JPH07236819A - Air bubble disperser - Google Patents

Air bubble disperser

Info

Publication number
JPH07236819A
JPH07236819A JP6052948A JP5294894A JPH07236819A JP H07236819 A JPH07236819 A JP H07236819A JP 6052948 A JP6052948 A JP 6052948A JP 5294894 A JP5294894 A JP 5294894A JP H07236819 A JPH07236819 A JP H07236819A
Authority
JP
Japan
Prior art keywords
hollow fiber
bubble
fiber membrane
bubbles
case
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Withdrawn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
JP6052948A
Other languages
Japanese (ja)
Inventor
Ichiro Tominaga
一郎 富永
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.)
Nok Corp
Original Assignee
Nok 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 Nok Corp filed Critical Nok Corp
Priority to JP6052948A priority Critical patent/JPH07236819A/en
Publication of JPH07236819A publication Critical patent/JPH07236819A/en
Withdrawn legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To enhance the washing effect of a hollow yarn membrane while achieving the protection of the hollow yarn membrane and facilitating the production of thereof. CONSTITUTION:This air bubble disperser is equipped with a rotary member 21 supported within a case having a liquid received therein in a freely rotatable manner, an air bubble supply part 12 supplying air bubbles A into the liquid from under side of the rotary member 21 and a rotary member driving means 20 converting the buoyancy of the air bubbles A to the rotatory power of the rotary member 21.

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、たとえば中空糸膜モジ
ュールのケース内の中空糸膜の表面に堆積した堆積物を
取り除くためにケース内の液中に気泡を供給する気泡分
散機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a bubble disperser for supplying bubbles into a liquid in a case of a hollow fiber membrane module in order to remove deposits accumulated on the surface of the hollow fiber membrane.

【0002】[0002]

【従来の技術】従来より、中空糸膜モジュールは、たと
えば図8に示すようなものがある。すなわち、この中空
糸膜モジュール100は、多数本の中空糸膜101の束
の両端末部にて各中空糸膜101の一方の端末を開口状
態に保ちつつ各中空糸膜101間を接着固定すべく各中
空糸膜101間の隙間を封止材102にて封止固定(ポ
ッティング)された中空糸膜束103を、各中空糸膜1
01の端末が開口されてポッティングされている中空糸
膜開口端面111を有するポッティング部104にてケ
ース105内に吊設部材106を介して吊設されたもの
である。
2. Description of the Related Art Conventionally, there is a hollow fiber membrane module as shown in FIG. That is, in this hollow fiber membrane module 100, one end of each hollow fiber membrane 101 is kept open at both end portions of a bundle of a large number of hollow fiber membranes 101 while the hollow fiber membranes 101 are bonded and fixed to each other. Therefore, the hollow fiber membrane bundle 103, in which the gap between the hollow fiber membranes 101 is sealed and fixed (potted) by the sealing material 102, is used for each hollow fiber membrane 1
The end of No. 01 is suspended in the case 105 via the suspending member 106 at the potting portion 104 having the open end surface 111 of the hollow fiber membrane which is opened and potted.

【0003】ケース105には、底部にケース105内
に気泡Aを供給する気泡供給部としての気泡供給ポート
107を有し、上部に透過液出口108を有し、ポッテ
ィング部104の軸方向内側近傍の側面にケース105
内に原液を供給するための原液供給口109を有し、そ
の原液供給口109と断面で見て対向する側面にケース
105から気泡Aを抜け出させる気泡抜口110を有し
ている。
The case 105 has a bubble supply port 107 as a bubble supply part for supplying the bubble A into the case 105 at the bottom, a permeate outlet 108 at the top, and an axially inner side of the potting part 104. On the side of the case 105
A stock solution supply port 109 for supplying the stock solution is provided therein, and a bubble outlet 110 for letting the bubbles A escape from the case 105 is provided on a side surface facing the stock solution supply port 109 in cross section.

【0004】そして、上記中空糸膜モジュール100
は、下水処理などの分野で用いられるもので、汚濁物質
が比較的多い濾過等に使用される。濾過は次のように行
なわれる。つまり、原液供給口109よりケース105
内に原液が供給され、この原液が各中空糸膜101の表
面から内部に通ることによって濾過されて透過液が得ら
れ、この透過液は中空糸膜開口端面111を介して透過
液出口108より流出される外圧式となっている。
The hollow fiber membrane module 100 described above is used.
Is used in the field of sewage treatment and the like, and is used for filtration and the like, which contains a relatively large amount of pollutants. Filtration is performed as follows. That is, from the undiluted solution supply port 109 to the case 105
An undiluted solution is supplied into the hollow fiber membrane 101, and the undiluted solution is filtered from the surface of each hollow fiber membrane 101 by passing through the inside to obtain a permeate. It is an external pressure type that is discharged.

【0005】このような濾過運転の際、たびたび濾過圧
が上昇する毎に、気泡Aを気泡供給ポート107を介し
て液中に供給させて、この気泡Aを中空糸膜101に当
てて中空糸膜101の表面に堆積した汚濁物質を取り除
く気泡洗浄を行なっている。
In such a filtration operation, each time the filtration pressure rises, air bubbles A are supplied into the liquid through the air bubble supply port 107, and the air bubbles A are applied to the hollow fiber membrane 101 to cause the hollow fibers to flow. Bubble cleaning is performed to remove contaminants deposited on the surface of the film 101.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記し
た従来技術の場合には、下部のポッティング部112に
気泡Aが当たると気泡Aが片寄って上昇してしまい、中
空糸膜101の片側しか洗浄できない。また、全体を洗
浄すべく気泡Aを多く供給すると、気泡が集中して当た
る部分ができ、その部分における中空糸膜101が損傷
する。
However, in the case of the above-mentioned conventional technique, when the bubble A hits the lower potting portion 112, the bubble A shifts upward, and only one side of the hollow fiber membrane 101 can be washed. . Further, when a large amount of bubbles A are supplied to wash the whole, a portion where the bubbles are concentrated and hit is formed, and the hollow fiber membrane 101 in that portion is damaged.

【0007】そこで、中空糸膜束103に対して全周的
に気泡Aを供給するために、図9に示すようなリング状
のチューブ113に下向きに開けられた複数の穴114
が全周的に設けられ、チューブ113には気泡供給ポー
ト107と連通する管115が連結された構造物をケー
ス105の底部に設けた中空糸膜モジュール100があ
る。
Therefore, in order to supply the air bubbles A to the hollow fiber membrane bundle 103 all around, a plurality of holes 114 opened downward in a ring-shaped tube 113 as shown in FIG.
There is a hollow fiber membrane module 100 in which a structure in which a tube 115 communicating with the bubble supply port 107 is connected to the tube 113 is provided on the bottom of the case 105.

【0008】しかしながら、気泡Aが全周的に供給され
はするものの、気泡Aは直接上昇するため、下部のポッ
ティング部112に気泡Aが当たり、気泡Aが片寄る場
合がある。これにより、中空糸膜束103の下部のポッ
ティング部112が気泡Aが片寄った側の反対側に傾
き、一度傾くと復帰できないので、気泡Aは片寄ったま
まとなり、中空糸膜101の片側しか洗浄できなくな
る。
However, although the bubble A is supplied all around, the bubble A rises directly, so that the bubble A may hit the lower potting portion 112 and the bubble A may be offset. As a result, the potting portion 112 at the bottom of the hollow fiber membrane bundle 103 tilts to the opposite side to the side where the air bubbles A are offset, and once tilted, it cannot be restored, so the air bubbles A remain offset and only one side of the hollow fiber membrane 101 is washed. become unable.

【0009】また、気泡Aの片寄りを無くすべく通常の
攪拌機を用いた場合、攪拌機の軸シール、電力供給など
複雑な機構が必要となる。
Further, when a normal stirrer is used to eliminate the deviation of the bubbles A, a complicated mechanism such as a shaft seal of the stirrer and power supply is required.

【0010】本発明は上記した従来技術の課題を解決す
るためになされたもので、その目的とするところは、中
空糸膜の洗浄性の向上を図ると共に、中空糸膜の保護を
図り、さらには製作容易化を図り得る気泡分散機を提供
することにある。
The present invention has been made to solve the above-mentioned problems of the prior art. The purpose of the present invention is to improve the cleaning properties of the hollow fiber membrane and to protect the hollow fiber membrane. Is to provide a bubble disperser capable of facilitating manufacture.

【0011】[0011]

【課題を解決するための手段】上記目的を達成するため
に、本発明にあっては、液体を収納したケース内に回転
自在に支持された回転部材と、該回転部材の下方から液
中に気泡を供給する気泡供給部と、気泡の浮力を回転部
材の回転力に変換する回転部材駆動手段と、を備えてな
ることを特徴とする。
In order to achieve the above object, according to the present invention, a rotating member rotatably supported in a case accommodating a liquid and a liquid from below the rotating member are inserted into the liquid. It is characterized by comprising a bubble supply unit for supplying bubbles, and a rotating member drive means for converting the buoyancy of the bubbles into the rotating force of the rotating member.

【0012】[0012]

【作用】上記構成の気泡分散機にあっては、回転部材が
気泡供給部から供給された気泡の浮力を回転力に変換す
る回転部材駆動手段により回転することにより、気泡の
上昇する位置が移動することになり、気泡が分散されて
液中に供給される。
In the bubble disperser having the above-mentioned structure, the rotating member is rotated by the rotating member drive means for converting the buoyancy of the bubble supplied from the bubble supply unit into the rotating force, whereby the position where the bubble rises is moved. Thus, the bubbles are dispersed and supplied into the liquid.

【0013】[0013]

【実施例】以下に本発明を図示の実施例に基づいて説明
する。図1は本発明の一実施例に係る気泡分散機を示し
ており、この気泡分散機1は図2及び図3に示す中空糸
膜モジュール2のケース3の底部に取付けられるもので
ある。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to illustrated embodiments. FIG. 1 shows a bubble disperser according to an embodiment of the present invention. The bubble disperser 1 is attached to the bottom of a case 3 of a hollow fiber membrane module 2 shown in FIGS. 2 and 3.

【0014】まず、図2に示す中空糸膜モジュール2に
ついて説明する。この中空糸膜モジュール2は、多数本
の中空糸膜4の束の両端末部にて各中空糸膜4の一方の
端末を開口状態に保ちつつ各中空糸膜4間を接着固定す
べく各中空糸膜4間の隙間を封止材5にて封止固定(ポ
ッティング)された中空糸膜束6を、各中空糸膜4の一
方の端末が開口されてポッティングされている中空糸膜
開口端面7を有するポッティング部8にてケース3内に
吊設部材9を介して吊設されたものである。
First, the hollow fiber membrane module 2 shown in FIG. 2 will be described. This hollow fiber membrane module 2 is configured to adhere and fix the hollow fiber membranes 4 to each other while keeping one end of each hollow fiber membrane 4 in an open state at both end portions of a bundle of a large number of hollow fiber membranes 4. A hollow fiber membrane bundle 6 in which one end of each hollow fiber membrane 4 is opened and potted with a hollow fiber membrane bundle 6 in which a gap between the hollow fiber membranes 4 is sealed (potted) with a sealing material 5. A potting portion 8 having an end face 7 is suspended in the case 3 via a suspending member 9.

【0015】ケース3は、中空糸膜束6が収納される収
納部31と、収納部31の一方の開口部を閉塞すると共
に気泡分散機1が取付けられる底部32と、収納部31
の他方の開口部を閉塞すると共に吊設部材9を介して中
空糸膜束6のポッティング部8が吊設されるキャップ3
3とから構成されている。
The case 3 has a housing portion 31 for housing the hollow fiber membrane bundle 6, a bottom portion 32 for closing one opening of the housing portion 31 and the bubble dispersing machine 1 attached thereto, and a housing portion 31.
Cap 3 on which the other opening of the hollow fiber membrane bundle 6 is suspended and the potting portion 8 of the hollow fiber membrane bundle 6 is suspended via the suspension member 9.
3 and 3.

【0016】収納部31は、両端を開口する筒状部材
で、両方の開口部端部にはそれぞれ外向きのフランジ部
31Aを有しており、また中空糸膜束6が吊設されてい
る状態でポッティング部8の軸方向内側近傍の側面にケ
ース3内に濾過対象液としての原液を供給するための原
液供給口10を有し、その原液供給口10と断面で見て
対向する側面にケース3から気泡Aを抜け出させる気泡
抜口11を有している。
The accommodating portion 31 is a tubular member having both ends open, and has outwardly facing flange portions 31A at both opening end portions, and the hollow fiber membrane bundle 6 is suspended. In this state, a stock solution supply port 10 for supplying a stock solution as a liquid to be filtered is provided in the case 3 on the side surface near the inner side in the axial direction of the potting portion 8. It has a bubble outlet 11 for letting out the bubble A from the case 3.

【0017】また底部32は、円盤状で径は収納部31
のフランジ部31Aの外径とほぼ同じとなっており、そ
の中央付近にはケース3内の液中に気泡Aを供給するた
めの気泡供給部としてのエアーノズル12が取付けられ
ている。
The bottom portion 32 has a disk shape and the diameter thereof is the storage portion 31.
The outer diameter of the flange portion 31A is substantially the same as that of the flange portion 31A, and an air nozzle 12 as a bubble supply portion for supplying the bubble A into the liquid in the case 3 is attached near the center thereof.

【0018】キャップ33は、円盤状で径は収納部31
のフランジ部31Aの外径とほぼ同じとなっており、そ
の中央付近には透過液を外部に流出するための軸方向外
側に突出する透過液出口13を有しており、内側には吊
設部材9を取付けるための環状凸部33Aが設けられて
いる。
The cap 33 has a disk shape and a diameter of the storage portion 31.
The outer diameter of the flange portion 31A is substantially the same as that of the outer peripheral portion of the flange portion 31A. An annular convex portion 33A for attaching the member 9 is provided.

【0019】一方吊設部材9は、キャップ33の環状凸
部33Aの内周面に取付けられる凸部91と、中空糸膜
束6のポッティング部8を吊設する吊設部92とから構
成されている。そして、この吊設部材9が集水部15を
有して凸部91の外周面が環状凸部32Aの内周面に対
してシール部材としてのOリング14を介して液密に取
付けられている。また、凸部91には集水部15と透過
液出口13とを連通する軸方向に貫通形成される通路9
3を有している。
On the other hand, the suspension member 9 is composed of a convex portion 91 attached to the inner peripheral surface of the annular convex portion 33A of the cap 33, and a suspension portion 92 for suspending the potting portion 8 of the hollow fiber membrane bundle 6. ing. The suspension member 9 has the water collecting portion 15, and the outer peripheral surface of the convex portion 91 is liquid-tightly attached to the inner peripheral surface of the annular convex portion 32A via the O-ring 14 as a seal member. There is. A passage 9 is formed in the convex portion 91 so as to penetrate the water collecting portion 15 and the permeate outlet 13 in the axial direction.
Have three.

【0020】そして、中空糸膜束6が吊設された後に、
ケース3の収納部31のそれぞれのフランジ部31Aと
底部32及びキャップ33の周縁部とを締付部材16に
て液密に締付ける。
After the hollow fiber membrane bundle 6 is suspended,
The flange portion 31A of the housing portion 31 of the case 3 and the peripheral portion of the bottom portion 32 and the cap 33 are liquid-tightly tightened by the tightening member 16.

【0021】上記構成の中空糸膜モジュール2は、例え
ば下水処理などの分野で用いられ、汚濁物質Dが比較的
多い濾過等に使用される。濾過は次のように行なわれ
る。つまり、原液供給口10よりケース3内に原液が供
給され、この原液が各中空糸膜4の表面から内部に通る
ことによって濾過されて透過液が得られ、この透過液は
中空糸膜開口端面7より集水部15,通路93を介して
透過液出口13より流出される外圧式となっている。
The hollow fiber membrane module 2 having the above structure is used in the field of sewage treatment, for example, and is used for filtration and the like in which pollutant D is relatively large. Filtration is performed as follows. That is, the stock solution is supplied into the case 3 from the stock solution supply port 10, and the stock solution is filtered by passing through the inside from the surface of each hollow fiber membrane 4 to obtain a permeate. The permeate is the hollow fiber membrane opening end surface. 7 is an external pressure type that flows out from the permeate outlet 13 through the water collecting portion 15 and the passage 93.

【0022】このような濾過運転の際、たびたび濾過圧
が上昇する毎に、気泡Aをエアーノズル12を介してケ
ース3内の液中に供給させて、図7(a)に示すように
各中空糸膜4間に堆積した汚濁物質を図7(b)に示す
ように各中空糸膜4に気泡Aを当てて取り除く気泡洗浄
を行なっている。
In such a filtration operation, each time the filtration pressure rises, the bubbles A are supplied into the liquid in the case 3 through the air nozzle 12, and as shown in FIG. As shown in FIG. 7B, bubble A is applied to each hollow fiber membrane 4 to remove the contaminants accumulated between the hollow fiber membranes 4, thereby performing bubble cleaning.

【0023】次に、上記気泡洗浄に用いられる本発明の
一実施例に係る気泡分散機1について図1に基づき説明
する。
Next, a bubble disperser 1 according to an embodiment of the present invention used for the bubble cleaning will be described with reference to FIG.

【0024】この気泡分散機1は、エアーノズル12の
近傍に取付けられており、概略、液体を収納したケース
3内に回転自在に支持された回転部材としての分散用翼
21と、気泡Aの浮力を分散用翼21の回転力に変換す
る回転部材駆動手段20とを備えてなるものである。
This bubble disperser 1 is mounted in the vicinity of the air nozzle 12, and roughly has a dispersing blade 21 as a rotating member rotatably supported in a case 3 containing a liquid, and a bubble A. The rotary member drive means 20 for converting the buoyancy into the rotational force of the dispersion blade 21 is provided.

【0025】分散用翼21は、図1(b)に示すように
円筒状の胴部23の外周面に矩形状の2枚の羽根22を
傾斜させ2等配に設けたものである。尚、羽根22は2
枚ではなく、分散から見て6枚の方が2枚より好適であ
る。
As shown in FIG. 1 (b), the dispersing blade 21 is formed by arranging two rectangular blades 22 on the outer peripheral surface of a cylindrical body portion 23 in an inclined manner. In addition, the blade 22 is 2
From the viewpoint of dispersion, not 6 sheets but 6 sheets is more preferable than 2 sheets.

【0026】回転部材駆動手段20は、軸25と、ケー
ス3の底部32に設けられた軸25の軸受26と、軸2
5に一体的に取付けられるプロペラ27と、分散用翼2
1を軸25に対して固定するための締付部材24とから
構成されている。
The rotary member driving means 20 includes a shaft 25, a bearing 26 for the shaft 25 provided on the bottom 32 of the case 3, and a shaft 2.
5, the propeller 27 integrally attached to the blade 5, and the dispersing blade 2
And a fastening member 24 for fixing 1 to the shaft 25.

【0027】プロペラ27は、軸25の中途部に一体的
に設けられており、その長さは装着時、エアーノズル1
2から供給される気泡Aの浮力を得ることが可能な寸法
となっている。そして、プロペラ27が一体となった軸
25の一端をエアーノズル12の近傍に設けられた軸受
26に挿入し、回転自在に支持する。この軸25の他端
部に分散用翼21の胴部23を挿入し、締付部材24を
介して一体的に固定する。
The propeller 27 is integrally provided at a midway portion of the shaft 25, and its length is such that the air nozzle 1 is mounted at the time of mounting.
The size is such that the buoyancy of the bubbles A supplied from 2 can be obtained. Then, one end of the shaft 25 with which the propeller 27 is integrated is inserted into a bearing 26 provided in the vicinity of the air nozzle 12, and is rotatably supported. The body portion 23 of the dispersing blade 21 is inserted into the other end portion of the shaft 25, and is integrally fixed via the tightening member 24.

【0028】このように構成された気泡分散機1は、エ
アーノズル12より気泡Aが液中に供給されると、この
気泡Aの浮力をプロペラ27が受け、プロペラ27が回
転する。このことにより、軸25を介して分散用翼21
が回転し、その回転による分散用翼21がつくる流れを
利用して分散用翼21の下方から供給された気泡Aが分
散される。このように気泡Aが分散された状態で、各中
空糸膜4間に堆積した汚濁物Dを取り除く洗浄が行なわ
れる。
In the bubble disperser 1 thus constructed, when the air bubble 12 is supplied into the liquid from the air nozzle 12, the propeller 27 receives the buoyancy of the air bubble A and the propeller 27 rotates. As a result, the dispersion blades 21
Rotates and the bubbles A supplied from below the dispersing blade 21 are dispersed by utilizing the flow created by the dispersing blade 21 due to the rotation. With the air bubbles A thus dispersed, cleaning is performed to remove the contaminant D accumulated between the hollow fiber membranes 4.

【0029】気泡洗浄の具体例を示すと、図3に示すよ
うな中空糸膜4の長さL:800〜1000mm、中空糸
膜束6の外径d:80mm、ケース3の外径D:100mm
の中空糸膜モジュール2の洗浄は約1〜1.5時間おき
に3〜5分の気泡Aを供給(バブリング)する。流量は
800Nl/hr 程度。そして、バブリング時間を3分とす
ると、上記気泡分散機1によれば0.3〜1rpm で良
い。
As a specific example of the bubble cleaning, the length L of the hollow fiber membrane 4 as shown in FIG. 3 is 800 to 1000 mm, the outer diameter d of the hollow fiber membrane bundle 6 is 80 mm, and the outer diameter D of the case 3 is: 100 mm
For cleaning the hollow fiber membrane module 2, the bubbles A are supplied (bubbled) for about 3 to 5 minutes at intervals of about 1 to 1.5 hours. The flow rate is about 800 Nl / hr. If the bubbling time is 3 minutes, 0.3 to 1 rpm is sufficient according to the bubble disperser 1.

【0030】上記構成の気泡分散機にあっては、回転部
材駆動手段20により、分散用翼21に回転力が作用
し、この回転力による分散用翼21がつくる流れにより
下方から供給される気泡Aの上昇する位置がまんべんな
く移動することになり、従来技術のように気泡Aが片寄
ったままになることがないので、中空糸膜4を全体にわ
たって洗浄することができ、洗浄性の向上を図ることが
できる。
In the bubble disperser having the above structure, the rotating member driving means 20 exerts a rotational force on the dispersing vanes 21, and the bubbles supplied from below by the flow created by the dispersing vanes 21 by this rotational force. Since the ascending position of A moves evenly, and the bubbles A do not remain unbalanced as in the prior art, the hollow fiber membrane 4 can be washed over the entire area and the cleaning performance is improved. be able to.

【0031】また、まんべんなく移動して気泡Aが中空
糸膜4に当たるため、気泡Aが集中して中空糸膜4に当
たることがないので、中空糸膜4の保護性が向上する。
Further, since the air bubbles A move evenly and hit the hollow fiber membranes 4, the air bubbles A do not concentrate and hit the hollow fiber membranes 4, so that the protection property of the hollow fiber membranes 4 is improved.

【0032】さらに、まんべんなく移動して気泡Aが中
空糸膜4に当たるため、多少気泡Aの量が減っても、洗
浄性が大きく劣ることがないので、運転の安定化が図れ
る。
Furthermore, since the air bubbles A move evenly and hit the hollow fiber membranes 4, even if the amount of the air bubbles A is slightly reduced, the washing performance is not significantly deteriorated, so that the operation can be stabilized.

【0033】そして、この気泡分散機の駆動源が気泡A
の浮力であるため、わざわざ駆動系の構成を要すること
がないので、製作容易化を図ることもできる。
The drive source of this bubble disperser is the bubble A.
Since it has the buoyancy, the structure of the drive system is not required, and thus the manufacturing can be facilitated.

【0034】図4には、本発明の第2の実施例が示され
ている。上記実施例では回転部材を分散用翼21とした
が、この実施例では円すい形状の傘部材21Aとしたも
ので、この傘部材21Aの周面の中途部に貫通した孔2
1Bを有したものである。
FIG. 4 shows a second embodiment of the present invention. Although the rotating member is the dispersing blade 21 in the above-described embodiment, the conical umbrella member 21A is used in this embodiment, and the hole 2 penetrating in the middle of the peripheral surface of the umbrella member 21A is used.
1B.

【0035】このように回転部材を傘部材21Aとする
ことにより、傘部材21A内に気泡溜りA0 が生じる
が、孔21Bを有しているため、その孔21Bから気泡
Aが出てくる。そして、この傘部材21Aは回転するた
め、孔21Bの位置が回転方向に移動することになる。
従って、気泡Aがまんべんなく移動することになる。
When the umbrella member 21A is used as the rotating member in this manner, a bubble pool A0 is generated in the umbrella member 21A, but since the hole 21B is provided, the bubble A comes out from the hole 21B. Then, since the umbrella member 21A rotates, the position of the hole 21B moves in the rotation direction.
Therefore, the bubbles A move evenly.

【0036】この実施例では、孔21Bによって気泡A
の上昇位置が移動することになるので、上記第1実施例
に比べて確実に気泡Aがまんべんなく分散することがで
きる。
In this embodiment, the air bubbles A are formed by the holes 21B.
Since the ascending position of No. 1 moves, it is possible to surely disperse the bubbles A evenly as compared with the first embodiment.

【0037】その他の構成及び作用については第1実施
例と同一なので、同一の構成部分については同一の符号
を付して、その説明は省略する。
Since the other constructions and operations are the same as those of the first embodiment, the same components are designated by the same reference numerals and the description thereof will be omitted.

【0038】また、図5には、傘部材21Aの他の態様
の傘部材21A’を示しており、これは孔21Bではな
く切欠き21Cを設けたものである。この場合の好適な
寸法関係は、傘部材21A’の外径をd1 、切欠き21
Cの内径をd2 、収納部31の内径をD1 とした場合、
d1 =0.8〜0.9D1 ,d2 =0.5〜0.8d1
である。尚、エアーノズル12’の供給源の位置はケー
ス3の収納部31となっている。
Further, FIG. 5 shows an umbrella member 21A 'which is another mode of the umbrella member 21A, which is provided with notches 21C instead of holes 21B. In this case, the preferred dimensional relationship is that the outer diameter of the umbrella member 21A 'is d1, the notch 21
When the inner diameter of C is d2 and the inner diameter of the storage part 31 is D1,
d1 = 0.8 to 0.9D1, d2 = 0.5 to 0.8d1
Is. The position of the supply source of the air nozzle 12 'is the storage portion 31 of the case 3.

【0039】図6には、本発明の第3の実施例が示され
ている。この実施例では、回転部材駆動手段を軸25に
羽根22Aをつる巻状に巻き付けたスクリュー状部材2
0Aとしたものである。このような構造とすることによ
り回転部材が不要になり、さらに製作容易化が図れる。
FIG. 6 shows a third embodiment of the present invention. In this embodiment, the screw member 2 in which the rotary member driving means is wound around the shaft 25 and the blades 22A are spirally wound.
It is set to 0A. With such a structure, the rotating member becomes unnecessary, and the manufacture can be further facilitated.

【0040】尚、上記各実施例では中空糸膜モジュール
2に用いたものを例にとって説明したが、これに限るも
のではない。
In each of the above embodiments, the one used for the hollow fiber membrane module 2 has been described as an example, but the present invention is not limited to this.

【0041】[0041]

【発明の効果】本発明は、以上の構成および作用を有す
るもので、気泡の浮力を回転部材の回転力に変換する回
転部材駆動手段により、回転部材に回転力が作用し、こ
の回転力により回転部材が回転し、回転部材の下方から
供給される気泡の上昇する位置がまんべんなく移動する
ことになり、従来技術のように気泡が片寄ったままにな
ることがないので、中空糸膜を全体にわたって洗浄する
ことができ、洗浄性の向上を図ることができる。
The present invention has the above-described configuration and operation. The rotating member driving means for converting the buoyancy of bubbles into the rotating force of the rotating member causes the rotating force to act on the rotating member. The rotating member rotates, the rising position of the bubbles supplied from the lower part of the rotating member moves evenly, and the bubbles do not remain unbalanced as in the prior art, so that the hollow fiber membrane is entirely covered. It can be washed, and the cleaning property can be improved.

【0042】また、まんべんなく移動して気泡が中空糸
膜に当たるため、気泡が集中して中空糸膜に当たること
がないので、中空糸膜の保護が図れる。
Further, since the bubbles move uniformly and hit the hollow fiber membrane, the bubbles do not concentrate and hit the hollow fiber membrane, so that the hollow fiber membrane can be protected.

【0043】さらに、まんべんなく移動して気泡が中空
糸膜に当たるため、多少気泡の量が減っても、洗浄性が
大きく劣ることがないので、運転の安定化が図れる。
Further, since the air bubbles move uniformly and hit the hollow fiber membrane, even if the amount of the air bubbles is slightly reduced, the cleaning property is not greatly deteriorated, and the operation can be stabilized.

【0044】そして、この気泡分散機の駆動源が気泡の
浮力であるため、わざわざ駆動系の構成を要することが
ないので、製作容易化を図ることもできる。
Since the drive source of this bubble disperser is the buoyancy of bubbles, there is no need to purposely construct a drive system, which facilitates production.

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

【図1】図1(a)は本発明の一実施例に係る気泡分散
機の概略構成図で、同図(b)は同図(a)の分散用翼
の斜視図である。
FIG. 1 (a) is a schematic configuration diagram of a bubble disperser according to an embodiment of the present invention, and FIG. 1 (b) is a perspective view of a dispersion blade of FIG. 1 (a).

【図2】図2は図1の気泡分散機を適用した中空糸膜モ
ジュールの概略断面図である。
FIG. 2 is a schematic cross-sectional view of a hollow fiber membrane module to which the bubble disperser of FIG. 1 is applied.

【図3】図3は中空糸膜モジュールの寸法を表す一部破
断斜視図である。
FIG. 3 is a partially cutaway perspective view showing the dimensions of the hollow fiber membrane module.

【図4】図4(a)は本発明の第2実施例に係る気泡分
散機を適用した中空糸膜モジュールの概略断面図であ
り、図(b)は同図(a)の傘部材の断面図である。
4 (a) is a schematic cross-sectional view of a hollow fiber membrane module to which a bubble disperser according to a second embodiment of the present invention is applied, and FIG. 4 (b) shows the umbrella member of FIG. 4 (a). FIG.

【図5】図5は傘部材の他の態様を示す斜視図である。FIG. 5 is a perspective view showing another aspect of the umbrella member.

【図6】図6は本発明の第3実施例に係る気泡分散機の
要部斜視図である。
FIG. 6 is a perspective view of an essential part of a bubble disperser according to a third embodiment of the present invention.

【図7】図7(a)は各中空糸膜間に汚濁物が堆積した
状態を示す平面図であり、同図(b)は気泡により汚濁
物が取り除かれている状態を示す平面図である。
FIG. 7 (a) is a plan view showing a state in which contaminants are accumulated between the hollow fiber membranes, and FIG. 7 (b) is a plan view showing a state in which contaminants are removed by air bubbles. is there.

【図8】図8は従来の気泡洗浄を表す中空糸膜モジュー
ルの模式図である。
FIG. 8 is a schematic view of a hollow fiber membrane module representing conventional bubble cleaning.

【図9】図9(a)は他の従来の気泡洗浄のための構造
物の概略斜視図であり、同図(b)は同図(a)の構造
物を適用した中空糸膜モジュールの要部断面図である。
9 (a) is a schematic perspective view of another conventional structure for cleaning air bubbles, and FIG. 9 (b) is a hollow fiber membrane module to which the structure of FIG. 9 (a) is applied. FIG.

【符号の説明】[Explanation of symbols]

1 気泡分散機 2 中空糸膜モジュール 3 ケース 31 収納部 31A フランジ部 32 底部 33 キャップ 33A 環状凸部 4 中空糸膜 5 封止材 6 中空糸膜束 7 中空糸膜開口端面 8,17 ポッティング部 9 吊設部材 91 凸部 92 吊設部 93 通路 10 原液供給口 11 気泡抜口 12,12’ エアーノズル(気泡供給部) 13 透過液出口 14 Oリング 15 集水部 16 締付部材 20 回転部材駆動手段 20A スクリュー状部材(回転部材駆動手段) 21 分散用翼(回転部材) 21A,21A’ 傘部材 21B 孔 21C 切欠き 22,22A 羽根 23 胴部 24 締付部材 25 軸 26 軸受 27 プロペラ 1 Bubble Disperser 2 Hollow Fiber Membrane Module 3 Case 31 Storage Section 31A Flange Section 32 Bottom 33 Cap 33A Annular Convexion 4 Hollow Fiber Membrane 5 Sealant 6 Hollow Fiber Membrane Bundle 7 Hollow Fiber Membrane Open End Face 8, 17 Potting Section 9 Suspended member 91 Convex part 92 Suspended part 93 Passage 10 Undiluted solution supply port 11 Bubble outlet 12, 12 'Air nozzle (bubble supply part) 13 Permeate outlet 14 O-ring 15 Water collecting part 16 Tightening member 20 Rotating member drive Means 20A Screw-shaped member (rotating member driving means) 21 Dispersion blades (rotating member) 21A, 21A 'Umbrella member 21B Hole 21C Notch 22, 22A Blade 23 Body 24 Clamping member 25 Shaft 26 Bearing 27 Propeller

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 液体を収納したケース内に回転自在に支
持された回転部材と、 該回転部材の下方から液中に気泡を供給する気泡供給部
と、 気泡の浮力を回転部材の回転力に変換する回転部材駆動
手段と、を備えてなることを特徴とする気泡分散機。
1. A rotating member rotatably supported in a case accommodating a liquid, a bubble supply unit for supplying bubbles into the liquid from below the rotating member, and a buoyant force of the bubble as a rotating force of the rotating member. A bubble disperser, comprising: a rotating member driving means for converting.
JP6052948A 1994-02-25 1994-02-25 Air bubble disperser Withdrawn JPH07236819A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6052948A JPH07236819A (en) 1994-02-25 1994-02-25 Air bubble disperser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6052948A JPH07236819A (en) 1994-02-25 1994-02-25 Air bubble disperser

Publications (1)

Publication Number Publication Date
JPH07236819A true JPH07236819A (en) 1995-09-12

Family

ID=12929109

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6052948A Withdrawn JPH07236819A (en) 1994-02-25 1994-02-25 Air bubble disperser

Country Status (1)

Country Link
JP (1) JPH07236819A (en)

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JP2003093849A (en) * 2001-09-27 2003-04-02 Yuasa Corp Immersion type membrane filter device
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WO2004018084A1 (en) 2002-08-21 2004-03-04 U.S. Filter Wastewater Group, Inc. Aeration method
AU2003254384B2 (en) * 2002-08-21 2008-09-25 Evoqua Water Technologies Llc Aeration method
JP2010058083A (en) * 2008-09-05 2010-03-18 Akira Morimoto Filter device having cleaning function
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US9022224B2 (en) 2010-09-24 2015-05-05 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
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