JPH09220452A - Membrane leakage detector and detecting method - Google Patents

Membrane leakage detector and detecting method

Info

Publication number
JPH09220452A
JPH09220452A JP2664296A JP2664296A JPH09220452A JP H09220452 A JPH09220452 A JP H09220452A JP 2664296 A JP2664296 A JP 2664296A JP 2664296 A JP2664296 A JP 2664296A JP H09220452 A JPH09220452 A JP H09220452A
Authority
JP
Japan
Prior art keywords
membrane
container
detection
detecting
leakage
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.)
Pending
Application number
JP2664296A
Other languages
Japanese (ja)
Inventor
Kazuhisa Kumami
和久 熊見
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.)
DAISEN MENBUREN SYST KK
Original Assignee
DAISEN MENBUREN SYST KK
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 DAISEN MENBUREN SYST KK filed Critical DAISEN MENBUREN SYST KK
Priority to JP2664296A priority Critical patent/JPH09220452A/en
Publication of JPH09220452A publication Critical patent/JPH09220452A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide the inexpensive and convenient device and method for rapidly detecting the damage of a membrane when the separation membrane damages and leaks. SOLUTION: A membrane leakage detector provided with a detecting membrane 1 having a larger average pore diameter and a much smaller membrane area than a membrane to be tested for leakage, a branch pipeline 2 for sampling a part of the permeated liq. of the membrane to be tested, a vessel 3 for accumulating the supplied permeated liq. and a sensor 4 for detecting the liq. surface of the vessel is attached. A part of the permeated liq. of the membrane to be tested is introduced into the vessel and then filtered by the detecting membrane, and the liq. leakage is detected by the sensor as the clogging of the detecting membrane.

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、分離膜モジュールの膜
漏れ検知に関し、さらに詳しくは膜濾過運転中におい
て、分離膜モジュールの膜損傷により生じた原液の膜漏
れを検知する付帯装置および検知方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to detection of a membrane leak in a separation membrane module, and more particularly, to an auxiliary device and a detection method for detecting a membrane leak of a stock solution caused by a membrane damage of a separation membrane module during a membrane filtration operation. It is about.

【0002】[0002]

【従来の技術】近年、表流水や地下水の濾過、海水の淡
水化、透析水の精製、血液濾過、人口透析、製薬用水や
半導体用水の精製、果汁の濃縮や清澄化、酵素や菌体の
濃縮および濾過、し尿や排液の濾過、ガス分離濃縮、液
体の脱気、液液抽出、有機溶媒の回収など様々な分野に
おいて、膜の選択透過性を利用した膜分離が行われてい
る。これらの分離には、通常、中空糸膜型、スパイラル
型、チューブ型、プレート・アンド・フレーム型などの
膜モジュールを備えた膜分離装置が用いられる。一方、
膜分離において、膜の破損などの事故を生じると、膜の
供給側から原液が漏れ、未処理のまま透過側に流入す
る。この様な場合に、透過液が濁るなどの現象を肉眼で
確認できれば、迅速な対応が可能であるため、未処理の
原液による汚染は最小限でとどめることが可能である。
しかし、漏れ量が小さい場合は、発見が遅れやすく透過
側の汚染が進行し、処理水に影響を及ぼす。
2. Description of the Related Art In recent years, surface water and groundwater filtration, seawater desalination, dialysis water purification, hemofiltration, artificial dialysis, pharmaceutical water and semiconductor water purification, fruit juice concentration and clarification, enzyme and cell purification In various fields such as concentration and filtration, human urine and waste liquid filtration, gas separation concentration, liquid degassing, liquid-liquid extraction, and organic solvent recovery, membrane separation utilizing the selective permeability of the membrane is performed. A membrane separation device including a membrane module of a hollow fiber membrane type, a spiral type, a tube type, a plate-and-frame type or the like is usually used for these separations. on the other hand,
In membrane separation, if an accident such as membrane damage occurs, the undiluted solution leaks from the membrane supply side and flows into the permeate side without treatment. In such a case, if a phenomenon such as turbidity of the permeated liquid can be confirmed with the naked eye, swift action can be taken, so that the contamination with the untreated undiluted liquid can be minimized.
However, if the amount of leakage is small, the discovery is likely to be delayed, and the contamination on the permeate side proceeds, affecting the treated water.

【0003】このため、膜分離装置全体や膜モジュール
として、漏れに伴うトラブルを速やかに検知し、装置の
運転を制御することが提案されている。例えば、特開平
6−15271号公報、特開平6−182164号公
報、特開平7−47236号公報および実開平6−34
730号公報では、分離をつかさどる膜モジュールの透
過液を、さらに後段に設けた孔径のより大きい膜を有す
る膜モジュールで濾過し、分離をつかさどる膜モジュー
ルに漏れが生じた場合には後段の膜が詰まり、膜の差圧
が生じることから、差圧を検知することで、膜の漏れを
検知する方法が提案されている。また、実開平6−21
728号公報では後段の膜の透過流束を検知することで
も膜の漏れを検知することが提案されている。また、特
開平6−170365号公報では透過液の濁度や微粒子
をセンサーによって検知する方法も使用されている。さ
らに、特開平7−248290号公報では透過水の一部
をサンプリングポンプにより分流してリーク検出用フィ
ルターに通し、フィルター入口の圧力上昇を圧力計で検
知するリーク検出器が提案されている。
Therefore, it has been proposed to promptly detect troubles due to leakage and control the operation of the device as the entire membrane separation device or the membrane module. For example, JP-A-6-15271, JP-A-6-182164, JP-A-7-47236 and JP-A-6-34.
In Japanese Patent No. 730, the permeate of a membrane module that controls separation is further filtered by a membrane module having a membrane with a larger pore size that is provided in a subsequent stage, and if a membrane module that controls separation causes leakage, Since clogging and a differential pressure of the membrane occur, a method of detecting the leak of the membrane by detecting the differential pressure has been proposed. Also, the actual Kaihei 6-21
In Japanese Patent No. 728, it is proposed to detect the membrane leakage by detecting the permeation flux of the latter membrane. Further, in Japanese Patent Laid-Open No. 6-170365, a method of detecting turbidity and fine particles of a permeated liquid by a sensor is also used. Further, Japanese Patent Application Laid-Open No. 7-248290 proposes a leak detector in which a part of permeated water is diverted by a sampling pump and passed through a leak detection filter to detect a pressure rise at a filter inlet with a pressure gauge.

【0004】しかし、これらはいずれも大掛かりな設備
を必要としたり、また高価なセンサーによって検知する
ため、設備費用が高くなるという欠点を有する。
However, all of these have the drawbacks that the equipment cost is high because they require large-scale equipment and are detected by an expensive sensor.

【0005】[0005]

【発明が解決しようとする課題】したがって、本発明の
目的は、分離膜に破損を生じて膜漏れしたとしても、迅
速に膜の破損を検知する装置および方法を提案すること
にある。さらには、安価で、汎用的なもので構成されて
いる検知装置および簡便な検知方法を提供することにあ
る。
SUMMARY OF THE INVENTION Therefore, it is an object of the present invention to propose an apparatus and method for promptly detecting the damage of a membrane even if the separation membrane is damaged and leaks. Another object of the present invention is to provide a low-cost, general-purpose detecting device and a simple detecting method.

【0006】[0006]

【課題を解決するための手段】本発明者は、種々検討し
た結果、分離をつかさどる膜モジュールの透過側から枝
配管を通して透過液の一部を蓄積する容器と、容器の液
面状態を検知するセンサーと、この容器から導かれる透
過液を濾過する膜を設けることで、前記目的を達成でき
ることを見出だし、本発明を完成した。
As a result of various studies, the inventor of the present invention detects a container for accumulating a part of permeate through a branch pipe from the permeate side of a membrane module that controls separation, and a liquid level state of the container. It has been found that the above object can be achieved by providing a sensor and a membrane for filtering permeated liquid introduced from this container, and completed the present invention.

【0007】すなわち、本発明の膜漏れ検知装置は、膜
漏れを検知したい対象分離膜より大きい孔径と遥かに小
さい膜面積とを有する検知膜、対象分離膜の透過液の一
部をを採取する枝配管、採取した透過液を蓄積する容器
およびこの容器の液面状態を検知するセンサーを有して
いる。また、検知膜の平均孔径は、対象分離膜の平均孔
径の2〜10000倍であり、さらに膜漏れ検知装置
は、対象分離膜モジュール単位当たり1個取り付けられ
ている。
That is, the membrane leakage detection device of the present invention collects a part of the permeated liquid of the detection membrane and the target separation membrane having a pore size larger than the target separation membrane whose membrane leak is to be detected and a far smaller membrane area. It has a branch pipe, a container for accumulating the collected permeated liquid, and a sensor for detecting the liquid surface state of this container. Further, the average pore diameter of the detection membrane is 2 to 10000 times the average pore diameter of the target separation membrane, and one membrane leak detection device is attached per unit of the target separation membrane module.

【0008】また、本発明の膜漏れ検知方法は、膜漏れ
を検知したい対象分離膜の透過液の一部を枝配管により
採取し、液面状態を検知するセンサーを有する容器に導
入した後、対象分離膜より大きい平均孔径と遥かに小さ
い膜面積とを有する検知膜で濾過し、膜漏れを検知膜の
閉塞現象として前記センサーにより検知する方法であ
る。また、検知膜の平均孔径が、対象分離膜の平均孔径
の2〜10000倍であり、さらに対象分離膜が漏れを
生じていない状態での容器に受ける透過液の流束が、検
知膜の濾過流束よりも小さい流束である膜漏れ検知方法
である。
In the membrane leak detection method of the present invention, a part of the permeate of the separation membrane to be subjected to membrane leak detection is collected by a branch pipe and introduced into a container having a sensor for detecting the liquid level state, In this method, a sensor membrane having an average pore size larger than the target separation membrane and a membrane area much smaller than the target membrane is used for filtration, and membrane leakage is detected by the sensor as a clogging phenomenon of the membrane. Further, the average pore size of the detection membrane is 2 to 10000 times the average pore size of the target separation membrane, and the flux of the permeated liquid received by the container in the state where the target separation membrane does not leak is the filtration of the detection membrane. This is a membrane leak detection method in which the flux is smaller than the flux.

【0009】本発明の膜漏れ検知装置は、本来の膜分離
設備の主系列とは別に付帯的に取り付けられて用いられ
る。以下、その検知機構について説明する。
The membrane leak detection device of the present invention is attached and used separately from the original main series of membrane separation equipment. The detection mechanism will be described below.

【0010】まず、対象分離膜の透過液の一部を枝配管
により採取し、連続的もしくは定期的に容器に受け、こ
こから検知膜に透過液を流し、検知膜で濾過する。通
常、枝配管の途中には液の遮断や流束の調節のためにバ
ルブ等が設けられる。対象分離膜が膜漏れを生じていな
い場合は、検知膜の平均孔径は対象分離膜より大きいた
め、検知膜は詰まりを生じず、透過流束は一定である。
しかし、対象分離膜が破損して膜の透過側に原液の漏れ
を生じると、検知膜を詰まらせるため、検知膜の透過流
束は低下する。容器に受ける液流束よりも検知膜を透過
する液流束の方が小さくなると、容器の液面が上昇する
ため、液面状態を検知するセンサーによって膜の漏れ、
如いては膜の破損を検知することができる。
First, a part of the permeated liquid of the target separation membrane is collected by a branch pipe and continuously or periodically received in a container, from which the permeated liquid is flowed to the detection membrane and filtered by the detection membrane. Usually, a valve or the like is provided in the middle of the branch pipe for shutting off the liquid or adjusting the flux. When the target separation membrane does not leak, the average pore size of the detection membrane is larger than that of the target separation membrane, so that the detection membrane is not clogged and the permeation flux is constant.
However, when the target separation membrane is damaged and the stock solution leaks to the permeate side of the membrane, the sensing membrane is clogged, and the permeation flux of the sensing membrane is reduced. When the liquid flux passing through the detection membrane becomes smaller than the liquid flux received in the container, the liquid level of the container rises, so the film leaks due to the sensor that detects the liquid level condition.
Therefore, the breakage of the membrane can be detected.

【0011】容器に受ける液流束はいくらでもよいが、
少量でも本発明には充分に適用できることが特徴であ
る。例えば、極少量の数ml/分程度でもよい。この場
合、使用する検知膜や容器も小さくできる。例えば、使
用する検知膜として数cm2 のものが可能である。これ
は、極小型の膜分離装置、例えば水道水の蛇口に取り付
けて用いられる中空糸膜型浄水器の膜面積の0.2m2
=2,000cm2 のものと比較しても遥かに小さい値
である。また、容器も数ml〜数十ml程度で充分であ
る。
The liquid flux received by the container may be any,
The present invention is characterized in that even a small amount can be sufficiently applied to the present invention. For example, an extremely small amount of about several ml / minute may be used. In this case, the detection film and container used can be made small. For example, the sensing film to be used may be several cm 2 . This is a very small membrane separation device, for example, a membrane area of 0.2 m 2 of a hollow fiber membrane water purifier used by being attached to a tap water tap.
The value is much smaller than that of the sample of 2,000 cm 2 . Further, it is sufficient for the container to have several ml to several tens of ml.

【0012】容器に受ける液流束は、対象分離膜が漏れ
を生じていない状態で、検知膜の濾過流束と同等かそれ
よりも遅い必要があり、遅い方がより好ましい。遅さの
程度は、圧力変動による容器に受ける液流束のばらつき
や、溶解有機物汚染による検知膜の濾過流束低下を勘案
して適宜決定する必要がある。
The liquid flux received by the container must be equal to or slower than the filtration flux of the detection membrane in the state where the target separation membrane is not leaking, and the slower is more preferable. The degree of slowness needs to be appropriately determined in consideration of variations in the liquid flux received by the container due to pressure fluctuations and reduction in the filtration flux of the detection membrane due to contamination of dissolved organic substances.

【0013】本発明において平均孔径とは、透過成分の
サイズに対応する平均径を意味する。例えば、精密濾過
膜の場合、透過成分のサイズは平均孔径で表すことがで
きる。一方、例えば、限外濾過膜や逆浸透膜において
は、孔径の測定が困難であるため、具体的には限外濾過
膜の場合、透過成分のサイズは、通常分画分子量で表さ
れ、また、逆浸透膜の場合は、通常、食塩排除率(食塩
除去率)で表される。したがって、本発明では、例え
ば、限外濾過膜における分画分子量や逆浸透膜における
食塩排除率という透過成分のサイズを表す表現を含め
て、便宜的に平均孔径という語を用いる。因みに、精密
濾過膜の孔径は0.08〜2.5μm(分画分子量15
0,000〜5,000,000)、限外濾過膜の孔径
は0.002〜0.4μm(分画分子量500〜80
0,000)、ルーズ逆浸透膜の孔径は0.0007〜
0.007μm(分画分子量140〜15,000)お
よび逆浸透膜の孔径(理論的に)は0〜0.0015μ
m(分画分子量0〜300)の範囲にあるといわれてい
る。
In the present invention, the average pore size means the average size corresponding to the size of the permeation component. For example, in the case of a microfiltration membrane, the size of the permeation component can be represented by the average pore size. On the other hand, for example, in an ultrafiltration membrane or a reverse osmosis membrane, it is difficult to measure the pore size. Therefore, specifically, in the case of an ultrafiltration membrane, the size of the permeation component is usually represented by a molecular weight cutoff, and In the case of a reverse osmosis membrane, it is usually represented by the salt elimination rate (salt removal rate). Therefore, in the present invention, for example, the term "average pore size" is used for convenience, including expressions representing the size of the permeation component, such as the molecular weight cutoff in the ultrafiltration membrane and the salt exclusion rate in the reverse osmosis membrane. Incidentally, the pore size of the microfiltration membrane is 0.08 to 2.5 μm (molecular weight cutoff of 15
50,000 to 5,000,000), and the pore size of the ultrafiltration membrane is 0.002 to 0.4 μm (molecular weight cutoff of 500 to 80).
10,000), and the pore size of the loose reverse osmosis membrane is 0.0007-
0.007 μm (molecular weight cutoff 140 to 15,000) and pore size (theoretical) of the reverse osmosis membrane are 0 to 0.0015 μm.
It is said to be in the range of m (molecular weight cutoff of 0 to 300).

【0014】本発明に使用する検知膜の平均孔径は、対
象分離膜の平均孔径より大きいことが必要であり、対象
分離膜の平均孔径の2〜10000倍であればよい。さ
らに、対象分離膜の平均孔径の10〜1000倍程度で
あれば、さらに好ましく、実用的である。また、検知膜
の材質は、どの様なものでもよい。例えば、酢酸セルロ
ース、ポリアミド、ポリカーボネート、ポリサルホン、
ポリエーテルサルホン、ポリオレフィン、アクリル系樹
脂,フッ素基含有樹脂、セラミックおよび金属などが挙
げられる。また、検知膜の形状は、どの様なものでもよ
く、例えば、平膜、中空糸膜、チューブ膜およびスパイ
ラル膜などが挙げられる。膜面積が小さくてよい場合
は、平膜が簡単でよい。
The average pore diameter of the detection membrane used in the present invention needs to be larger than the average pore diameter of the target separation membrane, and may be 2 to 10,000 times the average pore diameter of the target separation membrane. Furthermore, it is more preferable and practical if it is about 10 to 1000 times the average pore size of the target separation membrane. Further, the material of the detection film may be any material. For example, cellulose acetate, polyamide, polycarbonate, polysulfone,
Examples thereof include polyether sulfone, polyolefin, acrylic resin, fluorine group-containing resin, ceramic and metal. Further, the detection membrane may have any shape, and examples thereof include a flat membrane, a hollow fiber membrane, a tube membrane, and a spiral membrane. When the membrane area may be small, a flat membrane may be simple.

【0015】また、本発明に使用する液面状態を検知す
るセンサーは、液を検知できるものであれば、通常用い
られるどの様なものでもよく、例えば、電極で抵抗を測
定するものでもよいし、屈折率を測定するもの、光学的
検知でも静電容量方式でもよい。検知方法としては、容
器の壁部からセンサーを突き出し、液面を検知してもよ
いし、また容器の壁部に穴を開けて配管等を付設し、オ
ーバーフローした液を配管内部や、別に取り出して、当
該センサーで検知しても良い。
Further, the sensor for detecting the liquid surface state used in the present invention may be any of those commonly used as long as it can detect the liquid, for example, a sensor for measuring resistance with an electrode. , Which measures the refractive index, optical detection or capacitance method may be used. As a detection method, a sensor may be projected from the wall of the container to detect the liquid level, or a hole may be opened in the wall of the container to attach a pipe, etc., and the overflowed liquid may be taken out inside the pipe or separately. Then, it may be detected by the sensor.

【0016】また、本発明に使用する容器は、どの様な
ものでもよい。検知膜を入れるものも容器といえるし、
また例えば、配管そのままでもよいし、円柱状のプラス
チック容器でもよい。
Any container may be used in the present invention. It can be said that the container for the detection film is also a container,
Further, for example, the pipe may be used as it is, or a cylindrical plastic container may be used.

【0017】また、本発明において、容器から検知膜へ
の透過液の導入は、どの様な方法でもよいが、実用性と
コストを考慮すると、検知膜に精密濾過膜を使用して、
配管のみで導入するのがよい。この場合、検知膜を濾過
させる圧力は、配管内部に溜る液のヘッド圧力のみであ
るが、充分に濾過できる。
In the present invention, the permeated liquid may be introduced from the container to the detection membrane by any method, but in consideration of practicality and cost, a microfiltration membrane is used as the detection membrane,
It is recommended to introduce it only by piping. In this case, the pressure for filtering the detection film is only the head pressure of the liquid accumulated inside the pipe, but it can be sufficiently filtered.

【0018】検知膜で濾過した液は、対象分離膜の透過
液タンクに入れてもよいし、原液タンクに返してもよ
い。また、ドレインとして排水してもよい。本発明の装
置の利点を考慮すると、検知膜での濾過流束は、少量で
あるため、上記のどの方法を使用しても構わないが、排
水するのがコスト的に有利である。
The liquid filtered by the detection membrane may be put into the permeated liquid tank of the target separation membrane or returned to the stock solution tank. It may also be drained as a drain. Considering the advantages of the device of the present invention, since the filtration flux at the sensing membrane is small, any of the above methods may be used, but draining is cost effective.

【0019】[0019]

【発明の実施の形態】以下に添付図面を参照しつつ、本
発明をより詳細に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in more detail below with reference to the accompanying drawings.

【0020】図1は、本発明の膜漏れ検知装置の構造の
一例を示す断面図であり、液面検知のセンサーを内部に
備えた容器の底部に、平膜の検知膜が設置してある例で
ある。本図の装置は、対象分離膜からの透過液を採取す
る枝配管(2)、透過液を受ける容器(3)、容器の空
気抜き(5)、容器に取り付けた液面検知のセンサー
(4)および平膜の検知膜(1)から構成されている。
対象分離膜から枝配管(2)により採取された透過液
は、まず容器(3)に入り、ヘッド圧力によって検知膜
(1)で濾過される。透過液の液面は、容器(3)の内
部で平衡を保っている。対象分離膜が破損し、膜漏れを
生じた場合は、漏れによって検知膜の表面が濁質分で覆
われ流束が低下する。容器内へ流入する透過液の速度
(液流束)は変わらないことから、容器内の透過液の液
面は上昇し、液面検知のセンサー(4)で検知される。
FIG. 1 is a cross-sectional view showing an example of the structure of the membrane leak detection device of the present invention, in which a flat membrane detection membrane is installed at the bottom of a container having a liquid level detection sensor inside. Here is an example. The apparatus shown in the figure has a branch pipe (2) for collecting the permeated liquid from the target separation membrane, a container (3) for receiving the permeated liquid, an air vent (5) of the container, and a liquid level detection sensor (4) attached to the container. And a flat sensing film (1).
The permeated liquid collected from the target separation membrane by the branch pipe (2) first enters the container (3) and is filtered by the detection membrane (1) by the head pressure. The liquid level of the permeate is in equilibrium inside the container (3). When the target separation membrane is damaged and a membrane leak occurs, the surface of the sensing membrane is covered with suspended matter due to the leak, and the flux is reduced. Since the velocity (fluid flux) of the permeate flowing into the container does not change, the liquid level of the permeate in the container rises and is detected by the liquid level detection sensor (4).

【0021】図2は、本発明の膜漏れ検知装置の他の構
造の一例を示す断面図であり、液面検知のセンサーが、
容器の上部よりのオーバーフロー液を検知するように設
置してある。本図では、対象分離膜からの透過液を受け
る容器(3)、容器側部からでたオーバーフロー配管
(6)、漏水検知のセンサー(4)、平膜の検知膜
(1)および容器と検知膜をつなぐ配管(7)から構成
されている。図1と同様にして対象分離膜からの透過液
の液面は、容器(3)内部で平衡している。対象分離膜
が漏れを生じた場合は、容器内の透過液の液面が上昇
し、オーバーフロー配管(6)を通過して漏水検知のセ
ンサー(4)で検知される。
FIG. 2 is a cross-sectional view showing another example of the structure of the membrane leak detection device of the present invention, in which the liquid level detection sensor is
It is installed to detect the overflow liquid from the upper part of the container. In this figure, a container (3) that receives the permeated liquid from the target separation membrane, an overflow pipe (6) from the side of the container, a leak detection sensor (4), a flat membrane detection membrane (1) and a container and detection. It consists of piping (7) connecting the membranes. Similar to FIG. 1, the liquid level of the permeated liquid from the target separation membrane is in equilibrium inside the container (3). When the target separation membrane leaks, the liquid level of the permeated liquid in the container rises, passes through the overflow pipe (6), and is detected by the leak detection sensor (4).

【0022】図3は、図1または図2の本発明になる膜
漏れ検知装置(8)を対象分離膜モジュールの透過液配
管(10)に取り付けた例を示す概念図である。採取さ
れる透過液は、流量調節バルブ(11)で流束を調節し
てある。また、自動バルブ(12)により、対象分離膜
モジュールが非定常運転(例えば、逆洗浄時)になった
場合は、液が遮断される。膜漏れを検知した場合、液面
検知のセンサー(4)により検知され、本来の膜分離設
備に信号を伝え、運転を制御することが可能となる。
FIG. 3 is a conceptual diagram showing an example in which the membrane leak detection device (8) according to the present invention of FIG. 1 or 2 is attached to the permeate pipe (10) of the target separation membrane module. The flux of the permeated liquid collected is regulated by a flow regulating valve (11). Further, the automatic valve (12) shuts off the liquid when the target separation membrane module is in an unsteady operation (for example, during backwashing). When a membrane leak is detected, it is detected by the liquid level detection sensor (4), and a signal can be transmitted to the original membrane separation equipment to control the operation.

【0023】図4は、図3と同様にして本発明になる膜
漏れ検知装置(8)を、直接対象分離膜モジュールに取
り付けた例を示す概念図である。定流量弁(13)によ
り、透過液の流量調節が行える。
FIG. 4 is a conceptual diagram showing an example in which the membrane leak detection device (8) according to the present invention is directly attached to the target separation membrane module similarly to FIG. The flow rate of the permeate can be adjusted by the constant flow valve (13).

【0024】図3および図4において、流量調節バルブ
(11)と自動バルブ(12)との組合せ、および定流
量弁(13)とは同じ作用をするため、どちらを使用し
てもかまわない。
In FIGS. 3 and 4, the combination of the flow rate adjusting valve (11) and the automatic valve (12) and the constant flow rate valve (13) have the same operation, so either one may be used.

【0025】[0025]

【実施例】本発明を実施例にて具体的に説明するが、本
発明は、以下の実施例に限定されるものではない。
EXAMPLES The present invention will be specifically described with reference to examples, but the present invention is not limited to the following examples.

【0026】実施例1(膜漏れ検知装置の製作例) 図1に示す膜漏れ検知装置を製作した。内径20mm高
さ300mmの透過液を受ける容器の上部に漏水検知器
(オムロン社製61F−WLA型)のセンサーを取り付
け、容器の下部に、検知膜として、平均孔径1μmで、
膜直径12mm(膜面積1.1cm2 )のセルロース系
メンブレンフィルター(富士写真フイルム社製ミクロフ
ィルター、FR−100番)を取り付けた。検知膜から
漏水検知のセンサーまでの高さは、250mmであっ
た。また、容器の側部のセンサーより高い位置に、空気
抜きの穴を設けた。
Example 1 (Production Example of Membrane Leak Detection Device) The membrane leakage detection device shown in FIG. 1 was produced. A sensor of a water leakage detector (61F-WLA type manufactured by OMRON) is attached to the upper part of a container that receives a permeated liquid having an inner diameter of 20 mm and a height of 300 mm, and an average pore diameter of 1 μm is used as a detection film on the lower part of the container.
A cellulose-based membrane filter having a membrane diameter of 12 mm (membrane area 1.1 cm 2 ) (a micro filter manufactured by Fuji Photo Film Co., FR-100) was attached. The height from the detection film to the leak detection sensor was 250 mm. Also, an air vent hole was provided at a position higher than the sensor on the side of the container.

【0027】実施例2 対象分離膜として中空糸膜モジュールA(ダイセン・メ
ンブレン・システムズ社製、FF03−FL−FUS1
041、膜面積2.3m2 、分画分子量10万、平均孔
径0.01μm)を用いた。原水に工業用水を用い、
0.2m3 /時間の透過速度で全量濾過運転を行った。
中空糸膜モジュールAの透過液配管から、600ml/
時間の速度で、透過液の一部を枝配管により採取し、膜
漏れ検知装置に導入した。12時間運転したが何等異常
は無かった。この間、膜漏れ検知装置の容器内部の透過
液液面は、検知膜の約15cmの高さで平衡していた。
この後、中空糸膜モジュールAの中空糸を数本切断し、
膜漏れを生じさせた。この中空糸膜モジュールAを取り
付け同様に運転したところ、運転開始から約20分で、
膜漏れを検知することができた。
Example 2 Hollow fiber membrane module A (manufactured by Daisen Membrane Systems, FF03-FL-FUS1) as a target separation membrane
041, membrane area 2.3 m 2 , cut-off molecular weight 100,000, average pore size 0.01 μm) were used. Using industrial water as raw water,
A total volume filtration operation was performed at a permeation rate of 0.2 m 3 / hour.
From the permeate pipe of the hollow fiber membrane module A, 600 ml /
At a speed of time, a part of the permeated liquid was collected through a branch pipe and introduced into a membrane leak detection device. I ran for 12 hours, but there was nothing abnormal. During this time, the liquid level of the permeated liquid inside the container of the membrane leak detection device was in equilibrium at a height of about 15 cm of the detection membrane.
After that, several hollow fibers of the hollow fiber membrane module A were cut,
A membrane leak was created. When this hollow fiber membrane module A was attached and operated in the same manner, about 20 minutes from the start of operation,
Membrane leakage could be detected.

【0028】実施例3 対象分離膜として中空糸膜モジュールB(ダイセン・メ
ンブレン・システムズ社製、FE10−FC−FUC1
581、膜面積5m2 、分画分子量15万)を用いた。
原水に工業用水を用い、0.3m3 /時間の透過速度で
運転を行った。中空糸膜モジュールAの透過液配管か
ら、480ml/時間の速度で、透過液の一部を枝配管
により採取し、膜漏れ検知装置に導入して12時間運転
したが何等異常は無かった。この後、中空糸膜モジュー
ルBの中空糸を数本切断し、膜漏れを生じさせた。この
中空糸膜モジュールBを取り付け同様に運転したとこ
ろ、運転開始から約30分で、膜漏れを検知することが
できた。
Example 3 Hollow fiber membrane module B (manufactured by Daisen Membrane Systems, FE10-FC-FUC1) as a target separation membrane
581, membrane area 5 m 2 , fraction molecular weight 150,000).
Industrial water was used as raw water, and operation was performed at a permeation rate of 0.3 m 3 / hour. A part of the permeated liquid was sampled from the permeated liquid pipe of the hollow fiber membrane module A at a rate of 480 ml / hour through a branch pipe, introduced into a membrane leak detection device, and operated for 12 hours, but there was no abnormality. After that, several hollow fibers of the hollow fiber membrane module B were cut to cause membrane leakage. When this hollow fiber membrane module B was attached and operated in the same manner, it was possible to detect a membrane leak in about 30 minutes from the start of operation.

【0029】[0029]

【発明の効果】本発明の膜漏れ検知装置および検知方法
は、簡単な装置で簡便な方法であるため、本装置を組み
込んだ膜設備は、コスト的に有利になる。また、コンパ
クトで、安価な装置であることから、個々の膜モジュー
ルに付設でき、膜漏れ検知の信頼性も高い。また、本発
明の膜漏れ検知装置および検知方法にて検知された信号
を、本来の膜分離設備に連動させることで、膜漏れ検知
時の膜分離設備の運転を制御したりすることも可能であ
る。
Since the membrane leak detection device and the detection method of the present invention are simple and simple methods, the membrane equipment incorporating this device is advantageous in terms of cost. Further, since it is a compact and inexpensive device, it can be attached to each membrane module, and the reliability of membrane leak detection is high. Further, by interlocking the signal detected by the membrane leak detection device and the detection method of the present invention with the original membrane separation equipment, it is possible to control the operation of the membrane separation equipment at the time of membrane leak detection. is there.

【0030】また、本発明の膜漏れ検知装置および検知
方法は、どの様な用途のモジュールにでも適応できる。
例えば、中空糸膜モジュール、チューブラー膜モジュー
ル、プレート・アンド・フレームモジュール、スパイラ
ルモジュール、平膜モジュールなどが挙げられる。ま
た、適応できる用途は、どの様な分野でもよい。例え
ば、従来の凝集−沈殿−砂濾過−塩素滅菌工程を経る方
法に代わる新たな技術としての水浄化システムへの応用
が、また、食品分野においては、コーヒー、紅茶、果汁
の濃縮あるいは果汁の清澄化に、バイオ・酵素・製薬分
野においては、無菌パイロジェンフリー精製水の製造
等、さらに電子工業分野においては、ウェハー研磨排水
の再利用などが挙げられる。
Further, the membrane leak detection device and the detection method of the present invention can be applied to a module for any application.
Examples include hollow fiber membrane modules, tubular membrane modules, plate and frame modules, spiral modules, flat membrane modules, and the like. Further, the applicable application may be any field. For example, the application to a water purification system as a new technology replacing the conventional method of passing through a coagulation-precipitation-sand filtration-chlorine sterilization step, and in the food field, coffee, tea, juice concentration or clarification of juice. In the field of biotechnology, enzymes, and pharmaceuticals, production of aseptic pyrogen-free purified water and the like, and in the field of electronics industry, reuse of wafer polishing wastewater and the like can be mentioned.

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

【図1】 本発明の膜漏れ検知装置の一例を示す断面概
略図である。
FIG. 1 is a schematic sectional view showing an example of a membrane leakage detection device of the present invention.

【図2】 本発明の膜漏れ検知装置の他の一例を示す断
面概略図である。
FIG. 2 is a schematic cross-sectional view showing another example of the membrane leakage detection device of the present invention.

【図3】 本発明の膜漏れ検知装置を対象分離膜モジュ
ールの透過液配管に取り付けた一例を示す概念図であ
る。
FIG. 3 is a conceptual diagram showing an example in which the membrane leak detection device of the present invention is attached to a permeate pipe of a target separation membrane module.

【図4】 本発明の膜漏れ検知装置を直接対象分離膜モ
ジュールに取り付けた一例を示す概念図である。
FIG. 4 is a conceptual diagram showing an example in which the membrane leak detection device of the present invention is directly attached to a target separation membrane module.

【符号の説明】[Explanation of symbols]

1 検知膜 2 枝配管 3 容器 4 センサー 5 空気抜き 6 オーバーフロー配管 7 配管 8 膜漏れ検知装置 9 対象分離膜モジュール 10 透過液配管 11 流量調節バルブ 12 自動バルブ 13 定流量弁 1 Detection Membrane 2 Branch Piping 3 Container 4 Sensor 5 Air Venting 6 Overflow Piping 7 Piping 8 Membrane Leak Detection Device 9 Target Separation Membrane Module 10 Permeate Liquid Piping 11 Flow Control Valve 12 Automatic Valve 13 Constant Flow Valve

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 膜漏れを検知したい対象分離膜より大き
い平均孔径と遥かに小さい膜面積とを有する検知膜、前
記分離膜の透過液の一部を採取する枝配管、採取した透
過液を蓄積する容器および該容器の液面状態を検知する
センサーを有することを特徴とする膜漏れ検知装置。
1. A detection membrane having a larger average pore size and a much smaller membrane area than the target separation membrane for which membrane leakage is to be detected, a branch pipe for collecting a part of the permeate of the separation membrane, and collecting the collected permeate. A film leakage detection device, comprising: a container that operates and a sensor that detects a liquid surface state of the container.
【請求項2】 検知膜の平均孔径が、対象分離膜の平均
孔径の2〜10000倍であることを特徴とする請求項
1記載の膜漏れ検知装置。
2. The membrane leak detection device according to claim 1, wherein the average pore diameter of the detection membrane is 2 to 10000 times the average pore diameter of the target separation membrane.
【請求項3】 膜漏れ検知装置が、対象分離膜モジュー
ル単位当たり1個取り付けられていることを特徴とする
請求項1または2記載の膜漏れ検知装置。
3. The membrane leakage detection device according to claim 1, wherein one membrane leakage detection device is attached per target separation membrane module unit.
【請求項4】 膜漏れを検知したい対象分離膜の透過液
の一部を枝配管により採取し、液面状態を検知するセン
サーを有する容器に導入した後、前記分離膜より大きい
平均孔径と遥かに小さい膜面積とを有する検知膜で濾過
し、膜漏れを検知膜の閉塞現象として前記液センサーに
より検知することを特徴とする膜漏れ検知方法。
4. A part of the permeated liquid of a target separation membrane for which membrane leakage is to be detected is collected by a branch pipe and introduced into a container having a sensor for detecting a liquid level condition, and then the average pore diameter is far larger than that of the separation membrane. A method for detecting a membrane leak, which comprises filtering the membrane with a membrane having a small membrane area and detecting membrane leakage by the liquid sensor as a clogging phenomenon of the membrane.
【請求項5】 検知膜の平均孔径が、対象分離膜の平均
孔径の2〜10000倍であることを特徴とする請求項
4記載の膜漏れ検知方法。
5. The method for detecting a membrane leak according to claim 4, wherein the average pore diameter of the detection membrane is 2 to 10000 times the average pore diameter of the target separation membrane.
【請求項6】 対象分離膜が漏れを生じていない状態で
の容器に受ける透過液の流束が、検知膜の濾過流束より
も小さい流束である請求項4または5記載の膜漏れ検知
方法。
6. The membrane leak detection according to claim 4 or 5, wherein the flux of the permeated liquid received by the container when the target separation membrane is not leaking is smaller than the filtration flux of the detection membrane. Method.
JP2664296A 1996-02-14 1996-02-14 Membrane leakage detector and detecting method Pending JPH09220452A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2664296A JPH09220452A (en) 1996-02-14 1996-02-14 Membrane leakage detector and detecting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2664296A JPH09220452A (en) 1996-02-14 1996-02-14 Membrane leakage detector and detecting method

Publications (1)

Publication Number Publication Date
JPH09220452A true JPH09220452A (en) 1997-08-26

Family

ID=12199110

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2664296A Pending JPH09220452A (en) 1996-02-14 1996-02-14 Membrane leakage detector and detecting method

Country Status (1)

Country Link
JP (1) JPH09220452A (en)

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