JP4508094B2 - Sterilization system - Google Patents

Sterilization system Download PDF

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JP4508094B2
JP4508094B2 JP2005347596A JP2005347596A JP4508094B2 JP 4508094 B2 JP4508094 B2 JP 4508094B2 JP 2005347596 A JP2005347596 A JP 2005347596A JP 2005347596 A JP2005347596 A JP 2005347596A JP 4508094 B2 JP4508094 B2 JP 4508094B2
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air
sterilization
hydrogen peroxide
processing chamber
passage
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JP2007130404A (en
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義弘 佐々木
芳和 平野
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Daikin Industries Ltd
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Daikin Industries Ltd
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/16Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
    • A61L2/20Gaseous substances, e.g. vapours
    • A61L2/208Hydrogen peroxide
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/20Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/20Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation
    • F24F8/24Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation using sterilising media
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2202/00Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
    • A61L2202/10Apparatus features
    • A61L2202/12Apparatus for isolating biocidal substances from the environment
    • A61L2202/122Chambers for sterilisation
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2202/00Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
    • A61L2202/20Targets to be treated
    • A61L2202/21Pharmaceuticals, e.g. medicaments, artificial body parts

Description

本発明は、処理室を過酸化水素で滅菌処理する滅菌システムに関するものである。   The present invention relates to a sterilization system for sterilizing a processing chamber with hydrogen peroxide.

従来より、この種の滅菌システムとしては、密閉可能な処理室(例えば医薬品製造室)に、該処理室の気体を吸引する真空ポンプが設けられた気体吸引通路と、過酸化水素蒸気を発生させる過酸化水素発生器が設けられた過酸化水素供給通路と、処理空間内に無菌空気を供給する空気供給通路と、処理室内の気体を循環させながら触媒で過酸化水素を分解する気体循環通路とが接続されたシステムがある(例えば、特許文献1参照)。   Conventionally, as a sterilization system of this type, a gas-suction passage provided with a vacuum pump for sucking a gas in the processing chamber in a sealable processing chamber (for example, a pharmaceutical manufacturing chamber) and hydrogen peroxide vapor are generated. A hydrogen peroxide supply passage provided with a hydrogen peroxide generator, an air supply passage for supplying sterile air into the processing space, and a gas circulation passage for decomposing hydrogen peroxide with a catalyst while circulating the gas in the processing chamber; Are connected to each other (for example, see Patent Document 1).

この特許文献1の滅菌システムでは、まず真空ポンプを起動して処理室を真空状態にした後、過酸化水素を処理室内に供給して滅菌処理を行う。次に、空気供給通路から処理室に無菌空気を導入し、過酸化水素を処理室内に分散させる。そして、真空ポンプによる吸引工程、過酸化水素の供給工程、及び無菌空気の導入工程を数回繰り返して処理室の滅菌が終了すると、処理室から過酸化水素を除去する工程を行う。この工程では、気体循環通路の触媒により過酸化水素を分解しながら処理室の気体を循環させる。こうすることにより、処理室内の過酸化水素濃度を下げるようにしている。
特開平10−328276号公報
In the sterilization system disclosed in Patent Document 1, first, a vacuum pump is activated to evacuate a processing chamber, and then hydrogen peroxide is supplied into the processing chamber to perform sterilization. Next, aseptic air is introduced into the processing chamber from the air supply passage, and hydrogen peroxide is dispersed in the processing chamber. Then, when the sterilization of the processing chamber is completed by repeating the suction step by the vacuum pump, the hydrogen peroxide supply step, and the sterile air introduction step several times, the step of removing hydrogen peroxide from the processing chamber is performed. In this step, the gas in the processing chamber is circulated while decomposing hydrogen peroxide by the catalyst in the gas circulation passage. By doing so, the hydrogen peroxide concentration in the processing chamber is lowered.
JP-A-10-328276

ところで、上記の滅菌システムは、空調設備とは別個独立して微小風量が循環する設備として設けられている。そして、上記滅菌システムでは、多風量の気体の循環が可能な空調設備を停止した状態で微小風量の循環により滅菌処理を行うため、滅菌ガス(過酸化水素を含む空気)の室内拡散効果不良による滅菌性能のばらつきや、滅菌後に室内の過酸化水素濃度を下げて定常運転を行えるようになるまでに長時間を要するなど、様々な問題があった。   By the way, the above-described sterilization system is provided as a facility for circulating a small amount of air independently from an air conditioning facility. In the sterilization system, since the air-conditioning equipment capable of circulating a large amount of gas is stopped and the sterilization process is performed by circulating a small amount of air, the sterilization gas (air containing hydrogen peroxide) has a poor indoor diffusion effect. There were various problems such as variations in sterilization performance and a long time required for steady operation by lowering the hydrogen peroxide concentration in the room after sterilization.

本発明は、かかる点に鑑みてなされたものであり、その目的は、過酸化水素を用いて処理室の滅菌を行うシステムにおいて、滅菌性能の向上や滅菌後の後処理時間(過酸化水素の希釈時間)の短縮を可能にすることである。   The present invention has been made in view of the above points, and an object of the present invention is to improve the sterilization performance and the post-treatment time after sterilization (hydrogen peroxide concentration) in a system for sterilizing a processing chamber using hydrogen peroxide. (Dilution time) can be shortened.

第1の発明は、処理室(2)内の空調と滅菌処理とを行う滅菌システム(1)を前提としている。   1st invention presupposes the sterilization system (1) which performs the air conditioning and sterilization in a process chamber (2).

そして、この滅菌システム(1)は、外気の温度と湿度を調節するとともに処理室(2)に給気通路(11)と還気通路(12)を介して接続された外気処理空調機(13)と、給気通路(11)から処理室(2)への空気の入口に設けられたHEPAフィルタなどのフィルタ機構(14)と、還気通路(12)から給気通路(11)に戻し通路(15)を接続することにより構成された空調側循環通路(16)と、上記空調側循環通路(16)に設けられた顕熱空調機(17)と、上記処理室(2)に接続され、過酸化水素発生器(31)を備えた滅菌側循環通路(32)と、上記外気処理空調機(13)から滅菌側循環通路(32)に外気を導入する給気側連通路(39)と、滅菌側循環通路(32)において過酸化水素発生器(31)と並列に接続された過酸化水素分解器(36)と、過酸化水素分解器(36)を外気処理空調機(13)の還気通路(12)に接続する還気側連通路(38)と、を備えていることを特徴としている。   The sterilization system (1) regulates the temperature and humidity of the outside air and is connected to the processing chamber (2) through the air supply passage (11) and the return air passage (12). ), A filter mechanism (14) such as a HEPA filter provided at the air inlet from the air supply passage (11) to the processing chamber (2), and the return air passage (12) to the air supply passage (11). Connected to the air conditioning side circulation passage (16) configured by connecting the passage (15), the sensible heat air conditioner (17) provided in the air conditioning side circulation passage (16), and the processing chamber (2) A sterilization side circulation passage (32) provided with a hydrogen peroxide generator (31), and an air supply side communication passage (39) for introducing outside air from the outside air treatment air conditioner (13) to the sterilization side circulation passage (32). ), A hydrogen peroxide decomposer (36) connected in parallel with the hydrogen peroxide generator (31) in the sterilization side circulation passage (32), and hydrogen peroxide The return air side communication passage connecting to the return air passage of the solution vessel (36) outside air processing air conditioner (13) (12) (38), is characterized in that it comprises a.

この第1の発明では、外気処理空調機(13)と顕熱空調機(17)とフィルタ機構(14)とを備えた空調系統側の回路(10)と、過酸化水素発生器(31)と過酸化水素分解器(36)とを備えた滅菌系統側の回路(30)とを設けるとともに、空調系統側回路(10)と滅菌系統側回路(30)とを給気側連通路(39)と還気側連通路(38)によって接続している。したがって、後述の第4の発明に記載しているように、過酸化水素発生器(31)を停止した状態で、外気処理空調機(13)により処理室(2)の湿度を所定値以下に低下させる準備運転と、過酸化水素発生器(31)により発生した過酸化水素(過酸化水素の蒸気)を滅菌側循環通路(32)で循環させることにより処理室(2)に過酸化水素を所定濃度となるように供給する滅菌運転と、過酸化水素発生器(31)を停止して処理室(2)のガスを滅菌側循環通路(32)で循環させながら過酸化水素分解器(36)で過酸化水素濃度が第1の設定値以下になるまで分解する第1希釈運転と、外気処理空調機(13)からフィルタ機構(14)を介して空気を処理室(2)に供給しながら過酸化水素濃度が第1の設定値よりも低い第2の設定値以下になるまで排気を行う第2希釈運転と、外気処理空調機(13)により処理した外気を取り入れながら空調側循環通路(16)で顕熱空調機(17)を介して空調空気を循環させる定常運転と、を一連の動作として連続して行うことができる。第2希釈運転は、処理室(2)の空気(滅菌ガス)を大気中に放出しても影響が生じない過酸化水素濃度になったときに行う運転であり、このとき、外気処理空調機(13)及び顕熱空調機(17)からの大風量の空気で処理室(2)内の滅菌ガスを希釈できる。   In the first aspect of the invention, an air conditioning system circuit (10) including an outside air processing air conditioner (13), a sensible heat air conditioner (17), and a filter mechanism (14), and a hydrogen peroxide generator (31) And a circuit (30) on the sterilization system side provided with a hydrogen peroxide decomposer (36), and an air supply side communication path (39) between the air conditioning system side circuit (10) and the sterilization system side circuit (30). ) And the return air communication passage (38). Therefore, as described in the fourth invention described later, with the hydrogen peroxide generator (31) stopped, the outside air processing air conditioner (13) reduces the humidity of the processing chamber (2) to a predetermined value or less. Preparation operation to reduce, and hydrogen peroxide (hydrogen peroxide vapor) generated by the hydrogen peroxide generator (31) is circulated in the sterilization side circulation passage (32), so that hydrogen peroxide is supplied to the treatment chamber (2). Sterilization operation to supply a predetermined concentration, hydrogen peroxide generator (31) is stopped, and hydrogen peroxide decomposer (36) is circulated through the sterilization side circulation passage (32) through the gas in the processing chamber (2). ) In the first dilution operation that decomposes until the hydrogen peroxide concentration falls below the first set value, and air is supplied from the outside air treatment air conditioner (13) to the treatment chamber (2) via the filter mechanism (14). However, exhaust until the hydrogen peroxide concentration falls below the second set value, which is lower than the first set value. The second dilution operation and the steady operation of circulating the conditioned air through the sensible heat air conditioner (17) in the air conditioning side circulation passage (16) while taking in the outside air treated by the outside air treatment air conditioner (13) The operation can be performed continuously. The second dilution operation is an operation that is performed when the concentration of hydrogen peroxide that does not affect the release of air (sterilization gas) in the processing chamber (2) to the atmosphere is reached. The sterilization gas in the processing chamber (2) can be diluted with a large amount of air from (13) and the sensible heat air conditioner (17).

第2の発明は、第1の発明において、処理室(2)内の圧力を調整する圧力調整機構(25)が設けられていることを特徴としている。   The second invention is characterized in that, in the first invention, a pressure adjusting mechanism (25) for adjusting the pressure in the processing chamber (2) is provided.

この第2の発明では、滅菌運転、第1希釈運転、及び第2希釈運転などを行うときに、それぞれの運転に適した室内圧力を維持することができる。   In this 2nd invention, when performing sterilization operation, 1st dilution operation, 2nd dilution operation, etc., the room pressure suitable for each operation can be maintained.

第3の発明は、第1または第2の発明において、滅菌側循環通路(32)における処理室(2)への入口側が給気通路(11)のフィルタ機構(14)に接続されていることを特徴としている。   According to a third invention, in the first or second invention, the inlet side to the processing chamber (2) in the sterilization side circulation passage (32) is connected to the filter mechanism (14) of the air supply passage (11). It is characterized by.

この第3の発明では、滅菌運転時に処理室(2)の室内へ供給される過酸化水素がHEPAフィルタなどのフィルタ機構(14)を通過する。このため、フィルタ機構(14)に捕捉されている菌類を該フィルタ機構(14)上で死滅させることができる。   In the third aspect of the invention, the hydrogen peroxide supplied into the processing chamber (2) during the sterilization operation passes through the filter mechanism (14) such as a HEPA filter. For this reason, the fungi captured by the filter mechanism (14) can be killed on the filter mechanism (14).

第4の発明は、第1,第2または第3の発明において、運転制御を行う制御手段(50)を備え、該制御手段(50)が、過酸化水素発生器(31)を停止した状態で、外気処理空調機(13)により処理室(2)の湿度を所定値以下に低下させる準備運転と、過酸化水素発生器(31)により発生した過酸化水素(過酸化水素の蒸気)を滅菌側循環通路(32)で循環させることにより処理室(2)に過酸化水素を所定濃度となるように供給する滅菌運転と、過酸化水素発生器(31)を停止して処理室(2)のガスを滅菌側循環通路(32)で循環させながら過酸化水素分解器(36)で過酸化水素濃度が第1の設定値以下になるまで分解する第1希釈運転と、外気処理空調機(13)からフィルタ機構(14)を介して空気を処理室(2)に供給しながら過酸化水素濃度が第1の設定値よりも低い第2の設定値以下になるまで排気を行う第2希釈運転と、外気処理空調機(13)により処理した外気を取り入れながら空調側循環通路(16)で顕熱空調機(17)を介して空調空気を循環させる定常運転と、を行うことが可能に構成されていることを特徴としている。   According to a fourth invention, in the first, second or third invention, a control means (50) for controlling operation is provided, and the control means (50) stops the hydrogen peroxide generator (31). The preparation operation to reduce the humidity of the processing chamber (2) below a predetermined value by the outside air processing air conditioner (13) and the hydrogen peroxide (hydrogen peroxide vapor) generated by the hydrogen peroxide generator (31) Sterilization operation in which hydrogen peroxide is supplied to the treatment chamber (2) to a predetermined concentration by circulating it through the sterilization side circulation passage (32), and the hydrogen peroxide generator (31) is stopped and the treatment chamber (2 ) Gas in the sterilization side circulation passage (32), the hydrogen peroxide decomposer (36) decomposes until the hydrogen peroxide concentration falls below the first set value, and the outside air treatment air conditioner While supplying air from the (13) to the processing chamber (2) through the filter mechanism (14), the hydrogen peroxide concentration The sensible heat air conditioning in the air conditioning side circulation passage (16) while taking in the outside air treated by the outside air treatment air conditioner (13) and the second dilution operation that exhausts until the second set value lower than the set value of 1 or less And a steady operation in which conditioned air is circulated through a machine (17).

この第4の発明では、準備運転時の処理室(2)の湿度、滅菌運転時の処理室(2)内の過酸化水素濃度、第1希釈運転時の過酸化水素濃度(第1の設定値)、及び第2希釈運転時の過酸化水素濃度(第2の設定値)などを制御手段(50)において予め設定しておくことにより、準備運転と滅菌運転と第1希釈運転と第2希釈運転と定常運転とからなる一連の運転動作を自動的に効率よく行うことができる。   In the fourth invention, the humidity of the processing chamber (2) during the preparatory operation, the hydrogen peroxide concentration in the processing chamber (2) during the sterilization operation, the hydrogen peroxide concentration during the first dilution operation (first setting) Value) and the hydrogen peroxide concentration (second set value) at the time of the second dilution operation are set in advance in the control means (50), so that the preparatory operation, the sterilization operation, the first dilution operation, the second A series of operation operations including a dilution operation and a steady operation can be performed automatically and efficiently.

第5の発明は、第4の発明において、滅菌運転時における処理室(2)の室内湿度上昇時または室内圧力上昇時に、過酸化水素分解器(36)から還気側連通路(38)を通じて処理室(2)のガスを外気処理空調機(13)に還気するように構成されていることを特徴としている。   According to a fifth invention, in the fourth invention, when the indoor humidity of the processing chamber (2) during the sterilization operation increases or when the indoor pressure increases, the hydrogen peroxide decomposer (36) passes through the return air side communication passage (38). It is configured to return the gas in the processing chamber (2) to the outside air processing air conditioner (13).

この第5の発明では、滅菌運転時に処理室(2)に過酸化水素を供給することによって室内湿度が上昇したり室内圧力が上昇したりすると、過酸化水素分解器(36)で過酸化水素を分解したガスを外気処理空調機(13)に還気する。また、外気処理空調機(13)からは、湿度と風量を調節した空気を滅菌側循環通路(32)に戻すことができるので、処理室(2)の湿度や圧力を調節できる。   According to the fifth aspect of the present invention, when hydrogen peroxide is supplied to the treatment chamber (2) during sterilization operation to increase the indoor humidity or the indoor pressure, the hydrogen peroxide decomposer (36) The gas decomposed is returned to the outside air treatment air conditioner (13). Moreover, since the air which adjusted humidity and the air volume can be returned to the sterilization side circulation path (32) from the outside air processing air conditioner (13), the humidity and pressure of the processing chamber (2) can be adjusted.

第6の発明は、第4の発明において、第1希釈運転時における処理室(2)の圧力低下時に、外気処理空調機(13)から空調空気を滅菌側循環通路(32)に供給するように構成されていることを特徴としている。   According to a sixth aspect, in the fourth aspect, when the pressure in the processing chamber (2) is reduced during the first dilution operation, the conditioned air is supplied from the outside air processing air conditioner (13) to the sterilization side circulation passage (32). It is characterized by being configured.

この第6の発明では、第1希釈運転時に、滅菌システムまたは滅菌側循環通路(32)と処理室(2)内の過酸化水素が減量したときや、処理室(2)から空調系統側回路(10)へ滅菌ガスの漏れが生じたときなどに、外気処理空調機(13)から空調空気を滅菌側循環通路(32)に供給することにより、圧力が低下しすぎるのを防止できる。   In the sixth aspect of the invention, during the first dilution operation, when the amount of hydrogen peroxide in the sterilization system or the sterilization side circulation passage (32) and the processing chamber (2) is reduced, or from the processing chamber (2) to the air conditioning system side circuit When sterilization gas leaks to (10), the pressure can be prevented from dropping too much by supplying the conditioned air from the outside air processing air conditioner (13) to the sterilization side circulation passage (32).

第7の発明は、第4の発明において、第2希釈運転時に、外気処理空調機(13)と顕熱空調機(17)からフィルタ機構(14)を介して処理室(2)に空調空気を供給するとともに処理室(2)のガスを排気しながら、該処理室(2)のガスの一部を空調側循環通路(16)で循環させることを特徴としている。   In a seventh aspect based on the fourth aspect, in the second dilution operation, the conditioned air is supplied from the outside air processing air conditioner (13) and the sensible heat air conditioner (17) to the processing chamber (2) via the filter mechanism (14). And a part of the gas in the processing chamber (2) is circulated in the air conditioning side circulation passage (16) while exhausting the gas in the processing chamber (2).

この第7の発明では、空調系統側回路(10)を使って処理室(2)の還気のみを行うのではなく、処理室(2)のガスの一部を循環させながら滅菌ガスの希釈を行うことができる。   In the seventh aspect of the invention, not only the return air of the processing chamber (2) is performed using the air conditioning system side circuit (10), but the sterilizing gas is diluted while circulating a part of the gas in the processing chamber (2). It can be performed.

上記第1,第2,第3,第4,第5,第6,第7の発明によれば、外気処理空調機(13)と顕熱空調機(17)とフィルタ機構(14)とを備えた空調系統側の回路(10)と、過酸化水素発生器(31)と過酸化水素分解器(36)とを備えた滅菌系統側の回路(30)とを設けるとともに、空調系統側回路(10)と滅菌系統側回路(30)とを給気側連通路(39)と還気側連通路(38)によって接続したことにより、準備運転と滅菌運転と第1希釈運転と第2希釈運転と定常運転とを一連の動作として連続して行うことができる。そして、第2希釈運転時に、外気処理空調機(13)及び顕熱空調機(17)からの大風量の空気で処理室(2)内の滅菌ガスを希釈できるため、過酸化水素の室内拡散効果不良による滅菌性能のばらつきを防止できるとともに、定常運転を行うまで長時間を要する問題も防止できる。また、過酸化水素を使った滅菌システム(1)では処理室(2)内を低湿度に保つことが滅菌効果を高めるために重要であるが、本発明では空調系統側回路(10)の外気処理空調機(13)により処理室(2)の湿度を前もって調節できるので、高い滅菌効果を期待できる。   According to the first, second, third, fourth, fifth, sixth and seventh inventions, the outside air processing air conditioner (13), the sensible heat air conditioner (17), and the filter mechanism (14) are provided. The air conditioning system side circuit (10) and the sterilization system side circuit (30) including the hydrogen peroxide generator (31) and the hydrogen peroxide decomposer (36) are provided, and the air conditioning system side circuit (10) and the sterilization system side circuit (30) are connected by the supply side communication path (39) and the return air side communication path (38), so that the preparation operation, the sterilization operation, the first dilution operation, and the second dilution are performed. Operation and steady operation can be performed continuously as a series of operations. During the second dilution operation, the sterilization gas in the treatment chamber (2) can be diluted with a large amount of air from the outside air treatment air conditioner (13) and the sensible heat air conditioner (17), so that hydrogen peroxide diffuses indoors. In addition to preventing variations in sterilization performance due to poor effects, it is also possible to prevent problems that require a long time for steady operation. In the sterilization system (1) using hydrogen peroxide, keeping the inside of the processing chamber (2) at a low humidity is important for enhancing the sterilization effect. In the present invention, the outside air of the air conditioning system side circuit (10) is used. Since the humidity of the processing chamber (2) can be adjusted beforehand by the processing air conditioner (13), a high sterilization effect can be expected.

上記第2の発明によれば、処理室(2)内の圧力を調整する圧力調整機構(25)を設けたことにより、滅菌運転、第1希釈運転、及び第2希釈運転などを行うときに、それぞれの運転に適した室内圧力を維持することができるため、滅菌運転や希釈運転を効率よく行うことができる。   According to the second aspect of the present invention, when the sterilization operation, the first dilution operation, the second dilution operation, and the like are performed by providing the pressure adjustment mechanism (25) for adjusting the pressure in the processing chamber (2). Since the indoor pressure suitable for each operation can be maintained, sterilization operation and dilution operation can be performed efficiently.

上記第3の発明によれば、滅菌側循環通路(32)における処理室(2)への入口側を給気通路(11)のフィルタ機構(14)に接続したことにより、滅菌運転時に処理室(2)の室内へ供給される過酸化水素がHEPAフィルタなどのフィルタ機構(14)を通過する。したがって、フィルタ機構(14)に捕捉されている菌類を該フィルタ機構(14)上で死滅させることができるので、滅菌効率が向上する。   According to the third aspect of the invention, the inlet side to the processing chamber (2) in the sterilization side circulation passage (32) is connected to the filter mechanism (14) of the air supply passage (11), so that the processing chamber can be used during sterilization operation. Hydrogen peroxide supplied into the room of (2) passes through a filter mechanism (14) such as a HEPA filter. Therefore, since the fungi captured by the filter mechanism (14) can be killed on the filter mechanism (14), the sterilization efficiency is improved.

上記第4の発明によれば、準備運転時の処理室(2)の湿度、滅菌運転時の処理室(2)内の過酸化水素濃度、第1希釈運転時の過酸化水素濃度、及び第2希釈運転時の過酸化水素濃度などを制御手段(50)において予め設定しておくことにより、準備運転と滅菌運転と第1希釈運転と第2希釈運転と定常運転とからなる一連の運転動作を自動的に効率よく行うことができる。   According to the fourth aspect, the humidity of the processing chamber (2) during the preparation operation, the hydrogen peroxide concentration in the processing chamber (2) during the sterilization operation, the hydrogen peroxide concentration during the first dilution operation, By setting the hydrogen peroxide concentration and the like at the time of two dilution operations in advance in the control means (50), a series of operation operations including a preparation operation, a sterilization operation, a first dilution operation, a second dilution operation, and a steady operation. Can be performed automatically and efficiently.

上記第5の発明によれば、滅菌運転時に処理室(2)に過酸化水素を供給することによって室内湿度が上昇したり室内圧力が上昇したりすると、過酸化水素分解器(36)で過酸化水素を分解したガスを外気処理空調機(13)に還気し、外気処理空調機(13)から湿度と風量を調節した空気を滅菌側循環通路(32)に戻すことができるので、処理室(2)の湿度や圧力を滅菌処理に適した値に調節することができる。   According to the fifth aspect of the present invention, when hydrogen peroxide is supplied to the processing chamber (2) during sterilization operation and the indoor humidity increases or the indoor pressure increases, the hydrogen peroxide decomposer (36) The gas decomposed hydrogen oxide is returned to the outside air treatment air conditioner (13), and the air whose humidity and air volume are adjusted from the outside air treatment air conditioner (13) can be returned to the sterilization side circulation passage (32). The humidity and pressure of the chamber (2) can be adjusted to values suitable for sterilization.

上記第6の発明によれば、第1希釈運転時に、滅菌システムまたは滅菌側循環通路(32)と処理室(2)内の過酸化水素が減量したときや、処理室(2)から空調系統側回路(10)へ滅菌ガスの漏れが生じたときなどに、外気処理空調機(13)から空調空気を滅菌側循環通路(32)に供給することにより、圧力が低下しすぎるのを防止できるので、第1希釈運転に適した圧力を維持して運転を行うことができる。   According to the sixth invention, when the amount of hydrogen peroxide in the sterilization system or the sterilization side circulation passage (32) and the processing chamber (2) is reduced during the first dilution operation, or from the processing chamber (2) to the air conditioning system. Supplying conditioned air from the outside air treatment air conditioner (13) to the sterilization side circulation passage (32) when sterilization gas leaks to the side circuit (10) can prevent the pressure from dropping too much. Therefore, the operation can be performed while maintaining a pressure suitable for the first dilution operation.

上記第7の発明によれば、第2希釈運転時に、外気処理空調機(13)と顕熱空調機(17)からフィルタ機構(14)を介して処理室(2)に空調空気を供給するとともに処理室(2)のガスを排気しながら、該処理室(2)のガスの一部を空調側循環通路(16)で循環させるようにしているので、均一な希釈効果を得ることができる。   According to the seventh aspect of the invention, during the second dilution operation, conditioned air is supplied from the outside air processing air conditioner (13) and the sensible heat air conditioner (17) to the processing chamber (2) via the filter mechanism (14). In addition, while exhausting the gas in the processing chamber (2), a part of the gas in the processing chamber (2) is circulated in the air conditioning side circulation passage (16), so that a uniform dilution effect can be obtained. .

以下、本発明の実施形態を図面に基づいて詳細に説明する。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

《発明の実施形態》
本発明の実施形態について説明する。
"Implementation-shaped state of the invention"
To describe the exemplary form status of the present invention.

−全体の構成−
この実施形態は、医薬品等の製造室を処理室として、該処理室内の空調と滅菌処理とを行う滅菌システムに関するものである。この実施形態の配管系統図である図1に示すように、この滅菌システム(1)は、空調系統側回路(10)と滅菌系統側回路(30)とを備えている。
-Overall configuration-
This embodiment relates to a sterilization system that performs air conditioning and sterilization processing in a processing room using a manufacturing room for pharmaceuticals or the like as a processing room. As shown in FIG. 1 which is a piping system diagram of this embodiment, the sterilization system (1) includes an air conditioning system side circuit (10) and a sterilization system side circuit (30).

この滅菌システム(1)の空調系統側回路(10)は、外気の温度と湿度を調節するとともに、処理室(2)に給気通路(11)と還気通路(12)を介して接続された外気処理空調機(13)を備えている。給気通路(11)から処理室(2)への空気の入口と、処理室(2)から還気通路(12)への空気の出口には、フィルタ機構としてHEPAフィルタ(high efficiency particulate air filter)(14)が設けられている。   The air conditioning system side circuit (10) of this sterilization system (1) regulates the temperature and humidity of the outside air, and is connected to the processing chamber (2) via the air supply passage (11) and the return air passage (12). The outside air processing air conditioner (13) is equipped. An air inlet from the supply passage (11) to the processing chamber (2) and an outlet from the processing chamber (2) to the return air passage (12) have a HEPA filter (high efficiency particulate air filter) as a filter mechanism. ) (14) is provided.

還気通路(12)と給気通路(11)との間には戻し通路(15)が接続されており、給気通路(11)の一部と還気通路(12)の一部と戻し通路(15)とにより、処理室(2)の空気が循環する空調側循環通路(16)が構成されている。この空調側循環通路(16)には、給気側に空気の温度調節のみを行う顕熱空調機(17)が設けられ、排気側に空気を循環させる循環ファン(18)が設けられている。また、戻し通路(15)と給気通路(11)の合流箇所にはミキシングチャンバ(19)が設けられている。   A return passage (15) is connected between the return air passage (12) and the supply air passage (11), and a part of the supply air passage (11) and a part of the return air passage (12) are returned. The passage (15) constitutes an air conditioning side circulation passage (16) through which the air in the processing chamber (2) circulates. The air conditioning side circulation passage (16) is provided with a sensible heat air conditioner (17) that only adjusts the temperature of air on the air supply side, and a circulation fan (18) that circulates air on the exhaust side. . Further, a mixing chamber (19) is provided at the junction of the return passage (15) and the air supply passage (11).

滅菌系統側回路(30)では、過酸化水素発生器(31)を備えた滅菌側循環通路(32)が上記処理室(2)に接続されている。過酸化水素発生器(31)は過酸化水素発生流路(33)に設けられ、過酸化水素発生流路(33)が滅菌側循環通路(32)の主流路(34)に対して並列に設けられている。主流路(34)側の風量と過酸化水素発生流路(33)側の風量の比率は、10:1程度になるように定められている。なお、過酸化水素発生器(31)とは、過酸化水素の水溶液を霧化等することによって過酸化水素の蒸気を発生させる装置である。   In the sterilization system side circuit (30), a sterilization side circulation passage (32) including a hydrogen peroxide generator (31) is connected to the processing chamber (2). The hydrogen peroxide generator (31) is provided in the hydrogen peroxide generation channel (33), and the hydrogen peroxide generation channel (33) is in parallel with the main channel (34) of the sterilization side circulation channel (32). Is provided. The ratio of the air volume on the main flow path (34) side and the air volume on the hydrogen peroxide generation flow path (33) side is determined to be about 10: 1. The hydrogen peroxide generator (31) is a device that generates hydrogen peroxide vapor by atomizing an aqueous solution of hydrogen peroxide.

滅菌側循環通路(32)には、過酸化水素発生流路(33)の上流側で分岐する過酸化水素分解流路(35)が設けられ、この過酸化水素分解流路(35)には過酸化水素分解器(36)が設けられている。過酸化水素分解流路(35)における過酸化水素分解器(36)の下流側は、滅菌側循環通路(32)に合流する循環側通路(37)と、外気処理空調機(13)の還気通路(12)に合流する還気側通路(還気側連通路)(38)とに分岐している。   The sterilization side circulation passage (32) is provided with a hydrogen peroxide decomposition passage (35) branched upstream of the hydrogen peroxide generation passage (33). The hydrogen peroxide decomposition passage (35) A hydrogen peroxide decomposer (36) is provided. The downstream side of the hydrogen peroxide decomposer (36) in the hydrogen peroxide decomposition channel (35) is the circulation side passage (37) joining the sterilization side circulation passage (32) and the return of the outside air treatment air conditioner (13). It branches into a return air side passage (return air side communication passage) (38) that joins the air passage (12).

上記滅菌側循環通路(32)における処理室(2)への入口側は給気通路(11)側のHEPAフィルタ(14)に接続され、該滅菌側循環通路(32)における処理室(2)からの出口側は還気通路(12)側のHEPAフィルタ(14)に接続されている。   The inlet side to the treatment chamber (2) in the sterilization side circulation passage (32) is connected to the HEPA filter (14) on the air supply passage (11) side, and the treatment chamber (2) in the sterilization side circulation passage (32). The outlet side of the air is connected to the HEPA filter (14) on the return air passage (12) side.

この滅菌システム(1)では、外気処理空調機(13)から滅菌側循環通路(32)に外気を導入する給気側連通路(39)と、過酸化水素分解器(36)を外気処理空調機(13)の還気通路(12)に接続する上述の還気側連通路(38)とが設けられている点を特徴としている。   In this sterilization system (1), the air supply side communication passage (39) for introducing outside air from the outside air treatment air conditioner (13) to the sterilization side circulation passage (32) and the hydrogen peroxide decomposer (36) It is characterized in that the return air side communication passage (38) connected to the return air passage (12) of the machine (13) is provided.

−詳細な構成−
次に、滅菌システム(1)の構成の詳細について説明する。
-Detailed configuration-
Next, details of the configuration of the sterilization system (1) will be described.

<空調系統側回路>
まず、空調系統側回路(10)の構成について説明する。
<Air conditioning system side circuit>
First, the configuration of the air conditioning system side circuit (10) will be described.

上記外気処理空調機(13)は、ケーシング内が隔壁(13a)により第1通路(13b)と第2通路(13c)に分離されており、空気中の水分を吸脱着可能な吸着剤を担持したハニカム状の吸着ロータ(13d)が、上記隔壁(13a)に沿って設けられた回転軸(図示せず)を中心として回転可能に設けられている。第1通路(13b)には、上流側から順に、第1外気取り入れ口(13e)、第1冷却コイル(13f)、上記吸着ロータ(13d)、第2冷却コイル(13g)、第1加熱コイル(13h)、加湿器(13i)、ファン(13j)、及び給気口(13k)が設けられている。第2通路(13c)には、第2外気取り入れ口(13l)、第2加熱コイル(13m)、吸着ロータ(13d)、及び排気口(13n)が設けられている。排気口(13n)は、図示しない排気ファンに接続されている。   The outside air processing air conditioner (13) is separated into a first passage (13b) and a second passage (13c) by a partition wall (13a), and carries an adsorbent capable of adsorbing and desorbing moisture in the air. The honeycomb-shaped adsorption rotor (13d) is provided to be rotatable about a rotation shaft (not shown) provided along the partition wall (13a). In the first passage (13b), in order from the upstream side, the first outside air intake (13e), the first cooling coil (13f), the adsorption rotor (13d), the second cooling coil (13g), the first heating coil (13h), a humidifier (13i), a fan (13j), and an air supply port (13k) are provided. The second passage (13c) is provided with a second outside air inlet (13l), a second heating coil (13m), an adsorption rotor (13d), and an exhaust port (13n). The exhaust port (13n) is connected to an exhaust fan (not shown).

第1通路(13b)では、第1冷却コイル(13f)により冷却された外気(第1空気)中の水分が吸着ロータ(13d)に吸着され、該第1空気が減湿される。第1空気はその後に第2冷却コイル(13g)、第1加熱コイル(13h)、及び加湿器(13i)により温度と湿度が調節され、給気口(13k)より吹き出される。吸着ロータ(13d)は連続的または断続的に回転しており、水分を吸着した部分がやがて第2通路(13c)内へ移動する。第2通路(13c)では、外気(第2空気)が第2加熱コイル(13m)で加熱されてから吸着ロータ(13d)を通過することにより、該吸着ロータ(13d)が再生される。吸着ロータ(13d)の再生された部分は、さらに回転して第1通路(13b)側へ移動することにより、再び第1空気を減湿することができるようになる。   In the first passage (13b), moisture in the outside air (first air) cooled by the first cooling coil (13f) is adsorbed by the adsorption rotor (13d), and the first air is dehumidified. Thereafter, the temperature and humidity of the first air are adjusted by the second cooling coil (13g), the first heating coil (13h), and the humidifier (13i), and the first air is blown out from the air supply port (13k). The adsorption rotor (13d) rotates continuously or intermittently, and the portion that has adsorbed moisture eventually moves into the second passage (13c). In the second passage (13c), outside air (second air) is heated by the second heating coil (13m) and then passes through the adsorption rotor (13d), whereby the adsorption rotor (13d) is regenerated. The regenerated portion of the adsorption rotor (13d) further rotates and moves toward the first passage (13b), so that the first air can be dehumidified again.

外気処理空調機(13)とミキシングチャンバ(19)との間の給気通路(11)には、中性能フィルタ(20)と、第1給気切換ダンパ(21a)とが設けられている。上記顕熱空調機(17)は、給気通路(11)におけるミキシングチャンバ(19)の下流側に設けられている。この顕熱空調機(17)は、上流側から順に、空気流入口(17a)、冷却コイル(17b)、ファン(17c)、及び空気流出口(17d)を有している。   A medium performance filter (20) and a first air supply switching damper (21a) are provided in the air supply passage (11) between the outside air processing air conditioner (13) and the mixing chamber (19). The sensible heat air conditioner (17) is provided downstream of the mixing chamber (19) in the air supply passage (11). The sensible heat air conditioner (17) includes an air inlet (17a), a cooling coil (17b), a fan (17c), and an air outlet (17d) in this order from the upstream side.

処理室(2)は、3部屋の医薬品製造室(2a,2b,2c)から構成され、各医薬品製造室(2a,2b,2c)に対する給気通路(11)の接続部分に給気側のHEPAフィルタ(14)が設けられている。給気通路(11)は各HEPAフィルタ(14)に対応して3本の給気管(11a,11b,11c)に分岐し、各給気管(11a,11b,11c)には、上流側から定風量装置(22a,22b,22c)と給気側気密ダンパ(23a,23b,23c)とが設けられている。   The treatment room (2) consists of three drug manufacturing rooms (2a, 2b, 2c), and the supply side is connected to the supply passage (11) for each drug manufacturing room (2a, 2b, 2c). A HEPA filter (14) is provided. The air supply passage (11) branches to three air supply pipes (11a, 11b, 11c) corresponding to each HEPA filter (14), and each air supply pipe (11a, 11b, 11c) is fixed from the upstream side. An air volume device (22a, 22b, 22c) and an air supply side airtight damper (23a, 23b, 23c) are provided.

各医薬品製造室(2a,2b,2c)に対する還気通路(12)の接続部分には、還気側のHEPAフィルタ(14)が設けられている。還気通路(12)は各HEPAフィルタ(14)に対応して3本の還気管(12a,12b,12c)に分岐し、各還気管(12a,12b,12c)には、上流側から還気側気密ダンパ(24a,24b,24c)と室圧制御ダンパ(25a,25b,25c)とが設けられている。この室圧制御ダンパ(25a,25b,25c)により、処理室(2)内の圧力を調整する圧力調整機構(25)が構成されている。   A return air-side HEPA filter (14) is provided at the connection portion of the return air passage (12) to each pharmaceutical manufacturing room (2a, 2b, 2c). The return air passage (12) branches into three return air pipes (12a, 12b, 12c) corresponding to each HEPA filter (14), and returns to each return air pipe (12a, 12b, 12c) from the upstream side. Air-side airtight dampers (24a, 24b, 24c) and room pressure control dampers (25a, 25b, 25c) are provided. The chamber pressure control dampers (25a, 25b, 25c) constitute a pressure adjusting mechanism (25) that adjusts the pressure in the processing chamber (2).

還気通路(12)には、各還気管(12a,12b,12c)の合流箇所の下流側に上記循環ファン(18)が設けられている。また、還気通路(12)における循環ファン(18)と戻し通路(15)の間には還気調節ダンパ(26)が設けられ、該還気通路(12)における戻し通路(15)と外気処理空調機(13)の間には還気切換ダンパ(27)が設けられている。   In the return air passage (12), the circulation fan (18) is provided on the downstream side of the junction of the return air pipes (12a, 12b, 12c). Further, a return air adjustment damper (26) is provided between the circulation fan (18) and the return passage (15) in the return air passage (12), and the return passage (15) in the return air passage (12) and the outside air A return air switching damper (27) is provided between the processing air conditioners (13).

外気処理空調機(13)の還気通路(12)は、循環ファン(18)と還気調節ダンパ(26)の間で分岐した排気通路(28)が設けられている。この排気通路(28)には、排気調節ダンパ(29)が設けられている。この排気調節ダンパ(29)を開くことにより、外気処理空調機(13)の運転中に処理室(2)内の圧力が上昇しすぎるのを防止できる。   The return air passage (12) of the outside air processing air conditioner (13) is provided with an exhaust passage (28) branched between the circulation fan (18) and the return air adjustment damper (26). The exhaust passage (28) is provided with an exhaust adjustment damper (29). By opening the exhaust control damper (29), it is possible to prevent the pressure in the processing chamber (2) from increasing excessively during the operation of the outside air processing air conditioner (13).

<滅菌系統側回路>
次に滅菌系統側回路(30)の構成について説明する。
<Sterilization system side circuit>
Next, the configuration of the sterilization system side circuit (30) will be described.

滅菌側循環通路(32)は、上記主流路(34)と、この主流路(34)から分岐した3本の給気側流路(40a,40b,40c)と、同じくこの主流路(34)から分岐した3本の還気側流路(41a,41b,41c)とを備えている。各給気側流路(40a,40b,40c)には給気側ガスバルブ(42a,42b,42c)が設けられ、還気側流路(41a,41b,41c)には還気側ガスバルブ(43a,43b,43c)が設けられている。主流路(34)には、還気側から給気側に向かって順に、滅菌ガス循環ファン(44)と第1滅菌ガス切換バルブ(45a)が設けられている。上記過酸化水素発生器(31)を備えた過酸化水素発生流路(33)は、第1滅菌ガス切換バルブ(45a)と各給気側流路(40a,40b,40c)の間において主流路(34)と並列に接続されている。   The sterilization side circulation passage (32) includes the main passage (34), three supply side passages (40a, 40b, 40c) branched from the main passage (34), and the main passage (34). And three return air flow paths (41a, 41b, 41c) branched from the. Each air supply side flow path (40a, 40b, 40c) is provided with an air supply side gas valve (42a, 42b, 42c), and the return air side flow path (41a, 41b, 41c) is provided with a return air side gas valve (43a , 43b, 43c). The main flow path (34) is provided with a sterilization gas circulation fan (44) and a first sterilization gas switching valve (45a) in order from the return air side to the air supply side. The hydrogen peroxide generation flow path (33) provided with the hydrogen peroxide generator (31) is mainstream between the first sterilization gas switching valve (45a) and each supply side flow path (40a, 40b, 40c). It is connected in parallel with the path (34).

滅菌ガス循環ファン(44)と第1滅菌ガス切換バルブ(45a)の間には上記過酸化水素分解流路(35)の一端が接続され、該過酸化水素分解流路(35)の他端は、主流路(34)における過酸化水素発生流路(33)の下流端と各給気側流路(40a,40b,40c)の間に接続されている。過酸化水素分解流路(35)には、その上流側から順に、第2滅菌ガス切換バルブ(45b)、過酸化水素分解器(36)であるPt触媒、及び第3滅菌ガス切換バルブ(45c)が設けられている。また、過酸化水素分解流路(35)は、過酸化水素分解器(36)とその下流側の第3滅菌ガス切換バルブ(45c)の間から分岐した上記還気側連通路(38)が外気処理空調機(13)の還気通路(12)に合流している。この還気側連通路(38)には、第4滅菌ガス切換バルブ(45d)が設けられている。   One end of the hydrogen peroxide decomposition channel (35) is connected between the sterilization gas circulation fan (44) and the first sterilization gas switching valve (45a), and the other end of the hydrogen peroxide decomposition channel (35). Is connected between the downstream end of the hydrogen peroxide generation flow path (33) in the main flow path (34) and the supply side flow paths (40a, 40b, 40c). In order from the upstream side to the hydrogen peroxide decomposition flow path (35), the second sterilization gas switching valve (45b), the Pt catalyst as the hydrogen peroxide decomposition device (36), and the third sterilization gas switching valve (45c) ) Is provided. The hydrogen peroxide decomposition flow path (35) includes the return air side communication path (38) branched from between the hydrogen peroxide decomposer (36) and the third sterilization gas switching valve (45c) on the downstream side. It joins the return air passage (12) of the outside air processing air conditioner (13). The return air side communication passage (38) is provided with a fourth sterilization gas switching valve (45d).

上記外気処理空調機(13)の給気通路(11)は、中性能フィルタ(20)と第1給気切換ダンパ(21a)の間で上記給気側連通路(39)に分岐している。この給気側連通路(39)は、滅菌側循環通路(32)の主流路(34)における還気側流路(41a,41b,41c)と滅菌ガス循環ファン(44)との間に接続されている。この給気側連通路(39)には、第2給気切換ダンパ(21b)が設けられている。   The air supply passage (11) of the outside air processing air conditioner (13) branches to the air supply side communication passage (39) between the medium performance filter (20) and the first air supply switching damper (21a). . This air supply side communication path (39) is connected between the return air side flow path (41a, 41b, 41c) and the sterilization gas circulation fan (44) in the main flow path (34) of the sterilization side circulation path (32). Has been. A second air supply switching damper (21b) is provided in the air supply side communication path (39).

−運転制御−
次に、この滅菌システム(1)の運転制御と具体的な運転動作に関して説明する。
-Operation control-
Next, operation control and specific operation of the sterilization system (1) will be described.

この滅菌システム(1)は、空調系統側回路(10)と滅菌系統側回路(30)の運転制御を行うコントローラ(制御手段)(50)を備えている。このコントローラ(50)は、処理室(2)を低湿度にするための準備運転と、処理室(2)内の滅菌処理を行う滅菌運転と、処理室(2)の滅菌完了後に過酸化水素濃度を下げるための希釈運転(第1希釈運転及び第2希釈運転)と、希釈完了後に処理室(2)の空調を行う定常運転とを行うように構成されている。滅菌運転前に処理室(2)を低湿度にする準備運転を行うのは、過酸化水素による滅菌を行う場合、処理室(2)内が低湿度である方が高い滅菌効果が得られるためである。   The sterilization system (1) includes a controller (control means) (50) for controlling the operation of the air conditioning system side circuit (10) and the sterilization system side circuit (30). This controller (50) is equipped with a preparatory operation for reducing the humidity of the processing chamber (2), a sterilization operation for sterilizing the processing chamber (2), and hydrogen peroxide after the sterilization of the processing chamber (2) is completed. A dilution operation (first dilution operation and second dilution operation) for lowering the concentration and a steady operation in which the air conditioning of the processing chamber (2) is performed after the dilution is completed are performed. The preparatory operation for lowering the processing chamber (2) before sterilization operation is because when sterilizing with hydrogen peroxide, the lower the humidity in the processing chamber (2), the higher the sterilization effect is obtained. It is.

<準備運転>
準備運転は、過酸化水素発生器(31)を停止した状態で、外気処理空調機(13)により処理室(2)の湿度を所定値以下に低下させる工程であり、後述の定常運転時の状態で外気導入量を約1/2とし、処理室(2)内を低湿にする運転である。なお、準備運転では、滅菌に備えて医薬品等の製造機器の開放と建具類の目張りが行われる。この準備運転の空気の流れを図2に示している。
<Preparation operation>
The preparatory operation is a step of reducing the humidity of the processing chamber (2) below a predetermined value by the outside air processing air conditioner (13) while the hydrogen peroxide generator (31) is stopped. In this state, the outside air introduction amount is reduced to about ½, and the inside of the processing chamber (2) is reduced in humidity. In preparation for sterilization, manufacturing equipment such as pharmaceuticals is opened and fixtures are glazed. The air flow in this preparation operation is shown in FIG.

このとき、滅菌系統側回路(30)では、滅菌ガス循環ファン(44)及び過酸化水素発生器(31)は停止した状態となる。また、滅菌系統側回路(30)の各バルブ(42a,42b,42c)(43a,43b,43c)(45a,45b,45c,45d)は閉じた状態となり、第2給気切換ダンパ(21b)も閉じた状態となる。一方、空調系統側回路(10)の第1給気切換ダンパ(21a)、還気切換ダンパ(27)、還気調節ダンパ(26)、各定風量装置(22a,22b,22c)、各室圧制御ダンパ(25a,25b,25c)、各給気側気密ダンパ(23a,23b,23c)、及び各還気側気密ダンパ(24a,24b,24c)はそれぞれ開いた状態となり、排気調節ダンパ(29)は閉じた状態となる。   At this time, in the sterilization system side circuit (30), the sterilization gas circulation fan (44) and the hydrogen peroxide generator (31) are stopped. Moreover, each valve | bulb (42a, 42b, 42c) (43a, 43b, 43c) (45a, 45b, 45c, 45d) of the sterilization system side circuit (30) will be in the closed state, and the 2nd air supply switching damper (21b) Is also closed. On the other hand, the first air supply switching damper (21a), the return air switching damper (27), the return air adjusting damper (26), each constant air volume device (22a, 22b, 22c), each room of the air conditioning system side circuit (10) The pressure control dampers (25a, 25b, 25c), the air supply side airtight dampers (23a, 23b, 23c), and the return air side airtight dampers (24a, 24b, 24c) are opened, and the exhaust control dampers ( 29) is closed.

この状態で、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)を運転すると、外気処理空調機(13)で温度と湿度が調節された空気が給気通路(11)を流れるときにミキシングチャンバ(19)、顕熱空調機(17)を順に通過し、低湿の空気が各給気管(11a,11b,11c)から給気側のHEPAフィルタ(14)を介して処理室(2)に供給される。   In this state, when the outside air processing air conditioner (13), the sensible heat air conditioner (17), and the circulation fan (18) are operated, the air whose temperature and humidity are adjusted by the outside air processing air conditioner (13) is supplied to the air supply passage. When passing through (11), it passes through the mixing chamber (19) and sensible heat air conditioner (17) in order, and low-humidity air passes through the HEPA filter (14) on the supply side from each supply pipe (11a, 11b, 11c). To the processing chamber (2).

処理室(2)の空気は排気側のHEPAフィルタ(14)を通って流出し、各還気管(12a,12b,12c)から還気通路(12)で合流し、循環ファン(18)により、一部がミキシングチャンバ(19)を通って顕熱空調機(17)へ、他の一部が外気処理空調機(13)へ送られる。準備運転は、空気を以上のように循環させて、処理室(2)内の室温が約25℃、相対湿度が約30%になるまで行われる。なお、処理室(2)内には、温度と湿度を検出するため、温度センサと湿度センサが設けられている。   The air in the processing chamber (2) flows out through the HEPA filter (14) on the exhaust side, joins in each return air pipe (12a, 12b, 12c) in the return air passage (12), and is circulated by the circulation fan (18). A part is sent to the sensible heat air conditioner (17) through the mixing chamber (19), and the other part is sent to the outside air processing air conditioner (13). The preparatory operation is performed until the room temperature in the processing chamber (2) is about 25 ° C. and the relative humidity is about 30% by circulating air as described above. In the processing chamber (2), a temperature sensor and a humidity sensor are provided to detect temperature and humidity.

<滅菌運転>
準備運転が完了すると、空調機器を停止し、ダンパ類の設定を切り換えて滅菌運転に移行する。滅菌運転は、過酸化水素発生器(31)により発生した過酸化水素の蒸気を滅菌系統側回路(30)の滅菌側循環通路(32)で循環させることにより処理室(2)に所定濃度の過酸化水素を含むガスを供給する工程である。この滅菌運転時の滅菌ガスの流れを図3に示している。
<Sterilization operation>
When the preparatory operation is completed, the air conditioner is stopped, the damper settings are switched, and the sterilization operation is started. In sterilization operation, the hydrogen peroxide vapor generated by the hydrogen peroxide generator (31) is circulated in the sterilization side circulation passage (32) of the sterilization system side circuit (30), so that the treatment chamber (2) has a predetermined concentration. This is a step of supplying a gas containing hydrogen peroxide. The flow of sterilization gas during this sterilization operation is shown in FIG.

このとき、空調系統側回路(10)では、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)が停止し、各給気切換ダンパ(21a,21b)、還気切換ダンパ(27)、還気調節ダンパ(26)、及び排気調節ダンパ(29)が閉鎖される。また、各定風量装置(22a,22b,22c)、各室圧制御ダンパ(25a,25b,25c)、各給気側気密ダンパ(23a,23b,23c)、各還気側気密ダンパ(24a,24b,24c)も停止または閉鎖される。一方、滅菌系統側回路(30)では、滅菌ガス循環ファン(44)及び過酸化水素発生器(31)が運転され、各給気側ガスバルブ(42a,42b,42c)と各還気側ガスバルブ(43a,43b,43c)が開かれる。また、第1滅菌ガス切換バルブ(45a)は開放され、第2滅菌ガス切換バルブ(45b)、第3滅菌ガス切換バルブ(45c)、第4滅菌ガス切換バルブ(45d)は閉鎖される。   At this time, in the air conditioning system side circuit (10), the outside air processing air conditioner (13), the sensible heat air conditioner (17), and the circulation fan (18) are stopped, and the air supply switching dampers (21a, 21b), return The air switching damper (27), the return air adjusting damper (26), and the exhaust adjusting damper (29) are closed. Also, each constant air volume device (22a, 22b, 22c), each chamber pressure control damper (25a, 25b, 25c), each air supply side airtight damper (23a, 23b, 23c), each return air side airtight damper (24a, 24b, 24c) are also stopped or closed. On the other hand, in the sterilization system side circuit (30), the sterilization gas circulation fan (44) and the hydrogen peroxide generator (31) are operated, and each supply side gas valve (42a, 42b, 42c) and each return air side gas valve ( 43a, 43b, 43c) is opened. The first sterilization gas switching valve (45a) is opened, and the second sterilization gas switching valve (45b), the third sterilization gas switching valve (45c), and the fourth sterilization gas switching valve (45d) are closed.

この状態で、滅菌ガス循環ファン(44)と過酸化水素発生器(31)を運転すると、過酸化水素発生器(31)で発生した過酸化水素の蒸気が主流路(34)の空気と合流して滅菌ガスとなり、給気側流路(40a,40b,40c)から給気側のHEPAフィルタ(14)を通って処理室(2)に供給される。   When the sterilization gas circulation fan (44) and the hydrogen peroxide generator (31) are operated in this state, the hydrogen peroxide vapor generated by the hydrogen peroxide generator (31) joins the air in the main flow path (34). The sterilized gas is supplied to the processing chamber (2) from the supply side flow path (40a, 40b, 40c) through the supply side HEPA filter (14).

処理室(2)内の滅菌ガスは還気側のHEPAフィルタ(14)を通って流出し、各還気側流路(41a,41b,41c)から主流路(34)で合流する。合流した滅菌ガスは滅菌ガス循環ファン(44)により一部が過酸化水素発生流路(33)を流れ、残りが主流路(34)を流れる。上述したように、主流路(34)を流れる風量と過酸化水素発生流路(33)を流れる風量の比率は、約10:1に設定されている。こうすることにより、過酸化水素を空気中で十分に拡散させ、ひいては処理室(2)内で均一に拡散させる効果を得ることができる。   The sterilizing gas in the processing chamber (2) flows out through the HEPA filter (14) on the return air side, and merges from each return air side channel (41a, 41b, 41c) in the main channel (34). Part of the combined sterilized gas flows through the hydrogen peroxide generation flow path (33) and the rest flows through the main flow path (34) by the sterilization gas circulation fan (44). As described above, the ratio of the amount of air flowing through the main channel (34) and the amount of air flowing through the hydrogen peroxide generating channel (33) is set to about 10: 1. By doing so, it is possible to obtain an effect of sufficiently diffusing hydrogen peroxide in the air and thus uniformly in the processing chamber (2).

一方、過酸化水素の蒸気の発生に伴う室内圧力の上昇をコントロールするため、処理室(2)内には圧力センサ(図示せず)が設けられている。そして、滅菌運転中に処理室(2)の室内圧力が上昇したり、室内湿度が上昇したりすると、図に太い破線で流れを示すように、過酸化水素分解流路(35)の過酸化水素分解器(36)から還気側連通路(38)を通じて、処理室(2)のガスの一部を分解してから外気処理空調機(13)に還気する。過酸化水素分解器(36)を通して滅菌ガスを外気処理空調機に戻すのは、外気処理空調機やダクト類の腐食を防止するためである。   On the other hand, a pressure sensor (not shown) is provided in the processing chamber (2) in order to control an increase in the indoor pressure accompanying the generation of hydrogen peroxide vapor. When the chamber pressure in the processing chamber (2) increases or the chamber humidity increases during the sterilization operation, the hydrogen peroxide decomposition channel (35) is peroxidized as shown by the thick broken line in the figure. A part of the gas in the processing chamber (2) is decomposed from the hydrogen decomposer (36) through the return air side communication passage (38) and then returned to the outside air processing air conditioner (13). The reason why the sterilized gas is returned to the outside air treatment air conditioner through the hydrogen peroxide decomposer (36) is to prevent corrosion of the outside air treatment air conditioner and ducts.

この運転時、第2滅菌ガス切換バルブ(45b)と第4滅菌ガス切換バルブ(45d)が開かれ、外気処理空調機(13)が運転される。そして、第2給気切換ダンパ(21b)を開いて、外気処理空調機(13)により湿度を調節した空気の風量を調節しながら滅菌側循環通路(32)に戻すことで、室内湿度や室内圧力を調節できる。処理室(2)内の湿度が上昇し、結露が生じたりすると滅菌効果が著しく低下するため、室内湿度の上限は例えば約50%に設定される。なお、処理室(2)の室圧上昇を防止するだけであれば、処理室(2)の滅菌ガスを過酸化水素分解器(36)で分解してから外気処理空調機(13)を通じて外気に放出してもよい。   During this operation, the second sterilization gas switching valve (45b) and the fourth sterilization gas switching valve (45d) are opened, and the outside air processing air conditioner (13) is operated. Then, the second air supply switching damper (21b) is opened and returned to the sterilization side circulation passage (32) while adjusting the air volume of the humidity adjusted by the outside air processing air conditioner (13). The pressure can be adjusted. If the humidity in the processing chamber (2) increases and condensation occurs, the sterilization effect is significantly reduced, so the upper limit of the indoor humidity is set to about 50%, for example. If it is only necessary to prevent an increase in the chamber pressure in the processing chamber (2), the sterilization gas in the processing chamber (2) is decomposed by the hydrogen peroxide decomposer (36) and then passed through the outside air treatment air conditioner (13). May be released.

滅菌運転は、ガスを滅菌側循環通路(32)によって以上のように循環させて、処理室(2)の過酸化水素濃度が約500ppmになり、その濃度で所定時間が経過するまで行われる。なお、過酸化水素濃度を検出するため、滅菌側循環通路(32)の還気側には過酸化水素濃度センサが設けられている(図示せず)。   The sterilization operation is performed until the hydrogen peroxide concentration in the processing chamber (2) reaches about 500 ppm by circulating the gas as described above through the sterilization side circulation passage (32), and a predetermined time elapses at that concentration. In order to detect the hydrogen peroxide concentration, a hydrogen peroxide concentration sensor (not shown) is provided on the return air side of the sterilization side circulation passage (32).

<希釈運転>
滅菌運転の完了後、処理室(2)内の過酸化水素濃度は約500ppmになっている。この高濃度の状態では、外気処理空調機(13)、顕熱空調機(17)、HEPAフィルタ(14)で処理をした無菌空気を処理室(2)に導入するとともに処理室(2)のガスを室外へ放出することはできないので、処理室(2)内の過酸化水素濃度が5〜10ppm程度になるまでは過酸化水素を触媒により分解する第1希釈運転を行う(図4)。その後、外気処理空調機(13)、顕熱空調機(17)、HEPAフィルタ(14)で処理をした無菌空気を処理室(2)に導入するとともに処理室(2)のガスを室外へ放出する第2希釈運転を行う(図5)。第2希釈運転時に室外へ放出される滅菌ガスの過酸化水素濃度は十分に低いので、大気中への影響はない。
<Dilution operation>
After completion of the sterilization operation, the hydrogen peroxide concentration in the processing chamber (2) is about 500 ppm. In this high-concentration state, aseptic air treated with the outside air processing air conditioner (13), sensible heat air conditioner (17), and HEPA filter (14) is introduced into the processing chamber (2) and the processing chamber (2) Since the gas cannot be released outside, the first dilution operation is performed in which the hydrogen peroxide is decomposed by the catalyst until the hydrogen peroxide concentration in the processing chamber (2) reaches about 5 to 10 ppm (FIG. 4). After that, aseptic air treated with the outside air processing air conditioner (13), sensible heat air conditioner (17), and HEPA filter (14) is introduced into the processing chamber (2) and the gas in the processing chamber (2) is released to the outside. The second dilution operation is performed (FIG. 5). Since the hydrogen peroxide concentration of the sterilizing gas released to the outside during the second dilution operation is sufficiently low, there is no influence on the atmosphere.

(第1希釈運転)
第1希釈運転は、過酸化水素発生器(31)を停止して処理室(2)のガスを滅菌側循環通路(32)で循環させながら過酸化水素分解器(36)で過酸化水素濃度が第1の設定値(5〜10ppm)以下になるまで分解する工程であり、図4に空気の流れを示している。
(First dilution operation)
In the first dilution operation, the hydrogen peroxide generator (31) is stopped and the gas in the treatment chamber (2) is circulated in the sterilization side circulation passage (32) while the hydrogen peroxide concentration is increased in the hydrogen peroxide decomposer (36). Is a step of decomposing until the first set value (5 to 10 ppm) or less is reached, and FIG. 4 shows the air flow.

このとき、空調系統側回路(10)の設定は基本的に滅菌運転時と同じであり、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)は停止しており、各ダンパ(21a,21b)(23a,23b,23c)(24a,24b,24c)(25a,25b,25c)(26)(27)(29)や定風量装置(22a,22b,22c)などは閉鎖または停止している。一方、滅菌系統側回路(30)では、滅菌ガス循環ファン(44)は運転されるが過酸化水素発生器(31)が停止し、各給気側ガスバルブ(42a,42b,42c)と各還気側ガスバルブ(43a,43b,43c)は開かれたままである。また、第1滅菌ガス切換バルブ(45a)は閉鎖され、第2滅菌ガス切換バルブ(45b)及び第3滅菌ガス切換バルブ(45c)は開放され、第4滅菌ガス切換バルブ(45d)は閉鎖される。   At this time, the setting of the air conditioning system side circuit (10) is basically the same as in the sterilization operation, and the outside air processing air conditioner (13), the sensible heat air conditioner (17), and the circulation fan (18) are stopped. Each damper (21a, 21b) (23a, 23b, 23c) (24a, 24b, 24c) (25a, 25b, 25c) (26) (27) (29) and constant air volume devices (22a, 22b, 22c) Etc. are closed or stopped. On the other hand, in the sterilization system side circuit (30), the sterilization gas circulation fan (44) is operated but the hydrogen peroxide generator (31) is stopped, and each supply side gas valve (42a, 42b, 42c) and each return The gas side gas valves (43a, 43b, 43c) remain open. The first sterilization gas switching valve (45a) is closed, the second sterilization gas switching valve (45b) and the third sterilization gas switching valve (45c) are opened, and the fourth sterilization gas switching valve (45d) is closed. The

この状態で、滅菌ガス循環ファン(44)を運転すると、処理室(2)内の空気が滅菌側循環通路(32)を循環する際に過酸化水素分解器(36)を通過し、滅菌ガス中の過酸化水素が分解される。第1希釈運転は、過酸化水素濃度センサによる検出値(過酸化水素濃度)が5〜10ppmになるまで行われる。   When the sterilization gas circulation fan (44) is operated in this state, the air in the processing chamber (2) passes through the hydrogen peroxide decomposer (36) when circulating through the sterilization side circulation passage (32), and the sterilization gas Hydrogen peroxide inside is decomposed. The first dilution operation is performed until the detection value (hydrogen peroxide concentration) by the hydrogen peroxide concentration sensor becomes 5 to 10 ppm.

なお、第1希釈運転時に各給気側気密ダンパ(23a,23b,23c)や各還気側気密ダンパ(24a,24b,24c)からの滅菌ガスの漏れ等が生じて処理室(2)の圧力が低下した場合には、図に太い破線で流れを示すように、外気処理空調機(13)を運転するとともに第2給気切換ダンパ(21b)を開き、処理室(2)内を所定圧力(例えば数10Pa)に維持する操作を行う。   During the first dilution operation, sterilization gas leaks from the air supply side airtight dampers (23a, 23b, 23c) and the return air side airtight dampers (24a, 24b, 24c). When the pressure drops, as shown by the thick broken line in the figure, the outside air processing air conditioner (13) is operated and the second air supply switching damper (21b) is opened, and the inside of the processing chamber (2) is predetermined. An operation of maintaining the pressure (for example, several tens of Pa) is performed.

(第2希釈運転)
第2希釈運転は、外気処理空調機(13)からフィルタ機構である給気側のHEPAフィルタ(14)を介して空気を処理室(2)に供給しながら過酸化水素濃度が第1の設定値(5〜10ppm)よりも低い第2の設定値(1ppm)以下になるまで排気を行う換気工程である(図5)。この第2の設定値は、処理室(2)内に作業者が入室可能な濃度に設定されている。このように第2希釈運転で空調系統側回路(10)を使っているのは、滅菌系統側回路(30)での低風量の希釈運転(第1希釈運転)を続けたのでは過酸化水素濃度が第2の設定値に達するまでに相当長い時間を要するため、大風量での運転を行うこととしたものである。
(Second dilution operation)
In the second dilution operation, the hydrogen peroxide concentration is set to the first while supplying air from the outside air processing air conditioner (13) to the processing chamber (2) through the HEPA filter (14) on the supply side which is a filter mechanism. This is a ventilation process in which exhausting is performed until it becomes equal to or lower than a second set value (1 ppm) lower than the value (5 to 10 ppm) (FIG. 5). The second set value is set to a concentration at which an operator can enter the processing chamber (2). In this way, the air conditioning system side circuit (10) is used in the second dilution operation because the low air volume dilution operation (first dilution operation) in the sterilization system side circuit (30) is continued. Since a considerably long time is required for the concentration to reach the second set value, the operation is performed with a large air volume.

このとき、空調系統側回路(10)の設定と滅菌系統側回路(30)の設定は、基本的には準備運転と同じである。ただし、準備運転では還気調節ダンパ(26)が開放され、排気調節ダンパ(29)が閉鎖されていたのに対して、この第2希釈運転では還気調節ダンパ(26)が微小開度に設定され、排気調節ダンパ(29)が全開に近い開度に設定される。   At this time, the setting of the air conditioning system side circuit (10) and the setting of the sterilization system side circuit (30) are basically the same as the preparation operation. However, in the preparatory operation, the return air adjustment damper (26) was opened and the exhaust adjustment damper (29) was closed, whereas in the second dilution operation, the return air adjustment damper (26) was reduced to a small opening. The exhaust adjustment damper (29) is set to an opening close to full open.

この状態で、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)を運転すると、外気処理空調機(13)と顕熱空調機(17)で温度と湿度が調節され、給気側のHEPAフィルタ(14)で浄化された無菌空気が処理室(2)に供給され、処理室(2)内で滅菌ガスと均一に混合する。希釈された滅菌ガスは、還気側のHEPAフィルタ(14)を通って処理室(2)から流出する。この滅菌ガスは、排気調節ダンパ(29)を通って大部分が排気され、一部が還気調節ダンパ(26)を通ってミキシングチャンバ(19)へ流入した後に外気処理空調機(13)からの空調空気と混合され、さらに顕熱空調機(17)へと流れていく。   In this state, when the outside air treatment air conditioner (13), sensible heat air conditioner (17), and circulation fan (18) are operated, the temperature and humidity of the outside air treatment air conditioner (13) and sensible heat air conditioner (17) are reduced. Aseptic air that has been adjusted and purified by the HEPA filter (14) on the air supply side is supplied to the processing chamber (2) and is uniformly mixed with the sterilizing gas in the processing chamber (2). The diluted sterilization gas flows out of the processing chamber (2) through the HEPA filter (14) on the return air side. Most of this sterilized gas is exhausted through the exhaust control damper (29), and part of the sterilized gas flows into the mixing chamber (19) through the return air control damper (26) and then from the outside air processing air conditioner (13). It is mixed with the conditioned air and flows to the sensible heat air conditioner (17).

第2希釈運転では、空調空気及び滅菌ガスが以上のようにして循環することにより、処理室(2)の過酸化水素濃度が約1ppm以下になるまで行われる。排気調節ダンパ(29)が全開に近い開度に設定されているのは、室内圧力を建屋漏気上の対策により、定常値よりも低い圧力(例えば約15Pa)に保持するためである。   In the second dilution operation, the conditioned air and the sterilizing gas are circulated as described above until the hydrogen peroxide concentration in the processing chamber (2) is about 1 ppm or less. The reason why the exhaust control damper (29) is set to an opening degree close to full open is to keep the indoor pressure at a pressure (for example, about 15 Pa) lower than the steady value by measures against building air leakage.

なお、還気調節ダンパ(26)と排気調節ダンパ(29)の開度は運転状態に合わせて適宜変更してもよい。例えば、本実施形態では還気調節ダンパ(26)を微小開度に開いて滅菌ガスの一部を顕熱空調機(17)へ戻す(空調側循環通路(16)で循環させる)ようにしているが、必ずしも滅菌ガスの一部を顕熱空調機(17)へ戻さなくてもよい。 The opening degrees of the return air adjustment damper (26) and the exhaust adjustment damper (29) may be appropriately changed according to the operating state. For example, in this embodiment shaped state (circulating air conditioning side circulation path (16)) is opened to the minute opening the return air regulation damper (26) returning a portion of the sterilization gas sensible heat air conditioner to (17) so However, it is not always necessary to return a part of the sterilized gas to the sensible heat air conditioner (17).

また、第1希釈運転から第2希釈運転への移行時には、室圧の急激な変化を避けるため、外気処理空調機(13)、顕熱空調機(17)及び循環ファン(18)をスロースタートし、安定した移行を行うとよい。   Also, during the transition from the first dilution operation to the second dilution operation, the outside air processing air conditioner (13), the sensible heat air conditioner (17), and the circulation fan (18) are started slowly to avoid sudden changes in the room pressure. And make a stable transition.

<定常運転>
定常運転は、外気処理空調機(13)により処理した外気を取り入れながら空調側循環通路(16)で顕熱空調機(17)を介して空調空気を循環させる工程である。この定常運転の空気の流れを図6に示している。
<Normal operation>
The steady operation is a step of circulating the conditioned air through the sensible heat air conditioner (17) in the air conditioning side circulation passage (16) while taking in the outside air processed by the outside air processing air conditioner (13). The flow of air in this steady operation is shown in FIG.

このとき、空調系統側回路(10)の設定と滅菌系統側回路(30)の設定は、基本的には準備運転と同じである。ただし、準備運転では排気調節ダンパ(29)が閉鎖されていたのに対して、この定常運転では排気調節ダンパ(29)が所定開度に設定される。   At this time, the setting of the air conditioning system side circuit (10) and the setting of the sterilization system side circuit (30) are basically the same as the preparation operation. However, while the exhaust adjustment damper (29) is closed in the preparation operation, the exhaust adjustment damper (29) is set to a predetermined opening degree in this steady operation.

この状態で、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)を運転すると、外気処理空調機(13)と顕熱空調機(17)で温度と湿度が調節され、給気側のHEPAフィルタ(14)で浄化された無菌空気が処理室(2)に供給される。処理室(2)の無菌空気は、還気側のHEPAフィルタ(14)を通って処理室(2)から流出する。この無菌空気は、一部が排気調節ダンパ(29)を通って排気され、大部分が還気調節ダンパ(26)を通ってミキシングチャンバ(19)へ流入した後に外気処理空調機(13)からの空調空気と混合され、さらに顕熱空調機(17)へと流れていく。   In this state, when the outside air treatment air conditioner (13), sensible heat air conditioner (17), and circulation fan (18) are operated, the temperature and humidity of the outside air treatment air conditioner (13) and sensible heat air conditioner (17) are reduced. Aseptic air that has been adjusted and purified by the HEPA filter (14) on the supply side is supplied to the processing chamber (2). Aseptic air in the processing chamber (2) flows out of the processing chamber (2) through the HEPA filter (14) on the return air side. Part of this sterile air is exhausted through the exhaust control damper (29) and most of it enters the mixing chamber (19) through the return air control damper (26) and then from the outside air treatment air conditioner (13). It is mixed with the conditioned air and flows to the sensible heat air conditioner (17).

定常運転では、空調された無菌空気が空調系統側回路(10)で以上のようにして循環することにより、処理室(2)の温度と湿度が設定値に維持されるとともに、無菌状態が維持される。   In steady operation, air-conditioned sterile air circulates in the air-conditioning system side circuit (10) as described above, so that the temperature and humidity of the processing chamber (2) are maintained at the set values and the sterility is maintained. Is done.

−実施形態の効果−
本実施形態によれば、滅菌システム(1)に、外気処理空調機(13)と顕熱空調機(17)とHEPAフィルタ(14)とを備えた空調系統側回路(10)と、過酸化水素発生器(31)と過酸化水素分解器(36)とを備えた滅菌系統側回路(30)とを設けるとともに、空調系統側回路(10)と滅菌系統側回路(30)とを給気側連通路(39)と還気側連通路(38)によって接続したことにより、準備運転と滅菌運転と第1希釈運転と第2希釈運転と定常運転とを一連の動作として、自動的に効率よく行うことができる。そして、第2希釈運転時に、外気処理空調機(13)及び顕熱空調機(17)からの大風量の空気で処理室(2)内の滅菌ガスを希釈できるため、過酸化水素の室内拡散効果不良による滅菌性能のばらつきを防止できるとともに、定常運転を行うまで長時間を要する問題も防止できる。また、過酸化水素を使った滅菌システム(1)では、上述したように処理室(2)内を低湿度に保つことが滅菌効果を高めるために重要であるが、本実施形態では空調系統側回路(10)の外気処理空調機(13)により処理室(2)の湿度を前もって調節できるので、高い滅菌効果を期待できる。
- implementation-shaped state of the effect -
According to the present form condition, the sterilization system (1), outside air processing air conditioner (13) and the sensible heat air conditioner (17) and HEPA filter (14) and the air conditioning system side circuit having a (10), over A sterilization system side circuit (30) equipped with a hydrogen oxide generator (31) and a hydrogen peroxide decomposer (36) is provided, and an air conditioning system side circuit (10) and a sterilization system side circuit (30) are supplied. By connecting the air side communication passage (39) and the return air side communication passage (38), the preparatory operation, the sterilization operation, the first dilution operation, the second dilution operation, and the steady operation are automatically performed as a series of operations. It can be done efficiently. During the second dilution operation, the sterilization gas in the treatment chamber (2) can be diluted with a large amount of air from the outside air treatment air conditioner (13) and the sensible heat air conditioner (17), so that hydrogen peroxide diffuses indoors. In addition to preventing variations in sterilization performance due to poor effects, it is also possible to prevent problems that require a long time for steady operation. Further, the sterilization system using hydrogen peroxide (1), but to keep the process as described above chamber in (2) in a low humidity is important in order to enhance the sterilizing effect, the air conditioning in this embodiment shaped condition Since the humidity in the processing chamber (2) can be adjusted in advance by the outside air processing air conditioner (13) of the system side circuit (10), a high sterilization effect can be expected.

また、この実施形態では、処理室(2)内の圧力を調整する圧力調整機構(25)を設けているので、滅菌運転、第1希釈運転、及び第2希釈運転などを行うときに、それぞれの運転に適した室内圧力を維持することができるため、滅菌運転や希釈運転を効率よく行うことができる。 Further, in this embodiment shaped state, since there is provided a pressure adjusting mechanism for adjusting the pressure in the processing chamber (2) (25), sterilizing operation, a first dilution operation, and the like when performing a second dilution operation Since the indoor pressure suitable for each operation can be maintained, sterilization operation and dilution operation can be performed efficiently.

さらに、滅菌側循環通路(32)における処理室(2)への入口側を給気通路(11)側のHEPAフィルタ(14)に接続しているので、滅菌運転時に処理室(2)の室内へ供給される過酸化水素がHEPAフィルタ(14)を通過する。したがって、HEPAフィルタ(14)に捕捉されている菌類を該HEPAフィルタ(14)上で死滅させることができるので、滅菌効率が向上する。   Furthermore, since the inlet side to the processing chamber (2) in the sterilization side circulation passage (32) is connected to the HEPA filter (14) on the air supply passage (11) side, the chamber of the processing chamber (2) is sterilized. Hydrogen peroxide supplied to the water passes through the HEPA filter (14). Therefore, since the fungi captured by the HEPA filter (14) can be killed on the HEPA filter (14), the sterilization efficiency is improved.

また、滅菌運転時に処理室(2)に過酸化水素を供給することによって室内湿度が上昇したり室内圧力が上昇したりすると、過酸化水素分解器(36)で過酸化水素を分解したガスを外気処理空調機(13)に還気し、外気処理空調機(13)から湿度と風量を調節した空気を滅菌側循環通路(32)に戻すようにしているので、処理室(2)の湿度や圧力を滅菌処理に適した値に調節することができる。   In addition, if hydrogen peroxide is supplied to the treatment chamber (2) during sterilization operation and the indoor humidity increases or the indoor pressure increases, the hydrogen peroxide decomposer (36) decomposes the hydrogen peroxide gas. Returning air to the outside air treatment air conditioner (13) and returning the air with adjusted humidity and air volume from the outside air treatment air conditioner (13) to the sterilization side circulation passage (32), the humidity of the treatment room (2) And the pressure can be adjusted to values suitable for sterilization.

さらに、第1希釈運転時に処理室(2)から空調系統側回路(10)へ滅菌ガスの漏れが生じたときなどには、外気処理空調機(13)から空調空気を滅菌側循環通路(32)に供給することにより、圧力が低下しすぎるのを防止できるので、第1希釈運転に適した圧力を維持して運転を行うことができる。また、第2希釈運転時には、外気処理空調機(13)と顕熱空調機(17)からHEPAフィルタ(14)を介して処理室(2)に空調空気を供給するとともに処理室(2)のガスを排気しながら、該処理室(2)のガスの一部を空調側循環通路(16)で循環させるようにしているので、均一な希釈効果を得ることができる。   Further, when sterilization gas leaks from the processing chamber (2) to the air conditioning system side circuit (10) during the first dilution operation, the conditioned air is sent from the outside air processing air conditioner (13) to the sterilization side circulation passage (32 ), It is possible to prevent the pressure from dropping excessively, so that the operation can be performed while maintaining the pressure suitable for the first dilution operation. In addition, during the second dilution operation, conditioned air is supplied to the processing chamber (2) from the outside air processing air conditioner (13) and the sensible heat air conditioner (17) through the HEPA filter (14), and the processing chamber (2) Since a part of the gas in the processing chamber (2) is circulated in the air conditioning side circulation passage (16) while exhausting the gas, a uniform dilution effect can be obtained.

参考技術
参考技術について説明する。
Reference technology
Reference technology will be described.

−全体の構成−
この参考技術は、上記実施形態と同様に、医薬品等の製造室を処理室として、該処理室内の空調と滅菌処理とを行う滅菌システムに関するものである。この参考技術では、1室の処理室に対して滅菌システム(1)が構成されている。この参考技術の配管系統図である図7に示すように、この滅菌システム(1)は、空調系統側回路(10)と滅菌系統側回路(30)とを備えている。
-Overall configuration-
The reference technology, like on purpose above described type, as a processing chamber manufacturing chamber of pharmaceutical products, to a sterilization system for the sterilization and conditioning of the processing chamber. In this reference technique , a sterilization system (1) is configured for one processing chamber. As shown in FIG. 7 which is a piping system diagram of this reference technology, the sterilization system (1) includes an air conditioning system side circuit (10) and a sterilization system side circuit (30).

この滅菌システム(1)の空調系統側回路(10)は、処理室(2)の入口に接続された給気通路(11)と、処理室(2)の出口に接続された排気通路(28)とを備えている。給気通路(11)から処理室(2)への空気の入口と、処理室(2)から排気通路(28)への出口には、フィルタ機構としてHEPAフィルタ(high efficiency particulate air filter)(14)が設けられている。   The air conditioning system side circuit (10) of the sterilization system (1) includes an air supply passage (11) connected to the inlet of the processing chamber (2) and an exhaust passage (28 connected to the outlet of the processing chamber (2). ). An air inlet from the supply passage (11) to the processing chamber (2) and an outlet from the processing chamber (2) to the exhaust passage (28) have a high efficiency particulate air filter (HEPA filter) (14) as a filter mechanism. ) Is provided.

給気通路(11)と排気通路(28)との間には、処理室(2)内の空気を排気通路(28)から給気通路(11)へ戻すための戻し通路(15)が接続されている。そして、給気通路(11)の一部と還気通路(12)の一部と戻し通路(15)とにより、処理室(2)の空気が循環する空調側循環通路(16)が構成されている。なお、戻し通路(15)と給気通路(11)の合流箇所には、上記実施形態と同様に、ミキシングチャンバを設けてもよい。排気通路(28)には、戻し通路(15)との接続部の上流側に循環ファン(18)が設けられている。 A return passage (15) is connected between the air supply passage (11) and the exhaust passage (28) to return the air in the processing chamber (2) from the exhaust passage (28) to the air supply passage (11). Has been. The part of the air supply passage (11), the part of the return air passage (12) and the return passage (15) constitute an air conditioning side circulation passage (16) through which the air in the processing chamber (2) circulates. ing. Note that the merging portion of the return passage (15) and the supply passage (11), on purpose likewise the above-described type may be provided with a mixing chamber. In the exhaust passage (28), a circulation fan (18) is provided on the upstream side of the connection portion with the return passage (15).

給気通路(11)には、除湿器として構成された外気処理空調機(13)と、空気の温度調節のみを行う顕熱空調機(17)とが設けられている。外気処理空調機(13)及び顕熱空調機(17)は、空調装置を構成している。この外気処理空調機(13)は、上記実施形態のものと同様に、回転する吸着ロータ(13d)を用いて空気を除湿するものである。但し、本参考技術の外気処理空調機(13)では、第2冷却コイル(13g)、第1加熱コイル(13h)、及び加湿器(13i)が省略されている。他の構成は、上記実施形態のとほぼ同じであるため説明は省略する。なお、この外気処理空調機(13)では、外気取り入れ口(13e)と排気口(13n)とにそれぞれダクトが接続されており、外気取り入れ口(13e)側のダクトに中性能フィルタ(20)が設けられている。 The air supply passage (11) is provided with an outside air processing air conditioner (13) configured as a dehumidifier and a sensible heat air conditioner (17) that only adjusts the temperature of air. The outside air processing air conditioner (13) and the sensible heat air conditioner (17) constitute an air conditioner. The outside air processing air conditioner (13), similar to those of the above-described type condition, is to dehumidify air with adsorption rotor rotating (13d). However, in the outside air treatment air conditioner (13) of the present reference technology , the second cooling coil (13g), the first heating coil (13h), and the humidifier (13i) are omitted. Other configurations, explanation therefor is collected by almost the same of the above described type condition will be omitted. In this outside air processing air conditioner (13), ducts are connected to the outside air intake port (13e) and the exhaust port (13n), respectively, and the medium performance filter (20) is connected to the duct on the outside air intake port (13e) side. Is provided.

上記顕熱空調機(17)は、上流側から順に、空気流入口(17a)、冷却コイル(17b)、電気ヒータ(17e)、ファン(17c)、及び空気流出口(17d)を有している。この顕熱空調機(17)と外気処理空調機(13)と間には、中性能フィルタ(20)が設けられている。また、上記戻し通路(15)は、給気通路(11)における外気処理空調機(13)と中性能フィルタ(20)との間に接続されている。   The sensible heat air conditioner (17) has an air inlet (17a), a cooling coil (17b), an electric heater (17e), a fan (17c), and an air outlet (17d) in order from the upstream side. Yes. A medium performance filter (20) is provided between the sensible heat air conditioner (17) and the outside air processing air conditioner (13). The return passage (15) is connected between the outside air processing air conditioner (13) and the medium performance filter (20) in the air supply passage (11).

空調系統側回路(10)には、3つの空調ガス切換バルブ(56)が設けられている。具体的に、給気通路(11)における顕熱空調機(17)と処理室(2)との間には、第1空調ガス切換バルブ(56a)が設けられている。排気通路(28)における処理室(2)と循環ファン(18)との間には、第2空調ガス切換バルブ(56b)が設けられている。排気通路(28)における戻し通路(15)との接続部の下流側には、第3空調ガス切換バルブ(56c)が設けられている。   The air conditioning system side circuit (10) is provided with three air conditioning gas switching valves (56). Specifically, a first air-conditioning gas switching valve (56a) is provided between the sensible heat air conditioner (17) and the processing chamber (2) in the air supply passage (11). A second air conditioning gas switching valve (56b) is provided between the processing chamber (2) and the circulation fan (18) in the exhaust passage (28). A third air-conditioning gas switching valve (56c) is provided on the downstream side of the connection portion between the exhaust passage (28) and the return passage (15).

滅菌系統側回路(30)は、主流路(34)と、過酸化水素発生流路(33)と、過酸化水素分解流路(35)と、循環側通路(37)と、排気側通路(54)とを備えている。主流路(34)は、一端が給気通路(11)において第1空調ガス切換バルブ(56a)の下流に接続され、他端が排気通路(28)において第2空調ガス切換バルブ(56b)の上流に接続されている。これにより、給気通路(11)の一部と還気通路(12)の一部と主流路(34)とにより、処理室(2)の空気が循環する滅菌側循環通路(32)が構成されている。   The sterilization system side circuit (30) includes a main channel (34), a hydrogen peroxide generation channel (33), a hydrogen peroxide decomposition channel (35), a circulation side channel (37), and an exhaust side channel ( 54). One end of the main flow path (34) is connected downstream of the first air-conditioning gas switching valve (56a) in the air supply passage (11), and the other end is connected to the second air-conditioning gas switching valve (56b) in the exhaust passage (28). Connected upstream. As a result, a part of the supply air passage (11), a part of the return air passage (12) and the main flow path (34) constitute a sterilization side circulation passage (32) through which the air in the processing chamber (2) circulates. Has been.

主流路(34)には、滅菌側空調機(53)が設けられている。滅菌側空調機(53)は、上記顕熱空調機(17)と同じ構成で、顕熱空調機(17)よりも処理風量が小さい空調機である。滅菌側空調機(53)は、上流側から順に、空気流入口(53a)、冷却コイル(53b)、電気ヒータ(53e)、ファン(53c)、及び空気流出口(53d)を有している。なお、この参考技術の滅菌側空調機(53)は、その処理風量が顕熱空調機(17)よりも小さいが、顕熱空調機(17)以上であってもよい。 A sterilization side air conditioner (53) is provided in the main channel (34). The sterilization side air conditioner (53) is an air conditioner having the same configuration as the sensible heat air conditioner (17) and having a smaller processing air volume than the sensible heat air conditioner (17). The sterilization side air conditioner (53) has an air inlet (53a), a cooling coil (53b), an electric heater (53e), a fan (53c), and an air outlet (53d) in order from the upstream side. . The sterilization-side air conditioner (53) of this reference technique has a processing air volume smaller than that of the sensible heat air conditioner (17), but may be greater than or equal to the sensible heat air conditioner (17).

主流路(34)の滅菌側空調機(53)の上流部分には、上流側から順に過酸化水素分解流路(35)と循環側通路(37)と過酸化水素発生流路(33)とが接続されている。循環側通路(37)は、過酸化水素分解流路(35)から分岐している。すなわち、過酸化水素分解流路(35)及び循環側通路(37)からなる部分は、主流路(34)に対して並列になっている。   In the upstream part of the sterilization side air conditioner (53) of the main flow path (34), a hydrogen peroxide decomposition flow path (35), a circulation side path (37), and a hydrogen peroxide generation flow path (33) are arranged in order from the upstream side. Is connected. The circulation side passage (37) branches off from the hydrogen peroxide decomposition passage (35). That is, the portion composed of the hydrogen peroxide decomposition channel (35) and the circulation side channel (37) is in parallel with the main channel (34).

過酸化水素発生流路(33)は、滅菌ガス発生機(58)が設けられ、主流路(34)とは逆端が大気開放されている。滅菌ガス発生機(58)は、除湿器(57)と過酸化水素発生器(31)とを備えている。除湿器(57)は、室外から取り込んだ空気を除湿する。過酸化水素発生器(31)は、過酸化水素の水溶液を霧化等することにより過酸化水素の蒸気を発生させる。除湿器(57)で除湿するのは、低湿度の空気の方が過酸化水素が蒸発しやすいためである。この参考技術では、主流路(34)側の風量と過酸化水素発生流路(33)側の風量の比率が、10:1程度になるように定められている。 The hydrogen peroxide generation channel (33) is provided with a sterilization gas generator (58), and the end opposite to the main channel (34) is open to the atmosphere. The sterilization gas generator (58) includes a dehumidifier (57) and a hydrogen peroxide generator (31). The dehumidifier (57) dehumidifies the air taken from outside. The hydrogen peroxide generator (31) generates hydrogen peroxide vapor by atomizing an aqueous solution of hydrogen peroxide. The reason for dehumidifying with the dehumidifier (57) is that hydrogen in the low humidity air tends to evaporate. In this reference technique , the ratio of the air volume on the main channel (34) side and the air volume on the hydrogen peroxide generating channel (33) side is determined to be about 10: 1.

過酸化水素分解流路(35)は、主流路(34)側から過酸化水素分解器(36)であるPt触媒と排気ファン(55)とが設けられている。この過酸化水素分解流路(35)は、主流路(34)とは逆端が循環側通路(37)と排気側通路(54)とに分岐している。排気側通路(54)は、過酸化水素分解流路(35)とは逆端が大気開放されている。   The hydrogen peroxide decomposition channel (35) is provided with a Pt catalyst that is a hydrogen peroxide decomposer (36) and an exhaust fan (55) from the main channel (34) side. The hydrogen peroxide decomposition flow path (35) has an end opposite to the main flow path (34) branched into a circulation side passage (37) and an exhaust side passage (54). The exhaust-side passage (54) is open to the atmosphere at the end opposite to the hydrogen peroxide decomposition passage (35).

滅菌系統側回路(30)には、6つの滅菌ガス切換バルブ(45)が設けられている。具体的に、主流路(34)における過酸化水素分解流路(35)の接続部の上流側には、第1滅菌ガス切換バルブ(45a)が設けられている。過酸化水素分解流路(35)における過酸化水素分解器(36)の上流側には、第2滅菌ガス切換バルブ(45b)が設けられている。主流路(34)における過酸化水素分解流路(35)の接続部と循環側通路(37)の接続部との間には、第3滅菌ガス切換バルブ(45c)が設けられている。循環側通路(37)には、第4滅菌ガス切換バルブ(45d)が設けられている。過酸化水素発生流路(33)における滅菌ガス発生機(58)の下流側には、第5滅菌ガス切換バルブ(45e)が設けられている。主流路(34)における滅菌側空調機(53)の下流側には、第6滅菌ガス切換バルブ(45f)が設けられている。   The sterilization system side circuit (30) is provided with six sterilization gas switching valves (45). Specifically, a first sterilization gas switching valve (45a) is provided on the upstream side of the connection portion of the hydrogen peroxide decomposition channel (35) in the main channel (34). A second sterilization gas switching valve (45b) is provided upstream of the hydrogen peroxide decomposer (36) in the hydrogen peroxide decomposition channel (35). A third sterilization gas switching valve (45c) is provided between the connection part of the hydrogen peroxide decomposition flow path (35) and the connection part of the circulation side passage (37) in the main flow path (34). The circulation side passage (37) is provided with a fourth sterilization gas switching valve (45d). A fifth sterilization gas switching valve (45e) is provided on the downstream side of the sterilization gas generator (58) in the hydrogen peroxide generation flow path (33). A sixth sterilization gas switching valve (45f) is provided downstream of the sterilization side air conditioner (53) in the main channel (34).

−運転制御−
次に、この滅菌システム(1)の運転制御と具体的な運転動作に関して説明する。
-Operation control-
Next, operation control and specific operation of the sterilization system (1) will be described.

この滅菌システム(1)は、上記実施形態のと同様に、空調系統側回路(10)と滅菌系統側回路(30)の運転制御を行うコントローラ(制御手段)(50)を備えている。このコントローラ(50)は、準備運転と、滅菌運転と、希釈運転(第1希釈運転及び第2希釈運転)と、定常運転とを行うように構成されている。 The sterilization system (1), similar to the above-described type condition, and a controller which controls the operation of the air conditioning system side circuit (10) with a sterile system side circuit (30) (control means) (50). The controller (50) is configured to perform a preparation operation, a sterilization operation, a dilution operation (a first dilution operation and a second dilution operation), and a steady operation.

<準備運転>
準備運転は、滅菌ガス発生機(58)を停止した状態で、処理室(2)の湿度が目標湿度になるように外気処理空調機(13)によって処理室(2)の湿度を低下させる工程であり、外気導入量を後述の定常運転時の状態の約1/2とし、処理室(2)内を低湿にする運転である。準備運転では、処理室(2)の目標湿度が相対湿度で20%以上で30%以下の所定値に設定される。なお、目標湿度は20%以上で30%以下の範囲に限定されるものではなく、10%以上で50%以下の範囲であればよい。また、準備運転では、滅菌に備えて医薬品等の製造機器の開放と建具類の目張りが行われる。この準備運転の空気の流れを図8に示す。
<Preparation operation>
The preparatory operation is a process of reducing the humidity of the processing chamber (2) by the outside air processing air conditioner (13) so that the humidity of the processing chamber (2) becomes the target humidity with the sterilization gas generator (58) stopped. In this operation, the amount of outside air introduced is about ½ of the state in steady operation described later, and the inside of the processing chamber (2) is reduced in humidity. In the preparatory operation, the target humidity of the processing chamber (2) is set to a predetermined value of 20% to 30% relative humidity. Note that the target humidity is not limited to a range of 20% to 30%, and may be a range of 10% to 50%. Moreover, in preparation operation, in preparation for sterilization, a manufacturing apparatus, such as a pharmaceutical, is opened and the fittings are glazed. The flow of air in this preparation operation is shown in FIG.

このとき、空調系統側回路(10)の各バルブ(56a,56b,56c)は開いた状態となる。一方、滅菌系統側回路(30)の各バルブ(45a,45b,45c,45d,45e,45f)は閉じた状態となる。   At this time, each valve (56a, 56b, 56c) of the air conditioning system side circuit (10) is opened. On the other hand, each valve (45a, 45b, 45c, 45d, 45e, 45f) of the sterilization system side circuit (30) is closed.

この状態で、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)を運転すると、外気処理空調機(13)で除湿された空気が顕熱空調機(17)を通過して温度調節され、その温度調節された低湿の空気が入口側のHEPAフィルタ(14)を介して処理室(2)に供給される。   In this state, when the outside air processing air conditioner (13), the sensible heat air conditioner (17), and the circulation fan (18) are operated, the air dehumidified by the outside air processing air conditioner (13) is sensible heat air conditioner (17). The low-humidity air whose temperature is adjusted is supplied to the processing chamber (2) via the HEPA filter (14) on the inlet side.

処理室(2)の空気は、出口側のHEPAフィルタ(14)を通って流出して、循環ファン(18)により排気通路(28)を流通し、その一部が給気通路(11)へ戻って顕熱空調機(17)へ送られ、残りが排気通路(28)の出口から排気される。準備運転は、処理室(2)内の室温が25℃、相対湿度が所定値(例えば30%)になるまで行われる。なお、処理室(2)内には、温度と湿度を検出するため、温度センサと湿度センサが設けられている。   The air in the processing chamber (2) flows out through the HEPA filter (14) on the outlet side, circulates through the exhaust passage (28) by the circulation fan (18), and part of it flows to the air supply passage (11). It returns to the sensible heat air conditioner (17) and the remainder is exhausted from the outlet of the exhaust passage (28). The preparatory operation is performed until the room temperature in the processing chamber (2) reaches 25 ° C. and the relative humidity reaches a predetermined value (for example, 30%). In the processing chamber (2), a temperature sensor and a humidity sensor are provided to detect temperature and humidity.

<滅菌運転>
準備運転が完了すると、空調系統側回路(10)から処理室(2)への空気の供給を停止させるために、空調装置を構成する外気処理空調機(13)及び顕熱空調機(17)と循環ファン(18)とを停止し、バルブの設定を切り換えて滅菌運転に移行する。滅菌運転は、滅菌ガス発生機(58)から処理室(2)へ過酸化水素を供給することによって、処理室(2)内の過酸化水素の濃度を所定濃度(例えば500ppm)にして、その濃度の状態を所定時間に亘って維持する工程である。滅菌運転では、滅菌ガス発生機(58)の運転制御が、処理室(2)内の過酸化水素の濃度が所定濃度に到達するまでの調整モードと、所定濃度を維持するための滅菌モードとに分けられており、各モードにおいて処理室(2)への過酸化水素の供給量が調節される。なお、処理室(2)内の過酸化水素の濃度を検出するため、処理室(2)内には過酸化水素濃度センサが設けられている(図示せず)。この滅菌運転時の空気の流れを図9に示す。
<Sterilization operation>
When the preparatory operation is completed, in order to stop the supply of air from the air conditioning system side circuit (10) to the processing chamber (2), the outside air processing air conditioner (13) and the sensible heat air conditioner (17) that constitute the air conditioner And the circulation fan (18) are stopped, and the setting of the valve is switched to shift to the sterilization operation. The sterilization operation is performed by supplying hydrogen peroxide from the sterilization gas generator (58) to the processing chamber (2), thereby setting the concentration of hydrogen peroxide in the processing chamber (2) to a predetermined concentration (for example, 500 ppm). This is a step of maintaining the concentration state for a predetermined time. In sterilization operation, the operation control of the sterilization gas generator (58) includes an adjustment mode until the concentration of hydrogen peroxide in the processing chamber (2) reaches a predetermined concentration, and a sterilization mode for maintaining the predetermined concentration. In each mode, the supply amount of hydrogen peroxide to the processing chamber (2) is adjusted. In order to detect the concentration of hydrogen peroxide in the processing chamber (2), a hydrogen peroxide concentration sensor is provided in the processing chamber (2) (not shown). The air flow during this sterilization operation is shown in FIG.

このとき、空調系統側回路(10)の各バルブ(56a,56b,56c)は閉じた状態にする。一方、滅菌系統側回路(30)の各バルブは、第4滅菌ガス切換バルブ(45d)以外は開いた状態にする。   At this time, the valves (56a, 56b, 56c) of the air conditioning system side circuit (10) are closed. On the other hand, the valves of the sterilization system side circuit (30) are opened except for the fourth sterilization gas switching valve (45d).

この状態で、滅菌ガス発生機(58)、滅菌側空調機(53)、及び排気ファン(55)を運転すると、室外から取り込まれた空気が滅菌ガス発生機(58)へ送り込まれる。滅菌ガス発生機(58)へ流入した空気は、除湿器(57)で除湿された後に過酸化水素発生器(31)で過酸化酸素を付与される。そして、過酸化水素を含む空気(滅菌ガス)は、主流路(34)の空気と合流し、滅菌側空調機(53)で温度調節された後に入口側のHEPAフィルタ(14)を通って処理室(2)に供給される。上述したように、主流路(34)を流れる風量と過酸化水素発生流路(33)を流れる風量の比率は、約10:1に設定されている。こうすることにより、過酸化水素を空気中で十分に拡散させ、ひいては処理室(2)内で均一に拡散させる効果を得ることができる。   In this state, when the sterilization gas generator (58), the sterilization side air conditioner (53), and the exhaust fan (55) are operated, the air taken from outside is sent to the sterilization gas generator (58). The air flowing into the sterilization gas generator (58) is dehumidified by the dehumidifier (57) and then given oxygen peroxide by the hydrogen peroxide generator (31). Then, air containing hydrogen peroxide (sterilization gas) merges with the air in the main flow path (34), and after the temperature is adjusted by the sterilization side air conditioner (53), it is processed through the HEPA filter (14) on the inlet side. Supplied to chamber (2). As described above, the ratio of the amount of air flowing through the main channel (34) and the amount of air flowing through the hydrogen peroxide generating channel (33) is set to about 10: 1. By doing so, it is possible to obtain an effect of sufficiently diffusing hydrogen peroxide in the air and thus uniformly in the processing chamber (2).

処理室(2)内の滅菌ガスは出口側のHEPAフィルタ(14)を通って流出し、排気通路(28)から滅菌側循環通路(32)を構成する主流路(34)に流入する。主流路(34)に流入した滅菌ガスは、一部がそのまま主流路(34)を流れて滅菌側空調機(53)を通過した後に処理室(2)へ供給され、残りが過酸化水素分解流路(35)へ流入する。過酸化水素分解流路(35)へ流入した滅菌ガスは、過酸化水素分解器(36)で滅菌ガス中の過酸化水素が分解された後に排気ファン(55)によって排気側通路(54)の出口から室外へ排出される。   The sterilization gas in the processing chamber (2) flows out through the HEPA filter (14) on the outlet side, and flows from the exhaust passage (28) into the main channel (34) constituting the sterilization side circulation passage (32). Part of the sterilized gas that has flowed into the main flow path (34) flows directly through the main flow path (34), passes through the sterilization side air conditioner (53), and is then supplied to the treatment chamber (2), with the remainder being decomposed by hydrogen peroxide. It flows into the channel (35). The sterilization gas that has flowed into the hydrogen peroxide decomposition channel (35) is decomposed by the exhaust fan (55) after the hydrogen peroxide in the sterilization gas is decomposed by the hydrogen peroxide decomposer (36). It is discharged outside from the exit.

なお、排気側通路(54)から滅菌側循環通路(32)の空気を排気するのは、主流路(34)からの滅菌ガスの流入に伴う処理室(2)の室内圧力の上昇をコントロールするためである。排気側通路(54)から室外へ排出される空気の量、すなわち過酸化水素分解流路(35)の滅菌ガスの流量は、処理室(2)内に設けられた圧力センサ(図示せず)の計測値に基づいて調節されるが、過酸化水素発生流路(33)の流量に概ね近い値となる。従って、過酸化水素分解器(36)に流入する滅菌ガスの流量は、主流路(34)に比べてかなり小さくなる。ここで、この滅菌システム(1)では、主流路(34)の流量に対応した分解能力を有する過酸化水素分解器(36)が用いられている。このため、滅菌運転において過酸化水素分解器(36)に流入する滅菌ガスは、高濃度ではあるが過酸化水素の量は少ないので、過酸化水素分解器(36)でその滅菌ガスの過酸化水素の濃度を室外へ排出可能なレベルにまで低下させることができる。   Note that exhausting the air in the sterilization side circulation passage (32) from the exhaust side passage (54) controls the increase in the chamber pressure in the processing chamber (2) accompanying the inflow of sterilization gas from the main flow path (34). Because. The amount of air exhausted from the exhaust side passageway (54) to the outside, that is, the flow rate of the sterilizing gas in the hydrogen peroxide decomposition flow path (35), is a pressure sensor (not shown) provided in the processing chamber (2). Although it is adjusted based on the measured value, the value is substantially close to the flow rate of the hydrogen peroxide generation flow path (33). Therefore, the flow rate of the sterilizing gas flowing into the hydrogen peroxide decomposer (36) is considerably smaller than that of the main flow path (34). Here, in this sterilization system (1), a hydrogen peroxide decomposer (36) having a decomposition capability corresponding to the flow rate of the main flow path (34) is used. For this reason, the sterilization gas flowing into the hydrogen peroxide decomposer (36) in the sterilization operation has a high concentration but the amount of hydrogen peroxide is small. Therefore, the hydrogen peroxide decomposer (36) peroxidizes the sterilization gas. The concentration of hydrogen can be reduced to a level at which it can be discharged outside the room.

<希釈運転>
滅菌運転の完了後、処理室(2)内の過酸化水素の濃度は所定濃度の約500ppmになっている。この高濃度の状態では、処理室(2)内の滅菌ガスを過酸化水素分解器(36)に通過させて過酸化水素を分解しても、室外へ排出可能なレベルにまで過酸化水素の濃度を低下させることができない。そこで、処理室(2)内の過酸化水素の濃度が所定値(例えば10ppm)以下になるまでは、処理室(2)と過酸化水素分解器(36)との間で空気を循環させてその空気中の過酸化水素を過酸化水素分解器(36)で分解する第1希釈運転(循環動作)を行う(図10)。その後、外気処理空調機(13)及び顕熱空調機(17)を運転させてHEPAフィルタ(14)で処理をした無菌空気を処理室(2)へ供給しながら、その処理室(2)内の空気を室外へ排出する第2希釈運転(排気動作)を行う(図11)。なお、滅菌ガスの過酸化水素の濃度が10ppm(第1希釈運転の終了時点の濃度)ではそのまま室外へ排出できないが、10ppm以下になっていれば滅菌ガス中の過酸化水素を過酸化水素分解器(36)で分解することで室外へ排出可能なレベルにまで過酸化水素の濃度を低下させることができる。
<Dilution operation>
After completion of the sterilization operation, the concentration of hydrogen peroxide in the processing chamber (2) is a predetermined concentration of about 500 ppm. In this high concentration state, even if the sterilization gas in the treatment chamber (2) is passed through the hydrogen peroxide decomposer (36) to decompose the hydrogen peroxide, the hydrogen peroxide can be discharged to a level that can be discharged outside the chamber. The concentration cannot be reduced. Therefore, air is circulated between the treatment chamber (2) and the hydrogen peroxide decomposer (36) until the concentration of hydrogen peroxide in the treatment chamber (2) becomes a predetermined value (for example, 10 ppm) or less. A first dilution operation (circulation operation) is performed in which the hydrogen peroxide in the air is decomposed by the hydrogen peroxide decomposer (36) (FIG. 10). Then, while operating the outside air processing air conditioner (13) and sensible heat air conditioner (17) and supplying aseptic air treated with the HEPA filter (14) to the processing chamber (2), the inside of the processing chamber (2) A second dilution operation (exhaust operation) for discharging the air to the outside is performed (FIG. 11). If the concentration of hydrogen peroxide in the sterilization gas is 10 ppm (concentration at the end of the first dilution operation), it cannot be discharged to the outside as it is, but if it is 10 ppm or less, the hydrogen peroxide in the sterilization gas is decomposed into hydrogen peroxide. The concentration of hydrogen peroxide can be reduced to a level at which it can be discharged outside by being decomposed by the vessel (36).

(第1希釈運転)
第1希釈運転は、滅菌ガス発生機(58)を停止して、滅菌側空調機(53)を運転させる。この第1希釈運転時の空気の流れを図10に示す。
(First dilution operation)
In the first dilution operation, the sterilization gas generator (58) is stopped and the sterilization side air conditioner (53) is operated. FIG. 10 shows the air flow during the first dilution operation.

このとき、空調系統側回路(10)の設定は基本的に滅菌運転時と同じであり、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)は停止しており、各バルブ(56a,56b,56c)は閉じた状態にする。一方、滅菌系統側回路(30)の各バルブは、第3滅菌ガス切換バルブ(45c)及び第5滅菌ガス切換バルブ(45e)以外は開いた状態にする。   At this time, the setting of the air conditioning system side circuit (10) is basically the same as in the sterilization operation, and the outside air processing air conditioner (13), the sensible heat air conditioner (17), and the circulation fan (18) are stopped. Each valve (56a, 56b, 56c) is closed. On the other hand, the valves of the sterilization system side circuit (30) are opened except for the third sterilization gas switching valve (45c) and the fifth sterilization gas switching valve (45e).

この状態で、滅菌側空調機(53)及び排気ファン(55)を運転すると、処理室(2)と過酸化水素分解器(36)との間で空気が循環する際にその空気中の過酸化水素が過酸化水素分解器(36)で分解される。第1希釈運転は、過酸化水素濃度センサによる検出値(過酸化水素濃度)が所定値(10ppm)以下になるまで行われる。   When the sterilization side air conditioner (53) and the exhaust fan (55) are operated in this state, excess air in the air is circulated when the air circulates between the treatment chamber (2) and the hydrogen peroxide decomposer (36). Hydrogen oxide is decomposed by the hydrogen peroxide decomposer (36). The first dilution operation is performed until the value detected by the hydrogen peroxide concentration sensor (hydrogen peroxide concentration) becomes a predetermined value (10 ppm) or less.

なお、第1希釈運転時に処理室(2)の圧力が低下した場合には、滅菌ガス発生機(58)を停止した状態で第5滅菌ガス切換バルブ(45e)を開いて過酸化水素発生流路(33)から外気を導入して、処理室(2)内を所定圧力(例えば数10Pa)に維持する操作を行う。   If the pressure in the processing chamber (2) decreases during the first dilution operation, the sterilization gas generator (58) is stopped and the fifth sterilization gas switching valve (45e) is opened to generate hydrogen peroxide. Outside air is introduced from the passage (33), and an operation for maintaining the inside of the processing chamber (2) at a predetermined pressure (for example, several tens of Pa) is performed.

(第2希釈運転)
第2希釈運転は、外気処理空調機(13)から入口側のHEPAフィルタ(14)を介して空気を処理室(2)に供給しながら過酸化水素の濃度が所定値(10ppm)よりもさらに低い値(1ppm)以下になるまで排気を行う換気工程である(図11)。
(Second dilution operation)
In the second dilution operation, the concentration of hydrogen peroxide further exceeds a predetermined value (10 ppm) while supplying air from the outside air treatment air conditioner (13) to the treatment chamber (2) via the HEPA filter (14) on the inlet side. This is a ventilation process in which exhaust is performed until the value becomes lower than 1 ppm (FIG. 11).

このとき、滅菌ガス発生機(58)及び循環ファン(18)は停止させたままにしておく。空調系統側回路(10)の各バルブは、第1空調ガス切換バルブ(56a)のみを開いた状態にする。一方、滅菌系統側回路(30)の各バルブは、第1滅菌ガス切換バルブ(45a)及び第2滅菌ガス切換バルブ(45b)を開いた状態にする。また、排気ファン(55)を運転させる。   At this time, the sterilization gas generator (58) and the circulation fan (18) are stopped. Each valve of the air conditioning system side circuit (10) opens only the first air conditioning gas switching valve (56a). On the other hand, each valve of the sterilization system side circuit (30) opens the first sterilization gas switching valve (45a) and the second sterilization gas switching valve (45b). Further, the exhaust fan (55) is operated.

この状態で、外気処理空調機(13)、顕熱空調機(17)、及び排気ファン(55)を運転すると、外気処理空調機(13)と顕熱空調機(17)で温度と湿度が調節され、入口側のHEPAフィルタ(14)で浄化された無菌空気が処理室(2)に供給され、処理室(2)内で滅菌ガスと均一に混合する。希釈された滅菌ガスは、出口側のHEPAフィルタ(14)を通って処理室(2)から流出する。この滅菌ガスは、排気通路(28)から滅菌系統側回路(30)の主流路(34)を経て過酸化水素分解流路(35)に流入する。過酸化水素分解流路(35)に流入した滅菌ガスは、その滅菌ガス中の過酸化水素が過酸化水素分解器(36)で分解され、排気側通路(54)の出口から室外へ排出される。   In this state, when the outside air treatment air conditioner (13), sensible heat air conditioner (17), and exhaust fan (55) are operated, the temperature and humidity of the outside air treatment air conditioner (13) and sensible heat air conditioner (17) are reduced. Sterile air that has been adjusted and purified by the HEPA filter (14) on the inlet side is supplied to the processing chamber (2) and uniformly mixed with the sterilizing gas in the processing chamber (2). The diluted sterilization gas flows out of the processing chamber (2) through the HEPA filter (14) on the outlet side. The sterilizing gas flows from the exhaust passage (28) into the hydrogen peroxide decomposition passage (35) through the main passage (34) of the sterilization system side circuit (30). The sterilization gas that has flowed into the hydrogen peroxide decomposition channel (35) is decomposed by the hydrogen peroxide decomposer (36) and discharged from the outlet of the exhaust side passage (54) to the outside. The

この第2希釈運転では、第1希釈運転とは異なり、過酸化水素分解器(36)を通過した空気を処理室(2)へ戻さないので、第1希釈運転に比べて短時間で処理室(2)内の過酸化水素の濃度を下げることが可能である。また、処理室(2)への空気の供給が、空調装置を構成する外気処理空調機(13)及び顕熱空調機(17)を用いて行われている。これらの空調装置(13,17)は、滅菌側空調機(53)よりも大風量の空気を供給可能な装置として構成されているので、単位時間当たりの処理室(2)の空気の入れ換え量が第1希釈運転よりも多くなる。この点においても、第1希釈運転に比べて短時間で処理室(2)内の過酸化水素の濃度を下げることが可能である。   In this second dilution operation, unlike the first dilution operation, the air that has passed through the hydrogen peroxide decomposer (36) is not returned to the processing chamber (2), so that the processing chamber is shorter in time than the first dilution operation. It is possible to reduce the concentration of hydrogen peroxide in (2). Moreover, the supply of air to the processing chamber (2) is performed using an outside air processing air conditioner (13) and a sensible heat air conditioner (17) constituting the air conditioner. These air conditioners (13, 17) are configured as devices that can supply a larger volume of air than the sterilization side air conditioner (53), so the amount of air exchanged in the processing chamber (2) per unit time Is greater than in the first dilution operation. Also in this point, it is possible to reduce the concentration of hydrogen peroxide in the processing chamber (2) in a shorter time than in the first dilution operation.

第2希釈運転では、処理室(2)の過酸化水素濃度が約1ppm以下になるまで行われる。その際、室内圧力を建屋漏気上の対策により、定常値よりも低い圧力(例えば約15Pa)に保持するために、第1滅菌ガス切換バルブ(45a)及び第2滅菌ガス切換バルブ(45b)のそれぞれの開度を調節する。   The second dilution operation is performed until the hydrogen peroxide concentration in the processing chamber (2) is about 1 ppm or less. At that time, the first sterilization gas switching valve (45a) and the second sterilization gas switching valve (45b) are used in order to maintain the indoor pressure at a pressure lower than the steady value (for example, about 15 Pa) by taking measures against building air leakage. Adjust the opening of each.

また、第1希釈運転から第2希釈運転への移行時には、室圧の急激な変化を避けるため、外気処理空調機(13)、顕熱空調機(17)及び排気ファン(55)をスロースタートし、安定した移行を行うとよい。   Also, during the transition from the first dilution operation to the second dilution operation, the outside air treatment air conditioner (13), the sensible heat air conditioner (17), and the exhaust fan (55) are started slowly to avoid sudden changes in the room pressure. And make a stable transition.

<定常運転>
定常運転は、外気処理空調機(13)により処理した外気を取り入れながら処理室(2)内の換気及び室圧保持のためにその処理室(2)内の空気を室外へ排出する工程である。この定常運転の空気の流れを図12に示す。第2希釈運転と空気の流れはほぼ同じであるが、処理室(2)内の空気を排気側通路(54)ではなく排気通路(28)から排出する点で異なっている。
<Normal operation>
Steady operation is a process of exhausting the air in the processing chamber (2) to the outside in order to ventilate the inside of the processing chamber (2) and maintain the room pressure while taking in the outside air processed by the outside air processing air conditioner (13). . The flow of air in this steady operation is shown in FIG. The air flow is substantially the same as that in the second dilution operation, but differs in that the air in the processing chamber (2) is discharged from the exhaust passage (28) instead of the exhaust side passage (54).

このとき、空調系統側回路(10)の各バルブ(56a,56b,56c)は開いた状態にする。一方、滅菌系統側回路(30)の各バルブ(45a,45b,45c,45d,45e,45f)は閉じた状態にする。また、排気ファン(55)を停止させ、循環ファン(18)を運転させる。   At this time, each valve (56a, 56b, 56c) of the air conditioning system side circuit (10) is opened. On the other hand, each valve (45a, 45b, 45c, 45d, 45e, 45f) of the sterilization system side circuit (30) is closed. Further, the exhaust fan (55) is stopped and the circulation fan (18) is operated.

この状態で、外気処理空調機(13)、顕熱空調機(17)、及び循環ファン(18)を運転すると、外気処理空調機(13)と顕熱空調機(17)で温度と湿度が調節され、入口側のHEPAフィルタ(14)で浄化された無菌空気が処理室(2)に供給される。処理室(2)の無菌空気は、出口側のHEPAフィルタ(14)を通って処理室(2)から流出する。この無菌空気は、大部分が第3空調ガス切換バルブ(56c)を通って排気通路(28)の出口から排出され、一部が戻り通路(15)から給気通路(11)へ戻され、さらに顕熱空調機(17)へと流れていく。定常運転では、処理室(2)の温度と湿度が設定値に維持されるとともに、無菌状態が維持される。   In this state, when the outside air treatment air conditioner (13), sensible heat air conditioner (17), and circulation fan (18) are operated, the temperature and humidity of the outside air treatment air conditioner (13) and sensible heat air conditioner (17) are reduced. Aseptic air that has been adjusted and purified by the HEPA filter (14) on the inlet side is supplied to the processing chamber (2). Aseptic air in the processing chamber (2) flows out of the processing chamber (2) through the HEPA filter (14) on the outlet side. Most of this sterile air is discharged from the outlet of the exhaust passage (28) through the third air-conditioning gas switching valve (56c), and part is returned to the air supply passage (11) from the return passage (15), It further flows to the sensible heat air conditioner (17). In the steady operation, the temperature and humidity of the processing chamber (2) are maintained at the set values and the aseptic state is maintained.

参考技術の効果−
参考技術では、空調装置を構成する外気処理空調機(13)及び顕熱空調機(17)を滅菌ガス発生機(58)や過酸化水素分解器(36)と共に連動させることによって、滅菌運転において高い滅菌効果が期待できるように処理室(2)内を除湿する準備運転と、低湿度で滅菌処理が行われる滅菌運転と、処理室(2)内の過酸化水素の濃度を低下させる希釈運転とが一連の動作として実行される。即ち、この参考技術では、空調装置を含めた滅菌システム(1)を構成することで、過酸化水素を用いた滅菌処理の効果を高めるようにしている。従って、過酸化水素を用いて処理室(2)の滅菌を行う滅菌システム(1)において、滅菌性能を向上させることができる。
-Effect of reference technology-
In this reference technology , the external air processing air conditioner (13) and the sensible heat air conditioner (17) that constitute the air conditioner are linked with the sterilization gas generator (58) and the hydrogen peroxide decomposer (36) to perform sterilization operation. Preparation operation to dehumidify the processing chamber (2) so that a high sterilization effect can be expected, sterilization operation in which sterilization is performed at low humidity, and dilution to reduce the concentration of hydrogen peroxide in the processing chamber (2) Operation is performed as a series of operations. That is, in this reference technology , the sterilization system (1) including the air conditioner is configured to enhance the effect of sterilization treatment using hydrogen peroxide. Therefore, the sterilization performance can be improved in the sterilization system (1) that sterilizes the processing chamber (2) using hydrogen peroxide.

また、本参考技術では、希釈運転において、第1希釈運転によって処理室(2)内の過酸化水素の濃度が所定値以下となると、第1希釈運転よりも短時間で処理室(2)内の過酸化水素の濃度を下げることが可能な第2希釈運転に切り換えられる。従って、第2希釈運転への切り換えが可能な所定値を予め設定しておくことにより、希釈運転を効率よく行うことができる。 Further, in the present reference technology , in the dilution operation, when the concentration of hydrogen peroxide in the processing chamber (2) becomes a predetermined value or less in the first dilution operation, the processing chamber (2) has a shorter time than the first dilution operation. Is switched to the second dilution operation capable of lowering the concentration of hydrogen peroxide. Therefore, the dilution operation can be performed efficiently by setting in advance a predetermined value that can be switched to the second dilution operation.

また、本参考技術では、第2希釈運転において処理室(2)へ供給される空気中の菌類が捕捉されるようにフィルタ機構(14)が設けられている。従って、第2希釈運転の際に外部から処理室(2)へ侵入する菌類の量を削減できる。 Moreover, in this reference technique , the filter mechanism (14) is provided so that the fungi in the air supplied to the processing chamber (2) may be captured in the second dilution operation. Accordingly, the amount of fungi that enter the processing chamber (2) from the outside during the second dilution operation can be reduced.

また、本参考技術では、第2希釈運転の際に、第1希釈運転で運転させる滅菌側空調機(53)よりも大風量の空気を供給可能な外気処理空調機(13)及び顕熱空調機(17)を用いて処理室(2)への空気の供給を行う。これにより、短時間で処理室(2)内の過酸化水素の濃度を下げることができるので、第2希釈運転を短時間で終了させることができる。 In addition, in this reference technology , an external air treatment air conditioner (13) and a sensible heat air conditioner that can supply a larger air volume than the sterilization side air conditioner (53) operated in the first dilution operation in the second dilution operation. Air is supplied to the processing chamber (2) using the machine (17). Thereby, since the concentration of hydrogen peroxide in the processing chamber (2) can be lowered in a short time, the second dilution operation can be completed in a short time.

また、本参考技術では、準備運転において処理室(2)内の相対湿度が20%以上で30%以下の範囲の所定値になるように調節される。従って、滅菌運転において高い滅菌効果が得られるので、滅菌性能を向上させることができる。 In this reference technique , the relative humidity in the processing chamber (2) is adjusted to a predetermined value in the range of 20% to 30% in the preparation operation. Therefore, since a high sterilization effect is obtained in the sterilization operation, the sterilization performance can be improved.

また、本参考技術では、処理室(2)内の過酸化水素の濃度が外気処理空調機(13)及び顕熱空調機(17)の影響を受けずに滅菌ガス発生機(58)の運転制御によって調節されるように、滅菌運転中には外気処理空調機(13)及び顕熱空調機(17)から処理室(2)への空気の供給を停止させる。従って、滅菌運転中は滅菌ガス発生機(58)の運転制御を行うだけでよいので、処理室(2)内の過酸化水素の濃度の調節を容易に行うことができる。 In addition, in this reference technology , the concentration of hydrogen peroxide in the treatment chamber (2) is not affected by the outside air treatment air conditioner (13) and the sensible heat air conditioner (17). As controlled by the control, the supply of air from the outside air processing air conditioner (13) and the sensible heat air conditioner (17) to the processing chamber (2) is stopped during the sterilization operation. Accordingly, during the sterilization operation, it is only necessary to control the operation of the sterilization gas generator (58), so that the concentration of hydrogen peroxide in the processing chamber (2) can be easily adjusted.

また、本参考技術では、滅菌運転において、処理室(2)へ導入される過酸化水素を含んだ空気を温度調節することができるように、滅菌側空調機(53)が設けられている。従って、空調装置(13,17)から処理室(2)への空気の供給を停止させた状態で処理室(2)内の温度調節を行うことができる。 In this reference technology , the sterilization side air conditioner (53) is provided so that the temperature of the air containing hydrogen peroxide introduced into the processing chamber (2) can be adjusted in the sterilization operation. Therefore, the temperature in the processing chamber (2) can be adjusted in a state where the supply of air from the air conditioner (13, 17) to the processing chamber (2) is stopped.

参考技術の変形例1−
参考技術の変形例1について説明する。図13に示すように、この変形例1の滅菌システム(1)は、外気処理空調機(13)を経由して滅菌ガス発生機(58)に外気が取り込まれるように構成されている。
-Modification of reference technology 1-
A first modification of the reference technique will be described. As shown in FIG. 13, the sterilization system (1) of the first modification is configured such that outside air is taken into the sterilizing gas generator (58) via the outside air processing air conditioner (13).

具体的に、給気通路(11)と滅菌ガス発生機(58)とを接続する外気導入通路(59)が設けられている。外気導入通路(59)は、給気通路(11)の戻し通路(15)との接続部と外気処理空調機(13)との間において給気通路(11)から分岐している。滅菌運転において、第5滅菌ガス切換バルブ(45e)を開いて第1空調ガス切換バルブ(56a)を閉じた状態にすると、外気処理空調機(13)で除湿された空気が滅菌ガス発生機(58)に流入する。   Specifically, an outside air introduction passage (59) that connects the air supply passage (11) and the sterilization gas generator (58) is provided. The outside air introduction passage (59) is branched from the air supply passage (11) between the connection portion between the air supply passage (11) and the return passage (15) and the outside air processing air conditioner (13). In the sterilization operation, when the fifth sterilization gas switching valve (45e) is opened and the first air conditioning gas switching valve (56a) is closed, the air dehumidified by the outside air processing air conditioner (13) is supplied to the sterilization gas generator ( 58).

参考技術の変形例2−
参考技術の変形例2について説明する。図14に示すように、この変形例2の滅菌システム(1)では、滅菌系統側回路(30)の主流路(34)が、空調系統側回路(10)の給気通路(11)及び排気通路(28)ではなく直接処理室(2)に接続されている。
-Modification of reference technology 2-
A modification 2 of the reference technique will be described. As shown in FIG. 14, in the sterilization system (1) of the second modification, the main flow path (34) of the sterilization system side circuit (30) is connected to the air supply path (11) and the exhaust of the air conditioning system side circuit (10). It is connected directly to the processing chamber (2), not the passage (28).

参考技術の変形例3−
参考技術の変形例3について説明する。この変形例3では、滅菌システム(1)が複数の処理室に対して構成されている。この場合、上記実施形態のと同様に、給気通路(11)や排気通路(28)から分岐して各処理室(2)に接続される経路には、それぞれダンパ(23,24,25)、定風量装置(22)を設ける。これにより、各処理室(2)の滅菌処理を個別に実行することが可能になる。滅菌処理が行われていない処理室(2)へは、定常運転によって外気処理空調機(13)及び顕熱空調機(17)で空調された空気が流入するようにダンパ(23,24,25)、定風量装置(22)を調節する。
-Modification of reference technology 3-
A third modification of the reference technique will be described. In Modification 3, the sterilization system (1) is configured for a plurality of processing chambers. In this case, similarly to the above-described type state, the path connected branched from the supply passage (11) and the exhaust passage (28) to the processing chamber (2), respectively the damper (23,24,25 ) Install a constant air volume device (22). Thereby, it becomes possible to perform the sterilization process of each process chamber (2) separately. Dampers (23, 24, 25) so that the air conditioned by the outside air treatment air conditioner (13) and the sensible heat air conditioner (17) through the steady operation flows into the processing chamber (2) that has not been sterilized. ) Adjust the constant air volume device (22).

参考技術の変形例4−
参考技術の変形例4について説明する。図15に示すように、この変形例4では、空調系統側回路(10)が設けられておらず、処理室(2)の滅菌処理を滅菌系統側回路(30)のみで実行するように構成されている。
-Modification of reference technology 4-
A modification 4 of the reference technique will be described. As shown in FIG. 15, in the fourth modification, the air conditioning system side circuit (10) is not provided, and the sterilization process of the processing chamber (2) is executed only by the sterilization system side circuit (30). Has been.

この滅菌システム(1)では、準備運転において、滅菌ガス発生機(58)が過酸化水素発生器(31)を停止させて除湿器(57)のみを運転させるように制御される。これにより、室外から取り込まれて滅菌ガス発生機(58)で除湿された空気が、滅菌側空調機(53)で温度調節されて処理室(2)へ流入し、処理室(2)が目標湿度に調節される。   In this sterilization system (1), in the preparatory operation, the sterilization gas generator (58) is controlled to stop the hydrogen peroxide generator (31) and operate only the dehumidifier (57). As a result, the air taken from outside and dehumidified by the sterilization gas generator (58) is adjusted in temperature by the sterilization side air conditioner (53) and flows into the processing chamber (2), and the processing chamber (2) is targeted. Adjusted to humidity.

《その他の実施形態》
上記実施形態については、以下のような構成としてもよい。
<< Other Embodiments >>
About the said embodiment, it is good also as the following structures.

例えば、上記実施形態では、滅菌運転を滅菌ガス中の過酸化水素濃度が約500ppmになる高濃度の運転にしているが、滅菌をする度に必ずしも高濃度の滅菌運転をしなくてもよく、製造室を使用しない夜間などに短時間で処理するときには、準備運転、5〜10ppm程度の低濃度の滅菌運転、及び処理室(2)の換気を行う第2希釈運転を行うようにして、第1希釈運転を省略するようにしてもよい。   For example, in the above embodiment, the sterilization operation is a high concentration operation in which the concentration of hydrogen peroxide in the sterilization gas is about 500 ppm, but it is not always necessary to perform the high concentration sterilization operation every time sterilization is performed. When processing in a short time, such as at night, when the manufacturing room is not used, a preparatory operation, a sterilization operation with a low concentration of about 5 to 10 ppm, and a second dilution operation that ventilates the processing chamber (2) are performed. One dilution operation may be omitted.

また、上記実施形態では、すべての医薬品製造室(2a,2b,2c)を同時に滅菌する運転について説明したが、各製造室(2a,2b,2c)を個別に滅菌する運転を行ってもよく、その場合、滅菌を行う製造室(2a,2b,2c)に応じてバルブの開閉をするとよい。また、医薬品製造室(2a,2b,2c)は3室に限らず、3室以外の複数室であってもよいし、1室であってもよい。   In the above embodiment, the operation for sterilizing all the pharmaceutical manufacturing rooms (2a, 2b, 2c) at the same time has been described. However, the operation for individually sterilizing each manufacturing room (2a, 2b, 2c) may be performed. In that case, the valve should be opened and closed according to the sterilization room (2a, 2b, 2c). In addition, the pharmaceutical manufacturing rooms (2a, 2b, 2c) are not limited to three rooms, and may be a plurality of rooms other than the three rooms or a single room.

なお、以上の実施形態は、本質的に好ましい例示であって、本発明、その適用物、あるいはその用途の範囲を制限することを意図するものではない。   In addition, the above embodiment is an essentially preferable illustration, Comprising: It does not intend restrict | limiting the range of this invention, its application thing, or its use.

以上説明したように、本発明は、処理室を過酸化水素で滅菌処理する滅菌システムについて有用である。   As described above, the present invention is useful for a sterilization system that sterilizes a processing chamber with hydrogen peroxide.

本発明の実施形態のに係る滅菌システムの配管系統図である。A piping diagram of a sterilization system according to exemplary form status of the present invention. 図1の滅菌システムにおいて準備運転の動作を示す図である。It is a figure which shows the operation | movement of a preparatory operation in the sterilization system of FIG. 図1の滅菌システムにおいて滅菌運転の動作を示す図である。It is a figure which shows operation | movement of the sterilization driving | operation in the sterilization system of FIG. 図1の滅菌システムにおいて第1希釈運転の動作を示す図である。It is a figure which shows operation | movement of the 1st dilution driving | operation in the sterilization system of FIG. 図1の滅菌システムにおいて第2希釈運転の動作を示す図である。It is a figure which shows operation | movement of the 2nd dilution driving | operation in the sterilization system of FIG. 図1の滅菌システムにおいて定常運転の動作を示す図である。It is a figure which shows operation | movement of steady operation in the sterilization system of FIG. 参考技術に係る滅菌システムの配管系統図である。It is a piping system diagram of the sterilization system concerning a reference technology . 図7の滅菌システムにおいて準備運転の動作を示す図である。It is a figure which shows the operation | movement of a preparatory operation in the sterilization system of FIG. 図7の滅菌システムにおいて滅菌運転の動作を示す図である。It is a figure which shows operation | movement of the sterilization driving | operation in the sterilization system of FIG. 図7の滅菌システムにおいて第1希釈運転の動作を示す図である。It is a figure which shows operation | movement of a 1st dilution driving | operation in the sterilization system of FIG. 図7の滅菌システムにおいて第2希釈運転の動作を示す図である。It is a figure which shows operation | movement of the 2nd dilution driving | operation in the sterilization system of FIG. 図7の滅菌システムにおいて定常運転の動作を示す図である。It is a figure which shows operation | movement of steady operation in the sterilization system of FIG. 参考技術の変形例1に係る滅菌システムの配管系統図である。It is a piping system diagram of the sterilization system concerning modification 1 of a reference technique . 参考技術の変形例2に係る滅菌システムの配管系統図である。It is a piping system diagram of the sterilization system concerning modification 2 of a reference technique . 参考技術の変形例4に係る滅菌システムの配管系統図である。It is a piping system diagram of the sterilization system concerning modification 4 of a reference technique .

1 滅菌システム
2 処理室
10 空調系統側回路
11 給気通路
12 還気通路
13 外気処理空調機(空調装置)
14 HEPAフィルタ(フィルタ機構)
15 戻し通路
16 空調側循環通路
17 顕熱空調機(空調装置)
25 圧力調整機構
30 滅菌系統側回路
31 過酸化水素発生器
32 滅菌側循環通路
36 過酸化水素分解器
38 還気側連通路
39 給気側連通路
50 コントローラ(制御手段)
53 滅菌側空調機
57 除湿器
1 Sterilization system
2 Processing chamber
10 Air conditioning system side circuit
11 Air supply passage
12 Return passage
13 Outside air treatment air conditioner (air conditioner)
14 HEPA filter (filter mechanism)
15 Return passage
16 Air conditioning side circulation passage
17 Sensible heat air conditioner (air conditioner)
25 Pressure adjustment mechanism
30 Sterilization system side circuit
31 Hydrogen peroxide generator
32 Sterilization side circulation passage
36 Hydrogen peroxide decomposer
38 Return air side passage
39 Supply side communication passage
50 controller (control means)
53 Sterilization side air conditioner
57 Dehumidifier

Claims (7)

処理室(2)内の空調と滅菌処理とを行う滅菌システムであって、
外気の温度と湿度を調節するとともに、処理室(2)に給気通路(11)と還気通路(12)を介して接続された外気処理空調機(13)と、
給気通路(11)から処理室(2)への空気の入口に設けられたフィルタ機構(14)と、
還気通路(12)から給気通路(11)に戻し通路(15)を接続することにより構成された空調側循環通路(16)と、
上記空調側循環通路(16)に設けられた顕熱空調機(17)と、
上記処理室(2)に接続され、過酸化水素発生器(31)を備えた滅菌側循環通路(32)と、
上記外気処理空調機(13)から滅菌側循環通路(32)に外気を導入する給気側連通路(39)と、
滅菌側循環通路(32)において過酸化水素発生器(31)と並列に接続された過酸化水素分解器(36)と、
過酸化水素分解器(36)を外気処理空調機(13)の還気通路(12)に接続する還気側連通路(38)と、
を備えていることを特徴とする滅菌システム。
A sterilization system that performs air conditioning and sterilization in the processing chamber (2),
An outside air processing air conditioner (13) connected to the processing chamber (2) via an air supply passage (11) and a return air passage (12), while adjusting the temperature and humidity of the outside air;
A filter mechanism (14) provided at an air inlet from the air supply passage (11) to the processing chamber (2);
An air conditioning side circulation passage (16) configured by connecting the return passage (15) from the return air passage (12) to the air supply passage (11);
A sensible heat air conditioner (17) provided in the air conditioning side circulation passage (16);
A sterilization side circulation passage (32) connected to the treatment chamber (2) and provided with a hydrogen peroxide generator (31);
A supply side communication passage (39) for introducing outside air from the outside air processing air conditioner (13) to the sterilization side circulation passage (32);
A hydrogen peroxide decomposer (36) connected in parallel with the hydrogen peroxide generator (31) in the sterilization side circulation passage (32);
A return side communication passage (38) connecting the hydrogen peroxide decomposer (36) to the return air passage (12) of the outside air treatment air conditioner (13);
A sterilization system comprising:
請求項1において、
処理室(2)内の圧力を調整する圧力調整機構(25)が設けられていることを特徴とする滅菌システム。
In claim 1,
A sterilization system comprising a pressure adjusting mechanism (25) for adjusting the pressure in the processing chamber (2).
請求項1または2において、
滅菌側循環通路(32)における処理室(2)への入口側が給気通路(11)のフィルタ機構(14)に接続されていることを特徴とする滅菌システム。
In claim 1 or 2,
The sterilization system, wherein an inlet side to the processing chamber (2) in the sterilization side circulation passage (32) is connected to a filter mechanism (14) of the air supply passage (11).
請求項1,2または3において、
運転制御を行う制御手段(50)を備え、該制御手段(50)は、
過酸化水素発生器(31)を停止した状態で、外気処理空調機(13)により処理室(2)の湿度を所定値以下に低下させる準備運転と、
過酸化水素発生器(31)により発生した過酸化水素を滅菌側循環通路(32)で循環させることにより処理室(2)に過酸化水素を所定濃度になるように供給する滅菌運転と、
過酸化水素発生器(31)を停止して処理室(2)のガスを滅菌側循環通路(32)で循環させながら過酸化水素分解器(36)で過酸化水素濃度が第1の設定値以下になるまで分解する第1希釈運転と、
外気処理空調機(13)からフィルタ機構(14)を介して空気を処理室(2)に供給しながら過酸化水素濃度が第1の設定値よりも低い第2の設定値以下になるまで排気を行う第2希釈運転と、
外気処理空調機(13)により処理した外気を取り入れながら空調側循環通路(16)で顕熱空調機(17)を介して空調空気を循環させる定常運転と、
が可能に構成されていることを特徴とする滅菌システム。
In claim 1, 2 or 3,
A control means (50) for performing operation control is provided, and the control means (50)
With the hydrogen peroxide generator (31) stopped, a preparatory operation for reducing the humidity of the processing chamber (2) below a predetermined value by the outside air processing air conditioner (13),
A sterilization operation for supplying hydrogen peroxide to a predetermined concentration to the treatment chamber (2) by circulating the hydrogen peroxide generated by the hydrogen peroxide generator (31) in the sterilization side circulation passage (32);
Stop the hydrogen peroxide generator (31) and circulate the gas in the processing chamber (2) through the sterilization side circulation passage (32) while the hydrogen peroxide concentration in the hydrogen peroxide decomposer (36) is the first set value. A first dilution operation that decomposes until:
While supplying air from the outside air processing air conditioner (13) to the processing chamber (2) through the filter mechanism (14), exhausting until the hydrogen peroxide concentration becomes lower than the second set value lower than the first set value. A second dilution operation for performing
Steady operation of circulating the conditioned air through the sensible heat air conditioner (17) in the air conditioning side circulation passage (16) while taking in the outside air treated by the outside air treatment air conditioner (13);
A sterilization system characterized by being configured to be capable of.
請求項4において、
滅菌運転時における処理室(2)の室内湿度上昇時または室内圧力上昇時に、過酸化水素分解器(36)から還気側連通路(38)を通じて処理室(2)のガスを外気処理空調機(13)に還気するように構成されていることを特徴とする滅菌システム。
In claim 4,
When the indoor humidity of the processing chamber (2) during sterilization operation increases or when the indoor pressure increases, the gas from the processing chamber (2) is discharged from the hydrogen peroxide decomposer (36) through the return air side communication passage (38). A sterilization system configured to return to (13).
請求項4において、
第1希釈運転時における処理室(2)の圧力低下時に、外気処理空調機(13)から空調空気を滅菌側循環通路(32)に供給するように構成されていることを特徴とする滅菌システム。
In claim 4,
A sterilization system configured to supply conditioned air from the outside air processing air conditioner (13) to the sterilization side circulation passage (32) when the pressure in the processing chamber (2) is reduced during the first dilution operation. .
請求項4において、
第2希釈運転時に、外気処理空調機(13)と顕熱空調機(17)からフィルタ機構(14)を介して処理室(2)に空調空気を供給するとともに処理室(2)のガスを排気しながら、該処理室(2)のガスの一部を空調側循環通路(16)で循環させることを特徴とする滅菌システム。
In claim 4,
During the second dilution operation, conditioned air is supplied to the processing chamber (2) through the filter mechanism (14) from the outside air processing air conditioner (13) and the sensible heat air conditioner (17) and the gas in the processing chamber (2) is supplied. A sterilization system characterized in that a part of the gas in the processing chamber (2) is circulated in the air conditioning side circulation passage (16) while exhausting.
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