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JPH05161827A - Filter unit for fluid discharged from high pressure steam sterilizing device - Google Patents

Filter unit for fluid discharged from high pressure steam sterilizing device

Info

Publication number
JPH05161827A
JPH05161827A JP3352063A JP35206391A JPH05161827A JP H05161827 A JPH05161827 A JP H05161827A JP 3352063 A JP3352063 A JP 3352063A JP 35206391 A JP35206391 A JP 35206391A JP H05161827 A JPH05161827 A JP H05161827A
Authority
JP
Japan
Prior art keywords
filter
hydrophilic
hydrophobic
fluid
discharged
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
JP3352063A
Other languages
Japanese (ja)
Inventor
Osamu Kurisaka
修 栗坂
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.)
Toyo Roshi Kaisha Ltd
Original Assignee
Toyo Roshi Kaisha 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 Toyo Roshi Kaisha Ltd filed Critical Toyo Roshi Kaisha Ltd
Priority to JP3352063A priority Critical patent/JPH05161827A/en
Publication of JPH05161827A publication Critical patent/JPH05161827A/en
Pending legal-status Critical Current

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  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To prevent the contamination of the outside with bacteria by placing a hydrophilic element on the gravity side of a hydrophobic element when a substance having possibility containing microbiological contaminant is passed through a filter consisting of both elements from a high pressure steam sterilizing device. CONSTITUTION:A hydrophobic element 1 and a hydrophilic element 2 are set to the discharge piping routes 17, 18 of a high pressure steam sterilizing device 11 in such a state that the hydrophilic element 2 is positioned on the gravity side with respect to the hydrophobic element 1. When air, steam and condensed water are discharged, air and steam are filtered by the hydrophobic element 1 of a filter element 3 and also filtered by hydrophilic element 2 not wetted with condensed water. After the elements 1, 2 are wholly wetted with condensed water, air and steam are discharged only from the hydrophobic element and condensed water is discharged only from the hydrophilic element. Therefore, air, steam and condensed water can be smoothly discharged.

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、高圧蒸気滅菌器から排
出される、微生物を含んでいる可能性がある流体から微
生物を取り除き、無菌状態にして流体を排出するフィル
タ−組立体に関する。
FIELD OF THE INVENTION The present invention relates to a filter assembly for removing microorganisms from a potentially microbial-containing fluid discharged from a high pressure steam sterilizer to sterilize and discharge the fluid.

【0002】[0002]

【従来技術】従来より高圧蒸気滅菌(オ−トクレ−ブ滅
菌)は滅菌の有効な手段として医薬品工業、食品工業を
中心とする産業分野、及び微生物や細胞等を扱う生化
学、微生物学、遺伝子工学等の研究分野に広範に使われ
ている。近年、遺伝子操作を専門に扱うバイオハザ−ド
施設が各地に設置されているが、これは遺伝子組み替え
の結果作り出される予測出来ない生命体が実験設備の外
に漏出することをあらゆる手段を講じて防止しようとい
う思想からうまれたものである。実験室内は外界より気
圧が下げられ実験室内の空気が外へ流出することを防止
するとともに、室内空気をエア−フィルタ−で濾過滅菌
して、室内外の微生物的空気汚染を防いでいる。その実
験に使用された器具は、目的に応じた滅菌方法で滅菌さ
れて微生物的危険性を排除した後、廃棄または再使用さ
れる。
2. Description of the Related Art Conventionally, high-pressure steam sterilization (autoclave sterilization) has been used as an effective means of sterilization in industrial fields such as the pharmaceutical industry, food industry, and biochemistry, microbiology, and genes dealing with microorganisms and cells. It is widely used in research fields such as engineering. In recent years, bio-hazard facilities specializing in genetic engineering have been installed in various places, but it will take every possible measure to prevent the unpredictable life forms created by genetic recombination from leaking out of the experimental facility. It was born from the idea of trying. The atmospheric pressure in the laboratory is lowered from the outside to prevent the air in the laboratory from flowing out, and the indoor air is filtered and sterilized by an air filter to prevent microbial air pollution inside and outside the room. The instrument used in the experiment is sterilized by a sterilization method according to the purpose to eliminate microbial risk, and then discarded or reused.

【0003】高圧蒸気滅菌法は上記の用途に最も一般的
に使用されるが、滅菌効果を完全なものとするために滅
菌に先だって高圧蒸気滅菌器缶体内の残存空気を缶体外
へ排出し、蒸気に置換する操作が不可欠である。この
際、空気及び蒸気が凝縮水(ドレ−ン)と共に缶体外に
排出される。この排出流体は缶体内の被滅菌物に由来す
る微生物汚染の可能性が存在するため、なんらかの滅菌
措置の必要性が指摘されている。現在、バイオハザ−ド
施設においては、取り扱う生命体の危険性に応じてクラ
ス分けされているが、P−1,P−2レベル等の比較的
危険性が緩やかな施設では特に対策が講じられていない
のが実状であり、P−3,P−4レベル等の高度な生物
学的危険管理施設では安全性の高い微生物汚染管理技術
の確立が望まれている。これまでに排出ドレ−ンを再び
高圧蒸気化して滅菌し、排出するなどの特別の装置を組
み込んだものは一部大型機で見られるが、再蒸気化装置
が大型化することや、イニシャルコストが増大すること
などから小型、中型機への展開は進んでいない。そのた
めに、大型機を含め設置容積が少なく、簡便な方法によ
る排出液体の無菌化技術が待望されている。
The high pressure steam sterilization method is most commonly used for the above-mentioned applications, but in order to complete the sterilization effect, the residual air in the can body of the high pressure steam sterilizer is discharged to the outside of the can body before sterilization. The operation of substituting with steam is essential. At this time, air and steam are discharged out of the can body together with condensed water (drain). It is pointed out that some sort of sterilization is necessary because the discharged fluid has a possibility of microbial contamination derived from the substance to be sterilized in the can. Currently, biohazard facilities are classified into classes according to the risk of living organisms to be handled, but special measures are taken at facilities with relatively moderate risks such as P-1 and P-2 levels. The fact is that there is no such thing, and establishment of a highly safe microbial contamination control technology is desired in advanced biological risk management facilities such as P-3 and P-4 levels. Up to now, some large machines have built-in special equipment to sterilize the exhaust drain by high-pressure steam again and sterilize it, but this is due to the large size of the re-steamer and the initial cost. The expansion to small and medium-sized machines has not progressed due to the increase in the number of vehicles. Therefore, a technique for sterilizing discharged liquid by a simple method with a small installation volume including a large machine is desired.

【0004】高圧蒸気滅菌器による一般的な滅菌サイク
ルについて、図4に基いて説明すると、まず、被滅菌物
を高圧蒸気滅菌器缶体11内に入れた後、缶体11に耐
圧構造を有する蓋14をし滅菌物直下にある水15を電
気ヒ−タ−16により加熱し蒸気を発生させる。そして
滅菌を完全に行う為に缶体11内が飽和蒸気で満たされ
るまで缶体上部にある缶体11と連通する排出配管17
から缶内圧の上昇につれて缶体内の空気を排出させる。
すると缶体の水15が加熱されていくにつれ蒸気が発生
し、空気と蒸気が混在した状況を経てやがて蒸気のみが
排出されるようになる。この際、実際に排出される流体
は空気、蒸気、及び蒸気が排出配管17経路中で冷やさ
れて発生する凝縮水が混在したものとなる。この時点
で、缶体11と排出路17を繋ぐ配管に設置されたバル
ブ13が閉じられ、缶体内の蒸気圧が上がり、所定温
度、所定時間滅菌が行われる。滅菌終了後、ヒ−タ−1
6が切られ缶体内圧が所定の圧力まで下がった時点で、
排出バルブ13が開かれ残圧によって、空気、蒸気、凝
縮水が缶体外に排出される。缶体内が大気圧に戻った時
点で、1サイクルが終了となる。主に産業用に供する大
型の高圧蒸気滅菌器では缶体内の水を電気ヒ−タ−で加
熱する方式でなく、直接缶体内に加圧蒸気を吹き込む方
式が一般的であるが、蒸気発生方法の違いのみでこのサ
イクルは同一である。
A general sterilization cycle using a high-pressure steam sterilizer will be described with reference to FIG. 4. First, the object to be sterilized is put into the can 11 of the high-pressure steam sterilizer, and then the can 11 has a pressure resistant structure. The lid 14 is closed and the water 15 immediately below the sterilized product is heated by an electric heater 16 to generate steam. Then, for complete sterilization, a discharge pipe 17 communicating with the can body 11 located above the can body until the inside of the can body 11 is filled with saturated steam.
The air in the can is discharged as the internal pressure of the can increases.
Then, steam is generated as the water 15 in the can body is heated, and only steam is eventually discharged after a situation in which air and steam are mixed. At this time, the fluid actually discharged is a mixture of air, steam, and condensed water generated by cooling the steam in the discharge pipe 17 path. At this point, the valve 13 installed in the pipe connecting the can body 11 and the discharge path 17 is closed, the vapor pressure in the can body rises, and sterilization is performed at a predetermined temperature for a predetermined time. Heater-1 after sterilization
When 6 is cut and the internal pressure of the can falls to a predetermined pressure,
The discharge valve 13 is opened, and the residual pressure discharges air, steam, and condensed water out of the can body. One cycle is completed when the inside of the can returns to atmospheric pressure. In large-scale high-pressure steam sterilizers mainly used for industrial purposes, it is common to blow pressurized steam directly into the can instead of heating the water in the can with an electric heater. This cycle is the same except for the difference.

【0005】[0005]

【発明が解決しようとする課題】本発明は、上述した滅
菌サイクルの中で、高圧蒸気滅菌器缶体外に排出される
被滅菌物由来の微生物学的汚染物質を含む可能性のある
空気、蒸気、凝縮水を有効に濾過し、外界への微生物汚
染を防止するフィルタ−組立体を提供することにある。
DISCLOSURE OF THE INVENTION The present invention, in the above-mentioned sterilization cycle, has a possibility of containing microbiological contaminants derived from the substance to be sterilized, which is discharged outside the can of the high-pressure steam sterilizer, and steam. SUMMARY OF THE INVENTION It is an object of the present invention to provide a filter assembly that effectively filters condensed water and prevents microbial contamination to the outside.

【0006】即ち、これら排出エキゾ−ストは空気、蒸
気、液体の状態で同一排出配管から混然として排出され
るため、これら全ての状態の流体を効率よく濾過できる
フィルタ−の設定が必要である。フィルタ−には基本的
に疎水性の物と親水性の物があるが、疎水性フィルタ−
をこの用途に供すると空気、蒸気は濾過できるものの、
凝縮水は濾過できず、フィルタ−を収容する濾過器の濾
過1次側(フィルタ−の被濾過液側)に凝縮水が充満し
た時点で空気、蒸気も液体に妨げられ濾過できなくなっ
てしまう。一方親水性フィルタ−をこの用途に供した場
合、フィルタ−が水で濡れていない時は空気、蒸気を濾
過できるが凝縮水でフィルタ−が一度水に濡れると、空
気、水蒸気ともに全く濾過できず、所定のエキゾ−スト
が排出できなくなる。水で濡れた親水性フィルタ−は、
そのフィルタ−が持つ孔径由来のバブルポイント(孔径
を満たす液体を表面張力に抗して気体で押し出す時の気
体圧力値)以上の圧力で濾過しないと気体は濾過できな
いという性質を持っている。
That is, since these exhaust exhausts are exhausted in the same exhaust pipe in the state of air, vapor, and liquid, it is necessary to set a filter capable of efficiently filtering fluids in all of these states. .. There are basically hydrophobic and hydrophilic filters, but hydrophobic filters
Although air and steam can be filtered when this is used for,
The condensed water cannot be filtered, and when the condensed primary water of the filter housing the filter (the filtered liquid side of the filter) is filled with the condensed water, air and steam are also blocked by the liquid and cannot be filtered. On the other hand, when the hydrophilic filter is used for this purpose, air and steam can be filtered when the filter is not wet with water, but once the filter is wet with condensed water, neither air nor steam can be filtered at all. , The predetermined exhaust cannot be discharged. A hydrophilic filter wet with water
The filter has a property that the gas cannot be filtered unless it is filtered at a pressure higher than the bubble point derived from the pore diameter (the gas pressure value when the liquid satisfying the pore diameter is pushed out by the gas against the surface tension).

【0007】なお、微生物の除去には孔径0.2μm以
下のフィルタ−が必要であり、水でフィルタ−を濡らし
た場合のバブルポイント値も概ね3Kg/cm2 以上となる
が、このエキゾ−ストの排出圧力は一般的に0.5Kg/
cm2 以下であるため、一度水に濡れたフィルタ−からは
気体は排出されない。排出配管経路にある缶体内と外界
を画するバルブは缶体内の温度又は圧力を感知するセン
サ−と連動し作動する構造が一般的なため、缶体内の空
気が飽和蒸気と完全に置換しないうちに経路を閉じてし
まい、完全な滅菌が行えない結果となる。
It is to be noted that a filter having a pore size of 0.2 μm or less is required for removing microorganisms, and a bubble point value when the filter is wet with water is about 3 kg / cm 2 or more. The discharge pressure is generally 0.5 kg /
Since it is less than cm 2 , no gas is discharged from the filter once wet with water. The valve that separates the inside of the can from the outside is located in the discharge piping path and generally operates in conjunction with a sensor that detects the temperature or pressure inside the can, so that the air inside the can is not completely replaced with saturated steam. As a result, the path is closed and complete sterilization cannot be performed.

【0008】また、この用途におけるフィルタ−は滅菌
器内の排出配管系に置かれ設置空間が限られるため、形
状をコンパクトにする必要があることと、フィルタ−の
1次側が微生物汚染を受けている可能性があることか
ら、フィルタ−交換時濾過器からフィルタ−エレメント
を入れ替えする作業をなくし、人に対する危険を回避す
るため濾過器とエレメントを一体化し、フィルタ−ユニ
ットごと交換可能なカプセル形状にする必要がある。
Further, since the filter in this application is placed in the discharge piping system in the sterilizer and the installation space is limited, it is necessary to make the shape compact, and the primary side of the filter receives microbial contamination. Since there is a possibility that there is a possibility that there is a possibility that there is a possibility that there is a possibility that there is a replacement of the filter-element from the filter at the time of filter-replacement, to eliminate the danger to humans, the filter-element is integrated, and the filter-unit can be replaced with a capsule shape There is a need to.

【0009】[0009]

【課題を解決するための手段】上記目的を達成するため
本発明は、ハウジンク4に高圧蒸気滅菌器11からの排
出された流体を供給する流体入口5と、供給された流体
が濾過されて排出させる流体出口6を備え、その流体入
口5と流体出口6との間に、疎水性フィルタ−1aを組
み込んだ疎水性エレメント1と、親水性フィルタ−2a
を組み込んだ親水性エレメント2とを、重力側に前記親
水性エレメント2を配置して、相互に中央部に形成した
濾液流路10を介して連通させ、その中央部濾液流路1
0を前記流体出口6に接続させて成るものである。ま
た、前記疎水性フィルタ−1a及び親水性フィルタ−2
aの孔径が0.2μm〜0.01μmの範囲としたもの
である。
To achieve the above object, the present invention provides a fluid inlet 5 for supplying a discharged fluid from a high-pressure steam sterilizer 11 to a housing 4, and a supplied fluid which is filtered and discharged. A hydrophobic element 1 having a fluid outlet 6 for allowing the hydrophobic filter 1a to be incorporated between the fluid inlet 5 and the fluid outlet 6, and a hydrophilic filter-2a.
And the hydrophilic element 2 in which the hydrophilic element 2 is incorporated are made to communicate with each other through the filtrate channel 10 formed in the central portion by disposing the hydrophilic element 2 on the gravity side.
0 is connected to the fluid outlet 6. In addition, the hydrophobic filter-1a and the hydrophilic filter-2
The pore diameter of a is in the range of 0.2 μm to 0.01 μm.

【0010】[0010]

【作用】上記の構成なので、本発明のフィルタ−ユニッ
トは図4に示すように、高圧蒸気滅菌器11に、排出配
管経路17、18に疎水性エレメント1に対して親水性
エレメント2を重力側に位置する状態でセットされる。
高圧蒸気滅菌サイクルの初期では前述したように空気、
水蒸気、凝縮水が排出されるが、本発明によるフィルタ
−ユニットにより、これら諸状態の流体の空気及び水蒸
気は濾過エレメント3の疎水性エレメント1で濾過され
るとともに、まだ凝縮水で濡れていない親水性エレメン
ト2でも濾過され排出される。凝縮水で親水性エレメン
ト2が全て濡れた後は、その空気及び水蒸気は疎水性エ
レメント1のみより排出されることになる。また、凝縮
水は親水性エレメント2によってのみ排出される。この
際、濾過エレメント3が親水性エレメント2のみで形成
されていると、凝縮水でエレメント全てが濡れた時点か
ら空気、水蒸気は全く濾過されなくなり(いわゆるエア
−ロックの状態となり)、流体の流れが停止してしま
う。
With the above construction, the filter unit of the present invention, as shown in FIG. 4, has the high-pressure steam sterilizer 11 and the discharge pipe passages 17 and 18 in which the hydrophilic element 2 is placed on the gravity side with respect to the hydrophobic element 1. It is set in the state of being located at.
At the beginning of the autoclave cycle, as described above, air,
Water vapor and condensed water are discharged, but by the filter unit according to the present invention, air and water vapor of the fluids in these states are filtered by the hydrophobic element 1 of the filtration element 3 and hydrophilic not yet wet with condensed water. The sexual element 2 is also filtered and discharged. After the hydrophilic element 2 is completely wet with the condensed water, the air and water vapor are discharged only from the hydrophobic element 1. Further, the condensed water is discharged only by the hydrophilic element 2. At this time, if the filter element 3 is formed of only the hydrophilic element 2, air and water vapor will not be filtered at all from the time when all the elements are wet with the condensed water (in a so-called air-lock state), and the fluid flow. Will stop.

【0011】濾過エレメント3が疎水性エレメント1の
みで形成されていると、空気、水蒸気は濾過できるもの
の、凝縮水は全く濾過されないため、凝縮水がユニット
内部へ溜まって濾過エレメント3が水没状態となり、こ
の場合も流体の流れが停止してしまう。また、親水性エ
レメント2に対して疎水性エレメント1を重力側に位置
させて使用した場合も、凝縮水が疎水性エレメント1を
水没させた時点から、親水性エレメント2のみで使用し
たのと同一の状況となり、この場合も流体の流れが停止
してしまう。
When the filter element 3 is formed of only the hydrophobic element 1, the air and water vapor can be filtered, but the condensed water is not filtered at all, so the condensed water is accumulated inside the unit and the filter element 3 is submerged. Also in this case, the flow of fluid stops. Further, even when the hydrophobic element 1 is used on the gravity side with respect to the hydrophilic element 2, it is the same as the case where only the hydrophilic element 2 is used from the time when the condensed water submerges the hydrophobic element 1. In this case, the fluid flow also stops.

【0012】[0012]

【実施例】本発明を図の実施例に基づいて説明すると、
図1、図2及び図3に示すように、高圧蒸気滅菌器排出
流体用フィルタ−ユニットは、疎水性エレメント1及び
親水性エレメント2からなる濾過エレメント3とこれを
収納する濾過ハウジング4部分から構成される。濾過エ
レメント3は容積当たりの濾過面積を広く得るために、
フィルタ−を菊花状にプリ−ツし、両端部を液密に封止
した形状を採り、濾過エレメント3の外側を濾過一次側
とし、プリ−ツ状フィルタ−で濾過された液体が中央の
センタ−コアから流出する構造をとっている。濾過エレ
メント3は一方に疎水性フィルタ−1aを組み込んだ疎
水性エレメント1と、親水性フィルタ−2aとを組み込
んだ親水性エレメント2から成り、お互いに中央部に形
成した濾液流路10を介して連通している。この濾過エ
レメント3と、これを収納し、流体の濾液流路10を濾
過エレメント3と連通した流体出口6及び、濾過エレメ
ント3の1次側に濾過流体を供給する流体入口5を有す
る濾過ハウジング4より構成する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described based on the embodiments shown in the drawings.
As shown in FIG. 1, FIG. 2 and FIG. 3, the high pressure steam sterilizer exhaust fluid filter unit comprises a filter element 3 composed of a hydrophobic element 1 and a hydrophilic element 2 and a filter housing 4 part accommodating the filter element 3. To be done. The filtration element 3 has a large filtration area per volume,
The filter is pleated in a chrysanthemum shape, and both ends are liquid-tightly sealed. The outside of the filter element 3 is the primary side of filtration, and the liquid filtered by the pleated filter is at the center of the filter. -It has a structure that flows out from the core. The filtration element 3 is composed of a hydrophobic element 1 incorporating a hydrophobic filter-1a on one side and a hydrophilic element 2 incorporating a hydrophilic filter-2a, and a filtrate channel 10 formed in the center of each other through the hydrophobic element 1. It is in communication. This filtration element 3 and a filtration housing 4 having a fluid outlet 6 that accommodates the filtration element 3 and communicates a filtrate flow path 10 of the fluid with the filtration element 3, and a fluid inlet 5 that supplies the filtration fluid to the primary side of the filtration element 3. It consists of.

【0013】これらに使用される疎水性フィルタ−1a
及び親水性フィルタ−2aの孔径は0.2μm〜0.0
1μmの範囲内にあることが必要である。0.2μmよ
り孔径が大きいと、細菌やウイルス等の微生物が漏れる
危険性があり、0.01μmより孔径が小さいと所定の
濾過量が得られない。孔径を小さく設定するためには、
濾過量を満足させる都合上、濾過エレメントの濾過面積
を増やす必要があるが、疎水性フィルタ−1a及び親水
性フィルタ−2aの濾過面積を増やすと、濾過エレメン
ト3の容積が増大し、設置容積も多く要すためコンパク
トにすることができないので不適当である。また、一般
に存在する微生物の最も小さいものでも0.1μm〜
0.2μmのフィルタ−で除去可能であり、界面活性剤
の共存による微生物除去率の低下や新規微生物の作出を
勘案しても0.01μm以下の孔径は不必要と考えられ
る。
Hydrophobic filter-1a used for these
And the pore size of the hydrophilic filter-2a is 0.2 μm to 0.0
It must be in the range of 1 μm. If the pore diameter is larger than 0.2 μm, microorganisms such as bacteria and viruses may leak, and if the pore diameter is smaller than 0.01 μm, a predetermined filtration amount cannot be obtained. To set a small hole diameter,
In order to satisfy the filtration amount, it is necessary to increase the filtration area of the filtration element. However, if the filtration areas of the hydrophobic filter-1a and the hydrophilic filter-2a are increased, the volume of the filtration element 3 increases and the installation volume also increases. This is unsuitable because it cannot be made compact because it requires a large amount. In addition, even the smallest microorganisms generally present are 0.1 μm
It can be removed with a 0.2 μm filter, and it is considered that a pore size of 0.01 μm or less is unnecessary even if the removal rate of microorganisms due to the coexistence of a surfactant and the production of new microorganisms are taken into consideration.

【0014】疎水性エレメント1のフィルタ−1aの材
質は、シリコン、ポリテトラフルオロエチレン(PTF
E)、ポリビニリデンフロライド(PVDF)、ポリプ
ロピレン(PP)などからなる本質的に疎水性の微多孔
性膜であればどれでも好適に使用可能である。また、本
質的に親水性の材質からなる微多孔性膜てあっても、シ
リコンやPTFEなどの表面撥水化剤によって膜を撥水
化し、疎水性膜とすれば、同様に使用可能である。これ
らのなかでこの用途に特に好適に推奨される材質は、繰
り返しの熱的耐性に優れるPTFE製微多孔性膜であ
る。
The material of the filter-1a of the hydrophobic element 1 is silicon, polytetrafluoroethylene (PTF).
Any essentially hydrophobic microporous membrane made of E), polyvinylidene fluoride (PVDF), polypropylene (PP) or the like can be suitably used. Further, even a microporous film made of an essentially hydrophilic material can be similarly used if it is made hydrophobic by making the film water-repellent by a surface water-repellent agent such as silicon or PTFE. .. Among these, the material particularly preferably recommended for this application is a PTFE microporous membrane which is excellent in repeated thermal resistance.

【0015】親水性エレメント2のフィルタ−2aの材
質は、再生セルロ−ス、ナイロンなどからなる本質的に
親水性の微多孔性膜、または、本質的に疎水性の材質か
らなる微多孔性膜であっても、界面活性剤のコ−ティン
グや化学的表面改質などの親水化措置によって膜を親水
化し親水性膜と成したセルロ−スアセテ−ト、ポリサル
サン、ポリエ−テルサルサン、PVDF、PTFE、P
P製微多孔性膜等がどれでも好適に使用可能である。こ
れら濾過エレメント3の製造方法の一例は、フィルタ−
をプラスチックネットや不織布支持材と共にプリ−ツ
し、アコ−デオン状と成した後、それぞれのフィルタ−
の端部をヒ−トシ−ル等を行い一体化し、円筒状に形成
する。そしてこの中央部に濾液流路10となる円筒の金
網状センタ−コアと、外周に補強の円筒金網状アウトチ
ュ−ブをセットし円筒両端に液密にエンドプレ−ト7、
8を一体化する工程をとる。前記エンドプレ−トは濾液
流路10を確保するため少なくとも両端のうちの一端を
センタ−コア内径部と接合する中央部分について開口さ
せておく必要がある。
The material of the filter-2a of the hydrophilic element 2 is an essentially hydrophilic microporous membrane made of regenerated cellulose or nylon, or a microporous membrane made of an essentially hydrophobic material. However, cellulose acetate, polysarsan, polyethersalsan, PVDF, PTFE, which is made into a hydrophilic film by hydrophilicizing the film by hydrophilic treatment such as coating with a surfactant or chemical surface modification, P
Any P-made microporous membrane or the like can be suitably used. An example of a method of manufacturing these filtration elements 3 is a filter-
Pleated with a plastic net or non-woven fabric support material to form an accordion shape, and then filter each
The end portion of is subjected to heat sealing or the like to be integrated to form a cylindrical shape. A cylindrical wire-mesh center core which serves as the filtrate flow channel 10 is set in the central portion, and a reinforcing cylindrical wire-mesh outtube is set on the outer periphery, and liquid-tight end plates 7 are provided at both ends of the cylinder.
Take the step of integrating 8. In order to secure the filtrate flow channel 10, at least one end of the end plate is required to be open at the central portion where it is joined to the center core inner diameter portion.

【0016】疎水性(又は親水性)エレメント1(又は
2)はエンドキャップの一端を開口したエンドプレ−ト
を用い、濾液流路10が片側のみ開いた構成とする。一
方親水性(又は疎水性)エレメント2(又は1)は、濾
液流路10が両端に開口したエレメントとする。疎水性
エレメント1の濾液流路開口部と親水性エレメント2の
一方の濾液流路開口部を液密に一体化し、共通の濾液流
出口を有する濾過エレメント3を形成する。濾過エレメ
ント3を含むフィルタ−ユニットの製造方法を例示する
と、上記濾過エレメント3の組立体の濾液の液出口3a
を濾過ハウジング4の流体出口6と液密に一体化する。
As the hydrophobic (or hydrophilic) element 1 (or 2), an end plate having one end of the end cap opened is used, and the filtrate flow channel 10 is open only on one side. On the other hand, the hydrophilic (or hydrophobic) element 2 (or 1) is an element in which the filtrate channel 10 is open at both ends. The filtrate passage opening of the hydrophobic element 1 and the filtrate passage opening of one of the hydrophilic elements 2 are liquid-tightly integrated to form a filtration element 3 having a common filtrate outlet. As an example of the method for manufacturing a filter unit including the filtration element 3, the filtrate liquid outlet 3a of the assembly of the filtration element 3 is described.
Is fluid-tightly integrated with the fluid outlet 6 of the filtration housing 4.

【0017】また濾過ハウジング4には流体入口5を有
し、濾過エレメント3の全体を被う外殻部材と濾過ハウ
ジング4を液密一体化することで作成する。また、フィ
ルタ−ユニットは液体の出入口が図2と図3に示すよう
に濾過ハウジング4内の上下に位置する形態にとらわれ
ず、濾過時フィルタ−エレメントの疎水性エレメント1
に対して親水性エレメント2が重力側に位置する態樣を
取る構造であれば、同様に使用可能である。例えばフィ
ルタ−ユニットが図2に示す態樣である場合は、濾液開
口部を一端に設けた親水性エレメント2の開口部と、濾
液開口部を両端に設けた疎水性エレメント1の一端を液
密一体化した濾過エレメント3が用いられる。センタ−
コア、アウトチュ−ブ、エンドプレ−ト、ハウジング部
材は金属、プラスチックいずれも使用可能であるが、P
P、PVDF、ポリカ−ボネ−ト等の耐熱性熱化塑性樹
脂が、高圧蒸気滅菌の排出蒸気に熱耐性があり、かつ製
造時溶着作業がしやすいなど特に好適に使用できる。
The filtration housing 4 has a fluid inlet 5, which is formed by liquid-tightly integrating the outer shell member covering the entire filtration element 3 and the filtration housing 4. Further, the filter unit is not limited to the form in which the inlet and outlet of the liquid are located above and below the inside of the filtration housing 4 as shown in FIGS. 2 and 3, and the hydrophobic element 1 of the filter element during filtration is used.
On the other hand, if the structure is such that the hydrophilic element 2 is positioned on the gravity side, it can be similarly used. For example, when the filter unit is in the state shown in FIG. 2, the opening of the hydrophilic element 2 having the filtrate opening at one end and the end of the hydrophobic element 1 having the filtrate opening at both ends are liquid-tight. An integrated filter element 3 is used. Center
The core, the outtube, the end plate and the housing member can be made of metal or plastic.
A heat-resistant thermoplastic resin such as P, PVDF, polycarbonate, etc. can be particularly preferably used because it has heat resistance to the exhaust steam of high-pressure steam sterilization and the welding work is easy during manufacturing.

【0018】[0018]

【実験例1】親水性フィルタ−2として、ポリエ−テル
サルホン親水化膜(東洋濾紙株式会社製、孔径:0.2
μm)を0.1m2組み込んだ濾過エレメント3と、疎水
性フィルタ−1として、PTFE膜(ジャパン・ゴアテ
ックス株式会社製、孔径:0.2μm)を0.5m2組み
込んだ濾過エレメント3を疎水性エレメント1が上部に
位置するように一体化し、これをPP製の濾過ハウジン
グ4に納めフィルタ−ユニットを作成した。 このフィ
ルタ−ユニットの外形寸法は、径80mm、全長200
mmである。
[Experimental Example 1] As a hydrophilic filter-2, a poly (ether sulfone) hydrophilic membrane (manufactured by Toyo Roshi Kaisha, Ltd., pore size: 0.2)
(μm) is incorporated into the filter element 3 in which 0.1 m 2 is incorporated, and as the hydrophobic filter-1, a filter element 3 in which a PTFE membrane (manufactured by Japan GORE-TEX Co., Ltd., pore diameter: 0.2 μm) is incorporated into 0.5 m 2 is hydrophobic. The element 1 was integrated so as to be located on the upper side, and this was housed in the filtration housing 4 made of PP to form a filter unit. The external dimensions of this filter unit are 80 mm in diameter and 200 in total length.
mm.

【0019】[0019]

【実験例2】親水性のフィルタ−2として、ナイロン膜
(MSI株式会社製、孔径:0.1μm)を0.05m2
組み込んだエレメントと、疎水性フィルタ−1として、
PP膜(宇部興産株式会社製、孔径:0.05μm)を
0.05m2組み込んだ濾過エレメント3を、疎水性エレ
メント1が上部に位置するように一体化し、これをPP
製のハウジングに納めフィルタ−ユニットを作成した。
このフィルタ−ユニットの外形寸法は、径80mm、全
長130mmである。
[Experimental Example 2] As a hydrophilic filter-2, a nylon membrane (manufactured by MSI Co., Ltd., pore size: 0.1 μm) was used in an amount of 0.05 m 2.
As the incorporated element and hydrophobic filter-1,
A filtration element 3 incorporating 0.05 m 2 of a PP membrane (manufactured by Ube Industries, Ltd., pore size: 0.05 μm) was integrated so that the hydrophobic element 1 was located above,
The filter unit was made by putting it in a housing made of steel.
The outer dimensions of this filter unit are 80 mm in diameter and 130 mm in total length.

【0020】[0020]

【実験例3】親水性フィルタ−2として、ポリエリ−テ
ルサルホン親水化膜(東洋濾紙株式会社製、孔径:0.
2μm)を0.1m2組み込んだ濾過エレメント3を作成
した。このフィルタ−ユニットの外形寸法は、径80m
m、全長130mmである。
[Experimental Example 3] As a hydrophilic filter-2, a polyerither-sulfone hydrophilization membrane (manufactured by Toyo Roshi Kaisha, Ltd., pore size: 0.
2 μm) was incorporated to prepare 0.1 m 2 of the filter element 3. The external dimensions of this filter unit are 80m in diameter.
m, total length 130 mm.

【0021】[0021]

【実験例4】疎水性フィルタ−1として、PTFE膜
(ジャパン・ゴアテックス株式会社製、孔径:0.2μ
m)を0.1m2組み込んだ濾過エレメント3のみをPP
製のハウジングに納め、実験例1と同様にフィルタ−ユ
ニットを作成した。このフィルタ−ユニットの外形寸法
は、径80mm、全長130mmである。
[Experimental Example 4] As a hydrophobic filter-1, a PTFE membrane (manufactured by Japan Gore-Tex Co., Ltd., pore size: 0.2 μm)
m) 0.1 m 2 incorporated into the filter element 3 only PP
It was housed in a housing made of the same and a filter unit was prepared in the same manner as in Experimental Example 1. The outer dimensions of this filter unit are 80 mm in diameter and 130 mm in total length.

【0022】[0022]

【実験例5】親水性フィルタ−2として、ポリエ−テル
サルホン親水化膜(東洋濾紙株式会社製、孔径:0.2
μm)を0.05m2組み込んだ濾過エレメント3と、疎
水性フィルタ−1として、PTFE膜(ジャパン・ゴア
テックス株式会社製、孔径:0.2μm)を0.05m2
組み込んだ濾過エレメント3を実験例1と同様に、但し
使用時、疎水性エレメント1が下部に位置するように一
体化し、これをPP製の濾過ハウジング4に納めフィル
タ−ユニットを作成した。このフィルタ−ユニットの外
形寸法は、径80mm、全長130mmである。上記の
5種類のフィルタ−ユニットを、内容量60リットルの
高圧蒸気滅菌機(株式会社平山製作所製)の排出配管末
端部に取り付け試験に供した。この結果を表1及び表2
に示す。表1はフィルタ−ユニットの種類と排出流体量
である。
[Experimental Example 5] As a hydrophilic filter-2, a poly (ether sulfone) hydrophilic membrane (manufactured by Toyo Roshi Kaisha, Ltd., pore size: 0.2)
filter element 3 incorporating 0.05 m 2 ) and a PTFE membrane (manufactured by Japan Gore-Tex Co., Ltd., pore diameter: 0.2 μm) of 0.05 m 2 as the hydrophobic filter-1.
The built-in filter element 3 was integrated in the same manner as in Experimental Example 1, except that the hydrophobic element 1 was located at the bottom when used, and the filter element was housed in the PP filter housing 4 to form a filter unit. The outer dimensions of this filter unit are 80 mm in diameter and 130 mm in total length. The above-mentioned 5 types of filter units were attached to the end portion of the discharge pipe of a high-pressure steam sterilizer (manufactured by Hirayama Seisakusho Co., Ltd.) having an internal capacity of 60 liters and subjected to a test. The results are shown in Table 1 and Table 2.
Shown in. Table 1 shows the types of filter units and the amount of discharged fluid.

【0023】[0023]

【表1】 [Table 1]

【0024】この表1の結果から、実験例3、4、及び
5に於ける滅菌は、実験例1、2、及びフィルタ−なし
の場合に比べ、空気、蒸気、及び凝縮液量が少なく高圧
蒸気滅菌器缶体内が飽和蒸気状態となっていないまま滅
菌がおこなわれている可能性を示唆している。表2は排
出流体の無菌性に関するものである。
From the results shown in Table 1, the sterilization in Experimental Examples 3, 4, and 5 has less amount of air, vapor, and condensate than those in Experimental Examples 1, 2 and no filter, and the high pressure is high. This suggests that sterilization may be performed without the saturated steam state inside the steam sterilizer can. Table 2 relates to the sterility of the exhaust fluid.

【0026】[0026]

【表2】 [Table 2]

【0027】上記表2の排出流体の無菌性は、耐熱性芽
胞形成細菌 Batillus subtilis の乾燥菌体を高圧蒸気
滅菌器缶体内面部やフィルタ−ユニット手前の排出配管
内部に散布し、通常に滅菌操作を行った。フィルタ−ユ
ニット液出口後の配管を液体培地(トリプチケ−スソイ
・ブイヨン培地)液中に入れ、気体を含めた排出流体は
全て液体培地に接触するように配慮した。液体培地が高
温になり、採取した菌体数に影響を与えないよう、培地
量は5リットルとした。排出液のサンプリング終了後、
培地を温度32度で7日間培養し、培地の濁りで菌の有
無を判定した。この表2の結果を見ると、フィルタ−の
設置は排出流体の除菌に有効なことがわかる。
The sterility of the discharged fluid in Table 2 above is determined by spraying dry bacterial cells of the heat-resistant spore-forming bacterium Batillus subtilis onto the inner surface of the can of the high-pressure steam sterilizer and the discharge pipe in front of the filter unit to normally perform sterilization operation. I went. The pipe after the filter unit liquid outlet was put into a liquid medium (triptycease soy broth medium) so that all the discharged fluid including gas came into contact with the liquid medium. The amount of the medium was set to 5 liters so that the temperature of the liquid medium became high and the number of collected bacterial cells was not affected. After sampling the discharged liquid,
The medium was cultivated at a temperature of 32 ° C. for 7 days, and the presence or absence of bacteria was determined by the turbidity of the medium. From the results shown in Table 2, it can be seen that the installation of the filter is effective for sterilizing the discharged fluid.

【0028】[0028]

【発明の効果】以上のように、本発明は、高圧蒸気滅菌
器缶体外に排出される被滅菌物由来の微生物学的汚染物
質を含む可能性のある空気、蒸気、凝縮水を、濾過エレ
メント3が疎水性及び親水性エレメントの両方の特性を
生かし、親水性エレメント2を疎水性エレメント1に対
して重力側に位置させて構成するので、空気、水蒸気、
凝縮水を滞りなく排出することができる。その際、孔径
0.2μm〜0.01μmのフィルタ−を用いることに
よって被滅菌物由来の微生物学的汚染物質を含む空気、
蒸気、凝縮水を完全に濾過して外界へ排出することがで
きる。また、濾過エレメントがコンパクト化されてお
り、装置を小型化し、生物学的に安全且つ簡単に濾過エ
レメントの交換が可能となる。
INDUSTRIAL APPLICABILITY As described above, according to the present invention, the air, steam, and condensed water, which may be discharged from the can of the high-pressure steam sterilizer, may contain microbiological contaminants derived from the substance to be sterilized. 3 utilizes the characteristics of both the hydrophobic and hydrophilic elements, and the hydrophilic element 2 is positioned on the gravity side with respect to the hydrophobic element 1, so that air, water vapor,
Condensed water can be discharged smoothly. At that time, air containing microbiological contaminants derived from the substance to be sterilized by using a filter having a pore size of 0.2 μm to 0.01 μm,
The steam and condensed water can be completely filtered and discharged to the outside. Further, since the filter element is made compact, the device can be downsized, and the filter element can be replaced biologically safely and easily.

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

【図1】本発明の実施例を示し、(イ)が一部切欠面斜
視図、(ロ)が要部である濾過エレメントの部分縦断側
面図。
FIG. 1 shows an embodiment of the present invention, in which (a) is a partial cutaway perspective view and (b) is a partial vertical cross-sectional side view of a filtration element.

【図2】本発明の略図的縦断面図。FIG. 2 is a schematic vertical sectional view of the present invention.

【図3】本発明の略図的縦断面図。FIG. 3 is a schematic vertical sectional view of the present invention.

【図4】高圧蒸気滅菌器の排出流体濾過システムの模式
図。
FIG. 4 is a schematic diagram of an exhaust fluid filtration system of a high pressure steam sterilizer.

【符合の説明】[Explanation of sign]

1 疎水性エレメント 1a 疎水性フィルタ− 2 親水性エレメント 2a 親水性フィルタ− 3 濾過エレメント 4 濾液ハウジング 5 流体入口 6 流体出口 7 エンドプレ−ト 8 エンドプレ−ト 9 接続部 10 濾液流路 11 高圧蒸気滅菌器 12 被滅菌物 13 バルブ 14 高圧蒸気滅菌器蓋 15 水 16 ヒ−タ− 17 流体導入管 18 流体排出管 DESCRIPTION OF SYMBOLS 1 Hydrophobic element 1a Hydrophobic filter-2 Hydrophilic element 2a Hydrophilic filter-3 Filtration element 4 Filtrate housing 5 Fluid inlet 6 Fluid outlet 7 End plate 8 End plate 9 Connection part 10 Filtrate flow path 11 High pressure steam sterilizer 12 Sterilized object 13 Valve 14 High pressure steam sterilizer lid 15 Water 16 Heater 17 Fluid introduction pipe 18 Fluid discharge pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 濾過ハウジンク(4)に高圧蒸気滅菌器
(11)からの排出流体を供給する流体入口(5)と、
その供給された流体が濾過されて排出する流体出口
(6)を備え、その流体入口(5)と流体出口(6)と
の間に、疎水性フィルタ−(1a)を組み込んだ疎水性
エレメント(1)と、親水性フィルタ−(2a)を組み
込んだ親水性エレメント(2)とを、前記親水性エレメ
ント(2)を重力側に配置して、相互に中央部に形成し
た濾液流路(10)を介して連通させ、その中央部濾液
流路(10)を前記流体出口(6)に接続させて成る高
圧蒸気滅菌器排出流体用フィルタ−ユニット。
1. A fluid inlet (5) for supplying an exhaust fluid from a high pressure steam sterilizer (11) to a filter housing (4),
A hydrophobic element (6) having a fluid outlet (6) through which the supplied fluid is filtered and discharged, and incorporating a hydrophobic filter (1a) between the fluid inlet (5) and the fluid outlet (6). 1) and a hydrophilic element (2) incorporating a hydrophilic filter (2a), the hydrophilic element (2) is arranged on the gravity side, and the filtrate channel (10) is formed in the center part of each other. ), The central part filtrate flow path (10) is connected to the fluid outlet (6), the high pressure steam sterilizer discharge fluid filter unit.
【請求項2】 疎水性フィルタ−(1a)及び親水性フ
ィルタ−(2a)の孔径が0.2μm〜0.01μmの
範囲である請求項1の高圧蒸気滅菌器排出流体用フィル
タ−ユニット。
2. The high pressure steam sterilizer exhaust fluid filter unit according to claim 1, wherein the hydrophobic filter (1a) and the hydrophilic filter (2a) have a pore size in the range of 0.2 μm to 0.01 μm.
JP3352063A 1991-12-13 1991-12-13 Filter unit for fluid discharged from high pressure steam sterilizing device Pending JPH05161827A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3352063A JPH05161827A (en) 1991-12-13 1991-12-13 Filter unit for fluid discharged from high pressure steam sterilizing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3352063A JPH05161827A (en) 1991-12-13 1991-12-13 Filter unit for fluid discharged from high pressure steam sterilizing device

Publications (1)

Publication Number Publication Date
JPH05161827A true JPH05161827A (en) 1993-06-29

Family

ID=18421533

Family Applications (1)

Application Number Title Priority Date Filing Date
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Cited By (3)

* Cited by examiner, † Cited by third party
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WO2002043841A3 (en) * 2000-12-01 2003-02-27 Millipore Corp Chemical process system with multi-functional barrier filter
WO2014040669A1 (en) * 2012-09-12 2014-03-20 Sartorius Stedim Biotech Gmbh Combi-filter
JP2016501125A (en) * 2012-12-03 2016-01-18 イー・エム・デイー・ミリポア・コーポレイシヨン Method and apparatus used for double sterile filtration

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002043841A3 (en) * 2000-12-01 2003-02-27 Millipore Corp Chemical process system with multi-functional barrier filter
US6902671B2 (en) 2000-12-01 2005-06-07 Millipore Corporation Chemical process system with multi-functional barrier filter
JP2005329407A (en) * 2000-12-01 2005-12-02 Millipore Corp Chemical process system with multi-functional barrier filter
EP2110168A1 (en) * 2000-12-01 2009-10-21 Millipore Corporation Barrier filter with hydrophilic and hydrophobic membrane parts
WO2014040669A1 (en) * 2012-09-12 2014-03-20 Sartorius Stedim Biotech Gmbh Combi-filter
JP2015528300A (en) * 2012-09-12 2015-09-28 ザトーリウス ステディム ビオテーク ゲーエムベーハー Combined filter
US9963668B2 (en) 2012-09-12 2018-05-08 Sartorius Stedim Biotech Gmbh Combined filter
JP2016501125A (en) * 2012-12-03 2016-01-18 イー・エム・デイー・ミリポア・コーポレイシヨン Method and apparatus used for double sterile filtration
EP2925420A4 (en) * 2012-12-03 2016-09-21 Emd Millipore Corp METHODS AND DEVICES USED FOR REDUNDANT STERILE FILTRATION
US9694304B2 (en) 2012-12-03 2017-07-04 Emd Millipore Corporation Methods and devices used for redundant sterile filtration
US10195544B2 (en) 2012-12-03 2019-02-05 Emd Millipore Corporation Methods and devices used for redundant sterile filtration
EP4029586A1 (en) * 2012-12-03 2022-07-20 EMD Millipore Corporation Methods and devices used for redundant sterile filtration

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