JP6226129B2 - Sterilizer - Google Patents

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JP6226129B2
JP6226129B2 JP2014003890A JP2014003890A JP6226129B2 JP 6226129 B2 JP6226129 B2 JP 6226129B2 JP 2014003890 A JP2014003890 A JP 2014003890A JP 2014003890 A JP2014003890 A JP 2014003890A JP 6226129 B2 JP6226129 B2 JP 6226129B2
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heat exchanger
valve
cooling water
cooling
compressed air
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JP2015130825A (en
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健司 金澤
健司 金澤
暁 若狭
暁 若狭
泰三 松川
泰三 松川
松藤 幸樹
幸樹 松藤
康 田中
康 田中
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Miura Co Ltd
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  • Apparatus For Disinfection Or Sterilisation (AREA)

Description

本発明は、レトルト食品などの加熱殺菌とその後の冷却に用いられる殺菌装置に関するものである。   The present invention relates to a sterilizer used for heat sterilization and subsequent cooling of retort foods and the like.

従来、下記特許文献1に開示されるように、殺菌槽(1)内に被殺菌物(2)を収容すると共に水を貯留し、この貯留水を熱交換器(3)との間で循環させ、この循環水を熱交換器(3)において蒸気により加熱するか、クーリングタワー(8)からの冷却用水で冷却するかを切り替えて、被殺菌物(2)の加熱殺菌とその後の冷却を図る殺菌装置が知られている。   Conventionally, as disclosed in the following Patent Document 1, the sterilization tank (1) accommodates the article to be sterilized (2), stores water, and circulates the stored water between the heat exchanger (3). The circulating water is heated with steam in the heat exchanger (3) or with cooling water from the cooling tower (8) to switch between cooling and sterilization of the article to be sterilized (2) and subsequent cooling. Sterilizers are known.

特許第4229420号公報Japanese Patent No. 4229420

前記特許文献1に記載の殺菌装置のように、処理槽と熱交換器との間で水を循環させつつ、殺菌工程では熱交換器に蒸気を供給し、その後の冷却工程では熱交換器に冷却水を供給する場合、殺菌工程から冷却工程への移行時、蒸気が充満している熱交換器内に冷却水が流れ込むことになる。これに伴い、熱交換器および配管内において蒸気が急激に凝縮し、それに伴う急減圧による衝撃により、熱交換器の安全弁から蒸気が噴き出したり、配管から音や振動が発生したりする。   As in the sterilization apparatus described in Patent Document 1, while circulating water between the treatment tank and the heat exchanger, steam is supplied to the heat exchanger in the sterilization process, and then to the heat exchanger in the subsequent cooling process. When supplying cooling water, at the time of transfer from the sterilization process to the cooling process, the cooling water flows into the heat exchanger filled with steam. Along with this, steam condenses abruptly in the heat exchanger and the piping, and the steam is ejected from the safety valve of the heat exchanger or noise and vibration are generated from the piping due to the impact caused by the sudden decompression.

本発明が解決しようとする課題は、殺菌工程から冷却工程への移行時に、安全弁から蒸気が噴き出したり、配管から音や振動が発生したりするのを防止することにある。   The problem to be solved by the present invention is to prevent steam from spouting out from the safety valve or generating noise or vibration from the piping during the transition from the sterilization process to the cooling process.

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、被処理物が収容されると共に水が貯留される処理槽と、この処理槽内の貯留水を熱交換器との間で循環させる循環手段と、この循環手段による循環水を加熱するために、前記熱交換器に蒸気を供給する給蒸手段と、前記循環手段による循環水を冷却するために、前記熱交換器に冷却水を供給する冷却手段と、前記給蒸手段による前記熱交換器への蒸気供給の停止後、前記冷却手段による前記熱交換器への冷却水供給の開始前に、前記熱交換器へ圧縮空気を供給する圧縮空気供給手段とを備えることを特徴とする殺菌装置である。   The present invention has been made to solve the above-mentioned problems, and the invention according to claim 1 includes a treatment tank in which an object to be treated is stored and water is stored, and stored water in the treatment tank. Circulating means for circulating between the heat exchanger, steaming means for supplying steam to the heat exchanger to heat the circulating water by the circulating means, and cooling the circulating water by the circulating means A cooling means for supplying cooling water to the heat exchanger, and after the steam supply to the heat exchanger by the steaming means is stopped, before the cooling water supply to the heat exchanger by the cooling means is started, A sterilizer comprising compressed air supply means for supplying compressed air to the heat exchanger.

請求項1に記載の発明によれば、熱交換器には、蒸気供給の停止後、冷却水供給の開始前に、圧縮空気が供給されるので、冷却水供給時に冷却水により蒸気が凝縮しても急激に減圧されるのが防止される。これにより、急減圧による衝撃が防止され、安全弁から蒸気が噴き出したり、配管から音や振動が発生したりするのを防止できる。   According to the first aspect of the present invention, since the compressed air is supplied to the heat exchanger after the stop of the steam supply and before the start of the cooling water supply, the steam is condensed by the cooling water when the cooling water is supplied. However, sudden pressure reduction is prevented. Thereby, the impact by sudden pressure reduction is prevented and it can prevent that a vapor spouts from a safety valve, or a sound and a vibration generate | occur | produce from piping.

請求項2に記載の発明は、前記給蒸手段による前記熱交換器への蒸気供給を停止してから第一設定時間経過後、前記圧縮空気供給手段による前記熱交換器への圧縮空気の供給を開始し、前記圧縮空気供給手段による前記熱交換器への圧縮空気供給を開始してから第二設定時間経過後、前記冷却手段による前記熱交換器への冷却水の供給を開始し、前記圧縮空気供給手段による前記熱交換器への圧縮空気の供給は、前記冷却手段による前記熱交換器への冷却水供給の開始時までなされるか、前記冷却手段による前記熱交換器への冷却水供給を開始してから第三設定時間経過時までなされることを特徴とする請求項1に記載の殺菌装置である。   According to a second aspect of the present invention, the supply of compressed air to the heat exchanger by the compressed air supply means after the first set time has elapsed after the supply of steam to the heat exchanger by the steam supply means has been stopped. Starting a supply of compressed air to the heat exchanger by the compressed air supply means, after a second set time has elapsed, start supplying cooling water to the heat exchanger by the cooling means, The compressed air is supplied to the heat exchanger by the compressed air supply means until the start of the supply of the cooling water to the heat exchanger by the cooling means or the cooling water to the heat exchanger by the cooling means. The sterilizing apparatus according to claim 1, wherein the sterilizing apparatus is performed from the start of supply until a third set time elapses.

請求項2に記載の発明によれば、熱交換器には、蒸気供給の停止後、第一設定時間経過してから圧縮空気が供給され、その圧縮空気供給の開始後、第二設定時間経過してから冷却水が供給される。そして、冷却水供給の開始時またはそれから第三設定時間経過するまで、圧縮空気供給が継続される。これにより、冷却水供給時の急激な減圧を確実に防止して、安全弁からの蒸気の噴き出しと、配管からの音や振動の発生とをさらに確実に防止できる。   According to the second aspect of the present invention, the heat exchanger is supplied with compressed air after the first set time has elapsed after the steam supply is stopped, and after the start of the compressed air supply, the second set time has elapsed. Then, cooling water is supplied. Then, the compressed air supply is continued at the start of the cooling water supply or until the third set time has elapsed. Thereby, it is possible to reliably prevent sudden pressure reduction during the supply of cooling water, and more reliably prevent the ejection of steam from the safety valve and the generation of noise and vibration from the piping.

さらに、請求項3に記載の発明は、前記処理槽内には、前記被処理物を浸漬しない水位まで水が貯留され、前記循環手段は、前記処理槽内の底部からの水を、前記熱交換器を介して前記処理槽内の被処理物へ噴出して戻し、前記冷却手段は、前記熱交換器とクーリングタワーとの間で冷却水を循環させ、前記クーリングタワーから前記熱交換器への冷却水送り路に冷却水送り弁を備える一方、前記熱交換器から前記クーリングタワーへの冷却水戻し路に冷却水戻し弁を備え、前記給蒸手段は、給蒸弁を備える給蒸路が、前記冷却水送り弁よりも下流の前記冷却水送り路に接続され、前記給蒸手段による蒸気のドレンを外部へ排出するドレン排出手段は、ドレン排出弁を備えるドレン排出路が、前記冷却水戻し弁よりも上流の前記冷却水戻し路に接続され、前記圧縮空気供給手段は、圧縮空気供給弁を備える圧縮空気路が、前記冷却水送り弁よりも下流の前記冷却水送り路に接続されるか、前記給蒸弁よりも下流の前記給蒸路に接続され、前記冷却水送り弁、前記冷却水戻し弁および前記圧縮空気供給弁を閉じる一方、前記給蒸弁および前記ドレン排出弁を開けて、前記給蒸手段からの蒸気を前記熱交換器に供給して前記循環水を加熱することで、前記被処理物を殺菌し、前記処理槽内が殺菌温度以上で殺菌時間経過すると、前記給蒸弁を閉じ、前記給蒸弁を閉じてから第一設定時間経過すると、前記圧縮空気供給弁を開け、前記圧縮空気供給弁を開けてから第二設定時間経過すると、前記冷却水送り弁および前記冷却水戻し弁を開ける一方、前記ドレン排出弁を閉じて、前記クーリングタワーからの冷却水を前記熱交換器に供給して前記循環水を冷却することで、前記被処理物を冷却し、前記熱交換器への冷却水供給の開始時、またはその時点から第三設定時間経過時に、前記圧縮空気供給弁を閉じることを特徴とする請求項1または請求項2に記載の殺菌装置である。   Furthermore, in the invention according to claim 3, water is stored in the treatment tank up to a water level at which the object to be treated is not immersed, and the circulation means supplies water from the bottom in the treatment tank to the heat. The cooling means circulates cooling water between the heat exchanger and the cooling tower, and cools the cooling tower to the heat exchanger via an exchanger. While the water feed path is provided with a cooling water feed valve, the cooling water return path from the heat exchanger to the cooling tower is provided with a cooling water return valve, and the steaming means is provided with a steam feed valve. The drain discharge means connected to the cooling water feed path downstream of the cooling water feed valve and discharges steam drained by the steam supply means to the outside includes a drain discharge path provided with a drain discharge valve. The cooling water return path upstream from The compressed air supply means is connected to the cooling water feed path downstream of the cooling water feed valve, or the downstream side of the steam supply valve. The steam supply passage is connected, and the cooling water feed valve, the cooling water return valve and the compressed air supply valve are closed, while the steam supply valve and the drain discharge valve are opened, and the steam from the steam supply means is By supplying to a heat exchanger and heating the circulating water, the object to be treated is sterilized, and when the inside of the treatment tank is at or above the sterilization temperature, the steam supply valve is closed and the steam supply valve is When the first set time elapses after closing, the compressed air supply valve is opened, and when the second set time elapses after the compressed air supply valve is opened, the cooling water feed valve and the cooling water return valve are opened, Close the drain discharge valve and Cooling water from a tower is supplied to the heat exchanger to cool the circulating water, thereby cooling the object to be processed, and starting from or at the time when cooling water supply to the heat exchanger is started. The sterilizer according to claim 1 or 2, wherein the compressed air supply valve is closed when a set time has elapsed.

請求項3に記載の発明によれば、冷却水送り弁、冷却水戻し弁、給蒸弁、ドレン排出弁および圧縮空気供給弁の開閉制御により、殺菌工程から冷却工程への移行時における安全弁からの蒸気の噴き出しと、配管からの音や振動の発生とを防止できる。また、熱交換器には、蒸気供給の停止後、第一設定時間経過してから圧縮空気が供給され、その圧縮空気供給の開始後、第二設定時間経過してから冷却水が供給される。そして、冷却水供給の開始時またはそれから第三設定時間経過するまで、圧縮空気供給が継続される。これにより、冷却水供給時の急激な減圧を確実に防止して、安全弁からの蒸気の噴き出しと、配管からの音や振動の発生とをさらに確実に防止できる。   According to the third aspect of the present invention, the opening and closing control of the cooling water feed valve, the cooling water return valve, the steam supply valve, the drain discharge valve, and the compressed air supply valve allows the safety valve to be switched from the sterilization process to the cooling process. This prevents the generation of steam and the generation of noise and vibration from the piping. The heat exchanger is supplied with compressed air after the first set time elapses after the steam supply is stopped, and is supplied with cooling water after the second set time elapses after the compressed air supply starts. . Then, the compressed air supply is continued at the start of the cooling water supply or until the third set time has elapsed. Thereby, it is possible to reliably prevent sudden pressure reduction during the supply of cooling water, and more reliably prevent the ejection of steam from the safety valve and the generation of noise and vibration from the piping.

本発明によれば、殺菌工程から冷却工程への移行時に、安全弁から蒸気が噴き出したり、配管から音や振動が発生したりするのを防止することができる。   ADVANTAGE OF THE INVENTION According to this invention, it can prevent that a vapor | steam spouts from a safety valve, or a sound and a vibration generate | occur | produce from piping at the time of transfer from a sterilization process to a cooling process.

本発明の殺菌装置の一実施例を示す概略図であり、一部を断面にして示している。It is the schematic which shows one Example of the sterilizer of this invention, and has shown one part in cross section.

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。
図1は、本発明の殺菌装置1の一実施例を示す概略図であり、一部を断面にして示している。本実施例の殺菌装置1は、被処理物2を加熱殺菌後に冷却する装置である。被処理物2は、特に問わないが、典型的にはレトルト食品または缶詰など、容器に密閉された食材である。
Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic view showing an embodiment of the sterilizing apparatus 1 of the present invention, and a part thereof is shown in cross section. The sterilization apparatus 1 of the present embodiment is an apparatus that cools the workpiece 2 after heat sterilization. The workpiece 2 is not particularly limited, but is typically a food material sealed in a container, such as retort food or canned food.

本実施例の殺菌装置1は、被処理物2が収容される処理槽3と、この処理槽3内への給水手段4と、処理槽3外への排水手段5と、処理槽3内の加圧手段6と、処理槽3外への排気手段7と、処理槽3と熱交換器8との間で水を循環させる循環手段9と、循環手段9による循環水を加熱するために熱交換器8に蒸気を供給する給蒸手段10と、循環手段9による循環水を冷却するために熱交換器8に冷却水を供給する冷却手段11と、給蒸手段10による蒸気の凝縮水(ドレン)を排出するドレン排出手段12と、熱交換器8へ圧縮空気を供給する圧縮空気供給手段13と、これら各手段4〜7,9〜13を制御する制御手段(図示省略)とを備える。   The sterilization apparatus 1 of the present embodiment includes a treatment tank 3 in which an object to be treated 2 is accommodated, a water supply means 4 into the treatment tank 3, a drainage means 5 to the outside of the treatment tank 3, and a treatment tank 3 Pressurizing means 6, exhaust means 7 to the outside of the treatment tank 3, circulation means 9 for circulating water between the treatment tank 3 and the heat exchanger 8, and heat for heating the circulating water by the circulation means 9 Steam supply means 10 for supplying steam to the exchanger 8, cooling means 11 for supplying cooling water to the heat exchanger 8 to cool the circulating water by the circulation means 9, and steam condensate by the steam supply means 10 ( A drain discharge means 12 for discharging the drain), a compressed air supply means 13 for supplying compressed air to the heat exchanger 8, and a control means (not shown) for controlling these means 4 to 7 and 9 to 13 are provided. .

処理槽3は、被処理物2を収容する中空容器である。処理槽3は、その形状を特に問わないが、本実施例では水平に配置された円筒材を備え、この円筒材は、一方の開口部が閉塞されており、他方の開口部が扉で開閉可能とされている。扉を開けることで、処理槽3に対し被処理物2を出し入れすることができ、扉を閉じることで、処理槽3の開口部を気密に閉じることができる。なお、被処理物2は、台車に載せられるなどして、処理槽3内の底面よりも上方に保持される。   The treatment tank 3 is a hollow container that accommodates the workpiece 2. The shape of the treatment tank 3 is not particularly limited. In the present embodiment, the treatment tank 3 includes a horizontally disposed cylindrical material, and this cylindrical material has one opening closed and the other opening opened and closed by a door. It is possible. By opening the door, the workpiece 2 can be taken in and out of the processing tank 3, and by closing the door, the opening of the processing tank 3 can be closed airtight. In addition, the to-be-processed object 2 is hold | maintained above the bottom face in the processing tank 3 by mounting on the trolley | bogie.

処理槽3には、処理槽3内の温度を検出する温度センサ14が設けられると共に、処理槽3内の水位を検出する水位検出器(図示省略)が設けられる。なお、温度センサ14は、処理槽3ではなく、場合により、後述する循環路15(特に熱交換器8より下流側)に設けられてもよい。   The processing tank 3 is provided with a temperature sensor 14 for detecting the temperature in the processing tank 3 and a water level detector (not shown) for detecting the water level in the processing tank 3. In addition, the temperature sensor 14 may be provided not in the processing tank 3 but in the circulation path 15 described later (in particular, on the downstream side of the heat exchanger 8) in some cases.

給水手段4は、給水路16を介して処理槽3内へ水を供給する。給水路16は、処理槽3の底部に接続され、処理槽3へ向けて給水ポンプ17と給水弁18とが設けられている。給水ポンプ17を作動させた状態で給水弁18を開くことで、給水源からの水を処理槽3内に供給して、処理槽3内に水を貯留することができる。本実施例では、処理槽3内に収容した被処理物2を浸漬しない設定水位まで、処理槽3内に水が貯留される。   The water supply means 4 supplies water into the treatment tank 3 through the water supply path 16. The water supply path 16 is connected to the bottom of the processing tank 3, and a water supply pump 17 and a water supply valve 18 are provided toward the processing tank 3. By opening the water supply valve 18 in a state where the water supply pump 17 is operated, water from the water supply source can be supplied into the treatment tank 3 and water can be stored in the treatment tank 3. In a present Example, water is stored in the processing tank 3 to the setting water level which does not immerse the to-be-processed object 2 accommodated in the processing tank 3. FIG.

排水手段5は、排水路19を介して処理槽3内から水を排出する。排水路19は、処理槽3の底部に接続され、排水弁20が設けられている。排水弁20を開くことで、処理槽3内の水を外部へ排出することができる。   The drainage means 5 discharges water from the treatment tank 3 through the drainage channel 19. The drainage channel 19 is connected to the bottom of the treatment tank 3 and a drainage valve 20 is provided. By opening the drain valve 20, the water in the processing tank 3 can be discharged to the outside.

加圧手段6は、加圧路21を介して処理槽3内へ圧縮空気を供給する。加圧路21に設けた加圧弁22を開くことで、圧縮空気源からの圧縮空気を処理槽3内に供給して、大気圧を超える圧力に処理槽3内を加圧することができる。   The pressurizing unit 6 supplies compressed air into the processing tank 3 through the pressurizing path 21. By opening the pressurization valve 22 provided in the pressurization path 21, the compressed air from a compressed air source can be supplied in the process tank 3, and the inside of the process tank 3 can be pressurized to the pressure exceeding atmospheric pressure.

排気手段7は、大気圧を超える圧力下の処理槽3内から排気路23を介して気体を排出する。排気路23は、処理槽3の上部に接続され、排気弁24が設けられている。処理槽3内が大気圧を超える圧力にある状態で、排気弁24を開くと、処理槽3内の気体は排気路23を介して外部へ排出され、処理槽3内の圧力を下げることができる。   The exhaust means 7 exhausts the gas from the inside of the processing tank 3 under a pressure exceeding the atmospheric pressure through the exhaust path 23. The exhaust path 23 is connected to the upper part of the processing tank 3 and is provided with an exhaust valve 24. When the exhaust valve 24 is opened while the inside of the processing tank 3 is at a pressure exceeding the atmospheric pressure, the gas in the processing tank 3 is discharged to the outside through the exhaust path 23, and the pressure in the processing tank 3 may be lowered. it can.

熱交換器8は、処理槽3との間で水が循環され、その循環水と、蒸気または冷却水とを間接熱交換する。つまり、熱交換器8は、循環手段9により処理槽3からの水が通されると共に、この循環水を加熱するために給蒸手段10から蒸気が通されるか、循環水を冷却するために冷却手段11から冷却水が通される。また、後述するように、熱交換器8への蒸気供給の停止後、冷却水供給の開始前、熱交換器8(蒸気または冷却水が通される側)には、圧縮空気供給手段13からの圧縮空気が供給可能とされる。そして、その圧縮空気による熱交換器8の加圧は、冷却水供給の開始時に終了されるか、冷却水供給の開始直後の所定タイミングまで継続される。   In the heat exchanger 8, water is circulated with the treatment tank 3, and the circulated water and steam or cooling water exchange heat indirectly. In other words, the heat exchanger 8 allows water from the treatment tank 3 to be passed by the circulation means 9 and also allows steam to pass from the steam supply means 10 to heat the circulating water or to cool the circulating water. Cooling water is passed through the cooling means 11. Further, as will be described later, after the supply of steam to the heat exchanger 8 is stopped and before the start of the cooling water supply, the heat exchanger 8 (the side through which the steam or cooling water is passed) is connected to the compressed air supply means 13. Of compressed air can be supplied. The pressurization of the heat exchanger 8 with the compressed air is terminated at the start of the cooling water supply or is continued until a predetermined timing immediately after the start of the cooling water supply.

循環手段9は、処理槽3と熱交換器8との間で水を循環する。循環手段9は、循環路15と循環ポンプ25とを備える。循環路15は、一端部が処理槽3の底部に接続され、処理槽3の底部からの循環路15は、循環ポンプ25と熱交換器8とを順に介して、他端部が処理槽3内のノズル26に接続されている。このノズル26は、処理槽3内の側部および/または上部に設けられており、循環ポンプ25からの水を被処理物2へ向けて噴射する。   The circulation means 9 circulates water between the treatment tank 3 and the heat exchanger 8. The circulation means 9 includes a circulation path 15 and a circulation pump 25. One end of the circulation path 15 is connected to the bottom of the processing tank 3, and the circulation path 15 from the bottom of the processing tank 3 passes through the circulation pump 25 and the heat exchanger 8 in order, and the other end is connected to the processing tank 3. It is connected to the nozzle 26 inside. This nozzle 26 is provided in the side part and / or upper part in the processing tank 3, and injects the water from the circulation pump 25 toward the to-be-processed object 2. FIG.

給蒸手段10は、熱交換器8に蒸気を供給して、循環手段9による循環水を加熱する。給蒸手段10は、ボイラからの蒸気を熱交換器8へ供給する給蒸路27を備え、この給蒸路27には給蒸弁28が設けられている。循環手段9による循環中、温度センサ14の検出温度に基づき、給蒸弁28の開度を調整して、処理槽3内の温度を所望に調整することができる。   The steam supply means 10 supplies steam to the heat exchanger 8 to heat the circulating water by the circulation means 9. The steam supply means 10 includes a steam supply path 27 that supplies steam from the boiler to the heat exchanger 8, and a steam supply valve 28 is provided in the steam supply path 27. During the circulation by the circulation means 9, the temperature in the treatment tank 3 can be adjusted as desired by adjusting the opening degree of the steam supply valve 28 based on the temperature detected by the temperature sensor 14.

冷却手段11は、熱交換器8に冷却水を供給して、循環手段9による循環水を冷却する。冷却手段11は、クーリングタワー29を備え、クーリングタワー29にて冷却された水は、送水ポンプ30により、冷却水送り路31を介して熱交換器8へ供給され、熱交換器8を通過後の水は冷却水戻し路32を介してクーリングタワー29へ戻される。図示例の場合、冷却水送り路31と給蒸路27とは、熱交換器8の側で共通の管路とされている。   The cooling unit 11 supplies cooling water to the heat exchanger 8 to cool the circulating water by the circulation unit 9. The cooling means 11 includes a cooling tower 29, and the water cooled in the cooling tower 29 is supplied to the heat exchanger 8 via the cooling water feed path 31 by the water pump 30, and the water after passing through the heat exchanger 8. Is returned to the cooling tower 29 via the cooling water return path 32. In the case of the illustrated example, the cooling water feed path 31 and the steam supply path 27 are a common pipe line on the heat exchanger 8 side.

冷却水送り路31には冷却水送り弁33が設けられる一方、冷却水戻し路32には冷却水戻し弁34が設けられている。冷却水送り路31と給蒸路27との合流部は、冷却水送り弁33や給蒸弁28より下流側(熱交換器8側)に配置されている。   A cooling water feed valve 33 is provided in the cooling water feed path 31, while a cooling water return valve 34 is provided in the cooling water return path 32. The junction of the cooling water feed path 31 and the steam supply path 27 is disposed downstream (on the heat exchanger 8 side) from the cooling water feed valve 33 and the steam supply valve 28.

冷却水送り弁33および冷却水戻し弁34を開いた状態で、送水ポンプ30を作動させると、クーリングタワー29と熱交換器8との間で冷却水を循環させることができる。一方、冷却水送り弁33および冷却水戻し弁34を閉じれば、熱交換器8への冷却水の通水を停止することができる。   When the water supply pump 30 is operated with the cooling water feed valve 33 and the cooling water return valve 34 opened, the cooling water can be circulated between the cooling tower 29 and the heat exchanger 8. On the other hand, if the cooling water feed valve 33 and the cooling water return valve 34 are closed, the flow of the cooling water to the heat exchanger 8 can be stopped.

ドレン排出手段12は、給蒸手段10により熱交換器8に供給された蒸気の凝縮水を外部へ排出する。ドレン排出手段12は、冷却水戻し路32の内、冷却水戻し弁34より上流側(熱交換器8側)に設けられ、冷却水戻し路32から分岐するドレン排出路35に、ドレン排出弁36、スチームトラップ37および逆止弁38が順に設けられて構成される。熱交換器8への蒸気供給時、ドレン排出弁36を開けておくことで、蒸気の凝縮水を外部へ排出することができる。   The drain discharge means 12 discharges the condensed water of the steam supplied to the heat exchanger 8 by the steam supply means 10 to the outside. The drain discharge means 12 is provided upstream of the cooling water return valve 34 (on the heat exchanger 8 side) in the cooling water return path 32, and is connected to a drain discharge path 35 branched from the cooling water return path 32. 36, a steam trap 37 and a check valve 38 are provided in this order. When the steam is supplied to the heat exchanger 8, the condensate of the steam can be discharged to the outside by opening the drain discharge valve 36.

圧縮空気供給手段13は、熱交換器8に圧縮空気を供給して、熱交換器8内を加圧する。圧縮空気供給手段13は、圧縮空気源からの圧縮空気を熱交換器8へ供給する圧縮空気路39を備え、この圧縮空気路39には圧縮空気供給弁40が設けられている。詳細は後述するが、給蒸手段10による熱交換器8への蒸気供給の停止後、冷却手段11による熱交換器8への冷却水供給の開始前に、圧縮空気供給手段13により熱交換器8へ圧縮空気を供給することで、熱交換器8やその前後の配管(冷却水送り路31および冷却水戻し路32)内を加圧して、冷却水供給時の蒸気凝縮に伴う急減圧による衝撃を防止することができる。   The compressed air supply means 13 supplies compressed air to the heat exchanger 8 to pressurize the heat exchanger 8. The compressed air supply means 13 includes a compressed air passage 39 that supplies compressed air from a compressed air source to the heat exchanger 8, and a compressed air supply valve 40 is provided in the compressed air passage 39. Although details will be described later, after the steam supply to the heat exchanger 8 by the steam supply means 10 is stopped, before the cooling water supply to the heat exchanger 8 by the cooling means 11 is started, the compressed air supply means 13 is used to heat the heat exchanger. By supplying compressed air to 8, the inside of the heat exchanger 8 and the pipes before and after it (the cooling water feed path 31 and the cooling water return path 32) are pressurized, and due to the sudden pressure reduction accompanying steam condensation at the time of cooling water supply Impact can be prevented.

ところで、圧縮空気路39は、冷却水送り路31の内、冷却水送り弁33よりも下流側(熱交換器8側)に設けられる。この際、図示例のように、圧縮空気路39は、冷却水送り路31の内、給蒸路27との合流部よりも上流で、冷却水送り弁33よりも下流に接続されるのが好ましい。あるいは、圧縮空気路39は、給蒸路27の内、冷却水送り路31との合流部よりも上流で、給蒸弁28よりも下流に接続されるのが好ましい。   By the way, the compressed air passage 39 is provided in the cooling water feed passage 31 on the downstream side (the heat exchanger 8 side) from the cooling water feed valve 33. At this time, as in the illustrated example, the compressed air passage 39 is connected to the upstream of the junction with the steam supply passage 27 in the cooling water feed passage 31 and downstream of the cooling water feed valve 33. preferable. Alternatively, the compressed air passage 39 is preferably connected upstream of the joining portion with the cooling water feed passage 31 in the steam supply passage 27 and downstream of the steam supply valve 28.

制御手段は、温度センサ14および水位検出器の検出信号の他、経過時間などに基づき、前記各手段4〜7,9〜13を制御する制御器(図示省略)である。具体的には、給水ポンプ17、給水弁18、排水弁20、加圧弁22、排気弁24、循環ポンプ25、給蒸弁28、クーリングタワー29、送水ポンプ30、冷却水送り弁33、冷却水戻し弁34、ドレン排出弁36、圧縮空気供給弁40の他、温度センサ14および水位検出器などは、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3内の被処理物2の加熱殺菌やその後の冷却を行う。典型的には、給水工程、移行工程、殺菌工程、冷却工程および排水工程を順次に実行する。   The control means is a controller (not shown) that controls each of the means 4 to 7 and 9 to 13 based on the elapsed time in addition to the detection signals of the temperature sensor 14 and the water level detector. Specifically, the water supply pump 17, the water supply valve 18, the drain valve 20, the pressurization valve 22, the exhaust valve 24, the circulation pump 25, the steam supply valve 28, the cooling tower 29, the water supply pump 30, the cooling water supply valve 33, and the cooling water return. In addition to the valve 34, the drain discharge valve 36, the compressed air supply valve 40, the temperature sensor 14 and the water level detector are connected to the controller. And a controller performs the heat sterilization of the to-be-processed object 2 in the processing tank 3, and subsequent cooling according to a predetermined procedure (program) so that it may mention below. Typically, a water supply process, a transition process, a sterilization process, a cooling process, and a drainage process are sequentially performed.

以下、各工程について説明する。なお、殺菌装置1の運転に先立ち、処理槽3内には被処理物2が収容され、処理槽3の扉は閉じられる。その状態では、排気弁24は開かれ、その他の弁18,20,22,28,33,34,36,40は閉じられており、各ポンプ17,25,30は停止している。   Hereinafter, each step will be described. Prior to the operation of the sterilizer 1, the workpiece 2 is accommodated in the treatment tank 3, and the door of the treatment tank 3 is closed. In this state, the exhaust valve 24 is opened, the other valves 18, 20, 22, 28, 33, 34, 36, and 40 are closed, and the pumps 17, 25, and 30 are stopped.

≪(1)給水工程≫
給水工程では、処理槽3内の被処理物2を浸漬しない設定水位まで、給水手段4により処理槽3内に水を供給して、処理槽3内に水を貯留する。具体的には、給水ポンプ17を作動させた状態で給水弁18を開けばよい。処理槽3内に設定水位まで水が貯留されると、給水弁18を閉じると共に給水ポンプ17を停止させて、給水工程を終了する。
≪ (1) Water supply process≫
In the water supply process, water is supplied into the treatment tank 3 by the water supply means 4 to a set water level at which the workpiece 2 in the treatment tank 3 is not immersed, and the water is stored in the treatment tank 3. Specifically, the water supply valve 18 may be opened with the water supply pump 17 operated. When water is stored in the treatment tank 3 up to the set water level, the water supply valve 18 is closed and the water supply pump 17 is stopped to end the water supply process.

≪(2)移行工程≫
移行工程では、循環手段9により処理槽3と熱交換器8との間で水を循環させながら、その循環水を熱交換器8において給蒸手段10により加熱して、処理槽3内の温度を殺菌温度まで上昇させる。具体的には、循環ポンプ25を作動させることで、処理槽3内底部からの水を、熱交換器8を介して、ノズル26から処理槽3内へ戻すことで、処理槽3と熱交換器8との間で水を循環させる。また、この循環中、冷却水送り弁33、冷却水戻し弁34および圧縮空気供給弁40を閉じる一方、給蒸弁28およびドレン排出弁36を開けて、熱交換器8へ蒸気を供給する。これにより、熱交換器8において循環水と蒸気とを熱交換して、循環水の加熱を図ることができる。ドレン排出弁36を開けておくことで、蒸気の凝縮水は、スチームトラップ37を介して排出される。
≪ (2) Transition process≫
In the transition step, while circulating water between the treatment tank 3 and the heat exchanger 8 by the circulation means 9, the circulating water is heated by the steam supply means 10 in the heat exchanger 8, so that the temperature in the treatment tank 3 is increased. Is raised to the sterilization temperature. Specifically, by operating the circulation pump 25, the water from the inner bottom of the processing tank 3 is returned to the processing tank 3 from the nozzle 26 via the heat exchanger 8, thereby exchanging heat with the processing tank 3. Water is circulated to and from the vessel 8. During this circulation, the cooling water feed valve 33, the cooling water return valve 34 and the compressed air supply valve 40 are closed, and the steam supply valve 28 and the drain discharge valve 36 are opened to supply steam to the heat exchanger 8. Thereby, the circulating water and steam can be heat-exchanged in the heat exchanger 8, and the circulating water can be heated. By opening the drain discharge valve 36, the steam condensate is discharged through the steam trap 37.

このようにして、処理槽3内の温度を徐々に上昇させるが、それに伴い被処理物2が加熱により膨張して容器(レトルトパウチなど)が破裂するおそれがある。そこで、これを防止するために、加圧手段6により処理槽3内は徐々に加圧され、大気圧を超える圧力(処理槽内温度相当の飽和蒸気圧力よりも高圧)とされる。具体的には、加圧弁22と排気弁24とを制御することにより、処理槽3内の温度に応じた加圧がなされる。   Thus, although the temperature in the processing tank 3 is raised gradually, the to-be-processed object 2 expand | swells by heating, and there exists a possibility that a container (retort pouch etc.) may burst. Therefore, in order to prevent this, the inside of the processing tank 3 is gradually pressurized by the pressurizing means 6 to a pressure exceeding the atmospheric pressure (higher than the saturated vapor pressure corresponding to the temperature in the processing tank). Specifically, the pressurization according to the temperature in the processing tank 3 is performed by controlling the pressurization valve 22 and the exhaust valve 24.

以後、循環手段9による水の循環は、冷却工程の終了まで継続される。また、加圧手段6による処理槽3内の加圧は、処理槽3内が殺菌温度まで上昇した後も、処理槽内温度相当の飽和蒸気圧力よりも高圧に、冷却工程の終了まで継続される。   Thereafter, the circulation of water by the circulation means 9 is continued until the end of the cooling process. Further, the pressurizing means 6 pressurizes the treatment tank 3 after the temperature in the treatment tank 3 rises to the sterilization temperature, and continues to a pressure higher than the saturated vapor pressure corresponding to the treatment tank temperature until the end of the cooling step. The

≪(3)殺菌工程≫
殺菌工程では、処理槽3内の温度を殺菌温度に保持して、被処理物2を加熱して殺菌する。具体的には、処理槽3内の貯留水を循環手段9により循環させつつ、温度センサ14の検出温度を殺菌温度に維持するように、給蒸弁28の開度を調整する。処理槽3内が殺菌温度以上で殺菌時間経過すると、給蒸弁28を閉じて熱交換器8への給蒸を停止して、殺菌工程を終了する。
≪ (3) Sterilization process≫
In the sterilization step, the temperature in the treatment tank 3 is maintained at the sterilization temperature, and the workpiece 2 is heated and sterilized. Specifically, the opening degree of the steam supply valve 28 is adjusted so as to maintain the temperature detected by the temperature sensor 14 at the sterilization temperature while circulating the stored water in the treatment tank 3 by the circulation means 9. When the inside of the treatment tank 3 is at or above the sterilization temperature and the sterilization time has elapsed, the steam supply valve 28 is closed, the steam supply to the heat exchanger 8 is stopped, and the sterilization process is terminated.

殺菌工程の終了後、冷却工程の開始前、圧縮空気供給手段13により、熱交換器8(蒸気が供給されていた側)へ向けて圧縮空気が供給され、熱交換器8の加圧が開始される。そして、圧縮空気供給手段13による熱交換器8の加圧は、冷却工程の開始時または開始直後まで継続される。より具体的には、好ましくは、下記(a)に示す第一操作か、(b)に示す第二操作かのいずれかの移行時操作が実行される。   After the sterilization process is completed, before the cooling process is started, the compressed air supply means 13 supplies compressed air to the heat exchanger 8 (the side where the steam has been supplied), and pressurization of the heat exchanger 8 starts. Is done. And pressurization of the heat exchanger 8 by the compressed air supply means 13 is continued until the start of the cooling process or immediately after the start. More specifically, preferably, the transition operation, either the first operation shown in the following (a) or the second operation shown in (b), is executed.

<(a)第一操作>
給蒸手段10による熱交換器8への蒸気供給を停止(殺菌工程終了)してから第一設定時間経過後、圧縮空気供給手段13による熱交換器8への圧縮空気の供給を開始する。そして、圧縮空気供給手段13による熱交換器8への圧縮空気供給を開始してから第二設定時間経過後、冷却手段11による熱交換器8への冷却水の供給を開始(冷却工程開始)する。第一操作では、圧縮空気供給手段13による熱交換器8への圧縮空気の供給は、冷却手段11による熱交換器8への冷却水供給の開始時までなされる。より具体的には、次のとおりである。
<(A) First operation>
The supply of compressed air to the heat exchanger 8 by the compressed air supply means 13 is started after the first set time has elapsed since the supply of steam to the heat exchanger 8 by the steam supply means 10 is stopped (end of the sterilization step). Then, after the second set time has elapsed after the compressed air supply means 13 starts supplying compressed air to the heat exchanger 8, the cooling means 11 starts supplying cooling water to the heat exchanger 8 (cooling process start). To do. In the first operation, the compressed air is supplied to the heat exchanger 8 by the compressed air supply means 13 until the start of the cooling water supply to the heat exchanger 8 by the cooling means 11. More specifically, it is as follows.

前述したとおり、殺菌工程中、冷却水送り弁33、冷却水戻し弁34および圧縮空気供給弁40を閉じる一方、ドレン排出弁36を開けて、給蒸弁28の開度が調整される。殺菌工程終了時、給蒸弁28が閉じられる。そして、給蒸弁28を閉じてから第一設定時間(たとえば5秒)経過すると、圧縮空気供給弁40を開けると共に送水ポンプ30を作動させる。さらに、圧縮空気供給弁40を開けてから第二設定時間(たとえば5秒)経過すると、冷却水送り弁33および冷却水戻し弁34を開ける一方、ドレン排出弁36および圧縮空気供給弁40を閉じて、冷却工程を開始する。つまり、後述するように、クーリングタワー29からの冷却水を熱交換器8に供給して循環水を冷却することで、被処理物2の冷却を図る。   As described above, during the sterilization process, the cooling water feed valve 33, the cooling water return valve 34, and the compressed air supply valve 40 are closed, while the drain discharge valve 36 is opened to adjust the opening degree of the steam supply valve 28. At the end of the sterilization process, the steam supply valve 28 is closed. When the first set time (for example, 5 seconds) has elapsed since the steam supply valve 28 was closed, the compressed air supply valve 40 is opened and the water pump 30 is operated. Further, when the second set time (for example, 5 seconds) has elapsed since the compressed air supply valve 40 was opened, the cooling water feed valve 33 and the cooling water return valve 34 are opened, while the drain discharge valve 36 and the compressed air supply valve 40 are closed. The cooling process is started. That is, as will be described later, the workpiece 2 is cooled by supplying the cooling water from the cooling tower 29 to the heat exchanger 8 and cooling the circulating water.

<(b)第二操作>
給蒸手段10による熱交換器8への蒸気供給を停止(殺菌工程終了)してから第一設定時間経過後、圧縮空気供給手段13による熱交換器8への圧縮空気の供給を開始する。そして、圧縮空気供給手段13による熱交換器8への圧縮空気供給を開始してから第二設定時間経過後、冷却手段11による熱交換器8への冷却水の供給を開始(冷却工程開始)する。第二操作では、圧縮空気供給手段13による熱交換器8への圧縮空気の供給は、冷却手段11による熱交換器8への冷却水供給を開始してから第三設定時間経過時までなされる。より具体的には、次のとおりである。
<(B) Second operation>
The supply of compressed air to the heat exchanger 8 by the compressed air supply means 13 is started after the first set time has elapsed since the supply of steam to the heat exchanger 8 by the steam supply means 10 is stopped (end of the sterilization step). Then, after the second set time has elapsed after the compressed air supply means 13 starts supplying compressed air to the heat exchanger 8, the cooling means 11 starts supplying cooling water to the heat exchanger 8 (cooling process start). To do. In the second operation, the compressed air is supplied to the heat exchanger 8 by the compressed air supply means 13 from the start of the cooling water supply to the heat exchanger 8 by the cooling means 11 until the third set time has elapsed. . More specifically, it is as follows.

前述したとおり、殺菌工程中、冷却水送り弁33、冷却水戻し弁34および圧縮空気供給弁40を閉じる一方、ドレン排出弁36を開けて、給蒸弁28の開度が調整される。殺菌工程終了時、給蒸弁28が閉じられる。そして、給蒸弁28を閉じてから第一設定時間(たとえば5秒)経過すると、圧縮空気供給弁40を開けると共に送水ポンプ30を作動させる。さらに、圧縮空気供給弁40を開けてから第二設定時間(たとえば5秒)経過すると、冷却水送り弁33および冷却水戻し弁34を開ける一方、ドレン排出弁36を閉じて、冷却工程を開始する。これにより、クーリングタワー29からの冷却水が熱交換器8に通水されるが、その時点から第三設定時間(たとえば10秒)経過時に、圧縮空気供給弁40を閉じる。   As described above, during the sterilization process, the cooling water feed valve 33, the cooling water return valve 34, and the compressed air supply valve 40 are closed, while the drain discharge valve 36 is opened to adjust the opening degree of the steam supply valve 28. At the end of the sterilization process, the steam supply valve 28 is closed. When the first set time (for example, 5 seconds) has elapsed since the steam supply valve 28 was closed, the compressed air supply valve 40 is opened and the water pump 30 is operated. Further, when the second set time (for example, 5 seconds) has elapsed since the compressed air supply valve 40 was opened, the cooling water feed valve 33 and the cooling water return valve 34 are opened, while the drain discharge valve 36 is closed and the cooling process is started. To do. Thereby, the cooling water from the cooling tower 29 is passed through the heat exchanger 8, but the compressed air supply valve 40 is closed when a third set time (for example, 10 seconds) has elapsed from that point.

以上から明らかなとおり、第一操作と第二操作とは、いずれも殺菌工程終了後に熱交換器8内に圧縮空気を流し込むことで共通するが、第一操作では、圧縮空気の供給を停止した後に冷却工程に移行するのに対し、第二操作では、圧縮空気を流しながら冷却工程を開始し、所定時間経過後に圧縮空気の供給を停止する点で異なる。   As is clear from the above, the first operation and the second operation are both common by flowing compressed air into the heat exchanger 8 after the sterilization step, but in the first operation, the supply of compressed air was stopped. The second operation is different from the latter in that the cooling process is started while flowing compressed air, and the supply of compressed air is stopped after a predetermined time.

いずれにしても、このような移行操作を実行することで、熱交換器8は、圧縮空気が供給され加圧されるので、冷却水供給時の蒸気の凝縮による急激な減圧が防止される。それにより、冷却水供給時、安全弁からの蒸気が噴き出すのが防止され、また配管から音や振動が発生するのも防止される。また、蒸気供給の停止後、第一設定時間経過してから圧縮空気を供給したり、圧縮空気供給の開始後、第二設定時間経過してから冷却水を供給したり、冷却水供給の開始時またはそれから第三設定時間経過するまで圧縮空気供給を継続したりすることで、上述の作用効果を安定したものとする。   In any case, by executing such a transition operation, the heat exchanger 8 is supplied with pressurized air and pressurized, so that sudden pressure reduction due to steam condensation during cooling water supply is prevented. This prevents steam from being ejected from the safety valve when cooling water is supplied, and also prevents noise and vibration from being generated from the piping. Also, supply of compressed air after the first set time has elapsed after the stop of steam supply, supply of cooling water after the second set time has elapsed after the start of supply of compressed air, or start of supply of cooling water The above-mentioned operation and effect are stabilized by continuing the compressed air supply until the time or the third set time elapses thereafter.

ところで、圧縮空気供給手段13による加圧を行っても、冷却水戻し路32はクーリングタワー29において大気に開放されているので、冷却水や圧縮空気は逆流することなく、クーリングタワー29へ送られる。なお、本実施例では、圧縮空気供給手段13による圧縮空気の圧力は、送水ポンプ30の吐出圧と同等(両者の圧力差は所定範囲内)とされている。   By the way, even if the compressed air supply means 13 is pressurized, the cooling water return path 32 is open to the atmosphere in the cooling tower 29, so that the cooling water and compressed air are sent back to the cooling tower 29 without flowing back. In this embodiment, the pressure of the compressed air by the compressed air supply means 13 is equal to the discharge pressure of the water pump 30 (the pressure difference between the two is within a predetermined range).

≪(4)冷却工程≫
冷却工程では、循環手段9により処理槽3と熱交換器8との間で水を循環させながら、その循環水を熱交換器8において冷却手段11により冷却して、処理槽3内の被処理物2を冷却する。具体的には、循環ポンプ25を作動させることで、処理槽3内底部からの水を、熱交換器8を介して、ノズル26から処理槽3内へ戻すことで、処理槽3と熱交換器8との間で水を循環させる。また、この循環中、給蒸弁28およびドレン排出弁36を閉じる一方、冷却水送り弁33および冷却水戻し弁34を開けた状態で、クーリングタワー29および送水ポンプ30を作動させて、熱交換器8に冷却水を循環させればよい。
≪ (4) Cooling process≫
In the cooling process, while circulating water between the treatment tank 3 and the heat exchanger 8 by the circulation means 9, the circulating water is cooled by the cooling means 11 in the heat exchanger 8, and the treatment in the treatment tank 3 is performed. Item 2 is cooled. Specifically, by operating the circulation pump 25, the water from the inner bottom of the processing tank 3 is returned to the processing tank 3 from the nozzle 26 via the heat exchanger 8, thereby exchanging heat with the processing tank 3. Water is circulated to and from the vessel 8. During the circulation, the steam supply valve 28 and the drain discharge valve 36 are closed, while the cooling water feed valve 33 and the cooling water return valve 34 are opened, the cooling tower 29 and the water feed pump 30 are operated, and the heat exchanger What is necessary is just to circulate cooling water to 8.

冷却工程の開始から冷却時間経過するか、処理槽3内の温度が冷却温度よりも下がるか、冷却温度よりも下がってから所定時間経過すると、冷却手段11による熱交換器8への冷却水供給を停止して、冷却工程を終了する。この際、循環手段9による循環も停止するが、加圧手段6による処理槽3内の加圧は、排水工程における排水完了まで継続してもよい。   Supply of cooling water to the heat exchanger 8 by the cooling means 11 when the cooling time elapses from the start of the cooling process, when the temperature in the treatment tank 3 falls below the cooling temperature, or when a predetermined time elapses after falling below the cooling temperature. To stop the cooling process. At this time, the circulation by the circulation means 9 is also stopped, but the pressurization in the treatment tank 3 by the pressure means 6 may be continued until the drainage is completed in the drainage process.

≪(5)排水工程≫
排水工程では、排水手段5により処理槽3内から排水する。具体的には、排水弁20を開くことで、外部へ水を排出する。加圧手段6により処理槽3内を加圧したままで排水手段5により排水すれば、処理槽3内からの排水を迅速に行うことができる。その後、加圧弁22を閉じる一方、排気弁24を開いて、処理槽3内を大気圧まで戻した後、処理槽3の扉を開けて、処理槽3内から被処理物2を取り出すことができる。
≪ (5) Drainage process≫
In the drainage process, the drainage means 5 drains the water from the treatment tank 3. Specifically, water is discharged to the outside by opening the drain valve 20. If the drainage means 5 drains while the inside of the treatment tank 3 is pressurized by the pressurizing means 6, drainage from the treatment tank 3 can be performed quickly. Thereafter, the pressurizing valve 22 is closed, the exhaust valve 24 is opened, the inside of the processing tank 3 is returned to atmospheric pressure, the door of the processing tank 3 is opened, and the workpiece 2 is taken out from the processing tank 3. it can.

本発明の殺菌装置1は、前記実施例の構成に限らず、適宜変更可能である。特に、熱交換器8への圧縮空気供給手段13を備え、熱交換器8への蒸気供給の停止後、冷却水供給の開始前に、熱交換器8へ圧縮空気を供給して加圧しておくのであれは、その他の構成は適宜に変更可能である。たとえば、熱交換器8への蒸気供給停止後に圧縮空気供給を開始するタイミング(第一設定時間)、熱交換器8への圧縮空気供給開始後に冷却水供給を開始するタイミング(第二設定時間)、熱交換器8への圧縮空気供給を停止するタイミング(第三設定時間)は、適宜に設定され、また場合により熱交換器8内(蒸気や冷却水が通される側)の圧力に基づき制御するなどしてもよい。   The sterilization apparatus 1 of the present invention is not limited to the configuration of the above embodiment, and can be changed as appropriate. In particular, a compressed air supply means 13 for the heat exchanger 8 is provided, and after stopping the supply of steam to the heat exchanger 8 and before starting the cooling water supply, the compressed air is supplied to the heat exchanger 8 and pressurized. However, other configurations can be changed as appropriate. For example, the timing for starting the supply of compressed air after stopping the supply of steam to the heat exchanger 8 (first set time), the timing for starting the supply of cooling water after starting the supply of compressed air to the heat exchanger 8 (second set time) The timing (third set time) for stopping the supply of compressed air to the heat exchanger 8 is set as appropriate, and in some cases, based on the pressure in the heat exchanger 8 (side through which steam or cooling water is passed). It may be controlled.

さらに、いわゆる貯湯式の殺菌装置に適用することもできる。その場合、処理槽3内において、被処理物2を熱水に水没して殺菌を行うが、前記実施例と同様に、処理槽3内の貯留水を熱交換器8との間で循環させつつ、その循環水を、殺菌工程では蒸気により加熱し、冷却工程では冷却水により冷却する。そして、殺菌工程から冷却工程への移行時に、前記移行時操作を実行可能とすればよい。   Furthermore, it can also be applied to a so-called hot water storage type sterilizer. In that case, in the treatment tank 3, the object to be treated 2 is submerged in hot water for sterilization, but the stored water in the treatment tank 3 is circulated between the heat exchanger 8 as in the above embodiment. On the other hand, the circulating water is heated by steam in the sterilization process, and cooled by cooling water in the cooling process. And what is necessary is just to be able to perform the said operation at the time of transfer at the time of transfer from a sterilization process to a cooling process.

1 殺菌装置
2 被処理物
3 処理槽
4 給水手段
5 排水手段
6 加圧手段
7 排気手段
8 熱交換器
9 循環手段
10 給蒸手段
11 冷却手段
12 ドレン排出手段
13 圧縮空気供給手段
27 給蒸路
28 給蒸弁
29 クーリングタワー
30 送水ポンプ
31 冷却水送り路
32 冷却水戻し路
33 冷却水送り弁
34 冷却水戻し弁
35 ドレン排出路
36 ドレン排出弁
39 圧縮空気路
40 圧縮空気供給弁
DESCRIPTION OF SYMBOLS 1 Sterilizer 2 To-be-processed object 3 Processing tank 4 Water supply means 5 Drainage means 6 Pressurization means 7 Exhaust means 8 Heat exchanger 9 Circulation means 10 Steam supply means 11 Cooling means 12 Drain discharge means 13 Compressed air supply means 27 Steam supply path 28 Steam supply valve 29 Cooling tower 30 Water feed pump 31 Cooling water feed path 32 Cooling water return path 33 Cooling water feed valve 34 Cooling water return valve 35 Drain discharge path 36 Drain discharge valve 39 Compressed air path 40 Compressed air supply valve

Claims (3)

被処理物が収容されると共に水が貯留される処理槽と、
この処理槽内の貯留水を熱交換器との間で循環させる循環手段と、
この循環手段による循環水を加熱するために、前記熱交換器に蒸気を供給する給蒸手段と、
前記循環手段による循環水を冷却するために、前記熱交換器に冷却水を供給する冷却手段と、
前記給蒸手段による前記熱交換器への蒸気供給の停止後、前記冷却手段による前記熱交換器への冷却水供給の開始前に、前記熱交換器へ圧縮空気を供給する圧縮空気供給手段と
を備えることを特徴とする殺菌装置。
A treatment tank in which water is stored while a workpiece is stored;
Circulation means for circulating the stored water in the treatment tank with the heat exchanger;
In order to heat the circulating water by the circulation means, steam supply means for supplying steam to the heat exchanger,
Cooling means for supplying cooling water to the heat exchanger in order to cool the circulating water by the circulation means;
Compressed air supply means for supplying compressed air to the heat exchanger after the steam supply to the heat exchanger is stopped by the steam supply means and before the cooling water supply to the heat exchanger is started by the cooling means; A sterilizing apparatus comprising:
前記給蒸手段による前記熱交換器への蒸気供給を停止してから第一設定時間経過後、前記圧縮空気供給手段による前記熱交換器への圧縮空気の供給を開始し、
前記圧縮空気供給手段による前記熱交換器への圧縮空気供給を開始してから第二設定時間経過後、前記冷却手段による前記熱交換器への冷却水の供給を開始し、
前記圧縮空気供給手段による前記熱交換器への圧縮空気の供給は、前記冷却手段による前記熱交換器への冷却水供給の開始時までなされるか、前記冷却手段による前記熱交換器への冷却水供給を開始してから第三設定時間経過時までなされる
ことを特徴とする請求項1に記載の殺菌装置。
After the first set time has elapsed since stopping steam supply to the heat exchanger by the steam supply means, start supplying compressed air to the heat exchanger by the compressed air supply means,
After the second set time has elapsed since the compressed air supply means started the supply of compressed air to the heat exchanger, the cooling means started supplying cooling water to the heat exchanger,
Supply of compressed air to the heat exchanger by the compressed air supply means is performed until the start of supply of cooling water to the heat exchanger by the cooling means, or cooling to the heat exchanger by the cooling means The sterilization apparatus according to claim 1, wherein the sterilization apparatus is performed from the start of water supply until a third set time has elapsed.
前記処理槽内には、前記被処理物を浸漬しない水位まで水が貯留され、
前記循環手段は、前記処理槽内の底部からの水を、前記熱交換器を介して前記処理槽内の被処理物へ噴出して戻し、
前記冷却手段は、前記熱交換器とクーリングタワーとの間で冷却水を循環させ、前記クーリングタワーから前記熱交換器への冷却水送り路に冷却水送り弁を備える一方、前記熱交換器から前記クーリングタワーへの冷却水戻し路に冷却水戻し弁を備え、
前記給蒸手段は、給蒸弁を備える給蒸路が、前記冷却水送り弁よりも下流の前記冷却水送り路に接続され、
前記給蒸手段による蒸気のドレンを外部へ排出するドレン排出手段は、ドレン排出弁を備えるドレン排出路が、前記冷却水戻し弁よりも上流の前記冷却水戻し路に接続され、
前記圧縮空気供給手段は、圧縮空気供給弁を備える圧縮空気路が、前記冷却水送り弁よりも下流の前記冷却水送り路に接続されるか、前記給蒸弁よりも下流の前記給蒸路に接続され、
前記冷却水送り弁、前記冷却水戻し弁および前記圧縮空気供給弁を閉じる一方、前記給蒸弁および前記ドレン排出弁を開けて、前記給蒸手段からの蒸気を前記熱交換器に供給して前記循環水を加熱することで、前記被処理物を殺菌し、
前記処理槽内が殺菌温度以上で殺菌時間経過すると、前記給蒸弁を閉じ、
前記給蒸弁を閉じてから第一設定時間経過すると、前記圧縮空気供給弁を開け、
前記圧縮空気供給弁を開けてから第二設定時間経過すると、前記冷却水送り弁および前記冷却水戻し弁を開ける一方、前記ドレン排出弁を閉じて、前記クーリングタワーからの冷却水を前記熱交換器に供給して前記循環水を冷却することで、前記被処理物を冷却し、
前記熱交換器への冷却水供給の開始時、またはその時点から第三設定時間経過時に、前記圧縮空気供給弁を閉じる
ことを特徴とする請求項1または請求項2に記載の殺菌装置。
In the treatment tank, water is stored up to a water level where the workpiece is not immersed,
The circulating means jets water from the bottom in the processing tank back to the object to be processed in the processing tank via the heat exchanger,
The cooling means circulates cooling water between the heat exchanger and the cooling tower, and includes a cooling water feed valve in a cooling water feed path from the cooling tower to the heat exchanger, while from the heat exchanger to the cooling tower. A cooling water return valve is provided in the cooling water return path to
The steaming means is connected to the cooling water feed path downstream of the cooling water feed valve, a steam feed path having a steam feed valve,
The drain discharge means for discharging the steam drain by the steam supply means to the outside, a drain discharge path including a drain discharge valve is connected to the cooling water return path upstream of the cooling water return valve,
In the compressed air supply means, a compressed air path including a compressed air supply valve is connected to the cooling water feed path downstream from the cooling water feed valve, or the steam feed path downstream from the steam feed valve. Connected to
While closing the cooling water feed valve, the cooling water return valve, and the compressed air supply valve, the steam supply valve and the drain discharge valve are opened to supply steam from the steam supply means to the heat exchanger. By heating the circulating water, the object to be treated is sterilized,
When the inside of the treatment tank is at or above the sterilization temperature, the steam supply valve is closed,
When the first set time has elapsed after closing the steam supply valve, open the compressed air supply valve,
When the second set time elapses after opening the compressed air supply valve, the cooling water feed valve and the cooling water return valve are opened, the drain discharge valve is closed, and the cooling water from the cooling tower is supplied to the heat exchanger. And cooling the circulating water to cool the workpiece,
The sterilizer according to claim 1 or 2, wherein the compressed air supply valve is closed at the start of supply of cooling water to the heat exchanger, or when a third set time has elapsed since that time.
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