JPS6058530A - Method and apparatus for testing membrane filter - Google Patents

Method and apparatus for testing membrane filter

Info

Publication number
JPS6058530A
JPS6058530A JP16734383A JP16734383A JPS6058530A JP S6058530 A JPS6058530 A JP S6058530A JP 16734383 A JP16734383 A JP 16734383A JP 16734383 A JP16734383 A JP 16734383A JP S6058530 A JPS6058530 A JP S6058530A
Authority
JP
Japan
Prior art keywords
pressure
primary side
membrane filter
filter
gas
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
JP16734383A
Other languages
Japanese (ja)
Other versions
JPH0251135B2 (en
Inventor
Shigemitsu Hirayama
平山 重光
Akio Ikuta
生田 明夫
Isao Sasaki
功 佐々木
Takamichi Akashi
明石 隆道
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.)
Fujisawa Pharmaceutical Co Ltd
Original Assignee
Fujisawa Pharmaceutical Co 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 Fujisawa Pharmaceutical Co Ltd filed Critical Fujisawa Pharmaceutical Co Ltd
Priority to JP16734383A priority Critical patent/JPS6058530A/en
Priority to EP84110712A priority patent/EP0139202B1/en
Priority to DE8484110712T priority patent/DE3477691D1/en
Priority to AT84110712T priority patent/ATE42145T1/en
Publication of JPS6058530A publication Critical patent/JPS6058530A/en
Priority to US07/291,395 priority patent/US4872974A/en
Priority to US07/396,912 priority patent/US5064529A/en
Publication of JPH0251135B2 publication Critical patent/JPH0251135B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
    • G01N15/08Investigating permeability, pore-volume, or surface area of porous materials
    • G01N15/088Investigating volume, surface area, size or distribution of pores; Porosimetry
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
    • G01N15/08Investigating permeability, pore-volume, or surface area of porous materials
    • G01N15/082Investigating permeability by forcing a fluid through a sample

Abstract

PURPOSE:To test completeness of membrane filter readily and accurately, by increasing the pressure on the primary side by a gas, and checking whether the pressure reaches a specified judging value or not after the elapse of a specified time. CONSTITUTION:A two-way valve 29 is opened, a gas is supplied to the primary side of a housing 21 from a gas source 26. The pressure of the primary side is increased when there is no damage or poor mounting in the filter 20. When the pressure on the primary side reaches 2kg/cm<2>, the pressure increase is stopped for a specified time. The pressure is kept constant. After the elapse of a specified time, the pressure increase is restarted. When a specified time is elapsed after the restarting, whether the pressure on the primary side is larger than a specified judging value or not is automatically checked. When the normal state is judged, a normal lamp is turned ON, and a three-way valve 28 is switched- over.

Description

【発明の詳細な説明】 この発明は、メンブランフィルタ(膜濾過2:)の試験
方法および装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for testing a membrane filter (membrane filtration 2:).

メンブランフィルタは、lJどえば、と1川剤ぞの他の
医桑品を製造するざいの無菌濾過工程などで使用される
ものであり、フィルタの完全1!Iをこれを破壊したり
汚染したつづることなく容易に再現性良く試験できる方
法として、ΔS「M、F316−70で標準化されてい
るバルブポイン1−テスト(以下BPTと略J)が広く
用いられている。BPTは、フィルタの線孔を細管とみ
なし、後の表面張力の式(1)で表わされる圧力と濾孔
の最大半径との関係を利用して、圧力を測定することに
より濾孔の最大半径をめる方法ぐあり、従来は第1図に
一示でような装置を使用して次のJζうに行なわれてい
る。すなわち、内部に板状メンブランフィルタ(10)
が装着されたハウジング(11)の−次側に、指示圧力
計(12)を接続づるとともに、ボール弁(13)を協
えIζパイプ(14)を介して空気、窒素、二酸化炭素
などの気体源(15)を接続し、ハウジング(11)の
二次側に気泡検出用のパイプ(1G)を接続して、この
パイプ(16)の先端を容器(17)に入れな水(18
)の中に導いておく。ソL、T、フィルタ(10)を蒸
留水または波源過液などの液体で湿潤させ−C毛■1?
3′現象により線孔を液体で満たし、弁(13)を適当
な間曵に聞き、フィルタの一次側を気体にJ、って徐々
に加圧する。そして、人がハウジングからの液洩れの目
視ヂエツクを行ないながら、;−1カ泪(12)Jjよ
び気泡検出用のバイブ(16)の先端を観察づる。フィ
ルタ(io)の−次側を気体によって加圧すると、圧力
が比較的小さい間は、この圧力と線孔中の液体が平衡を
保ち、液体が線孔からJJI除されることはフ1(%8
1+できるが、圧力が一定の値に達すると、径の人さい
瀘几巾の液体が線孔から二次側にn1除され、気体がこ
れらの濾孔を通って二次側に出てくる。このことは気泡
検出用のバイブ(1G)の先端から気泡が発生すること
によって知ることができ、このどさの圧力をバルブポイ
ント圧(以下BP圧と略す)とする。そして、この圧力
Pと濾孔の最大半径「との間には、次の表面張力の式(
1)で表わされる関係がある。
Membrane filters are used in the sterile filtration process for manufacturing other medical products such as IJDoba and Ichikawa Pharmaceutical, and are the perfect solution for filters. The valve point 1 test (hereinafter abbreviated as BPT), which is standardized in ΔS M, F316-70, is widely used as a method that can easily and reproducibly test I without destroying or contaminating it. BPT treats the pores of the filter as thin tubes, and measures the pressure using the relationship between the pressure expressed by the surface tension equation (1) below and the maximum radius of the pore. There is a method of determining the maximum radius of
An indicating pressure gauge (12) is connected to the next side of the housing (11) in which a ball valve (13) is connected, and gases such as air, nitrogen, carbon dioxide, etc. Connect the air bubble detection pipe (1G) to the secondary side of the housing (11), and place the tip of this pipe (16) into the container (17).
). Wet the L, T, filter (10) with a liquid such as distilled water or filtrate liquid - C hair■1?
The wire hole is filled with liquid by the 3' phenomenon, the valve (13) is turned on at an appropriate interval, and the primary side of the filter is gradually pressurized with gas. Then, while visually checking for liquid leakage from the housing, a person observes the tip of the bubble detection vibrator (16) and the bubble detection vibrator (16). When the downstream side of the filter (io) is pressurized with gas, as long as the pressure is relatively small, this pressure and the liquid in the wire hole will maintain equilibrium, and the liquid will not be removed from the wire hole by JJI. %8
1+ is possible, but when the pressure reaches a certain value, a liquid with a small diameter filter width is divided by n1 from the wire holes to the secondary side, and gas comes out to the secondary side through these filter holes. . This can be known by the generation of bubbles from the tip of the bubble detection vibrator (1G), and this intense pressure is referred to as valve point pressure (hereinafter abbreviated as BP pressure). The following surface tension equation (
There is a relationship expressed by 1).

r =l((2acos θ /−P ) ・・−−・
−(1)ここで、σは表面張ノ〕、θは接触角、kは形
状補正係数である。したがって、上記のようにしてBP
圧を測定することによりフィルタ(10)の濾孔径を知
ることができる。ところが、上記の方法では、バイブ(
16)から気泡が発生するまで人が常に圧力H(12)
およびパイプ(1G)の先端を観察して気泡が発生しI
こときの圧力を読取る必要があり、作業が面倒で、かつ
自動化が困難である。
r = l((2acos θ/-P) ・---・
-(1) where σ is the surface tension, θ is the contact angle, and k is the shape correction coefficient. Therefore, as above, BP
By measuring the pressure, the pore diameter of the filter (10) can be determined. However, with the above method, the vibe (
16) until air bubbles are generated.
And when observing the tip of the pipe (1G), bubbles were generated.
It is necessary to read the pressure of the plant, which is cumbersome and difficult to automate.

また、メンブランフィルタの完全性を自動的P圧の約8
0%の圧ノコをかけたときの二次側への気1本の拡散流
量を測定J゛るものやノイルタの一次側に断続的に圧力
をか(Jてこの圧力の変化を測定づることにより131
〕几に達したことを知るものが提案されている。ところ
が、前者の場合は、フィルタの濾過面積によって試験値
が5°シなり、小形のフィルタでは誤差が大きくなると
いう問題があり、後者の場合は、ハウジングの6滑によ
り測定条件が異なるという問題がある。
In addition, the integrity of the membrane filter is automatically checked at approximately 8% of the P pressure.
Measure the diffusion flow rate of a single gas to the secondary side when applying a pressure saw at 0% Pressure is applied intermittently to the primary side of a pressure saw or noilter (measuring the change in pressure on the pressure saw) by 131
] It has been proposed to know when the temperature has been reached. However, in the former case, there is a problem that the test value deviates by 5 degrees depending on the filtration area of the filter, and the error becomes large with small filters, and in the latter case, there is a problem that the measurement conditions differ due to the 6-slip of the housing. be.

また、いずれの場合も、上記のj、うに微妙4T試験条
件の設定が必要であり、装δが複刹−ぐ高価なものにな
り、メンテノーンスが14・1グ11(−ある、2J、
た、試験自体は自Wt的に行イTわれるが、完全4I+
の良否は測定結果に基いて人が’r’l Ia’i L
 ’、< 4)れ(、■ならない。したがって、このよ
うな従来の装置なわらインラインでの試験装置としてラ
インに組込むことが困難である。
In addition, in any case, it is necessary to set the above-mentioned 4T test conditions, the equipment δ becomes complicated and expensive, and the maintenance cost is 14.1g11(-1, 2J,
In addition, the test itself is conducted independently, but it is completely 4I+
The quality of quality is determined by people based on the measurement results.
',<4) (,■) Therefore, it is difficult to incorporate such a conventional device into a line as an in-line test device.

この発明の目的は、上記の問題を解決し、メンブランフ
ィルタの完全性を容易にかつ正確に試験できる方法と、
この方法を実施りる装置を提供することにある。
The purpose of the present invention is to provide a method for solving the above problems and easily and accurately testing the integrity of a membrane filter;
The object of the present invention is to provide an apparatus for carrying out this method.

この発明の第1のものは、ハウジング内に固定されて液
体で湿潤されたメンブランフィルタの一次側を気体によ
って所定の割合で背圧し、所定時間経過後にメンブラン
フィルタの一次側の圧力が所定の判定IKiに達してい
るか否かを調べることを特徴とするメンブランフィルタ
の試験方法であり、この発明の第2のものは、上記方法
の発明の実施に直接使用する装置であって、この装置は
、ハウジング内に固定されて液体で湿潤されたメンブラ
ンフィルタの一次側に接続される気体源と、この気体に
よるメンブランフィルタの一次側の昇圧速度を所定の値
に保つために気体源とメンブランフィルタの一次側の間
に設(プられるR圧速度設定弁と、メンブランフィルタ
の一次側に設(jられるL「カ51とをMfiえている
ことを特徴とJ−るものである。
A first aspect of the present invention is to backpressure the primary side of a membrane filter fixed in a housing and moistened with liquid with gas at a predetermined rate, and after a predetermined time elapses, the pressure on the primary side of the membrane filter is determined to be a predetermined value. A second aspect of the present invention is a method for testing a membrane filter, which is characterized by checking whether IKi has been reached, and the second aspect of the present invention is an apparatus directly used for carrying out the invention of the above method, which apparatus includes: A gas source is fixed in the housing and connected to the primary side of the membrane filter that is wetted with liquid. It is characterized by having an R pressure speed setting valve installed between the two sides, and an L valve 51 installed on the primary side of the membrane filter.

発明者らは、メンブランフィルタの完全性試験について
研究を重ねた結果、次のようなjJi実を見出し、この
発明を完成した。づな4つら、液体で湿潤された欠陥の
ないフィルタの一次側を気体によって所定の割合で昇圧
した場合、−次側がBP圧に到達したのらは、−次側か
らの気体の供給量と二次側への気体のJJI出量が平衡
を保ち、−次側の圧力が一定にtff JSJされる1
、この場合、欠陥のないフィルタの一次側が131つ汀
に達J゛るj、での時間は、この〕、rルクσ月31〕
ハど昇圧速度によって決まる(Jぼ一定のものであり、
したがって、これより長い所定時間経過後に一次側の圧
力が所定の判定値に達しているか否かを調べることによ
ってフィルタの完全性を容易にかつ正確に試験すること
ができる。そして、従来のBPTの結果との間に測定値
の誤差がなく、フィルタの完全性を定m的に判断できる
ことが実験により確かめられている。なお、上記の判定
は、所定時間経過後に人が圧力h1を見て行なってもよ
い。また、所定時間経過するまで一次側の圧力を記録計
に記録して人がこれを見て判定づ′るようにしてもよい
し、所定時間経過後に装置で自動的に判定するようにし
てもよい。
As a result of repeated research on the integrity test of membrane filters, the inventors discovered the following fact and completed this invention. In other words, when the pressure on the primary side of a defect-free filter moistened with liquid is increased with gas at a predetermined rate, the reason why the - downstream side reaches BP pressure is due to the amount of gas supplied from the - downstream side. The JJI output of gas to the next side is balanced, and the pressure on the -next side is kept constant tff JSJ1
, in this case, the time it takes for the primary side of the defect-free filter to reach 131 points is 31 months)
It is determined by the pressure increase rate (J is constant,
Therefore, the integrity of the filter can be easily and accurately tested by checking whether the pressure on the primary side has reached a predetermined determination value after a longer predetermined time has elapsed. It has been confirmed through experiments that there is no error in the measured values compared to the results of conventional BPT, and that the integrity of the filter can be determined reliably. Note that the above determination may be made by a person looking at the pressure h1 after a predetermined period of time has elapsed. In addition, the pressure on the primary side may be recorded on a recorder until a predetermined time has elapsed so that a person can make a judgment by looking at this, or the device may automatically make a judgment after a predetermined time has elapsed. good.

この発明の方法によれば、ハウジング内に固定されて液
体で湿潤されたメンブランフィルタの一次側を気体によ
って所定の割合′c昇圧し、所定時間経過後にメンブラ
ンフィルタの一次側の圧力が所定の判定値に達している
か否かをHl、′]べるだけでよいから、必ずしもが圧
中に一次側の圧力を監視する必要がなく、メンブランフ
ィルタの完全性試験を容易にかつ正確に行なうことがで
きる。7iなわち、上記の判定を人が行なう場合でも、
従来のように常に圧力31J3よび気泡検出用のパイプ
の先端を観察している必要かな(、作業が非常に楽にな
る。また、上記の判定を装置で自動的に行なう場合でも
、所定時間経過後の圧ツノを所定の判定値と比較するだ
りで・よいから、装置の栴成とくに試験の自動詞911
ヤ)判定を行なう部分の電子回路のイ^1成が非常に簡
単なものになる。さらに、ハウシングの一次側に気体源
と圧力計を接続づるだ()でJζく、従来のように二次
側に気泡検出用のパイプを接続する必要もないから、イ
ンラインでの試験が容易になる。また、この発明による
装置は、気体源と、Fi圧速度設定弁と、圧力計とを備
えた簡単なものであり、上記のようにその電子回路も非
常に簡単なものになるから、安価に製作i」能であって
メンテナンスも容易であり、しかもインラインでの自動
試験装置としてラインに組込むことも容易である。
According to the method of the present invention, the pressure on the primary side of a membrane filter fixed in a housing and moistened with liquid is increased by a predetermined ratio 'c with gas, and after a predetermined period of time, the pressure on the primary side of the membrane filter reaches a predetermined determination. Since it is only necessary to check whether the value has been reached, it is not necessary to monitor the primary side pressure during pressurization, and the integrity test of the membrane filter can be performed easily and accurately. can. 7i, that is, even if the above judgment is made by a person,
Is it necessary to constantly observe the pressure 31J3 and the tip of the pipe for air bubble detection as in the past? (It makes the work much easier.Also, even if the above judgment is automatically made by the device, it is necessary to constantly observe the pressure 31J3 and the tip of the pipe for bubble detection.) It is possible to compare the pressure point of the device with a predetermined judgment value, so it is possible to compare the pressure point of the device with a predetermined judgment value.
(b) The configuration of the electronic circuit that performs the determination becomes extremely simple. Furthermore, since the gas source and pressure gauge are connected to the primary side of the housing, there is no need to connect a pipe for bubble detection to the secondary side, unlike conventional methods, making in-line testing easier. Become. In addition, the device according to the present invention is simple, comprising a gas source, an Fi pressure speed setting valve, and a pressure gauge, and as described above, its electronic circuit is also very simple, so it is inexpensive. It is easy to manufacture, easy to maintain, and easy to incorporate into a line as an in-line automatic test device.

メンブランフィルタの一次側を背圧していく場合、メン
ブランフィルタの一次側の圧力が上記判定値J:り小さ
い所定の圧力に)ヱしたどきに所定時間だcJ芹圧を停
止し、この間にメンブランフィルタの一次側の圧力が減
少づるか否かを調べるのが望ましい。このようにづれば
、ハウジングや配管のシール不良およびフィルタの湿潤
不良などをチェックすることができる。
When applying back pressure to the primary side of the membrane filter, when the pressure on the primary side of the membrane filter reaches a predetermined pressure that is smaller than the above-mentioned judgment value J), the pressure is stopped for a predetermined period of time, and during this time the membrane filter is It is desirable to check whether or not the pressure on the primary side decreases. In this way, it is possible to check for poor sealing of the housing or piping, poor wetting of the filter, etc.

以下第2図〜第5図を参照してこの発明の詳細な説明す
る。
The present invention will be described in detail below with reference to FIGS. 2 to 5.

第2図はラインに引込よれていないAノラインでの試験
装置を示してJ3す、この装置は、次のように、内部に
カートリッジ状メンブランフィルタ(20)が装着され
たハウジング(21)の−次側に接続されている。1な
わち、ハウジング<21)の−次側に十字継手(22)
の一端部か接続され、継手(22)の他の2つの端部に
指示圧力計(23)ど歪ゲージなどを使用したLL力検
出器(圧力it) (24)が接続されCいる。柑°手
(22)の残りの端部にバイブ(25)を介し゛(気体
源(2G)が接続され、このバイゾ(2!i)には、気
体源(26)側から順に、ニードル弁を使用した昇圧速
度設定弁(27) 、E1万切換電磁弁(三方弁)(2
8)および三方電磁弁(三方弁)(29)が設けちれて
いる。そして、三方弁(28)の1つのボートは大気に
開放されている。圧力検出器(24)、三方弁(28)
および二方弁(29)は制御回路(30)に接続され、
制御回路(30)には自動記録1i131)が接続され
ている。
Fig. 2 shows the test equipment on the A-no-line which is not drawn into the line. Connected to the next side. 1, that is, the cross joint (22) on the negative side of the housing <21)
One end of the joint (22) is connected, and an LL force detector (pressure it) (24) using an indicating pressure gauge (23), strain gauge, etc. is connected to the other two ends of the joint (22). A gas source (2G) is connected to the remaining end of the hand (22) via a vibrator (25), and a needle valve is connected to the vibrator (2!i) in order from the gas source (26) side. Boosting speed setting valve (27) using E10,000 switching solenoid valve (three-way valve) (27)
8) and a three-way solenoid valve (three-way valve) (29). One boat of the three-way valve (28) is open to the atmosphere. Pressure detector (24), three-way valve (28)
and the two-way valve (29) is connected to the control circuit (30),
An automatic recorder 1i131) is connected to the control circuit (30).

次に、濾孔径0.2μ■1のメンブランフィルタの完全
性試験を行なう場合を例にとって、上記の試験装置の動
作を説明する。なお、セルロースエステル、ナイロン6
−6またはポリビニリデンフルオリドなどの親水性のメ
ンブランフィルタの場合、線孔径0.2μmの欠陥のな
いもののBP圧は約3 、5 kg/ an’ Tニー
 アル。
Next, the operation of the above-mentioned test apparatus will be explained by taking as an example a case where a membrane filter having a pore diameter of 0.2 μm is tested for integrity. In addition, cellulose ester, nylon 6
In the case of a hydrophilic membrane filter such as -6 or polyvinylidene fluoride, the BP pressure is approximately 3.5 kg/an' T ne al.

試験開始前には、二方弁(29)は閉じ、三方弁(28
)は設定弁(27ン側から三方弁(29)側に気体が流
れるように切換えられている。そして、試験に先立ち、
所定の讐圧速度が得られるように、人が設定弁(27)
を一定の開度に問いておく。なお、この場合は、1秒に
つき0.1にΩ/傭′の割合で昇圧づる。J、た、液体
で湿潤させたフィルタ(20)をハウジング(21)に
装ftしてd5 <。
Before starting the test, the two-way valve (29) is closed and the three-way valve (28) is closed.
) is switched so that gas flows from the setting valve (27 side) to the three-way valve (29) side.
A person manually adjusts the setting valve (27) to obtain a predetermined pressure speed.
to a certain degree of opening. In this case, the voltage is increased at a rate of 0.1 Ω/min' per second. J. The filter (20) moistened with liquid is mounted in the housing (21) and d5<.

このような状態で始動スイッチを押すことにより、次の
Jζうに自動的に試験が行イrゎれ、試験途中に検出器
(24)にJ、り連続的に検出されるハウジング(21
)の−次側の圧力が第3図〜第5図に示ずように記録:
z3oに記録される。
By pressing the start switch in this state, the next test will be automatically started, and during the test, the housing (21) will be continuously detected by the detector (24).
) is recorded as shown in Figures 3 to 5:
Recorded in z3o.

なお、第3図〜第5図にJ5いて、横軸は時間(sec
 )を、縦1IIIIIはハウジング(21)の−次側
の圧力(kg/cm゛)を表、F)シている。
Note that J5 is shown in Figures 3 to 5, and the horizontal axis is time (sec
), vertical line 1III indicates the pressure (kg/cm') on the negative side of the housing (21), F).

始動スイッチを押ずと、まず、二方弁(29)が開かれ
て、気体源(26)からハウジング(21)の−次側に
気体が供給され、フィルタ(20)の破損や装着不良な
どがない場合は、−次側の圧力は第3図J3よび第4図
に直線(a )で示すように上記の割合で上F? ’J
る。そして、−次側の圧ツノが2k(1/Cjn’に達
したならば、一定時間([2=20S(IC)ti7圧
が停止される。ハウジング(21)や配管のシール不良
またはフィルタ(20)の湿潤不良などがある場合、昇
圧を停止している間に一次側の圧ノE 71’ 2 k
(]/ C111’から減少するので、警報が発註られ
、試験が中断される。このJ:うな異常がない揚台(ユ
、−次側の圧ノコは第3図おJζび第4図に直線(b)
で示づ゛ように一定に維持され、上記時間(t2)が経
過したのら昇圧が再開される。そして、響圧再聞後一定
時間(t 3=60sec )経過したときに、−次側
の圧力が所定の判定値(3kg/ C1n’、 )より
大きいか否かが自動的に調べられる。
If the start switch is not pressed, the two-way valve (29) is first opened and gas is supplied from the gas source (26) to the next side of the housing (21), causing damage to the filter (20) or improper installation. If there is no pressure, the pressure on the negative side will increase at the above rate as shown by the straight line (a) in Figure 3 J3 and Figure 4. 'J
Ru. Then, when the pressure horn on the negative side reaches 2k (1/Cjn'), the pressure is stopped for a certain period of time ([2=20S(IC)ti7 pressure. 20) If there is a moisture problem, check the primary side pressure while stopping the pressure increase.
(]/ Since it decreases from C111', an alarm is issued and the test is interrupted. straight line (b)
The pressure is maintained constant as shown by , and the pressure increase is resumed after the above-mentioned time (t2) has elapsed. Then, when a certain period of time (t3=60 sec) has elapsed after the acoustic pressure re-listening, it is automatically checked whether the pressure on the -next side is greater than a predetermined determination value (3 kg/C1n', ).

線孔径0.2μmの欠陥のないフィルタの場合、昇圧再
開後の一次側の圧力1.J、 、第3図に直線(C)で
示Jように上記の1.1j合でl:、 ’t7− L/
、13]〕圧(3、51tg10n’ )に達しICの
45は同図に直線(d )で示すように一定に賄持され
る。そして、背圧再開後上記時間([3)が経過したど
きの圧力(3、5kg/ [111’ )は判定値(3
kQ/ an’ )より大ぎいので、正常であると判定
され、正常ランプが点灯したのち、巳ブノ弁(28)が
切換えられて1ハウジンク(21)の−次側の空気かこ
の弁(28)から大気にIJI出され、試験が終了りる
In the case of a defect-free filter with a pore diameter of 0.2 μm, the pressure on the primary side after restarting pressure increase is 1. J, , As shown by the straight line (C) in Figure 3, in the above 1.1j case l:, 't7- L/
, 13]] pressure (3, 51tg10n') is reached, and the IC 45 is held constant as shown by the straight line (d) in the figure. Then, the pressure (3.5 kg/[111') at the time when the above time ([3) has elapsed after the back pressure was resumed is the judgment value (3
Since it is larger than kQ/an'), it is determined to be normal, and after the normal lamp lights up, the swivel valve (28) is switched and the air valve (28) on the next side of the 1st housing (21) is switched on. ) is released into the atmosphere, and the test ends.

フィルタの罐孔径が0.2μIllより人さい場合たと
えば誤って浦孔径0.<5μmのフィルタが装着された
場合IJ、4圧再聞後の一次側の圧ツノは、第4図に直
線(eat”承りように上記の割合で上界し、BP圧(
2,4kg/an’)に達したのらは同図に直線(f)
で示すJ:うに一定に維持される。そして、背圧再開後
上記時間(t3)が経過したときの圧力(2,4ko/
(2)f)は判定値(3kg/cn’ )より小さいの
で、異常であると判定され、警報がざtI!られたのら
、異常内容を明確にするためにざらに一定時間(t4=
=/IQsec)圧ツノが維持され、上記同様に一次側
の気体がIJI出されて、試験が終了する。
If the pore diameter of the filter is smaller than 0.2 μIll, for example, the pore diameter may be mistakenly set to 0.2 μIll. When a <5 μm filter is installed, the pressure horn on the primary side after re-listening to IJ and 4 pressures is shown in Figure 4 as a straight line.
The line that reached 2.4 kg/an') is a straight line (f) in the same figure.
Indicated by J: Sea urchins are maintained constant. Then, the pressure (2.4ko/
(2) Since f) is smaller than the judgment value (3 kg/cn'), it is determined that there is an abnormality, and an alarm is issued! After a certain period of time (t4=
=/IQsec) The pressure angle is maintained, the primary side gas is discharged at IJI in the same manner as above, and the test is completed.

フィルタの破損や装着不良があるような場合は、最初に
r?圧を始めたのらの一次側の圧力は、第5図に曲線(
g)で示づように上り?シ、臂圧間始後一定時間(t 
1 =40sec )経過しても2k<1/cm2に)
ヱしないので、異常であると判定される。そして、警報
が発せられたのら、上記同様に一次側の気体が171出
dれ、試験が終了する。
If the filter is damaged or improperly installed, first check the r? The pressure on the primary side after the pressure starts is shown in Figure 5 by the curve (
Upward as shown in g)? A certain period of time (t
1 = 40sec) 2k<1/cm2 even after passing)
Since there is no error, it is determined that there is an abnormality. Then, when the alarm is issued, 171 gases are discharged from the primary side in the same manner as above, and the test is completed.

上記実施例の装置d3 、Lび方法は、オフラインでの
試験を行なうものであるが、上記のJζうな装置をライ
ンに組込んでインラインでの試験を行なうようにするこ
とももらろん可能である。
Although the device d3 and the L-bi method in the above embodiment are for performing an offline test, it is of course possible to incorporate a device like the above Jζ into the line to perform an in-line test. be.

υ゛なわら、現在各工場で行なわれている1!I(α1
濾過システムにおいて、圧力検出器だりを無菌室内のラ
インに組込んでおくことにより、インラインでの試験を
無菌状態で自動的に行な・うことができる。この場合、
工場全体の試験結果を1箇所で集中的に監視したり記録
したりり゛ることb可能である。J、た、たとえば、洗
瓶別件上水の最II適用フィルタまたは蒸留水タンクの
エアベントフィルタなど長til1間にわたつで何回し
使用される複数のフィルタのハウジングの一次側に圧力
検出器を組込んで装置の他の部分はこれらのノイルタで
共用りるようにしてJ3りば、ラインを分解することな
く、定期的な試験を短時間で自動的に行なうことができ
る。
υ゛However, 1! which is currently being carried out at each factory! I(α1
In a filtration system, by incorporating a pressure detector into the line in a sterile room, in-line tests can be automatically performed under sterile conditions. in this case,
It is possible to centrally monitor and record test results for the entire factory in one location. For example, a pressure sensor is installed on the primary side of the housing of multiple filters that are used many times over a long period of time, such as the most applicable filter for clean water for washing bottles or the air vent filter for distilled water tanks. By sharing other parts of the equipment with these noilers, periodic tests can be automatically performed in a short period of time without disassembling the line.

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

第1図はバルブポイントデストを行なうための従来の装
置を示す管系紡口、第2図〜第5図はこの発明の実施例
を示し、第2図は試験装置の管系紡口、第3図〜第5図
は試験結果の3つの例をそれぞれ示すグラフである。 (20)・・・メンブランフィルタ、(21)・・・ハ
ウジング、(23)・・・指示圧力J1、(24)・・
・圧力検出器(圧力側)、(26)・・・気体源、(2
7)・・・背圧速度設定弁。 以 上 第1図 2
Fig. 1 shows a pipe spindle of a conventional device for performing valve point dest; Figs. 2 to 5 show embodiments of the present invention; 3 to 5 are graphs showing three examples of test results, respectively. (20)...Membrane filter, (21)...Housing, (23)...Indicated pressure J1, (24)...
・Pressure detector (pressure side), (26)... gas source, (2
7)...Back pressure speed setting valve. Above Figure 1 2

Claims (3)

【特許請求の範囲】[Claims] (1) ハウジング内に固定されて液体で湿潤されたメ
ンブランフィルタの一次側を気体によって所定の割合で
昇圧し、所定時間経過後にメンブランフィルタの一次側
の圧力が所定の判定値に達しているか否かを調べること
を特徴とするメンブランフィルタの試験方法。
(1) Pressurize the primary side of the membrane filter, which is fixed in the housing and moistened with liquid, at a predetermined rate with gas, and check whether the pressure on the primary side of the membrane filter reaches a predetermined judgment value after a predetermined time has elapsed. A method for testing membrane filters, which is characterized by examining whether
(2) メンブランフィルタの一次側の圧力が上記判定
値J:り小さい所定の圧力に達したときに所定時間だi
プ昇圧を停止し、この間にメンブランフィルタの一次側
の圧ツノが減少するか否かを調べることを特徴とする特
許請求の範囲第1項1す片のプリ1ラシフイル今の試助
方法。
(2) When the pressure on the primary side of the membrane filter reaches a predetermined pressure that is smaller than the above-mentioned judgment value J, the predetermined time has elapsed.
1. A method for testing a pre-1 filter as claimed in claim 1, characterized in that the pressure increase is stopped, and during this period, it is checked whether or not the pressure peak on the primary side of the membrane filter decreases.
(3) ハウジング内に固定されて液体で湿潤されたメ
ンブランフィルタの一次側に接続される気体源と、この
気体によるメンブランフィルタの一次側の4圧速度を所
定の伯に保つために気体源とメンブランフィルタの一次
側の間に設()られる昇圧速Ilf設定弁ど、メンブラ
ンフィルタの一次側に設りられる圧力81とを備えてい
ることを特徴どJ゛るメンブランフィルタの試験K W
l。
(3) A gas source connected to the primary side of the membrane filter that is fixed in the housing and moistened with liquid, and a gas source that is used to maintain the four-pressure velocity of the primary side of the membrane filter using this gas at a predetermined level. Test K W of a membrane filter characterized by having a pressure increase rate Ilf setting valve installed between the primary side of the membrane filter, and a pressure 81 installed on the primary side of the membrane filter.
l.
JP16734383A 1983-09-09 1983-09-09 Method and apparatus for testing membrane filter Granted JPS6058530A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP16734383A JPS6058530A (en) 1983-09-09 1983-09-09 Method and apparatus for testing membrane filter
EP84110712A EP0139202B1 (en) 1983-09-09 1984-09-07 Apparatus for testing membrane filters, and apparatus for sterilizing liquids with use of membrane filter
DE8484110712T DE3477691D1 (en) 1983-09-09 1984-09-07 Apparatus for testing membrane filters, and apparatus for sterilizing liquids with use of membrane filter
AT84110712T ATE42145T1 (en) 1983-09-09 1984-09-07 DEVICE FOR TESTING FILTER MEMBRANES, AND DEVICE FOR STERILIZING LIQUIDS BY MEANS OF A FILTER MEMBRANE.
US07/291,395 US4872974A (en) 1983-09-09 1988-12-27 Apparatus for testing membrane filters, and for sterilizing liquids with use of membrane filter
US07/396,912 US5064529A (en) 1983-09-09 1989-08-22 Apparatus for testing membrane filters

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16734383A JPS6058530A (en) 1983-09-09 1983-09-09 Method and apparatus for testing membrane filter

Publications (2)

Publication Number Publication Date
JPS6058530A true JPS6058530A (en) 1985-04-04
JPH0251135B2 JPH0251135B2 (en) 1990-11-06

Family

ID=15847965

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16734383A Granted JPS6058530A (en) 1983-09-09 1983-09-09 Method and apparatus for testing membrane filter

Country Status (1)

Country Link
JP (1) JPS6058530A (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63199053U (en) * 1987-06-13 1988-12-21
WO2001036074A1 (en) * 1999-11-18 2001-05-25 Zenon Environmental Inc. Immersed membrane element and module
KR20010054415A (en) * 1999-12-06 2001-07-02 박종섭 Device tu check the filter codition
WO2004086008A1 (en) * 2003-03-24 2004-10-07 Ngk Insulators Ltd. Method for measuring pore size of porous filter material
KR100569943B1 (en) * 1999-01-19 2006-04-10 현대자동차주식회사 Air filter testing device
KR100621610B1 (en) * 1999-05-10 2006-09-06 삼성전자주식회사 A simulation apparatus for filter test
JP2008209397A (en) * 2006-11-14 2008-09-11 Millipore Corp Rapid integrity testing for porous material
JP2008253888A (en) * 2007-04-02 2008-10-23 Metawater Co Ltd Membrane damage detecting method
JP2008298291A (en) * 2008-07-14 2008-12-11 Mitsubishi Motors Corp Right and left driving force distribution device
JP2012107930A (en) * 2010-11-16 2012-06-07 Fuirutetsuku Kk Integrity test method for membrane filter
WO2018179959A1 (en) * 2017-03-30 2018-10-04 日本碍子株式会社 Test method for separation membrane structure, manufacturing method for separation membrane module, and manufacturing method for separation membrane structure
US10617603B2 (en) 2016-01-22 2020-04-14 Baxter International Inc. Sterile solutions product bag
US11021275B2 (en) 2016-01-22 2021-06-01 Baxter International Inc. Method and machine for producing sterile solution product bags

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63199053U (en) * 1987-06-13 1988-12-21
KR100569943B1 (en) * 1999-01-19 2006-04-10 현대자동차주식회사 Air filter testing device
KR100621610B1 (en) * 1999-05-10 2006-09-06 삼성전자주식회사 A simulation apparatus for filter test
WO2001036074A1 (en) * 1999-11-18 2001-05-25 Zenon Environmental Inc. Immersed membrane element and module
KR20010054415A (en) * 1999-12-06 2001-07-02 박종섭 Device tu check the filter codition
WO2004086008A1 (en) * 2003-03-24 2004-10-07 Ngk Insulators Ltd. Method for measuring pore size of porous filter material
JP2008209397A (en) * 2006-11-14 2008-09-11 Millipore Corp Rapid integrity testing for porous material
JP2008253888A (en) * 2007-04-02 2008-10-23 Metawater Co Ltd Membrane damage detecting method
JP2008298291A (en) * 2008-07-14 2008-12-11 Mitsubishi Motors Corp Right and left driving force distribution device
JP2012107930A (en) * 2010-11-16 2012-06-07 Fuirutetsuku Kk Integrity test method for membrane filter
US10617603B2 (en) 2016-01-22 2020-04-14 Baxter International Inc. Sterile solutions product bag
US11021275B2 (en) 2016-01-22 2021-06-01 Baxter International Inc. Method and machine for producing sterile solution product bags
US11564867B2 (en) 2016-01-22 2023-01-31 Baxter International Inc. Sterile solutions product bag
US11623773B2 (en) 2016-01-22 2023-04-11 Baxter International Inc. Method and machine for producing sterile solution product bags
WO2018179959A1 (en) * 2017-03-30 2018-10-04 日本碍子株式会社 Test method for separation membrane structure, manufacturing method for separation membrane module, and manufacturing method for separation membrane structure
CN110430935A (en) * 2017-03-30 2019-11-08 日本碍子株式会社 Separate the inspection method, the manufacturing method of separating film module and the manufacturing method for separating film structure of film structure
JPWO2018179959A1 (en) * 2017-03-30 2020-02-06 日本碍子株式会社 Method for inspecting separation membrane structure, method for manufacturing separation membrane module, and method for manufacturing separation membrane structure
CN110430935B (en) * 2017-03-30 2022-04-29 日本碍子株式会社 Method for inspecting separation membrane structure, method for manufacturing separation membrane module, and method for manufacturing separation membrane structure
US11402314B2 (en) 2017-03-30 2022-08-02 Ngk Insulators, Ltd. Method for inspecting separation membrane structure, method for manufacturing separation membrane module, and method for manufacturing separation membrane structure

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