JP2000126563A - Method and device for sensing membrane breakage for hollow fiber membrane filter and filtration method thereof - Google Patents

Method and device for sensing membrane breakage for hollow fiber membrane filter and filtration method thereof

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Publication number
JP2000126563A
JP2000126563A JP10307315A JP30731598A JP2000126563A JP 2000126563 A JP2000126563 A JP 2000126563A JP 10307315 A JP10307315 A JP 10307315A JP 30731598 A JP30731598 A JP 30731598A JP 2000126563 A JP2000126563 A JP 2000126563A
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JP
Japan
Prior art keywords
hollow fiber
fiber membrane
treated water
raw water
air
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
JP10307315A
Other languages
Japanese (ja)
Other versions
JP3555468B2 (en
Inventor
Shinichi Yoshikawa
慎一 吉川
Naoki Okuma
那夫紀 大熊
Yutaka Okuno
裕 奥野
Teruhiro Kitazawa
照啓 北沢
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.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP30731598A priority Critical patent/JP3555468B2/en
Publication of JP2000126563A publication Critical patent/JP2000126563A/en
Application granted granted Critical
Publication of JP3555468B2 publication Critical patent/JP3555468B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a membrane breakage sensing method for a hollow membrane filter for sensing the membrane breakage of respective modules inexpensively and with good accuracy during the filtration process and also provide a device thereof. SOLUTION: In a membrane breakage sensing method, raw water in a raw water chamber 12 is filtered through a hollow fiber membrane 18 and introduced into a treatment chamber 14 wherein the raw water is treated, and treated water is discharged from the water treatment chamber 14 to the outside of a housing 10 through a purified water discharged pipe 26, and air reservoir 44 is formed in the treated water discharge pipe 26 and the fluctuation of the water level of the air reservoir 44 is sensed to detect the breakage of the hollow fiber membrane 18.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、中空糸膜濾過装置
における膜破断検知方法およびその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 a method for detecting membrane breakage in a hollow fiber membrane filtration device and a device therefor.

【0002】[0002]

【従来の技術】従来、中空糸膜濾過装置における膜破断
検知方法としては、特開平8ー173774号公報に開
示されたものがある。この公報に開示された膜破断検知
方法は、原水中に空気を導入して原水室を加圧した際、
もし中空糸膜に破断が生じている場合には、原水中の加
圧空気が中空糸膜を介して処理水室に漏出する事実か
ら、処理水中の気泡を検出することによって、中空糸膜
の破断を検出するものである。
2. Description of the Related Art Conventionally, as a method for detecting membrane breakage in a hollow fiber membrane filtration device, there is one disclosed in Japanese Patent Application Laid-Open No. 8-173774. The membrane rupture detection method disclosed in this publication, when air is introduced into raw water to pressurize the raw water chamber,
If the hollow fiber membrane is broken, pressurized air in the raw water leaks into the treated water chamber through the hollow fiber membrane. This is to detect breakage.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、この検
知方法では、気泡検出装置が高価なばかりでなく、ポン
プ等を必要とし装置が複雑になる。このようなことか
ら、この従来の検知方法は、膜モジュール個々に検知す
るのではなく、ユニット一式に対して微粒子モニタを設
置している。したがって、この方法では、ユニット中の
どのモジュールに膜破断が生じたのかを検知することは
できない。
However, in this detection method, not only is the bubble detecting device expensive, but also a pump and the like are required, and the device becomes complicated. For this reason, in this conventional detection method, a particle monitor is provided for a unit as a whole, instead of detecting each of the membrane modules individually. Therefore, in this method, it is impossible to detect which module in the unit has the film breakage.

【0004】本発明は、このような事情に鑑みてなされ
たもので、モジュール個々の膜破断を安価に精度よく検
知でき、しかも濾過工程中に検知することができる中空
糸膜濾過装置における膜破断検知方法およびその装置を
提供することを目的とする。
The present invention has been made in view of such circumstances, and a membrane breakage in a hollow fiber membrane filtration device capable of detecting a membrane breakage of each module accurately and inexpensively and detecting it during a filtration process. An object of the present invention is to provide a detection method and an apparatus therefor.

【0005】[0005]

【課題を解決するための手段】本発明は前記目的を達成
するために、本発明の請求項1の膜破断検知方法では、
原水室中の原水を中空糸膜を介して濾過して処理水室に
導き、該処理水室から処理水排出管を介して処理水をハ
ウジング外へ排出させる中空糸膜濾過装置における膜破
断検知方法であって、前記処理水排出管に空気溜まりを
形成し、該空気溜まりの水位の変化を検出することによ
って前記中空糸膜の破断を検知することを特徴としてい
る。
In order to achieve the above object, the present invention provides a method for detecting a film breakage according to claim 1 of the present invention.
Membrane break detection in a hollow fiber membrane filtration device that filters raw water in a raw water chamber through a hollow fiber membrane, guides it to a treated water chamber, and discharges treated water from the treated water chamber to outside the housing through a treated water discharge pipe. The method is characterized in that an air reservoir is formed in the treated water discharge pipe, and the breakage of the hollow fiber membrane is detected by detecting a change in the water level of the air reservoir.

【0006】本発明の請求項2の膜破断検知装置では、
原水室中の原水を中空糸膜を介して濾過して処理水室に
導き、該処理水室から処理水排出管を介して処理水をハ
ウジング外へ排出させる中空糸膜濾過装置において、前
記処理水排出管に空気溜まりを形成するとともに、該空
気溜まりに水位計を配設したことを特徴としている。ま
た、請求項3の中空糸膜濾過方法では、濾過工程,逆圧
洗浄工程,エアスクラビング工程,排水工程,注水工程
からなる作業工程において、前記エアスクラビング工程
と前記排水工程との間に、前記請求項1または2の膜破
断検知方法による膜破断検知工程を設けたことを特徴と
している。
According to the film rupture detecting device of the second aspect of the present invention,
In a hollow fiber membrane filtration device for filtering raw water in a raw water chamber through a hollow fiber membrane, guiding the raw water to a treated water chamber, and discharging treated water from the treated water chamber to outside the housing through a treated water discharge pipe, An air reservoir is formed in the water discharge pipe, and a water level gauge is provided in the air reservoir. Further, in the hollow fiber membrane filtration method according to the third aspect, in a work process including a filtration process, a back pressure cleaning process, an air scrubbing process, a drainage process, and a water injection process, the process may be performed between the air scrubbing process and the drainage process. A film rupture detecting step according to the film rupture detecting method according to claim 1 or 2 is provided.

【0007】上記発明では、中空糸膜が破断した場合に
は、空気溜まりに空気が溜まり、それによって空気溜ま
りの水位が低下する。その水位を例えば水位計等の安価
で簡単な測定機器により検出すれば、空気のリーク、即
ち中空糸膜の破断を検出できる。この発明によれば、気
泡モニタ等の高価な測定機器を必要とせず、したがっ
て、モジュール毎に膜破断検知装置を設けることが可能
であり、モジュール毎に膜破断の検知が可能となる。
[0007] In the above invention, when the hollow fiber membrane breaks, air is stored in the air pool, thereby lowering the water level of the air pool. If the water level is detected by an inexpensive and simple measuring instrument such as a water level meter, it is possible to detect air leakage, that is, breakage of the hollow fiber membrane. According to the present invention, an expensive measuring device such as a bubble monitor is not required, and therefore, a film breakage detecting device can be provided for each module, and the film breakage can be detected for each module.

【0008】[0008]

【発明の実施の形態】以下、添付図面に従って本発明に
係る中空糸膜濾過装置における膜破断検知方法およびそ
の装置の好ましい実施の形態について詳説する。図1
は、本発明に係る中空糸膜濾過装置の構造図である。図
示した中空糸膜濾過装置は、複数のハウジング10を有
しており、ハウジング10は、隔壁10aによって原水
室12と処理水室14に画成され、該隔壁10aには中
空糸膜支持部材16が配設されている。そして、該中空
糸膜支持部材16には、中空糸膜18が垂下支持され、
該中空糸膜18の開口端18aは処理水室14に臨んで
位置されている。したがって、それらの室12、14は
中空糸膜18を介して互いに連通されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of a method for detecting membrane breakage in a hollow fiber membrane filtration device according to the present invention and the device will be described in detail below with reference to the accompanying drawings. FIG.
1 is a structural diagram of a hollow fiber membrane filtration device according to the present invention. The illustrated hollow fiber membrane filtration device has a plurality of housings 10, and the housing 10 is defined by a partition 10a into a raw water chamber 12 and a treated water chamber 14, and the partition 10a has a hollow fiber membrane support member 16 Are arranged. The hollow fiber membrane support member 16 has a hollow fiber membrane 18 suspended therefrom,
The open end 18 a of the hollow fiber membrane 18 is located facing the treated water chamber 14. Therefore, these chambers 12 and 14 are connected to each other via the hollow fiber membrane 18.

【0009】各ハウジング10の原水室12の下部には
原水供給管20の一端がそれぞれ接続され、それらの原
水供給管20の他端は、原水供給本管22に接続されて
いる。この原水供給本管22には、原水供給弁24が介
在されており、該原水供給弁24を開くことによって原
水室12に原水が供給される。一方、各ハウジング10
の処理水室14の天井部には処理水排出管26の一端が
それぞれ接続され、それらの処理水排出管26の他端
は、処理水排出本管28に接続されている。この処理水
排出本管28には処理水排出弁30が介在されており、
該処理水排出弁30を開くことによって処理水室14の
処理水が外部へ排出される。
One end of a raw water supply pipe 20 is connected to a lower portion of the raw water chamber 12 of each housing 10, and the other end of the raw water supply pipe 20 is connected to a raw water supply main pipe 22. A raw water supply valve 24 is interposed in the raw water supply main pipe 22, and the raw water is supplied to the raw water chamber 12 by opening the raw water supply valve 24. On the other hand, each housing 10
One end of a treated water discharge pipe 26 is connected to the ceiling of the treated water chamber 14, and the other end of the treated water discharge pipe 26 is connected to a treated water discharge main pipe 28. A treated water discharge valve 30 is interposed in the treated water discharge main pipe 28,
By opening the treated water discharge valve 30, the treated water in the treated water chamber 14 is discharged to the outside.

【0010】さらに、各ハウジング10の原水室12の
下部には洗浄用空気供給管32の一端がそれぞれ接続さ
れ、それらの洗浄用空気供給管32の他端は、洗浄用空
気供給本管34に接続されている。この洗浄用空気供給
本管34には、洗浄用空気供給弁36が介在されてお
り、該洗浄用空気供給弁36を開くことによって原水室
12に洗浄用空気が供給される。また、各ハウジング1
0の原水室12の上部には、オーバーフロー管38の一
端がそれぞれ接続され、それらのオーバーフロー管38
の他端は、オーバーフロー本管40に接続されている。
オーバーフロー本管40には、オーバーフロー弁42が
介在され、該オーバーフロー弁42を開くことによって
原水室12の原水が排出される。
Further, one end of a cleaning air supply pipe 32 is connected to a lower portion of the raw water chamber 12 of each housing 10, and the other end of the cleaning air supply pipe 32 is connected to a cleaning air supply main pipe 34. It is connected. A cleaning air supply valve 36 is interposed in the cleaning air supply main pipe 34, and cleaning air is supplied to the raw water chamber 12 by opening the cleaning air supply valve 36. Also, each housing 1
The upper ends of the raw water chambers 12 are connected to one ends of overflow pipes 38, respectively.
Is connected to the overflow main pipe 40.
An overflow valve 42 is interposed in the overflow main pipe 40, and the raw water in the raw water chamber 12 is discharged by opening the overflow valve 42.

【0011】また、上記処理水排出管26は、一部を略
直角に屈曲して、鉛直部26aと水平部26bに構成さ
れ、その鉛直部26a延長上に空気溜まり44が形成さ
れている。この空気溜まり44の上端には空気抜き弁4
6が配設されている。さらに、この空気溜まり44には
水位計(水面計)48が配設されている。このように構
成された中空糸膜濾過装置では、原水供給本管22より
原水供給管20を介して原水室12に原水が供給され
る。この原水は、中空糸膜18によって濾過され、その
処理水は中空糸膜開口端18aから処理水室14に導か
れる。その際(運転開始時)に空気抜き弁46を開くこ
とで空気溜まり44は処理水で満水となる。したがっ
て、膜の破断が生じていない正常時には空気溜まり44
には空気が存在しない。
The treated water discharge pipe 26 is partially bent at a substantially right angle to form a vertical portion 26a and a horizontal portion 26b, and an air reservoir 44 is formed on an extension of the vertical portion 26a. An air vent valve 4 is provided at the upper end of the air reservoir 44.
6 are provided. Further, a water level gauge (water level gauge) 48 is provided in the air reservoir 44. In the hollow fiber membrane filtration device thus configured, raw water is supplied from the raw water supply main pipe 22 to the raw water chamber 12 via the raw water supply pipe 20. This raw water is filtered by the hollow fiber membrane 18, and the treated water is guided to the treated water chamber 14 from the hollow fiber membrane open end 18a. At this time (at the start of operation), the air reservoir 44 is filled with treated water by opening the air vent valve 46. Therefore, at the time of normal operation in which the film is not broken, the air pool 44
Has no air.

【0012】膜の破断を検知する場合は、オーバーフロ
ー弁42を閉止してオーバーフロー本管40を閉止する
とともに、洗浄用空気供給弁36を開いて洗浄用空気供
給管32を介して加圧空気を原水室12に供給する。そ
の際、中空糸膜18が破断していないときは、空気は膜
18を透過しないため、空気のリークが起こらず、空気
溜まり44は満水状態のままである。ここで、中空糸膜
18が破断していれば、膜18の破断部18bから処理
水室14へ空気がリークする。そして、リークした空気
は処理水排出管26中に設けた空気溜まり44に溜ま
る。したがって、その空気は、空気溜まり44内の処理
水を押し下げる。すると、その水位の変化を空気溜まり
44に設けた水位計または液面計48によって検知さ
れ、それによって中空糸膜18の破断が確認される。
To detect the breakage of the membrane, the overflow valve 42 is closed to close the overflow main pipe 40, and the cleaning air supply valve 36 is opened to supply pressurized air through the cleaning air supply pipe 32. It is supplied to the raw water chamber 12. At this time, when the hollow fiber membrane 18 is not broken, air does not pass through the membrane 18, so that no air leaks and the air reservoir 44 remains full. Here, if the hollow fiber membrane 18 is broken, air leaks from the broken portion 18b of the membrane 18 to the treated water chamber 14. Then, the leaked air accumulates in an air reservoir 44 provided in the treated water discharge pipe 26. Therefore, the air pushes down the treated water in the air pool 44. Then, the change in the water level is detected by a water level gauge or a liquid level gauge 48 provided in the air reservoir 44, whereby the breakage of the hollow fiber membrane 18 is confirmed.

【0013】このようにして、水位計または液面計48
によって、空気溜まり44の水位の変化(低下)が確認
されると、中空糸膜濾過装置の運転を停止する等して、
その該当するハウジング10の中空糸膜18を他のもの
と交換する。なお、各ハウジング10の原水供給管2
0,処理水排出管26,洗浄用空気供給管32、オーバ
ーフロー管38に閉止弁を介在させ、中空糸膜18が破
断されたハウジング10のみを機能停止させることもで
きる。その場合には、該当するハウジング10のみの機
能を停止させることによって、該ハウジング10の中空
糸膜18を他のものと交換することができる。
Thus, the water level gauge or the liquid level gauge 48
As a result, when a change (decrease) in the water level in the air pool 44 is confirmed, the operation of the hollow fiber membrane filtration device is stopped, for example,
The hollow fiber membrane 18 of the corresponding housing 10 is replaced with another one. The raw water supply pipe 2 of each housing 10
0, the treated water discharge pipe 26, the cleaning air supply pipe 32, and the overflow pipe 38 may be provided with a shut-off valve to stop the function of only the housing 10 in which the hollow fiber membrane 18 is broken. In that case, the function of only the corresponding housing 10 is stopped, so that the hollow fiber membrane 18 of the housing 10 can be replaced with another one.

【0014】この中空糸膜濾過装置では、各ハウジング
10毎に空気溜まり44が配設されているので、膜の破
断をモジュール毎に検知できる。なお、上記実施の形態
では、空気溜まり44を、処理水排出管26の鉛直部2
6a延長上に形成しているが、設置位置は処理水排出管
26の鉛直部26a延長上に限定されることなく、例え
ば水平部26bの途中に形成してもよい。
In this hollow fiber membrane filtration device, since the air reservoir 44 is provided for each housing 10, breakage of the membrane can be detected for each module. In the above embodiment, the air reservoir 44 is connected to the vertical portion 2 of the treated water discharge pipe 26.
Although it is formed on the extension of 6a, the installation position is not limited to the extension of the vertical portion 26a of the treated water discharge pipe 26, and may be formed, for example, in the middle of the horizontal portion 26b.

【0015】また、空気溜まり44に窓を設けること
で、目視によっても水位の変化、即ち膜の破断の有無を
検知できる。図2に膜破断検知工程のない通常運転時の
全工程のフローを示す。濾過工程においては、原水供給
水弁24を開き、原水供給管20より原水を原水室12
に供給する。本操作時はオーバーフロー弁42,洗浄用
空気供給弁36を閉止し、処理水排出弁30を開いてハ
ウジング10内を加圧して処理水を得る。一定時間濾過
後、即ち逆圧洗浄工程においては、原水供給弁24を閉
じ、オーバーフロー弁42を開けて処理水排出管26よ
り処理水を逆流させる。次いで、エアスクラビング工程
に入り、洗浄用空気供給弁36を開き、洗浄用空気供給
管32より洗浄用の空気を供給して中空糸膜18を互い
に擦り合わせて、逆圧洗浄と同じく、中空糸膜18表面
に付着した濁質を剥離させる。その後、排水工程におい
て、原水供給弁24を開けて、ハウジング10内の中空
糸膜18の表面から剥離した濁質が浮遊した濃縮水を排
水する。この時オーバーフロー弁42を開けて自然流下
で排水してもよく、オーバーフロー弁42を閉じて洗浄
用空気供給管32より空気を供給してハウジング10内
部を空気加圧して強制的に排水する場合もある。その
後、注水工程において、原水供給管20からハウジング
10内に原水を注入し、満水となった後は再び濾過工程
に戻る。
Further, by providing a window in the air reservoir 44, a change in the water level, that is, the presence or absence of breakage of the film can be visually detected. FIG. 2 shows the flow of all the steps during the normal operation without the film breakage detection step. In the filtration step, the raw water supply water valve 24 is opened, and the raw water is supplied from the raw water supply pipe 20 to the raw water chamber 12.
To supply. During this operation, the overflow valve 42 and the cleaning air supply valve 36 are closed, the treated water discharge valve 30 is opened, and the inside of the housing 10 is pressurized to obtain treated water. After filtration for a certain period of time, that is, in the back pressure washing step, the raw water supply valve 24 is closed, the overflow valve 42 is opened, and the treated water flows back through the treated water discharge pipe 26. Next, the air scrubbing process is started, the cleaning air supply valve 36 is opened, and the cleaning air is supplied from the cleaning air supply pipe 32 to rub the hollow fiber membranes 18 together. The turbidity adhering to the surface of the film 18 is removed. After that, in the drainage step, the raw water supply valve 24 is opened, and the concentrated water in which the turbid matter floating from the surface of the hollow fiber membrane 18 in the housing 10 floats is drained. At this time, the overflow valve 42 may be opened to drain the water under natural flow. Alternatively, the overflow valve 42 may be closed to supply air from the cleaning air supply pipe 32 to pressurize the inside of the housing 10 to forcibly drain the water. is there. Thereafter, in the water injection step, the raw water is injected into the housing 10 from the raw water supply pipe 20, and after the water is full, the flow returns to the filtration step again.

【0016】図3は、本発明に係る中空糸膜濾過装置の
運転の全工程を示すフロー図である。このフロー図で
は、図2に示した通常運転時のエアスクラビング工程後
に膜の破断を検知する膜破断検知工程を設けている。こ
の膜破断検知工程においては、エアスクラビング工程後
に、オーバーフロー弁42のみを閉じ、洗浄用空気供給
管32からはそのまま洗浄用の空気を供給する。これに
より、ハウジング10内上部には空気層が生じ、その空
気層が洗浄用空気によって加圧される。膜の破断は中空
糸膜支持部材16の5〜20mm下で生じるため、ハウ
ジング10内部に原水(濃縮水)が残存していても膜の
破断部18bは空気層中にあり、ここから加圧空気が処
理水へリークする。
FIG. 3 is a flow chart showing all the steps of the operation of the hollow fiber membrane filtration device according to the present invention. In this flow chart, a film break detection step for detecting a film break after the air scrubbing step during normal operation shown in FIG. 2 is provided. In the film rupture detection step, after the air scrubbing step, only the overflow valve 42 is closed, and the cleaning air supply pipe 32 supplies cleaning air as it is. As a result, an air layer is generated in the upper portion of the housing 10, and the air layer is pressurized by the cleaning air. Since the rupture of the membrane occurs 5 to 20 mm below the hollow fiber membrane support member 16, even if raw water (concentrated water) remains inside the housing 10, the rupture portion 18 b of the membrane is in the air layer and pressurized from there. Air leaks into treated water.

【0017】また、図4に示すように、排水工程の後に
膜破断検知工程を設ける場合もある。この場合は、注水
工程に入る際にオーバーフロー弁42を閉じた後に、原
水供給管20からハウジング10内に原水を注入する。
これによりハウジング10内部は加圧されることとな
り、膜の破断が生じていれば、破断部か18bから空気
がリークする。
Further, as shown in FIG. 4, there may be a case where a membrane rupture detecting step is provided after the draining step. In this case, the raw water is injected into the housing 10 from the raw water supply pipe 20 after closing the overflow valve 42 at the time of the water injection step.
As a result, the inside of the housing 10 is pressurized, and if the film is broken, air leaks from the broken portion or 18b.

【0018】[0018]

【発明の効果】本発明によれば、簡便な装置により膜の
破断が検知できるため、モジュール毎の検知を安価に精
度良く行うことができる。また、運転工程中に破断検知
を行うことができる。
According to the present invention, the breakage of the film can be detected by a simple device, so that the detection for each module can be performed accurately at low cost. In addition, break detection can be performed during the operation process.

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

【図1】本発明に係る膜破断検知方法を実施するための
中空糸膜濾過装置を概念的に示した斜視図
FIG. 1 is a perspective view conceptually showing a hollow fiber membrane filtration device for performing a membrane breakage detection method according to the present invention.

【図2】通常の運転方法を示したフロー図FIG. 2 is a flowchart showing a normal operation method.

【図3】本発明に係る運転方法を示したフロー図FIG. 3 is a flowchart showing an operation method according to the present invention.

【図4】本発明に係る別の運転方法を示したフロー図FIG. 4 is a flowchart showing another operation method according to the present invention.

【符号の説明】[Explanation of symbols]

10…ハウジング 10a…隔壁 12…原水室 14…処理水室 16…中空糸膜支持部材 18…中空糸膜 18a…開口端 18b…破断部 20…原水供給管 22…原水供給本管 24…原水供給弁 26…処理水排出管 26a…鉛直部 26b…水平部 28…処理水排出本管 30…処理水排出弁 32…洗浄用空気供給管 34…洗浄用空気供給本管 36…洗浄用空気供給弁 38…オーバーフロー管 40…オーバーフロー本管 42…オーバーフロー弁 44…空気溜まり 46…空気抜き弁 48…水位計(液面計) DESCRIPTION OF SYMBOLS 10 ... Housing 10a ... Partition wall 12 ... Raw water chamber 14 ... Treatment water chamber 16 ... Hollow fiber membrane support member 18 ... Hollow fiber membrane 18a ... Open end 18b ... Breaking part 20 ... Raw water supply pipe 22 ... Raw water supply main pipe 24 ... Raw water supply Valve 26: treated water discharge pipe 26a: vertical part 26b ... horizontal part 28 ... treated water discharge main pipe 30 ... treated water discharge valve 32 ... cleaning air supply pipe 34 ... cleaning air supply main pipe 36 ... cleaning air supply valve 38 ... overflow pipe 40 ... overflow main pipe 42 ... overflow valve 44 ... air reservoir 46 ... air vent valve 48 ... water level gauge (liquid level gauge)

フロントページの続き (72)発明者 北沢 照啓 東京都千代田区内神田1丁目1番14号 日 立プラント建設株式会社内 Fターム(参考) 4D006 GA02 HA03 HA19 JA18A JA70A KA11 KC02 KC03 KC13 KC14 KE24Q LA03Continued on the front page (72) Inventor Teruhiro Kitazawa 1-1-1 Uchikanda, Chiyoda-ku, Tokyo F-term in Hitachi Plant Construction Co., Ltd. 4D006 GA02 HA03 HA19 JA18A JA70A KA11 KC02 KC03 KC13 KC14 KE24Q LA03

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】原水室中の原水を中空糸膜を介して濾過し
て処理水室に導き、該処理水室から処理水排出管を介し
て処理水をハウジング外へ排出させる中空糸膜濾過装置
における膜破断検知方法であって、 前記処理水排出管に空気溜まりを形成し、該空気溜まり
の水位の変化を検出することによって前記中空糸膜の破
断を検知することを特徴とする中空糸膜濾過装置におけ
る膜破断検知方法。
1. A hollow fiber membrane filter for filtering raw water in a raw water chamber through a hollow fiber membrane, guiding the raw water to a treated water chamber, and discharging treated water from the treated water chamber to the outside of the housing through a treated water discharge pipe. A method of detecting membrane breakage in an apparatus, comprising forming an air pocket in the treated water discharge pipe and detecting a break in the hollow fiber membrane by detecting a change in the water level of the air pool. A method for detecting membrane breakage in a membrane filtration device.
【請求項2】原水室中の原水を中空糸膜を介して濾過し
て処理水室に導き、該処理水室から処理水排出管を介し
て処理水をハウジング外へ排出させる中空糸膜濾過装置
において、 前記処理水排出管に空気溜まりを形成するとともに、該
空気溜まりに水位計を配設したことを特徴とする中空糸
膜濾過装置。
2. A hollow fiber membrane filter for filtering raw water in a raw water chamber through a hollow fiber membrane, guiding the raw water to a treated water chamber, and discharging treated water from the treated water chamber to the outside of the housing via a treated water discharge pipe. In the apparatus, an air reservoir is formed in the treated water discharge pipe, and a water level gauge is provided in the air reservoir.
【請求項3】濾過工程、逆圧洗浄工程、エアスクラビン
グ工程、排水工程、注水工程からなる作業工程におい
て、前記エアスクラビング工程と前記排水工程との間
に、前記請求項1または2の膜破断検知方法による膜破
断検知工程を設けたことを特徴とする中空糸膜濾過方
法。
3. The membrane breakage according to claim 1, wherein in a working step including a filtration step, a back pressure washing step, an air scrubbing step, a drain step, and a water injection step, between the air scrubbing step and the drain step. A hollow fiber membrane filtration method comprising a membrane breakage detection step by a detection method.
JP30731598A 1998-10-28 1998-10-28 Method for detecting membrane breakage in hollow fiber membrane filtration device, device therefor and filtration method Expired - Fee Related JP3555468B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30731598A JP3555468B2 (en) 1998-10-28 1998-10-28 Method for detecting membrane breakage in hollow fiber membrane filtration device, device therefor and filtration method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30731598A JP3555468B2 (en) 1998-10-28 1998-10-28 Method for detecting membrane breakage in hollow fiber membrane filtration device, device therefor and filtration method

Publications (2)

Publication Number Publication Date
JP2000126563A true JP2000126563A (en) 2000-05-09
JP3555468B2 JP3555468B2 (en) 2004-08-18

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006082055A (en) * 2004-09-17 2006-03-30 Kurita Water Ind Ltd Membrane treatment device operating method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006082055A (en) * 2004-09-17 2006-03-30 Kurita Water Ind Ltd Membrane treatment device operating method
JP4591671B2 (en) * 2004-09-17 2010-12-01 栗田工業株式会社 Operation method of membrane treatment apparatus

Also Published As

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