JP2003144876A - Air diffuser - Google Patents

Air diffuser

Info

Publication number
JP2003144876A
JP2003144876A JP2001349506A JP2001349506A JP2003144876A JP 2003144876 A JP2003144876 A JP 2003144876A JP 2001349506 A JP2001349506 A JP 2001349506A JP 2001349506 A JP2001349506 A JP 2001349506A JP 2003144876 A JP2003144876 A JP 2003144876A
Authority
JP
Japan
Prior art keywords
air
diffuser
tube
base end
air diffuser
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.)
Granted
Application number
JP2001349506A
Other languages
Japanese (ja)
Other versions
JP3784303B2 (en
Inventor
Tatsuya Uejima
達也 上島
Masaaki Nagano
昌章 永野
Yasunobu Okajima
康信 岡島
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP2001349506A priority Critical patent/JP3784303B2/en
Publication of JP2003144876A publication Critical patent/JP2003144876A/en
Application granted granted Critical
Publication of JP3784303B2 publication Critical patent/JP3784303B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an air diffuser which can equalize an air quantity jetted from each diffusion hole of an air diffuser tube, consequently can increase the effect of an action by diffusion. SOLUTION: A plurality of diffusion holes 11 are provided in the diffuser tube 4 immersed in a tank, and an air supply source is connected to the base end of the diffuser tube 4. The diffuser tube 4 is arranged on the decline from the base end toward the tip part of the diffuser tube 4 so as to make a predetermined difference of water depth between the tip part and the base end. Thereby, back pressure which acts on each diffusion hole 11 of the diffuser tube 4 is gradually increased near the tip part.

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は散気装置に関し、反
応槽内に気体を平均して散気する技術に係るものであ
る。 【0002】 【従来の技術】従来、下水処理、上水処理等において反
応槽内に空気等の気体を散気する散気装置は、一般的に
槽内に浸漬する散気管に複数の散気孔を軸心方向に沿っ
て適当間隔で設けており、散気管は先端を構造的に閉塞
するか、バルブで閉栓しており、基端側にブロワを接続
している。 【0003】散気装置はブロワから供給する空気を散気
管の各散気孔から槽内液中に噴出させて槽内液の曝気や
攪拌、酸素供給等を行うが、散気による槽内液の攪拌や
酸素供給等の効果の有効性を高めるためには、散気管の
各散気孔から噴出する空気量が均一であることが望まし
い。 【0004】 【発明が解決しようとする課題】しかし、散気管が長尺
である場合には、散気管の各散気孔から噴出する空気量
は均一でなく、散気管は空気が流入する基端に近い程に
散気孔から噴出する空気量が少なく、先端に近い程に散
気孔から噴出する空気量が多くなる。 【0005】このため、基端に近い程に散気孔の口径を
大きくしてその圧力損失を小さくし、先端に近い程に散
気孔の口径を小さくしてその圧力損失を大きくすること
で、各散気孔から噴出する空気量を平均化することが可
能である。また、散気管に形成する散気孔の配置ピッチ
を基端に近い程に小さくしてその分布密度を高め、散気
孔の配置ピッチを先端に近い程に大きくしてその分布密
度を低めることで、噴出する空気量を散気管全体として
平均化することが可能である。 【0006】しかし、散気孔の口径や配置ピッチを計算
によって予め求めることは困難であり、散気孔の口径や
配置ピッチが異なる多数の散気管を用意し、経験則とし
て散気孔の口径や配置ピッチの最適条件を決定すること
は困難であり、現実的な方途ではない。 【0007】本発明は上記した課題を解決するものであ
り、散気管の各散気孔から噴出する空気量を平均化して
散気による作用効果を高めることができる散気装置を提
供することを目的とする。 【0008】 【課題を解決するための手段】上記課題を解決するため
に、本発明の散気装置は、槽内に浸漬する散気管に複数
の散気孔を設け、散気管の基端に空気供給源を接続し、
散気管を基端から先端に向けて下り勾配で傾斜配置して
散気管の先端と基端との間に所定水深差を生じさせるこ
とで、散気管の各散気孔に作用する背圧を先端に近い程
に漸次に高く設定したものである。 【0009】上記した構成において、各散気孔から噴出
する空気量は散気管内の圧力と各散気孔に背圧として作
用する水圧との差圧によって決まり、散気管内の圧力分
布の傾向は基端側から先端側へ漸次に高くなり、この圧
力分布は散気管の姿勢に影響されずほぼ一定である。こ
のため、先端に近い程に各散気孔に作用する背圧を高く
することで、散気管内の圧力と各散気孔の背圧との差圧
を一定となし、噴出する空気量を平均化する。 【0010】 【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1〜図3において、曝気槽1に
浸漬した散気装置2は散気ケース3の内部に散気管4を
配置しており、散気管4の基端に接続した空気供給管5
にブロワ6を設け、散気管4の先端に接続した洗浄用管
7に洗浄用バルブ8を設けている。 【0011】散気管4は所定口径の大径管からなる幹管
9と、幹管9の下方に配置した所定口径の小径管からな
る複数の枝管10とからなる。枝管10は逆T字形をな
し、上部の一端で幹管9に連通するとともに、両端が幹
管9の下方位置で開口しており、枝管10の上部位に複
数の散気孔11を設けている。 【0012】散気管4は幹管9の基端から先端に向けて
下り勾配で傾斜して配置しており、散気管4の幹管9の
先端と基端との間に5〜20mmの所定水深差Lを生じ
させている。この傾斜は散気管4と散気ケース3のフレ
ームとの間にスペーサ等を介装することで与える。この
結果、曝気槽1の槽内液の水圧によって散気管4の各散
気孔11に作用する背圧は幹管9の先端に近い程に漸次
に高くなる。 【0013】散気管4の両端の水深差の適値は散気管4
の勾配を変化させて経験的に求め、後述するように、散
気管4の内部圧力と各散気孔11の背圧との差圧が一定
となり、各散気孔11から噴出する空気量が均一となる
水深差とする。 【0014】以下、上記した構成における作用を説明す
る。散気運転時には洗浄用バルブ8を閉栓した状態で、
ブロア6から所定圧力の空気を散気管4へ供給する。こ
の空気は幹管9を通して各枝管10に流れ、枝管10の
両端の開口に達する前に各散気孔11から曝気槽1の槽
内液中に噴出する。 【0015】各散気孔11から噴出する空気量は散気管
4の内部圧力と各散気孔11に背圧として作用する水圧
との差圧によって決まる。散気管4の内部の圧力分布の
傾向は基端側から先端側へ漸次に高くなり、この圧力分
布は散気管4の姿勢に影響されずほぼ一定である。 【0016】図6は散気管4の内部の圧力分布を測定し
た結果を示すものであり、散気管4を水平に配置した状
態で散気管に供給する空気量を変化させた場合と、本実
施の形態のように散気管4を傾斜配置した状態で散気管
4に供給する空気量を変化させた場合とについて開示し
ており、測定位置を示す符号は幹管9の基端側から先端
側へ順次に大きくなる。 【0017】a折線は散気管4が水平で0.625m3
/minの空気量の場合を示し、b折線は散気管4が水
平で0.75m3/minの空気量の場合を示し、c折
線は散気管4が水平で0.9m3/minの空気量の場
合を示し、d折線は散気管4が入口側(基端側)で10
mm高くなるように傾斜して0.625m3/minの
空気量の場合を示し、e折線は散気管4が入口側(基端
側)で10mm高くなるように傾斜して0.75m3
minの空気量の場合を示し、f折線は散気管4が入口
側(基端側)で10mm高くなるように傾斜して0.9
3/minの空気量の場合を示している。a〜cを求
めた水位とe〜fを求めた水位とは多少異なっており、
そのために水圧に差異が見られる。 【0018】しかし、散気管4が水平であるか傾斜して
いるかに拘わらず、空気量の多寡に拘わらず、圧力分布
の傾向はほぼ一定であり、幹管9の先端に近い程に圧力
が高くなる傾向がある。 【0019】一方、散気管4の各散気孔11に作用する
背圧は、散気管4を先端に向けて下り勾配に傾斜して配
置し、散気管4の先端と基端との間に所定水深差を生じ
させることで、先端に近い程に各散気孔11に作用する
背圧が高くなる。このため、散気管4の内部圧力と各散
気孔11の背圧との差圧が一定となり、各散気孔11か
ら噴出する空気量が平均化される。 【0020】図4は散気管4を水平に配置した状態で各
枝管10の散気孔11における空気量を測定した結果を
示すものであり、a折線は供給空気量が0.625m3
/minの場合を示し、b折線は供給空気量が0.75
3/minの場合を示し、c折線は供給空気量が0.
9m3/minの場合を示している。 【0021】このように、散気管4を水平に配置した場
合には幹管9の先端に近い程に散気孔11から噴出する
空気量が多くなる。図5は散気管4を入口側(基端側)
で10mm高くなるように傾斜して配置した状態で各枝
管10の散気孔11における空気量を測定した結果を示
すものであり、a折線は供給空気量が0.625m3
minの場合を示し、b折線は供給空気量が0.75m
3/minの場合を示し、c折線は供給空気量が0.9
3/minの場合を示している。 【0022】このように、散気管4を先端と基端との間
に所定水深差が生じるように傾斜配置した場合には、各
散気孔11から噴出する空気量が平均化される。洗浄時
には、洗浄用バルブ8を開栓し、ブロア6から散気管4
の幹管9に供給する空気を洗浄用管7を通して大気圧下
に排気する。 【0023】このとき、散気管4の幹管9の内部を流れ
る空気が枝管10の散気孔11に比べて背圧および抵抗
の小さい洗浄用管7の排気口(大気圧下)へ向って流れ
ることで、槽内液が散気孔11を通して枝管10および
幹管9の内部に流入する。槽内液は枝管10および幹管
9の内部の付着物を洗い流し、幹管9を流れる空気とと
もに洗浄用管7へ流入し、エアリフト作用によって排気
口から排出される。 【0024】圧力の低下した散気管4へ槽内液が急激に
流入するとその抵抗によって内部の圧力が高まって槽内
液の流入が停止し、洗浄用管7でのエアリフト作用によ
って散気管4の内部の槽内液を排出して散気管4の内部
の圧力が低下すると槽内液が再び散気管4へ流入し、散
気管4および洗浄用管7において脈動が発生する。 【0025】このように脈動が発生して散気管4の内部
の圧力が急激な増減を繰り返して変化し、散気管4の内
部に急速な槽内液の流れが反復的に生じることで散気管
4の内部の付着物を洗浄する効果が高まる。 【0026】 【発明の効果】以上のように、本発明によれば、散気管
を空気供給源に接続する基端から先端に向けて下り勾配
で傾斜配置して散気管の先端と基端との間に所定水深差
を生じさせ、散気管の各散気孔に作用する背圧を先端に
近い程に漸次に高く設定することで、散気管内の圧力と
各散気孔の背圧との差圧を一定となし、噴出する空気量
を平均化することができる。
Description: BACKGROUND OF THE INVENTION [0001] 1. Field of the Invention [0002] The present invention relates to a diffuser, and more particularly to a technique for averaging and diffusing gas in a reaction tank. 2. Description of the Related Art Conventionally, a diffuser for diffusing gas such as air into a reaction tank in sewage treatment, water supply treatment, or the like, generally includes a plurality of diffusing holes in a diffuser pipe immersed in the tank. Are provided at appropriate intervals along the axial direction, and the diffuser tube is structurally closed at the distal end or closed with a valve, and a blower is connected to the proximal end side. [0003] The air diffuser blows air supplied from a blower into the liquid in the tank from each of the air diffusion holes of the air diffuser to aerate and agitate the liquid in the tank, supply oxygen, and the like. In order to enhance the effectiveness of effects such as stirring and oxygen supply, it is desirable that the amount of air ejected from each diffuser hole of the diffuser tube be uniform. [0004] However, when the air diffuser is long, the amount of air ejected from each diffuser hole of the air diffuser is not uniform, and the air diffuser is located at the base end where air flows in. The closer to the end, the smaller the amount of air ejected from the diffuser holes, and the closer to the tip, the greater the amount of air ejected from the diffuser holes. [0005] For this reason, by increasing the diameter of the diffuser hole closer to the base end to reduce its pressure loss, and by decreasing the diameter of the diffuser hole closer to the distal end to increase its pressure loss, It is possible to equalize the amount of air ejected from the diffusing holes. Also, by reducing the arrangement pitch of the diffuser holes formed in the diffuser tube closer to the base end to increase the distribution density, and increasing the arrangement pitch of the diffuser holes closer to the distal end to lower the distribution density, It is possible to average out the amount of air to be blown out as an entire diffuser. However, it is difficult to obtain the diameter and arrangement pitch of the diffusing holes in advance by calculation, and a large number of diffusing tubes having different diameters and arrangement pitches of the diffusing holes are prepared. It is difficult to determine the optimal conditions of the above, and it is not a practical way. An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to provide an air diffuser capable of averaging the amount of air blown out from each air diffuser hole of a diffuser tube to enhance the effect of the air diffuser. And [0008] In order to solve the above-mentioned problems, a diffuser according to the present invention is provided with a plurality of diffuser holes in a diffuser tube immersed in a tank, and air is provided at a base end of the diffuser tube. Connect the source,
The back pressure acting on each diffuser hole of the diffuser tube is set at the distal end by arranging the diffuser tube at a downward slope from the base end to the distal end and causing a predetermined water depth difference between the distal end and the base end of the diffuser tube. Is set to be gradually higher as is closer to. In the above arrangement, the amount of air ejected from each diffuser is determined by the pressure difference between the pressure in the diffuser and the water pressure acting as a back pressure on each diffuser. The pressure gradually increases from the end to the tip, and this pressure distribution is substantially constant without being affected by the attitude of the air diffuser. For this reason, by increasing the back pressure acting on each diffuser hole closer to the tip, the differential pressure between the pressure inside the diffuser pipe and the back pressure of each diffuser hole is made constant, and the amount of air blown out is averaged I do. Embodiments of the present invention will be described below with reference to the drawings. 1 to 3, an air diffuser 2 immersed in an aeration tank 1 has an air diffuser 4 disposed inside an air diffuser case 3 and an air supply pipe 5 connected to a base end of the diffuser 4.
Is provided with a blower 6, and a cleaning valve 8 is provided in a cleaning tube 7 connected to the tip of the diffuser tube 4. The air diffuser 4 comprises a main pipe 9 composed of a large-diameter pipe having a predetermined diameter, and a plurality of branch pipes 10 composed of small-diameter pipes having a predetermined diameter disposed below the main pipe 9. The branch pipe 10 has an inverted T-shape, communicates with the main pipe 9 at one upper end, and both ends are open at a position below the main pipe 9, and a plurality of air diffusion holes 11 are provided at an upper portion of the branch pipe 10. ing. The diffuser tube 4 is arranged so as to be inclined downward from the base end of the main tube 9 toward the distal end thereof, and a predetermined distance of 5 to 20 mm is provided between the distal end and the base end of the main tube 9 of the diffuser tube 4. A water depth difference L is generated. This inclination is given by interposing a spacer or the like between the diffuser tube 4 and the frame of the diffuser case 3. As a result, the back pressure acting on each diffuser hole 11 of the diffuser tube 4 due to the water pressure of the liquid in the aeration tank 1 gradually increases nearer to the tip of the main pipe 9. The appropriate value of the water depth difference between both ends of the diffuser 4 is
Empirically obtained by changing the gradient of the air, and as described later, the differential pressure between the internal pressure of the air diffuser 4 and the back pressure of each air diffuser 11 becomes constant, and the amount of air ejected from each air diffuser 11 becomes uniform. Water depth difference. The operation of the above configuration will be described below. During the aeration operation, with the cleaning valve 8 closed,
Air of a predetermined pressure is supplied from the blower 6 to the air diffuser 4. This air flows into each branch pipe 10 through the main pipe 9, and blows out from each air diffusion hole 11 into the liquid in the aeration tank 1 before reaching the openings at both ends of the branch pipe 10. The amount of air ejected from each diffuser hole 11 is determined by the pressure difference between the internal pressure of the diffuser tube 4 and the water pressure acting as a back pressure on each diffuser hole 11. The tendency of the pressure distribution inside the air diffuser 4 gradually increases from the base end to the distal end, and this pressure distribution is substantially constant without being affected by the attitude of the air diffuser 4. FIG. 6 shows the result of measuring the pressure distribution inside the air diffuser 4, in which the amount of air supplied to the air diffuser 4 is changed while the air diffuser 4 is horizontally arranged, and in the present embodiment. And the case where the amount of air supplied to the air diffuser 4 is changed in a state where the air diffuser 4 is inclined as in the embodiment described above, and the reference numeral indicating the measurement position is from the base end side to the distal end side of the main pipe 9. Sequentially increases. The folding line a indicates that the diffuser 4 is horizontal and 0.625 m 3.
The b-fold line shows the case where the air diffuser 4 is horizontal and the air amount is 0.75 m 3 / min, and the c-fold line shows the case where the air diffuser 4 is horizontal and the air amount is 0.9 m 3 / min. The d-fold line indicates that the air diffuser 4 has 10 points on the inlet side (base end side).
In this case, the air flow rate is 0.625 m 3 / min when the air diffuser 4 is inclined to increase by 10 mm on the inlet side (proximal end side) and 0.75 m 3 / min.
In the case of the air amount of min, the f-shaped line is inclined by 0.9 mm so that the air diffuser 4 becomes higher by 10 mm on the inlet side (base end side).
The case of the air amount of m 3 / min is shown. The water levels for which a to c were determined are slightly different from the water levels for which e to f were determined,
Therefore, there is a difference in water pressure. However, regardless of whether the air diffuser 4 is horizontal or inclined, the tendency of the pressure distribution is almost constant irrespective of the amount of air, and the closer the pressure is to the tip of the main pipe 9, the more the pressure becomes. Tends to be higher. On the other hand, the back pressure acting on each diffuser hole 11 of the diffuser tube 4 is set such that the diffuser tube 4 is arranged with a downward inclination toward the distal end, and is provided between the distal end and the proximal end of the diffuser tube 4. By producing a water depth difference, the back pressure acting on each diffuser hole 11 becomes higher nearer to the tip. For this reason, the differential pressure between the internal pressure of the diffuser pipe 4 and the back pressure of each diffuser hole 11 becomes constant, and the amount of air ejected from each diffuser hole 11 is averaged. FIG. 4 shows the result of measuring the amount of air in the air diffusing holes 11 of each branch pipe 10 in a state where the diffusing pipe 4 is arranged horizontally. The broken line a indicates that the supplied air amount is 0.625 m 3.
/ Min, and the b-fold line indicates that the supply air amount is 0.75.
The case of m 3 / min is shown.
The case of 9 m 3 / min is shown. As described above, when the diffuser tube 4 is arranged horizontally, the amount of air blown out from the diffuser holes 11 becomes larger as it comes closer to the tip of the main tube 9. Fig. 5 shows the diffuser 4 on the inlet side (proximal side)
FIG. 6 shows the result of measuring the air amount in the air diffusing holes 11 of each branch pipe 10 in a state where it is inclined so as to be higher by 10 mm. The a-fold line indicates that the supply air amount is 0.625 m 3 /.
min, the b-fold line indicates that the supply air amount is 0.75 m
3 / min, and the c-fold line indicates that the supply air amount is 0.9.
The case of m 3 / min is shown. As described above, when the diffuser tube 4 is arranged so as to be inclined so that a predetermined water depth difference is generated between the distal end and the proximal end, the amount of air ejected from each diffuser hole 11 is averaged. At the time of cleaning, the cleaning valve 8 is opened and the air diffuser 4
The air supplied to the main pipe 9 is exhausted under the atmospheric pressure through the cleaning pipe 7. At this time, the air flowing inside the main pipe 9 of the air diffuser 4 is directed toward the exhaust port (under atmospheric pressure) of the cleaning pipe 7 having a lower back pressure and resistance than the air diffuser holes 11 of the branch pipe 10. By flowing, the liquid in the tank flows into the branch pipe 10 and the main pipe 9 through the air diffusion holes 11. The liquid in the tank rinses off the deposits inside the branch pipe 10 and the main pipe 9, flows into the cleaning pipe 7 together with the air flowing through the main pipe 9, and is discharged from the exhaust port by an air lift action. When the liquid in the tank suddenly flows into the diffuser pipe 4 having a reduced pressure, the internal pressure increases due to the resistance, and the flow of the liquid in the tank is stopped. When the liquid in the tank is discharged and the pressure inside the diffuser tube 4 decreases, the liquid in the tank flows into the diffuser tube 4 again, and pulsation occurs in the diffuser tube 4 and the cleaning tube 7. As described above, the pulsation is generated, and the pressure inside the air diffuser 4 is repeatedly changed rapidly, and a rapid flow of the liquid in the tank is repeatedly generated inside the air diffuser 4. The effect of cleaning the deposits inside 4 is enhanced. As described above, according to the present invention, the air diffuser is inclined at a downward gradient from the base end connected to the air supply source to the front end, and the front end and the base end of the air diffuser are connected to each other. Between the pressure in the diffuser and the back pressure of each diffuser by gradually increasing the back pressure acting on each diffuser in the diffuser nearer to the tip. The pressure is kept constant, and the amount of air blown out can be averaged.

【図面の簡単な説明】 【図1】本発明の実施の形態における散気装置を示す正
面図である。 【図2】同散気装置の散気管を示す横断面図である。 【図3】同散気装置の散気管を示す要部拡大図である。 【図4】散気管を水平とする状態での各散気孔における
空気量を示すグラフ図である。 【図5】散気管を傾斜配置する状態での各散気孔におけ
る空気量を示すグラフ図である。 【図6】散気管の内部圧力分布を示すグラフ図である。 【符号の説明】 1 曝気槽 2 散気装置 3 散気ケース 4 散気管 5 空気供給管 6 ブロワ 7 洗浄用管 8 洗浄用バルブ 9 幹管 10 枝管 11 散気孔
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a front view showing an air diffuser according to an embodiment of the present invention. FIG. 2 is a cross-sectional view showing an air diffusion tube of the air diffusion device. FIG. 3 is an enlarged view of a main part showing an air diffusion tube of the air diffusion device. FIG. 4 is a graph showing the amount of air in each diffuser hole when the diffuser is horizontal. FIG. 5 is a graph showing the amount of air in each air diffusion hole in a state where the air diffusion pipe is inclined. FIG. 6 is a graph showing an internal pressure distribution of the air diffuser. [Description of Signs] 1 Aeration tank 2 Air diffuser 3 Air diffuser case 4 Air diffuser 5 Air supply pipe 6 Blower 7 Cleaning pipe 8 Cleaning valve 9 Main pipe 10 Branch pipe 11 Air diffuser

───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡島 康信 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 Fターム(参考) 4D029 AA01 AB07 BB10 4G035 AB07 AC15 AE13    ────────────────────────────────────────────────── ─── Continuation of front page    (72) Inventor Yasunobu Okajima             2-47 Shikitsu Higashi, Naniwa-ku, Osaka-shi, Osaka               Kubota Corporation F term (reference) 4D029 AA01 AB07 BB10                 4G035 AB07 AC15 AE13

Claims (1)

【特許請求の範囲】 【請求項1】 槽内に浸漬する散気管に複数の散気孔を
設け、散気管の基端に空気供給源を接続し、散気管を基
端から先端に向けて下り勾配で傾斜配置して散気管の先
端と基端との間に所定水深差を生じさせることで、散気
管の各散気孔に作用する背圧を先端に近い程に漸次に高
く設定したことを特徴とする散気装置。
Claims: 1. A plurality of air diffusion holes are provided in an air diffuser tube immersed in a tank, an air supply source is connected to a base end of the air diffuser tube, and the air diffuser tube descends from the base end to the distal end. By forming a predetermined difference in water depth between the tip and base end of the air diffuser by arranging it with a gradient, the back pressure acting on each air diffusion hole of the air diffuser is set to gradually increase as it approaches the tip. Characteristic air diffuser.
JP2001349506A 2001-11-15 2001-11-15 Air diffuser Expired - Fee Related JP3784303B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001349506A JP3784303B2 (en) 2001-11-15 2001-11-15 Air diffuser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001349506A JP3784303B2 (en) 2001-11-15 2001-11-15 Air diffuser

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Publication Number Publication Date
JP2003144876A true JP2003144876A (en) 2003-05-20
JP3784303B2 JP3784303B2 (en) 2006-06-07

Family

ID=19162164

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3784303B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011092835A (en) * 2009-10-28 2011-05-12 Mitsubishi Rayon Co Ltd Method for operating aeration device
WO2014065268A1 (en) 2012-10-25 2014-05-01 三菱レイヨン株式会社 Aeration device, operation method therefor, and water treatment apparatus
JP2015085314A (en) * 2013-09-26 2015-05-07 三菱レイヨン株式会社 Air diffusion device and water treatment apparatus
CN107935209A (en) * 2017-10-26 2018-04-20 上海市政工程设计研究总院(集团)有限公司 One kind aeration partial pressure control method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011092835A (en) * 2009-10-28 2011-05-12 Mitsubishi Rayon Co Ltd Method for operating aeration device
WO2014065268A1 (en) 2012-10-25 2014-05-01 三菱レイヨン株式会社 Aeration device, operation method therefor, and water treatment apparatus
JP2015085314A (en) * 2013-09-26 2015-05-07 三菱レイヨン株式会社 Air diffusion device and water treatment apparatus
CN107935209A (en) * 2017-10-26 2018-04-20 上海市政工程设计研究总院(集团)有限公司 One kind aeration partial pressure control method
CN107935209B (en) * 2017-10-26 2024-01-19 上海市政工程设计研究总院(集团)有限公司 Aeration partial pressure control method

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