JP2696462B2 - Sterilizing gas supply device for gas sterilizer - Google Patents

Sterilizing gas supply device for gas sterilizer

Info

Publication number
JP2696462B2
JP2696462B2 JP4280677A JP28067792A JP2696462B2 JP 2696462 B2 JP2696462 B2 JP 2696462B2 JP 4280677 A JP4280677 A JP 4280677A JP 28067792 A JP28067792 A JP 28067792A JP 2696462 B2 JP2696462 B2 JP 2696462B2
Authority
JP
Japan
Prior art keywords
gas
pipe
release
liquefied
recovery
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.)
Expired - Lifetime
Application number
JP4280677A
Other languages
Japanese (ja)
Other versions
JPH06105891A (en
Inventor
隆男 笹山
邦春 高見
Original Assignee
大同ほくさん株式会社
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 大同ほくさん株式会社 filed Critical 大同ほくさん株式会社
Priority to JP4280677A priority Critical patent/JP2696462B2/en
Publication of JPH06105891A publication Critical patent/JPH06105891A/en
Application granted granted Critical
Publication of JP2696462B2 publication Critical patent/JP2696462B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Apparatus For Disinfection Or Sterilisation (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、充填容器から受入れ
た酸化エチレン滅菌ガスを、滅菌に適当な圧力、温度に
氣化調整して滅菌器に送入するために使用される滅菌ガ
ス供給装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sterilizing gas supply apparatus used for vaporizing ethylene oxide sterilizing gas received from a filling container to a proper pressure and temperature for sterilization and sending the gas to a sterilizer. It is about.

【0002】[0002]

【従来の技術】酸化エチレン滅菌ガスの薬効成分である
酸化エチレンは、生菌、芽胞を含め各種菌に対する強い
殺菌力、浸透力を有するもので、その簡便性、確実性、
非湿潤性などから医療具製造産業用及び病院医療機関の
自家滅菌用等の分野に広く用いられている。
2. Description of the Related Art Ethylene oxide, which is a medicinal component of ethylene oxide sterilizing gas, has a strong bactericidal and penetrating power against various bacteria including viable bacteria and spores.
Because of its non-wetting properties, it is widely used in the medical device manufacturing industry and in the field of self-sterilization of hospital medical institutions.

【0003】この酸化エチレンガスは可燃性と毒性を有
するが、その可燃性については、不燃性液化ガスとの混
合稀釈により性質の緩和が図られている。例えば、フロ
ン12(又はフロン11,12)の混合による「フロン
系酸化エチレン滅菌ガス」は、その容器充填圧力が低い
(常温で10kg/cm2 未満)ことから、自家用滅菌
器の分野で多く用いられ、炭酸ガス混合による「炭酸ガ
ス系酸化エチレン滅菌ガス」は、容器充填圧力が高いな
がら低コストであるため主に産業用滅菌器の分野で多用
されて来た。しかしながら、最近のフロン規制によって
「フロン系酸化エチレン滅菌ガス」の使用が制限され、
後述の「封袋型滅菌器」を多用する自家滅菌の分野で、
高充填圧力(例えば、30℃ 酸化エチレン10%(w
t)、炭酸ガス90%(wt)のガスの充填圧力は65
kg/cm2 )の「炭酸ガス系」へ切替が必要となって
いる。
[0003] This ethylene oxide gas is flammable and toxic, but its flammability is mitigated by dilution with a nonflammable liquefied gas. For example, “Freon-based ethylene oxide sterilizing gas” obtained by mixing Freon 12 (or Freon 11, 12) is frequently used in the field of private sterilizers because of its low container filling pressure (less than 10 kg / cm 2 at room temperature). In addition, "carbon dioxide-based ethylene oxide sterilizing gas" obtained by mixing carbon dioxide has been widely used mainly in the field of industrial sterilizers because of its low pressure and high container filling pressure. However, the use of "Freon-based ethylene oxide sterilizing gas" has been restricted by recent Freon regulations,
In the field of self-sterilization that frequently uses the "sealable sterilizer" described below,
High filling pressure (for example, 30 ° C., ethylene oxide 10% (w
t), the filling pressure of 90% (wt) carbon dioxide gas is 65
kg / cm 2 ), it is necessary to switch to the “carbon dioxide system”.

【0004】また、毒性については、一例として炭酸ガ
スによる10倍稀釈(質量比)の滅菌ガスでも、その恕
限量(8時間)は10p.p.mであり、一過性でない
強い毒性作用をもつことから、室内・作業場環境の周辺
ではいたずらに放出すべきでなく、大量に滅菌ガスを消
費・排出する産業用滅菌器(鋼製缶体、バッチ式)では
その放出ガス系路に燃焼法等の廃ガス処理装置を設けて
いることが多い。
Regarding toxicity, as an example, even if sterilizing gas is diluted 10 times (by mass) with carbon dioxide gas, its limiting amount (8 hours) is 10 p. p. m, and has a strong, non-transitory toxic effect. Therefore, it should not be released unnecessarily around the indoor or workplace environment, and consumes and discharges a large amount of sterilization gas in industrial sterilizers (steel cans, In the case of the batch type), a waste gas treatment device such as a combustion method is often provided in the release gas system.

【0005】一方、病院医療機関での自家滅菌器として
は、小規模滅菌用の「封袋型滅菌器」が多用されてい
る。この装置は、予め内部に被滅菌物を収めた小型のガ
ス微透過・菌体不透過複合フィルム製の滅菌用袋の内部
を、挿入・脱出自在のノズルで自動的又は半自動的に真
空脱氣、滅菌ガス定量封入を行ったのちシールし、必要
な場合には加温インキュベーター等に入れるなどして、
経時的に滅菌するものである。この種の装置では、袋へ
の封入段階などで若干のガスが漏出するが、その漏出ガ
ス量は微量で、換氣扇等を設けておく以外に、特に排出
ガス回収対策はとられていない。
[0005] On the other hand, as a self-sterilizer at a hospital medical institution, a "sealable sterilizer" for small-scale sterilization is frequently used. This device automatically or semi-automatically vacuum-evacuates the inside of a small gas-permeable / cell-impermeable composite sterilization bag containing an object to be sterilized in advance with a nozzle that can be inserted and removed. , Sealed after a fixed amount of sterile gas sealed, and if necessary, put it in a heated incubator, etc.
It is sterilized over time. In this type of apparatus, a slight amount of gas leaks at the stage of enclosing in a bag or the like, but the amount of the leaked gas is very small, and no special measures for exhaust gas recovery are taken except for providing a ventilation fan and the like.

【0006】[0006]

【発明が解決しようとする課題】しかし、前述のよう
に、フロン規制の結果自家用滅菌器に多用された低平衡
蒸氣圧力(一例、常温で10kg/cm2 以下)のフロ
ン混合型酸化エチレン滅菌ガスの使用が制限され、高平
衡蒸氣圧力(一例、30℃ C24 O20%(w
t),CO2 80%(wt) 57kg/cm2 )の炭
酸ガス混合型の酸化エチレン滅菌ガスが、これまでの産
業用のほか、病院・医療現場に持込まれるようになる
と、例えば滅菌器の使用間断により生じる滅菌ガス供給
装置の氣化器(蛇管等)内への封止と、その残留液化ガ
スの高圧氣化による毒性ガス不時放出等による障害発生
の機会が増加しているが、産業用、自家用を通じて、滅
菌ガス供給装置に回収装置のシステムを加えたものはな
いのが現状であり、安全性の点で問題となっている。な
お、産業用であっても、滅菌器の設置場所が離れている
ときには、滅菌ガス供給装置独自で安全弁作動等による
不時放出ガスの回収装置をもつことが望まれる。そこ
で、本発明は、上記炭酸ガス混合型酸化エチレン滅菌ガ
スの供給装置の安全性を高めることを課題としている。
However, as described above, a fluorocarbon-mixed ethylene oxide sterilizing gas having a low equilibrium vapor pressure (for example, 10 kg / cm 2 or less at room temperature) frequently used in private sterilizers as a result of the regulations for fluorocarbons. Is restricted, and a high equilibrium steam pressure (for example, 30 ° C. C 2 H 4 O 20% (w
t), CO 2 80% (wt) 57 kg / cm 2 ) CO2 mixed type ethylene oxide sterilizing gas is introduced into hospitals and medical sites in addition to the conventional industrial ones. Although the sterilization gas supply device caused by discontinuation of use is sealed in a vaporizer (such as a serpentine tube) and the chance of trouble occurrence due to accidental release of toxic gas due to high-pressure vaporization of the residual liquefied gas is increasing, At present, there is no system that adds a recovery device system to a sterile gas supply device for industrial use and private use, which is a problem in terms of safety. In addition, even if it is for industrial use, when the installation place of the sterilizer is far away, it is desirable that the sterilization gas supply device has its own recovery device for the emergency release gas by operating a safety valve or the like. Accordingly, an object of the present invention is to enhance the safety of the carbon dioxide mixed type ethylene oxide sterilizing gas supply device.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するた
め、本発明は次のような構成を採用した。すなわち、本
発明にかかる滅菌ガス供給装置は、滅菌の薬効成分であ
る酸化エチレンに稀釈成分として炭酸ガスを混合し、液
化ガス状態で充填した酸化エチレン滅菌ガス容器に接続
される液化ガス受入配管と、該液化ガス受入配管を通し
て取り出される液化ガスを減圧する第一段液減圧調整器
と、液化ガスを気化させる液化ガス氣化器と、気化した
ガスを減圧する第二段ガス減圧調整器と、減圧調整され
た滅菌ガスを滅菌器に供給する接続用配管と、配管中に
介装されるガス安全弁及びガス放出弁と、当該ガス放出
弁から放出される放出ガスを回収する放出ガス回収管
と、前記放出ガス回収管の出口に接続されるガス収容型
回収装置とを備え、前記ガス収容型回収装置の回収ガス
収容部を、柔軟性を有する着脱自在な不透氣性の袋で構
成したことを特徴としている。
In order to solve the above problems, the present invention employs the following configuration. That is, the sterilizing gas supply device according to the present invention is a liquefied gas receiving pipe connected to an ethylene oxide sterilizing gas container filled with ethylene oxide, which is a medicinal component of sterilization, and carbon dioxide as a diluting component, and filled in a liquefied gas state. A first-stage liquid decompression regulator that decompresses the liquefied gas taken out through the liquefied gas receiving pipe, a liquefied gas vaporizer that vaporizes the liquefied gas, and a second-stage gas decompression regulator that decompresses the vaporized gas, A connection pipe for supplying the sterilized gas whose pressure has been adjusted to the sterilizer, a gas safety valve and a gas release valve interposed in the pipe, and a release gas recovery pipe for collecting release gas released from the gas release valve. And a gas storage type recovery device connected to the outlet of the release gas recovery pipe, wherein the recovery gas storage part of the gas storage type recovery device is formed of a flexible, detachable and impermeable bag. It is characterized by a door.

【0008】[0008]

【作用】酸化エチレンと炭酸ガスの混合ガスが液体の状
態で充填されている高圧の滅菌ガス容器から液化ガスが
受入配管を通して取り出され、第一段液減圧調整器によ
って減圧されたのち、液化ガス氣化器によって気化され
る。気化したガスは、第二段ガス減圧調整器によって所
定の圧力に減圧され、接続用配管を通して滅菌器に供給
される。
A liquefied gas is taken out from a high-pressure sterilization gas container filled with a mixed gas of ethylene oxide and carbon dioxide in a liquid state through a receiving pipe, decompressed by a first-stage liquid pressure regulator, and then liquefied gas. It is vaporized by a vaporizer. The vaporized gas is decompressed to a predetermined pressure by the second-stage gas decompression regulator, and supplied to the sterilizer through the connection pipe.

【0009】配管中にはガス安全弁とガス放出弁が介装
されており、このガス放出弁から放出される放出ガスは
放出ガス回収管を通してガス収容型回収装置に回収され
る。前述の理由で安全弁等から不時放出され、回収装置
の回収ガス収容袋に回収された回収ガスは、満杯となる
前に空袋と交換され、別に安全な方法で燃焼等処理され
る。
A gas safety valve and a gas discharge valve are interposed in the pipe, and the gas discharged from the gas discharge valve is collected by a gas storage type recovery device through a discharge gas recovery pipe. The collected gas discharged from the safety valve or the like accidentally for a reason described above and collected in the collected gas storage bag of the collection device is replaced with an empty bag before it becomes full, and is separately burned or treated by a safe method.

【0010】[0010]

【実施例】以下、図面に表された本発明の実施例につい
て具体的に説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention shown in the drawings will be specifically described below.

【0011】図1は本発明の1実施例を表すもので、こ
の滅菌ガス供給装置1は、炭酸ガス系、酸化エチレン滅
菌ガス充填容器(高圧ガス容器)2に設けられた容器弁
3の出口に容器接手4が接続され、容器切替弁5、連結
ホース6を経て、集合管7に接続されている。この滅菌
ガス受入配管系は並列に設けられた複数列で構成するこ
とが出来る。
FIG. 1 shows one embodiment of the present invention. This sterilizing gas supply device 1 is provided at an outlet of a container valve 3 provided in a container (high-pressure gas container) 2 filled with a carbon dioxide gas and ethylene oxide sterilizing gas. Is connected to a collecting pipe 7 via a container switching valve 5 and a connecting hose 6. This sterilization gas receiving piping system can be composed of a plurality of rows provided in parallel.

【0012】容器弁3及び容器切換弁5を開くことによ
り充填容器2の液化滅菌ガスが、該充填容器内に挿入さ
れ底部に開口が設けられた液送出管10を通して取り出
され、集合管7からストレーナー13を通して第一段液
減圧調整器14に送られ、ここで滅菌ガスの液は圧力3
0kg/cm2 〜70kg/cm2 程度の圧力から第一
段減圧出口圧力、例えば、通常10kg/cm2 未満、
好ましくは2kg/cm2 未満に減圧される。この液化
ガスは、空氣熱交換式又は電熱加温式等による氣化器1
5に送られ、その蛇管15aのなかで加温されて氣化し
ガス状となり、大氣温度から温度80℃以下の適当な温
度になって、第二段ガス減圧調整器16に送られ、ここ
で滅菌器への送入圧力、例えば、通常2kg/cm2
満、好ましくは0.5kg/cm2 程度に減圧されて、
滅菌器20に組込みの滅菌ガス送入操作弁21から滅菌
器20の缶体等の封入部へ、滅菌操作のサイクルに合せ
て送入、封入される。図中、22、22’は安全弁、2
3、23’は安全弁元弁、28は放出弁である。
When the container valve 3 and the container switching valve 5 are opened, the liquefied sterilizing gas in the filling container 2 is taken out through the liquid delivery pipe 10 which is inserted into the filling container and has an opening at the bottom, and is taken out of the collecting pipe 7. It is sent through a strainer 13 to a first-stage liquid pressure-reducing regulator 14, where the sterilizing gas liquid has a pressure of 3
0kg / cm 2 ~70kg / cm 2 about the first stage vacuum outlet pressure from the pressure, for example, usually less than 10 kg / cm 2,
Preferably, the pressure is reduced to less than 2 kg / cm 2 . The liquefied gas is supplied to a vaporizer 1 using an air heat exchange system or an electric heating system.
5 and is heated in the flexible tube 15a to be gasified and gasified. The temperature is changed from the atmospheric temperature to an appropriate temperature of 80 ° C. or less, and is sent to the second-stage gas decompression controller 16, where it is sent. The inlet pressure to the sterilizer, for example, usually reduced to less than 2 kg / cm 2 , preferably about 0.5 kg / cm 2 ,
The sterilized gas is supplied from the sterilizing gas supply operation valve 21 incorporated in the sterilizer 20 to a sealed portion such as a can body of the sterilizer 20 in accordance with the cycle of the sterilization operation and sealed. In the figure, 22, 22 'are safety valves, 2
Reference numerals 3 and 23 'denote safety valve base valves, and 28 denotes a discharge valve.

【0013】滅菌ガス送入操作弁21が締切られるとそ
の滅圧調整弁が閉じられ、氣化器15への新たな液化ガ
ス「液」の送入は停止されるが、その蛇管15a内に封
止残留された未氣化の液化ガス「液」は当該滅圧圧力で
は氣液の平衡條件がないので全て氣化してその締切範囲
を昇圧し、昇圧の程度はフロン系滅菌ガスより遥かに大
きいので、場合によっては安全弁22の設定圧力以上と
なってその出口等から放出され、放出ガス回収管24お
よび回収締切弁25、回収袋入口締切コック(弁コック
又はピンチコック)26を経て、交換袋式放出ガス回収
装置27内の回収ガス収容袋30に送入され、その外形
を伸脹、膨脹させる。満杯となった回収ガス収容袋は着
脱用接手20で着脱交換される。修理等に当っては放出
弁28等からガスを回収することがある。
When the sterilization gas supply operation valve 21 is closed, its decompression regulating valve is closed and the supply of new liquefied gas "liquid" to the vaporizer 15 is stopped. At the decompression pressure, there is no gas-liquid equilibrium condition, and all unsealed liquefied gas "liquid" that remains sealed is vaporized and its deadline range is raised. In some cases, the pressure is higher than the set pressure of the safety valve 22 and is discharged from the outlet or the like, and is exchanged through the release gas collection pipe 24, the collection cutoff valve 25, and the collection bag inlet cutoff cock (valve cock or pinch cock) 26. It is sent to the collected gas storage bag 30 in the bag type released gas recovery device 27, and its outer shape is expanded and expanded. The filled recovery gas storage bag is detached and replaced by the detachable joint 20. During repair, gas may be collected from the discharge valve 28 or the like.

【0014】この回収装置の回収ガス収容部が、容積・
外形が固定された缶体である場合には、内部の空氣駆除
置換の問題、圧力送入と圧力保有を要する障害などの問
題があり適当ではないが、アルミラミネートその他不透
氣性合成樹脂複合フィルム製又は、不透氣性樹脂加工布
等で伸脹、縮小、折畳み自在な回収袋としておくことに
より、(イ)初期残存空氣パージ不要(ロ)大氣圧まで
放出ガス回収(ハ)回収ポンプ不要(ニ)回収状態の外
観的目視確認容易(ホ)低圧力保管(ヘ)軽量(ト)交
換容易等の利点が得られる。
[0014] The recovery gas storage section of the recovery device has a capacity
If the outer shape of the can is fixed, it is not appropriate because there are problems such as air removal and replacement inside and obstacles requiring pressure supply and pressure holding, but aluminum laminate or other impermeable synthetic resin composite film By making a collection bag that can be expanded, contracted, and foldable with a non-permeable resin-made cloth or the like, (a) no need for initial residual air purge (b) collection of released gas up to atmospheric pressure (c) no collection pump ( D) Advantages such as easy visual confirmation of collected state (e) Low pressure storage (f) Light weight (g) Easy replacement, etc.

【0015】図2及び図3は交換袋式放出ガス回収装置
の1例を表すもので、この回収装置27は、鋼管製で高
さ調整ねじ31によって安定して自立した外枠33を備
えている。回収ガス収容袋30は、筒状の不透氣性合成
樹脂複合フィルムの上下を折込み熱シールして袋状に柔
軟に成形されており、下部には透明の塩化ビニル等を材
質とする回収ガス取入れチューブ34が接着され、その
先端を着脱自在なワンタッチ・カップリング接手35で
滅菌ガス供給装置の鋼管製放出ガス回収管24に接続さ
れており、上記の回収ガス取入れチューブ34の中間に
は、ピンチコック37が開かれた状態で取付けられてい
る。またこの回収ガス収容袋30は、上方を把み金具付
き吊線40で外枠33に吊り下げられており、下方はス
プリング付きの把み金具41で固定されている。不時放
出回収ガスは回収締切弁43を経て回収ガス収容袋30
に送入され、該袋を膨らませる。
FIGS. 2 and 3 show an example of an exchangeable bag type released gas recovery apparatus. This recovery apparatus 27 is provided with an outer frame 33 made of steel pipe and stably self-supported by a height adjusting screw 31. I have. The recovered gas storage bag 30 is formed by folding the upper and lower ends of a cylindrical air-impermeable synthetic resin composite film and heat-sealing to form a bag-like shape. The lower portion of the recovered gas intake bag is made of transparent vinyl chloride or the like. The tube 34 is adhered, and its tip is connected to the release gas collection tube 24 made of a steel pipe of the sterilization gas supply device by a detachable one-touch coupling joint 35. The cock 37 is attached in an open state. Further, the recovered gas storage bag 30 is suspended from the upper part by an outer frame 33 by a hanging wire 40 with a grip, and the lower part is fixed by a grip 41 with a spring. Unexpectedly released collected gas passes through the collection shut-off valve 43 and is returned to the collected gas storage bag 30.
To inflate the bag.

【0016】図3は、回収袋30の膨らんだ状態を表す
もので、中央部の断面形状が円形に近くなり、各部が膨
張すると満杯である。この満杯状態となると、回収締切
弁43を閉じ、ピンチコック(回収袋入口締切弁)37
を閉じ、ワンタッチ・カップリング接手35を離脱した
のち、吊り部を外して外枠から取外し、新しい袋に取り
替える。
FIG. 3 shows a state in which the collection bag 30 is inflated. The cross-sectional shape of the central portion is close to a circle, and each portion is full when inflated. When this state is full, the collection shutoff valve 43 is closed, and the pinch cock (collection bag inlet shutoff valve) 37
Is closed, the one-touch coupling joint 35 is detached, the hanging portion is removed, the frame is removed from the outer frame, and the bag is replaced with a new bag.

【0017】図の回収袋の寸法例は、例えばB=1.5
m、H=2.2mであり、この袋の回収ガス容量は、約
3m3 である。なお、室の入口の巾に制限があるときに
は、許容される径のものを複数設置すればよい。
The dimensions of the collection bag shown in the figure are, for example, B = 1.5
m, H = 2.2 m, and the collected gas capacity of this bag is about 3 m 3 . When the width of the entrance of the chamber is limited, a plurality of chambers having an allowable diameter may be installed.

【0018】[0018]

【発明の効果】以上の説明から明らかなように、本発明
のガス滅菌器用滅菌ガス供給装置は、高い平衡蒸氣圧、
高い容器充填圧力の炭酸ガス混合系酸化エチレン滅菌ガ
スを低い常用圧力の配管によって実用的に効率よく條件
調整をして、氣化ガスを滅菌器に自動送出出来るほか、
その不時放出ガスを自動的に回収出来ることにより安全
性が向上される。
As is clear from the above description, the sterilizing gas supply device for a gas sterilizer of the present invention has a high equilibrium vapor pressure,
It is possible to adjust the conditions of carbon dioxide mixed system ethylene oxide sterilization gas with high container filling pressure practically and efficiently by using low normal pressure piping, and to automatically send vaporized gas to the sterilizer.
The safety can be improved because the emergency release gas can be automatically recovered.

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

【図1】本発明の構成の一例を示した説明図である。FIG. 1 is an explanatory diagram showing an example of the configuration of the present invention.

【図2】交換袋式放出ガス回収装置の実施例を示す外観
図である。
FIG. 2 is an external view showing an embodiment of an exchange bag type released gas recovery device.

【図3】その膨らんだ状態の外観図である。FIG. 3 is an external view of the expanded state.

【符号の説明】[Explanation of symbols]

1 滅菌ガス充填容器 2 ガス容器 3 容器弁 4 容器接手 5 容器切換弁 7 集合管 10 液送出管 14 第一段液減圧調整器 15 氣化器 16 第二段ガス減圧調整器 20 滅菌器 22 一次側安全弁 22’ 二次側安全弁 28 放出弁 27 交換袋式放出ガス回収装置 30 回収ガス収容袋 DESCRIPTION OF SYMBOLS 1 Sterilizing gas filling container 2 Gas container 3 Container valve 4 Container joint 5 Container switching valve 7 Collecting pipe 10 Liquid delivery pipe 14 First stage liquid pressure regulator 15 Gasifier 16 Second stage gas pressure regulator 20 Sterilizer 22 Primary Side safety valve 22 'Secondary side safety valve 28 Release valve 27 Exchangeable bag type released gas recovery device 30 Recovered gas storage bag

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 滅菌の薬効成分である酸化エチレンに稀
釈成分として炭酸ガスを混合し、液化ガス状態で充填し
た酸化エチレン滅菌ガス容器に接続される液化ガス受入
配管と、該液化ガス受入配管を通して取り出される液化
ガスを減圧する第一段液減圧調整器と、液化ガスを気化
させる液化ガス氣化器と、気化したガスを減圧する第二
段ガス減圧調整器と、減圧調整された滅菌ガスを滅菌器
に供給する接続用配管と、配管中に介装されるガス安全
弁及びガス放出弁と、当該ガス放出弁から放出される放
出ガスを回収する放出ガス回収管と、前記放出ガス回収
管の出口に接続されるガス収容型回収装置とを備え、前
記ガス収容型回収装置の回収ガス収容部を、柔軟性を有
する着脱自在な不透氣性の袋で構成したことを特徴とす
るガス滅菌器用滅菌ガス供給装置。
1. A liquefied gas receiving pipe connected to an ethylene oxide sterilizing gas container filled with ethylene oxide, which is a medicinal ingredient for sterilization, as a diluent and filled with carbon dioxide as a liquefied gas, and the liquefied gas receiving pipe. A first-stage liquid decompression regulator for decompressing the liquefied gas taken out, a liquefied gas vaporizer for vaporizing the liquefied gas, a second-stage gas decompression regulator for decompressing the vaporized gas, and a sterilized gas that has been decompressed and adjusted. A connection pipe for supplying to the sterilizer, a gas safety valve and a gas release valve interposed in the pipe, a release gas recovery pipe for recovering release gas released from the gas release valve, and a release gas recovery pipe. A gas storage type recovery device connected to an outlet, wherein the recovery gas storage portion of the gas storage type recovery device is constituted by a flexible detachable air-impermeable bag. Sterilization Gas supply device.
JP4280677A 1992-09-24 1992-09-24 Sterilizing gas supply device for gas sterilizer Expired - Lifetime JP2696462B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4280677A JP2696462B2 (en) 1992-09-24 1992-09-24 Sterilizing gas supply device for gas sterilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4280677A JP2696462B2 (en) 1992-09-24 1992-09-24 Sterilizing gas supply device for gas sterilizer

Publications (2)

Publication Number Publication Date
JPH06105891A JPH06105891A (en) 1994-04-19
JP2696462B2 true JP2696462B2 (en) 1998-01-14

Family

ID=17628397

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4280677A Expired - Lifetime JP2696462B2 (en) 1992-09-24 1992-09-24 Sterilizing gas supply device for gas sterilizer

Country Status (1)

Country Link
JP (1) JP2696462B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108686240A (en) * 2017-04-10 2018-10-23 莎罗雅株式会社 Sterilizing methods and bactericidal unit

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115646144B (en) * 2022-11-04 2024-04-02 常熟荣瑞灭菌技术有限公司 Waste gas recycling treatment device of ethylene oxide sterilizing cabinet

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108686240A (en) * 2017-04-10 2018-10-23 莎罗雅株式会社 Sterilizing methods and bactericidal unit
CN108686240B (en) * 2017-04-10 2022-03-04 山东新华医疗器械股份有限公司 Sterilization method and sterilization apparatus

Also Published As

Publication number Publication date
JPH06105891A (en) 1994-04-19

Similar Documents

Publication Publication Date Title
US11097029B2 (en) Sterilization method and apparatus
ES2247379T3 (en) PROCEDURE AND APPARATUS FOR OZONE STERILIZATION.
US10953121B2 (en) Devices, systems and methods for ozone sanitization of continuous positive airway pressure devices
AU2003301239B2 (en) Flexible walk-in environmental enclosure
AU2002340663A1 (en) Method and apparatus for ozone sterilization
US20100196198A1 (en) Ozonoe sterilizaation process and apparatus
ES2278588T3 (en) METHOD AND APPARATUS FOR OZONE STERILIZATION.
JP6687718B2 (en) Sterile liquefied gas manufacturing apparatus and method for manufacturing sterilized liquefied gas
JP2696462B2 (en) Sterilizing gas supply device for gas sterilizer
US6290906B1 (en) Method for removing sterilant from objects subjected to gaseous sterilization
JPH0448064B2 (en)

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19970722

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080919

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080919

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090919

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090919

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100919

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100919

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110919

Year of fee payment: 14

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120919

Year of fee payment: 15

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130919

Year of fee payment: 16

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130919

Year of fee payment: 16