JP2005137573A - Sterilization equipment - Google Patents

Sterilization equipment Download PDF

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JP2005137573A
JP2005137573A JP2003377131A JP2003377131A JP2005137573A JP 2005137573 A JP2005137573 A JP 2005137573A JP 2003377131 A JP2003377131 A JP 2003377131A JP 2003377131 A JP2003377131 A JP 2003377131A JP 2005137573 A JP2005137573 A JP 2005137573A
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hypochlorous acid
sterilization
sterilized water
sterilization tank
acid concentration
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Kazuo Nakatsu
和夫 中津
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Abstract

<P>PROBLEM TO BE SOLVED: To provide sterilization equipment using hypochlorous acid which efficiently utilizes generated hypochlorous acid and performs a reliable sterilization processing. <P>SOLUTION: The sterilization equipment 1 is equipped with a sterilization tank 2 where articles to be processed are placed, a hypochlorous acid supply part 3 which generates the hypochlorous acid and supplies treated water for sterilization in which the concentration of hypochlorous acid is adjusted, supply piping 4, bypass piping 5, and a control device 6. If the treated water for sterilization in the bypass piping 5 is determined to be used for the sterilization processing as it is, the sterilization equipment performs the resupply processing 36 for resupplying the treated water for sterilization used in the sterilization tank 2 to the sterilization tank 2 through the bypass piping 5 and the supply piping 4. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は滅菌装置に関するものである。   The present invention relates to a sterilization apparatus.

近年、洗濯機や食器洗浄器などの用途において、洗濯や食器洗浄時に、次亜塩素酸や次亜塩素酸ソーダを用いて滅菌処理(殺菌処理)を行なうことが提案されている(特許文献1、2、3)。
特開2003−000992 特開2003−52609 特開平5−137689号公報
In recent years, it has been proposed to perform sterilization treatment (sterilization treatment) using hypochlorous acid or sodium hypochlorite at the time of washing or dish washing in applications such as washing machines and dishwashers (Patent Document 1). 2, 3).
JP2003-000992A JP 2003-52609 A JP-A-5-137589

上記の次亜塩素酸を用いた滅菌処理では、滅菌処理水中の次亜塩素酸が滅菌処理中に有機物などと反応することにより、滅菌処理水中の次亜塩素酸濃度が徐々に低下していく。また、次亜塩素酸を用いた滅菌処理では、細菌の種類により、殺菌時間が違うので、完全に滅菌するためには、滅菌処理中の次亜塩素酸濃度を一定以上に保った上で、一定時間滅菌処理を行なうことが必要である。また、滅菌槽で滅菌処理に用いられた滅菌処理水は排水されるが、この排水中には次亜塩素酸が多量に残留しており、生成された次亜塩素酸が必ずしも有効に利用されているわけではない。   In the above sterilization using hypochlorous acid, hypochlorous acid in the sterilized water gradually decreases as hypochlorous acid in the sterilized water reacts with organic substances during the sterilization process. . In addition, in sterilization using hypochlorous acid, the sterilization time differs depending on the type of bacteria, so to completely sterilize, keep the hypochlorous acid concentration during sterilization above a certain level, It is necessary to sterilize for a certain period of time. In addition, the sterilized water used for sterilization in the sterilization tank is drained, but a large amount of hypochlorous acid remains in the drainage, and the generated hypochlorous acid is not necessarily effectively used. I don't mean.

そこで、本発明は、生成した次亜塩素酸の有効利用を図ること、及び、確実な滅菌処理を行なうことができる次亜塩素酸を用いた滅菌装置を提供することを目的とする。   Then, an object of this invention is to provide the sterilization apparatus using hypochlorous acid which can aim at the effective utilization of the produced | generated hypochlorous acid, and can perform a reliable sterilization process.

本発明に係る滅菌装置は、被処理物を入れる滅菌槽と、次亜塩素酸濃度及びPHを調整して次亜塩素酸を含んだ滅菌処理水を供給する次亜塩素酸供給部と、次亜塩素酸供給部から滅菌槽に滅菌処理水を供給する供給配管と、滅菌槽で使用された後の滅菌処理水を、次亜塩素酸供給部を経由せずに滅菌槽に循環させるバイパス配管と、滅菌槽に滅菌処理水を供給して滅菌槽内の被処理物を滅菌処理する滅菌処理工程において、滅菌槽で使用された後の滅菌処理水が、滅菌処理を行なうのに適した次亜塩素酸濃度及びPHを維持している場合に、バイパス配管を通して滅菌槽で使用された後の滅菌処理水を滅菌槽に再供給するようにした制御手段とを備えていることを特徴としている。   A sterilization apparatus according to the present invention includes a sterilization tank in which an object to be treated is placed, a hypochlorous acid supply unit that adjusts hypochlorous acid concentration and pH and supplies sterilized water containing hypochlorous acid, Supply piping that supplies sterilized water from the chlorous acid supply unit to the sterilization tank, and bypass piping that circulates sterilized water after being used in the sterilization tank to the sterilization tank without going through the hypochlorous acid supply unit In the sterilization process of supplying sterilization water to the sterilization tank and sterilizing the object in the sterilization tank, the sterilization water after being used in the sterilization tank is suitable for performing the sterilization process. And a control means for re-supplying the sterilization tank with the sterilized water after being used in the sterilization tank through the bypass pipe when maintaining the chlorous acid concentration and PH. .

この滅菌装置は、滅菌槽で使用された後の滅菌処理水が、滅菌処理を行なうのに適した次亜塩素酸濃度及びPHを維持している場合に、バイパス配管を通して滅菌槽で使用された後の滅菌処理水を滅菌槽に再供給するようになっているので、生成した次亜塩素酸の有効利用を図ることができる。また、バイパス配管を通して、滅菌槽内の滅菌処理水を入れ替えながら滅菌処理が行なわれるので、効率良く滅菌処理が行なえる。   This sterilizer was used in the sterilization tank through the bypass pipe when the sterilized water after being used in the sterilization tank maintained the hypochlorous acid concentration and PH suitable for performing the sterilization process. Since the subsequent sterilized water is supplied again to the sterilization tank, the generated hypochlorous acid can be effectively used. Further, since the sterilization process is performed through the bypass pipe while replacing the sterilization water in the sterilization tank, the sterilization process can be performed efficiently.

制御手段は、滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサと、滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、第1センサで測定された次亜塩素酸濃度及びPHが記憶手段に記憶された次亜塩素酸濃度の範囲及びPHの範囲内である場合に、滅菌槽で使用された後の滅菌処理水を、バイパス配管を通して滅菌槽に再供給するようにするとよい。   The control means includes a first sensor for measuring hypochlorous acid concentration and PH of sterilized water after being used in the sterilization tank, and a range of hypochlorous acid concentration of sterilized water suitable for performing sterilization. And storage means for storing the PH range, and the hypochlorous acid concentration and PH measured by the first sensor are within the hypochlorous acid concentration range and PH range stored in the storage means. In addition, the sterilized water after being used in the sterilization tank may be re-supplied to the sterilization tank through the bypass pipe.

また、滅菌装置は、被処理物を入れる滅菌槽と、次亜塩素酸濃度及びPHを調整して次亜塩素酸を含んだ滅菌処理水を供給する次亜塩素酸供給部と、次亜塩素酸供給部から滅菌槽に滅菌処理水を供給する供給配管と、供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサと、滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、滅菌槽で使用された後の滅菌処理水を、供給配管に再供給するとともに、第2センサで測定された滅菌処理水の次亜塩素酸濃度及びPHが、記憶手段に記憶された次亜塩素酸濃度及びPHの範囲内になるように、次亜塩素酸供給部から供給する滅菌処理水の次亜塩素酸濃度及びPHを調整する制御手段を備えているとよい。この場合は、供給配管に再供給された滅菌槽で使用された後の滅菌処理水は、供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサに基づいて、次亜塩素酸濃度及びPHが調整されて滅菌槽に再供給されるので、生成した次亜塩素酸の有効利用を図ることができ、また、滅菌槽内の滅菌処理水を入れ替えながら滅菌処理が行なわれるので、効率良く滅菌処理が行なえる。   In addition, the sterilizer includes a sterilization tank for storing an object to be treated, a hypochlorous acid supply unit that adjusts hypochlorous acid concentration and pH and supplies sterilized water containing hypochlorous acid, and hypochlorous acid. A supply pipe for supplying sterilized water from the acid supply unit to the sterilization tank, a second sensor for measuring hypochlorous acid concentration and pH of the sterilized water supplied from the supply pipe to the sterilization tank, and sterilization Storage means for storing the hypochlorous acid concentration range and the PH range suitable for sterilization water, and re-supplying the sterilization water after being used in the sterilization tank to the supply pipe, Sterilization supplied from the hypochlorous acid supply unit so that the hypochlorous acid concentration and PH measured by the two sensors are within the range of the hypochlorous acid concentration and PH stored in the storage means. Control means for adjusting hypochlorous acid concentration and pH of treated water Good. In this case, the sterilized water after being used in the sterilization tank re-supplied to the supply pipe is the second sensor for measuring the hypochlorous acid concentration and PH of the sterilized water supplied from the supply pipe to the sterilization tank. Therefore, the hypochlorous acid concentration and pH are adjusted and re-supplied to the sterilization tank, so that the generated hypochlorous acid can be used effectively, and the sterilized water in the sterilization tank is replaced. However, since sterilization is performed, sterilization can be performed efficiently.

また、制御手段は、滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサと、供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサとを備え、制御装置が、第2センサによって測定された次亜塩素酸濃度と、第1センサにより測定された次亜塩素酸濃度とを比べて、供給配管から滅菌槽に供給される滅菌処理水に比べて、滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度が所定以上の低下しているか否かを判定することにより、被処理物に残留する汚れの程度を判定する汚れ判定手段を備えているとよい。この場合、被処理物に有機物などの汚れが多く残留している場合には、次亜塩素酸と有機物などの汚れの成分とが反応してしまい、次亜塩素酸の濃度がすぐに著しく低下し、次亜塩素酸の殺菌作用を利用した効率の良い滅菌処理が実現できない場合があるが、この汚れ判定手段により、汚れ有りと判定される場合には滅菌装置を中断し、被処理物の洗浄を行なうようにすればよいので、次亜塩素酸の有効利用を図ることができる。   Further, the control means includes a first sensor for measuring hypochlorous acid concentration and PH of the sterilized water after being used in the sterilization tank, and hypochlorous acid of the sterilized water supplied from the supply pipe to the sterilization tank. A second sensor for measuring concentration and pH, and the control device compares the hypochlorous acid concentration measured by the second sensor with the hypochlorous acid concentration measured by the first sensor, and supplies the piping Compared with the sterilized water supplied to the sterilization tank from the sterilization tank, it is determined whether or not the hypochlorous acid concentration of the sterilized water after being used in the sterilization tank is lower than a predetermined level. It is preferable to include a stain determination means for determining the degree of stain remaining on the surface. In this case, if a lot of dirt such as organic matter remains on the object to be treated, hypochlorous acid reacts with the dirt component such as organic matter, and the concentration of hypochlorous acid decreases rapidly. However, efficient sterilization using the sterilizing action of hypochlorous acid may not be realized, but if this dirt determination means determines that there is dirt, the sterilizer is interrupted and Since it is sufficient to perform cleaning, hypochlorous acid can be effectively used.

また、制御手段は、滅菌処理の初期段階において、滅菌処理を行なうのに適した滅菌処理水よりも、次亜塩素酸濃度が低い水を滅菌槽に供給し、汚れ判定手段により被処理物に残留する汚れの程度を判定するとよい。供給する次亜塩素酸濃度を低くしておくと、被処理物に汚れが残留している場合に滅菌槽を通過した水の次亜塩素酸濃度が極めて低い状態になるので、その差が顕著なものになるので汚れ判定が容易かつ精度良く行なえるようになる。   In addition, the control means supplies water having a hypochlorous acid concentration lower than sterilized water suitable for performing sterilization treatment to the sterilization tank in the initial stage of sterilization treatment, and applies the soil determination means to the object to be treated. The degree of remaining dirt should be determined. If the concentration of hypochlorous acid to be supplied is kept low, the concentration of hypochlorous acid in the water that has passed through the sterilization tank will be extremely low when dirt remains on the object to be treated. Therefore, it is possible to easily and accurately determine the dirt.

また、制御手段は、滅菌処理時間を記録するタイマーと、滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、滅菌槽内を、タイマーに記録された一定時間、記憶手段に記憶された所定の次亜塩素酸濃度の範囲内に維持されたか否かを判定する完全滅菌判定処理を行なうようにするとよい。   The control means includes a timer for recording the sterilization time, and a storage means for storing the range of hypochlorous acid concentration and pH range of sterilized water suitable for performing the sterilization process. It is preferable to perform a complete sterilization determination process for determining whether or not the inside has been maintained within a predetermined hypochlorous acid concentration range stored in the storage means for a fixed time recorded in the timer.

この場合、滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサと、供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサとを備え、第1センサと第2センサにより測定される滅菌槽で使用された後の滅菌処理水と、滅菌槽に供給される滅菌処理水の次亜塩素酸濃度が、タイマーに記録された一定時間、記憶手段に記憶された所定の次亜塩素酸濃度の範囲内に維持されたか否かを判定することにより、完全滅菌判定処理を行なうとよい。   In this case, the first sensor for measuring the hypochlorous acid concentration and PH of the sterilized water after being used in the sterilization tank, and the hypochlorous acid concentration and PH of the sterilized water supplied from the supply pipe to the sterilization tank. A second sensor for measuring sterilization water after being used in the sterilization tank measured by the first sensor and the second sensor, and a hypochlorous acid concentration of the sterilization water supplied to the sterilization tank. The complete sterilization determination process may be performed by determining whether or not the predetermined hypochlorous acid concentration stored in the storage means is maintained for a certain period of time recorded in the timer.

また、滅菌槽内の滅菌処理水の次亜塩素酸及びPHを測定する第3センサと、滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、第3センサにより測定される滅菌槽内の滅菌処理水の次亜塩素酸濃度が、タイマーに記録された一定時間、記憶手段に記憶された所定の次亜塩素酸濃度の範囲内に維持されたか否かを判定することにより、完全滅菌判定処理を行なうようにしてもよい。   In addition, the third sensor for measuring hypochlorous acid and PH of sterilized water in the sterilization tank, and the range of hypochlorous acid concentration and PH range of sterilized water suitable for sterilization are stored. A predetermined hypochlorous acid concentration stored in the storage means for a certain period of time when the concentration of hypochlorous acid in the sterilization tank measured by the third sensor is recorded in the timer. The complete sterilization determination process may be performed by determining whether or not the value is maintained within the range.

また、滅菌槽で使用された後の滅菌処理水からゴミを除去するフィルタを備えているとよい。また、滅菌槽で使用された後の滅菌処理水からトリハロメタンを除去するフィルタを備え、バイパス配管を通してトリハロメタンを除去した水を循環させることにより、被処理物からトリハロメタンを除去するすすぎ処理を行なうようにするとよい。   Moreover, it is good to provide the filter which removes garbage from the sterilization process water after being used with the sterilization tank. In addition, a filter that removes trihalomethane from sterilized water after being used in a sterilization tank is provided, and the water from which trihalomethane has been removed is circulated through a bypass pipe so as to perform a rinsing process that removes trihalomethane from an object to be treated. Good.

この滅菌装置は、衣類などの洗濯機(大型のリネン装置を含む)や、食器洗浄器や、内視鏡や医療器具の洗浄装置などの用途に用いることができる。これらの用途ではこの滅菌装置による滅菌処理は洗浄工程後に行なうようにするとよい。   This sterilizer can be used for washing machines such as clothes (including large linen devices), dishwashers, endoscopes, and cleaning devices for medical instruments. In these applications, the sterilization process using this sterilizer is preferably performed after the cleaning process.

本発明に係る滅菌装置は、滅菌処理水の有効利用ができ、また、次亜塩素酸濃度及びPHを管理しつつ滅菌時間を確実に滅菌処理を行なうことができる。   The sterilization apparatus according to the present invention can effectively use sterilized water, and can reliably perform sterilization time while managing hypochlorous acid concentration and PH.

以下、本発明の実施形態に係る滅菌装置を図面に基づいて説明する。   Hereinafter, a sterilization apparatus according to an embodiment of the present invention will be described with reference to the drawings.

この滅菌装置1は、図1に示すように、被処理物を入れる滅菌槽2と、次亜塩素酸を生成し、次亜塩素酸の濃度を調整した滅菌処理水を供給する次亜塩素酸供給部3と、供給配管4と、バイパス配管5と、制御装置6とを備えている。なお、図1中、7は次亜塩素酸供給部3に水(水道水)を供給する供給部であり、8は滅菌槽2から使用後の滅菌処理水を排水する排水管であり、9は排水管8に取り付けた弁であり、10はゴミなどを除去するフィルタである。   As shown in FIG. 1, the sterilizer 1 includes a sterilization tank 2 in which an object to be treated is placed, hypochlorous acid that generates hypochlorous acid and supplies sterilized water having a adjusted concentration of hypochlorous acid. A supply unit 3, a supply pipe 4, a bypass pipe 5, and a control device 6 are provided. In FIG. 1, 7 is a supply unit that supplies water (tap water) to the hypochlorous acid supply unit 3, 8 is a drain pipe that drains used sterilized water from the sterilization tank 2, and 9 Is a valve attached to the drain pipe 8, and 10 is a filter for removing dust and the like.

供給配管4は、次亜塩素酸供給部3で生成され、又は、次亜塩素酸の濃度が調整された滅菌処理水を滅菌槽2に供給する配管である。この実施形態では、供給配管4はポンプ11と噴射ノズル12が取り付けられており、滅菌槽2内に滅菌処理水を噴射するようになっている。   The supply pipe 4 is a pipe that supplies the sterilization tank 2 with sterilized water generated by the hypochlorous acid supply unit 3 or adjusted in concentration of hypochlorous acid. In this embodiment, the supply pipe 4 is provided with a pump 11 and an injection nozzle 12 so as to inject sterilized water into the sterilization tank 2.

バイパス配管5は、滅菌槽2から供給配管4に配設された配管であり、滅菌槽2で使用された後の滅菌処理水を、次亜塩素酸供給部3を経由せずに、供給配管4に戻し、滅菌槽2に再供給する配管である。バイパス配管5の中間部には弁13とポンプ14を備えており、さらにバイパス配管5にバイパスさせ、弁15とフィルタ16が取り付けられた配管17を備えている。フィルタ16はトリハロメタンを除去するフィルタであり、例えば、活性炭ろ過器や、活性炭ろ過器に逆浸透膜ろ過器を付加したフィルタが用いられている。なお、より好ましくはろ過器には逆洗浄装置を備えたものを用いると良い。   The bypass pipe 5 is a pipe arranged from the sterilization tank 2 to the supply pipe 4, and supplies the sterilized water after being used in the sterilization tank 2 without going through the hypochlorous acid supply unit 3. The pipe is returned to 4 and re-supplied to the sterilization tank 2. An intermediate portion of the bypass pipe 5 includes a valve 13 and a pump 14, and further includes a pipe 17 to which the bypass pipe 5 is bypassed and a valve 15 and a filter 16 are attached. The filter 16 is a filter that removes trihalomethane. For example, an activated carbon filter or a filter obtained by adding a reverse osmosis membrane filter to the activated carbon filter is used. More preferably, a filter equipped with a back cleaning device is used.

制御装置6は、滅菌槽2で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサ(21、22)と、滅菌槽2に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサ(23、24)と、滅菌槽2内の滅菌処理水の次亜塩素酸濃度及びPHを測定する第3センサ(25、26)と、タイマー27と、記憶手段28と、コントローラ29とを備えている。   The control device 6 includes a first sensor (21, 22) for measuring the hypochlorous acid concentration and PH of the sterilized water after being used in the sterilization tank 2, and the next of the sterilized water supplied to the sterilization tank 2. A second sensor (23, 24) for measuring chlorous acid concentration and PH, a third sensor (25, 26) for measuring the hypochlorous acid concentration and PH of sterilized water in the sterilization tank 2, and a timer 27 And a storage means 28 and a controller 29.

この実施形態では、図1に示すように、バイパス配管5、供給配管4及び滅菌槽2にそれぞれ次亜塩素酸濃度センサとPHセンサが取り付けられている。バイパス配管5に取り付けられた次亜塩素酸濃度センサ21とPHセンサ22は、滅菌槽2で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定するようになっている。また供給配管4に取り付けられた次亜塩素酸濃度センサ23とPHセンサ24は、滅菌槽2に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定するするようになっている。また、滅菌槽2に取り付けられた次亜塩素酸濃度センサ25とPHセンサ26は、滅菌槽2内の滅菌処理水の次亜塩素酸濃度及びPHを測定するようになっている。そして、各次亜塩素酸濃度センサ21、23、25とPHセンサ22、24、26の測定信号は、それぞれコントローラ29に送られるようになっている。コントローラ29は、次亜塩素酸濃度センサ21、23、25とPHセンサ22、24、26の測定信号に基づいて、所定の制御プログラムに沿って、弁9、13を開閉操作するアクチュエータ及び次亜塩素酸供給部3などに制御信号を出すようになっている。   In this embodiment, as shown in FIG. 1, a hypochlorous acid concentration sensor and a PH sensor are attached to the bypass pipe 5, the supply pipe 4, and the sterilization tank 2, respectively. A hypochlorous acid concentration sensor 21 and a PH sensor 22 attached to the bypass pipe 5 measure the hypochlorous acid concentration and PH of sterilized water after being used in the sterilization tank 2. A hypochlorous acid concentration sensor 23 and a PH sensor 24 attached to the supply pipe 4 measure the hypochlorous acid concentration and PH of the sterilized water supplied to the sterilization tank 2. The hypochlorous acid concentration sensor 25 and the PH sensor 26 attached to the sterilization tank 2 measure the hypochlorous acid concentration and PH of the sterilized water in the sterilization tank 2. The measurement signals from the hypochlorous acid concentration sensors 21, 23, 25 and the PH sensors 22, 24, 26 are sent to the controller 29. Based on the measurement signals of the hypochlorous acid concentration sensors 21, 23, 25 and the PH sensors 22, 24, 26, the controller 29 performs actuators for opening and closing the valves 9, 13 and hypoxia according to a predetermined control program. A control signal is output to the chloric acid supply unit 3 and the like.

また、タイマー27は滅菌処理時間を設定するものであり、次亜塩素酸により細菌が死滅する時間を考慮して十分な滅菌効果が得られる時間が設定されている。また記憶手段28には滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲が記憶されている。   The timer 27 sets the sterilization time, and is set to a time when a sufficient sterilization effect can be obtained in consideration of the time when bacteria are killed by hypochlorous acid. The storage means 28 stores a hypochlorous acid concentration range and a PH range that are suitable for sterilization.

次亜塩素酸供給部3は、供給部7から供給された水(例えば、水道水)で、塩酸と次亜塩素酸ナトリウムを水で希釈し、濃度を調整することで次亜塩素酸を多く含む滅菌処理水を生成したり、供給部7から供給された水(例えば、水道水)に電解質(例えば、食塩)を注入して電気分解したりして滅菌処理水を得ている。(なお、供給部7から供給された水が、水道水など電解質を十分に含んでいる場合には、電解質を注入せずにそのまま電気分解してもよい。)これにより、次亜塩素酸供給部3は、PHを調整して、次亜塩素酸を多く含む滅菌処理水を生成することができる。次亜塩素酸供給部3は、図示は省略するが、電解質の注入や電解処理をフィードバック制御して滅菌処理水に含まれる次亜塩素酸の濃度を調整することができるようになっている。例えば、生成槽内に次亜塩素酸濃度センサやPHセンサを備え、このセンサの測定信号を基に、電解質の注入や電解処理をフィードバック制御して滅菌処理水に含まれる次亜塩素酸の濃度を調整するとよい。   The hypochlorous acid supply unit 3 dilutes hydrochloric acid and sodium hypochlorite with water supplied from the supply unit 7 (for example, tap water) and adjusts the concentration to increase the amount of hypochlorous acid. The sterilized water is obtained by generating sterilized water that contains it, or by injecting electrolyte (for example, salt) into water (for example, tap water) supplied from the supply unit 7 and electrolyzing it. (In addition, when the water supplied from the supply unit 7 sufficiently contains an electrolyte such as tap water, it may be electrolyzed as it is without injecting the electrolyte.) Thereby, hypochlorous acid is supplied. The unit 3 can adjust the pH to generate sterilized water containing a large amount of hypochlorous acid. Although not shown in the figure, the hypochlorous acid supply unit 3 can adjust the concentration of hypochlorous acid contained in the sterilized water by feedback control of electrolyte injection and electrolytic treatment. For example, a hypochlorous acid concentration sensor and a PH sensor are provided in the production tank, and the concentration of hypochlorous acid contained in the sterilized water is controlled based on the measurement signal of this sensor by feedback control of electrolyte injection and electrolytic treatment. It is good to adjust.

また、次亜塩素酸供給部3は、図2に示すPHと有効塩素存在比との関係を利用し、電気分解、及び、塩酸と次亜塩素酸ソーダを入れてPH調整することにより、所定の酸性域に調整して、所望の次亜塩素酸濃度の滅菌処理水を効率良く発生させるものが望ましい。例えば、図2中ハッチングを付したPH4〜6程度の弱酸性域、望ましくはPH4.8〜5.8の弱酸性域にPHを調整して次亜塩素酸の濃度が高い滅菌処理水を効率良く発生させるとよい。なお、電気分解により得られるPH2.2〜3.0の強酸性域の電解水を滅菌処理水に用いても良い。   Further, the hypochlorous acid supply unit 3 uses the relationship between the PH and the effective chlorine abundance ratio shown in FIG. 2, and performs electrolysis and adjusts the pH by adding hydrochloric acid and sodium hypochlorite so as to obtain a predetermined value. It is desirable to adjust the acid range to efficiently generate sterilized water having a desired hypochlorous acid concentration. For example, sterilized water with a high concentration of hypochlorous acid can be obtained by adjusting the pH to a slightly acidic range of PH 4 to 6 with hatching in FIG. 2, preferably a weakly acidic range of PH 4.8 to 5.8. It should be generated well. In addition, you may use the electrolyzed water of the strongly acidic range of PH2.2-3.0 obtained by electrolysis for sterilization water.

次亜塩素酸供給部3の滅菌処理水の生成では、例えば、供給された水のPHが所望のPH域よりも高い場合には塩酸を注入してPHを下げ、供給された水のPHが所望のPH域よりも低い場合には苛性ソーダを注入してPHを上げるようにするとよい。また次亜塩素酸濃度が低い場合には電気分解を行なって次亜塩素酸濃度を上げ、次亜塩素酸濃度が高い場合には水道水などを供給することにより希釈して次亜塩素酸濃度を下げるようにするとよい。   In the generation of sterilized water in the hypochlorous acid supply unit 3, for example, when the supplied water has a pH higher than the desired PH range, hydrochloric acid is injected to lower the pH, and the supplied water has a PH of When the pH is lower than the desired pH range, caustic soda may be injected to increase the pH. If hypochlorous acid concentration is low, electrolysis is performed to increase hypochlorous acid concentration. If hypochlorous acid concentration is high, dilute by supplying tap water etc. to reduce hypochlorous acid concentration. It is good to lower.

以下、この滅菌装置の滅菌処理を説明する。   Hereinafter, the sterilization process of this sterilizer will be described.

図3はこの滅菌処理のフロー図を示したものである。この滅菌装置1は、次亜塩素酸供給部3により次亜塩素酸の濃度を所定の濃度に調整した滅菌処理水を、供給配管4を通して滅菌槽2に供給し、次亜塩素酸(HClO)の殺菌作用を利用して滅菌を行なう。なお、この滅菌装置1では予め洗浄工程で洗浄されたものなど汚れがほとんどないものを被処理物として滅菌処理で扱う。これは被処理物に有機物などの汚れが多く残留している場合には、次亜塩素酸と有機物などの汚れの成分とが反応してしまい、次亜塩素酸の濃度がすぐに著しく低下し、次亜塩素酸の殺菌作用を利用した効率の良い滅菌処理が実現できない場合があるからである。   FIG. 3 shows a flowchart of this sterilization process. The sterilizer 1 supplies sterilized water whose hypochlorous acid concentration is adjusted to a predetermined concentration by the hypochlorous acid supply unit 3 to the sterilization tank 2 through the supply pipe 4, and hypochlorous acid (HClO). Sterilize using the bactericidal action of In this sterilization apparatus 1, those that are hardly contaminated, such as those previously washed in the washing process, are handled as sterilization treatments. This is because if there is a lot of dirt such as organic matter remaining on the object to be treated, hypochlorous acid reacts with the dirt components such as organic matter, and the concentration of hypochlorous acid decreases rapidly. This is because an efficient sterilization process using the bactericidal action of hypochlorous acid may not be realized.

このため、この滅菌装置1の滅菌処理では、先ず被処理物の洗浄が十分に行なわれているかを判定する汚れ判定処理31を行なう。   For this reason, in the sterilization process of the sterilization apparatus 1, first, the dirt determination process 31 is performed to determine whether the object to be processed is sufficiently cleaned.

汚れ判定処理31は、滅菌槽2に供給された滅菌処理水と滅菌槽2で使用された後の滅菌処理水との間で、次亜塩素酸濃度が著しく低下している場合に、洗浄が十分に行なわれていないとの判定が行なわれるようになっている。この実施形態では、バイパス配管5と供給配管4に取り付けられた次亜塩素酸濃度センサ21、23の測定情報を基に判定され、供給配管4とバイパス配管5との間で次亜塩素酸濃度が著しく低下している場合には、被処理物の洗浄が十分に行なわれていないと判定される。なお、汚れ判定処理31で用いる次亜塩素酸濃度の低下に関する汚れの判定基準は、制御装置6の記憶手段28に記憶させておくとよい。   The dirt determination process 31 is performed when the concentration of hypochlorous acid is significantly reduced between the sterilized water supplied to the sterilization tank 2 and the sterilized water after being used in the sterilization tank 2. Judgment is made that it is not performed sufficiently. In this embodiment, the determination is made based on the measurement information of hypochlorous acid concentration sensors 21 and 23 attached to the bypass pipe 5 and the supply pipe 4, and the hypochlorous acid concentration between the supply pipe 4 and the bypass pipe 5 is determined. Is significantly reduced, it is determined that the workpiece is not sufficiently cleaned. In addition, it is preferable to store the determination criterion of the stain relating to the decrease in hypochlorous acid concentration used in the stain determination process 31 in the storage unit 28 of the control device 6.

この汚れ判定処理31において、被処理物の洗浄が十分に行なわれていないと判定された場合には、滅菌処理を中断し、被処理物の洗浄処理32を行なう処理を開始するようになっている(s1)。   In this dirt determination process 31, when it is determined that the object to be processed is not sufficiently cleaned, the sterilization process is interrupted, and the process of performing the object cleaning process 32 is started. (S1).

これは第1センサ(21、22)によって測定された次亜塩素酸濃度やPHが、前記第2センサ(23、24)によって測定された次亜塩素酸濃度やPHに比べて著しい差がある場合には、被処理物が十分に洗浄されておらず、有機物などを含む汚れが残留しており滅菌処理を行なう状態にないと判断できるからである。なお、継続するか中断するかの判定の基準となる、次亜塩素酸濃度又はPHの差についての情報は記憶手段28に記憶させておくと良い。   This is because the hypochlorous acid concentration and PH measured by the first sensor (21, 22) are significantly different from the hypochlorous acid concentration and PH measured by the second sensor (23, 24). In this case, it can be determined that the object to be treated is not sufficiently cleaned, and dirt including organic matters remains, so that the sterilization process is not performed. It should be noted that information on the hypochlorous acid concentration or the difference in PH, which is a criterion for determining whether to continue or stop, may be stored in the storage unit 28.

この実施形態では、供給配管4に噴射ノズル12とポンプ11を設けて次亜塩素酸を含んだ滅菌処理水を噴射することにより、汚れの検知がより確実に行なえるようになっている。また、汚れ判定処理31では滅菌処理の場合よりも次亜塩素酸濃度が低い電解水を用いるのが好ましい。このように供給する次亜塩素酸濃度を低くしておくと、汚れが残留している場合に滅菌槽2を通過した水の次亜塩素酸濃度が極めて低い状態になり、その差が顕著なものになるので判定が容易になる。   In this embodiment, by providing the injection nozzle 12 and the pump 11 in the supply pipe 4 and injecting sterilized water containing hypochlorous acid, contamination can be detected more reliably. In the soil determination process 31, it is preferable to use electrolyzed water having a lower hypochlorous acid concentration than in the case of sterilization. When the concentration of hypochlorous acid supplied in this way is kept low, the concentration of hypochlorous acid in the water that has passed through the sterilization tank 2 becomes extremely low when dirt remains, and the difference is remarkable. Since it becomes a thing, determination becomes easy.

なお、汚れ判定処理において、「被処理物の洗浄処理を行なう処理」には、被処理物の洗浄処理32を行なわせる種々の処理が含まれる。例えば、滅菌槽2に洗浄槽を兼ねさせ、制御装置6の制御信号により、滅菌槽2に滅菌処理水を供給するのを止め、滅菌槽2に洗剤を入れて洗浄を行なわせる処理や、作業者に被処理物の洗浄が不十分であることを知らせる信号を発して、作業者に然るべき洗浄処理を行なわせるようにする処理が含まれる。この滅菌装置1は、上記汚れ判定処理31で被処理物の洗浄が十分に行なわれていることを確保してから、滅菌処理33を行なうようになっているので、被処理物の洗浄が不十分なために、生成した次亜塩素酸が滅菌処理以外で消費されるのを防止することができる。   In the stain determination process, the “process for cleaning the object to be processed” includes various processes for causing the object to be cleaned 32 to be cleaned. For example, the sterilization tank 2 is also used as a washing tank, and the control signal from the control device 6 stops the supply of sterilized water to the sterilization tank 2 and puts the detergent into the sterilization tank 2 for cleaning. This includes a process for issuing a signal notifying the operator that the workpiece is not sufficiently cleaned so that the worker can perform an appropriate cleaning process. Since the sterilization apparatus 1 performs the sterilization process 33 after ensuring that the object to be processed is sufficiently cleaned in the dirt determination process 31, the object to be processed cannot be cleaned. This is sufficient to prevent the generated hypochlorous acid from being consumed outside the sterilization treatment.

次に、この滅菌装置1は、図3に示すように、上記汚れ判定処理31で被処理物の洗浄(有機物などの除去)が十分に行なわれていることを確保してから滅菌処理33を行なう(s2)。   Next, as shown in FIG. 3, the sterilization apparatus 1 performs the sterilization process 33 after ensuring that the object to be processed is sufficiently washed (removal of organic substances, etc.) in the dirt determination process 31. Perform (s2).

滅菌処理33は、次亜塩素酸供給部3で生成した滅菌処理水を、供給配管4を通して滅菌槽2に供給することにより行なわれる。このとき滅菌槽2の被処理物は、十分に洗浄されているので、また十分に清潔な状態が保たれている。そして、滅菌処理33が進むにつれて被処理物から細菌などが除去されていくので、滅菌槽2で消費される次亜塩素酸が徐々に減る。このため、滅菌槽2で使用された後の滅菌処理水には、再び滅菌処理で用いるのに十分な次亜塩素酸濃度を維持している場合が生じる。そこで、次亜塩素酸の有効利用を図るため、滅菌槽2で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定し、滅菌処理水としてそのまま使えるかを判定する再供給判定処理34を行なう(s3)。   The sterilization process 33 is performed by supplying the sterilized water generated by the hypochlorous acid supply unit 3 to the sterilization tank 2 through the supply pipe 4. At this time, the object to be processed in the sterilization tank 2 is sufficiently cleaned, and thus a sufficiently clean state is maintained. And since bacteria etc. are removed from a to-be-processed object as the sterilization process 33 progresses, the hypochlorous acid consumed in the sterilization tank 2 reduces gradually. For this reason, in the sterilized water after being used in the sterilization tank 2, there is a case where the hypochlorous acid concentration sufficient to be used again in the sterilization process is maintained. Therefore, in order to use hypochlorous acid effectively, the hypochlorous acid concentration and pH of the sterilized water after being used in the sterilization tank 2 are measured, and a resupply judgment is made to determine whether the sterilized water can be used as it is. Processing 34 is performed (s3).

具体的にこの実施形態に係る滅菌装置1では、滅菌槽2で使用された後の滅菌処理水は、フィルタ10で浮遊物などのゴミが除去されてバイパス配管5に流れていき、バイパス配管5に取り付けた第1センサ(21、22)によって次亜塩素酸濃度及びPHが測定されようになっている。そして、制御装置6において、第1センサ(21、22)の測定信号に基づいて、第1センサ(21、22)で測定された次亜塩素酸濃度及びPHが、それぞれ記憶手段28に記憶させた次亜塩素酸濃度及びPHの範囲内である場合に、バイパス配管5の滅菌処理水はそのまま滅菌処理に使えると判定し、範囲外の場合にバイパス配管5の滅菌処理水はそのまま滅菌処理に使えないと判定する。   Specifically, in the sterilization apparatus 1 according to this embodiment, the sterilized water after being used in the sterilization tank 2 flows to the bypass pipe 5 after the dust such as suspended matters is removed by the filter 10, and the bypass pipe 5 Hypochlorous acid concentration and PH are measured by the first sensors (21, 22) attached to the. Then, in the control device 6, based on the measurement signal of the first sensor (21, 22), the hypochlorous acid concentration and PH measured by the first sensor (21, 22) are stored in the storage means 28, respectively. When the concentration of hypochlorous acid is within the range of PH, the sterilized water in the bypass pipe 5 is determined to be usable for sterilization as it is. It is determined that it cannot be used.

この再供給判定処理34でバイパス配管5の滅菌処理水はそのまま滅菌処理に使えないと判定された場合には、弁9を開け、滅菌槽2で使用された後の滅菌処理水を排水管8から排水する排水処理35を行なう(s4)。また、この再供給判定処理34で、バイパス配管5の滅菌処理水はそのまま滅菌処理に使えると判定された場合には、滅菌槽2で使用された後の滅菌処理水をバイパス配管5、供給配管4を通して滅菌槽2に再供給する再供給処理36を行なう(s5)。この実施形態では、再供給処理36では、制御装置6は各弁9、13、15を開閉操作するアクチュエータに制御信号を発して、弁9、15を閉じ、バイパス配管5の弁13を開け、ポンプ14を駆動させて、滅菌槽2で使用された後の滅菌処理水をバイパス配管5及び供給配管4を通して滅菌槽2に再供給するようにする。この再供給処理36により、生成した次亜塩素酸の有効利用を図ることができる。また、滅菌槽2内の滅菌処理水を入れ替えながら滅菌処理を行なっているので、効率良く滅菌処理が行なえる。なお、排水処理35で排水された水は、十分に清潔な状態にあるので、洗浄などの他の用途に利用できる。   When it is determined in the resupply determination process 34 that the sterilized water in the bypass pipe 5 cannot be used for sterilization as it is, the valve 9 is opened, and the sterilized water after being used in the sterilization tank 2 is discharged into the drain pipe 8. Then, the waste water treatment 35 for draining is performed (s4). If it is determined in this resupply determination process 34 that the sterilized water in the bypass pipe 5 can be used for sterilization as it is, the sterilized water after being used in the sterilization tank 2 is used as the bypass pipe 5 and the supply pipe. Then, a resupply process 36 for resupplying to the sterilization tank 2 through 4 is performed (s5). In this embodiment, in the resupply process 36, the control device 6 issues a control signal to an actuator that opens and closes the valves 9, 13, 15, closes the valves 9, 15, opens the valve 13 of the bypass pipe 5, The pump 14 is driven so that the sterilized water after being used in the sterilization tank 2 is re-supplied to the sterilization tank 2 through the bypass pipe 5 and the supply pipe 4. By this resupply process 36, the produced hypochlorous acid can be effectively used. In addition, since the sterilization process is performed while replacing the sterilization process water in the sterilization tank 2, the sterilization process can be performed efficiently. In addition, since the water drained by the waste water treatment 35 is in a sufficiently clean state, it can be used for other purposes such as washing.

次に、この滅菌装置1は、再供給処理36が行なわれている状態において、完全滅菌を判定する完全滅菌判定処理37を行なう(s6)。   Next, the sterilizer 1 performs a complete sterilization determination process 37 for determining complete sterilization in a state where the resupply process 36 is performed (s6).

完全滅菌判定処理37では、滅菌槽2で使用された後の滅菌処理水がバイパス配管5、供給配管4を通して滅菌槽2に再供給されている状態が、タイマー27に記憶された一定時間維持されているか否かを判定する。これにより、滅菌槽2内を、一定時間、滅菌処理水の次亜塩素酸が所定の濃度より高い状態に維持されたか否かを判定することができるので、細菌を完全に死滅させたか否かの判定を行なうことができる。この実施形態では、完全滅菌判定処理37は、制御装置6において、滅菌槽2で使用された後の滅菌処理水がバイパス配管5、供給配管4を通して滅菌槽2に再供給されている状態が、タイマー27に記憶された一定時間維持されたか否かを判定させることにより実現させている。   In the complete sterilization determination process 37, the state in which the sterilized water after being used in the sterilization tank 2 is re-supplied to the sterilization tank 2 through the bypass pipe 5 and the supply pipe 4 is maintained for a certain period of time stored in the timer 27. It is determined whether or not. This makes it possible to determine whether or not the hypochlorous acid in the sterilized water has been maintained at a level higher than the predetermined concentration in the sterilization tank 2 for a certain period of time, so whether or not the bacteria have been completely killed. Can be determined. In this embodiment, in the complete sterilization determination process 37, the control device 6 is in a state where the sterilized water after being used in the sterilization tank 2 is re-supplied to the sterilization tank 2 through the bypass pipe 5 and the supply pipe 4. This is realized by determining whether or not the fixed time stored in the timer 27 is maintained.

なお、完全滅菌判定処理37は、滅菌槽2内の滅菌処理水の次亜塩素酸濃度及びPHを測定する第3センサ(25、26)及びタイマー27を利用して、滅菌槽2で使用される滅菌処理水の次亜塩素酸が所定の濃度より高い状態及び所定の範囲内のPHに、一定時間、維持されたか否かを判定してもよい。上記完全滅菌判定処理37により、滅菌槽2で使用される滅菌処理水の次亜塩素酸が所定の濃度より高い状態及び所定の範囲内のPHに、一定時間、維持されたことが判定された場合には、完全滅菌処理を完了する。   The complete sterilization determination process 37 is used in the sterilization tank 2 by using the third sensor (25, 26) and the timer 27 for measuring the hypochlorous acid concentration and PH of the sterilized water in the sterilization tank 2. It may be determined whether or not hypochlorous acid in the sterilized water is maintained for a certain period of time at a pH higher than a predetermined concentration and at a PH within a predetermined range. By the complete sterilization determination process 37, it was determined that the hypochlorous acid of the sterilized water used in the sterilization tank 2 was maintained for a certain period of time in a state higher than a predetermined concentration and at a PH within a predetermined range. In some cases, complete sterilization is completed.

次に、この滅菌装置1は、すすぎ処理38を行なう(s7)。すすぎ処理38は主に被処理物からトリハロメタンを除去して、被処理物の安全性を確保する処理である。この実施形態では、すすぎ処理38は、弁9及び13を閉じ、弁15を開け、バイパス配管5を循環する滅菌処理水をバイパス配管5にバイパスさせた配管17に通し、フィルタ16によりトリハロメタンを除去した水を、一定時間滅菌槽2に循環させることにより行なう。滅菌槽2ではトリハロメタンを除去した水を噴射ノズル12から被処理物に噴射してすすぎ処理を行なう。このすすぎ処理では滅菌処理水の有効利用を図ることができる。この滅菌装置1は、上記すすぎ処理38により、トリハロメタンの除去が完了した後に、滅菌処理を完了させる。   Next, the sterilizer 1 performs a rinsing process 38 (s7). The rinsing process 38 is a process that mainly removes trihalomethane from the object to be processed and ensures the safety of the object to be processed. In this embodiment, the rinsing process 38 closes the valves 9 and 13, opens the valve 15, passes the sterilized water circulating in the bypass pipe 5 through the pipe 17 bypassed to the bypass pipe 5, and removes the trihalomethane by the filter 16. The circulated water is circulated through the sterilization tank 2 for a certain period of time. In the sterilization tank 2, the water from which the trihalomethane has been removed is sprayed from the spray nozzle 12 onto the object to be treated, thereby performing a rinsing process. In this rinsing process, the sterilized water can be effectively used. The sterilization apparatus 1 completes the sterilization process after the rinsing process 38 completes the removal of the trihalomethane.

以上、本発明の滅菌装置の一実施形態を説明したが、本発明に係る滅菌装置は上記の実施形態に限定されるものではない。   As mentioned above, although one Embodiment of the sterilizer of this invention was described, the sterilizer which concerns on this invention is not limited to said embodiment.

例えば、次亜塩素酸の有効利用を図る他の実施形態として、図4に示すように、滅菌槽2で使用された後の滅菌処理水を、供給配管4に再供給するとともに、第2センサ(23、24)で測定された供給配管4の滅菌処理水の次亜塩素酸濃度及びPHが、記憶手段28に記憶された次亜塩素酸濃度及びPHの範囲内になるように、次亜塩素酸供給部3から供給する滅菌処理水の次亜塩素酸濃度及びPHを調整する制御をしてもよい。   For example, as another embodiment for effectively using hypochlorous acid, as shown in FIG. 4, the sterilized water after being used in the sterilization tank 2 is re-supplied to the supply pipe 4 and the second sensor The hypochlorous acid concentration and PH of the sterilized water of the supply pipe 4 measured in (23, 24) are within the ranges of the hypochlorous acid concentration and PH stored in the storage means 28. You may control to adjust the hypochlorous acid concentration and PH of the sterilization process water supplied from the chloric acid supply part 3. FIG.

具体的には、滅菌処理において、滅菌槽2で使用された後の滅菌処理水を、バイパス配管5を通して供給配管4に供給41する(s4’)。次に、第2センサ(23、24)で測定された供給配管4から滅菌槽2に供給する滅菌処理水の次亜塩素酸濃度及びPHが、記憶手段28に記憶された次亜塩素酸濃度の範囲及びPHの範囲内になるように、次亜塩素酸供給部3で次亜塩素酸濃度及びPHを調整した滅菌処理水を供給配管4に供給し、供給配管4内の滅菌処理水の次亜塩素酸濃度及びPHを調整42する(s5’)。そして、このようにして次亜塩素酸濃度及びPHを調整した滅菌処理水を滅菌槽2に再供給43するとよい(s6)。   Specifically, in the sterilization process, the sterilized water after being used in the sterilization tank 2 is supplied 41 to the supply pipe 4 through the bypass pipe 5 (s4 '). Next, the hypochlorous acid concentration and PH of the sterilized water supplied to the sterilization tank 2 from the supply pipe 4 measured by the second sensor (23, 24) are stored in the storage means 28. Then, sterilized water whose hypochlorous acid concentration and PH are adjusted by the hypochlorous acid supply unit 3 is supplied to the supply pipe 4 so as to be within the range of PH and PH, and the sterilized water in the supply pipe 4 is supplied. Hypochlorous acid concentration and pH are adjusted 42 (s5 '). Then, the sterilized water whose hypochlorous acid concentration and PH have been adjusted in this way may be supplied 43 again to the sterilization tank 2 (s6).

この場合、バイパス配管5から供給配管4に供給される滅菌処理水と、次亜塩素酸供給部3から供給配管4に供給される滅菌処理水が、供給配管4内で混ざり合い、記憶手段28に記憶された次亜塩素酸濃度の範囲及びPHの範囲内の滅菌処理水を、常に供給配管4から滅菌槽2に供給することができる。従って、再供給判定処理34は必要が無くなり、また、上述の例で、再供給判定処理34でバイパス配管5の滅菌処理水はそのまま滅菌処理に使えないと判定された場合でも、滅菌槽2で使用された後の滅菌処理水を排水する排水処理35を行なう必要が無く、次亜塩素酸の有効利用を図ることができる。   In this case, the sterilized water supplied from the bypass pipe 5 to the supply pipe 4 and the sterilized water supplied from the hypochlorous acid supply unit 3 to the supply pipe 4 are mixed in the supply pipe 4 and stored in the storage means 28. The sterilized water within the range of hypochlorous acid concentration and the range of PH stored in can be always supplied from the supply pipe 4 to the sterilization tank 2. Accordingly, the resupply determination process 34 is not necessary, and in the above-described example, even if it is determined in the resupply determination process 34 that the sterilized water in the bypass pipe 5 cannot be used as it is for the sterilization process, It is not necessary to perform the waste water treatment 35 for draining the sterilized water after being used, and it is possible to effectively use hypochlorous acid.

また、滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサや、供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサの位置は、図1に図示される位置に限定されない。例えば、第1センサは滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定できればよく、滅菌槽の出口近傍に設けてもよいし、第2センサは供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定できればよく、滅菌槽の入口近傍や滅菌槽内のノズルに設けてもよい。   In addition, the first sensor that measures the hypochlorous acid concentration and PH of sterilized water after use in the sterilization tank, and the hypochlorous acid concentration and PH of sterilized water supplied from the supply pipe to the sterilization tank. The position of the second sensor to be measured is not limited to the position illustrated in FIG. For example, the first sensor only needs to be able to measure the hypochlorous acid concentration and PH of sterilized water after being used in the sterilization tank, and may be provided near the outlet of the sterilization tank. The second sensor is sterilized from the supply pipe. What is necessary is just to be able to measure the hypochlorous acid concentration and PH of the sterilized water supplied to the tank, and it may be provided in the vicinity of the inlet of the sterilization tank or in the nozzle in the sterilization tank.

また、滅菌装置1の用途は、例えば、衣類などの洗濯機(大型のリネン装置を含む)や、食器洗浄器や、内視鏡や医療器具の洗浄装置などの用途に用いることができる。特に、この滅菌装置1は、滅菌処理の確実性を保証できるので、食器洗浄器や内視鏡や医療器具の洗浄装置など衛生上の要求が高い用途になればなる程有効であり、また大型の装置になればなる程、次亜塩素酸の有効利用による経済的効果を得ることができる。また、リネン洗濯機では、次亜塩素酸を用いた滅菌処理を行っており、40℃程度の温度で完全滅菌処理が行なえるので、衣類を傷めなくて済む。また、上述した滅菌装置は、滅菌槽には滅菌処理水の反応を早めるため、撹拌器を備えたものを用いると良い。   The sterilization apparatus 1 can be used for applications such as washing machines for clothes (including large linen devices), dishwashers, endoscopes, and cleaning devices for medical instruments. In particular, since the sterilization apparatus 1 can guarantee the certainty of the sterilization process, it is more effective as it becomes a use with higher hygiene requirements such as a dishwasher, endoscope, and medical instrument cleaning apparatus. The more it becomes, the more economical effects can be obtained by the effective use of hypochlorous acid. Further, in the linen washing machine, sterilization using hypochlorous acid is performed, and complete sterilization can be performed at a temperature of about 40 ° C., so that clothes are not damaged. Moreover, in order to speed up the reaction of the sterilized water in the sterilization tank, the sterilization apparatus described above may be a device equipped with a stirrer.

本発明の一実施形態に係る滅菌装置の概略を示す平面図。The top view which shows the outline of the sterilizer which concerns on one Embodiment of this invention. PHと有効塩素存在比との関係を示す図。The figure which shows the relationship between PH and effective chlorine abundance ratio. 本発明の一実施形態に係る滅菌装置のフロー図。The flowchart of the sterilizer which concerns on one Embodiment of this invention. 本発明の他の実施形態に係る滅菌装置のフロー図。The flowchart of the sterilizer which concerns on other embodiment of this invention.

符号の説明Explanation of symbols

1 滅菌装置
2 滅菌槽
3 次亜塩素酸供給部
4 供給配管
5 バイパス配管
6 制御装置
7 供給部
8 排水管
9 弁
10 フィルタ
11 ポンプ
12 噴射ノズル
13 弁
14 ポンプ
15 弁
16 フィルタ
17 配管
21 次亜塩素酸濃度センサ
22 PHセンサ
23 次亜塩素酸濃度センサ
24 PHセンサ
25 次亜塩素酸濃度センサ
26 PHセンサ
27 タイマー
28 記憶手段
29 コントローラ
31 判定処理
32 洗浄処理
33 滅菌処理
34 再供給判定処理
35 排水処理
36 再供給処理
37 完全滅菌判定処理
38 すすぎ処理
DESCRIPTION OF SYMBOLS 1 Sterilizer 2 Sterilization tank 3 Hypochlorous acid supply part 4 Supply pipe 5 Bypass pipe 6 Control apparatus 7 Supply part 8 Drain pipe 9 Valve 10 Filter 11 Pump 12 Injection nozzle 13 Valve 14 Pump 15 Valve 16 Filter 17 Pipe 21 Pipe 21 Chloric acid concentration sensor 22 PH sensor 23 Hypochlorous acid concentration sensor 24 PH sensor 25 Hypochlorous acid concentration sensor 26 PH sensor 27 Timer 28 Storage means 29 Controller 31 Determination process 32 Cleaning process 33 Sterilization process 34 Resupply determination process 35 Drainage Process 36 Resupply process 37 Complete sterilization determination process 38 Rinse process

Claims (10)

被処理物を入れる滅菌槽と、
次亜塩素酸濃度及びPHを調整して次亜塩素酸を含んだ滅菌処理水を供給する次亜塩素酸供給部と、
前記次亜塩素酸供給部から滅菌槽に滅菌処理水を供給する供給配管と、
前記滅菌槽で使用された後の滅菌処理水を、前記次亜塩素酸供給部を経由せずに滅菌槽に再供給するバイパス配管と、
前記滅菌槽に滅菌処理水を供給して滅菌槽内の被処理物を滅菌処理する滅菌処理工程において、前記滅菌槽で使用された後の滅菌処理水が、滅菌処理を行なうのに適した次亜塩素酸濃度及びPHを維持している場合に、前記バイパス配管を通して滅菌槽で使用された後の滅菌処理水を滅菌槽に再供給するようにした制御手段とを備えていることを特徴とする滅菌装置。
A sterilization tank for storing the workpiece,
A hypochlorous acid supply unit that adjusts the hypochlorous acid concentration and pH to supply sterilized water containing hypochlorous acid; and
A supply pipe for supplying sterilized water to the sterilization tank from the hypochlorous acid supply unit;
Bypass piping for re-supplying the sterilized water after being used in the sterilization tank to the sterilization tank without going through the hypochlorous acid supply unit,
In the sterilization process of supplying sterilization water to the sterilization tank and sterilizing the object to be processed in the sterilization tank, the sterilization water after being used in the sterilization tank is suitable for performing the sterilization process. And a control means for re-supplying the sterilization tank with the sterilized water after being used in the sterilization tank through the bypass pipe when maintaining the chlorous acid concentration and PH. Sterilizer to do.
前記制御手段が、前記滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサと、前記滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、
前記第1センサで測定された次亜塩素酸濃度及びPHが前記記憶手段に記憶された次亜塩素酸濃度の範囲及びPHの範囲内である場合に、滅菌槽で使用された後の滅菌処理水を、前記バイパス配管を通して滅菌槽に再供給することを特徴とする請求項1に記載の滅菌装置。
The control means includes a first sensor for measuring hypochlorous acid concentration and PH of sterilized water after being used in the sterilization tank, and hypochlorous acid for sterilized water suitable for performing the sterilization process. Storage means for storing a concentration range and a PH range;
When the hypochlorous acid concentration and PH measured by the first sensor are within the range of hypochlorous acid concentration and PH stored in the storage means, the sterilization treatment after use in the sterilization tank The sterilizer according to claim 1, wherein water is supplied again to the sterilization tank through the bypass pipe.
被処理物を入れる滅菌槽と、
次亜塩素酸濃度及びPHを調整して次亜塩素酸を含んだ滅菌処理水を供給する次亜塩素酸供給部と、
前記次亜塩素酸供給部から滅菌槽に滅菌処理水を供給する供給配管と、
前記供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサと、前記滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、
前記滅菌槽で使用された後の滅菌処理水を、前記供給配管に再供給するとともに、前記第2センサで測定された滅菌処理水の次亜塩素酸濃度及びPHが、前記記憶手段に記憶された次亜塩素酸濃度及びPHの範囲内になるように、前記次亜塩素酸供給部から供給する滅菌処理水の次亜塩素酸濃度及びPHを調整する制御手段を備えていることを特徴とする滅菌装置。
A sterilization tank for storing the workpiece,
A hypochlorous acid supply unit that adjusts the hypochlorous acid concentration and pH to supply sterilized water containing hypochlorous acid; and
A supply pipe for supplying sterilized water to the sterilization tank from the hypochlorous acid supply unit;
A second sensor for measuring hypochlorous acid concentration and PH of sterilized water supplied to the sterilization tank from the supply pipe, a range of hypochlorous acid concentration of sterilized water suitable for performing the sterilization process, and Storage means for storing the PH range,
The sterilized water after being used in the sterilization tank is re-supplied to the supply pipe, and the hypochlorous acid concentration and PH measured by the second sensor are stored in the storage means. And a control means for adjusting the hypochlorous acid concentration and PH of the sterilized water supplied from the hypochlorous acid supply unit so as to be within the range of hypochlorous acid concentration and PH. Sterilizer to do.
前記制御手段が、前記滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサと、前記供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサとを備え、
前記制御装置が、前記第2センサによって測定された次亜塩素酸濃度と、前記第1センサにより測定された次亜塩素酸濃度とを比べて、供給配管から滅菌槽に供給される滅菌処理水に比べて、滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度が所定以上の低下しているか否かを判定することにより、被処理物に残留する汚れの程度を判定する汚れ判定手段を備えていることを特徴とする請求項1から3の何れかに記載の滅菌装置。
The control means includes a first sensor that measures hypochlorous acid concentration and pH of sterilized water after use in the sterilization tank, and hypochlorous acid supplied from the supply pipe to the sterilization tank. A second sensor for measuring acid concentration and pH,
The control device compares the hypochlorous acid concentration measured by the second sensor with the hypochlorous acid concentration measured by the first sensor, and sterilized water supplied from the supply pipe to the sterilization tank. Compared with, the degree of dirt remaining on the object to be treated is determined by determining whether or not the hypochlorous acid concentration in the sterilized water after use in the sterilization tank is lower than a predetermined level. The sterilizer according to any one of claims 1 to 3, further comprising a determination unit.
前記制御手段が、滅菌処理の初期段階において、滅菌処理を行なうのに適した滅菌処理水よりも、次亜塩素酸濃度が低い水を滅菌槽に供給し、前記汚れ判定手段により被処理物に残留する汚れの程度を判定していることを特徴とする請求項4に記載の滅菌装置。   In the initial stage of the sterilization process, the control unit supplies water having a hypochlorous acid concentration lower than sterilized water suitable for performing the sterilization process to the sterilization tank. 5. The sterilizer according to claim 4, wherein the degree of remaining dirt is determined. 前記制御手段が滅菌処理時間を記録するタイマーと、前記滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、前記滅菌槽内を、前記タイマーに記録された一定時間、前記記憶手段に記憶された所定の次亜塩素酸濃度の範囲内に維持されたか否かを判定する完全滅菌判定処理を行なうことを特徴とする請求項1から5の何れかに記載の滅菌装置。   The sterilization tank, wherein the control means includes a timer for recording a sterilization time, and a storage means for storing a range of hypochlorous acid concentration and pH range of sterilized water suitable for performing the sterilization process. A complete sterilization determination process is performed to determine whether or not the inside has been maintained within a predetermined hypochlorous acid concentration range stored in the storage means for a predetermined time recorded in the timer. Item 6. The sterilizer according to any one of Items 1 to 5. 前記滅菌槽で使用された後の滅菌処理水の次亜塩素酸濃度及びPHを測定する第1センサと、前記供給配管から滅菌槽に供給される滅菌処理水の次亜塩素酸濃度及びPHを測定する第2センサとを備え、
前記第1センサと第2センサにより測定される滅菌槽で使用された後の滅菌処理水と、滅菌槽に供給される滅菌処理水の次亜塩素酸濃度が、前記タイマーに記録された一定時間、前記記憶手段に記憶された所定の次亜塩素酸濃度の範囲内に維持されたか否かを判定することにより、前記完全滅菌判定処理を行なうことを特徴とする請求項6に記載の滅菌装置。
A first sensor for measuring hypochlorous acid concentration and PH of sterilized water after being used in the sterilization tank, and a hypochlorous acid concentration and PH of sterilized water supplied from the supply pipe to the sterilization tank. A second sensor for measuring,
The sterilized water after being used in the sterilization tank measured by the first sensor and the second sensor and the hypochlorous acid concentration of the sterilized water supplied to the sterilization tank are recorded for a certain period of time. The sterilization apparatus according to claim 6, wherein the complete sterilization determination process is performed by determining whether or not the concentration is maintained within a predetermined hypochlorous acid concentration range stored in the storage unit. .
前記滅菌槽内の滅菌処理水の次亜塩素酸及びPHを測定する第3センサと、前記滅菌処理を行なうのに適した滅菌処理水の次亜塩素酸濃度の範囲及びPHの範囲を記憶させた記憶手段とを備え、
前記第3センサにより測定される滅菌槽内の滅菌処理水の次亜塩素酸濃度が、前記タイマーに記録された一定時間、前記記憶手段に記憶された所定の次亜塩素酸濃度の範囲内に維持されたか否かを判定することにより、前記完全滅菌判定処理を行なうことを特徴とする請求項6に記載の滅菌装置。
A third sensor for measuring hypochlorous acid and PH of sterilized water in the sterilization tank, and a range of hypochlorous acid concentration and PH range of sterilized water suitable for performing the sterilization are stored. Storage means,
The hypochlorous acid concentration of the sterilized water in the sterilization tank measured by the third sensor is within a predetermined hypochlorous acid concentration range stored in the storage means for a predetermined time recorded in the timer. The sterilization apparatus according to claim 6, wherein the complete sterilization determination process is performed by determining whether or not the sterilization is maintained.
前記滅菌槽で使用された後の滅菌処理水からゴミを除去するフィルタを備えていることを特徴とする請求項1から8の何れかに記載の滅菌装置。   The sterilizer according to any one of claims 1 to 8, further comprising a filter for removing dust from sterilized water after being used in the sterilization tank. 前記滅菌槽で使用された後の滅菌処理水からトリハロメタンを除去するフィルタを備え、バイパス配管を通してトリハロメタンを除去した水を循環させることにより、被処理物からトリハロメタンを除去するすすぎ処理を備えていることを特徴とする請求項1から9の何れかに記載の滅菌装置。   It is equipped with a filter that removes trihalomethane from sterilized water after being used in the sterilization tank, and a rinsing treatment that removes trihalomethane from the object to be treated by circulating water from which trihalomethane has been removed through a bypass pipe. 10. The sterilizer according to any one of claims 1 to 9, wherein
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009511047A (en) * 2005-10-13 2009-03-19 イーコラブ インコーポレイティド Systems and methods for on-site regeneration, reconditioning, and reapplication of poultry treated water
JP2012200456A (en) * 2011-03-25 2012-10-22 Mitsubishi Heavy Industries Food & Packaging Machinery Co Ltd Method for treating bactericide solution and device for treating the bactericide solution
JPWO2016166862A1 (en) * 2015-04-16 2017-12-14 大和ハウス工業株式会社 Food cleaning equipment
JP2019063782A (en) * 2017-10-02 2019-04-25 株式会社ホクエツ Hypochlorous acid water generator with pH automatic measurement device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009511047A (en) * 2005-10-13 2009-03-19 イーコラブ インコーポレイティド Systems and methods for on-site regeneration, reconditioning, and reapplication of poultry treated water
JP2012200456A (en) * 2011-03-25 2012-10-22 Mitsubishi Heavy Industries Food & Packaging Machinery Co Ltd Method for treating bactericide solution and device for treating the bactericide solution
JPWO2016166862A1 (en) * 2015-04-16 2017-12-14 大和ハウス工業株式会社 Food cleaning equipment
JP2019063782A (en) * 2017-10-02 2019-04-25 株式会社ホクエツ Hypochlorous acid water generator with pH automatic measurement device

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