JP7229463B2 - Food machine and its sterilization method - Google Patents

Food machine and its sterilization method Download PDF

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JP7229463B2
JP7229463B2 JP2019057521A JP2019057521A JP7229463B2 JP 7229463 B2 JP7229463 B2 JP 7229463B2 JP 2019057521 A JP2019057521 A JP 2019057521A JP 2019057521 A JP2019057521 A JP 2019057521A JP 7229463 B2 JP7229463 B2 JP 7229463B2
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processing tank
valve
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sterilizing agent
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雅夫 蔵野
裕孝 小原
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Miura Co Ltd
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Description

本発明は、処理槽内を減圧する減圧手段として熱交換器および真空ポンプを備えた各種食品機械と、その食品機械の除菌方法に関するものである。 BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to various food machines equipped with heat exchangers and vacuum pumps as depressurizing means for decompressing the inside of a processing tank, and a sterilization method for the food machines.

従来、下記特許文献1に開示されるように、減圧手段として熱交換器および真空ポンプを備えた食品機械が知られている。この食品機械では、処理槽内に食品を収容しない状態で、水蒸気を用いて、処理槽内および減圧系統の所定域(処理槽から熱交換器の二次側までの真空配管内)の殺菌が可能とされる。 2. Description of the Related Art Conventionally, food machines equipped with heat exchangers and vacuum pumps as depressurizing means are known, as disclosed in Patent Document 1 below. In this food machine, steam is used to sterilize the inside of the processing tank and a predetermined area of the decompression system (inside the vacuum piping from the processing tank to the secondary side of the heat exchanger) without storing food in the processing tank. It is possible.

特開2011-200468号公報Japanese Unexamined Patent Application Publication No. 2011-200468

電化厨房の普及により、水蒸気を使用しない食品機械も増えてきている。水蒸気のない環境下では、前記特許文献1に開示されるような水蒸気を用いた殺菌ができない。また、水蒸気があっても、水蒸気以外で処理槽内や減圧系統の除菌を図りたい場合もある。除菌剤で除菌を図る場合でも、簡易な構成および制御で、減圧系統に除菌剤を導入して、容易に確実に除菌を図ることが望まれる。 With the spread of electric kitchens, the number of food machines that do not use steam is increasing. In an environment without water vapor, sterilization using water vapor as disclosed in the aforementioned Patent Document 1 cannot be performed. Moreover, even if there is steam, there are cases where it is desired to sterilize the inside of the processing tank or the decompression system using a method other than steam. Even when sterilizing with a sterilizing agent, it is desired to easily and reliably sterilize by introducing the sterilizing agent into the decompression system with a simple configuration and control.

本発明が解決しようとする課題は、水蒸気を用いることなく、処理槽内や減圧系統の除菌を図ることができる食品機械とその除菌方法を提供することにある。また、簡易な構成および制御で、減圧系統に除菌剤を導入して、容易に確実に除菌を図ることができる食品機械とその除菌方法を提供することを課題とする。 The problem to be solved by the present invention is to provide a food machine and a disinfecting method thereof that can disinfect the inside of the processing tank and the decompression system without using steam. Another object of the present invention is to provide a food machine and its disinfecting method that can easily and reliably disinfect the food machine by introducing a disinfecting agent into the decompression system with a simple configuration and control.

本発明は、前記課題を解決するためになされたもので、請求項1に記載の発明は、処理槽と、この処理槽内の気体を外部へ吸引排出する減圧手段と、減圧された前記処理槽内へ外気を導入する復圧手段と、前記各手段を制御する制御手段とを備え、前記減圧手段として、前記処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプを順に備え、固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、前記処理槽内の空気中に供給する除菌剤発生部が、前記処理槽に設けられる食品機械であって、前記処理槽内に食品が収容されず且つ前記処理槽のドアが閉じられた状態で、前記制御手段により除菌運転を実行可能とされ、前記除菌運転では、前記一次弁を閉じた状態で前記除菌剤発生部から発生させた除菌剤を前記処理槽内に供給する一方、前記真空ポンプにより前記一次弁よりも下流側を減圧した後、前記二次弁が閉じられた状態で前記一次弁を開けることを特徴とする食品機械である。 The present invention has been made in order to solve the above-mentioned problems. A pressure recovery means for introducing outside air into the tank and a control means for controlling each of the above means are provided, and as the pressure reduction means, a primary valve, a heat exchanger, a secondary valve and a A food product in which a sterilizing agent generating unit equipped with a vacuum pump in order and supplying solid particles, liquid particles, or gaseous sterilizing agents singly or in a mixed state into the air in the processing tank is provided in the processing tank. The machine is capable of performing a sterilization operation by the control means in a state in which no food is contained in the processing tank and the door of the processing tank is closed, and in the sterilization operation, the primary valve While the sterilizing agent generated from the sterilizing agent generating unit is supplied into the processing tank in a closed state, the vacuum pump reduces the pressure downstream of the primary valve, and then the secondary valve is closed. The food machine is characterized in that the primary valve is opened in a closed state .

請求項1および請求項5に記載の発明によれば、減圧手段として、処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプを順に備えた食品機械において、処理槽には除菌剤発生部が設けられる。この除菌剤発生部は、固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、処理槽内の空気中に供給可能である。除菌剤発生部からの除菌剤により、処理槽内と減圧系統の除菌を図ることができる。 According to the inventions of claims 1 and 5 , the food processing machine comprises a primary valve, a heat exchanger, a secondary valve and a vacuum pump in this order in an exhaust passage from the processing tank as decompression means. A disinfectant generator is provided in the tank. This sterilizing agent generator can supply solid particles, liquid particles, or gaseous sterilizing agents singly or in a mixed state into the air in the processing tank. The sterilizing agent from the sterilizing agent generator can be used to sterilize the inside of the processing tank and the decompression system.

請求項1に記載の発明によれば、除菌運転では、まず、一次弁を閉じた状態で除菌剤発生部から発生させた除菌剤を処理槽内に供給する一方、真空ポンプにより一次弁よりも下流側を減圧する。この場合、処理槽内は減圧されず、処理槽内の空気中に除菌剤が供給され、固体微粒子、液体微粒子または気体の除菌剤は、空気に浮遊および/または混合される。その後、二次弁が閉じられた状態で一次弁を開けることで、処理槽内の空気は、減圧系統の所定域(処理槽から熱交換器の二次側)に引き込まれる。この際、空気に浮遊および/または混合された除菌剤も、空気と共に、減圧系統の所定域に到達するので、熱交換器や配管内の除菌が図られる。 According to the first aspect of the invention , in the sterilization operation, first, the sterilizing agent generated from the sterilizing agent generator is supplied into the processing tank while the primary valve is closed, while the primary valve is driven by the vacuum pump. Reduce the pressure downstream of the valve. In this case, the inside of the processing bath is not decompressed, the sterilizing agent is supplied to the air in the processing bath, and solid particles, liquid particles, or gaseous sterilizing agents are suspended and/or mixed in the air. After that, by opening the primary valve while the secondary valve is closed, the air in the processing tank is drawn into a predetermined region of the decompression system (from the processing tank to the secondary side of the heat exchanger). At this time, the sterilizing agent floating and/or mixed in the air also reaches a predetermined area of the pressure reducing system together with the air, so that the inside of the heat exchanger and piping is sterilized.

請求項2に記載の発明は、前記除菌運転では、前記二次弁が閉じられた状態で前記一次弁を開けて設定時間保持してから、前記減圧手段により前記処理槽内を減圧後、前記復圧手段により前記処理槽内を復圧することを特徴とする請求項1に記載の食品機械である。 In the sterilization operation, after the primary valve is opened with the secondary valve closed and held for a set time, the inside of the treatment tank is decompressed by the decompressing means, 2. The food machine according to claim 1, wherein the pressure in the processing tank is restored by the pressure restoring means.

請求項2に記載の発明によれば、除菌運転では、二次弁が閉じられた状態で一次弁を開けて設定時間保持するので、減圧系統の除菌を確実に図ることができる。その後、減圧手段により処理槽内を減圧してから復圧手段により処理槽内を復圧するので、処理槽内や減圧系統から除菌剤を排出することができる。これにより、処理槽のドアを開けた際の除菌剤の放出を抑制して、安全性を高めることができる。 According to the second aspect of the invention , in the sterilization operation, the secondary valve is closed, the primary valve is opened, and the operation is held for the set time. After that, the inside of the processing tank is decompressed by the decompressing means, and then the pressure in the processing tank is restored by the depressurizing means, so that the sterilizing agent can be discharged from the inside of the processing tank or the decompression system. As a result, it is possible to suppress the release of the sterilizing agent when the door of the treatment tank is opened, thereby enhancing safety.

請求項3に記載の発明は、前記処理槽には、前記除菌剤発生部としての除菌剤発生器が接続されていることを特徴とする請求項1または請求項2に記載の食品機械である。 According to the invention of claim 3 , the food processing machine according to claim 1 or claim 2, wherein a disinfectant generator as the disinfectant generator is connected to the processing tank. is.

請求項3に記載の発明によれば、除菌運転では、処理槽に接続された除菌剤発生器を用いて、固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、処理槽内の空気中に供給することができる。 According to the third aspect of the invention , in the sterilization operation, the sterilization agent generator connected to the treatment tank is used to generate solid particles, liquid particles, or gaseous sterilization agents alone or in a mixed state. , can be supplied into the air in the treatment tank.

請求項4に記載の発明は、除菌運転において、前記処理槽内には、前記除菌剤発生部として、燻煙剤または燻蒸剤が収容されることを特徴とする請求項1または請求項2に記載の食品機械である。
請求項5に記載の発明は、処理槽と、この処理槽内の気体を外部へ吸引排出する減圧手段と、減圧された前記処理槽内へ外気を導入する復圧手段と、前記各手段を制御する制御手段とを備え、前記減圧手段として、前記処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプを順に備え、固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、前記処理槽内の空気中に供給する除菌剤発生部が、前記処理槽に設けられる食品機械であって、除菌運転において、前記処理槽内には、前記除菌剤発生部として、燻煙剤または燻蒸剤が収容されることを特徴とする食品機械である。
The invention according to claim 4 is characterized in that, in the sterilization operation, a smoking agent or a fumigant is accommodated in the processing tank as the sterilization agent generator. 2. The food machine according to 2 .
According to a fifth aspect of the present invention, there is provided a processing tank, a depressurizing means for sucking and discharging gas in the processing tank to the outside, a pressure restoring means for introducing outside air into the decompressed processing tank, and each of the above means. and a control means for controlling, and as the decompression means, a primary valve, a heat exchanger, a secondary valve and a vacuum pump are provided in order in an exhaust passage from the processing tank, and solid particles, liquid particles or gas are sterilized. The food machine is provided with a sterilizing agent generating unit that supplies a sterilizing agent to the air in the processing tank, either alone or in a mixed state, in the processing tank, and in the sterilization operation, in the processing tank, and a food machine characterized in that a smoking agent or a fumigating agent is accommodated as the sterilizing agent generating portion.

請求項4および請求項5に記載の発明によれば、除菌運転では、処理槽内に燻煙剤または燻蒸剤を収容することで、固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、処理槽内の空気中に供給することができる。 According to the inventions of claims 4 and 5 , in the sterilization operation, the fumigation agent or the fumigant is accommodated in the treatment tank, so that the solid fine particles, the liquid fine particles, or the gaseous sterilization agent is Alternatively, they can be supplied to the air in the processing bath in a mixed state.

請求項6に記載の発明は、前記一次弁は、前記制御手段により開閉制御される弁であり、前記二次弁は、前記真空ポンプの作動の有無に伴い開閉する逆止弁であることを特徴とする請求項1~5のいずれか1項に記載の食品機械である。 According to a sixth aspect of the invention, the primary valve is a valve that is controlled to open and close by the control means, and the secondary valve is a check valve that opens and closes depending on whether or not the vacuum pump is operated. A food machine according to any one of claims 1-5.

請求項6に記載の発明によれば、二次弁は、真空ポンプの作動の有無に伴い開閉する逆止弁であるから、制御の必要がない。そのため、一次弁の開閉を制御しつつ、除菌運転を行うことができる。 According to the sixth aspect of the invention, the secondary valve is a check valve that opens and closes depending on whether the vacuum pump is operating or not, so no control is required. Therefore, the sterilization operation can be performed while controlling the opening and closing of the primary valve.

請求項7に記載の発明は、処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプが順に設けられる一方、前記処理槽内への給気路に真空解除弁が設けられた食品機械の除菌方法であって、固体微粒子、液体微粒子および気体の内、いずれか一以上の状態の除菌剤、または当該除菌剤を含む空気を、前記一次弁を閉じた状態で、前記処理槽内の空気中に供給する一方、前記真空ポンプにより前記一次弁よりも下流側を減圧する第一工程と、前記二次弁が閉じられた状態で、前記一次弁を開けて、前記処理槽内の除菌剤を前記熱交換器へ導入する第二工程と、前記真空解除弁を開ける第三工程とを順次に行うことを特徴とする食品機械の除菌方法である。 According to the seventh aspect of the invention, an exhaust passage from the inside of the processing bath is provided with a primary valve, a heat exchanger, a secondary valve and a vacuum pump in this order, and an air supply passage into the processing bath is provided with a vacuum release valve. is provided, wherein the sterilizing agent in any one or more states of solid particles, liquid particles, and gas, or air containing the sterilizing agent, is supplied to the primary valve by closing the A first step of supplying the air in the processing tank in a state in which it is closed, while reducing the pressure downstream of the primary valve with the vacuum pump, and closing the primary valve with the secondary valve closed. A sterilization method for a food machine, characterized by sequentially performing a second step of opening the processing tank to introduce the sterilizing agent in the processing tank into the heat exchanger and a third step of opening the vacuum release valve. be.

請求項7に記載の発明によれば、処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプが順に設けられる一方、処理槽内への給気路に真空解除弁が設けられた食品機械において、固体微粒子、液体微粒子および気体の内、いずれか一以上の状態の除菌剤、または当該除菌剤を含む空気を用いて、処理槽内と、減圧系統の所定域(処理槽から熱交換器の二次側)の除菌を図ることができる。具体的には、まず、第一工程として、一次弁を閉じた状態で除菌剤(または当該除菌剤を含む空気)を処理槽内に供給する一方、真空ポンプにより一次弁よりも下流側を減圧する。この場合、処理槽内は減圧されず、処理槽内の空気中に除菌剤(または当該除菌剤を含む空気)が供給され、固体微粒子、液体微粒子または気体の除菌剤は、空気に浮遊および/または混合される。その後、第二工程として、二次弁が閉じられた状態で一次弁を開けることで、処理槽内の除菌剤を熱交換器に導入する。空気に浮遊および/または混合された除菌剤を、空気と共に、減圧系統に引き込むことで、熱交換器や配管内の除菌を確実に図ることができる。その後、第三工程として、真空解除弁を開けて、処理槽内を大気圧まで復圧すればよい。 According to the seventh aspect of the invention, a primary valve, a heat exchanger, a secondary valve, and a vacuum pump are provided in order in the exhaust passage from the inside of the processing bath, and the vacuum release is provided in the air supply passage into the processing bath. In a food machine provided with a valve, a sterilizing agent in one or more states of solid particulates, liquid particulates, and gas, or air containing the sterilizing agent is used to sterilize the inside of the processing tank and the pressure reduction system. It is possible to sterilize a predetermined area (from the treatment tank to the secondary side of the heat exchanger). Specifically, first, as the first step, while the sterilizing agent (or air containing the sterilizing agent) is supplied into the processing tank with the primary valve closed, a vacuum pump is operated to the downstream side of the primary valve. is decompressed. In this case, the inside of the treatment tank is not decompressed, the disinfectant (or air containing the disinfectant) is supplied to the air in the treatment tank, and the solid particles, liquid particles, or gaseous disinfectant is released into the air. Float and/or mix. After that, as a second step, the sterilizing agent in the treatment tank is introduced into the heat exchanger by opening the primary valve while the secondary valve is closed. By drawing the sterilizing agent floating and/or mixed in the air into the decompression system together with the air, the inside of the heat exchanger and the pipes can be reliably sterilized. After that, as the third step, the vacuum release valve is opened to restore the pressure in the processing tank to the atmospheric pressure.

さらに、請求項8に記載の発明は、前記第三工程では、前記真空ポンプにより前記処理槽内を減圧後、前記真空解除弁を開けることを特徴とする請求項7に記載の食品機械の除菌方法である。 Furthermore, the invention according to claim 8 is characterized in that, in the third step, the vacuum release valve is opened after the inside of the processing tank is decompressed by the vacuum pump. fungus method.

請求項8に記載の発明によれば、第三工程では、真空ポンプにより処理槽内を減圧後、真空解除弁を開けて処理槽内を復圧するので、処理槽内や減圧系統から除菌剤を排出することができる。これにより、処理槽のドアを開けた際の除菌剤の放出を抑制して、安全性を高めることができる。 According to the eighth aspect of the invention, in the third step, after the inside of the processing tank is decompressed by the vacuum pump, the vacuum release valve is opened to restore the pressure inside the processing tank. can be discharged. As a result, it is possible to suppress the release of the sterilizing agent when the door of the treatment tank is opened, thereby enhancing safety.

本発明の食品機械とその除菌方法によれば、水蒸気を用いることなく、処理槽内や減圧系統の除菌を図ることができる。また、簡易な構成および制御で、減圧系統に除菌剤を導入して、容易に確実に除菌を図ることができる。 According to the food machine and its sterilization method of the present invention, it is possible to sterilize the inside of the processing tank and the decompression system without using steam. In addition, with a simple configuration and control, it is possible to introduce the sterilizing agent into the decompression system to easily and reliably perform sterilization.

本発明の一実施例の食品機械を示す概略図である。1 is a schematic diagram showing a food machine according to one embodiment of the present invention; FIG.

以下、本発明の具体的実施例を図面に基づいて詳細に説明する。 Specific embodiments of the present invention will now be described in detail with reference to the drawings.

図1は、本発明の一実施例の食品機械1を示す概略図である。 FIG. 1 is a schematic diagram showing a food machine 1 of one embodiment of the invention.

本実施例の食品機械1は、真空冷却装置であり、処理槽2と、この処理槽2内の気体を外部へ吸引排出して処理槽2内を減圧する減圧手段3と、減圧された処理槽2内へ外気を導入して処理槽2内を復圧する復圧手段4と、処理槽2内の空気中に除菌剤を供給する除菌剤発生器5と、前記各手段3,4および除菌剤発生器5などを制御する制御手段(図示省略)とを備える。 The food machine 1 of this embodiment is a vacuum cooling device, and includes a processing tank 2, a decompression means 3 for sucking and discharging the gas in the processing tank 2 to the outside to reduce the pressure in the processing tank 2, and Pressure restoring means 4 for introducing outside air into the tank 2 to restore the pressure inside the processing tank 2, a sterilizing agent generator 5 for supplying a sterilizing agent to the air in the processing tank 2, and the above means 3 and 4. and control means (not shown) for controlling the disinfectant generator 5 and the like.

処理槽2は、内部空間の減圧に耐える中空容器であり、ドアで開閉可能とされる。処理槽2は、典型的には略矩形の箱状に形成され、正面の開口部がドアで開閉可能とされる。ドアを開けることで、処理槽2に食品を出し入れすることができ、ドアを閉じることで、処理槽2の開口部を気密に閉じることができる。ドアは、処理槽2の正面および背面の双方に設けられてもよい。 The processing tank 2 is a hollow container that can withstand the pressure reduction of the internal space, and can be opened and closed with a door. The processing tank 2 is typically formed in a substantially rectangular box shape, and the front opening can be opened and closed with a door. By opening the door, food can be taken in and out of the processing tank 2, and by closing the door, the opening of the processing tank 2 can be airtightly closed. Doors may be provided on both the front and back sides of the processing tank 2 .

処理槽2には、所望により、圧力センサ、温度センサおよび品温センサの内、一または複数のセンサが設けられる。圧力センサは処理槽2内の圧力を検出し、温度センサは処理槽2内の温度を検出し、品温センサは処理槽2内の食品の温度を検出する。 If desired, the processing tank 2 is provided with one or a plurality of sensors among pressure sensors, temperature sensors, and product temperature sensors. The pressure sensor detects the pressure in the processing tank 2 , the temperature sensor detects the temperature in the processing tank 2 , and the product temperature sensor detects the temperature of the food in the processing tank 2 .

減圧手段3は、処理槽2内の気体を外部へ吸引排出して、処理槽2内を減圧する手段である。本実施例では、減圧手段3は、処理槽2内からの排気路6に、一次弁7、蒸気凝縮用の熱交換器8、二次弁9、および水封式の真空ポンプ10を順に備える。 The decompression means 3 is means for decompressing the inside of the processing bath 2 by sucking and discharging the gas in the processing bath 2 to the outside. In this embodiment, the decompression means 3 includes a primary valve 7, a steam condensing heat exchanger 8, a secondary valve 9, and a water-sealed vacuum pump 10 in this order in an exhaust passage 6 from the inside of the processing tank 2. .

一次弁7は、制御手段により開閉を制御される弁である。一次弁7は、電磁弁でもよいが、排気路6の口径を考慮して、本実施例では電動弁(モータバルブ)から構成される。 The primary valve 7 is a valve whose opening and closing is controlled by control means. Although the primary valve 7 may be an electromagnetic valve, in consideration of the diameter of the exhaust passage 6, the primary valve 7 is composed of an electric valve (motor valve) in this embodiment.

熱交換器8は、排気路6内の流体(熱交換器8を通過する排気流体)と、冷却水とを混ぜることなく熱交換する間接熱交換器である。熱交換器8において、排気流体中の蒸気を、冷却水により冷却し凝縮させることができる。熱交換器8に対する冷却水の通水の有無は、熱交給水弁11の開閉により切り替えられる。 The heat exchanger 8 is an indirect heat exchanger that exchanges heat between the fluid in the exhaust path 6 (exhaust fluid passing through the heat exchanger 8) and cooling water without mixing. In heat exchanger 8, steam in the exhaust fluid can be cooled and condensed by cooling water. Whether or not the cooling water flows to the heat exchanger 8 is switched by opening and closing the heat exchange water supply valve 11 .

二次弁9は、制御手段による開閉制御を不要とするために、逆止弁から構成されるのが好ましい。二次弁9を逆止弁から構成した場合、二次弁9は、真空ポンプ10の発停と連動して自力で開閉される。つまり、真空ポンプ10の作動中、二次弁9は開放され、真空ポンプ10の停止中、二次弁9は閉鎖される。但し、後述するように、二次弁9も、制御手段により開閉を制御される弁から構成してもよい。 The secondary valve 9 preferably consists of a check valve in order to eliminate the need for opening/closing control by control means. When the secondary valve 9 is composed of a check valve, the secondary valve 9 is automatically opened and closed in conjunction with the starting and stopping of the vacuum pump 10 . That is, when the vacuum pump 10 is operating, the secondary valve 9 is open, and when the vacuum pump 10 is stopped, the secondary valve 9 is closed. However, as will be described later, the secondary valve 9 may also be composed of a valve whose opening and closing is controlled by control means.

真空ポンプ10は、水封式であり、周知のとおり、封水と呼ばれる水が供給されつつ運転される。そのために、真空ポンプ10には、封水給水弁(図示省略)を介して水が供給される。封水給水弁は、真空ポンプ10の発停と連動して開閉される。 The vacuum pump 10 is of a water ring type, and as is well known, is operated while being supplied with water called seal water. Therefore, water is supplied to the vacuum pump 10 via a water seal water supply valve (not shown). The sealing water supply valve is opened and closed in conjunction with the start and stop of the vacuum pump 10 .

復圧手段4は、減圧された処理槽2内へ外気を導入して、処理槽2内を復圧する手段である。本実施例では、復圧手段4は、処理槽2内への給気路12に、エアフィルタ13および真空解除弁14を順に備える。処理槽2内が減圧された状態で、真空解除弁14を開けると、外気がエアフィルタ13を介して処理槽2内へ導入され、処理槽2内を復圧することができる。真空解除弁14は、好ましくは開度調整可能な弁から構成される。 The pressure restoring means 4 is a means for introducing outside air into the decompressed processing tank 2 to restore the pressure inside the processing tank 2 . In this embodiment, the pressure recovery means 4 includes an air filter 13 and a vacuum release valve 14 in order in the air supply path 12 into the processing tank 2 . When the vacuum release valve 14 is opened while the inside of the processing tank 2 is depressurized, outside air is introduced into the processing tank 2 through the air filter 13, and the pressure inside the processing tank 2 can be restored. The vacuum release valve 14 preferably comprises a valve whose opening is adjustable.

除菌剤発生器5は、固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、処理槽2内の空気中に供給する。言い換えれば、除菌剤発生器5は、固体微粒子、液体微粒子および気体の内、いずれか一以上の状態の除菌剤を、処理槽2内の空気中に供給する。固体微粒子の場合、除菌剤は煙状となり、液体微粒子の場合、除菌剤はミスト状となり、気体の場合、除菌剤はガス状となる。なお、除菌剤発生器5は、上述のような状態の除菌剤だけでなく、そのような除菌剤を含む空気(またはその他の気体)を、処理槽2内の空気中に供給するようにしてもよい。 The sterilizing agent generator 5 supplies the air in the processing tank 2 with solid particles, liquid particles, or gaseous sterilizing agents singly or in a mixed state. In other words, the sterilizing agent generator 5 supplies the sterilizing agent in the state of any one or more of solid particles, liquid particles and gas into the air in the processing tank 2 . In the case of solid fine particles, the sterilizing agent becomes smoke, in the case of liquid fine particles, the sterilizing agent becomes mist, and in the case of gas, the sterilizing agent becomes gaseous. The sterilizing agent generator 5 supplies not only the sterilizing agent in the state described above, but also air (or other gas) containing such a sterilizing agent to the air in the processing tank 2. You may do so.

除菌剤発生器5で発生させるのは、文字通り除菌剤である。そのため、たとえば、水蒸気発生器(ボイラ)は、除菌剤発生器ではない。つまり、水蒸気のみの気体は、除菌剤には含まれない。なお、除菌とは、増殖可能な菌数を対象物から有効数減少させることをいう。 What is generated by the disinfectant generator 5 is literally the disinfectant. So, for example, a steam generator (boiler) is not a disinfectant generator. In other words, the gas containing only water vapor is not included in the sterilizing agent. In addition, eradication refers to reducing the effective number of proliferative bacteria from an object.

本実施例では、除菌剤発生器5は、処理槽2外に設けられ、処理槽2と除菌剤供給路15を介して接続される。除菌剤供給路15には、除菌剤供給弁16が設けられている。除菌剤供給弁16を開けることで、除菌剤発生器5からの除菌剤(または除菌剤を含む空気)を処理槽2内へ供給することができる。 In this embodiment, the disinfectant generator 5 is provided outside the treatment tank 2 and is connected to the treatment tank 2 via the disinfectant supply path 15 . A disinfectant supply valve 16 is provided in the disinfectant supply path 15 . By opening the disinfectant supply valve 16 , the disinfectant (or air containing the disinfectant) from the disinfectant generator 5 can be supplied into the processing tank 2 .

除菌剤発生器5と処理槽2とは、除菌剤供給路15で接続される以外に、図1において破線で示すように、循環返送路17を介して接続されてもよい。たとえば、図1では、除菌剤発生器5は、処理槽2の下部と除菌剤供給路15を介して接続されると共に、処理槽2の上部と循環返送路17を介して接続されている。そして、除菌剤発生器5には、ファン(図示省略)が設けられている。このファンを作動させることで、除菌剤発生器5と処理槽2との間で、空気を循環させることができる。 The disinfectant generator 5 and the treatment tank 2 may be connected via a circulation return line 17 as indicated by the dashed line in FIG. For example, in FIG. 1, the sterilizing agent generator 5 is connected to the lower portion of the processing tank 2 via the sterilizing agent supply path 15, and is connected to the upper portion of the processing tank 2 via the circulation return path 17. there is The disinfectant generator 5 is provided with a fan (not shown). By operating this fan, air can be circulated between the disinfectant generator 5 and the treatment tank 2 .

具体的には、ファンを作動させることで、処理槽2内の空気を循環返送路17から除菌剤発生器5に戻しつつ、その空気に除菌剤を混入して、除菌剤供給路15から処理槽2内へ送り込むことができる。このようにして、処理槽2内の空気を除菌剤発生器5との間で循環させながら、処理槽2内の空気中の除菌剤濃度を高めていくことができる。 Specifically, by operating the fan, the air in the processing tank 2 is returned from the circulation return path 17 to the sterilizing agent generator 5, and the sterilizing agent is mixed with the air to produce the sterilizing agent supply path. 15 into the processing tank 2 . In this manner, the concentration of the sterilizing agent in the air within the processing tank 2 can be increased while circulating the air within the processing tank 2 with the sterilizing agent generator 5 .

循環返送路17には、循環返送弁(図示省略)を設けるのが好ましい。循環返送弁は、典型的には、除菌剤供給弁16と同様に開閉制御される。つまり、除菌剤供給弁16を開ける際、循環返送弁も開け、除菌剤供給弁16を閉じる際、循環返送弁も閉じるのがよい。 A circulation return valve (not shown) is preferably provided in the circulation return path 17 . The circulation return valve is typically controlled to open and close in the same manner as the disinfectant supply valve 16 . In other words, when the disinfectant supply valve 16 is opened, the circulation return valve should also be opened, and when the disinfectant supply valve 16 is closed, the circulation return valve should also be closed.

なお、除菌剤供給路15および/または循環返送路17は、処理槽2側の端部が処理槽2に接続される以外に、真空解除弁14よりも処理槽2側の給気路12に接続されたり、一次弁7よりも処理槽2側の排気路6に接続されたりしてもよい。図示例の場合、循環返送路17は、給気路12から分岐するように設けられている。このようにすれば、処理槽2に除菌剤発生器5を容易に接続することができる。 The disinfectant supply path 15 and/or the circulation/return path 17 is connected to the processing tank 2 at its end on the processing tank 2 side, and the air supply path 12 on the processing tank 2 side of the vacuum release valve 14 is connected to the processing tank 2 side. , or connected to the exhaust passage 6 closer to the processing tank 2 than the primary valve 7 . In the illustrated example, the circulation return path 17 is provided so as to branch off from the air supply path 12 . By doing so, the disinfectant generator 5 can be easily connected to the treatment tank 2 .

除菌剤発生器5は、固体微粒子、液体微粒子および気体の内、いずれか一以上の状態の除菌剤を発生させるのであれば、除菌剤の種類は特に問わない。たとえば、除菌剤として、次亜塩素酸のミスト(液体微粒子)もしくはガス(気体)、またはこれらの混合物を用いることができる。 The sterilizing agent generator 5 is not particularly limited in the type of sterilizing agent as long as it generates the sterilizing agent in one or more states of solid particles, liquid particles and gas. For example, hypochlorous acid mist (liquid fine particles) or gas (gas), or a mixture thereof can be used as the sterilizing agent.

すなわち、除菌剤発生器5は、たとえば、次亜塩素酸のミストを生成して処理槽2内へ供給する。この場合、除菌剤発生器5は、たとえば超音波霧化器を備え、次亜塩素酸の水溶液を霧化して、次亜塩素酸を含むミストを生成する。あるいは、これに代えてまたは加えて、除菌剤発生器5は、たとえばヒータを備え、次亜塩素酸を含むガスを生成する。そして、生成した次亜塩素酸のミスト(および/またはガス)を、ファンにより処理槽2内へ送り込めばよい。この際、前述したとおり、除菌剤発生器5と処理槽2との間で、気体を循環させながら、処理槽2内の空気中の次亜塩素酸濃度を所定まで高めることができる。なお、次亜塩素酸は、水道水と塩(塩化ナトリウム)を電気分解して得ることもできる。 That is, the disinfectant generator 5 generates, for example, hypochlorous acid mist and supplies it into the processing tank 2 . In this case, the disinfectant generator 5 is equipped with, for example, an ultrasonic atomizer, and atomizes the hypochlorous acid aqueous solution to generate mist containing hypochlorous acid. Alternatively or additionally, the sanitizer generator 5 is provided with, for example, a heater to generate a gas containing hypochlorous acid. Then, the generated hypochlorous acid mist (and/or gas) may be sent into the processing tank 2 by a fan. At this time, as described above, the concentration of hypochlorous acid in the air in the treatment tank 2 can be increased to a predetermined level while the gas is circulated between the disinfectant generator 5 and the treatment tank 2 . Hypochlorous acid can also be obtained by electrolyzing tap water and salt (sodium chloride).

また、除菌剤として、二酸化塩素を用いることもできる。この場合、除菌剤発生器5において、二酸化塩素のガスを発生させ、そのガスを処理槽2内へ供給する。この場合も、除菌剤発生器5と処理槽2との間で、気体を循環させながら、処理槽2内の空気中の二酸化塩素濃度を所定まで高めることができる。あるいは、除菌剤発生器5として、ガスボンベを備え、二酸化塩素などのガスを処理槽2内へ噴出させる構成としてもよい。除菌剤発生器5としてガスボンベを用いる場合、前記ファンや循環返送路17の設置は不要である。 Chlorine dioxide can also be used as a disinfectant. In this case, chlorine dioxide gas is generated in the sterilizing agent generator 5 and supplied into the treatment tank 2 . In this case as well, the concentration of chlorine dioxide in the air in the treatment tank 2 can be increased to a predetermined level while circulating the gas between the disinfectant generator 5 and the treatment tank 2 . Alternatively, a gas cylinder may be provided as the sterilizing agent generator 5 to eject a gas such as chlorine dioxide into the treatment tank 2 . When a gas cylinder is used as the sterilizing agent generator 5, installation of the fan and the circulation return path 17 is unnecessary.

その他、後述する実施例2で用いる燻煙剤または燻蒸剤と同様に、除菌剤発生器5において、たとえば煙状(固体微粒子)の除菌剤を発生させてもよい。 In addition, like the fumigating agent or the fumigant used in Example 2 described later, the sterilizing agent generator 5 may generate, for example, a smoke-like (solid particulate) sterilizing agent.

いずれにしても、除菌剤発生器5を用いて、固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、処理槽2内の空気中に供給して、その除菌剤を処理槽2内の空気に浮遊および/または混合することができる。固体微粒子または液体微粒子の大きさは、空気に浮遊および/または混合できる程度の大きさということができる。 In any case, using the sterilizing agent generator 5, solid particles, liquid particles, or gaseous sterilizing agents are supplied singly or in a mixed state into the air in the processing tank 2 to sterilize the sterilization. The agents can be suspended and/or mixed with the air within the treatment tank 2 . The size of solid or liquid particles can be said to be such that they can be suspended and/or mixed with air.

制御手段は、減圧手段3および復圧手段4の他、除菌剤発生器5などを制御する制御器(図示省略)である。具体的には、一次弁7、真空ポンプ10、熱交給水弁11、封水給水弁(図示省略)、真空解除弁14、除菌剤発生器5、除菌剤供給弁16、循環返送弁(図示省略)の他、各種センサや操作盤(図示省略)などは、制御器に接続されている。そして、制御器は、以下に述べるように、所定の手順(プログラム)に従い、処理槽2内の食品の冷却運転の他、処理槽2内および減圧系統(処理槽2から熱交換器8の二次側までの区間)の除菌運転を実行可能(つまり本実施例の除菌方法を実施可能)とされる。 The control means is a controller (not shown) that controls the depressurizing means 3 and the pressure restoring means 4, as well as the disinfectant generator 5 and the like. Specifically, the primary valve 7, vacuum pump 10, heat exchange water supply valve 11, sealing water supply valve (not shown), vacuum release valve 14, disinfectant generator 5, disinfectant supply valve 16, circulation return valve (not shown), various sensors, an operation panel (not shown), etc. are connected to the controller. Then, as described below, the controller operates to cool the food in the processing tank 2 in accordance with a predetermined procedure (program), as well as to control the inside of the processing tank 2 and the pressure reduction system (two section to the next side) can be executed (that is, the sterilization method of the present embodiment can be executed).

≪冷却運転≫
冷却運転は、処理槽2内に食品を収容して、処理槽2のドアを気密に閉じた状態で実行される。冷却運転では、減圧手段3により処理槽2内を減圧して、処理槽2内の食品を所望温度まで冷却後、減圧手段3を停止して、復圧手段4により処理槽2内を大気圧まで復圧する。冷却運転では、減圧手段3により処理槽2内を減圧中、所望により真空解除弁14の開度を調整して、処理槽2内の減圧速度を調整してもよい。
≪Cooling operation≫
The cooling operation is performed with the food stored in the processing tank 2 and the door of the processing tank 2 airtightly closed. In the cooling operation, the inside of the processing tank 2 is decompressed by the decompression means 3, and after cooling the food in the processing tank 2 to a desired temperature, the decompression means 3 is stopped, and the inside of the processing tank 2 is returned to the atmospheric pressure by the pressure recovery means 4. pressurize up to In the cooling operation, while the inside of the processing tank 2 is being decompressed by the decompression means 3, the opening degree of the vacuum release valve 14 may be adjusted as desired to adjust the decompression rate in the processing tank 2. FIG.

≪除菌運転≫
除菌運転は、処理槽2内に食品を収容せず、処理槽2のドアを気密に閉じた状態で実行される。ここでは、操作盤から除菌運転の開始を指示されると、下記に示すように、第一工程、第二工程および第三工程を順次に含んで実行する。
≪Sterilization operation≫
The sterilization operation is performed in a state in which no food is stored in the processing tank 2 and the door of the processing tank 2 is airtightly closed. Here, when an instruction to start the sterilization operation is given from the control panel, the first step, second step and third step are sequentially executed as shown below.

第一工程では、一次弁7を閉じた状態で、除菌剤発生器5からの除菌剤を、処理槽2内の空気中に供給する。この際、好適には前述したとおり、除菌剤発生器5と処理槽2との間で空気を循環させながら、空気中に除菌剤を供給する。この循環を設定供給時間行うことで、処理槽2内の空気中の除菌剤濃度を設定濃度とすることができる。このようにして、固体微粒子、液体微粒子または気体の除菌剤は、空気に浮遊および/または混合される。たとえば、次亜塩素酸のミストが、処理槽2内の空気に浮遊および/または混合される。このような処理の終了後、除菌剤発生器5を停止すると共に、除菌剤供給弁16および循環返送弁を閉じる。 In the first step, the sterilizing agent from the sterilizing agent generator 5 is supplied into the air in the treatment tank 2 while the primary valve 7 is closed. At this time, preferably, as described above, the disinfectant is supplied into the air while circulating the air between the disinfectant generator 5 and the treatment tank 2 . By performing this circulation for a set supply time, the concentration of the sterilizing agent in the air in the treatment tank 2 can be adjusted to the set concentration. In this way, the solid particulate, liquid particulate or gaseous sanitizer is suspended and/or mixed with the air. For example, hypochlorous acid mist is suspended and/or mixed with the air in the treatment tank 2 . After completion of such treatment, the disinfectant generator 5 is stopped, and the disinfectant supply valve 16 and the circulation return valve are closed.

なお、仮に、第一工程において、処理槽2内を減圧後(つまり空気排除後)に除菌剤を供給するのでは、除菌剤を空気に浮遊および/または混合することができない。特に固体微粒子または液体微粒子の除菌剤の場合には、媒体としての空気がなければ浮遊状態を保つことができない。気体の除菌剤としても、大気圧程度まで復圧するには、大量の除菌剤が必要となる。また、真空状態の処理槽2内に外部から空気を導入しつつ、固体微粒子、液体微粒子または気体の除菌剤を供給して、除菌剤を空気に浮遊および/または混合するにしても、一度の処理で供給できる除菌剤を含む空気の体積は処理槽2の容積に制限されるため、除菌剤が処理槽2内の壁面に吸着するなどにより、処理槽2内の除菌剤濃度は供給初期濃度より低下してしまう。本実施例では、第一工程において、好ましくは処理槽2内を減圧することなく(つまり処理槽2内から空気排除することなく)、処理槽2内の空気中に除菌剤を供給するので、壁面吸着などによる不都合を防止することができる。 If, in the first step, the sterilizing agent is supplied after decompressing the processing tank 2 (that is, after removing the air), the sterilizing agent cannot be suspended and/or mixed in the air. In particular, in the case of a sterilizing agent composed of solid particles or liquid particles, it is impossible to maintain a floating state without air as a medium. Even with a gaseous sterilizing agent, a large amount of sterilizing agent is required to restore the pressure to about atmospheric pressure. In addition, even if solid particles, liquid particles, or gaseous sterilizing agents are supplied while air is introduced from the outside into the processing tank 2 in a vacuum state, and the sterilizing agents are suspended and/or mixed in the air, Since the volume of air containing the sterilizing agent that can be supplied in one treatment is limited to the volume of the processing tank 2, the sterilizing agent adsorbs to the walls of the processing tank 2. The concentration will be lower than the initial supply concentration. In this embodiment, in the first step, preferably, the disinfectant is supplied into the air in the processing tank 2 without reducing the pressure in the processing tank 2 (that is, without removing the air from the processing tank 2). Inconvenience due to wall surface adsorption can be prevented.

このような処理と並行して(または前後して)、第一工程では、一次弁7を閉じた状態で、真空ポンプ10を作動させて、排気路6の内、一次弁7よりも下流側を減圧する。この減圧時、典型的には、熱交給水弁11を閉じたままとすることで、熱交換器8に通水する必要はない。減圧開始から設定減圧時間が経過するか、または一次弁7よりも下流側の排気路6(好ましくは一次弁7と熱交換器8との間)に圧力センサを設けてその検出圧力が設定減圧圧力になると、真空ポンプ10を停止する。真空ポンプ10を停止することで、二次弁(逆止弁)9は閉鎖される。これにより、一次弁7と二次弁9との間の区間が、所定の減圧状態に保持されることになる。 In parallel with (or before or after) such processing, in the first step, with the primary valve 7 closed, the vacuum pump 10 is operated to is decompressed. During this depressurization, typically, by keeping the heat exchange water supply valve 11 closed, there is no need to supply water to the heat exchanger 8 . A set pressure reduction time has elapsed since the start of pressure reduction, or a pressure sensor is provided in the exhaust passage 6 downstream of the primary valve 7 (preferably between the primary valve 7 and the heat exchanger 8), and the detected pressure reaches the set pressure reduction. Once the pressure is reached, the vacuum pump 10 is stopped. By stopping the vacuum pump 10, the secondary valve (check valve) 9 is closed. As a result, the section between the primary valve 7 and the secondary valve 9 is maintained in a predetermined reduced pressure state.

第二工程では、二次弁9が閉じられた状態のまま、一次弁7を開ける。これにより、処理槽2内の空気(除菌剤を含む空気)は、減圧系統の所定域(処理槽2から熱交換器8の二次側)まで導入される。空気に浮遊および/または混合された除菌剤を、空気と共に、減圧系統に引き込むことで、熱交換器8や配管(処理槽2から熱交換器8の二次側までの排気路6)内の除菌を確実に図ることができる。 In the second step, the primary valve 7 is opened while the secondary valve 9 remains closed. As a result, the air in the processing tank 2 (air containing the sterilizing agent) is introduced to a predetermined area of the decompression system (from the processing tank 2 to the secondary side of the heat exchanger 8). By drawing the sterilizing agent floating and/or mixed in the air into the decompression system together with the air, the inside of the heat exchanger 8 and piping (exhaust path 6 from the processing tank 2 to the secondary side of the heat exchanger 8) can be reliably sterilized.

減圧下に気体の除菌剤を導入する場合、断熱膨張による温度低下により、除菌剤を凝縮液化させ、配管壁面や熱交換器8内面に有効に作用させることも期待される。なお、第二工程では、熱交給水弁11を開けて、熱交換器8に通水してもよい。これにより、熱交換器8への除菌剤の凝縮液化を一層効率的に図ることができる。一次弁7の開放後、好ましくは設定保持時間経過すると、次工程へ移行する。一次弁7の開放後、設定保持時間経過するまで待機することで、除菌剤による除菌効果を確実なものとすることができる。 When a gaseous sterilizing agent is introduced under reduced pressure, it is expected that the sterilizing agent will be condensed and liquefied due to a temperature drop due to adiabatic expansion, and will effectively act on the pipe wall surface and the inner surface of the heat exchanger 8 . In addition, in the second step, water may be supplied to the heat exchanger 8 by opening the heat exchange water supply valve 11 . As a result, the condensed liquid of the sterilizing agent to the heat exchanger 8 can be more efficiently achieved. After the primary valve 7 is opened, preferably when the set holding time has elapsed, the next step is performed. After the primary valve 7 is opened, the sterilizing effect of the sterilizing agent can be ensured by waiting until the set retention time elapses.

第三工程では、真空解除弁14を開けて、処理槽2内を大気圧まで復圧する。但し、第三工程では、真空解除弁14を開ける前に、まずは真空ポンプ10を作動させて、処理槽2内を所定時間または所定圧力まで減圧した後、真空ポンプ10を停止してから、真空解除弁14を開けてもよい。これにより、処理槽2内や減圧系統から除菌剤を排出できるから、処理槽2のドアを開けた際の除菌剤の放出を抑制して、安全性を高めることができる。なお、第三工程では、真空ポンプ10により処理槽2内を減圧後、大気圧未満の所定圧まで復圧し、再び、真空ポンプ10により所定まで減圧してから、大気圧まで復圧してもよい。 In the third step, the vacuum release valve 14 is opened to restore the pressure inside the processing tank 2 to atmospheric pressure. However, in the third step, before opening the vacuum release valve 14, the vacuum pump 10 is first operated to decompress the inside of the processing tank 2 for a predetermined time or to a predetermined pressure. Release valve 14 may be opened. As a result, the sterilizing agent can be discharged from the inside of the processing tank 2 and the decompression system, so that the release of the sterilizing agent when the door of the processing tank 2 is opened can be suppressed, and the safety can be improved. In the third step, the inside of the processing tank 2 may be depressurized by the vacuum pump 10, then repressurized to a predetermined pressure less than the atmospheric pressure, depressurized to the predetermined pressure again by the vacuum pump 10, and then repressurized to the atmospheric pressure. .

以上説明したとおり、本実施例の食品機械1によれば、水蒸気を用いることなく、処理槽2内や減圧系統の除菌を図ることができる。また、簡易な構成および制御で、減圧系統(熱交換器8や真空配管内)に除菌剤を導入して、容易に確実に除菌を図ることができる。 As described above, according to the food machine 1 of the present embodiment, it is possible to sterilize the inside of the processing tank 2 and the decompression system without using steam. In addition, with a simple configuration and control, it is possible to introduce the sterilizing agent into the decompression system (inside the heat exchanger 8 and the vacuum piping) to easily and reliably sterilize the system.

次に、本発明の実施例2の食品機械1について説明する。本実施例2の食品機械1も、基本的には前記実施例1と同様である。そこで、以下においては、両者の異なる点を中心に説明し、同様の箇所については説明を省略する。 Next, the food machine 1 of Example 2 of this invention is demonstrated. The food machine 1 of the second embodiment is also basically the same as the first embodiment. Therefore, in the following description, the points of difference between the two will be mainly described, and the description of the similar portions will be omitted.

処理槽2内の空気中に除菌剤を供給する除菌剤発生部として、前記実施例1では、除菌剤発生器5を処理槽2に接続したが、本実施例2では、除菌運転において処理槽2内に「燻煙剤または燻蒸剤」18が収容される。つまり、図1において、除菌剤発生器5、除菌剤供給路15および循環返送路17の設置が省略される代わりに、除菌運転において、二点鎖線で示すように、処理槽2内に燻煙剤または燻蒸剤18が入れられる。 In the first embodiment, the sterilizing agent generator 5 is connected to the processing tank 2 as the sterilizing agent generator for supplying the sterilizing agent to the air in the processing tank 2. In operation, a "fumigation or fumigant" 18 is contained within the treatment vessel 2 . That is, in FIG. 1, instead of omitting the installation of the disinfectant generator 5, the disinfectant supply path 15, and the circulation return path 17, during the disinfection operation, the inside of the treatment tank 2 is shown by a two-dot chain line. contains a fumigant or fumigant 18.

燻煙剤18とは、典型的には、加熱によって有効成分を煙状の微粒子(固体微粒子の除菌剤)として空中に拡散させる薬剤である。除菌剤を拡散させる際、化学薬品類の分解熱を利用したり、電熱器などの熱源を利用したり、蒸散器を利用して加熱水蒸気で有効成分を飛散させたりすることができる。 The fumigating agent 18 is typically a chemical that, when heated, diffuses an active ingredient into the air as smoke-like microparticles (sterilizing agent of solid microparticles). When diffusing the disinfectant, the decomposition heat of chemicals can be used, a heat source such as an electric heater can be used, or an evaporator can be used to scatter the active ingredient with heated steam.

たとえば、石灰と水が化学反応する際に発生する熱と水蒸気を利用して、除菌成分である「銀イオン」を三次元構造を持つゼオライトに保持させた「銀ゼオライト」を煙とともに放出する燻煙剤18を用いることができる。あるいは、イソプロピルメチルフェノールを有効成分とする煙状の除菌剤を放出する燻煙剤18を用いることができる。 For example, by using the heat and steam generated when lime and water chemically react, silver zeolite, which is a sterilizing component held in zeolite with a three-dimensional structure, is emitted along with the smoke. A fumigant 18 can be used. Alternatively, a fumigant 18 can be used that emits a smoke-like sanitizer with isopropylmethylphenol as the active ingredient.

燻蒸剤18とは、典型的には、常温で気体の状態で作用させて除菌する薬剤である。たとえば、所定濃度の二酸化塩素ガスを放出する燻蒸剤18を用いることができる。 The fumigant 18 is typically an agent that acts in a gaseous state at room temperature to sterilize. For example, a fumigant 18 that releases a concentration of chlorine dioxide gas can be used.

本実施例2の場合も、除菌運転(除菌方法)は、基本的には前記実施例1と同様であるが、以下の点で異なる。 In the case of the second embodiment as well, the sterilization operation (sterilization method) is basically the same as that of the first embodiment, but the following points are different.

本実施例2でも、除菌運転では、処理槽2内に食品を収容しないが、処理槽2内には、燻煙剤または燻蒸剤18を収容した状態で、処理槽2のドアを気密に閉じる。この際、燻煙剤または燻蒸剤18から、直ちに(あるいはその後遅れて)、固体微粒子、液体微粒子または気体の除菌剤が、単独または混在した状態で、処理槽2内の空気中に放出されるように、所定の準備をしてから処理槽2内に収容する。たとえば、燻煙剤18の容器に所定量の水を入れると共に薬液缶を入れて、処理槽2内に収容すればよい。 In the present embodiment 2 as well, in the sterilization operation, food is not stored in the processing tank 2, but the processing tank 2 contains a smoking agent or a fumigant 18, and the door of the processing tank 2 is closed airtightly. close. At this time, from the fumigating agent or fumigating agent 18, immediately (or later), solid particles, liquid particles, or gaseous sterilizing agents are released into the air in the treatment tank 2 alone or in a mixed state. As shown in FIG. For example, a container of fumigation agent 18 may be filled with a predetermined amount of water and a canister of chemical solution, and placed in processing tank 2 .

そして、処理槽2のドアを気密に閉じた状態で、操作盤から除菌運転の開始を指示すればよい。これにより、基本的には実施例1と同様に、第一工程、第二工程および第三工程を順次に実行する。 Then, with the door of the processing tank 2 airtightly closed, the start of the sterilization operation can be instructed from the control panel. As a result, the first step, the second step and the third step are sequentially performed basically in the same manner as in the first embodiment.

第一工程では、一次弁7を閉じた状態で、真空ポンプ10を作動させて、排気路6の内、一次弁7よりも下流側を減圧する。この減圧時、典型的には、熱交給水弁11を閉じたままとすることで、熱交換器8に通水する必要はない。減圧開始から設定減圧時間が経過するか、または一次弁7の出口側などに設けた圧力センサの検出圧力が設定減圧圧力になると、真空ポンプ10を停止する。真空ポンプ10を停止することで、二次弁(逆止弁)9は閉鎖される。これにより、一次弁7と二次弁9との間の区間が、所定の減圧状態に保持されることになる。 In the first step, with the primary valve 7 closed, the vacuum pump 10 is operated to reduce the pressure downstream of the primary valve 7 in the exhaust passage 6 . During this depressurization, typically, by keeping the heat exchange water supply valve 11 closed, there is no need to supply water to the heat exchanger 8 . When the set pressure reduction time elapses from the start of pressure reduction or when the pressure detected by the pressure sensor provided on the outlet side of the primary valve 7 reaches the set pressure reduction pressure, the vacuum pump 10 is stopped. By stopping the vacuum pump 10, the secondary valve (check valve) 9 is closed. As a result, the section between the primary valve 7 and the secondary valve 9 is maintained in a predetermined reduced pressure state.

第一工程中(または除菌運転の開始時もしくはドア閉鎖時(燻煙剤等のセット時)から所定時間経過するまで)、処理槽2内では、固体微粒子、液体微粒子および気体の内、いずれか一以上の状態の除菌剤が、燻煙剤または燻蒸剤18から処理槽2内の空気中に放出される。つまり、燻煙剤または燻蒸剤18から、煙状、ミスト状またはガス状の除菌剤が放出される。 During the first step (or until a predetermined time has passed since the start of the sterilization operation or the closing of the door (when setting the fumigant, etc.)), in the treatment tank 2, any of solid particles, liquid particles, and gas One or more of the sterilizing agents are released from the fumigant or fumigant 18 into the air within the treatment tank 2 . That is, the fumigant or fumigant 18 emits a smoke, mist or gaseous sanitizing agent.

上述のようにして、一次弁7よりも下流側を所定まで減圧すると共に、処理槽2内に所定まで除菌剤を充満させ終えると、次工程へ移行する。なお、第一工程において、燻煙剤または燻蒸剤18からの発熱や蒸気等によって処理槽2内の圧力が設定圧まで上昇した場合は、一次弁7を開いて除菌剤を減圧系統に導入してもよい(つまり第二工程へ移行してもよい)。いずれにしても、第一工程の終了後、第二工程および第三工程が順次に実行されるが、これら工程の内容は前記実施例1と同様のため、説明を省略する。 As described above, the downstream side of the primary valve 7 is depressurized to a predetermined level, and when the treatment tank 2 is completely filled with the sterilizing agent to a predetermined level, the process proceeds to the next step. In the first step, when the pressure in the treatment tank 2 rises to the set pressure due to the heat or steam from the fumigating agent or the fumigant 18, the primary valve 7 is opened to introduce the sterilizing agent into the decompression system. may be performed (that is, the second step may be performed). In any case, after the completion of the first step, the second step and the third step are sequentially executed.

本実施例2でも、第一工程において、空気に浮遊および/または混合された除菌剤を、第二工程において、空気と共に減圧系統の所定域に導入して、熱交換器8や配管内の除菌を容易に確実に図ることができる。 Also in the present embodiment 2, in the first step, the sterilizing agent suspended and/or mixed in the air is introduced into a predetermined region of the pressure reduction system together with the air in the second step, and the heat exchanger 8 and the inside of the piping Sterilization can be achieved easily and reliably.

本発明の食品機械1とその除菌方法は、前記各実施例(変形例を含む)の内容に限らず適宜変更可能である。 The food machine 1 and its sterilization method of the present invention are not limited to the contents of the above-described embodiments (including modifications) and can be modified as appropriate.

特に、本発明の食品機械1は、(a)処理槽2と、この処理槽2内の気体を外部へ吸引排出する減圧手段3と、減圧された処理槽2内へ外気を導入する復圧手段4と、各手段3,4を制御する制御手段とを備え、(b)減圧手段3として、処理槽2内からの排気路6に、一次弁7、熱交換器8、二次弁9および真空ポンプ10を順に備え、(c)固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、処理槽2内の空気中に供給する除菌剤発生部が、処理槽2に設けられるのであれば、その他の構成は適宜に変更可能である。 In particular, the food processing machine 1 of the present invention comprises (a) a processing tank 2, a depressurizing means 3 for sucking and discharging the gas in the processing tank 2 to the outside, and a pressure restoring means for introducing outside air into the decompressed processing tank 2. (b) as the decompression means 3, a primary valve 7, a heat exchanger 8, and a secondary valve 9 are provided in an exhaust passage 6 from the processing tank 2; and a vacuum pump 10 in this order, and (c) a sterilizing agent generator that supplies solid particles, liquid particles, or gaseous sterilizing agents singly or in a mixed state into the air in the processing tank 2. 2, other configurations can be changed as appropriate.

また、本発明の食品機械1の除菌方法は、処理槽2内からの排気路6に、一次弁7、熱交換器8、二次弁9および真空ポンプ10が順に設けられる一方、処理槽2内への給気路12に真空解除弁14が設けられた食品機械1の除菌方法であって、(a)固体微粒子、液体微粒子および気体の内、いずれか一以上の状態の除菌剤、または当該除菌剤を含む空気を、一次弁7を閉じた状態で、処理槽2内の空気中に供給する一方、真空ポンプ10により一次弁7よりも下流側を減圧する第一工程と、(b)二次弁9が閉じられた状態で、一次弁7を開けて、処理槽2内の除菌剤を熱交換器8へ導入する第二工程と、(c)真空解除弁14を開ける第三工程とを順次に行うのであれば、その他の内容は適宜に変更可能である。 In addition, in the sterilization method for the food machine 1 of the present invention, the primary valve 7, the heat exchanger 8, the secondary valve 9 and the vacuum pump 10 are provided in order in the exhaust passage 6 from the processing tank 2. A method of sterilizing a food machine 1 in which a vacuum release valve 14 is provided in an air supply path 12 to the inside of the food machine 1, comprising: A first step of supplying the agent or air containing the sterilizing agent to the air in the processing tank 2 with the primary valve 7 closed, and reducing the pressure downstream of the primary valve 7 by the vacuum pump 10. (b) a second step of opening the primary valve 7 while the secondary valve 9 is closed to introduce the sterilizing agent in the treatment tank 2 into the heat exchanger 8; and (c) a vacuum release valve. If the third step of opening 14 is performed sequentially, other contents can be changed as appropriate.

たとえば、除菌剤発生部として、どのような除菌剤発生器5、燻煙剤または燻蒸剤18などを用いて、どのような除菌剤を発生させるかは、前記各実施例に限定されない。 For example, what kind of disinfectant generator 5, fumigating agent or fumigating agent 18 is used as the disinfectant generating section, and what kind of disinfectant is generated is not limited to the above-described embodiments. .

また、前記実施例1では、処理槽2に除菌剤発生器5が接続されたが、除菌剤発生器5は、処理槽2に対し着脱可能に設けられてもよい。 Moreover, in the first embodiment, the disinfectant generator 5 is connected to the treatment tank 2 , but the disinfectant generator 5 may be detachably attached to the treatment tank 2 .

また、前記各実施例では、処理槽2内を減圧することなく、除菌剤発生器5(ガスボンベを含む)、燻煙剤または燻蒸剤18などから処理槽2内の空気中に除菌剤を供給したが、場合により、処理槽2内を一旦減圧後、復圧しながら除菌剤を供給するようにしてもよい。たとえば、第一工程において、一次弁7を開けた状態で真空ポンプ10を作動させて、処理槽2内も減圧後、一次弁7を閉じた状態で、除菌剤または当該除菌剤を含む空気を処理槽2内に供給して復圧し、以後、前記各実施例と同様にして、一次弁7を開けて、熱交換器8などの除菌を図ればよい。第一工程において、真空ポンプ10による減圧途中で、一次弁7を閉じて(つまり処理槽2内に空気を多少残して)、一次弁7の上流側(処理槽2内)と下流側(熱交換器8内)との間に圧力差を設けてもよい。 Further, in each of the above embodiments, the sterilizing agent generator 5 (including a gas cylinder), the fumigating agent or the fumigating agent 18, etc., are supplied to the air in the processing tank 2 without depressurizing the inside of the processing tank 2 . However, depending on the situation, the sterilizing agent may be supplied while the inside of the treatment tank 2 is once decompressed and then the pressure is restored. For example, in the first step, the vacuum pump 10 is operated with the primary valve 7 open, and after the inside of the processing tank 2 is also decompressed, with the primary valve 7 closed, the disinfectant or the disinfectant is added. Air is supplied into the processing tank 2 to restore the pressure, and then the primary valve 7 is opened to sterilize the heat exchanger 8 and the like in the same manner as in the above embodiments. In the first step, the primary valve 7 is closed while the pressure is reduced by the vacuum pump 10 (that is, some air is left in the processing tank 2), and the upstream side (in the processing tank 2) and the downstream side (heat A pressure difference may be provided between the exchanger 8).

また、前記各実施例において、除菌運転では、第一工程、第二工程および第三工程を順次に実行したが、第一工程から第三工程までのセットを複数回繰り返してもよい。 Moreover, in each of the above examples, the first step, the second step and the third step were sequentially performed in the sterilization operation, but the set from the first step to the third step may be repeated multiple times.

また、前記各実施例において、二次弁9は、逆止弁から構成されたが、遮断弁(電磁弁、電動弁の他、手動弁でもよい)から構成されてもよい。いずれの場合も、前記逆止弁の開閉と同様に、遮断弁を開閉(真空ポンプ10の発停と遮断弁の開閉を連動)させればよい。 In each of the above embodiments, the secondary valve 9 is composed of a check valve, but may be composed of a shutoff valve (a solenoid valve, an electric valve, or a manual valve). In either case, the shut-off valve may be opened and closed (starting/stopping of the vacuum pump 10 and opening/closing of the shut-off valve may be interlocked) in the same manner as the opening and closing of the check valve.

また、前記各実施例において、減圧手段3は、処理槽2内からの排気路6に、一次弁7、熱交換器8、二次弁9および真空ポンプ10を順に備えるのであれば、その他の構成は適宜に変更可能である。たとえば、前記各実施例において、場合により、蒸気エゼクタをさらに備えてもよい。 Further, in each of the above embodiments, if the decompression means 3 is equipped with the primary valve 7, the heat exchanger 8, the secondary valve 9 and the vacuum pump 10 in order in the exhaust passage 6 from the inside of the processing tank 2, other The configuration can be changed as appropriate. For example, each of the above embodiments may optionally further include a steam ejector.

さらに、前記各実施例では、真空冷却装置に適用した例について説明したが、減圧手段3を備えるのであれば、真空冷却装置以外の各種食品機械1にも同様に適用可能である。 Furthermore, in each of the above-described embodiments, an example of application to a vacuum cooling device has been described, but as long as the decompression means 3 is provided, it can be similarly applied to various food machines 1 other than the vacuum cooling device.

1 食品機械
2 処理槽
3 減圧手段
4 復圧手段
5 除菌剤発生器(除菌剤発生部)
6 排気路
7 一次弁
8 熱交換器
9 二次弁
10 真空ポンプ
11 熱交給水弁
12 給気路
13 エアフィルタ
14 真空解除弁
15 除菌剤供給路
16 除菌剤供給弁
17 循環返送路
18 燻煙剤・燻蒸剤(除菌剤発生部)
1 food machine 2 treatment tank 3 decompression means 4 pressure recovery means 5 sanitizer generator (sanitizer generator)
6 exhaust path 7 primary valve 8 heat exchanger 9 secondary valve 10 vacuum pump 11 heat exchange water supply valve 12 air supply path 13 air filter 14 vacuum release valve 15 disinfectant supply path 16 disinfectant supply valve 17 circulation return path 18 Fumigation agent / fumigation agent (disinfectant generation part)

Claims (8)

処理槽と、この処理槽内の気体を外部へ吸引排出する減圧手段と、減圧された前記処理槽内へ外気を導入する復圧手段と、前記各手段を制御する制御手段とを備え、
前記減圧手段として、前記処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプを順に備え、
固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、前記処理槽内の空気中に供給する除菌剤発生部が、前記処理槽に設けられる食品機械であって、
前記処理槽内に食品が収容されず且つ前記処理槽のドアが閉じられた状態で、前記制御手段により除菌運転を実行可能とされ、
前記除菌運転では、
前記一次弁を閉じた状態で前記除菌剤発生部から発生させた除菌剤を前記処理槽内に供給する一方、前記真空ポンプにより前記一次弁よりも下流側を減圧した後、
前記二次弁が閉じられた状態で前記一次弁を開ける
ことを特徴とする食品機械。
a processing tank, decompression means for sucking and discharging gas in the processing tank to the outside, pressure recovery means for introducing outside air into the decompressed processing tank, and control means for controlling each of the means,
A primary valve, a heat exchanger, a secondary valve and a vacuum pump are provided in this order in an exhaust passage from the processing tank as the decompression means,
A food machine in which a sterilizing agent generating unit that supplies solid particles, liquid particles, or gaseous sterilizing agents alone or in a mixed state to the air in the processing tank is provided in the processing tank,
The sterilization operation can be executed by the control means in a state where no food is stored in the processing tank and the door of the processing tank is closed,
In the sterilization operation,
While the sterilizing agent generated from the sterilizing agent generating unit is supplied into the processing tank with the primary valve closed, after the vacuum pump reduces the pressure downstream of the primary valve,
opening the primary valve while the secondary valve is closed
A food machine characterized by:
前記除菌運転では、前記二次弁が閉じられた状態で前記一次弁を開けて設定時間保持してから、前記減圧手段により前記処理槽内を減圧後、前記復圧手段により前記処理槽内を復圧する
ことを特徴とする請求項1に記載の食品機械。
In the sterilization operation, after the primary valve is opened with the secondary valve closed and held for a set time, the inside of the processing tank is decompressed by the decompression means, and the inside of the processing tank is depressurized by the pressure recovery means. 2. The food machine according to claim 1, wherein the pressure is restored.
前記処理槽には、前記除菌剤発生部としての除菌剤発生器が接続されている
ことを特徴とする請求項1または請求項2に記載の食品機械。
The food machine according to claim 1 or 2, wherein a disinfectant generator as the disinfectant generator is connected to the processing tank.
除菌運転において、前記処理槽内には、前記除菌剤発生部として、燻煙剤または燻蒸剤が収容される
ことを特徴とする請求項1または請求項2に記載の食品機械。
3. The food machine according to claim 1, wherein in the sterilization operation, a smoking agent or a fumigating agent is accommodated in the processing tank as the sterilization agent generator.
処理槽と、この処理槽内の気体を外部へ吸引排出する減圧手段と、減圧された前記処理槽内へ外気を導入する復圧手段と、前記各手段を制御する制御手段とを備え、
前記減圧手段として、前記処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプを順に備え、
固体微粒子、液体微粒子または気体の除菌剤を、単独または混在した状態で、前記処理槽内の空気中に供給する除菌剤発生部が、前記処理槽に設けられる食品機械であって、
除菌運転において、前記処理槽内には、前記除菌剤発生部として、燻煙剤または燻蒸剤が収容される
ことを特徴とする食品機械。
a processing tank, decompression means for sucking and discharging gas in the processing tank to the outside, pressure recovery means for introducing outside air into the decompressed processing tank, and control means for controlling each of the means,
A primary valve, a heat exchanger, a secondary valve and a vacuum pump are provided in this order in an exhaust passage from the processing tank as the decompression means,
A food machine in which a sterilizing agent generating unit that supplies solid particles, liquid particles, or gaseous sterilizing agents alone or in a mixed state to the air in the processing tank is provided in the processing tank,
A food machine according to claim 1, wherein, in the disinfecting operation, a smoking agent or a fumigating agent is accommodated in the processing tank as the disinfecting agent generator.
前記一次弁は、前記制御手段により開閉制御される弁であり、
前記二次弁は、前記真空ポンプの作動の有無に伴い開閉する逆止弁である
ことを特徴とする請求項1~5のいずれか1項に記載の食品機械。
The primary valve is a valve that is controlled to open and close by the control means,
The food machine according to any one of claims 1 to 5, wherein the secondary valve is a check valve that opens and closes depending on whether or not the vacuum pump is operated.
処理槽内からの排気路に、一次弁、熱交換器、二次弁および真空ポンプが順に設けられる一方、前記処理槽内への給気路に真空解除弁が設けられた食品機械の除菌方法であって、
固体微粒子、液体微粒子および気体の内、いずれか一以上の状態の除菌剤、または当該除菌剤を含む空気を、前記一次弁を閉じた状態で、前記処理槽内の空気中に供給する一方、前記真空ポンプにより前記一次弁よりも下流側を減圧する第一工程と、
前記二次弁が閉じられた状態で、前記一次弁を開けて、前記処理槽内の除菌剤を前記熱交換器へ導入する第二工程と、
前記真空解除弁を開ける第三工程と
を順次に行うことを特徴とする食品機械の除菌方法。
Sterilization of a food machine in which a primary valve, a heat exchanger, a secondary valve, and a vacuum pump are provided in order in an exhaust passage from the processing tank, and a vacuum release valve is provided in the air supply passage to the processing tank. a method,
A sterilizing agent in one or more states of solid particulates, liquid particulates and gas, or air containing the sterilizing agent is supplied into the air in the processing tank with the primary valve closed. On the other hand, a first step of reducing the pressure downstream of the primary valve with the vacuum pump;
a second step of opening the primary valve while the secondary valve is closed to introduce the sterilizing agent in the treatment tank into the heat exchanger;
and a third step of opening the vacuum release valve.
前記第三工程では、前記真空ポンプにより前記処理槽内を減圧後、前記真空解除弁を開ける
ことを特徴とする請求項7に記載の食品機械の除菌方法。
8. The sterilization method for a food machine according to claim 7, wherein, in said third step, said vacuum release valve is opened after reducing the pressure in said processing tank by said vacuum pump.
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Cited By (1)

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US7059300B2 (en) 2003-12-24 2006-06-13 Mitsubishi Denki Kabushiki Kaisha Ignition control apparatus for internal combustion engine

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