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JP6130745B2 - Peracetic acid disinfectant solution processing equipment - Google Patents
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JP6130745B2 - Peracetic acid disinfectant solution processing equipment - Google Patents

Peracetic acid disinfectant solution processing equipment Download PDF

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JP6130745B2
JP6130745B2 JP2013129735A JP2013129735A JP6130745B2 JP 6130745 B2 JP6130745 B2 JP 6130745B2 JP 2013129735 A JP2013129735 A JP 2013129735A JP 2013129735 A JP2013129735 A JP 2013129735A JP 6130745 B2 JP6130745 B2 JP 6130745B2
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peracetic acid
additive
sterilizer
disinfectant solution
circulation tank
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JP2015002855A (en
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健太 岡田
健太 岡田
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Mitsubishi Heavy Industries Machinery Systems Co Ltd
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Mitsubishi Heavy Industries Mechatronics Systems Ltd
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Description

本発明は、包装材料(以下、包材と称する。)殺菌用の殺菌剤溶液(以下、単に殺菌剤と称することがある。)が循環タンクから包材の殺菌機へ加熱装置を経由して高温状態で供給され、包材殺菌後の前記殺菌剤が前記殺菌機から前記循環タンクへ回収される循環回路を形成した過酢酸系殺菌剤溶液の処理装置に関する。 In the present invention, a bactericidal solution for sterilization of packaging material (hereinafter referred to as a packaging material) (hereinafter also referred to simply as a bactericidal agent) is transferred from a circulation tank to a packaging material sterilizer via a heating device. The present invention relates to an apparatus for treating a peracetic acid-based disinfectant solution that forms a circulation circuit that is supplied in a high temperature state and that recovers the disinfectant after sterilization of packaging material from the disinfecting machine to the circulation tank.

従来、包材殺菌用の殺菌剤が循環タンクから殺菌機へ供給され、包材殺菌後の前記殺菌剤が循環タンクへ回収される循環回路を形成した殺菌剤溶液の処理装置においては、殺菌剤を高温状態で殺菌機へ供給して包材殺菌効果を高めるようにする工夫、また、殺菌剤の濃度低下に伴って殺菌力が低下しないように殺菌剤を自動補充して所定の濃度に維持する工夫、さらには、殺菌剤に添加剤を添加して循環タンク内で添加剤との反応により殺菌力を強化させる工夫がなされてきた。   Conventionally, a disinfectant for treating a disinfectant solution that forms a circulation circuit in which a disinfectant for disinfecting packaging material is supplied from a circulation tank to a disinfection machine and the disinfectant after disinfecting the packaging material is collected into the recirculation tank To increase the sterilization effect of the packaging material by supplying the sterilizer to the sterilizer at a high temperature, and to maintain the prescribed concentration by automatically replenishing the sterilizing agent so that the sterilizing power does not decrease as the concentration of the sterilizing agent decreases In addition, a device has been devised to add an additive to the bactericide and enhance the bactericidal power by reaction with the additive in the circulation tank.

循環タンク内の反応によって殺菌剤の殺菌力強化作用を済ませた後の添加剤は、殺菌力強化に不活性となってしまい、前記不活性のものの割合が増加すると、殺菌剤の殺菌力強化作用が低下するので、前記不活性のものを添加剤捕集用フィルターによって捕集して、新しい添加剤を追加投入している(例えば、特許文献1参照)。
前記不活性になったものの粒子が細かい場合、前記添加剤捕集用フィルターは濾過部の目を細かいものとする必要があって目詰まりしやすいため、早期目詰まりを防止する技術への要望が高まっている。
The additive after enhancing the sterilizing power of the sterilizing agent by the reaction in the circulation tank becomes inactive in enhancing the sterilizing power. Therefore, the inactive substance is collected by an additive collecting filter, and a new additive is additionally introduced (for example, see Patent Document 1).
When the particles of the inactive material are fine, the additive collecting filter needs to have a fine filter part and is easily clogged. Therefore, there is a demand for a technique for preventing early clogging. It is growing.

特開2012−200456号公報JP 2012-200456 A

従来の殺菌剤溶液の処理装置について、図3に基づいて説明する。
図3は、従来の殺菌剤溶液の処理装置を式的に示した図である。
図3において、従来の殺菌剤溶液の処理装置3は、所定濃度の殺菌剤が、ポンプPAにより循環タンク5から配管P1を通して、途中の添加剤捕集用フィルター3F、熱交換装置8、加熱装置6を経由して所定の高温状態で殺菌機4へ供給され、殺菌機4で図示しない包材を殺菌した後、包材殺菌に使用された殺菌剤が、一旦回収タンク7に回収されて、ポンプPBにより配管P2を通して途中の熱交換装置8、冷却装置9を経由して循環タンク5へ回収される循環回路になっていて、前記熱交換装置8は、殺菌機4で包材殺菌に使用された高温状態の殺菌剤と、循環タンク5から加熱装置6へ向けて供給される低温状態の殺菌剤が経由して熱交換をする構成となっている。
なお、重複する説明となるが、前記添加剤捕集用フィルター3Fは循環タンク5の出口側に設けられている。
A conventional disinfectant solution processing apparatus will be described with reference to FIG.
FIG. 3 is a diagram schematically showing a conventional disinfectant solution processing apparatus.
In FIG. 3, a conventional disinfectant solution processing device 3 is configured such that a disinfectant having a predetermined concentration passes through a pipe P1 from a circulation tank 5 by a pump PA, and an additive collecting filter 3F, a heat exchange device 8, and a heating device. 6 is supplied to the sterilizer 4 at a predetermined high temperature state through 6 and sterilizes the packaging material (not shown) with the sterilizer 4, and then the sterilizer used for sterilization of the packaging material is once recovered in the recovery tank 7, It is a circulation circuit that is recovered to the circulation tank 5 via the heat exchange device 8 and the cooling device 9 on the way through the pipe P2 by the pump PB, and the heat exchange device 8 is used for sterilization of the packaging material by the sterilizer 4 The heat exchange is performed via the high-temperature sterilizing agent and the low-temperature sterilizing agent supplied from the circulation tank 5 to the heating device 6.
In addition, although it becomes the description which overlaps, the said filter 3F for additive collection is provided in the exit side of the circulation tank 5. FIG.

また、従来の殺菌剤溶液の処理装置3は、前記循環タンク5の上流側の配管P2に該配管P2を通過する殺菌剤の濃度を計測する濃度計測装置(A)CAが設けられ、濃度計測値が制御装置10に送られるようになっており、また、前記殺菌機4の上流側の配管P1に該配管P1を通過する殺菌剤の濃度を計測する濃度計測装置(B)CBが設けられ、濃度計測値が制御装置10に送られるようになっていて、前記濃度計測装置(A)CA又は濃度計測装置(B)CBによる濃度計測値が所定濃度より低下していると前記制御装置10が判断したときに、制御装置10からの指令により開閉弁V1を開にして、殺菌剤バッファタンク12から配管P3を通して、殺菌に使用する濃度以上の濃度の殺菌剤がポンプPCにより前記循環タンク5の入口部に必要量を自動注入されるように構成されている。
さらに、前記循環タンク5には、図示のように矢印Q0或いは矢印Q1からもそれぞれ所定濃度で必要量の殺菌剤或いは後述する添加剤が注入できるようになっている。
Further, the conventional disinfectant solution processing apparatus 3 is provided with a concentration measuring device (A) CA for measuring the concentration of the disinfectant passing through the pipe P2 on the upstream side pipe P2 of the circulation tank 5 to measure the concentration. A value is sent to the control device 10, and a concentration measuring device (B) CB for measuring the concentration of the disinfectant passing through the pipe P1 is provided on the upstream side pipe P1 of the sterilizer 4. The concentration measurement value is sent to the control device 10, and if the concentration measurement value by the concentration measurement device (A) CA or the concentration measurement device (B) CB is lower than a predetermined concentration, the control device 10 Is opened by the command from the control device 10, and the sterilizing agent having a concentration higher than the concentration used for sterilization is supplied from the sterilizing agent buffer tank 12 through the pipe P3 by the pump PC by the circulation tank 5. of It is configured to be automatically injected required amount mouth.
Further, as shown in the figure, a necessary amount of bactericidal agent or an additive to be described later can be injected into the circulation tank 5 from an arrow Q0 or an arrow Q1 as shown.

ここでは、前記殺菌剤が1例として過酢酸系殺菌剤(例えば1500PPMの過酢酸と3000PPMの過酸化水素水の混合溶液。以下殺菌剤を過酢酸溶液と称することがある。)である場合について説明すると、前記殺菌剤バッファタンク12の上流に調合タンク13が設けられていて、殺菌剤原液である過酢酸溶液原液(例えば前記殺菌機4で使用する過酢酸溶液の50倍の濃度のもの)S0、前記過酢酸溶液原液S0を所定濃度に希釈する清水W、および、前記過酢酸溶液の殺菌力を強化する添加剤(例えば前記過酸化水素を分解する作用のある酵素を主成分とする添加剤)S1を投入して前記過酢酸溶液が所定濃度および所定状態に調合されるようになっており、前記調合タンク13と前記殺菌剤バッファタンク12が開閉弁V9を介して配管P4により接続された構成となっている。   Here, as an example, the bactericidal agent is a peracetic acid type bactericidal agent (for example, a mixed solution of 1500 PPM peracetic acid and 3000 PPM hydrogen peroxide solution. Hereinafter, the bactericidal agent may be referred to as a peracetic acid solution). To explain, a preparation tank 13 is provided upstream of the sterilizing agent buffer tank 12 and a peracetic acid solution stock solution that is a sterilizing agent stock solution (for example, 50 times the concentration of the peracetic acid solution used in the sterilizer 4). S0, clear water W for diluting the peracetic acid solution stock solution S0 to a predetermined concentration, and an additive for strengthening the sterilizing power of the peracetic acid solution (for example, an additive mainly composed of an enzyme capable of decomposing hydrogen peroxide) Agent) S1 is introduced so that the peracetic acid solution is prepared at a predetermined concentration and in a predetermined state, and the preparation tank 13 and the bactericidal buffer tank 12 are provided with an on-off valve V9. To have a connection configurations through a pipe P4.

次に、従来の殺菌剤溶液の処理装置3の作用を説明する。
殺菌剤である過酢酸溶液は、殺菌機4において該過酢酸溶液が包材を殺菌する殺菌効果を高めるために、前記殺菌機4へ供給される直前に前記加熱装置6により所定の高温状態(1例として70℃)に加熱されるが、包材殺菌後に前記循環タンク5で高温状態(1例として65℃)に長時間放置されると、分解が加速されて該過酢酸溶液の濃度が低下およびそれに伴う殺菌効果の低下を招いてしまうので、冷却装置9を経由して所定の低温状態(1例として40℃)に冷却されて循環タンク5に回収される。
ここで、過酢酸溶液は、高温状態の前記回収タンク7から冷却装置9への途中、および、低温状態の循環タンク5から加熱装置6への途中で熱交換装置8によって、高温状態の過酢酸溶液は熱を奪われて中温状態に(1例として65℃→約50℃;予備放熱)、低温状態の過酢酸溶液は熱を与えられて中温状態に(1例として40℃→約50℃;予備加熱)という熱交換が行われて、熱エネルギーの有効利用がなされている。
Next, the operation of the conventional disinfectant solution processing apparatus 3 will be described.
In order to enhance the sterilizing effect of the peracetic acid solution that sterilizes the packaging material in the sterilizer 4, the peracetic acid solution that is a sterilizing agent is heated to a predetermined high temperature state by the heating device 6 immediately before being supplied to the sterilizer 4 ( 70 ° C as an example), but after sterilization of the packaging material, if the circulation tank 5 is left in a high temperature state (eg 65 ° C as an example) for a long time, the decomposition is accelerated and the concentration of the peracetic acid solution is increased. As a result, the sterilization effect is lowered, and the cooling tank 9 is cooled to a predetermined low temperature state (40 ° C. as an example) and collected in the circulation tank 5.
Here, the peracetic acid solution is heated in the high temperature state by the heat exchange device 8 on the way from the recovery tank 7 to the cooling device 9 and on the way from the low temperature circulation tank 5 to the heating device 6. The solution is deprived of heat to an intermediate temperature state (for example, 65 ° C. to about 50 ° C .; preliminary heat release), and the low-temperature peracetic acid solution is heated to an intermediate temperature state (for example, 40 ° C. to about 50 ° C.) Heat exchange (preheating) is performed, and thermal energy is effectively used.

また、前記過酢酸溶液は、殺菌機4において高温状態で包材の殺菌に使用されることにより小幅な分解が生じるので、濃度計測装置(A)CAおよび濃度計測装置(B)CBにより過酢酸溶液の濃度を計測して、制御装置10からの指令により開閉弁V1を開にして、殺菌剤バッファタンク12から所定状態に調合された必要量の過酢酸溶液が自動注入されることにより、或いは、図示矢印Q0から所定濃度の殺菌剤が必要量注入されることにより、前記循環タンク5では所定濃度に維持されて、前記過酢酸溶液の殺菌効果が維持される。   Further, since the peracetic acid solution is used for sterilization of the packaging material in a high temperature state in the sterilizer 4, a slight decomposition occurs. Therefore, the peracetic acid solution is obtained by the concentration measuring device (A) CA and the concentration measuring device (B) CB. By measuring the concentration of the solution, opening the on-off valve V1 according to a command from the control device 10, and automatically injecting a necessary amount of peracetic acid solution prepared in a predetermined state from the bactericide buffer tank 12, or When a necessary amount of a sterilizing agent having a predetermined concentration is injected from the illustrated arrow Q0, the circulating tank 5 is maintained at a predetermined concentration, and the sterilizing effect of the peracetic acid solution is maintained.

さらに、前記過酢酸系殺菌剤は、循環タンク5内で殺菌力強化のために過酸化水素を分解する作用のある酵素を主成分とする添加剤S1が添加され、該添加剤の酵素の内の或るものは殺菌力強化の反応をした後は前記過酸化水素を分解する作用が不活性のものとなってしまう。そして、殺菌力強化に対して不活性となったものの粒子が循環タンク5の出口側の添加剤捕集用フィルター3Fによって捕集され、濃度計測装置(A)CAおよび濃度計測装置(B)CBによる濃度計測値に基づいて、制御装置10からの指令により添加剤S1が所定量注入されて殺菌力強化作用が維持される。   Further, the peracetic acid-based disinfectant is added with an additive S1 mainly composed of an enzyme having an action of decomposing hydrogen peroxide in the circulation tank 5 to enhance the disinfecting power. In some cases, the action of decomposing hydrogen peroxide becomes inactive after reacting to enhance sterilizing power. Then, particles that have become inactive with respect to the enhancement of sterilizing power are collected by the additive collecting filter 3F on the outlet side of the circulation tank 5, and the concentration measuring device (A) CA and the concentration measuring device (B) CB. Based on the measured concentration value, a predetermined amount of additive S1 is injected according to a command from the control device 10, and the sterilizing power enhancing action is maintained.

しかしながら、従来の殺菌剤溶液の処理装置3の技術では、添加剤捕集用フィルター3Fが循環タンク5の出口側に設けられており、循環タンク5内で低温になっていることから、前記不活性となった添加剤の粒子が細かいものとなっていて、添加剤捕集用フィルター3Fの濾過部の目は細かい不活性添加剤を捕集するために細かい目とすることが必要で、早期に目詰まりが発生してしまうという恐れがある。   However, in the technology of the conventional disinfectant solution processing apparatus 3, the additive collecting filter 3F is provided on the outlet side of the circulation tank 5 and is at a low temperature in the circulation tank 5. The particles of the additive which became active are fine, and it is necessary to make the eyes of the filter part of the additive collecting filter 3F fine to collect the fine inert additive. There is a risk of clogging.

本発明は、上述の事情に鑑み、添加剤捕集用フィルターの早期目詰まりを防止し、フィルター交換寿命を長くしてメンテナンスコストを低減できる過酢酸系殺菌剤溶液の処理装置を提供することを目的としている。 In view of the above-mentioned circumstances, the present invention provides a peracetic acid disinfectant solution processing apparatus that prevents early clogging of an additive collecting filter, prolongs filter replacement life, and reduces maintenance costs. It is aimed.

前記の課題に対し、本発明は以下の手段により解決を図る。
(1)第1の手段の過酢酸系殺菌剤溶液の処理装置は、循環タンク内で過酸化水素を分解する作用のある酵素を主成分とする添加剤との反応により殺菌力を強化された過酢酸系殺菌剤溶液が循環タンクから殺菌機へ加熱装置で加熱された後に供給され、被殺菌物である包装材料を殺菌した後の前記過酢酸系殺菌剤溶液が前記殺菌機から冷却装置を経て前記循環タンクへ回収される循環回路を形成した過酢酸系殺菌剤溶液の処理装置、或いは、循環タンク内で前記添加剤との反応により殺菌力を強化された前記過酢酸系殺菌剤溶液が循環タンクから殺菌機へ熱交換装置での予備加熱を経て加熱装置で加熱された後に供給され、前記包装材料を殺菌した後の前記過酢酸系殺菌剤溶液が前記殺菌機から前記熱交換装置での予備放熱及び冷却装置での冷却を経て前記循環タンクへ回収される循環回路を形成した過酢酸系殺菌剤溶液の処理装置において、殺菌力強化反応後の前記添加剤を捕集する添加剤捕集用フィルターが、前記加熱装置の下流側で前記殺菌機の上流側、或いは、前記熱交換装置の下流側で前記加熱装置の上流側に設けられたことを特徴とする。
The present invention solves the above problems by the following means.
(1) The peracetic acid disinfectant solution processing apparatus of the first means has enhanced disinfecting power by reaction with an additive mainly composed of an enzyme having an action of decomposing hydrogen peroxide in a circulation tank. The peracetic acid-based disinfectant solution is supplied from the circulation tank to the sterilizer after being heated by the heating device, and the peracetic acid-based disinfectant solution after sterilizing the packaging material to be sterilized is transferred from the sterilizer to the cooling device. after the processing of the peracetic acid-based disinfectant solution to form a circulation circuit to be collected into the circulating tank device, or the peracetic acid-based disinfectant solutions with enhanced microbiocidal by reaction with the additive in circulation tank The peracetic acid-based disinfectant solution supplied from the circulation tank to the sterilizer after being heated by the heating device through the preheating in the heat exchange device and sterilizing the packaging material is transferred from the sterilizer to the heat exchange device. In preliminary heat dissipation and cooling equipment In the processing apparatus of the peracetic acid-based disinfectant solution to form a circulation circuit to be recovered to the circulation tank through the retirement, additives collecting filter for collecting said additive after reinforcing germicidal reaction, the heating device It is provided on the upstream side of the sterilizer on the downstream side, or on the upstream side of the heating device on the downstream side of the heat exchange device.

請求項1に係わる本発明は、添加剤捕集用フィルターを加熱装置の下流側で殺菌機の上流側、或いは、熱交換器の下流側で加熱装置の上流側に設けたことにより、前記殺菌剤が過酢酸系殺菌剤であり、前記添加剤が前記過酢酸系殺菌剤の中の過酸化水素を分解する作用のある酵素を主成分とする添加剤である場合に、殺菌力強化の反応をした後の過酸化水素分解作用が不活性となった添加剤の粒子が、加熱装置或いは熱交換装置での適度な加熱によって熱変性或いは凝縮して大きくなっているため、濾過部の目が粗いフィルターで捕集できるとともに、フィルター交換寿命も長くなるという効果を有する。 The present invention according to claim 1 is characterized in that the additive collecting filter is provided on the upstream side of the sterilizer on the downstream side of the heating device or on the upstream side of the heating device on the downstream side of the heat exchanger. When the agent is a peracetic acid-based disinfectant and the additive is an additive mainly composed of an enzyme having the action of decomposing hydrogen peroxide in the peracetic acid-based disinfectant, a reaction for enhancing the disinfecting power Since the additive particles that have become inactive after hydrogen peroxide decomposition have become thermally denatured or condensed by appropriate heating in a heating device or heat exchange device, The filter can be collected with a coarse filter, and the filter replacement life is increased.

本発明の第1の実施の形態に係わる殺菌剤溶液の処理装置を式的に示した図である。The processing apparatus of disinfectant solutions according to the first embodiment of the present invention is a diagram schematically showing. 本発明の第2の実施の形態に係わる殺菌剤溶液の処理装置を式的に示した図で、図1に相当する図である。In view of the processing apparatus of disinfectant solutions according to the second embodiment of the present invention shown schematically and is a view corresponding to FIG. 従来の殺菌剤溶液の処理装置を式的に示した図である。The processing apparatus of a conventional disinfectant solutions is a diagram schematically showing.

以下、この発明の実施の形態につき図面を参照しつつ詳細に説明する。なお、この実施の形態によりこの発明が限定されるものではない。また、下記実施の形態における構成要素には、当業者が容易に想定できるもの、あるいは実質的に同一のものが含まれる。
(本発明の第1の実施の形態)
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. Note that the present invention is not limited to the embodiments. In addition, constituent elements in the following embodiments include those that can be easily assumed by those skilled in the art or those that are substantially the same.
(First embodiment of the present invention)

本発明の第1の実施の形態を図1に基づいて説明する。
図1は、本発明の第1の実施の形態に係わる殺菌剤溶液の処理装置を式的に示した図である。
図1において、従来技術として説明した図3と同じ構造のものについては同じ記号を付してあり、重複する説明は省略する。
図1において、殺菌剤溶液の処理装置1は、添加剤捕集用フィルター1Fが加熱装置6の下流側で、殺菌機4の上流側に設けられており、添加剤捕集用フィルター1Fの濾過部の目は適度に粗いものとなっている。
A first embodiment of the present invention will be described with reference to FIG.
FIG. 1 is a diagram schematically showing a disinfectant solution processing apparatus according to a first embodiment of the present invention.
In FIG. 1, the same structure as that of FIG. 3 explained as the prior art is given the same symbol, and duplicate explanation is omitted.
In FIG. 1, the disinfectant solution processing apparatus 1 includes an additive collecting filter 1F provided downstream of the heating device 6 and upstream of the sterilizer 4, and filtering the additive collecting filter 1F. The eyes of the part are moderately rough.

次に、本発明の第1の実施の形態に係わる殺菌剤溶液の処理装置1の作用を説明する。
先ず、本発明は、過酸化水素を分解する作用のある酵素を主成分とする添加剤が、循環タンク5内で反応して過酢酸系殺菌剤溶液の殺菌力強化作用をした後に、殺菌力強化に不活性となった添加剤の酵素成分の粒子が、加熱することによって熱変性或いは凝縮して大きくなることを発見したことに由来している。
Next, the operation of the disinfectant solution processing apparatus 1 according to the first embodiment of the present invention will be described.
First, according to the present invention, after an additive mainly composed of an enzyme capable of decomposing hydrogen peroxide reacts in the circulation tank 5 to enhance the sterilizing power of the peracetic acid-based sterilizing agent solution, the sterilizing power is increased. This is because the particles of the enzyme component of the additive, which became inactive for strengthening, were found to be enlarged by heat denaturation or condensation upon heating.

循環タンク5内で過酸化水素を分解する作用のある酵素を主成分とする添加剤との反応により殺菌力を強化された過酢酸系殺菌剤溶液が加熱装置6で高温状態(1例として70℃)に加熱されることにより、殺菌機4での包材(被殺菌物)の殺菌力が強化される。
また、循環タンク5内の反応で殺菌力強化に不活性となった酵素成分の粒子が、前記加熱装置6で加熱されることによって熱変性或いは凝縮して大きくなり、添加剤捕集用フィルター1Fを通過する際に、フィルターの濾過部の目が適度に粗くても捕集される。
前記濾過部の目が粗いフィルターは目詰まりしにくく、フィルター交換寿命が長い。
なお、前記説明では、熱交換装置8を設けた場合を説明したが、熱交換装置8を設けない場合としても本発明の趣旨は同じであり、詳細説明は省略する。
A peracetic acid-based disinfectant solution whose sterilizing power is strengthened by a reaction with an additive mainly composed of an enzyme capable of decomposing hydrogen peroxide in the circulation tank 5 is heated in a high temperature state (for example, 70 The sterilizing power of the packaging material (object to be sterilized) in the sterilizer 4 is enhanced.
In addition, the enzyme component particles, which are inactive to enhance the sterilizing power due to the reaction in the circulation tank 5, are heated and denatured or condensed by the heating device 6, and the additive collecting filter 1 </ b> F. When passing through the filter, it is collected even if the filter portion of the filter is moderately rough.
A filter having a coarse filter section is not easily clogged and has a long filter replacement life.
In the above description, the case where the heat exchange device 8 is provided has been described. However, even if the heat exchange device 8 is not provided, the gist of the present invention is the same, and detailed description thereof is omitted.

次に、本発明の第2の実施の形態を図2に基づいて説明する。
図2は、本発明の第2の実施の形態に係わる殺菌剤溶液の処理装置を式的に示した図である。
図2において、図1と同じ構造のものは同じ記号を付してあり、重複する説明は省略する。
図2において、殺菌剤溶液の処理装置2は、添加剤捕集用フィルター2Fが熱交換装置8の下流側で加熱装置6の上流側に設けられており、添加剤捕集用フィルター2Fの濾過部の目は適度に粗いものとなっている。
Next, a second embodiment of the present invention will be described with reference to FIG.
FIG. 2 is a diagram schematically showing a disinfectant solution processing apparatus according to the second embodiment of the present invention.
In FIG. 2, the same structure as that of FIG.
In FIG. 2, the disinfectant solution processing apparatus 2 includes an additive collecting filter 2F provided downstream of the heat exchange device 8 and upstream of the heating device 6, and filtering of the additive collecting filter 2F. The eyes of the part are moderately rough.

次に、本発明の第2の実施の形態に係わる殺菌剤溶液の処理装置2の作用を説明する。
循環タンク5内で過酸化水素を分解する作用のある酵素を主成分とする添加剤との反応により殺菌力を強化された過酢酸系殺菌剤溶液が熱交換装置8で中温状態(1例として50℃)に加熱されて(予備加熱)、殺菌力強化に不活性となった酵素成分の粒子が、熱変性或いは凝縮して大きくなり、添加剤捕集用フィルター2Fを通過する際に、フィルターの濾過部の目が適度に粗くても捕集される。
前記濾過部の目が粗いフィルターは目詰まりしにくく、フィルター交換寿命が長い。
Next, the operation of the disinfectant solution processing apparatus 2 according to the second embodiment of the present invention will be described.
The peracetic acid-based disinfectant solution whose sterilizing power is enhanced by the reaction with an additive mainly composed of an enzyme capable of decomposing hydrogen peroxide in the circulation tank 5 is in a medium temperature state (as an example) When the enzyme component particles heated to 50 ° C. (preliminary heating) and deactivated to enhance the sterilizing power are enlarged by heat denaturation or condensation and pass through the additive collecting filter 2F, the filter Even if the eyes of the filtration part are moderately rough, they are collected.
A filter having a coarse filter section is not easily clogged and has a long filter replacement life.

前記本発明の第1の実施の形態の説明では、前記殺菌剤溶液が加熱装置6によって高温状態(1例として70℃)に加熱された後に添加剤捕集用フィルター1Fを通過する場合を説明し、前記本発明の第2の実施の形態の説明では、前記殺菌剤溶液が熱交換装置8によって中温状態(1例として50℃)に加熱された後に添加剤捕集用フィルター2Fを通過する場合を説明したが、過酸化水素を分解する作用のある添加剤の主成分の酵素で、殺菌力強化反応の後に殺菌力強化に不活性となった酵素成分の粒子が高温状態(1例として70℃)で熱変性或いは凝縮しやすい場合には、本発明の第1の実施の形態が好ましく、また、前記不活性となった酵素成分の粒子が中温状態(1例として50℃)で熱変性および凝縮しやすい場合には、本発明の第2の実施の形態が好ましく、適宜に選択できる。   In the description of the first embodiment of the present invention, the case where the disinfectant solution is heated to a high temperature state (70 ° C. as an example) by the heating device 6 and then passes through the additive collecting filter 1F is described. In the description of the second embodiment of the present invention, the disinfectant solution is heated to an intermediate temperature state (for example, 50 ° C.) by the heat exchange device 8 and then passes through the additive collecting filter 2F. In the case of the enzyme as the main component of the additive that has the action of decomposing hydrogen peroxide, the particles of the enzyme component that became inactive for enhancing the bactericidal power after the reaction for enhancing the bactericidal power are In the case where heat denaturation or condensation tends to occur at 70 ° C., the first embodiment of the present invention is preferable, and the inactive enzyme component particles are heated in an intermediate temperature state (50 ° C. as an example). If it is easy to denature and condense, The second embodiment of preferred, can be appropriately selected.

また、本発明の第2の実施の形態の前記説明では、添加剤捕集用フィルターを前記熱交換装置の下流側で前記加熱装置の上流側に設けた場合を説明したが、添加剤捕集用フィルターを、前記加熱装置の下流側で前記殺菌機の上流側および前記熱交換装置の下流側で前記加熱装置の上流側の両方に設ける場合としてもよく、この場合は2箇所の添加剤捕集用フィルターで殺菌力強化に不活性となった酵素成分の粒子を捕集することになるので、フィルターの交換頻度を減らすことができる。   In the description of the second embodiment of the present invention, the case where the additive collecting filter is provided on the downstream side of the heat exchange device and the upstream side of the heating device has been described. Filters may be provided on both the upstream side of the sterilizer on the downstream side of the heating device and on the upstream side of the heating device on the downstream side of the heat exchange device. Since the particles of the enzyme component that have become inactive to enhance the bactericidal activity are collected by the collecting filter, the frequency of filter replacement can be reduced.

1、2 殺菌剤溶液の処理装置
1F、2F 添加剤捕集用フィルター
4 殺菌機
5 循環タンク
6 加熱装置
8 熱交換装置
S0 過酢酸溶液原液
S1 添加剤
1, 2 Disinfectant solution processing equipment 1F, 2F Additive collecting filter 4 Sterilizer 5 Circulating tank 6 Heating device 8 Heat exchange device S0 Peracetic acid solution stock solution S1 Additive

Claims (1)

循環タンク内で過酸化水素を分解する作用のある酵素を主成分とする添加剤との反応により殺菌力を強化された過酢酸系殺菌剤溶液が循環タンクから殺菌機へ加熱装置で加熱された後に供給され、被殺菌物である包装材料を殺菌した後の前記過酢酸系殺菌剤溶液が前記殺菌機から冷却装置を経て前記循環タンクへ回収される循環回路を形成した過酢酸系殺菌剤溶液の処理装置、或いは、循環タンク内で前記添加剤との反応により殺菌力を強化された前記過酢酸系殺菌剤溶液が循環タンクから殺菌機へ熱交換装置での予備加熱を経て加熱装置で加熱された後に供給され、前記包装材料を殺菌した後の前記過酢酸系殺菌剤溶液が前記殺菌機から前記熱交換装置での予備放熱及び冷却装置での冷却を経て前記循環タンクへ回収される循環回路を形成した過酢酸系殺菌剤溶液の処理装置において、殺菌力強化反応後の前記添加剤を捕集する添加剤捕集用フィルターが、前記加熱装置の下流側で前記殺菌機の上流側、或いは、前記熱交換装置の下流側で前記加熱装置の上流側に設けられたことを特徴とする過酢酸系殺菌剤溶液の処理装置。 A peracetic acid-based disinfectant solution with enhanced sterilization power by reaction with an additive mainly composed of an enzyme capable of decomposing hydrogen peroxide in the circulation tank was heated from the circulation tank to the sterilizer with a heating device. A peracetic acid-based disinfectant solution that is supplied later and forms a circulation circuit in which the peracetic acid-based disinfectant solution after sterilizing the packaging material to be sterilized is recovered from the sterilizer through the cooling device to the circulation tank. processing apparatus, or heated by the heating device through the pre-heating of the heat exchange device to sterilizer the peracetic acid-based disinfectant solutions with enhanced microbiocidal by reaction with the additive in a circulating tank from the circulation tank The peracetic acid-based disinfectant solution after being supplied and sterilizing the packaging material is recovered to the circulation tank from the sterilizer through preliminary heat dissipation in the heat exchange device and cooling in the cooling device Forming circuit And the processor of peracetic acid-based disinfectant solutions, additives for trapping filter for collecting said additive after reinforcing germicidal reaction, upstream of the sterilizer at a downstream side of the heating device, or the An apparatus for treating a peracetic acid-based disinfectant solution, which is provided downstream of a heat exchange device and upstream of the heating device.
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