JP2002095723A - Vapor sterilizer and vapor sterilizing method - Google Patents

Vapor sterilizer and vapor sterilizing method

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Publication number
JP2002095723A
JP2002095723A JP2000287835A JP2000287835A JP2002095723A JP 2002095723 A JP2002095723 A JP 2002095723A JP 2000287835 A JP2000287835 A JP 2000287835A JP 2000287835 A JP2000287835 A JP 2000287835A JP 2002095723 A JP2002095723 A JP 2002095723A
Authority
JP
Japan
Prior art keywords
steam
processing chamber
sterilization
steam generator
pressure
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
JP2000287835A
Other languages
Japanese (ja)
Inventor
Makoto Otani
真 大谷
Satoru Sanukida
哲 讃岐田
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.)
SANUKIDA SEISAKUSHO KK
Iwatani International Corp
Original Assignee
SANUKIDA SEISAKUSHO KK
Iwatani International Corp
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 SANUKIDA SEISAKUSHO KK, Iwatani International Corp filed Critical SANUKIDA SEISAKUSHO KK
Priority to JP2000287835A priority Critical patent/JP2002095723A/en
Publication of JP2002095723A publication Critical patent/JP2002095723A/en
Pending legal-status Critical Current

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  • Apparatus For Disinfection Or Sterilisation (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a vapor sterilizer of a simple structure which can accurately perform sterilization and its sterilizing method. SOLUTION: A vapor jacket (10) is formed between the inner and outer tanks for a sterilizing can (3) of double-structure. A vapor generator (4) is closely arranged beneath the sterilizing can (3) in a way of direct connection and successively connected to the bottom of a processing chamber (16) inside the sterilization can (3). Plural filters for removing bacteria (18), (19) are arranged in series in an exhaust system route (7) being led out from the upper part of the processing chamber (16). A vapor heating coil (5) is fixed in the vapor generator (4), and the supply of purified water to the vapor generator (4) is made available. A vacuum pump (23) is communicated and connected with the inside of the processing chamber (16).

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、実験室や研究室あ
るいは検査室もしくは一般病棟(以下単に実験室等とい
う)で細菌等に汚染された使用済み器具や液体培地等あ
るいは遺伝子組換実験で使用した器具類などの被処理物
を実験室等の外に搬出する際に使用する蒸気滅菌装置及
び蒸気滅菌方法に関する。
The present invention relates to a laboratory, a laboratory, a laboratory, or a general ward (hereinafter simply referred to as a laboratory, etc.) which is used for a used instrument or liquid medium contaminated with bacteria, etc., or for genetic recombination experiments. The present invention relates to a steam sterilization apparatus and a steam sterilization method used when carrying out an object to be treated such as used instruments outside a laboratory or the like.

【0002】[0002]

【従来の技術】実験室では、各種細菌やウイルスを培養
したり、細菌やウイルスを使用した実験・検査等が行わ
れる。このような実験や検査に使用した器具類は、細菌
やウイルス(以下、単に微生物という)に汚染されている
ことから、実験室等外に持ち出す際には、滅菌処理を施
さなければならない。また、遺伝子組換実験に使用した
器具類の実験室等への搬出時にも、滅菌処理を施さなけ
ればならない。
2. Description of the Related Art In a laboratory, various bacteria and viruses are cultured, and experiments and inspections using the bacteria and viruses are performed. The instruments used for such experiments and inspections are contaminated with bacteria and viruses (hereinafter simply referred to as microorganisms), and thus must be sterilized when taken out of the laboratory or the like. In addition, sterilization must be performed when the equipment used in the genetic modification experiment is carried out to a laboratory or the like.

【0003】そこで、従来は、被処理物を収容した滅菌
処理室に高圧蒸気を送給し、所定温度(例えば121℃
以上)で一定時間(例えば20分以上)処理することで滅
菌処理していた。そして、この場合、処理室に導入され
た高圧蒸気は被処理物との接触によって熱を奪われて処
理室内で凝縮し、この凝縮水は処理室外に排出するよう
にしてある。
Therefore, conventionally, high-pressure steam is supplied to a sterilization chamber accommodating an object to be processed, and a predetermined temperature (for example, 121 ° C.) is supplied.
For a certain period of time (for example, 20 minutes or more). In this case, the high-pressure steam introduced into the processing chamber is deprived of heat by contact with the object to be processed and condensed in the processing chamber, and this condensed water is discharged outside the processing chamber.

【0004】[0004]

【発明が解決しようとする課題】ところが、処理室から
滅菌完了前に排出される凝縮水(ドレン)は微生物に汚染
された状態であることから、ドレン排水系にさらに滅菌
処理するドレン水処理設備を配置しなければならなかっ
た。また、仮に、ドレン排水系にドレン水処理設備を設
置したとしても、滅菌処理室とそのドレン水処理設備と
の間の配管部分は微生物に汚染された状態のままになる
という問題があった。
However, since the condensed water (drain) discharged from the treatment chamber before the completion of sterilization is in a state of being contaminated with microorganisms, a drain water treatment facility for further sterilizing the drain water drainage system. Had to be placed. Further, even if drain water treatment equipment is installed in the drain drainage system, there is a problem that a pipe portion between the sterilization treatment chamber and the drain water treatment equipment remains contaminated with microorganisms.

【0005】このような点に着目して本発明は、簡単な
構造で確実に滅菌処理することのできる蒸気滅菌方法及
びその装置を提供することを目的とする。
[0005] Focusing on such points, an object of the present invention is to provide a steam sterilization method and an apparatus thereof that can surely perform sterilization with a simple structure.

【0006】[0006]

【課題を解決するための手段】上述の目的を達成するた
めに本第1発明は、処理対象物である被滅菌物を収容す
る収容室を構成する内槽と、内槽の外部にジャケットを
介して位置している外槽とで滅菌缶を構成し、この滅菌
缶の下側に蒸気発生器を直結状に接近配置し、蒸気発生
器を内槽の底部に連通接続し、内槽の上部から導出した
排気路中に複数の除菌フィルターを直列に配置し、蒸気
発生器に加熱用蒸気コイルを配置するとともに、この蒸
気発生器に精製水を供給可能に構成し、内槽内を真空ポ
ンプに連通接続させたことを特徴としている。
According to a first aspect of the present invention, there is provided an inner tank forming a storage chamber for storing an object to be treated, and a jacket provided outside the inner tank. A sterilization can is constituted by an outer tank positioned through the steam generator, a steam generator is disposed directly below the sterilization can so as to be directly connected to the sterilization can, and the steam generator is connected to the bottom of the inner tank and is connected to the inner tank. A plurality of disinfecting filters are arranged in series in the exhaust path derived from the upper part, a heating steam coil is arranged in the steam generator, and the steam generator is configured to be able to supply purified water. It is characterized by being connected to a vacuum pump.

【0007】また本第2発明は、二重缶構造に形成した
滅菌缶の内外槽体間に形成したジャケットに蒸気を送給
してジャケット内が所定の圧力に達するまで加熱し、ジ
ャケット内が所定の圧力に達すると内層で構成した処理
室内を所定時間減圧し、処理室内の減圧が完了すると、
滅菌缶の下側に直結状に配置した蒸気発生器内に精製水
を所定の水位まで供給し、精製水が所定水位に達する
と、蒸気発生器内に配置した加熱用蒸気コイルに加熱蒸
気を流通させて蒸気発生器内の精製水で発生した水蒸気
を滅菌缶の処理室内に送給して処理室内を蒸気飽和状態
に維持し、被滅菌物との接触によって凝縮したドレン水
を蒸気発生器に返送して再蒸気化させるようにし、処理
室の内圧が加圧状態になると、排気路から直列配置した
複数の除菌フィルターを通して排気し、排気路での下流
側に配置した除菌フィルターの温度が所定温度に達した
後、予め設定した時間が経過するまで蒸気加熱を継続
し、設定時間経過後に蒸気発生器のドレン路を開通させ
て、蒸気発生器から貯留水を抜き取るとともに、処理室
の内圧を降下させ、その後処理室を真空ポンプに連通さ
せた減圧状態と、処理室に大気を導入した大気圧状態で
所定時間保持する状態とを数回繰り返して真空乾燥させ
るようにしたことを特徴としている。
In the second invention, steam is supplied to a jacket formed between the inner and outer tanks of a sterilized can having a double can structure, and the jacket is heated until a predetermined pressure is reached. When the pressure reaches a predetermined pressure, the pressure in the processing chamber formed of the inner layer is reduced for a predetermined time, and when the pressure in the processing chamber is completed,
The purified water is supplied to a predetermined level in a steam generator arranged directly below the sterilization can, and when the purified water reaches the predetermined level, the heating steam is supplied to a heating steam coil disposed in the steam generator. The steam generated by the purified water in the steam generator is sent into the processing chamber of the sterilization can to maintain the processing chamber in a steam-saturated state, and drain water condensed by contact with the object to be sterilized is generated by the steam generator. When the internal pressure of the processing chamber is in a pressurized state, the air is exhausted from the exhaust path through a plurality of sterilization filters arranged in series, and the air is removed from the sterilization filter arranged downstream in the exhaust path. After the temperature reaches the predetermined temperature, the steam heating is continued until a preset time elapses, and after the elapse of the set time, the drain path of the steam generator is opened, the stored water is extracted from the steam generator, and the processing chamber is removed. Internal pressure, and A reduced pressure state that communicates the post-processing chamber to the vacuum pump, by repeating several times the state for a predetermined time at atmospheric pressure while introducing the atmosphere is characterized in that so as to vacuum drying in the processing chamber.

【0008】[0008]

【発明の作用】本発明では、滅菌缶の下側に蒸気発生器
を直結状に近接配置し、この蒸気発生器内に精製水を供
給するとともに加熱用蒸気コイルを配設して、蒸気発生
器内で発生させた水蒸気を処理室内に導入するようにし
ていることから、処理室内で凝縮したドレン水は蒸気発
生器内に流れ込み、ここで再び加熱されることになるか
ら、処理開始当初に高温保持時間が短くて微生物に汚染
されたドレン水でも、再加熱されて循環しているうち
に、処理時間・処理温度が十分になることから、滅菌装
置での滅菌処理完了時にはドレン水も確実に滅菌される
ことになる。
According to the present invention, a steam generator is disposed in direct proximity to the lower side of a sterilization can, purified water is supplied into the steam generator, and a heating steam coil is provided. Since the steam generated in the chamber is introduced into the processing chamber, the drain water condensed in the processing chamber flows into the steam generator and is heated again there. Even for drain water contaminated with microorganisms due to a short high-temperature holding time, the processing time and temperature are sufficient while reheating and circulating. Will be sterilized.

【0009】[0009]

【発明の実施の形態】図は本発明の一実施形態を示す滅
菌装置の概略構成図であり、この滅菌装置は、内外二重
槽(1)(2)で形成した滅菌缶(3)と、この滅菌缶(3)の
下側に内槽(1)と直結する状態で配置された蒸気発生器
(4)と、蒸気発生器(4)内に配置された加熱用コイル
(5)と、加熱用蒸気供給系路(6)と、排気系路(7)と、
蒸気発生器(4)への給水系路(8)とを有している。な
お、図示は省略したが滅菌缶(3)の内槽(1)は対向する
壁面にそれぞれ開閉扉が形成してあり、一方の開閉扉が
実験室等の汚染源存在空間に、他方の開閉扉が準備室等
の空間に臨んでいる。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic structural view of a sterilization apparatus showing one embodiment of the present invention. This sterilization apparatus has a sterilization can (3) formed by an inner and outer double tank (1) (2). , A steam generator arranged directly below the inner tank (1) under the sterilization can (3)
(4) and a heating coil arranged in the steam generator (4)
(5), a heating steam supply system (6), an exhaust system (7),
A water supply line (8) to the steam generator (4). Although not shown, the inner tank (1) of the sterilization can (3) has an opening / closing door formed on opposing wall surfaces. One opening / closing door is located in a space where a contamination source exists, such as a laboratory, and the other opening / closing door is provided. Faces a space such as a preparation room.

【0010】加熱用蒸気供給系路(6)は、蒸気発生器
(4)の加熱用コイル(5)に蒸気を供給する精製水加熱用
蒸気供給路(9)と、滅菌缶(3)の内槽(1)と外槽(2)と
の間の間隙に形成したジャケット(10)に蒸気を供給する
滅菌缶加熱用蒸気供給路(11)とで構成してあり、これら
精製水加熱用蒸気供給路(9)と滅菌缶加熱用蒸気供給路
(11)とは同一の蒸気発生源からの蒸気を分岐して供給す
るように構成してある。そして、加熱用コイル(5)から
の蒸気排出路(12)及びジャケット(10)からの蒸気排出路
(13)は集合排出路(14)に接続されている。また、滅菌缶
加熱用蒸気供給路(11)から分岐導出された分岐通路(15)
が滅菌缶(3)の内槽(1)に連通遮断切換可能に接続して
ある。
[0010] The heating steam supply line (6) is a steam generator.
In the gap between the inner tank (1) and the outer tank (2) of the sterilization can (3) and the purified water heating steam supply path (9) for supplying steam to the heating coil (5) of (4). And a steam supply path (11) for heating the sterilized can for supplying steam to the formed jacket (10). The steam supply path (9) for heating the purified water and the steam supply path for heating the sterilized can.
(11) is configured to branch and supply steam from the same steam generation source. And a steam discharge path (12) from the heating coil (5) and a steam discharge path from the jacket (10).
(13) is connected to the collective discharge path (14). In addition, a branch passage (15) branched from the steam supply passage (11) for heating the sterilization can.
Is connected to the inner tank (1) of the sterilization can (3) so as to be able to switch communication.

【0011】排気経路(7)は、処理室(16)となる滅菌缶
(3)での内槽(1)の天井壁から導出してあり、この排気
経路(7)に2つの除菌フィルター(18)(19)が直列に配置
してある。この除菌フィルター(18)(19)はそれぞれ0.
2μm除菌グレードのフィルターで構成してあり、下流
側に位置している除菌フィルター(19)の出口部分に温度
センサー(20)が配置してある。そして、除菌フィルター
(18)と除菌フィルター(19)との間からガス排出路(21)が
分岐導出してあり、このガス排出路(21)と前記排気系路
(7)とは集合排出路(14)に連通接続されている。
The exhaust path (7) is a sterilization can that becomes the processing chamber (16).
It is led out from the ceiling wall of the inner tank (1) in (3), and two sterilization filters (18) and (19) are arranged in series in this exhaust path (7). Each of the disinfecting filters (18) and (19) has a capacity of 0.1.
A temperature sensor (20) is arranged at the outlet of the sterilization filter (19) located on the downstream side. And the sanitizing filter
A gas discharge path (21) is branched and led out from between (18) and the sterilization filter (19), and the gas discharge path (21) and the exhaust path
(7) is connected to the collective discharge path (14).

【0012】また、下流側除菌フィルター(19)よりも下
流側での排気系路(7)部分にサクション通路(22)が連通
接続してあり、このサクション通路(22)に配置した真空
ポンプ(23)の作動で滅菌缶(3)の内槽(1)内を減圧処理
できるようにしてある。なお、この真空ポンプ(23)の吐
出側は集合排出路(14)に連通接続してある。さらに、下
流側除菌フィルター(19)よりも下流側での排気系路(7)
部分には大気導入路(24)が連通接続してある。
A suction passage (22) is connected to the exhaust system (7) downstream of the downstream sterilization filter (19), and a vacuum pump disposed in the suction passage (22). By the operation of (23), the inside of the inner tank (1) of the sterilization can (3) can be decompressed. The discharge side of the vacuum pump (23) is connected to the collective discharge path (14). Furthermore, an exhaust system (7) downstream of the downstream sanitizing filter (19)
An air introduction passage (24) is communicatively connected to the portion.

【0013】蒸気発生器(4)は、精製水給水路(25)が接
続されるとともに、底部からドレン排水路(26)が連出し
てあり、このドレン排水路(26)は集合排出路(14)に連通
接続させてある。図中符号(27)は真空ポンプ(23)に接続
されている封止水路である。
The steam generator (4) is connected to a purified water supply channel (25), and has a drain discharge channel (26) extending from the bottom. The drain discharge channel (26) is connected to a collective discharge channel (25). It is connected to 14). Reference numeral (27) in the figure denotes a sealing water channel connected to the vacuum pump (23).

【0014】上述の構成からなる滅菌装置を使用しての
除菌手順を述べる。実験室等の汚染源存在空間側の開閉
扉を開いて、処理室(16)に被処理物(汚染物)を収容した
後、開閉扉を閉じ滅菌缶(3)を締めきる。次いで運転開
始ボタンを押すと、滅菌缶加熱用蒸気供給路(11)が開通
してジャケット(10)に蒸気を供給し、内槽(1)を加熱す
る。このとき、ジャケット内で凝縮液化したドレン水は
蒸気排出路(13)を介して集合排出路(14)に排出される。
このドレン水は汚染物との接触がないことから清浄な状
態である。このジャケット(10)への蒸気供給は滅菌処理
完了まで継続される。
[0014] A sterilization procedure using the sterilizer having the above-described configuration will be described. After opening and closing the door on the side of the space where the contamination source exists, such as a laboratory, and storing the object to be treated (contaminant) in the processing chamber (16), close the door and close the sterilization can (3). Then, when the operation start button is pressed, the steam supply path (11) for heating the sterilization can is opened to supply steam to the jacket (10) and heat the inner tank (1). At this time, the drain water condensed and liquefied in the jacket is discharged to the collective discharge path (14) via the vapor discharge path (13).
This drain water is in a clean state because there is no contact with contaminants. The steam supply to the jacket (10) is continued until the sterilization process is completed.

【0015】ジャケット(10)が蒸気で加熱・加圧されて
ジャケットの内圧が所定圧(例えばゲージ圧で0.08M
Pa)になると、真空ポンプ(23)を作動させて処理室(1
6)内を減圧する。このとき、汚染されている処理室(16)
内の空気は、内槽(1)から導出した排気経路(7)を経由
してサクション通路(22)に流れ込むことになるが、排気
経路(7)には2つの除菌フィルター(18)(19)が直列に配
置してあることから、除菌された状態で排出されること
になる。そして、真空ポンプ(23)は一定時間作動した後
に停止し、サクション通路(22)は閉止される。
The jacket (10) is heated and pressurized with steam so that the internal pressure of the jacket becomes a predetermined pressure (for example, a gauge pressure of 0.08M).
Pa), the vacuum pump (23) is operated to activate the processing chamber (1).
6) Reduce the pressure inside. At this time, the contaminated processing chamber (16)
The air inside flows into the suction passage (22) via the exhaust passage (7) derived from the inner tank (1), and the two sanitizing filters (18) ( Since (19) is arranged in series, it is discharged in a state where bacteria are removed. Then, the vacuum pump (23) is stopped after operating for a predetermined time, and the suction passage (22) is closed.

【0016】次いで、精製水給水路(25)から蒸気発生器
(4)に精製水を所定水位を維持する状態に給水し、精製
水加熱用蒸気供給路(9)から加熱用コイル(5)に加熱用
蒸気を供給し、精製水を加熱して蒸気を発生させる。蒸
気発生器(4)と処理室(16)とは直結されており、また処
理室(16)内は前の段階で減圧されていることから、処理
室(16)は発生した蒸気により、絶えず飽和状態を保って
加熱されることになる。また、発生した蒸気は処理室内
に収容された被処理物と接触して熱を奪われ、凝縮する
が、この凝縮したドレン水は蒸気発生器(4)内に流下し
て加熱用コイル(5)で加熱されることになる。
Next, a steam generator is connected to the purified water supply channel (25).
(4) The purified water is supplied to maintain the predetermined water level, and the purified water heating steam supply passage (9) supplies heating steam to the heating coil (5) to heat the purified water to produce steam. generate. The steam generator (4) is directly connected to the processing chamber (16), and the processing chamber (16) is constantly depressurized by the generated steam because the pressure in the processing chamber (16) is reduced in the previous stage. It will be heated while maintaining the saturated state. The generated steam comes in contact with the object to be processed accommodated in the processing chamber, and is deprived of heat and condenses. The condensed drain water flows down into the steam generator (4) and flows into the heating coil (5). ) Will be heated.

【0017】蒸気発生器(4)からの蒸気供給により処理
室(16)内が減圧状態から加圧状態に移行すると、排気経
路(7)及びガス排出路(21)が開通し、処理室(16)内の気
体成分は、直列に配置してある2つの除菌フィルター(1
8)(19)を通過することにより除菌されて集合排出路(14)
から排出される。そして、下流側除菌フィルター(19)の
出口部分に配置した温度センサー(20)が所定温度(例え
ば121℃)に達することで次の工程にすすむ。
When the inside of the processing chamber (16) shifts from a reduced pressure state to a pressurized state by the supply of steam from the steam generator (4), the exhaust path (7) and the gas discharge path (21) are opened, and the processing chamber (16) is opened. 16), the gas components in the two sterilization filters (1
8) It is sterilized by passing through (19) and is collected and discharged (14)
Is discharged from Then, when the temperature sensor (20) arranged at the outlet of the downstream-side sterilization filter (19) reaches a predetermined temperature (for example, 121 ° C.), the process proceeds to the next step.

【0018】滅菌温度の制御は、滅菌缶(3)での最も低
い温度となる下流側除菌フィルター(18)での出口部分の
温度を検出する温度センサー(20)の検出温度に基づき加
熱コイル(5)への蒸気供給量を制御することに行うよう
にしてある。そして、所定の滅菌雰囲気温度を所定時間
保持することにより、滅菌処理される。なお、このとき
処理室(16)内で凝縮したドレン水は、蒸気発生器(4)に
戻り、再蒸気化される。さらに、排気経路(7)に介装し
てある除菌フィルター(18)(19)も処理室(16)内の雰囲気
温度に曝されるから除菌フィルター(18)(19)も同時に除
菌されることになる。
The control of the sterilization temperature is based on the temperature detected by the temperature sensor (20) for detecting the temperature at the outlet of the downstream sterilization filter (18), which is the lowest temperature in the sterilization can (3). The control is performed by controlling the amount of steam supply to (5). Then, a predetermined sterilization atmosphere temperature is maintained for a predetermined time to perform a sterilization process. At this time, the drain water condensed in the processing chamber (16) returns to the steam generator (4) and is re-vaporized. Furthermore, since the sterilizing filters (18) and (19) interposed in the exhaust path (7) are also exposed to the ambient temperature in the processing chamber (16), the sterilizing filters (18) and (19) are simultaneously sterilized. Will be done.

【0019】所定時間の滅菌操作がおわると、ドレン排
水路(26)を開通させて、蒸気発生器(4)内の貯留水が一
定水位になるまで排出し、処理室(16)内の圧力が所定の
圧力(例えば0.02MPa)になると、ドレン排水路(2
6)、排気経路(7)及びガス排出路(21)を閉止する。
When the sterilization operation for a predetermined time is completed, the drainage drain (26) is opened, and the water stored in the steam generator (4) is discharged until the water level reaches a certain level, and the pressure in the processing chamber (16) is reduced. When the pressure reaches a predetermined pressure (for example, 0.02 MPa), the drain drainage channel (2
6) Close the exhaust path (7) and the gas exhaust path (21).

【0020】次いで、真空乾燥工程にはいる。真空乾燥
工程は、真空ポンプ(23)を作動させるとともに、真空ポ
ンプ(23)を処理室(16)に連通させて、処理室(16)内を減
圧して乾燥させ、所定の乾燥時間が経過すると、大気導
入路(24)を処理室(16)内に連通させる。このとき、大気
は除菌フィルター(19)(18)を介して導入されることか
ら、除菌された大気が処理室(16)内に流入することにな
る。処理室(16)内を大気圧に保持することにより、ジャ
ケット(10)からの熱で被処理物を加熱して、次の減圧操
作時の気化熱を補充する。この減圧から大気圧保持まで
の工程を数回繰り返し、真空乾燥を完了させる。
Next, a vacuum drying step is started. In the vacuum drying step, the vacuum pump (23) is operated, the vacuum pump (23) is connected to the processing chamber (16), the inside of the processing chamber (16) is depressurized and dried, and a predetermined drying time elapses. Then, the air introduction path (24) is communicated with the inside of the processing chamber (16). At this time, since the air is introduced through the sterilization filters (19) and (18), the sterilized air flows into the processing chamber (16). By maintaining the inside of the processing chamber (16) at atmospheric pressure, the object to be processed is heated by the heat from the jacket (10) to replenish the heat of vaporization at the time of the next pressure reduction operation. This process from the reduced pressure to the atmospheric pressure is repeated several times to complete the vacuum drying.

【0021】以上の操作がおわると、汚染源が存在しな
い側の空間側に位置する処理室(16)の開閉扉を開放して
滅菌処理済の被処理物を取出す。
When the above operation is completed, the opening and closing door of the processing chamber (16) located on the side of the space where the contamination source does not exist is opened to take out the sterilized processed object.

【0022】実験室等に実験器具等を搬入する場合には
この滅菌缶を搬入路として使用することで、実験室外か
ら雑菌に汚染された器具や空気が実験室内に入り込むこ
とを防止できる。この雑菌等で汚染さた空気や器具類が
入り込むのを防止する為、処理室(16)内を空滅菌処理を
した後に、実験室等側に位置する開閉扉を開ける。
When carrying the laboratory equipment and the like into the laboratory or the like, by using this sterilized can as a carrying path, it is possible to prevent equipment or air contaminated with various bacteria from entering the laboratory from outside the laboratory. In order to prevent air and instruments contaminated by the germs and the like from entering, the inside of the processing chamber (16) is subjected to empty sterilization, and then the opening / closing door located on the laboratory or the like side is opened.

【0023】また、実験室等がクリーンルームの場合、
処理物(被滅菌物)を連続して搬出する場合には、前回の
処理で滅菌処理されて処理物を取出す際、実験室外部空
間側の開閉扉を開けることにより、処理室内には雑菌で
汚染されている外部空気が流れ込み充満する。この為、
連続して処理物を搬出するべく実験室等側の扉を開ける
と、処理室内の空気が実験室等に流れ込むことになるか
ら、この連続搬出操作時にも空滅菌処理を施した後、実
験室側に位置する開閉扉を開ける。
When the laboratory is a clean room,
When unloading the processed material (substance to be sterilized) continuously, open the door on the outside space side of the laboratory at the time of taking out the processed material after sterilization in the previous process, so that various bacteria may enter the processing room. Contaminated external air flows in and fills. Because of this,
If the door on the laboratory or the like side is opened in order to carry out the processed material continuously, the air in the processing room flows into the laboratory or the like. Open the door located on the side.

【0024】この空滅菌処理は、ジャケット(10)内に蒸
気を供給して処理室(16)内を加温し、次いで、処理室(1
6)内に真空ポンプ(23)を連通させて処理室(16)内を減圧
雰囲気に保持し、この減圧状態の処理室(16)に分岐通路
(15)から蒸気を供給して処理室(16)内を滅菌処理する。
この処理室(16)内で凝縮したドレン水は、蒸気発生器
(4)内に流下し、ドレン排水路(26)から排出される。
In this empty sterilization process, steam is supplied into the jacket (10) to heat the inside of the processing chamber (16), and then the processing chamber (1) is heated.
A vacuum pump (23) is connected to the inside of the processing chamber (16) so that the inside of the processing chamber (16) is maintained in a reduced pressure atmosphere.
Steam is supplied from (15) to sterilize the inside of the processing chamber (16).
The drain water condensed in this processing chamber (16) is
It flows down into (4) and is discharged from the drain drainage channel (26).

【0025】分岐通路(15)から供給される蒸気によっ
て、処理室(16)内が加圧状態になると、その蒸気は排気
経路(7)から排出される。このとき、排出蒸気は除菌フ
ィルター(18)(19)を介して排出されることになるから、
汚染された蒸気が外部に排出されることはない。そし
て、排気経路(7)での下流側除菌フィルター(19)の出口
部分に配設されている温度センサー(20)が所定温度(例
えば121℃)以上になったことを検出すると、その状
態を維持するように供給蒸気量を制御し、滅菌雰囲気温
度を所定時間維持する。
When the processing chamber (16) is pressurized by the steam supplied from the branch passage (15), the steam is discharged from the exhaust path (7). At this time, the discharged steam will be discharged through the sterilization filters (18) and (19),
No polluted vapor is released to the outside. When the temperature sensor (20) disposed at the outlet of the downstream sterilization filter (19) in the exhaust path (7) detects that the temperature has reached a predetermined temperature (for example, 121 ° C.), the state is determined. Is controlled so as to maintain the sterilization atmosphere temperature for a predetermined time.

【0026】定められた滅菌時間が経過すると、処理室
(16)への蒸気供給を停止することにより、ドレン通路(2
6)、排気経路(7)及びガス排出路(21)を通って蒸気が逃
散して、処理室(16)が所定の圧力(例えば0.02MPa)
になると、ドレン通路(26)、排気経路(7)及びガス排出
路(21)を閉じ、前述と同様の真空乾燥工程に入り、真空
乾燥が終わると、大気を導入して処理室(16)内を大気圧
に戻し、実験室等側に位置する処理室(16)の開閉扉を開
放する。
After the specified sterilization time has elapsed, the processing chamber
By stopping the steam supply to (16), the drain passage (2
6), the steam escapes through the exhaust path (7) and the gas discharge path (21), and the processing chamber (16) is set to a predetermined pressure (for example, 0.02 MPa).
Then, the drain passage (26), the exhaust passage (7) and the gas exhaust passage (21) are closed, and the same vacuum drying process as described above is started. When the vacuum drying is completed, the atmosphere is introduced into the processing chamber (16). The inside is returned to the atmospheric pressure, and the opening and closing door of the processing chamber (16) located on the laboratory room side is opened.

【0027】また、液体培地の滅菌では、前述の器具類
の滅菌処理手順と同様の手順で滅菌処理し、真空乾燥工
程を採らずに自然放熱で冷却する。
In the sterilization of the liquid medium, sterilization is performed by the same procedure as the sterilization procedure of the above-mentioned instruments, and the apparatus is cooled by natural heat radiation without using a vacuum drying step.

【0028】このように、本発明では、滅菌缶(3)の下
側に直結する状態で蒸気発生器(4)を配置し、滅菌缶
(3)内の処理室(16)で凝縮したドレン水を蒸気発生器
(4)で受けとめ、再蒸気化するようにしていることか
ら、最終的に排出される蒸気発生器(4)内の貯留水は滅
菌温度で十分加熱されたものとなる為、排出される貯留
水は滅菌処理されたものとなる。この為、二次的な滅菌
処理は不要になる。
As described above, in the present invention, the steam generator (4) is arranged in a state directly connected to the lower side of the sterilization can (3),
(3) Drain water condensed in the processing chamber (16) in the steam generator
Since it is received in (4) and re-evaporated, the stored water in the steam generator (4) that is finally discharged is heated sufficiently at the sterilization temperature, so the stored water is discharged. The water will be sterilized. Therefore, a secondary sterilization process is not required.

【0029】[0029]

【発明の効果】本発明では、滅菌缶の下側に蒸気発生器
を直結状に近接配置し、この蒸気発生器内に精製水を供
給するとともに加熱用蒸気コイルを配設して、蒸気発生
器内で発生させた水蒸気を処理室内に導入するようにし
ていることから、処理室内で凝縮したドレン水は蒸気発
生器内に流れ込み、ここで再び加熱されることになる。
このため、処理開始当初に高温保持時間が短くて微生物
に汚染されたドレン水でも、再加熱されて循環している
うちに、処理時間・処理温度が十分になることから、滅
菌装置での滅菌処理完了時にはドレン水も確実に滅菌す
ることができる。
According to the present invention, a steam generator is disposed in direct proximity to the lower side of a sterilization can, purified water is supplied into the steam generator, and a heating steam coil is provided. Since the steam generated in the vessel is introduced into the processing chamber, the drain water condensed in the processing chamber flows into the steam generator, where it is heated again.
For this reason, even if the drain water contaminated by microorganisms is short due to a short high-temperature holding time at the beginning of the treatment, the treatment time and the treatment temperature become sufficient while it is being reheated and circulated. When the treatment is completed, the drain water can be surely sterilized.

【0030】これにより、ドレン水を処理するための処
理設備が不要になるうえ、前述のようにドレン水は完全
に除菌された状態で流出することになるから、ドレン水
経路が微生物等で汚染されることもない。
This eliminates the need for a treatment facility for treating the drain water and, as described above, the drain water flows out in a completely sterilized state. There is no pollution.

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

【図1】図は本発明の一実施形態を示す概略構成図であ
る。
FIG. 1 is a schematic configuration diagram showing one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…内槽、2…外槽、3…滅菌缶、4…蒸気発生器、5
…加熱用蒸気コイル、7…排気系路、10…ジャケット、
16…処理室、18・19…除菌フィルター、23…真空ポンプ
部、26…ドレン路。
DESCRIPTION OF SYMBOLS 1 ... Inner tank, 2 ... Outer tank, 3 ... Sterilized can, 4 ... Steam generator, 5
... Steam coil for heating, 7 ... Exhaust system, 10 ... Jacket,
16: treatment chamber, 18/19: sanitizing filter, 23: vacuum pump section, 26: drain path.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 讃岐田 哲 大阪府大阪市平野区加美東6丁目1番27号 株式会社讃岐田製作所内 Fターム(参考) 4C058 AA12 BB05 CC04 CC07 DD02 DD04 EE12 EE26  ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Satoshi Sankita 6-27 Kamihigashi, Hirano-ku, Osaka City, Osaka Prefecture F-term (reference) 4C058 AA12 BB05 CC04 CC07 DD02 DD04 EE12 EE26

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 処理対象物である被滅菌物を収容する処
理室(16)を構成する内槽(1)と、内槽(1)の外側にジャ
ケット(10)を介して位置している外槽(2)とで滅菌缶
(3)を構成し、この滅菌缶(3)の下側に蒸気発生器(4)
を直結状に接近配置し、蒸気発生器(4)を内槽(1)の底
部に連通接続し、内槽(1)の上部から導出した排気系路
(7)中に複数の除菌フィルター(18)(19)を直列に配置
し、蒸気発生器(4)に加熱用蒸気コイル(5)を配置する
とともに、この蒸気発生器(4)に精製水を供給可能に構
成し、内槽(1)内を真空ポンプ(23)に連通接続させてあ
る蒸気滅菌装置。
1. An inner tank (1) constituting a processing chamber (16) for accommodating an object to be processed, which is an object to be sterilized, and is located outside the inner tank (1) via a jacket (10). Sterilized can with outer tank (2)
(3) and a steam generator (4) below the sterilization can (3).
And the steam generator (4) is connected to the bottom of the inner tank (1), and the exhaust line is drawn out from the upper part of the inner tank (1).
A plurality of sterilizing filters (18) and (19) are arranged in series in (7), a heating steam coil (5) is arranged in a steam generator (4), and purification is performed on the steam generator (4). A steam sterilizer configured to be able to supply water and having the inside of the inner tank (1) connected to a vacuum pump (23).
【請求項2】 二重構造に形成した滅菌缶(3)の内外槽
体間に形成したジャケット(10)に蒸気を送給してジャケ
ット(10)内が所定の圧力に達するまで加熱し、ジャケッ
ト(10)内が所定の圧力に達すると内槽(1)で形成した処
理室(16)内を所定時間減圧し、処理室(16)内の減圧が完
了すると、滅菌缶(3)の下側に直結状に配置した蒸気発
生器(4)内に精製水を所定の水位まで供給し、精製水が
所定水位に達すると、蒸気発生器(4)内に配置した加熱
用蒸気コイル(5)に加熱用蒸気を流通させて蒸気発生器
(4)内の精製水で発生した水蒸気を滅菌缶(3)の処理室
(16)内に送給して処理室(16)内を蒸気飽和状態に維持
し、被滅菌物との接触によって凝縮したドレン水を蒸気
発生器(4)に返送して再蒸気化させるようにし、処理室
(16)の内圧が加圧状態になると、排気系路(7)から直列
配置した複数の除菌フィルター(18)(19)を通して排気
し、排気系路(7)での下流側に配置した除菌フィルター
(19)の温度が所定温度に達した後、予め設定した時間が
経過するまで蒸気加熱を継続し、設定時間経過後に蒸気
発生器(4)のドレン路(26)を開通させて、蒸気発生器
(4)から貯留水を抜き取るとともに、処理室(16)の内圧
を降下させ、その後処理室(16)を真空ポンプ(23)に連通
させた減圧状態と、処理室(16)に大気を導入した大気圧
状態で所定時間保持する状態とを数回繰り返して真空乾
燥させるようにしたことを特徴とする蒸気滅菌方法。
2. Steam is supplied to a jacket (10) formed between the inner and outer tank bodies of the sterilization can (3) formed in a double structure, and heated until the inside of the jacket (10) reaches a predetermined pressure, When the pressure in the jacket (10) reaches a predetermined pressure, the pressure in the processing chamber (16) formed by the inner tank (1) is reduced for a predetermined time, and when the pressure in the processing chamber (16) is completed, the sterilization can (3) is removed. Purified water is supplied to a predetermined water level into a steam generator (4) arranged directly below, and when the purified water reaches a predetermined water level, a heating steam coil ( 5) Heating steam is passed through the steam generator
(4) The steam generated by the purified water in the sterilization can (3)
(16) to maintain the inside of the processing chamber (16) in a steam-saturated state, and to return the drain water condensed by contact with the object to be sterilized to the steam generator (4) for re-vaporization. And processing room
When the internal pressure of (16) is in a pressurized state, the air is exhausted from the exhaust system (7) through a plurality of sterilization filters (18) and (19) arranged in series, and arranged downstream of the exhaust system (7). Disinfection filter
After the temperature of (19) reaches the predetermined temperature, the steam heating is continued until a preset time elapses, and after the elapse of the set time, the drain path (26) of the steam generator (4) is opened to generate steam. vessel
Withdrawing the stored water from (4), reducing the internal pressure of the processing chamber (16), and then reducing the pressure by connecting the processing chamber (16) to the vacuum pump (23), and introducing air into the processing chamber (16). A method of maintaining the atmospheric pressure for a predetermined period of time, and repeating vacuum drying several times.
JP2000287835A 2000-09-22 2000-09-22 Vapor sterilizer and vapor sterilizing method Pending JP2002095723A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000287835A JP2002095723A (en) 2000-09-22 2000-09-22 Vapor sterilizer and vapor sterilizing method

Publications (1)

Publication Number Publication Date
JP2002095723A true JP2002095723A (en) 2002-04-02

Family

ID=18771516

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
JP (1) JP2002095723A (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6250643U (en) * 1985-09-20 1987-03-28
JPS62102929U (en) * 1985-12-18 1987-06-30
JPH04265191A (en) * 1991-05-30 1992-09-21 Aoki Corp Sterilizing equipment in drainage system
JPH06190024A (en) * 1992-12-22 1994-07-12 Nippon Metal Ind Co Ltd Method and apparatus for high-pressure steam sterilization
JPH0713338U (en) * 1993-08-06 1995-03-07 末子 長田 Steam sterilizer
JPH09285527A (en) * 1996-04-25 1997-11-04 Miura Co Ltd Steam sterilizer
JPH105316A (en) * 1996-06-25 1998-01-13 ▲高▼崎科学器械株式会社 Autoclave
JP2001178798A (en) * 1999-12-24 2001-07-03 Miura Co Ltd Steam sterilizer and operation method therefor

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6250643U (en) * 1985-09-20 1987-03-28
JPS62102929U (en) * 1985-12-18 1987-06-30
JPH04265191A (en) * 1991-05-30 1992-09-21 Aoki Corp Sterilizing equipment in drainage system
JPH06190024A (en) * 1992-12-22 1994-07-12 Nippon Metal Ind Co Ltd Method and apparatus for high-pressure steam sterilization
JPH0713338U (en) * 1993-08-06 1995-03-07 末子 長田 Steam sterilizer
JPH09285527A (en) * 1996-04-25 1997-11-04 Miura Co Ltd Steam sterilizer
JPH105316A (en) * 1996-06-25 1998-01-13 ▲高▼崎科学器械株式会社 Autoclave
JP2001178798A (en) * 1999-12-24 2001-07-03 Miura Co Ltd Steam sterilizer and operation method therefor

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