JPH06320185A - Aeration device - Google Patents

Aeration device

Info

Publication number
JPH06320185A
JPH06320185A JP10966993A JP10966993A JPH06320185A JP H06320185 A JPH06320185 A JP H06320185A JP 10966993 A JP10966993 A JP 10966993A JP 10966993 A JP10966993 A JP 10966993A JP H06320185 A JPH06320185 A JP H06320185A
Authority
JP
Japan
Prior art keywords
aeration
air
valve member
float
tubular body
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.)
Withdrawn
Application number
JP10966993A
Other languages
Japanese (ja)
Inventor
Chiaki Niwa
千明 丹羽
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.)
Shimizu Construction Co Ltd
Shimizu Corp
Original Assignee
Shimizu Construction Co Ltd
Shimizu Corp
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 Shimizu Construction Co Ltd, Shimizu Corp filed Critical Shimizu Construction Co Ltd
Priority to JP10966993A priority Critical patent/JPH06320185A/en
Publication of JPH06320185A publication Critical patent/JPH06320185A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

PURPOSE:To provide an aeration device which can uniformize the amt. of air supplied from each air feed pipe to perform a uniform aerating operation. CONSTITUTION:An aeration amt. controller 100 is provided with a valve member 17 freely movable between a lower and an upper position of an outer cylinder 10 and the valve member is provided integrally with a lower float 18 which gradually decreases the space between itself and the outer cylinder 10 as it moves downward and an upper float 19 which gradually decreases the space between itself and the outer cylinder 10 as it moves upward. When the amt. of air supplied from air feed pipe is increased, the valve member 17 is entirely moved upward to decrease the space between its upper float 19 and the outer cylinder 10, thereby holding down an increase in the overall amt. of air flow in the aeration amt. controller 100.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、水槽内に貯留された処
理水、水処理装置における各種曝気槽、池、湖沼等の自
然水域の水質保全に活用できる曝気装置に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to treated water stored in a water tank, various aeration tanks in a water treatment apparatus, an aeration apparatus which can be utilized for water quality conservation in natural water areas such as ponds, lakes and marshes.

【0002】[0002]

【従来の技術】従来より、有機性廃水の微生物処理
(例えば活性汚泥処理法、接触曝気法)、有機性廃水
あるいは汚泥の処理槽の嫌気化防止、修景用池、湖
沼、堀の水質改善、バイオパーティクルを含んだ水を
循環させる流動床法では、処理槽内の処理水に空気を泡
状に送り込むための曝気装置50〜52を使用してい
る。
2. Description of the Related Art Conventionally, microbial treatment of organic wastewater (for example, activated sludge treatment method, contact aeration method), prevention of anaerobic treatment of organic wastewater or sludge treatment tank, water quality improvement of landscape ponds, lakes and moats. In the fluidized bed method in which water containing bioparticles is circulated, aeration devices 50 to 52 for blowing air into the treated water in the treatment tank are used.

【0003】曝気装置50は、図4に示されるように、
処理槽1の一方の壁面2下部近傍に沿って散気塔3を水
平方向に一列に配置し、これら散気塔3のそれぞれに空
気を供給するための空気供給管4を接続し、これら空気
供給管4の途中に、空気の供給量を調節するための調節
弁5をそれぞれ設けたものであって、これら各空気供給
管4には、分岐部を通じて共通の送風機6から空気が供
給されるようになっている。なお、図4の曝気装置50
は片側旋回流方式による活性汚泥法、又は接触曝気法を
示す。また、以下の説明において共通とする構成要素に
同一の符号を付すことにする。
The aeration device 50, as shown in FIG.
The diffusing towers 3 are horizontally arranged in a row along the vicinity of the lower part of one wall surface 2 of the treatment tank 1, and an air supply pipe 4 for supplying air to each of these diffusing towers 3 is connected to the air. A control valve 5 for controlling the supply amount of air is provided in the middle of the supply pipe 4, and air is supplied to each of these air supply pipes 4 from a common blower 6 through a branch portion. It is like this. The aeration device 50 of FIG.
Indicates the activated sludge method by the one-sided swirling flow method or the contact aeration method. Also, in the following description, common components will be assigned the same reference numerals.

【0004】曝気装置51は、図5に示されるように、
処理槽1内の底部付近の水平面内にマトリックス状に多
数の散気塔3を配置し、これら散気塔3のそれぞれに空
気を供給するための空気供給管4を接続し、これら空気
供給管4の途中に、前述した曝気装置50と同様に、空
気の供給量を調節するための調節弁5をそれぞれ設けた
ものであって、これら各空気供給管4には、分岐部を通
じて共通の送風機6から空気が供給されるようになって
いる。なお、図5の曝気装置51は全面曝気方式による
活性汚泥法、又は接触曝気法を示す。
The aeration device 51, as shown in FIG.
A large number of air diffusion towers 3 are arranged in a matrix in a horizontal plane near the bottom of the treatment tank 1, and air supply pipes 4 for supplying air to each of these air diffusion towers 3 are connected to these air supply pipes. Similar to the aeration device 50 described above, control valves 5 for controlling the supply amount of air are provided in the middle of 4, respectively, and each of these air supply pipes 4 has a common blower through a branch portion. Air is supplied from 6. In addition, the aeration device 51 of FIG. 5 shows the activated sludge method by a full surface aeration method, or a contact aeration method.

【0005】曝気装置52は、図6に示されるように、
複数に分割された処理槽1A〜1Dのそれぞれに散気塔
3を配置し、各処理槽1A〜1Dの散気塔3のそれぞれ
に空気を供給するための空気供給管4を接続し、これら
空気供給管4の途中に、前述した曝気装置50、51と
同様に、空気の供給量を調節するための調節弁5をそれ
ぞれ設けたものであって、これら各空気供給管4には、
分岐部を通じて共通の送風機6から空気が供給されるよ
うになっている。なお、図6の曝気装置52は、例え
ば、中水道処理施設の地中ばり空間に設けられた複数の
処理槽、汚泥貯留槽の汚水、雑排水貯留槽等に適用さ
れ、活性汚泥処理槽、汚泥貯留槽さらには各種貯留槽に
同一の送風機6により空気を送り込むものである。な
お、これらの図4〜図6に示す曝気装置50〜52では
符号7で示される調節弁が設けられており、この調節弁
7によって、曝気開始時において最初の流量が決定され
るようになっている(図4、図5のみ図示)。
The aeration device 52, as shown in FIG.
An air diffuser tower 3 is arranged in each of the plurality of divided treatment tanks 1A to 1D, and an air supply pipe 4 for supplying air to each of the air diffusion towers 3 of the respective treatment tanks 1A to 1D is connected. Similar to the aeration devices 50 and 51 described above, control valves 5 for controlling the supply amount of air are provided in the middle of the air supply pipes 4, and these air supply pipes 4 are
Air is supplied from a common blower 6 through the branch portion. In addition, the aeration device 52 of FIG. 6 is applied to, for example, a plurality of treatment tanks provided in the underground beam space of a wastewater treatment facility, sewage of a sludge storage tank, a gray water storage tank, an activated sludge treatment tank, Air is sent to the sludge storage tank and various storage tanks by the same blower 6. The aeration devices 50 to 52 shown in FIGS. 4 to 6 are provided with a control valve denoted by reference numeral 7, and the control valve 7 determines the initial flow rate at the start of aeration. (Only shown in FIGS. 4 and 5).

【0006】[0006]

【発明が解決しようとする課題】ところで、図4、図5
に示される曝気装置では、各散気塔3につながる空気供
給管4のそれぞれに調節弁5を設けておいても、曝気処
理を続けていると、散気塔3にゴミが付着して目詰まり
したり、汚泥が付着したりすることがあり、これによっ
て、目詰まりした散気塔3に通じる空気供給管4の空気
供給量が減少するとともに、他の空気供給管4の空気供
給量が相対的に増加することになり、その結果、処理槽
1の曝気がアンバランスとなり、全体の浄化効率が低下
することになる。
By the way, FIG. 4 and FIG.
In the aeration apparatus shown in Fig. 3, even if the air supply pipes 4 connected to the air diffusing towers 3 are each provided with the control valve 5, if the aeration process is continued, dust may be attached to the air diffusing tower 3 The air supply amount of the air supply pipe 4 leading to the clogged air diffusing tower 3 may decrease and the air supply amount of the other air supply pipes 4 may decrease due to clogging or adhesion of sludge. As a result, the aeration of the processing tank 1 becomes unbalanced, resulting in a decrease in overall purification efficiency.

【0007】また、図6に示される曝気装置では、複数
の処理槽1A〜1Dのそれぞれに共通の空気源から空気
を供給するようにしたので、各処理槽1A〜1D内の水
位が不均一に変動し、各散気塔3にかかる水位が不均一
となる。その結果、水位が低下した散気塔3にかかる水
圧が減少することから、この散気塔3からの空気の曝気
量が、他の散気塔3と比較して増加することになり、そ
の結果、他の散気塔3では空気の曝気量が減少するとい
う不具合があった。
Further, in the aeration apparatus shown in FIG. 6, since the air is supplied from the common air source to each of the plurality of treatment tanks 1A to 1D, the water levels in the respective treatment tanks 1A to 1D are not uniform. And the water level applied to each air diffusing tower 3 becomes non-uniform. As a result, the water pressure applied to the diffusing tower 3 having the lowered water level is reduced, so that the aeration amount of the air from the diffusing tower 3 is increased as compared with the other diffusing towers 3. As a result, the other aeration tower 3 has a problem that the aeration amount of air is reduced.

【0008】そして、このように処理槽内の曝気量が不
均一となると、一部活性汚泥が沈積し、腐敗する(活性
汚泥処理法)、槽内の流れにむらができ、局部的に目詰
まりを生じる(接触曝気法)、バイオパーティクルが局
所的に沈積する(流動床法)、嫌気化し、固形物が沈積
する(有機性廃水、汚泥の貯留槽の場合)、溶存酸素濃
度にむらができ、その結果、浄化効率が低下する、腐
敗、臭気が発生するという問題が生じる。
When the amount of aeration in the treatment tank becomes non-uniform as described above, some activated sludge is deposited and decomposed (activated sludge treatment method), and the flow in the tank becomes uneven, which causes a local problem. Occurrence of clogging (contact aeration method), local deposition of bioparticles (fluidized bed method), anaerobicization, solid matter deposition (in the case of organic wastewater and sludge storage tank), uneven oxygen concentration As a result, there are problems that the purification efficiency is lowered, and rotting and odor are generated.

【0009】本発明は、上記の事情に鑑みてなされたも
のであって、共通の空気源から送られた空気が、分岐さ
れた複数の空気供給管にそれぞれ供給される場合に、各
空気供給管に対する空気の供給量を均一化して、処理槽
内においてむらのない曝気を行うことできる曝気装置の
提供を目的とする。
The present invention has been made in view of the above circumstances, and when air sent from a common air source is supplied to each of a plurality of branched air supply pipes, each air supply is performed. An object of the present invention is to provide an aerator capable of uniformizing the supply amount of air to the pipe and performing uniform aeration in the treatment tank.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するため
に本発明では、共通の送風機から送られた曝気流体を複
数の供給管に分割し、かつ各供給管の途中に、曝気流体
の流量を調節する曝気量調節計が上下方向に設けられた
曝気装置において、前記曝気量調節計を、曝気流体が流
通する筒状体と、筒状体内に配置されかつ該筒状体の軸
方向に沿って移動自在に設けられた弁部材とから構成
し、前記弁部材を、筒状体の下部位置と上部位置との間
で移動自在であり、下方への移動に伴って筒状体との間
隔を漸次縮小させる下部フロートと、上方への移動に伴
って筒状体との間隔を漸次縮小させる上部フロートとを
一体化した構成とした。
In order to achieve the above object, in the present invention, the aeration fluid sent from a common blower is divided into a plurality of supply pipes, and the flow rate of the aeration fluid is in the middle of each supply pipe. In the aerating device in which the aeration amount controller for adjusting the aeration amount is provided in the vertical direction, the aeration amount controller is provided with a tubular body through which the aeration fluid flows, and in the axial direction of the tubular body that is arranged in the tubular body. A valve member movably provided along the tubular member, the valve member being movable between a lower position and an upper position of the tubular body, The lower float, which gradually reduces the distance, and the upper float, which gradually decreases the distance between the cylindrical body as it moves upward, are integrated.

【0011】[0011]

【作用】この発明によれば、複数に分割された各供給管
の途中に、曝気流体が流通する筒状体と、筒状体内に配
置されかつ該筒状体の軸方向に沿って移動自在に設けら
れた弁部材とからなる曝気量調節計を設け、更に、この
曝気量調節計の弁部材を、筒状体の下部位置と上部位置
との間で移動自在に設けるとともに、下方への移動に伴
って筒状体との間隔を漸次縮小させる下部フロートと、
上方への移動に伴って筒状体との間隔を漸次縮小させる
上部フロートとを一体化した構成としたので、供給管を
下方から上方に流れる曝気流体の供給圧力、弁部材の自
重等によって、弁部材の下部フロートが上下方向に対し
てバランスした位置に止まる。
According to the present invention, in the middle of each of the plurality of divided supply pipes, a tubular body through which the aeration fluid flows, and a tubular body which is disposed in the tubular body and is movable along the axial direction of the tubular body. An aeration amount controller consisting of a valve member provided on the cylindrical body is provided, and the valve member of the aeration amount controller is movably provided between a lower position and an upper position of the tubular body, and is moved downward. A lower float that gradually reduces the interval with the tubular body as it moves,
Since the upper float that gradually reduces the distance from the tubular body along with the upward movement is integrated, the supply pressure of the aeration fluid flowing from the lower side to the upper side of the supply pipe, the weight of the valve member, etc. The lower float of the valve member stays in a vertically balanced position.

【0012】そして、このとき、例えば、ある供給管に
てゴミによる目詰まりが生じた場合には、目詰まりした
供給管では、曝気流体の流量が減少することになり、か
つ、相対的に他の供給管の曝気流体の流量が増加するこ
とになる。そして、このように供給管の曝気流体の流量
が増加した場合には、この供給管が設けられている曝気
量調節計において、曝気流体量の増加によって弁部材が
全体的に上方に移動させられ、更に、この弁部材が上方
に一定量移動した場合には、該弁部材の上部フロート
と、筒状体との間隔が縮小することになり、これによっ
て該曝気量調節計全体の流量は微小量増加しただけに抑
えられる。すなわち、本発明の曝気装置では、他の系統
の影響等で、供給管の曝気流体流量が相対的に増加した
場合であっても、該供給管に設けられている曝気量調節
計により、曝気流体の増加が微小量に抑えられ、これに
よって各供給管で流れる曝気流体の量にばらつきが生じ
ない。
At this time, for example, when a certain supply pipe is clogged with dust, the flow rate of the aeration fluid is decreased in the clogged supply pipe, and relatively other Will increase the flow rate of the aeration fluid in the supply pipe. Then, when the flow rate of the aeration fluid in the supply pipe increases in this way, in the aeration amount controller provided with the supply pipe, the valve member is generally moved upward due to the increase in the aeration fluid amount. Further, when the valve member moves upward by a certain amount, the interval between the upper float of the valve member and the cylindrical body is reduced, which causes the flow rate of the entire aeration amount controller to be small. It can be suppressed only by increasing the amount. That is, in the aeration apparatus of the present invention, even when the aeration fluid flow rate of the supply pipe is relatively increased due to the influence of other systems, the aeration amount controller provided in the supply pipe aerates the aeration. The increase of the fluid is suppressed to a minute amount, so that the amount of the aeration fluid flowing in each supply pipe does not vary.

【0013】[0013]

【実施例】以下、本発明の実施例を図1〜図3に基づい
て説明する。なお、本実施例に示される曝気量調節計1
00、101は、図4〜図6で示される調節弁5に代え
てそれぞれ設けられるものであり、かつ空気供給管4に
沿って上下方向に配置されるものである。
Embodiments of the present invention will be described below with reference to FIGS. Note that the aeration amount controller 1 shown in this embodiment is
00 and 101 are provided instead of the control valve 5 shown in FIGS. 4 to 6, and are arranged vertically along the air supply pipe 4.

【0014】まず、図1を参照して、第1実施例である
曝気量調節計100について説明する。この図において
符号10で示すものは外筒であって、この外筒10は、
下側約1/3に設けられて、上方に向けて径が漸次拡大
される下部テーパ管10aと、中間部に同一径に設けら
れた円筒管10bと、上側約1/4〜1/3に設けられ
て、上方に向けて径が漸次縮小する上部テーパ管10c
とから構成されている。また、この外筒10の上端部、
下端部には、前述した空気供給管4に接続するための取
付フランジ11、12が設けられ、この外筒10内の空
気流通路13には、センターシャフト支持具14、15
によって固定されたセンターシャフト16が、中心線に
沿うように配置されている。
First, referring to FIG. 1, an aeration amount controller 100 according to a first embodiment will be described. In this figure, the reference numeral 10 is an outer cylinder, and the outer cylinder 10 is
A lower taper pipe 10a provided on the lower side about 1/3 and having a diameter gradually increasing upward, a cylindrical pipe 10b having the same diameter on the middle portion, and about 1/4 to 1/3 on the upper side. The upper taper pipe 10c, which is provided in the
It consists of and. In addition, the upper end of the outer cylinder 10,
Mounting flanges 11 and 12 for connecting to the above-described air supply pipe 4 are provided at the lower end portion, and the center shaft supports 14 and 15 are provided in the air flow passage 13 in the outer cylinder 10.
The center shaft 16 fixed by is arranged along the center line.

【0015】また、この外筒10の空気流通路13に
は、センターシャフト16を貫通するように、かつ該セ
ンターシャフト16に沿って移動自在な弁部材17が設
けられている。この弁部材17は、下部側に設けられた
下部フロート18と、上部側に設けられた上部フロート
19と、これらフロート18、19を連結するタイロッ
ド20とから構成されたものであって、下部フロート1
8が、下部テーパ管10aのテーパにより下方への移動
が規制される下部位置と、上部フロート19が、上部テ
ーパ管10cのテーパにより上方への移動が規制される
上部位置との間の範囲内で、上下方向に移動されるよう
になっている。
A valve member 17 is provided in the air flow passage 13 of the outer cylinder 10 so as to penetrate the center shaft 16 and to be movable along the center shaft 16. The valve member 17 is composed of a lower float 18 provided on the lower side, an upper float 19 provided on the upper side, and a tie rod 20 connecting the floats 18 and 19 to each other. 1
8 is within a range between a lower position where downward movement is restricted by the taper of the lower tapered pipe 10a and an upper float 19 is between upper position where upward movement is restricted by the taper of the upper tapered pipe 10c. It is designed to be moved vertically.

【0016】そして、このような構成により、弁部材1
7が下方側に移動した場合には、該弁部材17が下方に
移動するに従って、下部フロート18が下部テーパ管1
0aのテーパ状壁面に近接して、これら下部フロート1
8と下部テーパ管10aとの間に形成された隙間を漸次
縮小してゆき、また、弁部材17が上方側に移動した場
合には、該弁部材17が上方に移動するに従って、上部
フロート19が上部テーパ管10cのテーパ状壁面に近
接して、これら上部フロート19と上部テーパ管10c
との間に形成された隙間を漸次縮小する。すなわち、前
記下部テーパ管10a、上部テーパ管10cの内面側に
それぞれ位置するテーパ状壁面は、弁部材17の下部フ
ロート18、上部フロート19の弁座として機能する。
With this structure, the valve member 1
When the valve member 17 moves downward, the lower float 18 moves the lower taper pipe 1 as the valve member 17 moves downward.
The lower float 1 close to the tapered wall of 0a
8 and the lower taper pipe 10a are gradually reduced, and when the valve member 17 moves upward, as the valve member 17 moves upward, the upper float 19 Is close to the tapered wall surface of the upper taper pipe 10c, and the upper float 19 and the upper taper pipe 10c are
The gap formed between and is gradually reduced. That is, the tapered wall surfaces respectively located on the inner surface sides of the lower taper pipe 10 a and the upper taper pipe 10 c function as valve seats of the lower float 18 and the upper float 19 of the valve member 17.

【0017】次に、上記のように構成された曝気量調節
計100の作用について説明する。外筒10の下部テー
パ管10aは上方に向けて拡開するように設けられてい
るので、下方から上方に流れる空気によって、弁部材1
7は下部フロート18がバランスした位置に止まる。な
お、下部フロート18の位置は、空気を送風する送風機
6の供給圧力、空気流の状態、弁部材17の自重等によ
り決定される。
Next, the operation of the aeration amount controller 100 configured as described above will be described. Since the lower taper pipe 10a of the outer cylinder 10 is provided so as to expand upward, the valve member 1 is opened by the air flowing upward from below.
7 stops at the position where the lower float 18 is balanced. The position of the lower float 18 is determined by the supply pressure of the blower 6 that blows air, the state of the air flow, the weight of the valve member 17, and the like.

【0018】そして、このような空気供給管4毎に設け
られた曝気量調節計100において、例えば、ある散気
塔3にてゴミによる目詰まりが生じた場合(図4、図5
の例)には、このような事態が生じた空気供給管4では
空気流量が減少することになり、相対的に他方の空気供
給管4の空気流量が増加することになる。また、図6の
例において、各処理槽1A〜1D内の水位がばらばらに
変動して、ある処理槽1A〜1Dの水面が低下する事態
が生じた場合には、このような事態が生じた空気供給管
4では空気流量が増加することになり、相対的に他方の
空気供給管4の空気流量が減少することになる。
In the aeration amount controller 100 provided for each of the air supply pipes 4 as described above, for example, when clogging due to dust occurs in a diffuser 3 (FIGS. 4 and 5).
In the example), the air flow rate in the air supply pipe 4 in which such a situation occurs decreases, and the air flow rate in the other air supply pipe 4 relatively increases. Further, in the example of FIG. 6, when the water level in each of the processing tanks 1A to 1D fluctuates and the water surface of a certain processing tank 1A to 1D lowers, such a situation occurs. The air flow rate in the air supply pipe 4 increases, and the air flow rate in the other air supply pipe 4 relatively decreases.

【0019】そして、このように空気供給管4の空気流
量が増加した場合には、この増加した空気の圧力によっ
て弁部材17が全体的に上方に移動させられ、更に、こ
の弁部材17が上方に一定量移動した場合には、該弁部
材17の上部フロート19と、外筒10の上部テーパ管
10cとの間隔が縮小することになり、これによって該
曝気量調節計100全体の流量は微小量増加しただけに
抑えられる。すなわち、この曝気量調節計100では、
他の系統の影響で空気流量が相対的に増加した場合であ
っても、この空気の増加が微小量に抑えられ、これによ
って各空気供給管4で流れる空気の量にばらつきが生じ
ず、上述した処理槽1または1A〜1Dにおいてむらの
無い曝気を行うことができる。
When the air flow rate of the air supply pipe 4 is increased in this way, the valve member 17 is entirely moved upward by the increased air pressure, and the valve member 17 is further moved upward. When the fixed amount is moved to a certain amount, the distance between the upper float 19 of the valve member 17 and the upper taper pipe 10c of the outer cylinder 10 is reduced, so that the flow rate of the entire aeration amount controller 100 is very small. It can be suppressed only by increasing the amount. That is, in this aeration amount controller 100,
Even when the air flow rate is relatively increased due to the influence of other systems, the increase of the air is suppressed to a very small amount, so that the amount of air flowing through each air supply pipe 4 does not vary, Uniform aeration can be performed in the treated tank 1 or 1A to 1D.

【0020】次に、本発明の第2実施例を図2を参照し
て説明する。この第2実施例の曝気量調節計101が第
1実施例の曝気量調節計100と構成を異にする点は、
弁部材及びこれに対応した外筒の構成にある。すなわ
ち、第2実施例の弁部材21は、下部側に設けられた下
部フロート22と、中間部に設けられた中間フロート2
3と、上部側に設けられた上部フロート24と、これら
フロート22〜24を連結し、かつ各フロート22、2
3を回転自在に支持するタイロッド25とから構成され
たものである。
Next, a second embodiment of the present invention will be described with reference to FIG. The difference between the aeration amount controller 101 of the second embodiment and the aeration amount controller 100 of the first embodiment is that
In the structure of the valve member and the outer cylinder corresponding to the valve member. That is, the valve member 21 of the second embodiment includes the lower float 22 provided on the lower side and the intermediate float 2 provided on the intermediate portion.
3 and the upper float 24 provided on the upper side, and the floats 22 to 24 are connected to each other.
3 and a tie rod 25 that rotatably supports 3.

【0021】また、外筒10は、上方に向けて径が漸次
拡大される下部テーパ管10aと、中間部に設けられた
中間管10dと、上方に向けて径が漸次縮小する上部テ
ーパ管10cとから構成されたものであって、中間管1
0dは、弁部材21の中間フロート23に対応して上部
側が、上方に向けて径が漸次拡大される形状に形成され
ている。そして、以上のような構成の弁部材21は、下
部フロート22、中間フロート23が、下部テーパ管1
0a、中間管10dのテーパによりそれぞれ下方への移
動が規制される下部位置と、上部フロート24が、上部
テーパ管10cのテーパにより上方への移動が規制され
る上部位置との間で、上下方向に移動されるようになっ
ている。
Further, the outer cylinder 10 has a lower taper pipe 10a whose diameter gradually increases upward, an intermediate pipe 10d provided in an intermediate portion, and an upper taper pipe 10c whose diameter gradually decreases upward. And an intermediate tube 1
0d is formed in a shape in which the upper side corresponding to the intermediate float 23 of the valve member 21 gradually increases in diameter upward. In the valve member 21 configured as described above, the lower float 22 and the intermediate float 23 are
0a, the lower position of the intermediate pipe 10d is restricted by the taper of the intermediate pipe 10d, and the upper float 24 between the upper position where the upward movement of the upper taper pipe 10c is restricted by the taper of the upper taper pipe 10c. It is supposed to be moved to.

【0022】また、下部フロート22、中間フロート2
3において、外側に一部突出した箇所であるかさ部分に
は切り子22A、23Aが形成され、この切り子22
A、23Aによって、空気流通路13に空気が送られた
場合に、下部フロート22、中間フロート23が強制的
に高速回転させられ、これによって弁部材21が外筒1
0の中心部に位置されるようになっている。すなわち、
弁部材21は、図1で示すように外筒10内においてセ
ンターシャフト16に案内されることなく、水平方向に
も自由に動き得る状態にあるが、該弁部材21の下部フ
ロート22、中間フロート23が、切り子22A、23
Aによって高速回転されるようになっているので、該弁
部材21は外筒10側に寄らず、該外筒10の中心に位
置することになる。
Further, the lower float 22 and the intermediate float 2
In FIG. 3, facets 22A and 23A are formed in the bulge portion that is a part that protrudes to the outside.
When air is sent to the air flow passage 13 by A and 23A, the lower float 22 and the intermediate float 23 are forcibly rotated at high speed, whereby the valve member 21 is moved to the outer cylinder 1.
It is located at the center of 0. That is,
As shown in FIG. 1, the valve member 21 is in a state in which it can be freely moved in the horizontal direction without being guided by the center shaft 16 in the outer cylinder 10, but the lower float 22 and the intermediate float of the valve member 21. 23 is a facet 22A, 23
Since the valve member 21 is rotated at a high speed by A, the valve member 21 is located at the center of the outer cylinder 10 without being closer to the outer cylinder 10 side.

【0023】そして、このように下部フロート22、中
間フロート23が回転することによって、弁部材21全
体が外筒10の中心部に位置される第2実施例の方式で
は、第1実施例の弁部材17のように、弁部材17とセ
ンターシャフト16との摩擦が影響することは無く、こ
れによって流量調節時の弁部材21の上下方向の移動を
支障なく行うことができる。
In this way, in the system of the second embodiment in which the whole of the valve member 21 is located in the central portion of the outer cylinder 10 by rotating the lower float 22 and the intermediate float 23 in this way, the valve of the first embodiment is used. Unlike the member 17, the friction between the valve member 17 and the center shaft 16 does not affect, so that the vertical movement of the valve member 21 at the time of adjusting the flow rate can be performed without hindrance.

【0024】なお、上記実施例では、共通の送風機6に
より空気を供給するようにしたが、この共通の送風機6
は1台に限定されず、図3に示すように2台もしくはそ
れ以上設けても良い。また、上記実施例に示す曝気量調
節計100、101のいずれにおいても、タイロッド2
0、25の長さを適宜変更することによって、流量調節
の幅を任意に設定することができる。
Although air is supplied by the common blower 6 in the above embodiment, the common blower 6 is used.
The number is not limited to one, but two or more may be provided as shown in FIG. In addition, in each of the aeration amount controllers 100 and 101 shown in the above embodiment, the tie rod 2
By appropriately changing the lengths of 0 and 25, the width of flow rate adjustment can be set arbitrarily.

【0025】[0025]

【発明の効果】以上の説明から明らかなように本発明の
曝気装置では、供給管の空気流量が相対的に増加した場
合であっても、該供給管に設けられている曝気量調節計
により、空気の増加が微小量に抑えられ、これによって
各供給管で流れる空気の量にばらつきが生じず、処理槽
に貯留される処理液に対してむらの無い曝気を行うこと
ができ、その結果、浄化効率が低下する、腐敗、臭気が
発生する事態を未然に防ぐことが可能となる。
As is apparent from the above description, in the aeration apparatus of the present invention, even if the air flow rate of the supply pipe is relatively increased, the aeration amount controller provided in the supply pipe , The increase in air is suppressed to a very small amount, so that there is no variation in the amount of air flowing through each supply pipe, and it is possible to perform even aeration of the processing liquid stored in the processing tank. It is possible to prevent deterioration of purification efficiency, deterioration, and odor.

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

【図1】第1実施例の曝気量調節計100を示す正断面
図であって、(a)はその正断面図、(b)はセンター
シャフト支持具15(14)の平面図。
FIG. 1 is a front sectional view showing an aeration amount controller 100 of a first embodiment, (a) is a front sectional view thereof, and (b) is a plan view of a center shaft support 15 (14).

【図2】第2実施例の曝気量調節計101を示す正断面
図である。
FIG. 2 is a front sectional view showing an aeration amount controller 101 of a second embodiment.

【図3】共通の送風機を1台または2台設けた場合の配
管図。
FIG. 3 is a piping diagram when one or two common blowers are provided.

【図4】(a)従来の曝気量調節装置50を示す平面
図、(b)は(a)の側面図。
FIG. 4A is a plan view showing a conventional aeration amount control device 50, and FIG. 4B is a side view of FIG.

【図5】従来の曝気量調節装置51を示す平面図。FIG. 5 is a plan view showing a conventional aeration amount adjusting device 51.

【図6】従来の曝気量調節装置52を示す平面図。FIG. 6 is a plan view showing a conventional aeration amount adjusting device 52.

【符号の説明】[Explanation of symbols]

1 処理槽 4 空気供給管 6 送風機 10 外筒(筒状体) 13 空気流通路 17 弁部材 18 下部フロート 19 上部フロート 21 弁部材 22 下部フロート 24 上部フロート 100 曝気量調節計 101 曝気量調節計 1 treatment tank 4 air supply pipe 6 blower 10 outer cylinder (cylindrical body) 13 air flow passage 17 valve member 18 lower float 19 upper float 21 valve member 22 lower float 24 upper float 100 aeration amount controller 101 aeration amount controller

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 共通の送風機から送られた曝気流体を複
数の供給管に分割し、各供給管の途中にて、曝気量調節
計により曝気流体の流量を調節するようにした曝気装置
において、 前記曝気量調節計は、曝気流体が流通する筒状体と、筒
状体内に配置されかつ該筒状体の軸方向に沿って移動自
在に設けられた弁部材とを有し、 前記弁部材は、筒状体の下部位置と上部位置との間で移
動自在であり、下方への移動に伴って筒状体との間隔を
漸次縮小させる下部フロートと、上方への移動に伴って
筒状体との間隔を漸次縮小させる上部フロートとが一体
に設けられたものであることを特徴とする曝気装置。
1. An aerator in which aeration fluid sent from a common blower is divided into a plurality of supply pipes, and the flow rate of the aeration fluid is adjusted by an aeration amount controller in the middle of each supply pipe, The aeration amount controller has a tubular body through which the aeration fluid flows, and a valve member disposed in the tubular body and movably provided along an axial direction of the tubular body, the valve member Is movable between a lower position and an upper position of the tubular body, and has a lower float that gradually reduces the interval between the tubular body and the tubular body as it moves downward and a tubular shape that moves upward. An aerator characterized by being integrally provided with an upper float that gradually reduces the distance from the body.
JP10966993A 1993-05-11 1993-05-11 Aeration device Withdrawn JPH06320185A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10966993A JPH06320185A (en) 1993-05-11 1993-05-11 Aeration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10966993A JPH06320185A (en) 1993-05-11 1993-05-11 Aeration device

Publications (1)

Publication Number Publication Date
JPH06320185A true JPH06320185A (en) 1994-11-22

Family

ID=14516172

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10966993A Withdrawn JPH06320185A (en) 1993-05-11 1993-05-11 Aeration device

Country Status (1)

Country Link
JP (1) JPH06320185A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006205125A (en) * 2005-01-31 2006-08-10 Nishihara Engineering Co Ltd System for treating waste water
JP2007229662A (en) * 2006-03-02 2007-09-13 Japan Water Agency Submerged combined aerator
CN111747544A (en) * 2020-07-06 2020-10-09 泉州奔众空气过滤网有限公司 Sewage precipitation treatment pre-buried formula prevents blockking up decontamination aeration pipe subassembly
CN111747543A (en) * 2020-07-06 2020-10-09 泉州奔众空气过滤网有限公司 Aeration treatment method of aeration pipe assembly

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006205125A (en) * 2005-01-31 2006-08-10 Nishihara Engineering Co Ltd System for treating waste water
JP2007229662A (en) * 2006-03-02 2007-09-13 Japan Water Agency Submerged combined aerator
JP4747006B2 (en) * 2006-03-02 2011-08-10 独立行政法人水資源機構 Submerged combined aeration equipment
CN111747544A (en) * 2020-07-06 2020-10-09 泉州奔众空气过滤网有限公司 Sewage precipitation treatment pre-buried formula prevents blockking up decontamination aeration pipe subassembly
CN111747543A (en) * 2020-07-06 2020-10-09 泉州奔众空气过滤网有限公司 Aeration treatment method of aeration pipe assembly

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