JP2001205056A - Method for inspecting leak of separation membrane - Google Patents
Method for inspecting leak of separation membraneInfo
- Publication number
- JP2001205056A JP2001205056A JP2000019718A JP2000019718A JP2001205056A JP 2001205056 A JP2001205056 A JP 2001205056A JP 2000019718 A JP2000019718 A JP 2000019718A JP 2000019718 A JP2000019718 A JP 2000019718A JP 2001205056 A JP2001205056 A JP 2001205056A
- Authority
- JP
- Japan
- Prior art keywords
- separation membrane
- organic solvent
- aqueous solution
- membrane
- immersed
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、固液分離を行う分
離膜のリーク検査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 a method for inspecting a leakage of a separation membrane for performing solid-liquid separation.
【0002】[0002]
【従来の技術】従来より、浄水処理、下排水処理、或い
は産業排水の処理、発電、食品製造、薬品製造、電子部
品製造等、様々な産業分野において、中空糸膜、平膜等
の分離膜を配設した分離膜モジュールを用いて、固液分
離を行う方法が広く行われている。2. Description of the Related Art Conventionally, separation membranes such as hollow fiber membranes and flat membranes have been used in various industrial fields such as water purification treatment, sewage treatment, or industrial wastewater treatment, power generation, food production, chemical production, and electronic component production. A method for performing solid-liquid separation by using a separation membrane module provided with is widely used.
【0003】この様な分離膜モジュールにおいては、その製
造時或いはモジュールを使用に供する前に、配設された
分離膜に欠陥が無いことを確認するため、リーク検査が
行われる。[0003] In such a separation membrane module, a leak test is performed at the time of its manufacture or before using the module, in order to confirm that there is no defect in the provided separation membrane.
【0004】この際、分離膜モジュールを液体に浸漬して分
離膜を濡らした後、浸漬した液体中で分離膜のバブルポ
イント以下の圧力で、分離膜の二次側より空気が圧入さ
れる。この時、分離膜が本来有する孔径よりも大きな孔
があると、分離膜表面より気泡が漏洩するので、この気
泡を検知することによりリークの有無を確認することが
できる。なお、この様なリーク検査方法においては、前
もって分離膜を液体により完全に濡らす必要があるた
め、浸漬させる液体には通常水溶性の有機溶剤が用いら
れる。[0004] At this time, after the separation membrane module is immersed in a liquid to wet the separation membrane, air is injected from the secondary side of the separation membrane into the immersed liquid at a pressure equal to or lower than the bubble point of the separation membrane. At this time, if there is a pore larger than the pore diameter originally possessed by the separation membrane, bubbles leak from the surface of the separation membrane. Therefore, the presence or absence of the leak can be confirmed by detecting the bubbles. In such a leak inspection method, since it is necessary to completely wet the separation membrane with a liquid in advance, a water-soluble organic solvent is usually used as the liquid to be immersed.
【0005】[0005]
【発明が解決しようとする課題】通常、分離膜モジュー
ルにおいては、分離膜がポッティング材により集水部に
固定されており、分離膜を透過した処理液を前記集水部
を介して引き抜くことで、固液分離が行われる。また、
前述した分離膜モジュールは、その形態にもよるが、通
常樹脂製のハウジング内に収納される。前述したポッテ
ィング材としては、一般にウレタン樹脂、エポキシ樹脂
等が、また前記ハウジングや集水部には一般に、成形が
容易で安価なことから、塩ビ樹脂、ABS樹脂等の合成
樹脂が用いられている。Generally, in a separation membrane module, a separation membrane is fixed to a water collecting portion by a potting material, and a treatment liquid that has passed through the separation membrane is drawn out through the water collecting portion. Then, solid-liquid separation is performed. Also,
The above-described separation membrane module is usually housed in a resin housing, depending on its form. As the above-mentioned potting material, a urethane resin, an epoxy resin, or the like is generally used, and a synthetic resin such as a PVC resin, an ABS resin, or the like is generally used for the housing and the water collecting portion because molding is easy and inexpensive. .
【0006】しかしながら、リーク検査を行う目的で分離膜
モジュールを有機溶剤に浸漬させると、ポッティング材
として用いられているウレタン樹脂、エポキシ樹脂が膨
潤を起こすため、耐久性が低下するといった不都合を有
する。また、ハウジング、集水部等に用いられる塩ビ樹
脂、ABS樹脂等も、有機溶剤に浸漬した際に、いわゆ
るソルベントクラックが発生する場合がある。[0006] However, if the separation membrane module is immersed in an organic solvent for the purpose of performing a leak test, the urethane resin or epoxy resin used as a potting material swells, so that there is a disadvantage that the durability is reduced. In addition, when a PVC resin, an ABS resin, or the like used for a housing, a water collecting portion, or the like is immersed in an organic solvent, a so-called solvent crack may occur.
【0007】一方で、分離膜を有機溶剤に浸漬することなく
水中に浸漬し、分離膜の二次側より気体を圧入すると、
分離膜表面全体が完全に水に濡れないため、分離膜に欠
陥がない場合でも、バブルポイントよりも低い圧力で、
分離膜中の濡れていない部分から気体が漏出するため、
リークの有無の判断ができない。On the other hand, when the separation membrane is immersed in water without being immersed in an organic solvent, and gas is injected from the secondary side of the separation membrane,
Since the entire surface of the separation membrane is not completely wetted with water, even if the separation membrane has no defects, at a pressure lower than the bubble point,
Because gas leaks from the non-wet part of the separation membrane,
It is not possible to determine the presence or absence of a leak.
【0008】[0008]
【課題を解決するための手段】本発明は、この様な不都
合を解決するためになされたものであり、分離膜モジュ
ールを構成する部材に影響を与えることなく、分離膜の
リーク検査を行う方法を提供することを目的とする。す
なわち、本発明の要旨は、分離膜を有機溶剤水溶液に浸
漬した後、分離膜の二次側より分離膜のバブルポイント
以下の圧力で気体を圧入することにより、分離膜のリー
クの有無を検査する方法であって、検査に用いる分離膜
は、その表面と水との接触角φが135°未満である分
離膜であり、前記有機溶剤水溶液における有機溶剤の濃
度X(vol%)が、式(1)を満足することを特徴と
する分離膜のリーク検査方法にある。 60>X≧98/exp(1.2+cosφ) ・・・(1)SUMMARY OF THE INVENTION The present invention has been made to solve such inconveniences, and there is provided a method for inspecting a leakage of a separation membrane without affecting members constituting a separation membrane module. The purpose is to provide. That is, the gist of the present invention is to test whether or not there is a leak in the separation membrane by immersing the separation membrane in an organic solvent aqueous solution and then injecting gas from the secondary side of the separation membrane at a pressure not higher than the bubble point of the separation membrane. The separation membrane used in the inspection is a separation membrane having a contact angle φ between its surface and water of less than 135 °, and the concentration X (vol%) of the organic solvent in the organic solvent aqueous solution is represented by the following formula: A method for inspecting a leak of a separation film, which satisfies (1). 60> X ≧ 98 / exp (1.2 + cosφ) (1)
【0009】分離膜を有機溶剤水溶液に浸漬した後、浸漬し
た有機溶剤水溶液中で分離膜の二次側より気体を圧入す
る構成とすると、時間効率に優れたリーク検査を行うこ
とができる。また、分離膜を有機溶剤水溶液に浸漬した
後、この分離膜を取り出して水中に浸漬し、分離膜の二
次側より気体を圧入する構成とすると、分離膜モジュー
ルの有機溶剤水溶液中への浸漬時間が短縮され、構成部
材への影響が更に低減される。用いる有機溶剤が、メタ
ノール、エタノール、プロパノール、イソプロパノー
ル、ブタノールから選ばれる少なくとも1種であると、
他の有機溶剤と比べ、分離膜モジュールへの影響が小さ
く好ましい。When the separation membrane is immersed in an organic solvent aqueous solution and then gas is injected from the secondary side of the separation membrane in the immersed organic solvent aqueous solution, a leak test excellent in time efficiency can be performed. Further, if the separation membrane is immersed in an organic solvent aqueous solution, the separation membrane is taken out and immersed in water, and gas is injected from the secondary side of the separation membrane, so that the separation membrane module is immersed in the organic solvent aqueous solution. The time is reduced and the effect on the components is further reduced. When the organic solvent used is at least one selected from methanol, ethanol, propanol, isopropanol, and butanol,
The influence on the separation membrane module is small as compared with other organic solvents, which is preferable.
【0010】[0010]
【発明の実施の形態】以下本発明の実施の形態を説明す
るが、本発明はそれらに限定されるものではない。図1
は、本発明のリーク検査方法の実施態様の一例を示す概
略図である。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described, but the present invention is not limited thereto. FIG.
1 is a schematic view showing an example of an embodiment of a leak inspection method according to the present invention.
【0011】まず容器1に有機溶剤の水溶液2を入れる。次
いで、分離膜が配設された分離膜モジュール3が完全に
水溶液2に浸漬するように、分離膜モジュールを容器1
内に挿入する。有機溶剤水溶液への浸漬時間は、1分〜
1時間とすることが好ましい。浸漬時間が1分未満であ
ると、分離膜の濡れが不十分となることがあり、1時間
を超えると、構成部材への影響が発生する可能性が生じ
る。更に好ましくは、浸漬時間を5〜30分とすると、
リーク検査効率の観点からも好適である。First, an aqueous solution 2 of an organic solvent is placed in a container 1. Next, the separation membrane module is placed in the container 1 so that the separation membrane module 3 provided with the separation membrane is completely immersed in the aqueous solution 2.
Insert inside. The immersion time in the organic solvent aqueous solution is from 1 minute to
Preferably, it is one hour. When the immersion time is less than 1 minute, the wetting of the separation membrane may be insufficient. When the immersion time exceeds 1 hour, there is a possibility that the influence on the constituent members may occur. More preferably, when the immersion time is 5 to 30 minutes,
It is also preferable from the viewpoint of leak test efficiency.
【0012】ここで、有機溶剤水溶液における有機溶剤濃度
X(vol%)は、下記式(1)を満たす濃度とする。 60>X≧98/exp(1.2+cosφ) ・・・(1) ここでφは、分離膜表面と水との接触角(°)をいう。
なお、本発明の検査方法は、φが135°未満である分
離膜に適用される。Here, the concentration X (vol%) of the organic solvent in the aqueous solution of the organic solvent is a concentration satisfying the following equation (1). 60> X ≧ 98 / exp (1.2 + cosφ) (1) Here, φ indicates a contact angle (°) between the surface of the separation membrane and water.
Note that the inspection method of the present invention is applied to a separation membrane having φ of less than 135 °.
【0013】ここで、分離膜表面と水との接触角は、図2に
示すように、水中に、中空糸膜、平膜等分離膜モジュー
ルに配設する分離膜を概ね垂直に浸漬させた際に、膜表
面と水との接触部分を写真撮影行うことにより測定する
ことができる。なお、測定に使用する水の温度は20℃
±5℃とし、水に浸漬させてから5分後に膜表面と水と
の接触部分を観察するものとする。観察の際は膜及び水
面が揺らぐことのないよう、静止状態にて観察を行うも
のとする。As shown in FIG. 2, the contact angle between the surface of the separation membrane and water is such that a separation membrane provided in a separation membrane module such as a hollow fiber membrane or a flat membrane is immersed substantially vertically in water. At this time, it can be measured by taking a photograph of a contact portion between the film surface and water. The temperature of the water used for the measurement was 20 ° C.
The temperature was set to ± 5 ° C., and 5 minutes after immersion in water, the contact portion between the film surface and water was observed. At the time of observation, observation shall be performed in a stationary state so that the film and the water surface do not fluctuate.
【0014】浸漬させる有機溶剤の濃度が、98/exp
(1.2+cosφ)の値未満となると、分離膜を短時
間の浸漬時間内で完全に濡らすことが困難となる。そし
て、分離膜が完全に濡れていないと、分離膜の二次側よ
り気体を圧入した際に、分離膜に欠陥がない場合でも、
完全に濡れていない部分より気体が漏出するためリーク
の有無を判断することができない。When the concentration of the organic solvent to be immersed is 98 / exp
When the value is less than (1.2 + cosφ), it is difficult to completely wet the separation membrane within a short immersion time. And if the separation membrane is not completely wet, when gas is injected from the secondary side of the separation membrane, even if there is no defect in the separation membrane,
Since gas leaks out from a part that is not completely wet, it is not possible to determine whether or not there is a leak.
【0015】また、有機溶剤の濃度が60vol%以上とな
ると、前述したごとく、分離膜膜モジュールを構成する
部材のダメージが懸念される。なお、分離膜表面と水と
の接触角が135°以上である分離膜は、疎水性が高
く、有機溶剤濃度が60vol%以上である有機溶剤水
溶液への浸漬が必要となるため、本発明のリーク検査方
法を適用できない。[0015] When the concentration of the organic solvent is 60 vol% or more, as described above, there is a concern that members constituting the separation membrane module may be damaged. The separation membrane having a contact angle of 135 ° or more between the surface of the separation membrane and water has high hydrophobicity and requires immersion in an organic solvent aqueous solution having an organic solvent concentration of 60 vol% or more. The leak inspection method cannot be applied.
【0016】本発明に使用する有機溶剤は、水溶性の有機溶
剤で有れば特に限定されるものではないが、分離膜モジ
ュールの構成部材への影響が少ないことから、メタノー
ル、エタノール、プロパノール、イソプロパノール、ブ
タノールから選ばれる少なくとも1種を用いることが好
ましい。これらの内、安全性が高く安価であることか
ら、エタノールを用いることが更に好ましい。The organic solvent used in the present invention is not particularly limited as long as it is a water-soluble organic solvent. However, since the organic solvent has little influence on the components of the separation membrane module, methanol, ethanol, propanol, It is preferable to use at least one selected from isopropanol and butanol. Of these, ethanol is more preferably used because of its high safety and low cost.
【0017】また、本発明においては、分離膜を有機溶剤水
溶液に浸漬させた後、分離膜の二次側より分離膜のバブ
ルポイント以下の圧力で気体を圧入する。なお、分離膜
のバブルポイントとは日本工業規格JIS K 383
2にて定められた方法で測定された圧力を指す。In the present invention, after the separation membrane is immersed in an organic solvent aqueous solution, gas is injected from the secondary side of the separation membrane at a pressure equal to or lower than the bubble point of the separation membrane. The bubble point of the separation membrane is defined by Japanese Industrial Standard JIS K 383.
Refers to the pressure measured by the method specified in 2.
【0018】この際、有機溶剤水溶液に浸漬させた後、その
ままの状態で、分離膜の二次側より加圧して、気泡の発
生の有無を確認する構成とすると、時間効率に優れたリ
ーク検査を行うことができる。但し、有機溶剤水溶液中
に浸漬される時間が長くなるため、耐溶剤性の低いポッ
ティング材やハウジングを用いた分離膜モジュールに配
設された分離膜のリーク検査を行う場合にはこの方法は
好ましくない。[0018] At this time, if a configuration is adopted in which the presence or absence of bubbles is confirmed by immersing the substrate in an aqueous solution of an organic solvent and then pressing it from the secondary side of the separation membrane as it is, a leak test excellent in time efficiency It can be performed. However, this method is preferable when performing a leak test on a separation membrane provided in a separation membrane module using a potting material or a housing having low solvent resistance, since the time for immersion in an organic solvent aqueous solution becomes longer. Absent.
【0019】この様な場合、分離膜を有機溶剤水溶液に浸漬
して分離膜を濡らした後、有機溶剤水溶液より取り出し
てこれを水中に浸漬して、分離膜の二次側より気体を圧
入する構成とすると、有機溶剤水溶液中への浸漬時間を
短くすることができる。In such a case, the separation membrane is immersed in an organic solvent aqueous solution to wet the separation membrane, taken out of the organic solvent aqueous solution, immersed in water, and gas is injected from the secondary side of the separation membrane. With this configuration, the immersion time in the organic solvent aqueous solution can be shortened.
【0020】分離膜の二次側に圧入する気体は、空気、酸
素、窒素、炭酸ガス等任意の気体を用いることができ
る。また、気体の圧入は、コンプレッサー、ブロワー、
ガスボンベ等の加圧源を用いて行うことができるが、加
圧に際してはレギュレーター等の圧力調整可能な器具を
用いて行うことが好ましい。As the gas to be injected into the secondary side of the separation membrane, any gas such as air, oxygen, nitrogen and carbon dioxide can be used. Gas injection is performed by compressor, blower,
It can be performed using a pressurizing source such as a gas cylinder, but it is preferable to perform pressurization using a pressure-adjustable instrument such as a regulator.
【0021】気体の圧入は、分離膜のバブルポイント以下の
圧力であれば、リークの有無を評価できるが、分離膜モ
ジュールに負荷がかかることから、バブルポイントの6
0%以下の圧力で導入するのが好ましい。When gas is injected at a pressure equal to or lower than the bubble point of the separation membrane, the presence or absence of a leak can be evaluated.
It is preferably introduced at a pressure of 0% or less.
【0022】[0022]
【実施例】以下、本発明を実施例により具体的に説明す
る。 <実施例1>エバール樹脂で親水化されたポリエチレン
中空糸膜をスクリーン状に展開固定した中空糸膜モジュ
ール(商品名:ステラポアL、三菱レイヨン(株)製;
平均孔径0.1μm、バブルポイント180kPa、中
空糸膜表面の水との接触角50°、ハウジング部材はA
BS樹脂、ポッテイング部材にはウレタン樹脂からな
る)を用いて、以下の手順でリーク検査を行った。 (1)20vol%のエタノール水溶液中に中空糸膜モ
ジュールを10分間浸漬する。 (2)前記エタノール水溶液中にて、コンプレッサーを
用いて加圧した空気を、50kPaの圧力にて中空糸膜
の二次側より圧入する。その結果、中空糸膜の一次側よ
り空気の漏洩は無く、リークが無いことが確認できた。The present invention will be described below in more detail with reference to examples. <Example 1> A hollow fiber membrane module (trade name: Stellapore L, manufactured by Mitsubishi Rayon Co., Ltd.) in which a polyethylene hollow fiber membrane hydrophilized with an Evar resin is developed and fixed in a screen shape.
Average pore diameter 0.1 μm, bubble point 180 kPa, contact angle of water on the surface of hollow fiber membrane 50 °, housing member A
Using a BS resin and a potting member made of a urethane resin), a leak test was performed in the following procedure. (1) The hollow fiber membrane module is immersed in a 20 vol% ethanol aqueous solution for 10 minutes. (2) Into the ethanol aqueous solution, air pressurized using a compressor is injected at a pressure of 50 kPa from the secondary side of the hollow fiber membrane. As a result, there was no air leakage from the primary side of the hollow fiber membrane, and it was confirmed that there was no leakage.
【0023】また、リーク検査後の膜モジュールについて、
下記の手順にて圧力耐久性試験を実施した。 (1)中空糸膜部分をポッテイング材にて封止した近傍
より切り取り、さらに中空部分をウレタン樹脂にて封止
した。 (2)ハウジングの濾過液取り出し口から、水を圧送し
て加圧した後、加圧を停止し、ハウジング或いはポッテ
イング部材が破壊されるまで加圧/停止を繰り返した。
この際、加圧時の圧力は300kPa、加圧保持時間は
5秒間、停止時間は5秒間とした。その結果、表1に示
すように、リーク検査を実施していない新品の中空糸膜
モジュールとほぼ同等の耐久性を示した。なお、本実施
例において使用される中空糸膜に関して、式(1)の右
項により算出される値は15.5である。Further, regarding the membrane module after the leak inspection,
A pressure durability test was performed according to the following procedure. (1) The hollow fiber membrane portion was cut off from the vicinity sealed with a potting material, and the hollow portion was further sealed with urethane resin. (2) After pressurizing and feeding water from the filtrate outlet of the housing, the pressurization was stopped, and the pressurization / stop was repeated until the housing or the potting member was broken.
At this time, the pressure during the pressurization was 300 kPa, the pressurization holding time was 5 seconds, and the stop time was 5 seconds. As a result, as shown in Table 1, the durability was almost the same as that of a new hollow fiber membrane module not subjected to the leak test. The value calculated from the right term of the equation (1) for the hollow fiber membrane used in this example is 15.5.
【0024】[0024]
【表1】 [Table 1]
【0025】<実施例2>実施例1と同様の中空糸膜モジュ
ールを用いて、以下の方法によりリーク検査を行った。 (1)20vol%のエタノール水溶液に中空糸膜モジ
ュールを10分間浸漬する。 (2)エタノール水溶液より中空糸膜モジュールを取り
出し、これを水中に浸漬させて、コンプレッサーを用い
て加圧した空気を、50kPaの圧力にて中空糸膜の二
次側より圧入した。その結果、中空糸膜の一次側より空
気の漏洩は無く、リークが無いことが確認できた。ま
た、リーク検査後の膜モジュールについて、実施例1と
同様の方法にて圧力耐久性試験を実施したところ、表1
に示すように、リーク検査を実施していない新品の中空
糸膜モジュールとほぼ同等の耐久性を示した。Example 2 Using the same hollow fiber membrane module as in Example 1, a leak test was performed by the following method. (1) The hollow fiber membrane module is immersed in a 20 vol% ethanol aqueous solution for 10 minutes. (2) The hollow fiber membrane module was taken out from the aqueous ethanol solution, immersed in water, and air pressurized using a compressor was injected from the secondary side of the hollow fiber membrane at a pressure of 50 kPa. As a result, there was no air leakage from the primary side of the hollow fiber membrane, and it was confirmed that there was no leakage. In addition, a pressure durability test was performed on the membrane module after the leak inspection in the same manner as in Example 1.
As shown in the figure, the durability was almost the same as that of a new hollow fiber membrane module not subjected to the leak test.
【0026】<比較例1>実施例1と同様の中空糸膜モジュ
ールを用いて以下の方法でリーク検査を行った。 (1)10vol%エタノール水溶液中に中空糸膜モジ
ュールを10分間浸漬した。 (2)前記エタノール水溶液中にて、コンプレッサーを
用いて加圧した空気を、50kPaの圧力にて中空糸膜
モジュールの二次側より圧入した。その結果中空糸膜表
面で気泡が漏洩したが、この中空糸モジュールについて
実施例1記載の方法でリーク検査を行うと、気泡の漏洩
は起こらず、リークが無いことが確認できた。<Comparative Example 1> Using the same hollow fiber membrane module as in Example 1, a leak test was performed by the following method. (1) The hollow fiber membrane module was immersed in a 10 vol% ethanol aqueous solution for 10 minutes. (2) Into the ethanol aqueous solution, air pressurized using a compressor was injected at a pressure of 50 kPa from the secondary side of the hollow fiber membrane module. As a result, air bubbles leaked on the surface of the hollow fiber membrane. When a leak test was performed on the hollow fiber module by the method described in Example 1, no air bubbles leaked, and it was confirmed that there was no leak.
【0027】<比較例2>実施例1と同様の中空糸膜モジュ
ールを用いて以下の方法でリーク検査を行った。 (1)100%エタノールに中空糸膜モジュールを10
分間浸漬した。 (2)前記エタノール水溶液中にて、コンプレッサーを
用いて加圧した空気を、50kPaの圧力にて中空糸膜
モジュールの二次側より圧入した。その結果気泡の漏洩
は起こらず、リークが無いことが確認できたものの、リ
ーク検査後の膜モジュールについて、実施例1と同様の
方法にて圧力耐久性試験を実施したところ、表1に示す
ように、リーク検査を実施していない新品の中空糸膜モ
ジュールと比較して耐久性が低下していた。<Comparative Example 2> Using the same hollow fiber membrane module as in Example 1, a leak test was performed by the following method. (1) 10 hollow fiber membrane modules in 100% ethanol
Soak for minutes. (2) Into the ethanol aqueous solution, air pressurized using a compressor was injected at a pressure of 50 kPa from the secondary side of the hollow fiber membrane module. As a result, no leakage of air bubbles occurred, and it was confirmed that there was no leakage. However, a pressure durability test was performed on the membrane module after the leak inspection in the same manner as in Example 1, and as shown in Table 1. In addition, the durability was lower than that of a new hollow fiber membrane module that had not been subjected to a leak test.
【0028】[0028]
【発明の効果】本発明の分離膜のリーク検査方法によれ
ば、分離膜モジュールが濃度の薄い有機溶剤水溶液中に
浸漬されるので、分離膜モジュールを構成する部材にダ
メージを与えることなく、分離膜のリーク検査を行うこ
とができる。According to the method for inspecting the leak of a separation membrane according to the present invention, the separation membrane module is immersed in a low-concentration aqueous solution of an organic solvent. A film leak inspection can be performed.
【図1】本発明の分離膜のリーク検査方法の実施形態を
示す概略図である。FIG. 1 is a schematic view showing an embodiment of a separation membrane leak inspection method of the present invention.
【図2】分離膜と水との接触角を測定する方法を示す概
略図である。FIG. 2 is a schematic view showing a method for measuring a contact angle between a separation membrane and water.
1:容器 2:有機溶剤水溶液 3:分離膜モジュール 1: container 2: organic solvent aqueous solution 3: separation membrane module
フロントページの続き (72)発明者 竹田 哲 愛知県名古屋市東区砂田橋四丁目1番60号 三菱レイヨン株式会社商品開発研究所内 (72)発明者 本城 賢治 愛知県名古屋市東区砂田橋四丁目1番60号 三菱レイヨン株式会社商品開発研究所内 Fターム(参考) 4D006 HA01 KD28 LA03 MA01 MB20 MC22 PB02 PB08 PC01 PC11 PC42 Continued on the front page (72) Inventor Tetsu Takeda 4-1-1-60 Sunadabashi, Higashi-ku, Nagoya City, Aichi Prefecture Inside Mitsubishi Rayon Co., Ltd. (72) Inventor Kenji Honjo 4--60, Sunadabashi, Higashi-ku, Nagoya City, Aichi Prefecture No. F-term in Mitsubishi Rayon Co., Ltd. Product Development Laboratory (reference) 4D006 HA01 KD28 LA03 MA01 MB20 MC22 PB02 PB08 PC01 PC11 PC42
Claims (4)
分離膜の二次側より分離膜のバブルポイント以下の圧力
で気体を圧入することにより、分離膜のリークの有無を
検査する方法であって、 検査に用いる分離膜は、その表面と水との接触角φが1
35°未満である分離膜であり、 前記有機溶剤水溶液における有機溶剤の濃度X(vol
%)が、式(1)を満足することを特徴とする分離膜の
リーク検査方法。 60>X≧98/exp(1.2+cosφ) ・・・(1)After immersing the separation membrane in an organic solvent aqueous solution,
This is a method to check for leaks in the separation membrane by injecting gas from the secondary side of the separation membrane at a pressure equal to or less than the bubble point of the separation membrane. Contact angle φ is 1
A separation membrane having an angle of less than 35 °, and a concentration X (vol) of the organic solvent in the aqueous organic solvent solution.
%) Satisfies the expression (1). 60> X ≧ 98 / exp (1.2 + cosφ) (1)
浸漬した有機溶剤水溶液中で分離膜の二次側より気体を
圧入することを特徴とする請求項1記載の分離膜のリー
ク検査方法。2. After immersing the separation membrane in an organic solvent aqueous solution,
2. The method according to claim 1, wherein a gas is injected from a secondary side of the separation membrane into the immersed organic solvent aqueous solution.
この分離膜を取り出して水中に浸漬し、分離膜の二次側
より気体を圧入することを特徴とする請求項1記載の分
離膜のリーク検査方法。3. After immersing the separation membrane in an organic solvent aqueous solution,
2. The method according to claim 1, wherein the separation membrane is taken out, immersed in water, and pressurized with gas from a secondary side of the separation membrane.
ール、プロパノール、イソプロパノール、ブタノールか
ら選ばれる少なくとも1種であることを特徴とする請求
項1〜3のいずれか1項記載の分離膜のリーク検査方
法。4. The method according to claim 1, wherein the organic solvent used is at least one selected from methanol, ethanol, propanol, isopropanol, and butanol. .
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Cited By (6)
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JP2002320829A (en) * | 2001-04-25 | 2002-11-05 | Mitsubishi Rayon Co Ltd | Method for inspecting perfectibility of membrane module |
WO2005084785A1 (en) * | 2004-03-03 | 2005-09-15 | Asahi Kasei Pharma Corporation | Method for permeation of gas through porous membrane |
JP2006184189A (en) * | 2004-12-28 | 2006-07-13 | Mitsubishi Rayon Co Ltd | Defect inspection method for hollow fiber membrane |
WO2012173232A1 (en) | 2011-06-16 | 2012-12-20 | 三菱レイヨン株式会社 | Hollow fiber membrane module repair method and hollow fiber membrane module |
WO2019202978A1 (en) | 2018-04-18 | 2019-10-24 | 住友電気工業株式会社 | Pressure test method for solar power generation device housing unit |
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2000
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Cited By (10)
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JP2002320829A (en) * | 2001-04-25 | 2002-11-05 | Mitsubishi Rayon Co Ltd | Method for inspecting perfectibility of membrane module |
WO2005084785A1 (en) * | 2004-03-03 | 2005-09-15 | Asahi Kasei Pharma Corporation | Method for permeation of gas through porous membrane |
JP2006184189A (en) * | 2004-12-28 | 2006-07-13 | Mitsubishi Rayon Co Ltd | Defect inspection method for hollow fiber membrane |
JP4557287B2 (en) * | 2004-12-28 | 2010-10-06 | 三菱レイヨン株式会社 | Hollow fiber membrane defect inspection method and defect inspection apparatus |
WO2012173232A1 (en) | 2011-06-16 | 2012-12-20 | 三菱レイヨン株式会社 | Hollow fiber membrane module repair method and hollow fiber membrane module |
US20140116935A1 (en) * | 2011-06-16 | 2014-05-01 | Mitsubishi Rayon Co., Ltd. | Hollow fiber membrane module repair method and hollow fiber membrane module |
US10898862B2 (en) | 2011-06-16 | 2021-01-26 | Mitsubishi Chemical Corporation | Hollow fiber membrane module repair method and hollow fiber membrane module |
WO2019202978A1 (en) | 2018-04-18 | 2019-10-24 | 住友電気工業株式会社 | Pressure test method for solar power generation device housing unit |
CN115245746A (en) * | 2021-04-28 | 2022-10-28 | 天津膜天膜科技股份有限公司 | Membrane module aperture optimization method |
CN115245746B (en) * | 2021-04-28 | 2023-08-04 | 天津膜天膜科技股份有限公司 | Membrane module aperture optimization method |
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