1)

Country Link
JP (1) JPS62250996A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5745917A (en) * 1980-09-02 1982-03-16 Nissin Electric Co Ltd Condenser

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5745917A (en) * 1980-09-02 1982-03-16 Nissin Electric Co Ltd Condenser

Also Published As

Publication number Publication date
JPS62250996A (en) 1987-10-31

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